无钥匙条例(EU) No 68/2013,关于饲料原料产品目录(1)

技术法规类型:欧盟Eurlex法规 来源:tbtmap

EURLEX ID:32013R0068

OJ编号:OJ L 29, 30.1.2013, p. 1-64

中文标题:委员会条例(EU) No 68/2013,关于饲料原料产品目录(1)

原文标题:Commission Regulation (EU) No 68/2013 of 16 January 2013 on the Catalogue of feed materials (1)

分类:03.50.10_动物饲料

文件类型:二级立法 Regulation|条例

生效日期:2013-02-19

废止日期:2058-12-31

法规全文:查看欧盟官方文件

EN
30.1.2013 Official
Journal
of
the
European
Union
L
29/1
II
(Non-legislative acts)
REGULATIONS
COMMISSION REGULATION (EU) No 68/2013
of 16 January 2013
on the Catalogue of feed materials
(Text with EEA relevance)
THE EUROPEAN COMMISSION,
manufacturing process or from processing aids to be
set according to point 1 of Annex I to Regulation (EC)
No 767/2009. Specific rules should apply to former
Having regard to the Treaty on the Functioning of the European
foodstuff e.g. production surplus, misshapen products
Union,
or food with expired use-by date that had been
produced in compliance with EU food law.
Having regard to Regulation (EC) No 767/2009 of the European
Parliament and of the Council of 13 July 2009 on the placing
on the market and use of feed, amending European Parliament
(5) The
conditions
set
out
in
Article
26
of
Regulation
(EC)
and Council Regulation (EC) No 1831/2003 and repealing
No 767/2009 are fulfilled.
Council Directive 79/373/EEC, Commission Directive
80/511/EEC, Council Directives 82/471/EEC, 83/228/EEC,
93/74/EEC, 93/113/EC and 96/25/EC and Commission
(6) Given
the
very
high
number
of
amendments
to
be
made
Decision 2004/217/EC ( 1 ), and in particular Article 26(2) and
to Regulation (EU) No 575/2011, it is appropriate, for
(3) thereof,
reasons of coherence, clarity and simplification, to repeal
and replace that Regulation.
Whereas:
(7) It
is
appropriate
to
reduce
the
administrative
burden
on
(1) Commission
Regulation
(EU)
No
575/2011
of
16
June
the operators by providing a period of time allowing a
2011 on the Catalogue of feed materials ( 2 ) (the Cata
smooth conversion of labelling to avoid unnecessary
logue) replaced the first version of the Catalogue of
disruption to commercial practices.
feed materials set out in Commission Regulation (EU)
No 242/2010 of 19 March 2010 creating the
Catalogue of feed materials ( 3 ).
(8) The
measures
provided
for
in
this
Regulation
are
in
accordance with the opinion of the Standing
(2) The
appropriate
representatives
of
the
European
feed
Committee on the Food Chain and Animal Health,
business sectors have, in consultation with other parties
concerned, in collaboration with the competent national
authorities and taking into account relevant experience
HAS ADOPTED THIS REGULATION:
from opinions issued by the European Food Safety
Authority and scientific or technological developments,
developed amendments to Regulation (EU) No
Article 1
575/2011.
The Catalogue of feed materials referred to in Article 24 of
Regulation (EC) No 767/2009 is established, as set out in the
(3) These
amendments
concern
new
entries
of
treatment Annex to this Regulation.
processes and feed materials and improvements of
existing entries, in particular for oil and fat derivatives.
Article 2
(4) Furthermore,
the
amendments
concern
maximum
contents of chemical impurities resulting from their
Regulation (EU) No 575/2011 is repealed.
( 1 ) OJ L 229, 1.9.2009, p. 1.
( 2 ) OJ L 159, 17.6.2011, p. 25.
References to the repealed Regulation shall be construed as
( 3 ) OJ L 77, 24.3.2010, p. 17.
references to this Regulation.

L 29/2
EN
Official Journal of the European Union
30.1.2013
Article 3
Feed materials which have been labelled in accordance with Regulation (EU) No 575/2011 before
19 August 2013 may continue to be placed on the market and used until stocks are exhausted.
Article 4
This Regulation shall enter into force on the twentieth day following that of its publication in the Official
Journal of the European Union.
This Regulation shall be binding in its entirety and directly applicable in all Member States.
Done at Brussels, 16 January 2013.
For the Commission
The President
José Manuel BARROSO

EN
30.1.2013 Official
Journal
of
the
European
Union
L
29/3
ANNEX
CATALOGUE OF FEED MATERIALS
PART A
General provisions
(1) The use of this Catalogue by the feed business operators shall be voluntary. However, the name of a feed material
listed in Part C may be used only for a feed material complying with the requirements of the entry concerned.
(2) All entries in the list of feed materials in Part C shall comply with the restrictions on the use of feed materials in
accordance with the relevant legislation of the Union. Feed business operators using a feed material entered in the
Catalogue shall ensure that it complies with Article 4 of Regulation (EC) No 767/2009.
(3) ‘Former foodstuffs’ means foodstuffs, other than catering reflux, which were manufactured for human consumption
in full compliance with the EU food law but which are no longer intended for human consumption for practical or
logistical reasons or due to problems of manufacturing or packaging defects or other defects and which do not
present any health risks when used as feed. The setting of maximum contents as referred to in point 1 of Annex I to
Regulation (EC) No 767/2009 shall not be applicable to former foodstuffs and catering reflux. It shall apply when
further processed as feed.
(4) In accordance with good practice as referred to in Article 4 of Regulation (EC) No 183/2005 of the European
Parliament and of the Council ( 1 ), feed materials shall be free from chemical impurities resulting from their manu
facturing process and from processing aids, unless a specific maximum content is fixed in the Catalogue. Substances
prohibited for use in feed shall not be present and for those substances such maximum contents shall not be fixed.
In the interest of transparency, feed materials with tolerated residues are complemented with relevant information
provided by feed business operators in the context of usual commercial transactions.
(5) In accordance with good practice as referred to in Article 4 of Regulation (EC) No 183/2005, application of the
ALARA ( 2 ) principle and without prejudice to the application of Regulation (EC) No 183/2005, Directive
2002/32/EC of the European Parliament and of the Council of 7 May 2002 on undesirable substances in animal
feed ( 3 ), Regulation (EC) No 396/2005 of the European Parliament and of the Council of 23 February 2005 on
maximum residue levels of pesticides in or on food and feed of plant and animal origin and amending Council
Directive 91/414/EEC ( 4 ) and Regulation (EC) No 1831/2003 of the European Parliament and of the Council of
22 September 2003 on additives for use in animal nutrition ( 5 ), it is appropriate to specify in the Catalogue of feed
materials the maximum contents for chemical impurities resulting from the manufacturing process or from
processing aids that are present at levels of 0,1 % or above. Maximum contents may also be set in the
Catalogue for chemical impurities and processing aids present at levels lower than 0,1 % if deemed suitable for
good trading practices. Unless otherwise specified in Part B or C of the present Annex, any maximum content is
expressed on a weight/weight basis.
(6) The specific maximum contents for chemical impurities and processing aids are set either in the description of the
process in Part B, in the description of the feed material in Part C or at the end of a category in Part C. Unless a
specific maximum content is set in Part C, any maximum content set in Part B for a given process is applicable to
any feed material listed in Part C in so far as the description of the feed material makes reference to this process in
its description and in so far as the process at stake meets the description given in Part B.
(7) The botanical purity of a feed material shall not be less than 95 %. However, botanical impurities such as residues of
other oil seeds or oil fruits derived from a previous manufacturing process shall not exceed 0,5 % for each type of
oil seed or fruit. Derogating from these general rules a specific level shall be set in the list of feed materials in Part C.
( 1 ) OJ L 35, 8.2.2005, p. 1.
( 2 ) As Low As Reasonably Achievable.
( 3 ) OJ L 140, 30.5.2002, p. 10.
( 4 ) OJ L 70, 16.3.2005, p. 1.
( 5 ) OJ L 268, 18.10.2003, p. 29.

L 29/4
EN
Official Journal of the European Union
30.1.2013
(8) The common name/qualifier of one or more of the processes, as listed in the last column of the glossary of
processes in Part B, shall ( 1 ) be added to the name of the feed material to indicate that it has undergone the
respective process or processes. A feed material whose name is a combination of a name listed in Part C with the
common name/qualifier of one or more of the processes listed in Part B shall be considered as included in the
Catalogue and its label shall bear the compulsory declarations applicable for this feed material as set out in the last
columns of Parts B and C, as applicable. Whenever set out in the last column of Part B, the specific method used for
the process shall be specified in the name of the feed material.
(9) If the manufacturing process for a feed material differs from the description of the process concerned, as set out in
the glossary of processes in Part B, the manufacturing process shall be set out in the description of the feed material
concerned.
(10) For a number of feed materials, synonyms may be used. Such synonyms are included in square brackets in the
column ‘name’ of the entry for the feed material concerned in the list of feed materials in Part C.
(11) In the description of the feed materials in the list of feed materials in Part C, the word ‘product’ is used instead of the
word ‘by-product’ to reflect the market situation and the language used in practice by feed business operators to
highlight the commercial value of feed materials.
(12) The botanical name of a plant is only given in the description of the first entry in the list of feed materials in Part C
concerning that plant.
(13) The underlying principle for the compulsory labelling of analytical constituents of a certain feed material in the
Catalogue is, whether a certain product contains high concentrations of a specific constituent, or the manufacturing
process has changed the nutritional characteristics of the product.
(14) Article 15(g) of Regulation (EC) No 767/2009 in conjunction with point 6 of Annex I to that Regulation lays down
labelling requirements as regards the moisture content. Article 16(1)(b) of that Regulation in conjunction with its
Annex V lays down labelling requirements as regards other analytical constituents. In addition, point 5 of Annex I to
Regulation (EC) No 767/2009 requires the declaration of the level of ash insoluble in hydrochloric acid if it exceeds
2,2 % in general or for certain feed material if it exceeds the level set in the relevant section of Annex V to that
Regulation. However, some entries in the list of feed materials in Part C deviate from those rules as follows:
(a) compulsory declarations regarding analytical constituents in the list of feed materials in Part C replace the
compulsory declarations as set out in the relevant section of Annex V to Regulation (EC) No 767/2009;
(b) if the column relating to compulsory declarations in the list of feed materials in Part C is left blank with respect
to the analytical constituents that would have to be declared in accordance with the relevant section of Annex V
to Regulation (EC) No 767/2009, none of those constituents need be labelled. For ash insoluble in hydrochloric
acid, however, where no level is set in the list of feed materials in Part C, the level shall be declared if it exceeds
2,2 %;
(c) where one or more specific moisture levels are set in the column ‘compulsory declarations’ of the list of feed
materials in Part C, those levels shall apply instead of the levels in point 6 of Annex I to Regulation (EC) No
767/2009. However, if the moisture content is below 14 % its declaration is not compulsory. Where no specific
moisture level is set in that column, point 6 of Annex I to Regulation (EC) No 767/2009 shall apply.
(15) A feed business operator, who claims a feed material has more properties than those specified in the column
‘description’ of the list of feed materials in Part C, or refers to a process listed in Part B that can be assimilated as a
claim (e.g. rumen protection), has to comply with Article 13 of Regulation (EC) No 767/2009. Furthermore, feed
materials may meet a particular nutritional purpose in accordance with Articles 9 and 10 of Regulation (EC) No
767/2009.
( 1 ) By derogation from this obligation, for the process ‘drying’ it may be added.

EN
30.1.2013 Official
Journal
of
the
European
Union
L
29/5
PART B
Glossary of processes
Process Definition Common
name/qualifier
1 Air
fractionation
Separation of particles by means of an air stream Air
fractionated
2 Aspiration Process
to
remove
dust,
fine
particles
and
other
Aspirated
parts with suspended cereal fines from a bulk of
grain during transfer by means of an air-flow
3 Blanching
Process consisting of heat treatment of an organic Blanched
substance by boiling or steaming in order to
denature natural enzymes, soften tissue and
remove raw flavouring and followed by
immersion in cold water to halt the cooking
process
4 Bleaching Removing
naturally
occurring
colour Bleached
5 Chilling Lowering
the
temperature
below
ambient
but
Chilled
above freezing point to aid preservation
6 Chopping Reduction
of
particle
size
using
one
or
more
Chopped
knives
7 Cleaning Removal
of
objects
(contaminants,
e.g.
stones)
or
Cleaned/sorted
vegetative parts of the plant e.g. unattached
particles of straw or husks or weeds
8 Concentration ( 1 ) Increase
in
certain
contents
by
removal
of
water
Concentrate
and/or other constituents
9 Condensation Transition
of
a
substance
from
a
gaseous
to
a
Condensed
liquid phase
10 Cooking The
application
of
heat
to
change
the
physical
Cooked
and chemical characteristics of feed materials
11 Crushing Reduction
of
particle
size
using
a
crusher Crushed,
crushing
12 Crystallisation Purification
by
the
formation
of
solid
crystals
Crystallised
from a liquid solution. Impurities in the liquid are
usually not incorporated into the lattice structure
of the crystal.

L 29/6
EN
Official Journal of the European Union
30.1.2013
Process Definition Common
name/qualifier
13 Decortication ( 2 ) Complete
or
partial
removal
of
outer
layers
from
Decorticated, partially
grains, seeds, fruits, nuts and others
decorticated
14 Dehulling/dehusking
Removal of the outer skins of beans, grains and Dehulled or dehusked ( 3 )
seeds usually by physical means
15 Depectinising Extraction
of
pectins
from
a
feed
material Depectinised
16 Desiccation Process
of
extracting
moisture Desiccated
17 Desliming Process
used
to
remove
the
slime
layer
on
the
Deslimed
surface
18 Desugaring Complete
or
partial
removal
of
mono-
and
Desugared, partially desugared
disaccharides from molasses and other material
containing sugar by chemical or physical means
19 Detoxification Process
by
which
toxic
contaminants
are
Detoxified
destroyed or reduced in concentration
20 Distillation Fractionation
liquids
by
boiling
and
collecting
the
Distilled
condensed vapour into a separate container
21 Drying Dehydration
by
artificial
or
natural
processes Dried
(sun
or
artificially)
22 Ensiling Storage
of
feed
materials
in
a
silo
possibly
with
Ensiled
the addition of preservatives or by using
anaerobic conditions possibly with silage
additives
23 Evaporation Reducing
the
water
content Evaporated
24 Expansion Thermal
process
during
which
the
product’s
Expanded or puffed
internal water content, abruptly steamed, leads to
the breaking-up of the product
25 Expelling Removal
of
oil/fat
by
pressing Expeller/cake
and
oil/fat
26 Extraction Removal
either
by
organic
solvent
of
fat/oil
from
Extracted/meal and fat/oil,
certain materials or by aqueous solvent of sugar molasses/pulp and sugar or
or other water-soluble components
other water-soluble components
27 Extrusion Thermal
process
during
which
the
product’s
Extruded
internal water content, abruptly steamed, leads to
the breaking-up of the product combined with
special shaping by passing through an orifice

EN
30.1.2013 Official
Journal
of
the
European
Union
L
29/7
Process Definition Common
name/qualifier
28 Fermentation Process
in
which
micro-organisms
such
as
Fermented
bacteria, fungi or yeasts are produced or used to
act on materials to promote a change in their
chemical composition/properties
29 Filtration
Separation of a mixture of liquid and solid
Filtered
materials by passing the liquid through a porous
medium or membrane
30 Flaking Rolling
of
moist
heat-treated
material Flakes
31 Flour
milling Reduction
of
particle
size
of
dry
grain
and
to
Flour, bran, middlings ( 4 ), feed
facilitate separation into constituent fractions
(principally flour, bran and middlings)
32 Fractionation Separation
of
feed
material
fragments
by
sieving
Fractionated
and/or treated with a stream of air that carries the
light shell pieces away
33 Fragmentation
Process of breaking a feed material into fragments Fragmented
34 Frying Process
of
cooking
feed
materials
in
a
oil
or
fat Fried
35 Gelling
Process to form a gel, a solid, jelly-like material Gelled
that can have properties ranging from soft and
weak to hard and tough usually using gelling
agents
36 Granulation Treatment
of
feed
materials
to
obtain
a
specific
Granulated
particle size and consistency
37 Grinding/milling Reducing
the
particle
size
of
solid
feed
materials
Ground or milled
in a dry or wet process
38 Heating Heat
treatments
carried
out
under
specific
Heat treated
conditions
39 Hydrogenation Catalytic
process
aimed
at
saturating
double
Hydrogenated, partially
bonds of oils/fats/fatty acids, carried out at high hydrogenated
temperature under hydrogen pressure, in order to
obtain partially of or fully saturated
triglycerides/fatty acids, or aimed at obtaining
polyols by reduction of carbonyl groups of
carbohydrates to hydroxyl groups
40 Hydrolysis Reduction
of
molecular
size
by
appropriate
Hydrolysed
treatment with water and either heat/pressure,
enzymes or acid/alkali

L 29/8
EN
Official Journal of the European Union
30.1.2013
Process Definition Common
name/qualifier
41 Liquefying
Transition from a solid or a gas phase into a
Liquefied
liquid
42 Maceration Reducing
the
size
of
feed
materials
using
Macerated
mechanical means often in the presence of water
or other liquids
43 Malting Allowing
grain
to
commence
germination
to
Malted
activate naturally occurring enzymes that are able
to break down starch to fermentable
carbohydrates and proteins to amino acids and
peptides
44 Melting
Transition from a solid to a liquid phase by the Melted
application of heat
45 Micronisation
Process of reducing the average diameter of a
Micronised
solid material’s particles to the micrometer scale
46 Parboiling Process
of
soaking
in
water
and
subjecting
to
a
Par-boiled
heat treatment so that the starch is fully
gelatinised, followed by a drying process
47 Pasteurisation
Heating to a critical temperature for a specified
Pasteurised
‘amount’ of time to eliminate harmful micro-
organisms followed by rapid cooling
48 Peeling
Removal of the skin/peel from fruit and
Peeled
vegetables
49 Pelleting Shaping
by
compression
through
a
die Pellet,
pelleted
50 Rice
milling Removing
almost
all
or
part
of
the
bran
and
Milled
embryo from husked rice
51 Pregelatinisation Modification
of
starch
to
improve
significantly
its
Pregelatinised ( 5 )
swelling properties in cold water
52 Pressing ( 6 )
Physical removal of liquids like fat, oil, water or Expeller/cake (in case of oil-
juice from solids
containing materials)
Pulp, pomace (in case of fruits,
etc.)
Pressed pulp (in case of sugar
beet)
53 Refining Complete
or
partial
removal
of
impurities
or
Refined, partially refined
unwanted components by chemical/physical
treatment

EN
30.1.2013 Official
Journal
of
the
European
Union
L
29/9
Process Definition Common
name/qualifier
54 Roasting Heating
of
feed
materials
in
a
dry
state
to
Roasted
improve digestibility, increase colour and/or
reduce naturally occurring anti-nutritive factors
55 Rolling Reduction
of
particle
size
by
passing
the
feed
Rolled
material, e.g. grains, between pairs of rollers
56 Rumen
protection Process
which,
either
by
physical
treatment
with
Rumen protected through the
use of heat, pressure, steam and combination of action of [insert as applicable]
such conditions and/or through the action of e.g.
aldehydes, lignosulfonates, sodium hydroxide or
organic acids (such as propionic or tannic acid)
aims to protect the nutrients from degradation in
the rumen
Feed materials rumen protected by aldehydes may
contain up to 0,12 % of free aldehydes.
57 Sieving/Screening
Separation of particles of different sizes by
Sieved, sifted, screened
passing feed materials through screen(s) while
being shaken or poured
58 Skimming Separating
the
top
floating
layer
of
a
liquid
by
Skimmed
mechanical means, e.g. milk fat
59 Slicing Cutting
feed
materials
into
flat
pieces Sliced
60 Soaking/Steeping Moistening
and
softening
of
feed
materials,
Steeped
usually seeds, to reduce cooking time, aid in seed
coat removal, facilitate the uptake of water to
activate the germination process or reduce the
concentration of naturally occurring anti-nutritive
factors
61 Spray
drying Reducing
the
moisture
content
of
a
liquid
by
Spray dried
creating a spray or mist of the feed material to
increase the surface area to weight ratio through
which warm air is blown
62 Steaming Process
using
pressurised
steam
for
heating
and
Steamed
cooking to increase digestibility
63 Toasting Heating
using
dry
heat
usually
applied
to
oilseeds,
Toasted
e.g. to reduce or remove naturally occurring anti-
nutritive factors

