LegalizeCommission Regulation (EU) No 68/2013 of 16 January 2013 on the Catalogue of feed materials Text with EEA relevance
Feed materials in this chapter shall fulfil the requirements of Regulation (EC) No 1069/2009 and the specific requirements for milk, colostrum, and certain other products derived from milk according to Annex X to Regulation (EU) No 142/2011.
| Number | Name (1) | Description | Compulsory declarations |
|---|---|---|---|
| 8.1.1 | Butter and butter products | Butter and products obtained by production or processing of butter (e.g. butter serum), unless listed separately | Crude protein Crude fat Lactose Moisture if > 6 % |
| 8.2.1 | Buttermilk/buttermilk powder (1) | Product obtained by churning butter out of cream or similar processes. 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 % inorganic acids: sulphuric acid, hydrochloric acid, phosphoric acid, used for pH adjustments in many stages of production processes; — up to 0,5 % alkali e.g. sodium, potassium, calcium, magnesium hydroxides, used for pH adjustments in many stages 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 | Crude protein Crude fat Lactose Moisture if > 6 % |
| 8.3.1 | Casein | Product obtained from skimmed or buttermilk by drying casein precipitated by means of acids or rennet | Crude protein Moisture if > 10 % |
| 8.4.1 | Caseinate | Product extracted from curd or casein through use of neutralising substances and drying | Crude protein Moisture if > 10 % |
| 8.5.1 | Cheese and cheese products | Cheese and products made of cheese and of milk based products | Crude protein Crude fat |
| 8.6.1 | Colostrum/colostrum powder (1) | The fluid secreted by the mammary glands of milk-producing animals up to five days post parturition | Crude protein |
| 8.7.1 | Dairy by-products | Products obtained when producing dairy products, including centrifuge or separator sludge, white water, milk minerals. 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 % inorganic acids: sulphuric acid, hydrochloric acid, phosphoric acid, used for pH adjustments in many stages of production processes; — up to 0,5 % alkali e.g. sodium, potassium, calcium, magnesium hydroxides, used for pH adjustments in many stages 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 | Moisture Crude protein Crude fat Total sugars, calculated as sucrose |
| 8.8.1 | Fermented milk products | Products obtained by fermentation of milk (e.g. yoghurt etc.) | Crude protein Crude fat |
| 8.9.1 | Lactose | The sugar separated from milk or whey by purification and drying | Moisture if > 5 % |
| 8.10.1 | Milk/milk powder (18) | Normal mammary secretion obtained from one or more milkings | Crude protein Crude fat Moisture if > 5 % |
| 8.11.1 | Skimmed milk/skimmed milk powder (1) | Milk whose fat content has been reduced by separation | Crude protein Moisture if > 5 % |
| 8.12.1 | Milk fat | Product obtained by skimming milk | Crude fat |
| 8.13.1 | Milk protein powder (1) | Product obtained by drying protein compounds extracted from milk by chemical or physical treatment | Crude protein Moisture if > 8 % |
| 8.14.1 | Condensed and evaporated milk and their products | Condensed and evaporated milk and products obtained by production or processing of these products | Crude protein Crude fat Moisture if > 5 % |
| 8.15.1 | Milk permeate/Milk permeate powder (1) | Product obtained from the liquid phase of (ultra, nano or micro) filtration of milk and from which lactose may have been partly removed. Reverse osmosis may be applied | Crude ash Crude protein Lactose Moisture if > 8 % |
| 8.16.1 | Milk retentate/milk retentate powder (1) | Product retained on the membrane from (ultra, nano or micro) filtration of milk | Crude protein Crude ash Lactose Moisture if > 8 % |
| 8.17.1 | Whey/whey powder (1) | Product of cheese, quark or casein manufacturing or similar processes. 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 % inorganic acids: sulphuric acid, hydrochloric acid, phosphoric acid, used for pH adjustments in many stages of production processes; — up to 0,5 % alkali e.g. sodium, potassium, calcium, magnesium hydroxides, used for pH adjustments in many stages 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 | Crude protein Lactose Moisture if > 8 % Crude ash |
| 8.18.1 | Delactosed whey/delactosed whey powder (1) | Whey from which the lactose has been partly removed. 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 % inorganic acids: sulphuric acid, hydrochloric acid, phosphoric acid, used for pH adjustments in many stages of production processes; — up to 0,5 % alkali e.g. sodium, potassium, calcium, magnesium hydroxides, used for pH adjustments in many stages 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 | Crude protein Lactose Moisture if > 8 % Crude ash |