L 29/10
EN
Official Journal of the European Union
30.1.2013
Process Definition Common
name/qualifier
64 Ultra-filtration Filtration
of
liquids
through
a
membrane
Ultra-filtrated
permeable only for small molecules
65 Degermination
Process of complete or partial removal of germ Degermed, degerminated
from crushed cereal grain
66 Infra-red
micronisation Thermal
process
using
infra
red
heat
for
cooking Infra red micronised
and roasting cereals, roots, seeds or tubers, or
their co-products, usually followed by flaking
67 Oil/fats
and
Chemical process of hydrolysis of fats/oils. The
Split
hydrogenated oils/fats
reaction of fats/oils with water, carried out at
splitting
high temperatures and pressures, allows obtaining
crude fatty acids in the hydrophobic phase and
sweet waters (crude glycerol) in the hydrophilic
phase.
( 1 ) In German ‘Konzentrieren’ may be replaced by ‘Eindicken’ where appropriate, in which case the common qualifier should be
‘eingedickt’.
( 2 ) ‘Decortication’ may be replaced by ‘dehulling’ or ‘dehusking’ where appropriate, in which case the common qualifier should be
‘dehulled’ or ‘dehusked’.
( 3 ) In the case of rice, this process is referred to as ‘husking’ and the common qualifier as ‘husked’.
( 4 ) In French the name ‘issues’ may be used.
( 5 ) In German the qualifier ‘aufgeschlossen’ and the name ‘Quellwasser’ (referring to starch) may be used. In Danish the qualifier
‘Kvldning’ and the name ‘Kvldet’ (referring to starch) may be used.
( 6 ) In French ‘Pressage’ may be replaced by ‘Extraction mécanique’ where appropriate.
PART C
List of feed materials
1. Cereal
grains
and
products
derived
thereof
Number Name Description Compulsory
declarations
1.1.1 Barley Grains
of Hordeum vulgare L. It may be rumen
protected
1.1.2 Barley,
puffed Product
obtained
from
milled
or
broken
barley
Starch
by means of a treatment in humid, warm
conditions and under pressure
1.1.3 Barley,
roasted Product
of
barley
roasting
process
which
is
Starch, if > 10 %
partially roasted with low colour
Crude protein, if > 15 %
1.1.4 Barley
flakes Product
obtained
by
steaming
or
infra
red
Starch
micronising and rolling dehusked barley. It may
contain a small proportion of barley husks. It
may be rumen protected.
1.1.5 Barley
fibre Product
of
barley
starch
manufacture.
It
consists
Crude fibre
of particles of endosperm and principally of
fibre.
Crude protein, if > 10 %
1.1.6 Barley
hulls
Product of ethanol-starch manufacture after dry Crude fibre
milling, screening and dehulling of barley grains Crude protein, if > 10 %

EN
30.1.2013 Official
Journal
of
the
European
Union L
29/11
Number Name Description Compulsory
declarations
1.1.7 Barley
middlings Product
obtained
during
the
processing
of
Crude fibre
screened, dehusked barley into pearl barley,
semolina or flour. It consists principally of
Starch
particles of endosperm with fine fragments of
the outer skins and some grain screenings.
1.1.8 Barley
protein
Product from barley obtained after starch and Crude protein
bran separation. It consists principally of
protein.
1.1.9 Barley
protein
feed
Product from barley obtained after starch
Moisture, if < 45 % or > 60 %
separation. It consists principally of protein and
particles of endosperm.
If moisture < 45 %:
— Crude protein
— Starch
1.1.10 Barley
solubles Product
from
barley
obtained
after
wet
protein
Crude protein
and starch extraction
1.1.11 Barley
bran Product
of
flour
manufacture,
obtained
from
Crude fibre
screened grains of dehusked barley. It consists
principally of fragments of the outer skins and
of particles of grain from which the greater part
of the endosperm has been removed.
1.1.12 Liquid
barley
starch Secondary
starch
fraction
from
the
production
If moisture < 50 %:
of starch from barley
— Starch
1.1.13 Malting
barley
Product from mechanical screening (size
Crude fibre
screenings
fractionation) consisting of undersized barley
kernels and fractions of barley kernels separated Crude ash if > 2,2 %
before the malting process
1.1.14 Malting
barley
and
malt Product consisting of fractions of barley kernels Crude fibre
fines
and malt separated during the production of
malt
1.1.15 Malting
barley
husks Product
from
malting
barley
cleaning
consisting
Crude fibre
of fractions of husk and fines
1.1.16 Barley
distillers
solids, Product of ethanol manufacture from barley. It Moisture, if < 65 % or > 88 %
wet
contains solid feed fraction from distillation.
If moisture < 65 %:
— Crude protein
1.1.17 Barley
distillers
Product of ethanol manufacture from barley. It Moisture, if < 45 % or > 70 %
solubles, wet
contains soluble feed fraction from distillation. If moisture < 45 %
— Crude protein
1.1.18 Malt ( 1 ) Product
from
germinated
cereals,
dried,
milled
and/or extracted
1.1.19 Malt
rootlets ( 1 ) Product
from
malting
cereals
germination
and
malt cleaning consisting of rootlets, cereal fines,
husks and small broken malted cereal grains. It
may be milled.
1.2.1 Maize ( 2 ) Grains
of Zea mays L. ssp. mays. It may be
rumen protected.

L 29/12
EN
Official Journal of the European Union
30.1.2013
Number Name Description Compulsory
declarations
1.2.2 Maize
flakes Product
obtained
by
steaming
or
infra
red
Starch
micronising and rolling dehusked maize. It may
contain a small proportion of maize husks.
1.2.3 Maize
middlings Product
of
the
manufacture
of
flour
or
semolina
Crude fibre
from maize. It consists principally of fragments
of the outer skins and of particles of grain from Starch
which less of the endosperm has been removed
than in maize bran. It may contain some maize
germ fragments.
1.2.4 Maize
bran Product
of
the
manufacture
of
flour
or
semolina
Crude fibre
from maize. It consists principally of outer
skins and some maize germ fragments, with
some endosperm particles.
1.2.5 Maize
cobs Central
core
of
a
maize
ear.
It
comprises
Crude fibre
unseparated rachis, grain and leaves.
Starch
1.2.6 Maize
screenings Fraction
of
maize
kernels
separated
by
the
screening process at product intake
1.2.7 Maize
fibre
Product of the manufacture of maize starch. It Moisture, if < 50 % or > 70 %
consists principally of fibre.
If moisture < 50 %:
— Crude fibre
1.2.8 Maize
gluten
Product of the manufacture of maize starch. It Moisture, if < 70 % or > 90 %
consists principally of gluten obtained during
separation of starch.
If moisture < 70 %:
— Crude protein
1.2.9 Maize
gluten
feed Product
obtained
during
the
manufacture
of
Moisture, if < 40 % or > 65 %
maize starch. It is composed of bran and maize
solubles. The product may also include broken If moisture < 40 %:
maize and residues from the oil extraction of
— Crude protein
maize germs. Other products derived from
starch and from the refining or fermentation of — Crude fibre
starch products may be added.
— Starch
1.2.10 Maize
germ
Product of the manufacture of semolina, flour Moisture, if < 40 % or > 60 %
or starch from maize. It consists predominately
of maize germ, outer skins and parts of the
If moisture < 40 %:
endosperm.
— Crude protein
— Crude fat
1.2.11 Maize
germ
expeller Product
of
oil
manufacture
obtained
by
pressing
Crude protein
of processed maize germ to which parts of the
endosperm and testa may still adhere
Crude fat
1.2.12 Maize
germ
meal Product
of
oil
manufacture,
obtained
by Crude protein
extraction of processed maize germ
1.2.13 Crude
maize
germ
oil Product
obtained
from
maize
germ Crude
fat

EN
30.1.2013 Official
Journal
of
the
European
Union L
29/13
Number Name Description Compulsory
declarations
1.2.14 Maize,
puffed Product
obtained
from
milled
or
broken
maize
Starch
by means of a treatment in humid, warm
conditions and under pressure
1.2.15 Maize
steep
liquor Concentrated
liquid
fraction
from
the
steeping
Moisture, if < 45 % or > 65 %
process of corn
If moisture < 45 %:
— Crude protein
1.2.16 Sweet
corn
silage By-product
of
the
sweet
corn
processing Crude fibre
industry, composed of centre cobs, husks, base
of the kernels, chopped and drained or pressed.
Generated by chopping the sweet corn cobs,
husks and leaves, with presence of sweet corn
kernels.
1.2.17 Crushed
degerminated Product obtained by degermination of crushed Crude fibre
(degermed) Maize
maize. It consists principally of endosperm
fragments and may contain some maize germ Starch
and outer skin particles.
1.3.1 Millet Grains
of Panicum miliaceum L.
1.4.1 Oats Grains
of Avena sativa L. and other cultivars of
oats
1.4.2 Dehulled
oats Dehulled
grains
of
oats.
It
may
be
steam
treated.
1.4.3 Oat
flakes Product
obtained
by
steaming
or
infra
red
Starch
micronising and rolling dehusked oats. It may
contain a small proportion of oat husks.
1.4.4 Oat
middlings Product
obtained
during
the
processing
of
Crude fibre
screened, dehusked oats into oat groats and
flour. It consists principally of oat bran and
Starch
some endosperm.
1.4.5 Oat
bran Product
of
flour
manufacture,
obtained
from
Crude fibre
screened grains of dehusked oat. It consists
principally of fragments of the outer skins and
of particles of grain from which the greater part
of the endosperm has been removed.
1.4.6 Oat
hulls Product
obtained
during
dehulling
of
oat
grains Crude
fibre
1.4.7 Oat,
puffed Product
obtained
from
milled
or
broken
oat
by
Starch
means of a treatment in humid, warm
conditions and under pressure
1.4.8 Oat
groats Cleaned
oats
with
the
hull
removed Crude
fibre
Starch
1.4.9 Oat
flour Product
obtained
by
milling
of
oat
grains Crude
fibre
Starch
1.4.10 Fodder
oat
flour Oats
product
with
high
content
in
starch,
after
Crude fibre
decortication

L 29/14
EN
Official Journal of the European Union
30.1.2013
Number Name Description Compulsory
declarations
1.4.11 Oat
feed Product
obtained
during
the
processing
of
Crude Fibre
screened, dehusked oats into oat groats and
flour. It consists principally of oat bran and
some endosperm.
1.5.1 Quinoa
seed,
extracted Cleaned
whole
seed
of
the
quinoa
plant
(Chenopodium quinoa Willd.) from which the
saponin contained in the seeds outer layer has
been removed
1.6.1 Broken
rice Part
of
rice
kernel
of Oryza Sativa L. with a
Starch
length less than three-quarters of a whole
kernel. The rice may have been parboiled.
1.6.2 Milled
rice
Husked rice from which almost all the bran and Starch
embryo have been removed during rice milling.
The rice may have been parboiled.
1.6.3 Pre-gelatinised
rice Product
obtained
from
milled
or
broken
rice
by
Starch
pre-gelatinisation
1.6.4 Extruded
rice Product
obtained
by
extruding
rice
flour Starch
1.6.5 Rice
flakes Product
obtained
by
flaking
pre-gelatinised
rice
Starch
kernels or broken kernels
1.6.6 Husked
rice Paddy
(Oryza Sativa L.) from which the husk
Starch
only has been removed. It may be parboiled.
The processes of husking and handling may
Crude fibre
result in some loss of bran.
1.6.7 Ground
fodder
rice Product
obtained
by
grinding
fodder
rice, Starch
consisting either of green, chalky or unripe
grains, sifted out during the milling of husked
rice, or of normal husked grains which are
yellow or spotted
1.6.8 Rice
flour Product
obtained
by
grinding
milled
rice.
The
Starch
rice may have been parboiled.
1.6.9 Husked
rice,
flour Product
obtained
by
grinding
husked
rice.
The
Starch
rice may have been parboiled.
Crude fibre
1.6.10 Rice
bran Product
obtained
during
rice
milling,
mainly
Crude fibre
consisting of the outer layers of the kernel
(pericarp, seed coat, nucleus, aleurone) with part
of the germ. The rice may have been parboiled
or extruded.
1.6.11 Rice
bran
with
calcium Product obtained during rice milling, mainly
Crude fibre
carbonate
consisting of the outer layers of the kernel
(pericarp, seed coat, nucleus, aleurone) with part Calcium carbonate
of the germ. It may contain up to 23 % of
calcium carbonate used as processing aid. The
rice may have been parboiled.

EN
30.1.2013 Official
Journal
of
the
European
Union L
29/15
Number Name Description Compulsory
declarations
1.6.12 Defatted
rice
bran Rice
bran
resulting
from
oil
extraction.
It
may
Crude fibre
be rumen protected
1.6.13 Rice
bran
oil Oil
extracted
from
stabilised
rice
bran Crude
fat
1.6.14 Rice
middlings Product
of
rice
flour
and
starch
production,
Starch, if > 20 %
obtained by dry or wet milling and sieving. It
consists principally of starch, protein, fat and
Crude protein, if > 10 %
fibre. The rice may have been parboiled. May
Crude fat, if > 5 %
contain up to 0,25 % sodium and up to 0,25 %
sulphate.
Crude fibre
1.6.15 Rice
middlings
with Product obtained during rice milling, mainly
Starch
calcium carbonate
consisting of particles of aleurone layer and
endosperm, It may contain up 23 % of calcium Crude protein
carbonate used as processing aid. The rice may Crude fat
have been parboiled.
Crude fibre
Calcium carbonate
1.6.17 Rice
germ Product
obtained
during
rice
milling,
mainly
Crude fat
consisting of the embryo
Crude protein
1.6.18 Rice
germ
expeller
Product remaining after rice germ has been
Crude protein
crushed to expel the oil
Crude fat
Crude fibre
1.6.20 Rice
protein Product
of
rice
starch
production,
obtained
by
Crude protein
wet milling sieving, separation, concentration
and drying
1.6.21 Liquid
rice
feed Concentrated
liquid
product
of
wet
milling
and
Starch
sieving rice
1.6.22 Rice,
puffed Product
obtained
by
expanding
rice
kernels
or
Starch
broken kernels
1.6.23 Rice,
fermented Product
obtained
by
fermentation
of
rice Starch
1.6.24 Malformed
rice,
Product obtained during rice milling, mainly
Starch
milled/chalky rice,
consisting of malformed kernel and/or chalky
milled
kernel and/or damaged kernel, whole or broken.
It may be parboiled.
1.6.25 Immature
rice,
milled Product
obtained
during
rice
milling,
mainly Starch
consisting of immature and/or chalky kernel
1.7.1 Rye Grains
of Secale cereale L.
1.7.2 Rye
middlings Product
of
flour
manufacture,
obtained
from
Starch
screened rye. It consists principally of particles
of endosperm, with fine fragments of the outer Crude fibre
skins and some miscellaneous parts of the
grain.

L 29/16
EN
Official Journal of the European Union
30.1.2013
Number Name Description Compulsory
declarations
1.7.3 Rye
feed Product
of
flour
manufacture,
obtained
from
Starch
screened rye. It consists principally of fragments
of the outer skins, and of particles of grain
Crude fibre
from which less of the endosperm has been
removed than in rye bran.
1.7.4 Rye
bran Product
of
flour
manufacture,
obtained
from
Starch
screened rye. It consists principally of fragments
of the outer skins, and of particles of grain
Crude fibre
from which most of the endosperm has been
removed
1.8.1 Sorghum;
[Milo] Grains/seeds
of Sorghum bicolor (L.) Moench
1.8.2 Sorghum
white Grains
of
white
Sorghum
1.8.3 Sorghum
gluten
feed Dried
product
obtained
during
the
separation
of
Crude protein
sorghum starch. It consists principally of bran
and a small quantity of gluten. The product
may also include dried residues of maceration
water and germs could be added
1.9.1 Spelt Grains
of
spelt Triticum spelta L., Triticum
dicoccum Schrank, Triticum monococcum
1.9.2 Spelt
bran
Product of the manufacture of spelt flour. It
Crude fibre
consists principally of outer skins and some
spelt germ fragments, with some endosperm
particles.
1.9.3 Spelt
hulls Product
obtained
during
dehulling
of
spelt
Crude fibre
grains
1.9.4 Spelt
middlings Product
obtained
during
the
processing
of
Crude fibre
screened, dehulled spelt into spelt flour. It
consists principally of particles of endosperm
Starch
with fine fragments of the outer skins and some
grain screenings.
1.10.1 Triticale Grains
of Triticum × Secale cereale L. Hybrid
1.11.1 Wheat Grains
of Triticum aestivum L., Triticum durum
Desf. and other cultivars of wheat. It may be
rumen protected.
1.11.2 Wheat
rootlets Product
from
malting
wheat
germination
and
malt cleaning consisting of rootlets, cereal fines,
husks and small broken malted wheat grains
1.11.3 Wheat,
pre-gelatinised Product
obtained
from
milled
or
broken
wheat
Starch
by means of a treatment in humid, warm
conditions and under pressure
1.11.4 Wheat
middlings Product
of
flour
manufacture
obtained
from
Crude fibre
screened grains of wheat or dehusked spelt. It
consists principally of particles of endosperm
Starch
with fine fragments of the outer skins and some
grain screenings.

EN
30.1.2013 Official
Journal
of
the
European
Union L
29/17
Number Name Description Compulsory
declarations
1.11.5 Wheat
flakes Product
obtained
by
steaming
or
infra
red
Crude fibre
micronising and rolling dehusked wheat. It may
contain a small proportion of wheat husks. It Starch
may be rumen protected.
1.11.6 Wheat
feed
Product of flour or malting manufacture
Crude fibre
obtained from screened grains of wheat or
dehusked spelt. It consists principally of
fragments of the outer skins and of particles of
grain from which less of the endosperm has
been removed than in wheat bran.
1.11.7 Wheat
bran ( 3 )
Product of flour or malting manufacture
Crude fibre
obtained from screened grains of wheat or
dehusked spelt. It consists principally of
fragments of the outer skins and of particles of
grain from which the greater part of the
endosperm has been removed.
1.11.8 Malted
fermented
Product obtained by a process combining
Starch
wheat particles
malting and fermentation of wheat and wheat
bran. The product is then dried and ground.
Crude fibre
1.11.10 Wheat
fibre Fibre
extracted
from
wheat
processing.
It
Moisture, if < 60 % or > 80 %
consists principally of fibre.
If moisture < 60 %:
— Crude fibre
1.11.11 Wheat
germ Product
of
flour
milling
consisting
essentially
of
Crude protein
wheat germ, rolled or otherwise, to which
fragments of endosperm and outer skin may
Crude fat
still adhere
1.11.12 Wheat
germ,
fermented Product of fermentation of wheat germ, with
Crude protein
inactivated micro-organisms
Crude fat
1.11.13 Wheat
germ
expeller Product
of
oil
manufacture,
obtained
by
Crude protein
pressing of wheat germ (Triticum aestivum L.,
Triticum durum Desf. and other cultivars of
wheat and dehusked spelt (Triticum spelta L.,
Triticum dicoccum Schrank, Triticum monococcum
L.)) to which parts of the endosperm and testa
may still adhere
1.11.15 Wheat
protein Wheat
protein
extracted
during
starch
or
Crude protein
ethanol production, maybe partially hydrolysed
1.11.16 Wheat
gluten
feed Product
of
the
manufacture
of
wheat
starch
and
Moisture, if < 45 % or > 60 %
gluten. It consists of bran, from which the germ
may have been partially removed. Wheat
If moisture < 45 %:
solubles, broken wheat and other products
— Crude protein
derived from starch and from the refining or
fermentation of starch products may be added. — Starch
1.11.18 Vital
wheat
gluten Wheat
protein
characterised
by
a
high
Crude protein
viscoelasticity as hydrated, with minimum 80 %
protein (N × 6,25) and maximum 2 % ash on
dry substance

L 29/18
EN
Official Journal of the European Union
30.1.2013
Number Name Description Compulsory
declarations
1.11.19 Liquid
wheat
starch Product
obtained
from
the
production
of Moisture, if < 65 % or > 85 %
starch/glucose and gluten from wheat
If moisture < 65 %:
— Starch
1.11.20 Wheat
starch
Product obtained during the production of
Crude protein
containing protein,
wheat starch mainly comprising partially
partially de-sugared
sugared starch, the soluble proteins and other Starch
soluble parts of the endosperm
Total sugar calculated as
sucrose
1.11.21 Wheat
solubles
Product of wheat obtained after wet protein and Moisture if < 55 % or > 85 %
starch extraction. May be hydrolysed
If moisture < 55 %:
— Crude protein
1.11.22 Wheat
yeast
Wet by-product that is released after the
Moisture, if < 60 % or > 80 %
concentrate
fermentation of wheat starch for alcohol
production
If moisture < 60 %:
— Crude protein
1.11.23 Malting
wheat
Product from mechanical screening (size
Crude fibre
screenings
fractionation) consisting of undersized wheat
kernels and fractions of wheat kernels separated
before the malting process
1.11.24 Malting
wheat
and
malt Product consisting of fractions of wheat kernels Crude fibre
fines
and malt separated during the production of
malt
1.11.25 Malting
wheat
husks Product
from
malting
wheat
cleaning
consisting
Crude fibre
of fractions of husk and fines
1.12.2 Grain
flour ( 4 ) Flour
from
milling
grains Starch
Crude fibre
1.12.3 Grain
protein
Concentrate and dried product obtained from
Crude protein
concentrate ( 4 )
grain after starch removing through yeast
fermentation
1.12.4 Cereal
grains
Products from mechanical screening (size
Crude fibre
screenings ( 4 )
fractionation) consisting of small grains and
fractions of grain kernels, which may be
germinated, separated before further processing
of the grain. The products contain more crude
fibre (e.g. hulls) than the unfractionated cereals.
1.12.5 Grain
germ ( 4 ) Product
of
flour
milling
and
the
manufacture
of
Crude protein,
starch consisting principally of grain germ,
rolled or otherwise, to which fragments of
Crude fat
endosperm and outer skin may still adhere

EN
30.1.2013 Official
Journal
of
the
European
Union L
29/19
Number Name Description Compulsory
declarations
1.12.6 Grain
spent
wash
Product of grain obtained through the
Moisture, if < 45 % or > 70 %
syrup ( 4 )
evaporation of the concentrate of the spent
wash from the fermentation and distillation of If moisture < 45 %:
grain used in the production of grain spirit
— Crude protein
1.12.7 Moist
distillers’
Moist product produced as the solid fraction by Moisture, if < 65 % or > 88 %
grains ( 4 )
centrifuging and/or filtration of the spent wash
from fermented and distilled grains used in the If moisture < 65 %:
production of grain spirit
— Crude protein
1.12.8 Concentrated
distillers Moist product from production of alcohol by
Moisture, if < 65 % or > 88 %
solubles ( 4 )
fermentation and distilling a mash of wheat and
sugar syrup after previous separation of bran
If moisture < 65 %:
and gluten. They may contain dead cells and/or — Crude protein, if > 10 %
parts of the fermentation micro-organisms.
1.12.9 Distillers’
grains
and Product obtained when producing alcohol by
Moisture, if < 60 % or > 80 %
solubles ( 4 )
fermentation and distilling grain mash of cereals
and/or other starchy and sugar containing
If moisture < 60 %:
products. They may contain dead cells and/or — Crude protein
parts of the fermentation micro-organisms. May
contain 2 % sulphate. It may be rumen
protected.
1.12.10 Distillers’
dried
grains Product
of
alcohol
distilling
obtained
by
drying
Crude protein
solid residues of fermented grains. It may be
rumen protected.
1.12.11 Distillers’
dark
Product of alcohol distilling obtained by drying Crude protein
grains ( 4 ); [Distillers’
solid residues of fermented grains to which pot
dried grains and
ale syrup or evaporated spent wash has been
solubles] ( 4 )
added. It may be rumen protected.
1.12.12 Brewers’
grains ( 4 ) Product
of
brewing
composed
by
residues
of
Moisture, if < 65 % or > 88 %
malted and unmalted cereals and other starchy
products, which may contain hop materials.
If moisture < 65 %:
Typically marketed in a moist condition but
— Crude protein
may also be sold in a dried form. May contain
up to 0,3 % dimethyl polysiloxane, may contain
up to 1,5 % enzymes, may contain up to 1,8 %
bentonite
1.12.13 Draff ( 4 ) Solid
product
of
cereal
whisky
production.
It
Moisture, if < 65 % or > 88 %
consists of the residues from hot water
extraction of malted cereal. Typically marketed If moisture < 65 %:
in the moist form after the extract has been
— Crude protein
removed by gravity

L 29/20
EN
Official Journal of the European Union
30.1.2013
Number Name Description Compulsory
declarations
1.12.14 Mash
filter
grains Solid
product
obtained
through
the
production
Moisture, if < 65 % or > 88 %
of beer, malt extract and whisky spirit. It
consists of the residues of hot water extraction If moisture < 65 %:
of ground malt and possibly other sugar or
— Crude protein
starch-rich adjuncts. Typically marketed in the
moist form after the extract has been removed
by pressing.
1.12.15 Pot
ale
The product remaining in the still from the first Crude protein, if > 10 %
(wash) distillation of a malt distillery
1.12.16 Pot
ale
syrup Product
from
the
first
(wash)
distillation
of
a
Moisture, if < 45 % or > 70 %
malt distillery produced by evaporating the pot
ale remaining in the still
If moisture < 45 %:
Crude protein
( 1 ) The name may be supplemented by the cereal species.
( 2 ) Please note that ‘maize’ can either be referred to as such or as ‘corn’. This is valid for all maize products.
( 3 ) If this product has been subject to a finer milling the word ‘fine’ may be added to the name or the name may be replaced by a
corresponding denomination.
( 4 ) The name may be supplemented by the grain species.
2. Oil
seeds,
oil
fruits,
and
products
derived
thereof
Number Name Description Compulsory
declarations
2.1.1 Babassu
expeller Product
of
oil
manufacture,
obtained
by Crude protein
pressing Babassu palm nuts Orbignya varieties
Crude fat
Crude fibre
2.2.1 Camelina
seed Seeds
of Camelina sativa L. Crantz
2.2.2 Camelina,
expeller Product
of
oil
manufacture,
obtained
by Crude protein
pressing of seeds of Camelina
Crude fat
Crude fibre
2.2.3 Camelina
meal Product
of
oil
manufacture,
obtained
by
Crude protein
extraction and appropriate heat treatment of
Camelina seed expeller
2.3.1 Cocoa
husks Teguments
of
the
dried
and
roasted
beans
of
Crude fibre
Theobroma cacao L.
2.3.2 Cocoa
hulls Product
obtained
by
processing
of
cocoa
beans Crude
fibre
Crude protein
2.3.3 Cocoa
bean
meal,
Product of oil manufacture, obtained by
Crude protein
partially decorticated
extraction of dried and roasted cocoa beans
Theobroma cacao L. from which part of the husks Crude fibre
has been removed

EN
30.1.2013 Official
Journal
of
the
European
Union L
29/21
Number Name Description Compulsory
declarations
2.4.1 Copra
expeller Product
of
oil
manufacture,
obtained
by
Crude protein
pressing the dried kernel (endosperm) and outer
husk (tegument) of the seed of the coconut
Crude fat
palm Cocos nucifera L.
Crude fibre
2.4.2 Copra,
hydrolysed
Product of oil manufacture, obtained by
Crude protein
expeller
pressing and enzymatic hydrolisation of the
dried kernel (endosperm) and outer husk
Crude fat
(tegument) of the seed of the coconut palm
Crude fibre
Cocos nucifera L.
2.4.3 Copra
meal Product
of
oil
manufacture,
obtained
by
Crude protein
extraction of the dried kernel (endosperm) and
outer husk (tegument) of the seed of the
coconut palm
2.5.1 Cotton
seed Seeds
of Gossypium spp. from which the fibres
have been removed. It may be rumen protected.
2.5.2 Cotton
seed
meal,
Product of oil manufacture, obtained by
Crude protein
partially decorticated
extraction of seeds of cotton from which the
fibres and part of the husks have been removed. Crude fibre
(Maximum crude fibre 22,5 % in the dry
matter). It may be rumen protected.
2.5.3 Cotton
seed
expeller Product
of
oil
manufacture,
obtained
by
Crude protein
pressing of seeds of cotton from which the
fibres have been removed
Crude fibre
Crude fat
2.6.1 Groundnut
expeller, Product of oil manufacture, obtained by
Crude protein
partially decorticated
pressing of partially decorticated groundnuts
Arachis hypogaea L. and other species of Arachis Crude fat
(Maximum crude fibre content 16 % in the dry Crude fibre
matter)
2.6.2 Groundnut
meal,
Product of oil manufacture, obtained by
Crude protein
partially decorticated
extraction of partially decorticated groundnut
expeller (Maximum crude fibre content 16 % in Crude fibre
the dry matter)
2.6.3 Groundnut
expeller, Product of oil manufacture, obtained by
Crude protein
decorticated
pressing of decorticated groundnuts
Crude fat
Crude fibre
2.6.4 Groundnut
meal,
Product of oil manufacture, obtained by
Crude protein
decorticated
extraction of decorticated groundnut expeller
Crude fibre
2.7.1 Kapok
expeller Product
of
oil
manufacture
obtained
by
pressing
Crude protein
of Kapok seeds (Ceiba pentadra L. Gaertn.)
Crude fibre

L 29/22
EN
Official Journal of the European Union
30.1.2013
Number Name Description Compulsory
declarations
2.8.1 Linseed Seeds
of
linseed Linum usitatissimum L.
(Minimum botanical purity 93 %) as whole,
flattened or ground linseed. It may be rumen
protected.
2.8.2 Linseed
expeller Product
of
oil
manufacture,
obtained
by Crude protein
pressing of linseed. (Minimum botanical purity
93 %)
Crude fat
Crude fibre
2.8.3 Linseed
meal Product
of
oil
manufacture,
obtained
by
Crude protein
extraction and appropriate heat treatment of
linseed expeller. It may be rumen protected.
2.8.4 Linseed
expeller
feed Product
of
oil
manufacture,
obtained
by
Crude protein
pressing of linseed. (Minimum botanical purity
93 %). May contain up to 1 % used bleaching
Crude fat
earth and filter aid (e.g. diatomaceous earth,
Crude fibre
amorphous silicates and silica, phyllosilicates
and cellulosic or wood fibres) and crude
lecithins from integrated crushing and refining
plants
2.8.5 Linseed
meal
feed Product
of
oil
manufacture,
obtained
by Crude protein
extraction and appropriate heat treatment of
linseed expeller. May contain up to 1 % used
bleaching earth and filter aid (e.g. diatomaceous
earth, amorphous silicates and silica,
phyllosilicates and cellulosic or wood fibres)
and crude lecithins from integrated crushing
and refining plants. It may be rumen protected
2.9.1 Mustard
bran Product
of
the
manufacture
of
mustard
(Brassica Crude fibre
juncea L.). It consists of fragments of the outer
skins and particles of grain.
2.9.2 Mustard
seed
meal Product
obtained
by
the
extraction
of
volatile
Crude protein
mustard oil from mustard seeds
2.10.1 Niger
seed Seeds
of
the
niger
plant Guizotia abyssinica (L. F.)
Cass
2.10.2 Niger
seed
expeller Product
of
oil
manufacture,
obtained
by Crude protein
pressing of seeds of the niger plant (Ash
insoluble in HCl: maximum 3,4 %)
Crude fat
Crude fibre
2.11.1 Olive
pulp Product
of
oil
manufacture,
obtained
by
Crude protein
extraction of pressed olives Olea europea L.
separated as far as possible from parts of the
Crude fibre
kernel
Crude fat

EN
30.1.2013 Official
Journal
of
the
European
Union L
29/23
Number Name Description Compulsory
declarations
2.11.2 Defatted
olive
meal
Product of olive oil manufacture, obtained by
Crude protein
feed
extraction and appropriate heat treatment of
olive pulp expeller separated as far as possible Crude fibre
from parts of the kernel. May contain up to 1 %
used bleaching earth and filter aid (e.g.
diatomaceous earth, amorphous silicates and
silica, phyllosilicates and cellulosic or wood
fibres) and crude lecithins from integrated
crushing and refining plants
2.11.3 Defatted
olive
meal Product
of
olive
oil
manufacture,
obtained
by
Crude protein
extraction and appropriate heat treatment of
olive pulp expeller separated as far as possible Crude fibre
from parts of the kernel
2.12.1 Palm
kernel
expeller Product
of
oil
manufacture,
obtained
by
Crude protein
pressing of palm kernels Elaeis guineensis Jacq.,
Corozo oleifera (HBK) L. H. Bailey (Elaeis
Crude fibre
melanococca auct.) from which as much as
Crude fat
possible of the hard shell has been removed
2.12.2 Palm
kernel
meal Product
of
oil
manufacture,
obtained
by Crude protein
extraction of palm kernels from which as much
as possible of the hard shell has been removed Crude fibre
2.13.1 Pumpkin
and
squash Seeds of Cucurbita pepo L. and plants of the
seed
genus Cucurbita
2.13.2 Pumpkin
and
squash Product of oil manufacture, obtained by
Crude protein
seed, expeller
pressing of seeds of Cucurbita pepo and plants of
the genus Cucurbita
Crude fat
2.14.1 Rape
seed ( 1 ) Seeds
of
rape Brassica napus L. ssp. oleifera
(Metzg.) Sinsk., of Indian sarson Brassica napus
L. var. glauca (Roxb.) O.E. Schulz and of rape
Brassica rapa ssp. oleifera (Metzg.) Sinsk.
Minimum botanical purity 94 %. It may be
rumen protected.
2.14.2 Rape
seed,
expeller Product
of
oil
manufacture,
obtained
by Crude protein
pressing of seeds of rape. It may be rumen
protected.
Crude fat
Crude fibre
2.14.3 Rape
seed
meal Product
of
oil
manufacture,
obtained
by
Crude protein
extraction and appropriate heat treatment of
rape seed expeller. It may be rumen protected.
2.14.4 Rape
seed,
extruded Product
obtained
from
whole
rape
by
means
of
Crude protein
a treatment in humid, warm conditions and
under pressure increasing starch gelatinisation. Crude fat
It may be rumen protected.

L 29/24
EN
Official Journal of the European Union
30.1.2013
Number Name Description Compulsory
declarations
2.14.5 Rape
seed
protein
Product of oil manufacture, obtained by
Crude protein
concentrate
separation of protein fraction of rape seed
expeller or rape seed
2.14.6 Rape
seed
expeller
feed Product
of
oil
manufacture,
obtained
by
Crude protein
pressing of seeds of rape. May contain up to
1 % used bleaching earth and filter aid (e.g.
Crude fat
diatomaceous earth, amorphous silicates and
Crude fibre
silica, phyllosilicates and cellulosic or wood
fibres) and crude lecithins from integrated
crushing and refining plants. It may be rumen
protected.
2.14.7 Rape
seed
meal
feed Product
of
oil
manufacture,
obtained
by
Crude protein
extraction and appropriate heat treatment of
rape seed expeller. May contain up to 1 % used
bleaching earth and filter aid (e.g. diatomaceous
earth, amorphous silicates and silica,
phyllosilicates and cellulosic or wood fibres)
and crude lecithins from integrated crushing
and refining plants. It may be rumen protected.
2.15.1 Safflower
seed Seeds
of
the
safflower Carthamus tinctorius L.
2.15.2 Safflower
seed
meal, Product of oil manufacture, obtained by
Crude protein
partially decorticated
extraction of partially decorticated seeds of
safflower
Crude fibre
2.15.3 Safflower
hulls Product
obtained
during
dehulling
of
safflower
Crude fibre
seeds
2.16.1 Sesame
seed Seeds
of Sesamum indicum L.
2.17.1 Sesame
seed,
partially Product of oil manufacture, obtained by
Crude protein
dehulled
removing part of the husks
Crude fibre
2.17.2 Sesame
hulls Product
obtained
during
dehulling
of
sesame
Crude fibre
seeds
2.17.3 Sesame
seed
expeller Product
of
oil
manufacture,
obtained
by
Crude protein
pressing of seeds of the sesame plant (Ash
insoluble in HCl: maximum 5 %)
Crude fibre
Crude fat
2.18.1 Toasted
soya
(beans) Soya
beans
(Glycine max. L. Merr.) subjected to
an appropriate heat treatment. (Urease activity
maximum 0,4 mg N/g × min.). It may be rumen
protected.
2.18.2 Soya
(bean)
expeller Product
of
oil
manufacture,
obtained
by
Crude protein
pressing the seed of soya
Crude fat
Crude fibre

EN
30.1.2013 Official
Journal
of
the
European
Union L
29/25
Number Name Description Compulsory
declarations
2.18.3 Soya
(bean)
meal Product
of
oil
manufacture,
obtained
from
soya
Crude protein
beans after extraction and appropriate heat
treatment. (Urease activity maximum 0,4 mg
Crude fibre
N/g × min.)
if > 8 % in dry matter
It may be rumen protected.
2.18.4 Soya
(bean)
meal,
Product of oil manufacture, obtained from
Crude protein
dehulled
dehulled soya beans after extraction and
appropriate heat treatment. (Urease activity
maximum 0,5 mg N/g × min.). It may be rumen
protected.
2.18.5 Soya
(bean)
hulls Product
obtained
during
dehulling
of
soya
Crude fibre
beans
2.18.6 Soya
beans,
extruded Product
obtained
from
soya
beans
by
means
of
Crude protein
a treatment in humid, warm conditions and
under pressure increasing starch gelatinisation. Crude fat
It may be rumen protected.
2.18.7 Soya
(bean)
protein Product obtained from dehulled, fat extracted
Crude protein
concentrate
soya beans, after fermentation or a second
extraction to reduce the level of nitrogen-free
extract
2.18.8 Soya
bean
pulp;
[Soya Product obtained during extraction of soya
Crude protein
bean paste]
beans for food preparation
2.18.9 Soya
bean
molasses Product
obtained
during
the
processing
of
soya
Crude protein
bean
Crude fat
2.18.10 By-product
from
Products obtained when processing soybeans to Crude protein
soybean preparation
obtain soybean food preparations
2.18.11 Soya
(beans) Soya
beans
(Glycine max. L. Merr.) Urease
activity
if
>
0,4
mg
N/g × min
2.18.12 Soybean,
flakes Product
obtained
by
steaming
or
infra
red
Crude protein
micronising and rolling dehulled soya beans
(Urease activity maximum 0,4 mg N/g × min.)
2.18.13 Soya
(bean)
meal
feed Product
of
oil
manufacture,
obtained
from
soya
Crude protein
beans after extraction and appropriate heat
treatment. (Urease activity maximum 0,4 mg
Crude fibre
N/g × min.). May contain up to 1 % used
if > 8 % in dry matter
bleaching earth and filter aid (e.g. diatomaceous
earth, amorphous silicates and silica,
phyllosilicates and cellulosic or wood fibres)
and crude lecithins from integrated crushing
and refining plants. It may be rumen protected.

L 29/26
EN
Official Journal of the European Union
30.1.2013
Number Name Description Compulsory
declarations
2.18.14 Soya
(bean)
meal
feed, Product of oil manufacture, obtained from
Crude protein
dehulled
dehulled soya beans after extraction and
appropriate heat treatment. (Urease activity
maximum 0,5 mg N/g × min.). May contain up
to 1 % used bleaching earth and filter aid (e.g.
diatomaceous earth, amorphous silicates and
silica, phyllosilicates and cellulosic or wood
fibres) and crude lecithins from integrated
crushing and refining plants. It may be rumen
protected.
2.19.1 Sunflower
seed Seeds
of
the
sunflower Helianthus annuus L. It
may be rumen protected.
2.19.2 Sunflower
seed
Product of oil manufacture, obtained by
Crude protein
expeller
pressing of seeds of the sunflower
Crude fat
Crude fibre
2.19.3 Sunflower
seed
meal Product
of
oil
manufacture,
obtained
by
Crude protein
extraction and appropriate heat treatment of
sunflower seed expeller. It may be rumen
protected.
2.19.4 Sunflower
seed
meal, Product of oil manufacture, obtained by
Crude protein
dehulled
extraction and appropriate heat treatment of
expeller of sunflower seeds from which part or Crude fibre
all of the husks has been removed. Maximum
crude fibre 27,5 % in the dry matter
2.19.5 Sunflower
seed
hulls Product
obtained
during
dehulling
of
sunflower
Crude fibre
seeds
2.19.6 Sunflower
seed
meal Product of oil manufacture, obtained by
Crude protein
feed
extraction and appropriate heat treatment of
sunflower seed expeller. May contain up to 1 %
used bleaching earth and filter aid (e.g.
diatomaceous earth, amorphous silicates and
silica, phyllosilicates and cellulosic or wood
fibres) and crude lecithins from integrated
crushing and refining plants. It may be rumen
protected.
2.19.7 Sunflower
seed
meal Product of oil manufacture, obtained by
Crude protein
feed, dehulled
extraction and appropriate heat treatment of
expeller of sunflower seeds from which part or Crude fibre
all of the husks has been removed. May contain
up to 1 % used bleaching earth and filter aid
(e.g. diatomaceous earth, amorphous silicates
and silica, phyllosilicates and cellulosic or wood
fibres) and crude lecithins from integrated
crushing and refining plants Maximum crude
fibre 27,5 % in the dry matter

EN
30.1.2013 Official
Journal
of
the
European
Union L
29/27
Number Name Description Compulsory
declarations
2.20.1 Vegetable
oil
and
fat ( 2 ) Oil
and
fat
obtained
from
plants
(excluding
Moisture, if > 1 %
castor oil from the ricinus plant), it may be
degummed, refined and/or hydrogenated.
2.21.1 Crude
lecithins Product
obtained
during
degumming
of
crude
oil from oilseeds and oil fruits with water. Citric
acid, phosphoric acid or sodium hydroxide may
be added during degumming of the crude oil
2.22.1 Hemp
seed Controlled
hemp
seed Cannabis sativa L. with a
maximum THC content according to EU
legislation
2.22.2 Hemp
expeller Product
of
oil
manufacture
obtained
by
pressing
Crude protein
of hemp seed
Crude fibre
2.22.3 Hemp
oil Product
of
oil
manufacture,
obtained
by
Crude protein
pressing of hemp plant and seed
Crude fat
Crude fibre
2.23.1 Poppy
seed Seeds
of Papaver somniferum L.
2.23.2 Poppy
meal Product
of
oil
manufacture,
obtained
by
Crude protein
extraction of expeller of poppy seed
( 1 ) The indication ‘low in glucosinolate’ as defined in Community legislation may be added, where appropriate. This is valid for all rape
seed products.
( 2 ) The name shall be supplemented by the plant species.
3. Legume
seeds
and
products
derived
thereof
Number Name Description Compulsory
declarations
3.1.1 Beans,
toasted Seeds
of Phaseolus spp. or Vigna spp. submitted
to an appropriate heat treatment. It may be
rumen protected.
3.1.2 Bean
protein
Product obtained from the separated bean fruit Crude protein
concentrate
water, when producing starch
3.2.1 Carob,
dried Dried
fruits
of
the
carob
tree Ceratonia siliqua L. Crude
fibre
3.2.3 Carob
pods,
dried Product
obtained
by
crushing
the
dried
fruits
Crude fibre
(pods) of the carob tree and from which the
locust beans have been removed
3.2.4 Dried
carob
pod
meal, Product obtained by micronisation of the dried Crude fibre
micronised
fruits of the carob tree from which the locust Total sugars, calculated as
beans have been removed
sucrose
3.2.5 Carob
germ
Germ of the locust bean of the carob tree Crude
protein

L 29/28
EN
Official Journal of the European Union
30.1.2013
Number Name Description Compulsory
declarations
3.2.6 Carob
germ,
expeller Product
of
oil
manufacture,
obtained
by
Crude protein
pressing of germ of carob
3.2.7 Locust
bean
(seed) Bean
of
the
carob
tree Crude
fibre
3.3.1 Chick
peas Seeds
of Cicer arietinum L.
3.4.1 Ervil Seeds
of Ervum ervilia L.
3.5.1 Fenugreek
seed Seed
of
fenugreek
(Trigonella foenum-graecum)
3.6.1 Guar
meal
Product obtained after extraction of the
Crude protein
mucilage from seeds of guar bean Cyamopsis
tetragonoloba (L.) Taub
3.6.2 Guar
germs
meal Product
of
mucilage
extraction
from
the
germ
Crude protein
of seeds of guar bean.
3.7.1 Horse
beans Seeds
of Vicia faba L. ssp. faba var. equina Pers.
and var. minuta (Alef.) Mansf.
3.7.2 Horse
bean
flakes Product
obtained
by
steaming
or
infra
red Starch
micronising and rolling dehusked horse beans. Crude protein
3.7.3 Film
horse
beans;
[Faba
Product obtained during dehulling horse bean Crude fibre
bean hulls]
seeds, consisting mainly of external envelopes. Crude protein
3.7.4 Horse
beans,
dehulled Product
obtained
during
dehulling
horse
bean Crude protein
seeds, consisting mainly of bean kernels from
horse beans.
Crude fibre
3.7.5 Horse
bean
protein Product
obtained
by
grinding
and
air
Crude protein
fractionation of horse beans.
3.8.1 Lentils Seeds
of Lens culinaris a.o. Medik.
3.8.2 Lentil
hulls Product
obtained
during
dehulling
process
of
Crude fibre
lentil seeds.
3.9.1 Sweet
lupins Seeds
of Lupinus spp. low in bitter seed content.
3.9.2 Sweet
lupins,
dehulled Dehulled
lupin
seeds. Crude
protein
3.9.3 Film
lupins;
[lupin
Product obtained during dehulling of lupin
Crude protein
hulls]
seeds, consisting mainly of external envelopes. Crude fibre
3.9.4 Lupin
pulp
Product obtained after extraction of
Crude fibre
components of lupin.
3.9.5 Lupin
middlings Product
obtained
during
the
manufacture
of
Crude protein
lupin flour from lupin. It consists principally of
particles of cotyledon, and to a lesser extent, of Crude fibre
skins.
3.9.6 Lupin
protein Product
obtained
from
the
separated
lupin
fruit
Crude protein
water when producing starch, or after grinding
and air fractionation.
3.9.7 Lupin
protein
meal Product
of
lupin
processing
to
produce
a
high
Crude protein
protein meal.

EN
30.1.2013 Official
Journal
of
the
European
Union L
29/29
Number Name Description Compulsory
declarations
3.10.1 Mung
beans Beans
of Vigna radiata L.
3.11.1 Peas Seeds
of Pisum spp. It may be rumen protected.
3.11.2 Pea
bran Product
obtained
during
the
manufacture
of
pea
Crude fibre
meal. It is composed mainly of skins removed
during the skinning and cleaning of peas.
3.11.3 Pea
flakes Product
obtained
by
steaming
or
infra
red
Starch
micronising and rolling dehulled seeds of peas.
3.11.4 Pea
flour Product
obtained
during
the
grinding
of
peas. Crude
protein
3.11.5 Pea
hulls Product
obtained
during
the
manufacture
of
pea
Crude fibre
meal from peas. It is mainly composed of skins
removed during the skinning and cleaning and,
to a lesser extent, of endosperm.
3.11.6 Peas,
dehulled Dehulled
pea
seeds. Crude
protein
Crude fibre
3.11.7 Pea
middlings Product
obtained
during
the
manufacture
of
pea
Crude protein
flour. It consists principally of particles of
cotyledon, and to a lesser extent, of skins.
Crude fibre
3.11.8 Pea
screenings Product
from
the
mechanical
screening
Crude fibre
consisting of fractions of pea kernels separated
before further processing.
3.11.9 Pea
protein Product
obtained
from
the
separated
pea
fruit
Crude protein
water when producing starch, or after grinding
and air fractionation, maybe partially
hydrolysed.
3.11.10 Pea
pulp Product
obtained
from
starch
and
protein
wet
Moisture if < 70 % or > 85 %
extraction from peas. It is mainly composed of
internal fibre and starch.
Starch
Crude fibre
Ash insoluble in HCl,
if > 3,5 % of dry matter
3.11.11 Pea
solubles Product
obtained
from
starch
and
protein
wet
Moisture if < 60 % or > 85 %
extraction from peas. It is mainly composed of
soluble proteins and oligosaccharides.
Total sugars
Crude protein
3.11.12 Pea
fibre
Product obtained by extraction after grinding
Crude fibre
and sieving of the dehulled pea.
3.12.1 Vetches Seeds
of Vicia sativa L. var sativa and other
varieties.
3.13.1 Chickling
vetch Seeds
of Lathyrus sativus L. submitted to an
Method of heat treatment
appropriate heat treatment.
3.14.1 Monantha
vetch Seeds
of Vicia monanthos Desf.

L 29/30
EN
Official Journal of the European Union
30.1.2013
4. Tubers,
roots,
and
products
derived
thereof
Number Name Description Compulsory
declarations
4.1.1 Sugar
beet Root
of Beta vulgaris L. ssp. vulgaris var. altissima
Doell.
4.1.2 Sugar
beet
tops
and Fresh product of the manufacture of sugar
Ash insoluble in HCl, if > 5 %
tails
consisting mainly of cleaned pieces of sugar
of dry matter
beet with or without parts of beet leaves.
Moisture if < 50 %
4.1.3 (Beet)
sugar;
[sucrose] Sugar
extracted
from
sugar
beets
using
water. Sucrose
4.1.4 (Sugar)
beet
molasses Syrupy
product
obtained
during
the
Total sugars, calculated as
manufacture or refining of sugar from sugar
sucrose
beets. May contain up to 0,5 % antifoaming
agents. May contain up to 0,5 % antiscaling
Moisture, if > 28 %
agents. May contain up to 2 % sulphate. May
contain up to 0,25 % sulphite.
4.1.5 (Sugar)
beet
molasses, Product obtained after further extraction using Total sugars, calculated as
partially desugared
water of sucrose and/or betaine from sugar beet sucrose
and/or debetainised
molasses. May contain up to 2 % sulphate. May
contain up to 0,25 % sulphite.
Moisture, if > 28 %
4.1.6 Isomaltulose
molasses Non-crystallised
fraction
from
the
manufacture
Moisture if > 40 %
of isomaltulose by enzymatic conversion of
sucrose from sugar beets.
4.1.7 Wet
(sugar)
beet
pulp Product
of
the
manufacture
of
sugar
consisting
Ash insoluble in HCl, if > 5 %
of slices of sugar beet that have had sugar
of dry matter
extracted with water. Minimum moisture
content: 82 %. Sugar content is low and
Moisture, if < 82 % or > 92 %
declines towards zero due to (lactic acid)
fermentation.
4.1.8 Pressed
(sugar)
beet Product of the manufacture of sugar consisting Ash insoluble in HCl, if > 5 %
pulp
of slices of sugar beet that have had sugar
of dry matter
extracted with water and have been
mechanically pressed. Maximum moisture
Moisture if < 65 % or > 82 %
content: 82 %. Sugar content is low and
declines towards zero due to (lactic acid)
fermentation. May contain up to 1 % sulphate.
4.1.9 Pressed
(sugar)
beet Product of the manufacture of sugar consisting Ash insoluble in HCl, if > 5 %
pulp, molassed
of slices of sugar beet that have had sugar
of dry matter
extracted with water, have been mechanically
pressed, and with molasses added. Maximum
Moisture if < 65 % or > 82 %
moisture content: 82 %. Sugar content declines
due to (lactic acid) fermentation. May contain
up to 1 % sulphate.

EN
30.1.2013 Official
Journal
of
the
European
Union L
29/31
Number Name Description Compulsory
declarations
4.1.10 Dried
(sugar)
beet
pulp Product of the manufacture of sugar consisting Ash insoluble in HCl, if
of slices of sugar beet that have had sugar
> 3,5 % of dry matter
extracted with water, mechanically pressed and
dried. May contain up to 2 % sulphate.
Total sugars, calculated as
sucrose, if > 10,5 %
4.1.11 Dried
(sugar)
beet
pulp, Product of the manufacture of sugar consisting Ash insoluble in HCl, if
molassed
of slices of sugar beet that have had sugar
> 3,5 % of dry matter
extracted with water, mechanically pressed, and
dried, with molasses added. May contain up to Total sugars, calculated as
0,5 % antifoaming agents. May contain up to
sucrose
2 % sulphate.
4.1.12 Sugar
syrup Product
obtained
by
processing
of
sugar
and/or
Total sugars, calculated as
molasses. May contain up to 0,5 % sulphate.
sucrose
May contain up to 0,25 % sulphite.
Moisture, if > 35 %
4.1.13 (Sugar)
beet
pieces,
Product of the manufacture of edible syrup
If dried
boiled
from sugar beet, which may be pressed or
dried.
ash insoluble in HCl, if
> 3,5 % of dry matter
If pressed
ash insoluble in HCl, if > 5 %
of dry matter
Moisture, if < 50 %
4.1.14 Fructo-oligosaccharides Product obtained from sugar from sugar beet
Moisture if > 28 %
through an enzymatic process.
4.2.1 Beetroot
juice Juice
from
pressing
of
red
beet
(Beta vulgaris
Moisture if < 50 % or > 60 %
convar. crassa var. conditiva) with subsequent
concentration and pasteurisation, maintaining
Ash insoluble in HCl, if
the typical vegetable-like taste and flavour.
> 3,5 % of dry matter
4.3.1 Carrots Root
of
the
yellow
or
red
carrot Daucus carota L.
4.3.2 Carrot
peelings,
Moist product from the carrot processing
Starch
steamed
industry consisting of the peelings removed
from the carrot root by steam treatment to
Crude fibre
which auxiliary flows of gelatinous carrot starch Ash insoluble in HCl, if
may be added. Maximum moisture content:
> 3,5 % of dry matter
97 %.
Moisture, if < 87 % or > 97 %
4.3.3 Carrot
scrapings Moist
product
which
is
released
via
mechanical
Starch
separation in the processing of carrots and
which mostly consists of dried carrots and
Crude fibre
carrot remnants. The product may have been
Ash insoluble in HCl, if
subject to heat treatment. Maximum moisture > 3,5 % of dry matter
content: 97 %.
Moisture, if < 87 % or > 97 %
4.3.4 Carrot
flakes Product
obtained
by
flaking
roots
of
the
yellow
or red carrot, which are subsequently dried.
4.3.5 Carrot,
dried Root
of
the
yellow
or
red
carrot
regardless
of
Crude fibre
their presentation, which are subsequently
dried.
4.3.6 Carrot
feed,
dried Product
constituted
of
internal
pulp
and
outer
Crude fibre
skins that are dried.
4.4.1 Chicory
roots Roots
of Cichorium intybus L.

L 29/32
EN
Official Journal of the European Union
30.1.2013
Number Name Description Compulsory
declarations
4.4.2 Chicory
tops
and
tails Fresh
product
from
chicory
processing.
It
Ash insoluble in HCl, if
consists predominantly of cleaned pieces of
> 3,5 % of dry matter
chicory and parts of leaves.
Moisture if < 50 %
4.4.3 Chicory
seed Seed
of Cichorium intybus L.
4.4.4 Pressed
chicory
pulp Product
of
the
manufacture
of
inulin
from
roots
Crude fibre
of Cichorium intybus L. consisting of extracted
and mechanically pressed slices of chicory. The Ash insoluble in HCl, if
(soluble) chicory carbohydrates and water have > 3,5 % of dry matter
been partly removed. May contain up to 1 %
Moisture if < 65 % or > 82 %
sulphate, and may contain up to 0,2 % sulphite.
4.4.5 Dried
chicory
pulp Product
of
the
manufacture
of
inulin
from
roots
Crude fibre
of Cichorium intybus L. consisting of extracted
and mechanically pressed slices of chicory and Ash insoluble in HCl, if
subsequent drying. The (soluble) chicory
> 3,5 % of dry matter
carbohydrates have been partly extracted. May
contain up to 2 % sulphate, and may contain
up to 0,5 % sulphite.
4.4.6 Chicory
roots
powder Product
obtained
by
chopping,
drying
and
Crude fibre
grinding of chicory roots. May contain up to
1 % of anticaking agents.
Ash insoluble in HCl, if
> 3,5 % of dry matter
4.4.7 Chicory
molasses Product
of
chicory
processing,
obtained
during
Crude protein
the production of inulin and oligofructose.
Chicory molasses consists of organic plant
Crude ash
material and minerals. May contain up to 0,5 % Moisture if < 20 % or > 30 %
antifoaming agents.
4.4.8 Chicory
vinasses By-product
from
chicory
processing
obtained
Crude protein
after the separation of inulin and oligofructose
and ion exchange eluation. Chicory vinasses
Crude ash
consists of organic plant material and minerals. Moisture if < 30 % or > 40 %
May contain up to 1 % antifoaming agents.
4.4.9 Chicory
inulin Inulin
is
a
fructan
extracted
from
roots
of
Cichorium intybus L.; raw chicory inulin may
contain up to 1 % sulphate and may contain up
to 0,5 % sulphite.
4.4.10 Oligofructose
syrup Product
obtained
by
partial
hydrolysis
of
inulin
Moisture if < 20 % or > 30 %
from Cichorium intybus L.; raw oligofructose
syrup may contain up to 1 % sulphate and may
contain up to 0,5 % sulphite.
4.4.11 Oligofructose,
dried Product
obtained
by
partial
hydrolysis
of
inulin
from Cichorium intybus L. and subsequent
drying.
4.5.1 Garlic,
dried White
to
yellow
powder
of
pure,
ground
garlic,
Allium sativum L.
4.6.1 Manioc;
[tapioca];
Roots of Manihot esculenta Crantz, regardless of Moisture if < 60 % or > 70 %
[cassava]
their presentation.

EN
30.1.2013 Official
Journal
of
the
European
Union L
29/33
Number Name Description Compulsory
declarations
4.6.2 Manioc,
dried Roots
of
Manioc,
regardless
of
their Starch
presentation, which are subsequently dried.
Ash insoluble in HCl, if
> 3,5 % of dry matter
4.7.1 Onion
pulp Moist
product
which
is
released
during
the
Crude fibre
processing of onions (genus Allium) and
consists of both skins and whole onions. If
Ash insoluble in HCl, if
from the production process for onion oil, then > 3,5 % of dry matter
it mostly consists of cooked remains of onions.
4.7.2 Onions,
fried Skinned
and
crumbed
onion
pieces
which
are
Crude fibre
then fried.
Ash insoluble in HCl, if
> 3,5 % of dry matter
Crude fat
4.7.3 Onions
solubles
Dry product which is released during the
Crude fibre
processing of fresh onions. It is obtained by
alcoholic and/or water extraction, the water or
alcoholic fraction is separated and spray dried.
It consists mainly in carbohydrates.
4.8.1 Potatoes Tubers
of Solanum tuberosum L.
Moisture if < 72 % or > 88 %
4.8.2 Potatoes,
peeled Potatoes
from
which
the
skin
is
removed
using
Starch
steam treatment.
Crude fibre
Ash insoluble in HCl, if
> 3,5 % of dry matter
4.8.3 Potato
peelings,
Moist product from the potato processing
Moisture if < 82 % or > 93 %
steamed
industry consisting of the peelings removed by
steam treatment from the potato tuber to which Starch
auxiliary flows of gelatinous potato starch may Crude fibre
be added. It may be mashed.
Ash insoluble in HCl, if
> 3,5 % of dry matter
4.8.4 Potato
cuttings,
raw Product
released
from
potatoes
during
the Moisture if < 72 % or > 88 %
preparation of potato products for human
consumption, which may have been peeled.
Starch
Crude fibre
Ash insoluble in HCl, if
> 3,5 % of dry matter
4.8.5 Potato
scrapings Product
which
is
released
via
mechanical
Moisture if < 82 % or > 93 %
separation in the processing of potatoes and
which mostly consists of dried potatoes and
Starch
potato remnants. The product may have been Crude fibre
subject to heat treatment.
Ash insoluble in HCl, if
> 3,5 % of dry matter
4.8.6 Potato,
mashed Blanched
or
boiled
and
then
mashed
potato
Starch
product.
Crude fibre
Ash insoluble in HCl, if
> 3,5 % of dry matter

L 29/34
EN
Official Journal of the European Union
30.1.2013
Number Name Description Compulsory
declarations
4.8.7 Potato
flakes Product
obtained
by
rotary
drying
of
washed,
Starch
peeled or unpeeled steamed potatoes.
Crude fibre
Ash insoluble in HCl, if
> 3,5 % of dry matter
4.8.8 Potato
pulp
Product of the manufacture of potato starch
Moisture, if < 77 % or > 88 %
consisting of extracted ground potatoes.
4.8.9 Potato
pulp,
dried
Dried product of the manufacture of potato
starch consisting of extracted ground potatoes.
4.8.10 Potato
protein Product
of
starch
manufacture
composed
Crude protein
mainly of protein substances obtained after the
separation of starch.
4.8.11 Potato
protein,
Protein obtained by a controlled enzymatic
Crude protein
hydrolysed
hydrolysis of potato proteins.
4.8.12 Potato
protein,
Product obtained by fermentation of potato
Crude protein
fermented
protein and subsequent spray drying.
4.8.13 Potato
protein
Liquid product obtained by fermentation of
Crude protein
fermented, liquid
potato protein.
4.8.14 Potato
juice,
Concentrated product of the manufacture of
Moisture if < 50 % or > 60 %
concentrated
potato starch, consisting of the remaining
substance after the partial removal of fibre,
If moisture < 50 %:
proteins and starch from the whole potato pulp — Crude protein
and evaporation of part of the water.
— Crude ash
4.8.15 Potato
granules Dried
potatoes
(potatoes
after
washing,
peeling,
size reduction — cutting, flaking, etc. and water
content removal).
4.9.1 Sweet
potato Tubers
of Ipomoea batatas L. regardless of their Moisture if < 57 % or > 78 %
presentation.
4.10.1 Jerusalem
artichoke; Tubers of Helianthus tuberosus L. regardless of
Moisture if < 75 % or > 80 %
[Topinambur]
their presentation.
5. Other seeds and fruits, and products derived thereof
Number Name Description Compulsory
declarations
5.1.1 Acorn Whole
fruits
of
the
pendunculate
oak Quercus
robur L., the sessile oak Quercus petraea (Matt.)
Liebl., the cork oak of Quercus suber L., or other
species of oak.
5.1.2 Acorn,
dehulled Product
obtained
during
dehulling
of
acorn. Crude
protein
Crude fibre
5.2.1 Almond Whole
or
broken
fruit Prunus dulcis, with or
without hulls.
5.2.2 Almond
hulls Almond
hulls
obtained
from
dehusked
almond
Crude fibre
seeds by physical separation from the kernels
and ground.

EN
30.1.2013 Official
Journal
of
the
European
Union L
29/35
Number Name Description Compulsory
declarations
5.2.3 Almond
kernel
expeller Product
of
oil
manufacture
obtained
by
pressing Crude protein
of almond kernels.
Crude fibre
5.3.1 Anise
seed Seeds
of Pimpinella anisum.
5.4.1 Apple
pulp,
dried;
Product obtained from the production of juice Crude fibre
[apple pomace, dried]
of Malus domestica or cider production. It
consists principally of internal pulp and outer
skins that are dried. It may have been
depectinised.
5.4.2 Apple
pulp,
pressed; Moist product obtained from the production of Crude fibre
[apple pomace, pressed] apple juice or cider production. It consists
principally of internal pulp and outer skins that
are pressed. It may have been depectinised.
5.4.3 Apple
molasses
Product obtained after producing pectin from
Crude protein
apple pulp. It may have been depectinised.
Crude fibre
Crude oils and fats, if > 10 %
5.5.1 Sugar
beet
seed Seeds
of
sugar
beet.
5.6.1 Buckwheat Seeds
of Fagopyrum esculentum.
5.6.2 Buckwheat
hulls
and Product obtained during the milling of
Crude fibre
bran
buckwheat grains.
5.6.3 Buckwheat
middlings Product
of
flour
manufacture,
obtained
from Crude fibre
screened buckwheat. It consists principally of
particles of endosperm, with fine fragments of Starch
the outer and some miscellaneous parts of the
grain. It must contain no more than 10 % crude
fibre.
5.7.1 Red
cabbage
seed Seeds
of Brassica oleracea var. capitata f. Rubra.
5.8.1 Canary
grass
seed Seeds
of Phalaris canariensis.
5.9.1 Caraway
seed Seeds
from Carum carvi L.
5.12.1 Broken
chestnuts
Product of the production of chestnut flour,
Crude protein
consisting mainly of particles of endosperm,
with fine fragments of envelopes and a few
Crude fibre
remnants of chestnut (Castanea spp.).
5.13.1 Citrus
pulp Product
obtained
by
pressing
citrus
fruits Citrus Crude fibre
(L.) spp. or during the production of citrus
juice. It may have been depectinised.
5.13.2 Citrus
pulp,
dried Product
obtained
by
pressing
citrus
fruits
or
Crude fibre
during the production of citrus juice, which is
subsequently dried. It may have been
depectinised.
5.14.1 Red
clover
seed Seeds
of Trifolium pratense L.
5.14.2 White
clover
seed Seeds
of Trifolium repens L.
5.15.1 Coffee
skins Product
obtained
from
dehusked
seeds
of
the
Crude fibre
Coffea plant.

L 29/36
EN
Official Journal of the European Union
30.1.2013
Number Name Description Compulsory
declarations
5.16.1 Cornflower
seed Seeds
of Centaurea cyanus L.
5.17.1 Cucumber
seed Seeds
of Cucumis sativus L.
5.18.1 Cypress
seed Seeds
of Cupressus L.
5.19.1 Date
fruit Fruits
of Phoenix dactylifera L. It may be dried.
5.19.2 Date
seed Whole
seeds
of
the
date
plant. Crude
fibre
5.20.1 Fennel
seed Seeds
of Foeniculum vulgare Mill.
5.21.1 Fig
fruit Fruits
of Ficus carica L. It may be dried.
5.22.1 Fruit
kernels ( 1 ) Product
consisting
of
the
inner,
edible
seeds
of
a nut or fruit stone.
5.22.2 Fruit
pulp ( 1 ) Product
obtained
during
the
production
of
fruit
Crude fibre
juice and fruit puree. It may have been
depectinised.
5.22.3 Fruit
pulp,
dried ( 1 ) Product
obtained
during
the
production
of
fruit
Crude fibre
juice and fruit puree which is subsequently
dried. It may have been depectinised.
5.23.1 Garden
cress Seeds
from Lepidium sativum L. Crude
fibre
5.24.1 Graminaceous
seeds Seeds
from
graminoids
of
the
families Poaceae,
Cyperaceae and Juncaceae.
5.25.1 Grape
pips Pips
from vitis L. separated from grape pulp,
Crude fat
from which the oil has not been removed.
Crude fibre
5.25.2 Grape
pips
meal Product
obtained
during
the
extraction
of
oil
Crude fibre
from grape pips.
5.25.3 Grape
pulp
[grape
Grape pulp dried rapidly after the extraction of Crude fibre
marc]
alcohol from which as much as possible of the
stalks and pips have been removed.
5.25.4 Grape
pips
soluble Product
obtained
from
grape
pips
after Crude fibre
producing grape juice. It principally contains
carbohydrates. It may be concentrated.
5.26.1 Hazelnut Whole
or
broken
fruit
of Corylus (L.) spp., with
or without hulls.
5.26.2 Hazelnut
expeller Product
of
oil
manufacture
obtained
by
pressing
Crude protein
of hazelnut kernels.
Crude fibre

EN
30.1.2013 Official
Journal
of
the
European
Union L
29/37
Number Name Description Compulsory
declarations
5.27.1 Pectin Pectin
is
obtained
by
aqueous
extraction
(of
natural strains) of appropriate plant material,
usually citrus fruits or apples. No organic
precipitant shall be used other than methanol,
ethanol and propane-2-ol. May contain up to
1 % methanol, ethanol and propane-2-ol singly
or in combination, on an anhydrous basis.
Pectin consists mainly of the partial methyl
esters of polygalacturonic acid and their
ammonium, sodium, potassium and calcium
salts.
5.28.1 Perilla
seed Seeds
of Perilla frutescens L. and its milling
products.
5.29.1 Pine
nut Seeds
from Pinus (L.) spp.
5.30.1 Pistachio Fruit
of Pistacia vera L.
5.31.1 Plantago
seed Seeds
of Plantago (L.) spp.
5.32.1 Radish
seed Seeds
of Raphanus sativus L.
5.33.1 Spinach
seed Seeds
of Spinacia oleracea L.
5.34.1 Thistle
seed Seeds
from Carduus marianus L.
5.35.1 Tomato
pulp
[tomato Product obtained by pressing tomatoes Solanum Crude fibre
pomace]
lycopersicum L. during the production of tomato
juice. It consists principally of tomato peel and
seeds.
5.36.1 Yarrow
seed Seeds
of Achillea millefolium L.
5.37.1 Apricot
kernel
expeller Product
of
oil
manufacture
obtained
by
pressing Crude protein
of apricot kernels (Prunus armeniaca L.). It may
contain hydrocyanic acid.
Crude fibre
5.38.1 Black
cumin
expeller Product
of
oil
manufacture
obtained
by
pressing
Crude protein
of black cumin seeds (Bunium persicum L.).
Crude fibre
5.39.1 Borrage
seed
expeller Product
of
oil
manufacture
obtained
by
pressing
Crude protein
of borrage seeds (Borago officinalis L.).
Crude fibre
5.40.1 Evening
primrose
Product of oil manufacture obtained by pressing Crude protein
expeller
of evening primrose seeds (Oenothera L.).
Crude fibre
5.41.1 Pomegranate
expeller Product
of
oil
manufacture
obtained
by
pressing
Crude protein
of pomegranate seeds (Punica granatum L.).
Crude fibre
5.42.1 Walnut
kernel
expeller Product
of
oil
manufacture
obtained
by
pressing Crude protein
of walnut kernels (Juglans regia L.).
Crude fibre
( 1 ) The name shall be supplemented by the plant species.

L 29/38
EN
Official Journal of the European Union
30.1.2013
6. Forages
and
roughage,
and
products
derived
thereof
Number Name Description Compulsory
declarations
6.1.1 Beet
leaves Leaves
of Beta spp.
6.2.1 Cereal
plants ( 1 ) Whole
plants
of
cereal
species
or
parts
thereof.
It may be dried, fresh or ensiled.
6.3.1 Cereals
straw ( 1 ) Straw
of
cereals.
6.3.2 Cereal
straw,
Product obtained by an appropriate treatment Sodium, if treated with NaOH
treated ( 1 ) ( 2 )
of cereal straw.
6.4.1 Clover
meal Product
obtained
by
drying
and
milling
clover Crude protein
Trifolium spp. It may contain up to 20 %
lucerne (Medicago sativa L. and Medicago var.
Crude fibre
Martyn) or other forage crops dried and milled Ash insoluble, in HCI, if
at the same time as the clover.
> 3,5 % of dry matter
6.5.1 Forage
meal ( 3 ); [Grass
Product obtained by drying and milling and in Crude protein
meal] ( 3 ); [Green
some cases compacting forage plants.
meal] (
Crude fibre

3 )
Ash insoluble, in HCI, if
> 3,5 % of dry matter
6.6.1 Grass,
field
dried,
[Hay] Species
of
any
grass,
field
dried. Ash
insoluble,
in
HCI,
if
> 3,5 % of dry matter
6.6.2 Grass,
high
temperature
Product obtained from grass (any variety) that Crude protein
dried
has been artificially dehydrated (in any form).
Fibre
Ash insoluble, in HCI, if
> 3,5 % of dry matter
6.6.3 Grass,
herbs,
legume Fresh, ensiled or dried arable crops consisting of Ash insoluble, in HCI, if
plants, [green forage]
grass, legumes or herbs, commonly described as > 3,5 % of dry matter
silage, haylage, hay or green forage.
6.7.1 Hemp
flour Flour
ground
from
dried
leaves
from
Cannabis Crude protein
sativa L.
6.7.2 Hemp
fibre Product
obtained
during
the
processing
of
hemp, green coloured, dried, fibrous.
6.8.1 Horse
bean
straw Straw
of
horse
bean.
6.9.1 Linseed
straw Straw
of
linseed
(Linum usitatissimum L.).
6.10.1 Lucerne;
[alfalfa] Medicago
sativa L. and Medicago var. Martyn
Ash insoluble, in HCI, if
plants or parts thereof.
> 3,5 % of dry matter
6.10.2 Lucerne
field
dried;
Lucerne, field dried. Ash
insoluble,
in
HCI,
if
[alfalfa field dried]
> 3,5 % of dry matter

EN
30.1.2013 Official
Journal
of
the
European
Union L
29/39
Number Name Description Compulsory
declarations
6.10.3 Lucerne,
high
Lucerne artificially dehydrated, in any form. Crude
protein
temperature dried;
[alfalfa, high
Crude fibre
temperature dried]
Ash insoluble, in HCI, if
> 3,5 % of dry matter
6.10.4 Lucerne,
extruded;
Alfalfa pellets that have been extruded.
[alfalfa, extruded]
6.10.5 Lucerne
meal ( 4 ); [alfalfa Product obtained by drying and milling
Crude protein
meal] ( 4 )
Lucerne. It may contain up to 20 % clover or
other forage crop dried and milled at the same Crude fibre
time as the lucerne.
Ash insoluble, in HCI, if
> 3,5 % of dry matter
6.10.6 Lucerne
pomace;
Dried product obtained by pressing of the juice Crude protein
[alfalfa pomace]
from lucerne.
Crude fibre
6.10.7 Lucerne
protein
Product obtained by artificially drying fractions Crude protein
concentrate; [alfalfa
of lucerne press juice, which have been
protein concentrate]
separated by centrifugation and heat treated to Carotene
precipitate the proteins.
6.10.8 Lucerne
solubles Product
obtained
after
the
extraction
of
proteins
Crude protein
from lucerne juice, it may be dried
6.11.1 Maize
silage Ensiled
plants
or
parts
thereof
of Zea mays L.
ssp. mays.
6.12.1 Pea
Straw Straw
of Pisum spp.
( 1 ) The name shall be supplemented by the plant species.
( 2 ) The name must be supplemented by an indication of the nature of the treatment carried out.
( 3 ) The species of forage crop may be added to the name.
( 4 ) The term ‘meal’ may be replaced by ‘pellets’. The method of drying may be added to the name.
7. Other
plants,
algae
and
products
derived
thereof
Number Name Description Compulsory
declarations
7.1.1 Algae ( 1 ) Algae,
live
or
processed,
including
fresh,
chilled
Crude protein
or frozen algae. May contain up to 0,1 % of
antifoaming agents.
Crude fat
Crude ash
7.1.2 Dried
algae ( 1 ) Product
obtained
by
drying
algae.
This
product
Crude protein
may have been washed to reduce the iodine
content. May contain up to 0,1 % of
Crude fat
antifoaming agents.
Crude ash
7.1.3 Algae
meal ( 1 ) Product
of
algae
oil
manufacture,
obtained
by
Crude protein
extraction of algae. May contain up to 0,1 % of
antifoaming agents.
Crude fat
Crude ash
7.1.4 Algal
oil ( 1 ) Product
of
the
oil
manufacture
from
algae
Crude fat
obtained by extraction. May contain up to
0,1 % of antifoaming agents.
Moisture if > 1 %

L 29/40
EN
Official Journal of the European Union
30.1.2013
Number Name Description Compulsory
declarations
7.1.5 Algae
extract ( 1 ); [algae Watery or alcoholic extract of algae that
fraction] ( 1 )
principally contains carbohydrates. May contain
up to 0,1 % of antifoaming agents.
7.2.6 Seaweed
meal Product
obtained
by
drying
and
crushing
Crude ash
macro-algae, in particular brown seaweed. This
product may have been washed to reduce the
iodine content. May contain up to 0,1 % of
antifoaming agents.
7.3.1 Barks ( 2 ) Cleaned
and
dried
barks
of
trees
or
bushes. Crude
fibre
7.4.1 Blossoms ( 2 ), dried
All parts of dried blossoms of consumable
Crude fibre
plants and their fractions.
7.5.1 Broccoli,
dried Product
obtained
by
drying
the
plant Brassica
oleracea L. after washing, size reduction (cutting,
flaking, etc.) and water content removal.
7.6.1 (Sugar)
cane
molasses Syrupy
product
obtained
during
the
Total sugars calculated as
manufacture or refining of sugar from
sucrose
Saccharum L. May contain up to 0,5 %
antifoaming agents. May contain up to 0,5 %
Moisture, if > 30 %
antiscaling agents. May contain up to 3,5 %
sulphate. May contain up to 0,25 % sulphite.
7.6.2 (Sugar)
cane
Molasses, Product obtained after further extraction using Total sugars calculated as
partially desugared
water of sucrose from sugar cane molasses.
sucrose
Moisture, if > 28 %
7.6.3 (Cane)
sugar
[sucrose] Sugar
extracted
from
sugar
canes
using
water. Sucrose
7.6.4 Cane
bagasse Product
obtained
during
extraction
using
water
Crude fibre
of sugar from sugar canes. It consists mainly of
fibres.
7.7.1 Leaves,
dried, ( 2 ) Dried
leaves
of
consumable
plants
and
their
Crude fibre
fractions.
7.8.1 Lignocellulose ( 2 ) Product
obtained
by
means
of
mechanical
Crude fibre
processing of raw natural dried wood and
which predominantly consists of lignocellulose.
7.9.1 Liquorice
root Root
of Glycyrrhiza L.
7.10.1 Mint Product
obtained
from
drying
aerial
parts
of
the
plants Mentha apicata, Mentha piperita or Mentha
viridis (L.), regardless of their presentation.
7.11.1 Spinach,
dried Product
obtained
from
drying
the
plant Spinacia
oleracea L., regardless of its presentation.

EN
30.1.2013 Official
Journal
of
the
European
Union L
29/41
Number Name Description Compulsory
declarations
7.12.1 Mojave
yucca Pulverised Yucca schidigera Roezl. Crude
fibre
7.13.1 Vegetal
carbon;
Product obtained by carbonisation of organic
Crude fibre
[charcoal]
vegetal material.
7.14.1 Wood ( 2 ) Chemically
untreated
mature
wood
or
wood
Crude fibre
fibres.
( 1 ) The name shall be supplemented by the species.
( 2 ) Expressions are not synonymous and differ mainly in their moisture content, respective expression to be used as appropriate.
8. Milk products and products derived thereof
Number Name Description Compulsory
declarations
8.1.1 Butter
and
butter
Butter and products obtained by production or Crude protein
products
processing of butter (e.g. butter serum), unless
listed separately.
Crude fat
Lactose
Moisture if > 6 %
8.2.1 Buttermilk/buttermilk Product obtained by churning butter out of
Crude protein
powder ( 1 )
cream or similar processes.
Crude fat
Concentration and/or drying may be applied.
Lactose
Where specifically prepared as feed material,
may contain:
Moisture if > 6 %
— up to 0,5 % phosphates e.g. polyphosphates
(e.g. sodium hexametaphosphate),
diphosphates (e.g.
tetrasodiumpyrophosphate), used to
decrease the viscosity and to stabilise
protein during processing;
— up to 0,3 % acids e.g. organic acids: citric
acid, formic acid, propionic acid, Inorganic
acids: sulphuric acid, hydrochloric acid,
phosphoric acid, used for pH adjustments in
many parts of production processes;
— up to 0,5 % akalis e.g. sodium, potassium,
calcium, magnesium hydroxides, used for
pH adjustments in many parts of
production processes;
— up to 2 % free-flowing agents e.g. silicium
dioxide, penta-sodium-triphosphate, tri-
calcium-phosphate, used to improve powder
flowing properties;
— up to 0,4 % emulsifier lecithin.

L 29/42
EN
Official Journal of the European Union
30.1.2013
Number Name Description Compulsory
declarations
8.3.1 Casein Product
obtained
from
skimmed
or
buttermilk
Crude protein
by drying casein precipitated by means of acids
or rennet.
Moisture if > 10 %
8.4.1 Caseinate
Product extracted from curd or casein through Crude protein
use of neutralising substances and drying.
Moisture if > 10 %
8.5.1 Cheese
and
cheese
Cheese and products made of cheese and of
Crude protein
products
milk based products.
Crude fat
8.6.1 Colostrum/colostrum The fluid secreted by the mammary glands of Crude protein
powder
milk-producing animals up to five days post
parturition. Concentration and/or drying may
be applied.
8.7.1 Dairy
by-products Products
obtained
when
producing
dairy Moisture
products (including, but not limited to: former
dairy foodstuffs, centrifuge or separator sludge, Crude protein
white water, milk minerals).
Crude fat
Where specifically prepared as feed material,
may contain:
Total sugars
— up to 0,5 % phosphates e.g. polyphosphates
(e.g. sodium hexametaphosphate),
diphosphates (e.g.
tetrasodiumpyrophosphate), used to
decrease the viscosity and to stabilise
protein during processing;
— up to 0,3 % acids e.g. organic acids: citric
acid, formic acid, propionic acid, Inorganic
acids: sulphuric acid, hydrochloric acid,
phosphoric acid, used for pH adjustments in
many parts of production processes;
— up to 0,5 % akalis e.g. sodium, potassium,
calcium, magnesium hydroxides, used for
pH adjustments in many parts of
production processes;
— up to 2 % free-flowing agents e.g. silicium
dioxide, penta-sodium-triphosphate, tri-
calcium-phosphate, used to improve powder
flowing properties;
— up to 0,4 % emulsifier lecithin.
8.8.1 Fermented
milk
Products obtained by fermentation of milk (e.g. Crude protein
products
yoghurt etc.).
Crude fat
8.9.1 Lactose The
sugar
separated
from
milk
or
whey
by
Lactose
purification and drying.
Moisture if > 5 %
8.10.1 Milk/milk
powder ( 1 ) Normal
mammary
secretion
obtained
from
one
Crude protein
or more milkings. Concentration and/or drying
may be applied.
Crude fat
Moisture if > 5 %

EN
30.1.2013 Official
Journal
of
the
European
Union L
29/43
Number Name Description Compulsory
declarations
8.11.1 Skimmed
Milk whose fat content has been reduced by
Crude protein
milk/skimmed milk
separation.
powder ( 1 )
Moisture if > 5 %
Concentration and/or drying may be applied.
8.12.1 Milk
fat Product
obtained
by
skimming
milk. Crude
fat
8.13.1 Milk
protein
powder Product
obtained
by
drying
the
protein
Crude protein
compounds extracted from milk by chemical or
physical treatment.
Moisture if > 8 %
8.14.1 Condensed
and
Condensed and evaporated milk and products Crude protein
evaporated milk and
obtained by production or processing of these
their products
products.
Crude fat
Moisture if > 5 %
8.15.1 Milk
permeate/Milk
Product obtained by filtration (ultra, nano or
Crude ash
permeate powder ( 1 )
micro) of milk (penetrating through the
membrane) and from which lactose may have Crude protein
been partly removed.
Lactose
Reverse osmosis and concentration and/or
drying may be applied.
Moisture if > 8 %
8.16.1 Milk
retentate/milk
Product obtained by filtration (ultra, nano or
Crude protein
retentate powder ( 1 )
micro) of milk (withheld by the membrane).
Crude ash
Concentration and/or drying may be applied.
Lactose
Moisture if > 8 %
8.17.1 Whey/whey
powder ( 1 ) Product
of
cheese,
quark
or
casein
Crude protein
manufacturing or similar processes.
Lactose
Concentration and/or drying may be applied.
Moisture if > 8 %
Where specifically prepared as feed material,
may contain:
Crude ash
— up to 0,5 % phosphates e.g. polyphosphates
(e.g. sodium hexametaphosphate),
diphosphates (e.g.
tetrasodiumpyrophosphate), used to
decrease the viscosity and to stabilise
protein during processing;
— up to 0,3 % acids e.g. organic acids: citric
acid, formic acid, propionic acid, Inorganic
acids: sulphuric acid, hydrochloric acid,
phosphoric acid, used for pH adjustments in
many parts of production processes;
— up to 0,5 % akalis e.g. sodium, potassium,
calcium, magnesium hydroxides, used for
pH adjustments in many parts of
production processes;
— up to 2 % free-flowing agents e.g. silicium
dioxide, penta-sodium-triphosphate, tri-
calcium-phosphate, used to improve powder
flowing properties;
— up to 0,4 % emulsifier lecithin.

L 29/44
EN
Official Journal of the European Union
30.1.2013
Number Name Description Compulsory
declarations
8.18.1 Delactosed
Whey from which the lactose has been partly Crude protein
whey/delactosed whey removed.
powder (
Lactose

1 )
Concentration and/or drying may be applied.
Moisture if > 8 %
Where specifically prepared as feed material,
may contain:
Crude ash
— up to 0,5 % phosphates e.g. polyphosphates
(e.g. sodium hexametaphosphate),
diphosphates (e.g.
tetrasodiumpyrophosphate), used to
decrease the viscosity and to stabilise
protein during processing;
— up to 0,3 % acids e.g. organic acids: citric
acid, formic acid, propionic acid, Inorganic
acids: sulphuric acid, hydrochloric acid,
phosphoric acid, used for pH adjustments in
many parts of production processes;
— up to 0,5 % akalis e.g. sodium, potassium,
calcium, magnesium hydroxides, used for
pH adjustments in many parts of
production processes;
— up to 2 % free-flowing agents e.g. silicium
dioxide, penta-sodium-triphosphate, tri-
calcium-phosphate, used to improve powder
flowing properties;
— up to 0,4 % emulsifier lecithin.
8.19.1 Whey
protein/whey Product obtained by drying the whey protein
Crude protein
protein powder ( 1 )
compounds extracted from whey by chemical
or physical treatment. Concentration and/or
Moisture if > 8 %
drying may be applied.
Where specifically prepared as feed material,
may contain:
— up to 0,5 % phosphates e.g. polyphosphates
(e.g. sodium hexametaphosphate),
diphosphates (e.g.
tetrasodiumpyrophosphate), used to
decrease the viscosity and to stabilise
protein during processing;
— up to 0,3 % acids e.g. organic acids: citric
acid, formic acid, propionic acid, Inorganic
acids: sulphuric acid, hydrochloric acid,
phosphoric acid, used for pH adjustments in
many parts of production processes;
— up to 0,5 % akalis e.g. sodium, potassium,
calcium, magnesium hydroxides, used for
pH adjustments in many parts of
production processes;
— up to 2 % free-flowing agents e.g. silicium
dioxide, penta-sodium-triphosphate, tri-
calcium-phosphate, used to improve powder
flowing properties;
— up to 0,4 % emulsifier lecithin.

EN
30.1.2013 Official
Journal
of
the
European
Union L
29/45
Number Name Description Compulsory
declarations
8.20.1 Demineralised,
Whey from which the lactose and minerals
Crude protein
delactosed
have been partly removed.
Lactose
whey/demineralised,
delactosed whey
Concentration and/or drying may be applied.
Crude ash
powder ( 1 )
Where specifically prepared as feed material,
Moisture if > 8 %
may contain:
— up to 0,5 % phosphates e.g. polyphosphates
(e.g. sodium hexametaphosphate),
diphosphates (e.g.
tetrasodiumpyrophosphate), used to
decrease the viscosity and to stabilise
protein during processing;
— up to 0,3 % acids e.g. organic acids: citric
acid, formic acid, propionic acid, Inorganic
acids: sulphuric acid, hydrochloric acid,
phosphoric acid, used for pH adjustments in
many parts of production processes;
— up to 0,5 % akalis e.g. sodium, potassium,
calcium, magnesium hydroxides, used for
pH adjustments in many parts of
production processes;
— up to 2 % free-flowing agents e.g. silicium
dioxide, penta-sodium-triphosphate, tri-
calcium-phosphate, used to improve powder
flowing properties;
— up to 0,4 % emulsifier lecithin.
8.21.1 Whey
permeate/whey Product obtained by filtration (ultra, nano or
Crude ash
permeate powder ( 1 )
micro) of whey (penetrating through the
Crude protein
membrane) and from which lactose may have
been partly removed. Reverse osmosis and
Lactose
concentration and/or drying may be applied.
Moisture if > 8 %
Where specifically prepared as feed material,
may contain:
— up to 0,5 % phosphates e.g. polyphosphates
(e.g. sodium hexametaphosphate),
diphosphates (e.g.
tetrasodiumpyrophosphate), used to
decrease the viscosity and to stabilise
protein during processing;
— up to 0,3 % acids e.g. organic acids: citric
acid, formic acid, propionic acid, Inorganic
acids: sulphuric acid, hydrochloric acid,
phosphoric acid, used for pH adjustments in
many parts of production processes;
— up to 0,5 % akalis e.g. sodium, potassium,
calcium, magnesium hydroxides, used for
pH adjustments in many parts of
production processes;
— up to 2 % free-flowing agents e.g. silicium
dioxide, penta-sodium-triphosphate, tri-
calcium-phosphate, used to improve powder
flowing properties;
— up to 0,4 % emulsifier lecithin.

L 29/46
EN
Official Journal of the European Union
30.1.2013
Number Name Description Compulsory
declarations
8.22.1 Whey
retentate/whey Product obtained by filtration (ultra, nano or
Crude protein
retentate powder ( 1 )
micro) of whey (withheld by the membrane).
Crude ash
Concentration and/or drying may be applied.
Lactose
Where specifically prepared as feed material,
Moisture if > 8 %
may contain:
— up to 0,5 % phosphates e.g. polyphosphates
(e.g. sodium hexametaphosphate),
diphosphates (e.g.
tetrasodiumpyrophosphate), used to
decrease the viscosity and to stabilise
protein during processing;
— up to 0,3 % acids e.g. organic acids: citric
acid, formic acid, propionic acid, Inorganic
acids: sulphuric acid, hydrochloric acid,
phosphoric acid, used for pH adjustments in
many parts of production processes;
— up to 0,5 % akalis e.g. sodium, potassium,
calcium, magnesium hydroxides, used for
pH adjustments in many parts of
production processes;
— up to 2 % free-flowing agents e.g. silicium
dioxide, penta-sodium-triphosphate, tri-
calcium-phosphate, used to improve powder
flowing properties;
— up to 0,4 % emulsifier lecithin.
( 1 ) Expressions are not synonymous and differ mainly in their moisture content, respective expression to be used as appropriate.
9. Land animal products and products derived thereof
Number Name Description Compulsory
declarations
9.1.1 Animal
by-products ( 1 ) Whole
or
parts
of
warm-blooded
land
animals, Crude protein
fresh, frozen, cooked, acid treated or dried.
Crude fat
Moisture if > 8 %
9.2.1 Animal
fat ( 2 ) Product
composed
of
fat
from
warm-blooded
Crude fat
land animals.
Moisture if > 1 %
If extracted with solvents, may contain up to
0,1 % hexane.
9.3.1 Apiculture
by-products Honey,
beeswax,
royal
jelly,
propolis,
pollen, Total sugar calculated as
processed or unprocessed
sucrose
9.4.1 Processed
animal
Product obtained by heating, drying and
Crude protein
protein ( 2 )
grinding whole or parts of warm-blooded land Crude fat
animals from which the fat may have been
partially extracted or physically removed
Crude ash
If extracted with solvents, may contain up to
Moisture if > 8 %
0,1 % hexane.

EN
30.1.2013 Official
Journal
of
the
European
Union L
29/47
Number Name Description Compulsory
declarations
9.5.1 Gelatine
process
Dried animal proteins of food quality derived
Crude protein
derived proteins ( 2 )
from gelatine production.
Crude fat
Crude ash
Moisture if > 8 %
9.6.1 Hydrolysed
animal
Hydrolysed proteins obtained by heat and/or
Crude protein
proteins ( 2 )
pressure, chemical, microbiological or
Moisture if > 8 %
enzymatic hydrolysis of animal protein.
9.7.1 Blood
meal ( 2 ) Product
derived
from
the
heat
treatment
of
Crude protein
blood of slaughtered warm-blooded animals.
Moisture if > 8 %
9.8.1 Blood
products ( 1 ) Products
derived
from
blood
or
fractions
of
Crude protein
blood of slaughtered warm-blooded animals;
Moisture if > 8 %
they include dried/frozen/liquid plasma, dried
whole blood, dried/frozen/liquid red cells or
fractions thereof and mixtures.
9.9.1 Catering
reflux
All waste food containing material of animal
Crude protein
[catering recycling]
origin including used cooking oil originating in Crude fat
restaurants, catering facilities and kitchens,
including central kitchens and household
Crude ash
kitchens.
Moisture if > 8 %
9.10.1 Collagen ( 2 ) Protein-based
product
derived
from
animal
Crude protein
bones, hides, skins and tendons.
Moisture if > 8 %
9.11.1 Feather
meal Product
obtained
by
drying
and
grinding
Crude protein
feathers of slaughtered animals, it may be
Moisture if > 8 %
hydrolysed.
9.12.1 Gelatine ( 2 ) Natural,
soluble
protein,
gelling
or
non-gelling,
Crude protein
obtained by the partial hydrolysis of collagen
Moisture if > 8 %
produced from bones, hides and skins, tendons
and sinews of animals.
9.13.1 Greaves ( 2 ) Product
obtained
from
the
manufacture
of
Crude protein
tallow, lard and other extracted or physically
Crude fat
removed fats of animal origin, fresh, frozen or
dried.
Crude ash
If extracted with solvents, may contain up to
Moisture if > 8 %
0,1 %hexane.
9.14.1 Products
of
animal
Former foodstuff containing animal products;
Crude protein
origin ( 1 )
with or without treatment such as fresh, frozen, Crude fat
dried.
Moisture if > 8 %
9.15.1 Eggs Whole
eggs
of Gallus gallus L. with or without
shells.

L 29/48
EN
Official Journal of the European Union
30.1.2013
Number Name Description Compulsory
declarations
9.15.2 Albumen
Product obtained from eggs after the separation Crude protein
of shells and yolk, pasteurised and possibly
Method of denaturation if
denatured.
applicable
9.15.3 Egg
products,
dried Products
consisting
of
pasteurised
dried
eggs,
Crude protein
without shells or a mixture of different
Crude fat
proportions of dried albumen and dried egg
yolk.
Moisture if > 5 %
9.15.4 Egg
powder
sugared Dried
whole
or
parts
of
sugared
eggs. Crude
protein
Crude fat
Moisture if > 5 %
9.15.5 Egg
shells,
dried
Product obtained from poultry eggs, after the
Crude ash
content (yolk and albumen) has been removed.
Shells are dried.
9.16.1 Terrestrial
Whole or parts of terrestrial invertebrates, in all
invertebrates ( 1 )
their life stages, other than species pathogenic
to humans and animals; with or without
treatment such as fresh, frozen, dried.
9.17.1 Chondroitin
sulphate Product
obtained
by
extraction
from
tendons, Sodium
bones and other animal tissues containing
cartilage and soft connective tissues.
( 1 ) Without prejudice to mandatory requirements concerning commercial documents and health certificates for animal by-products and
derived products as laid down in Commission Regulation (EU) No 142/2011 (Annex VIII, Chapter III) (OJ L 54, 26.2.2011, p. 1), if the
catalogue is used for labelling purposes the name shall be, replaced as appropriate by
— the animal species and
— the part of the animal product (e.g. liver, meat (only if skeletal muscle)), and/or
— the naming of the animal species not used in respect of the ban on intra-species recycling (e.g. poultry-free) or
supplemented as appropriate by
— the animal species and/or
— the part of the animal product (e.g. liver, meat (only if skeletal muscle)), and/or
— the naming of the animal species not used in respect of the ban on intra-species recycling.
( 2 ) Without prejudice to mandatory requirements concerning commercial documents and health certificates for animal by-products and
derived products as laid down in Regulation (EU) No 142/2011 (Annex VIII, Chapter III), if the catalogue is used for labelling purposes
the name shall be supplemented as appropriate by
— the animal species processed (e.g. porcine, ruminant, avian) and/or
— the material processed (e.g. bone) and/or
— the process used (e.g. defatted, refined) and/or
— the naming of the animal species not used in respect of the ban on intra-species recycling (e.g. poultry-free).
10. Fish, other aquatic animals and products derived thereof
Number Name Description Compulsory
declarations
10.1.1 Aquatic
Whole or parts of marine or freshwater
invertebrates ( 1 )
invertebrates, in all their life stages, other than
species pathogenic to humans and animals;
with or without treatment such as fresh, frozen,
dried.
10.2.1 By-products
from
Originating from establishments or plants
Crude protein
aquatic animals ( 1 )
preparing or manufacturing products for
Crude fat
human consumption; with or without treatment
such as fresh, frozen, dried.
Crude ash
10.3.1 Crustacea
meal Product
produced
by
heating,
pressing
and
Crude protein
drying whole or parts of crustacean including Crude fat
wild and farmed shrimp.
Crude ash, if > 20 %
Moisture if > 8 %

EN
30.1.2013 Official
Journal
of
the
European
Union L
29/49
Number Name Description Compulsory
declarations
10.4.1 Fish ( 2 ) Whole
or
parts
of
fish:
fresh,
frozen,
cooked,
Crude protein
acid treated or dried.
Moisture if > 8 %
10.4.2 Fish
meal ( 2 ) Product
obtained
by
heating,
pressing
and
Crude protein
drying whole or parts of fish and to which fish Crude fat
solubles may have been re-added prior to
drying.
Crude ash, if > 20 %
Moisture if > 8 %
10.4.3 Fish
solubles Condensed
product
obtained
during Crude protein
manufacture of fishmeal which has been
Crude fat
separated and stabilised by acidification or
drying.
Moisture if > 5 %
10.4.4 Fish
protein,
Product obtained by acid hydrolysis of whole or Crude protein
hydrolysed
parts of fish often concentrated by drying.
Crude fat
Crude ash, if > 20 %
Moisture if > 8 %
10.4.5 Fishbone
meal Product
obtained
by
heating,
pressing
and
Crude ash
drying parts of fish. It consists principally of
fishbone.
10.4.6 Fish
oil
Oil obtained from fish or parts of fish followed Crude fat
by centrifugation to remove water (may include Moisture if > 1 %
species specific details e.g. cod liver oil).
10.4.7 Fish
oil,
hydrogenated Oil
obtained
from
hydrogenation
of
fish
oil Moisture
if
>
1
%
10.5.1 Krill
oil Oil
obtained
from
cooked
and
pressed
marine
Moisture if > 1 %
planktonic krill followed by centrifugation to
remove water.
10.5.2 Krill
protein
Product obtained by the enzymatic hydrolysis Crude protein
concentrate,
of whole or parts of krill often concentrated by Crude fat
hydrolysed
drying.
Crude ash, if > 20 %
Moisture if > 8 %
10.6.1 Marine
annelid
meal Product
produced
by
heating
and
drying
whole
Fat
or parts of marine annelids, including Nereis
Ash if > 20 %
virens.M. Sars.
Moisture if > 8 %
10.7.1 Marine
zooplankton Product produced by heating, pressing and
Crude protein
meal
drying marine zooplankton e.g. krill.
Crude fat
Crude ash, if > 20 %
Moisture if > 8 %

L 29/50
EN
Official Journal of the European Union
30.1.2013
Number Name Description Compulsory
declarations
10.7.2 Marine
zooplankton
oil Oil
obtained
from
cooked
and
pressed
marine Moisture if > 1 %
zooplankton followed by centrifugation to
remove water.
10.8.1 Mollusc
meal Product
produced
by
heating
and
drying
whole
Crude protein
or parts of molluscs including squid and bi-
Crude fat
valves.
Crude ash, if > 20 %
Moisture if > 8 %
10.9.1 Squid
meal Product
produced
by
heating,
pressing
and
Crude protein
drying whole squid or parts of squid.
Crude fat
Crude ash, if > 20 %
Moisture if > 8 %
( 1 ) The name shall be supplemented by the species.
( 2 ) The name shall be supplemented by the species when produced from farmed fish.
11. Minerals and products derived thereof
Number Name Description Compulsory
declarations
11.1.1 Calcium
carbonate ( 1 );
Product obtained by grinding sources of
Calcium, Ash insoluble in HCl
[limestone]
calcium carbonate (CaCO 3 ), such as limestone if > 5 %
or by precipitation from acid solution.
May contain up to 0,25 % propylene glycol.
May contain up to 0,1 % grinding aids.
11.1.2 Calcareous
marine
Product of natural origin, obtained from marine Calcium, Ash insoluble in HCl
shells
shells, ground or granulated, such as oyster
if > 5 %
shells or seashells.
11.1.3 Calcium
and
Natural mixture of calcium carbonate (CaCO 3 ) Calcium, Magnesium, Ash
magnesium carbonate
and magnesium carbonate (MgCO 3 ). May
insoluble in HCl if > 5 %
contain up to 0,1 % grinding aids.
11.1.4 Maerl Product
of
natural
origin
obtained
from
Calcium, Ash insoluble in HCl
calcareous marine algae, ground or granulated. if > 5 %
11.1.5 Lithothamn Product
of
natural
origin
obtained
from
Calcium, Ash insoluble in HCl
calcareous marine algae (Phymatolithon calcareum if > 5 %
(Pall.)), ground or granulated.
11.1.6 Calcium
chloride Calcium
chloride
(CaCl 2 ). May contain up to
Calcium, Ash insoluble in HCl
0,2 % barium sulphate.
if > 5 %
11.1.7 Calcium
hydroxide Calcium
hydroxide
(Ca(OH) 2 ).
Calcium, Ash insoluble in HCl
May contain up to 0,1 % grinding aids.
if > 5 %
11.1.8 Calcium
sulphate
Calcium sulphate anhydrous (CaSO 4 ) obtained Calcium, Ash insoluble in HCl
anhydrous
by grinding calcium sulphate anhydrous or
if > 5 %
dehydration of calcium sulphate dehydrate.

EN
30.1.2013 Official
Journal
of
the
European
Union L
29/51
Number Name Description Compulsory
declarations
11.1.9 Calcium
sulphate
Calcium sulphate hemihydrate (CaSO 4 ×
Calcium, Ash insoluble in HCl
hemihydrate
H 2 O) obtained by partially dehydrating calcium if > 5 %
sulphate dehydrate.
11.1.10 Calcium
sulphate
Calcium sulphate dihydrate (CaSO 4 × 2H 2 O)
Calcium, Ash insoluble in HCl
dihydrate
obtained by grinding calcium sulphate dihydrate if > 5 %
or hydration of calcium sulphate hemihydrate.
11.1.11 Calcium
salts
of
organic Calcium salts of edible organic acids with at
Calcium, Organic acid
acids ( 2 )
least 4 carbon atoms.
11.1.12 Calcium
oxide Calcium
oxide
(CaO)
obtained
from
calcination
Calcium, Ash insoluble in HCl
of naturally occurring limestone.
if > 5 %
May contain up to 0,1 % grinding aids.
11.1.13 Calcium
gluconate Calcium
salt
of
gluconic
acid
generally Calcium, Ash insoluble in HCl
expressed as Ca(C 6 H 11 O 7 ) 2 and its hydrated
if > 5 %
forms.
11.1.15 Calcium
Product obtained during the manufacturing of Calcium, Ash insoluble in HCl
sulphate/CARBONATE
sodium carbonate.
if > 5 %
11.1.16 Calcium
pidolate L-calcium
pidolate
(C 5 H 6 CaNO 3 ). May contain Calcium, Ash insoluble in HCl
up to 1,5 % glutamic acid and related
if > 5 %
substances.
11.1.17 Calcium
carbonate-
Product obtained by heating of natural calcium Calcium, magnesium
magnesium oxide
and magnesium containing substances like
dolomite. May contain up to 0,1 % grinding
aids.
11.2.1 Magnesium
oxide Calcined
magnesium
oxide
(MgO)
not
less
than
Magnesium, Ash insoluble in
70 % MgO.
HCl if > 15 %
11.2.2 Magnesium
sulphate Magnesium sulphate (MgSO 4 × 7 H 2 O). Magnesium,
Sulphur,
Ash
heptahydrate
insoluble in HCl if > 15 %
11.2.3 Magnesium
sulphate Magnesium sulphate (MgSO 4 × H 2 O). Magnesium,
Sulphur,
Ash
monohydrate
insoluble in HCl if > 15 %
11.2.4 Magnesium
sulphate Anhydrous magnesium sulphate (MgSO 4 ). Magnesium,
Sulphur,
ash
anhydrous
insoluble in HCl if > 10 %
11.2.5 Magnesium
propionate Magnesium
propionate
(C 6 H 10 MgO 4 ). Magnesium
11.2.6 Magnesium
chloride Magnesium
chloride
(MgCl 2) or solution
Magnesium, Chlorine, ash
obtained by natural concentration of sea water insoluble in HCl if > 10 %
after deposit of sodium chloride.
11.2.7 Magnesium
carbonate Natural
magnesium
carbonate
(MgCO 3 ). Magnesium,
ash
insoluble
in
HCl if > 10 %

L 29/52
EN
Official Journal of the European Union
30.1.2013
Number Name Description Compulsory
declarations
11.2.8 Magnesium
hydroxide Magnesium
hydroxide
(Mg(OH) 2 ). Magnesium,
ash
insoluble
in
HCl if > 10 %
11.2.9 Magnesium
potassium Magnesium potassium sulphate. Magnesium,
Potassium,
ash
sulphate
insoluble in HCl if > 10 %
11.2.10 Magnesium
salts
of
Magnesium salts of edible organic acids with at Magnesium, organic acid
organic acids ( 2 )
least 4 carbon atoms.
11.3.1 Dicalcium
Calcium monohydrogen phosphate obtained
Calcium, Total phosphorus, P
phosphate ( 3 ); [calcium
from bones or inorganic sources
insoluble in 2 % citric acid if
hydrogen
(CaHPO 4 × H 2 O)
> 10 %, Ash insoluble in HCl
orthophosphate]
Ca/P > 1,2
if > 5 %
May contain up to 3 % chloride expressed as
NaCl.
11.3.2 Monodicalcium
Product obtained chemically and composed of Total phosphorus, Calcium, P
phosphate
dicalcium phosphate and monocalcium
insoluble in 2 % citric acid if
phosphate (CaHPO 4 . Ca(H 2 PO 4 ) 2 × H 2 O)
> 10 %
0,8 < Ca/P < 1,3
11.3.3 Monocalcium
Calcium-bis dihydrogenphosphate
Total phosphorus, Calcium, P
phosphate; [calcium
(Ca(H 2 PO 4 ) 2 × H 2 O)
insoluble in 2 % citric acid if
tetrahydrogen
Ca/P < 0,9
> 10 %
diorthophosphate]
11.3.4 Tricalcium
phosphate; Tricalcium phosphate from bones or inorganic Calcium, Total phosphorus, P
[tricalcium
sources (Ca 3 (PO 4 ) 2 × H 2 O)
insoluble in 2 % citric acid if
orthophosphate]
Ca/P > 1,3
> 10 %
11.3.5 Calcium-magnesium
Calcium-magnesium phosphate. Calcium,
Magnesium,
Total
phosphate
phosphorus, P insoluble in 2 %
citric acid if > 10 %
11.3.6 Defluorinated
Natural phosphate, calcined and further heat
Total phosphorus, Calcium,
phosphate
treated than for the removal of impurities
Sodium, P insoluble in 2 %
necessary.
citric acid if > 10 %, Ash
insoluble in HCI if > 5 %
11.3.7 Dicalcium
Dicalcium pyrophosphate. Total
phosphorus,
Calcium,
P
pyrophosphate;
insoluble in 2 % citric acid if
[Dicalcium
> 10 %
diphosphate]
11.3.8 Magnesium
phosphate Product
consisting
of
monobasic
and/or
di-basic
Total phosphorus, Magnesium,
and/or tri-basic magnesium phosphate.
P insoluble in 2 % citric acid if
> 10 %, Ash insoluble in HCl
if > 10 %
11.3.9 Sodium-calcium-
Product consisting of sodium-calcium-
Total phosphorus, Magnesium,
magnesium phosphate
magnesium phosphate.
Calcium, Sodium, P insoluble
in 2 % citric acid if > 10 %

EN
30.1.2013 Official
Journal
of
the
European
Union L
29/53
Number Name Description Compulsory
declarations
11.3.10 Monosodium
Monosodium phosphate
Total phosphorus, Sodium, P
phosphate; [Sodium
(NaH 2 PO 4 × H 2 O)
insoluble in 2 % citric acid if
dihydrogen
> 10 %
orthophosphate]
11.3.11 Disodium
phosphate; Disodium phosphate (Na 2 HPO 4 × H 2 O) Total
phosphorus,
Sodium,
P
[Disodium hydrogen
insoluble in 2 % citric acid if
orthophosphate]
> 10 %
11.3.12 Trisodium
Phosphate; Trisodium phosphate (Na 3 PO 4 ) Total
phosphorus,
Sodium,
P
[Trisodium
insoluble in 2 % citric acid if
orthophosphate]
> 10 %
11.3.13 Sodium
pyrophosphate; Sodium pyrophosphate (Na 4 P 2 O 7 ) Total
phosphorus,
Sodium,
P
[Tetrasodium
insoluble in 2 % citric acid if
diphosphate]
> 10 %
11.3.14 Monopotassium
Monopotassium phosphate (KH 2 PO 4 × H 2 O) Total
phosphorus,
Potassium,
phosphate; [Potassium
P insoluble in 2 % citric acid if
dihydrogen
> 10 %
orthophosphate]
11.3.15 Dipotassium
phosphate; Dipotassium phosphate (K 2 HPO 4 × H 2 O) Total
phosphorus,
Potassium,
[Di-potassium
P insoluble in 2 % citric acid if
hydrogen
> 10 %
orthophosphate]
11.3.16 Calcium
sodium
Calcium sodium phosphate (CaNaPO 4 ) Total
phosphorus,
Calcium,
phosphate
Sodium, P insoluble in 2 %
citric acid if > 10 %
11.3.17 Monoammonium
Monoammonium phosphate (NH 4 H 2 PO 4 ) Total
nitrogen,
Total
phosphate;
phosphorus, P insoluble in 2 %
[Ammonium
citric acid if > 10 %
dihydrogen
orthophosphate]
11.3.18 Diammonium
Diammonium phosphate ((NH 4 ) 2 HPO 4 ) Total
nitrogen
Total
phosphate;
phosphorus P insoluble in 2 %
[Diammonium
citric acid if > 10 %
hydrogen
orthophosphate]
11.3.19 Sodium
Sodium tripolyphosphate (Na 5 P 3 O 9 ) Total
phosphorus
Sodium
P
tripolyphosphate;
insoluble in 2 % citric acid if
[Penta sodium
> 10 %
triphosphate]
11.3.20 Sodium
magnesium
Sodium-magnesium phosphate (MgNaPO 4 ) Total
phosphorus,
Magnesium,
phosphate
Sodium, P insoluble in 2 %
citric acid if > 10 %
11.3.21 Magnesium
Magnesium hypophosphite
Magnesium
hypophosphite
(Mg(H 2 PO 2 ) 2 × 6H 2 O)
Total phosphorus
P insoluble in 2 % citric acid if
> 10 %

L 29/54
EN
Official Journal of the European Union
30.1.2013
Number Name Description Compulsory
declarations
11.3.22 Degelatinised
bone
Degelatinised, sterilised and ground bones from Total phosphorus, Calcium,
meal
which the fat has been removed.
Ash insoluble in HCl if > 10 %
11.3.23 Bone
ash Mineral
residues
from
the
incineration,
Total phosphorus, Calcium,
combustion or gasification of animal by-
Ash insoluble in HCl if > 10 %
products.
11.3.24 Calcium
polyphosphate Heterogeneous
mixtures
of
calcium
salts
of
Total phosphorus, calcium, P
condensed polyphosphoric acids of general
insoluble in 2 % citric acid if
formula H(n + 2)PnO(3n 1) where ‘n’ is not less > 10 %
than 2.
11.3.25 Calcium
dihydrogen
Monocalcium dihydrogen
Total phosphorus, Calcium, P
diphosphate
pyrophosphate(CaH 2 P 2 O 7 )
insoluble in 2 % citric acid if
> 10 %
11.3.26 Magnesium
acid
Magnesium acid pyrophosphate (MgH 2 P 2 O 7 .)
Total phosphorus, Magnesium,
pyrophosphate
Produced from purified phosphoric acid and
P insoluble in 2 % citric acid if
purified magnesium hydroxide or magnesium
> 10 %
oxide by evaporation of water and
condensation of the orthophosphate to
diphosphate.
11.3.27 Disodium
dihydrogen Disodium dihydrogen diphosphate (Na 2 H 2 P 7 O 7 ) Total phosphorus, Calcium, P
diphosphate
insoluble in 2 % citric acid if
> 10 %
11.3.28 Trisodium
diphosphate Trisodium
monohydrogen
diphosphate
Total phosphorus, sodium, P
(anhydrous: Na 3 HP 2 O 7 ; monohydrate:
insoluble in 2 % citric acid if
Na 3 HP 2 O 7 × H 2 O)
> 10 %
11.3.29 Sodium
polyphosphate; Heterogeneous mixtures of sodium salts of
Total phosphorus, sodium, P
[Sodium
linear condensed polyphosphoric acids of
insoluble in 2 % citric acid if
hexametaphosphate]
general formula H(n + 2)PnO(3n + 1) where ‘n’ > 10 %
is not less than 2.
11.3.30 Tripotassium
phosphate Tripotassium
monophosphate
(anhydrous:
Total phosphorus, Potassium,
K 3 PO 4 ; hydrated: K 3 PO 4 × n H 2 O (n = 1 or 3)) P insoluble in 2 % citric acid if
> 10 %
11.3.31 Tetrapotassium
di-
Tetrapotassium pyrophosphate (K 4 P 2 O 7 ) Total
phosphorus,
Potassium,
phosphate
P insoluble in 2 % citric acid if
> 10 %
11.3.32 Pentapotassium
tri-
Pentapotassium tri-polyphosphate (K 5 P 3 O 10 ) Total
phosphorus,
Potassium,
phosphate
P insoluble in 2 % citric acid if
> 10 %
11.3.33 Potassium
Heterogeneous mixtures of potassium salts of
Total phosphorus, Potassium,
polyphosphate
linear condensed polyphosphoric acids of
P insoluble in 2 % citric acid if
general formula H(n + 2)PnO(3n + 1) where ‘n’ > 10 %
is not less than 2.
11.3.34 Calcium
sodium
Calcium sodium polyphosphate. Total
phosphorus,
sodium,
polyphosphate
calcium, P insoluble in 2 %
citric acid if > 10 %
11.4.1 Sodium
chloride ( 1 ) Sodium
chloride
(NaCl)
or
product
obtained
by
Sodium, Ash insoluble in HCl
evaporative crystallisation from brine (vacuum if > 10 %
salt) or evaporation of seawater (marine salt) or
grinding rock salt.

EN
30.1.2013 Official
Journal
of
the
European
Union L
29/55
Number Name Description Compulsory
declarations
11.4.2 Sodium
bicarbonate Sodium bicarbonate (NaHCO 3 ) Sodium,
Ash
insoluble
in
HCl
[sodium
if > 10 %
hydrogencarbonate]
11.4.3 Sodium/ammonium
Product obtained during the production of
Sodium, Ash insoluble in HCl
(bi)carbonate
sodium carbonate and sodium bicarbonate,
if > 10 %
[sodium/ammonium
with traces of ammonium bicarbonate
(hydrogen)carbonate]
(ammonium bicarbonate max. 5 %)
11.4.4 Sodium
carbonate Sodium
carbonate
(Na 2 CO 3 ) Sodium,
Ash
insoluble
in
HCl
if > 10 %
11.4.5 Sodium
Sodium sesquicarbonate (Na 3 H(CO 3 ) 2 ) Sodium,
Ash
insoluble
in
HCl
sesquicarbonate
if > 10 %
[trisodium
hydrogendicarbonate]
11.4.6 Sodium
sulphate Sodium
sulphate
(Na 2 SO 4 )
Sodium, Ash insoluble in HCl
May contain up to 0,3 % methionine
if > 10 %
11.4.7 Sodium
salts
of
organic Sodium salts of edible organic acids with at
Sodium, Organic acid
acids ( 2 )
least 4 carbon atoms
11.5.1 Potassium
chloride Potassium
chloride
(KCl)
or
product
obtained
Potassium, Ash insoluble in
by grinding natural sources of potassium
HCl if > 10 %
chloride
11.5.2 Potassium
sulphate Potassium
sulphate
(K 2 SO 4 ) Potassium,
Ash
insoluble
in
HCl if > 10 %
11.5.3 Potassium
carbonate Potassium
carbonate
(K 2 CO 3 ) Potassium,
Ash
insoluble
in
HCl if > 10 %
11.5.4 Potassium
bicarbonate Potassium bicarbonate (KHCO 3 ) Potassium,
Ash
insoluble
in
[potassium hydrogen
HCl if > 10 %
carbonate]
11.5.5 Potassium
salts
of
Potassium salts of edible organic acids with at Potassium, Organic acid
organic acids ( 2 )
least 4 carbon atoms.
11.6.1 Flower
of
sulphur Powder
obtained
from
natural
deposits
of
the
Sulphur
mineral. Also, product obtained from oil
refinery production as practised by sulphur
manufacturers.
11.7.1 Attapulgite Natural
magnesium-aluminium-silicon
mineral. Magnesium
11.7.2 Quartz Naturally
occurring
mineral
obtained
by
grinding sources of quartz.
May contain up to 0,1 % grinding aids.
11.7.3 Cristobalite Silicon
dioxide
(SiO 2 ) obtained from the re-
crystallisation of quartz.
May contain up to 0,1 % grinding aids.

L 29/56
EN
Official Journal of the European Union
30.1.2013
Number Name Description Compulsory
declarations
11.8.1 Ammonium
sulphate Ammonium
sulphate
((NH 4 ) 2 SO 4 ) obtained by Nitrogen expressed as crude
chemical synthesis.
protein, Sulphur
11.8.2 Ammonium
sulphate Ammonium sulphate in aqueous solution,
Nitrogen expressed as crude
solution
containing not less than 35 % Ammonium
protein
sulphate.
11.8.3 Ammonium
salts
of Ammonium salts of edible organic acids with at Nitrogen expressed as crude
organic acids ( 2 )
least 4 carbon atoms.
protein, Organic acid
11.8.4 Ammonium
lactate Ammonium
lactate
(CH 3 CHOHCOONH 4 ).
Nitrogen expressed as crude
Includes the Ammonium lactate produced by
protein, Crude ash
fermentation with Lactobacillus delbrueckii ssp.
Bulgaricus, Lactococcus lactis ssp., Leuconostoc
mesenteroides, Streptococcus thermophilus,
Lactobacillus spp, or Bifidobacterium spp.,
containing not less than 44 % Nitrogen
expressed as crude protein.
May contain up to 0,8 % phosphorus, 0,9 %
potassium, 0.7 % magnesium, 0,3 % sodium,
0,3 % sulphates 0,1 % chlorides, 5 % sugars and
0,1 % silicone antifoam.
11.8.5 Ammonium
acetate Ammonium
acetate
(CH 3 COONH 4 ) in aqueous Nitrogen expressed as crude
solution, containing not less than 55 %
protein
Ammonium acetate).
( 1 ) The nature of the source may be indicated additionally in the name or replace it.
( 2 ) The name shall be amended or supplemented to specify the organic acid.
( 3 ) The manufacturing process may be included in the name.
12. Fermentation (by-)products from micro-organisms
Number Name Description Compulsory
Declarations
12.1 Products
obtained
from
May contain up to 0,3 % antifoaming agents.
Propionic acid if > 0,5 %
the biomass of specific May contain up to 1,5 % filtration/clarifying
micro-organisms grown agents. May contain up to 2,9 % propionic acid.
on certain substrates
12.1.1 Protein
from
Protein product of fermentation obtained by
Crude protein
Methylophilus
culture of Methylophilus methylotrophus (NCIMB
methylotrophus
strain 10.515) (
Crude ash

1 ) on methanol, the crude
protein is at least 68 % and the reflectance
Crude fat
index at least 50.
12.1.2 Protein
from
Protein product of fermentation with
Crude protein
Methylococcus
Methylococcus capsulatus (Bath) (NCIMB strain
capsulatus (Bath), Alca
11132), Alcaligenes acidovorans (NCIMB strain
Crude ash
ligenes acidovorans,
12387), Bacillus brevis (NCIMB strain 13288)
Crude fat
Bacillus brevis and
and Bacillus firmus (NCIMB strain 13280) ( 1 ) on
Bacillus firmus
natural gas (approx. 91 % methane, 5 % ethane,
2 % propane, 0,5 % isobutane, 0,5 % n-butane),
ammonia, and mineral salts, the crude protein
is at least 65 %.

EN
30.1.2013 Official
Journal
of
the
European
Union L
29/57
Number Name Description Compulsory
Declarations
12.1.3 Bacterial
protein
from
Protein product, by-product from the
Crude protein
Escherichia coli
production of amino acids by culture of
Escherichia coli K12 ( 1 ) on substrates of vegetable
or chemical origin, ammonia or mineral salts; it
may be hydrolysed.
12.1.4 Bacterial
protein
from
Protein product, by-product from the
Crude protein
Corynebacterium
production of amino acids by culture of
glutamicum
Corynebacterium glutamicum ( 1 ) on substrates of
vegetable or chemical origin, ammonia or
mineral salts, it may be hydrolysed.
12.1.5 Yeasts
and
parts
All yeasts and parts thereof obtained from
Moisture if < 75 % or > 97 %
thereof [brewers’ yeast] Saccharomyces cerevisiae, Saccharomyces
[yeast product]
carlsbergensis, Kluyveromyces lactis, Kluyveromyces
If moisture < 75 %:
fragilis, Torulaspora delbrueckii, Candida
Crude protein
utilis/Pichia jadinii, Saccharomyces uvarum,
Saccharomyces ludwigii or Brettanomyces ssp. ( 1 ) ( 2 )
on substrates mostly of vegetable origin such as
molasses, sugar syrup, alcohol, distillery
residues, cereals and products containing starch,
fruit juice, whey, lactic acid, sugar, hydrolysed
vegetable fibres and fermentation nutrients such
as ammonia or mineral salts.
12.1.6 Mycelium
silage
from Mycelium (nitrogenous compounds), wet by-
Nitrogen expressed as crude
the production of
product from the production of penicillin by
protein
penicillin
Penicillium chrysogenum (ATCC48271) ( 1 ) on
different sources of carbohydrates and their
Crude ash
hydrolysates, heat treated and ensiled by means
of Lactobacillus brevis, plantarum, sake, collinoides
and Streptococcus lactis to inactive the penicillin,
Nitrogen expressed as crude protein is at least
7 %.
12.1.7 Yeasts
from
biodiesel All yeasts and parts thereof obtained from
Moisture if < 75 % or > 97 %
process
Yarrowia lipolytica ( 1 ) ( 2 ) grown on vegetable oils
and degumming and glycerol fractions formed If moisture < 75 %:
during biofuel production.
Crude protein
12.2 Other
fermentation
by-
May contain up to 0,6 % antifoaming agents.
products
May contain up to 0,5 % antiscaling agents.
May contain up to 0,2 % sulfites.
12.2.1 Vinasses
[condensed By-products derived from the industrial
Crude protein
molasses soluble]
processing of musts/worts issued from
fermentation processes such as alcohol, organic Substrate and indication of
acids, yeast manufacture. They are composed of production process as
the liquid/paste fraction obtained after the
appropriate
separation of the fermentation musts/worts.
They may also include dead cells and/or parts
thereof of the fermentation micro-organisms
used. The substrates are mostly of vegetable
origin such as molasses, sugar syrup, alcohol,
distillery residues, cereals and products
containing starch, fruit juice, whey, lactic acid,
sugar, hydrolysed vegetable fibres and
fermentation nutrients such as ammonia or
mineral salts.

L 29/58
EN
Official Journal of the European Union
30.1.2013
Number Name Description Compulsory
Declarations
12.2.2 By-products
from
the By-products from the production of L-glutamic Crude protein
production of L-
acid by fermentation with Corynebacterium
glutamic acid
melassecola ( 1 ) on substrate composed of sucrose,
molasses, starch products and their
hydrolysates, ammonium salts and other
nitrogenous compounds.
12.2.3 By-products
from
the By-products from the production of L-Lysine
Crude protein
production of L-lysine- monohydrochloride by fermentation with
monohydrochloride
Brevibacterium lactofermentum ( 1 ) on substrate
with Brevibacterium
composed of sucrose, molasses, starch products
lactofermentum
and their hydrolysates, ammonium salts and
other nitrogenous compounds.
12.2.4 By-products
from
the By-products from the production of amino
Crude protein
production of amino
acids by fermentation with Corynebacterium
acids with
glutamicum (
Crude ash

1 ) on substrate of vegetable or
Corynebacterium
chemical origin, ammonia or mineral salts.
glutamicum
12.2.5 By-products
from
the By-products from the production of amino
Crude protein
production of amino
acids by fermentation with Escherichia coli
acids with Escherichia
K12 (
Crude ash

1 ) on substrate of vegetable or chemical
coli K12
origin, ammonia or mineral salts.
12.2.6 By-product
of
enzyme By-product of fermentation of Aspergillus
Crude protein
production with
niger ( 1 ) on wheat and malt for enzyme
Aspergillus niger
production.
( 1 ) The cells of the micro-organisms have been inactivated or killed.
( 2 ) The usage name of yeast strains may vary from the scientific taxonomy, therefore, synonyms of the yeast strains listed could also be
used.
13. Miscellaneous
Number Name Description Compulsory
declarations
13.1.1 Products
from
the
Products obtained during and from the
Starch
bakery and pasta
production of bread, biscuits, wafers or pasta.
industry
They may be dried.
Total sugars, calculated as
sucrose,
Crude fat, if > 5 %
13.1.2 Products
from
the
Products obtained during and from the
Starch
pastry industry
production of pastry and cakes. They may be
dried.
Total sugars, calculated as
sucrose,
Crude fat, if > 5 %
13.1.3 Products
of
the
Substances or products that are intended or
Crude protein, if > 10 %
breakfast cereal
where it is reasonable to expect that they can
manufacture
be consumed by humans in their processed,
Crude fibre
partially processed or unprocessed forms. They Crude oils/fats, if > 10 %,
may be dried.
Starch, if > 30 %
Total sugar, calculated as
sucrose, if > 10 %

EN
30.1.2013 Official
Journal
of
the
European
Union L
29/59
Number Name Description Compulsory
declarations
13.1.4 Products
from
the
Products obtained during and from the
Starch
confectionery industry
production of sweets, inclusive chocolate. They
may be dried.
Crude fat, if > 5 %
Total sugars, calculated as
sucrose
13.1.5 Products
of
the
ice- Products obtained when producing ice-cream.
Starch
cream industry
They may be dried.
Total sugars, calculated as
sucrose,
Crude fat
13.1.6 Products
and
by-
Products obtained when processing fresh fruit Starch
products from
and vegetables (including peel, whole pieces of
processing fresh fruits
fruit/vegetables, and mixtures thereof). They
Crude fibre
and vegetables ( 1 )
may have been dried, or frozen.
Crude fat, if > 5 %
Ash insoluble in HCl, if
> 3,5 %
13.1.7 Products
from
the
Products obtained from freezing or drying
Crude Fibre
processing of plants ( 1 )
whole plants or their parts.
13.1.8 Products
from
Products obtained from freezing or drying
Crude protein, if > 10 %
processing of spices
spices and seasonings or their parts.
and seasonings (
Crude fibre

1 )
Crude oils/fats, if > 10 %,
Starch, if > 30 %
Total sugar, calculated as
sucrose, if > 10 %
13.1.9 Products
from
the
Products obtained from crushing, grinding,
Crude Fibre
processing of herbs ( 1 )
freezing or drying herbs or their parts.
13.1.10 Products
from
the
Products obtained when processing potatoes.
Starch
potato processing
They may have been dried or frozen.
industry
Crude fibre
Crude fat, if > 5 %
Ash insoluble in HCl, if
> 3,5 %
13.1.11 Products
and
by-
Substances from the sauces-production that are Crude fat
products of the sauces intended or where it is reasonable to expect
production
that they can be consumed by humans in their
processed, partially processed or unprocessed
forms. They may be dried.
13.1.12 Products
and
by-
Products and by-products of the savoury snacks Crude fat
products from the
industry obtained during and from the
savoury snacks
production of savoury snacks — potato chips,
industry
potato and/or cereal based snacks (direct
extruded, dough based and pelleted snacks) and
nuts.
13.1.13 Products
from
the
Products obtained during the production of
Crude fat, if > 5 %
ready-to-eat food
ready to eat food. They may be dried.
industry

L 29/60
EN
Official Journal of the European Union
30.1.2013
Number Name Description Compulsory
declarations
13.1.14 Plants
by-products
Solid products from plants (including berries
Crude protein, if > 10 %
from spirits production and seeds such as anise) obtained after
maceration of these plants in an alcoholic
Crude fibre
solution or after alcoholic
Crude oils/fats, if > 10 %
evaporation/distillation, or both, in the
elaboration of flavourings for the spirits
production. These products must be distilled to
eliminate the alcoholic residue.
13.1.15 Feed
beer Product
of
the
brewing
process
which
is
Alcohol content
unsalable as a human beverage.
13.2.1 Caramelised
sugar Product
obtained
by
the
controlled
heating
of
Total sugars, calculated as
any sugar.
sucrose
13.2.2 Dextrose Dextrose
is
obtained
after
hydrolysis
of
starch
Total sugars, calculated as
and consists of purified, crystallised glucose,
sucrose
with or without crystal water.
13.2.3 Fructose
Fructose as purified crystalline powder. It is
Total sugars, calculated as
obtained from glucose in glucose syrup by the sucrose
use of glucose isomerase and from sucrose
inversion.
13.2.4 Glucose
syrup Glucose
syrup
is
a
purified
and
concentrated
Total sugars
aqueous solution of nutritive saccharides
obtained through hydrolysis from starch.
Moisture if > 30 %
13.2.5 Glucose
molasses Product
produced
during
refining
process
of
Total sugars
glucose syrups.
13.2.6 Xylose Sugar
extracted
from
wood.
13.2.7 Lactulose Semi-synthetic
disaccharide
(4-O-D-
Lactulose
Galactopyranosyl-D-fructose) obtained from
lactose through the isomerisation of glucose to
fructose. Present in heat treated milk and milk
products.
13.2.8 Glucosamine
Amino sugar (monosaccharide) being part of
Sodium or Potassium, as
(Chitosamine)
the structure of the polysaccharides chitosan
applicable
and chitin. Produced by the hydrolysis of
crustacean and other arthropods exoskeletons
‘from aquatic animals’ or ‘from
or by fermentation of a grain such as corn or fermentation’, as appropriate
wheat.
13.3.1 Starch ( 2 ) Starch. Starch
13.3.2 Starch ( 2 ), pre-
Product consisting of starch expanded by heat Starch
gelatinised
treatment.
13.3.3 Starch ( 2 ) mixture Product
consisting
of
native
and/or
modified
Starch
food starch obtained from different botanical
sources.

EN
30.1.2013 Official
Journal
of
the
European
Union L
29/61
Number Name Description Compulsory
declarations
13.3.4 Starch ( 2 ) hydrolysates
Product from starch hydrolysis liquor filtration Moisture if < 25 % or > 45 %
cake
which consists of the following: protein, starch,
polysaccharides, fat, oil and filter aid (e.g.
If moisture < 25 %:
diatomaceous earth, wood fibre).
— Crude fat
— Crude protein
13.3.5 Dextrin Dextrin
is
partially
acid
hydrolysed
starch.
13.3.6 Maltodextrin Maltodextrin
is
the
partially
hydrolysed
starch
13.4.1 Polydextrose Randomly
bonded
bulk
polymer
of
glucose
produced by thermal polymerisation of D-
Glucose.
13.5.1 Polyols Product
obtained
by
hydrogenation
or
fermentation and consisting of reduced mono,
di- or oligosaccharides or polysaccharides.
13.5.2 Isomalt Sugar
alcohol
obtained
from
sucrose
after
enzymatic conversion and hydrogenation.
13.5.3 Mannitol Product
obtained
by
hydrogenation
or
fermentation and consisting of reduced glucose
and/or fructose.
13.5.4 Xylitol Product
obtained
by
hydrogenation
and
fermentation of xylose.
13.5.5 Sorbitol Product
obtained
by
hydrogenation
of
glucose
13.6.1 Acid
oils
from
chemical Product obtained during the deacidification of Crude fat
refining ( 3 )
oils and fats of vegetable or animal origin by
means of alkali, followed by an acidulation with Moisture if > 1 %
subsequent separation of the aqueous phase,
containing free fatty acids, oils or fats and
natural components of seeds, fruits or animal
tissues such as mono-, and diglycerides, lecithin
and fibres.
13.6.2 Fatty
acids
esterified Glycerides obtained by esterification of glycerol Moisture if > 1 %
with glycerol ( 4 )
with fatty acids. May contain up to 50 ppm
Nickel from hydrogenation.
Crude fat
Nickel if > 20 ppm
13.6.3 Mono
di
and
tri
Product consisting of mixtures of mono-, di-
Crude fat
glycerides of fatty
and triesters of glycerol with fatty acids.
acids (
Nickel if > 20 ppm

4 )
They may contain small amounts of free fatty
acids and glycerol.
May contain up to 50 ppm Nickel from
hydrogenation.

L 29/62
EN
Official Journal of the European Union
30.1.2013
Number Name Description Compulsory
declarations
13.6.4 Salts
of
fatty
acids ( 4 ) Product
obtained
by
reaction
of
fatty
acids
with
Crude fat (after hydrolysis)
at least four carbon atoms with calcium,
magnesium, sodium or potassium hydroxides, Moisture
oxides or salts.
Ca or Na or K or Mg (when
May contain up to 50 ppm Nickel from
appropriate)
hydrogenation.
Nickel if > 20 ppm
13.6.5 Fatty
acid
distillates Product obtained during the deacidification of Crude fat
from physical
oils and fats of vegetable or animal origin by
refining (
Moisture if > 1 %

3 )
means of distillation containing free fatty acids,
oils or fats and natural components of seeds,
fruits or animal tissues such as mono- and
diglycerides, sterols and tocopherols.
13.6.6 Crude
fatty
acids
from Product obtained by oil/fat splitting. By
Crude fat
splitting ( 3 )
definition it consists of crude fatty acids C 6 -C 24 ,
aliphatic, linear, monocarboxylic, saturated and Moisture if > 1 %
unsaturated. May contain up to 50 ppm Nickel Nickel if > 20 ppm
from hydrogenation.
13.6.7 Pure
distilled
fatty
acids Product obtained by the distillation of crude
Crude fat
from splitting ( 3 )
fatty acids from oil/fat splitting potentially plus
hydrogenation. By definition it consists of pure Moisture if > 1 %
distilled fatty acids C 6 -C 24 , aliphatic, linear,
Nickel if > 20 ppm
monocarboxylic, saturated and unsaturated.
May contain up to 50 ppm Nickel from
hydrogenation
13.6.8 Soap
stocks ( 3 ) Product
obtained
during
the
deacidification
of
Moisture if < 40 and > 50 %
vegetable oils and fats by means of aqueous
calcium, magnesium, sodium or potassium
Ca or Na or K or Mg, as
hydroxide solution, containing salts of fatty
appropriate
acids, oils or fats and natural components of
seeds, fruits or animal tissues such as mono-
and diglycerides, lecithin and fibres.
13.6.9 Mono-
and
diglycerides Mono- and diglycerides of fatty acids with at
Crude fat
of fatty acids esterified least four carbon atoms esterified with organic
with organic acids ( 4 ) ( 5 ) acids.
13.6.10 Sucrose
esters
of
fatty Esters of sachharose and fatty acids. Total
sugars,
calculated
as
acids ( 4 )
sucrose
Crude fat
13.6.11 Sucroglycerides
of
fatty Mixture of esters of saccharose and mono and Total sugars, calculated as
acids ( 4 )
di-glycerides of fatty acids.
sucrose
Crude fat

EN
30.1.2013 Official
Journal
of
the
European
Union L
29/63
Number Name Description Compulsory
declarations
13.8.1 Glycerine,
crude By-product
obtained
from:
Glycerol
— the oleochemical process of oil/fat splitting Potassium if > 1,5 %
to obtain fatty acids and sweet water,
Sodium if > 1,5 %
followed by concentration of the sweet
water to get crude glycerol or by
Nickel if > 20 ppm
transesterification (may contain up to 0,5 %
methanol) of natural oils/fats to obtain fatty
acid methyl esters and sweet water, followed
by concentration of the sweet water to get
crude glycerol;
— the production of biodiesel (methyl or ethyl
esters of fatty acids) by transesterification of
oils and fats of unspecified vegetable and
animal origin. Mineral and organic salts
might remain in the glycerine (up to 7,5 %).
May contain up to 0,5 % Methanol and up to
4 % of Matter Organic Non Glycerol (MONG)
comprising of Fatty Acid Methyl Esters, Fatty
Acid Ethyl Esters, Free Fatty Acids and
Glycerides;
— saponifications of oils/fats of vegetable or
animal origin, normally with alkali/alkaline
earths, to obtain soaps.
May contain up to 50 ppm Nickel from
hydrogenation.
13.8.2 Glycerine Product
obtained
from:
Glycerol if < 99 % on dry
— the oleochemical process of (a) oil/fat matter basis
splitting followed by concentration of
Sodium if > 0,1 %
sweet waters and refining by distillation (see Potassium if > 0,1 %
part B, glossary of processes, entry 20) or
ion-exchange process; (b) transesterification Nickel if > 20 ppm
of natural oils/fats to obtain fatty acid
methyl esters and crude sweet water,
followed by concentration of the sweet
water to get crude glycerol and refining by
distillation or ion-exchange process;
— the production of biodiesel (methyl or ethyl
esters of fatty acids) by transesterification of
oils and fats of unspecified vegetable and
animal origin with subsequent refining of
the glycerine. Minimum Glycerol content:
99 % of dry matter;
— saponifications of oils/fats of vegetable or
animal origin, normally with alkali/alkaline
earths, to obtain soaps, followed by refining
of crude Glycerol and distillation.
May contain up to 50 ppm Nickel from
hydrogenation.
13.9.1 Methyl
sulphonyl
Organo-sulfur compound ((CH 3 ) 2 SO 2 ) obtained Sulphur
methane
by synthetic way which is identical to the
naturally occurring source in plants.

L 29/64
EN
Official Journal of the European Union
30.1.2013
Number Name Description Compulsory
declarations
13.10.1 Peat Product
from
the
natural
decomposition
of
Crude Fibre
plant (mainly sphagnum) in anaerobic and
oligotrophic environment.
13.10.2 Leonardite Product
that
is
a
naturally
occurring
mineral
Crude Fibre
complex of phenolic hydrocarbons, also known
as humate, which originates from the
decomposition of organic matter over the
course of millions of years.
13.11.1 Propylene
glycol;
[1,2- Organic compound (a diol or double alcohol) Propylene glycol
propanediol; [propane- with formula C 3 H 8 O 2 . It is a viscous liquid with
1,2-diol]
a faintly sweet taste, hygroscopic and miscible
with water, acetone, and chloroform. May
contain up to 0,3 % di propylene glycol.
13.11.2 Mono-esters
of
Mono-esters of propylene glycol and fatty acids, Propylene glycol
propylene glycol and
alone or in mixtures with diesters.
Crude fat
fatty acids (


4 )
( 1 ) The name shall be supplemented by the fruit, vegetable, plant, spices and herbs species, as applicable.
( 2 ) The name shall be supplemented by the indication of the botanical origin.
( 3 ) The name shall be supplemented by the indication of the botanical or animal origin.
( 4 ) The name shall be amended or supplemented to specify the fatty acids used.
( 5 ) The name shall be amended or supplemented to specify the organic acid.

Document Outline


附件:

P020171219334894598721.pdf

托管标准,您可以接收以下服务:

1 标准定期系统查新,若有最新版本,会以站内短信或邮件的形式通知用户;

2 随时在标准托管页面中查看到该条标准的最新状态;

3 若用户有在学习和科研中的需要,可以在标准托管页面中试阅标准;

4 企业如果需要上新产品,我院及时提供标准查询、采购等方面的支持;

5 为企业在标准制修订、企业良好行为创建以及标准化试点过程中遇到的困难,可联系我院指定相关专家负责进行指导帮助、提供政策咨询;

6 为企业提供标准化政策的解读、标准化知识的推广培训、标准自我公开声明、标准文献的免费查询、企业标准化体系建设等方面的标准化服务;

进入企业标准托管

您可以通过编辑查新模板,批量查询指定标准集的最新情况。我们会通过查询,向您展示您所查询标准的:

1. 准确的标准号及标准名称(我们通过人工智能技术对您提交的标准号进行自动纠正)

2. 标准的最新状态(现行、废止或未发布)

3. 若标准已废止并被新标准替代,会反馈被替代的标准

4. 若您已托管此标准,便可以实时跟踪这个标准的最新状态

标准查新 模板下载

您可以在这里检索全球超过140万条标准,支持上百个国内国际标准组织的标准查询。您也可以在这里检索国内各类国家、部委和地方的法律法规。

更多标准子库在持续建设中。

标准检索

标准资讯点击排行榜 全部

资讯标题点击

[[ n.title ]] [[ n.read ]]

大连标准化公共服务平台

版权:大连标准化研究院有限公司

地址:大连市中山区高原街56号

电话:0411-82740851

大连标准