| 8.19.1 | Whey protein/whey protein powder (1) | Product obtained by drying whey protein compounds extracted from whey by chemical or physical treatment. 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 % inorganic acids: sulphuric acid, hydrochloric acid, phosphoric acid, used for pH adjustments in many stages of production processes; — up to 0,5 % alkali e.g. sodium, potassium, calcium, magnesium hydroxides, used for pH adjustments in many stages 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 | Crude protein Moisture if > 8 % |
| 8.20.1 | Demineralised, delactosed whey/demineralised, delactosed whey powder (1) | Whey from which lactose and minerals have been partly removed. 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 % inorganic acids: sulphuric acid, hydrochloric acid, phosphoric acid, used for pH adjustments in many stages of production processes; — up to 0,5 % alkali e.g. sodium, potassium, calcium, magnesium hydroxides, used for pH adjustments in many stages 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 | Crude protein Lactose Crude ash Moisture if > 8 % |
| 8.21.1 | Whey permeate/whey permeate powder (1) | Product from the liquid phase of (ultra, nano or micro) filtration of whey and from which lactose may have been partly removed. Reverse osmosis 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 % inorganic acids: sulphuric acid, hydrochloric acid, phosphoric acid, used for pH adjustments in many stages of production processes; — up to 0,5 % alkali e.g. sodium, potassium, calcium, magnesium hydroxides, used for pH adjustments in many stages 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 | Crude ash Crude protein Lactose Moisture if > 8 % |
| 8.22.1 | Whey retentate/whey retentate powder (1) | Product retained on the membrane from (ultra, nano or micro) filtration of whey. 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 % inorganic acids: sulphuric acid, hydrochloric acid, phosphoric acid, used for pH adjustments in many stages of production processes; — up to 0,5 % alkali e.g. sodium, potassium, calcium, magnesium hydroxides, used for pH adjustments in many stages 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 | Crude protein Crude ash Lactose Moisture if > 8 % |
| (1) Expressions are not synonymous and differ mainly in their moisture content, respective expression to be used as appropriate. The term ‘powder’ implies a moisture content below 12 % and may replace the term ‘dried’ or ‘concentrated and dried’. |
Feed materials in this chapter shall fulfil the requirements of Regulation (EC) No 1069/2009. The name of the feed materials shall be supplemented with the indication according to Annex X or Annex XIII to Regulation (EU) No 142/2011 or Annex IV to Regulation (EC) No 999/2001 for clarifying the specific requirements and a clear identification regarding restrictions to use according to Regulation (EC) No 999/2001.
| Number | Name (1) | Description | Compulsory declarations |
|---|---|---|---|
| 9.1.1 | Animal by-products (1) | Whole or parts of warm-blooded land animals, fresh, frozen, cooked, acid treated or dried | Crude protein Crude fat Moisture if > 8 % |
| 9.2.1 | Animal fat (2) | Product composed of fat from land animals, including invertebrates other than species pathogenic to humans and animals in all their life stages. If extracted with solvents, may contain up to 0,1 % hexane | Crude fat Moisture if > 1 % |
| 9.3.1 | Apiculture by-products (3) | Honey, beeswax, royal jelly, propolis, pollen, processed or unprocessed | Total sugars, calculated as sucrose |
| 9.4.1 | Processed animal protein (2) | Product obtained by heating, drying and grinding whole or parts of land animals, including invertebrates in all their life stages from which the fat may have been partially extracted or physically removed. If extracted with solvents, may contain up to 0,1 % hexane | Crude protein Crude fat Crude ash Moisture if > 8 % |
| 9.5.1 | Gelatine process derived proteins (2) | Dried animal proteins derived from the production of gelatine obtained from raw materials pursuant to Regulation (EC) No 853/2004 | Crude protein Crude fat Crude ash Moisture if > 8 % |
| 9.6.1 | Hydrolysed animal proteins (2) | Polypeptides, peptides and amino acids, and mixtures thereof, obtained by hydrolysis of animal by-products, which can be concentrated by drying | Crude protein Moisture if > 8 % |
| 9.7.1 | Blood meal (2) | Product derived from the heat treatment of blood of slaughtered warm-blooded animals | Crude protein Moisture if > 8 % |
| 9.8.1 | Blood products (1) | Products derived from blood or fractions of blood of slaughtered warm-blooded animals; they include dried/frozen/liquid plasma, dried whole blood, dried/frozen/liquid red cells or fractions thereof and mixtures | Crude protein Moisture if > 8 % |
| 9.9.1 | Catering reflux [catering recycling] | All waste food containing material of animal origin including used cooking oil originating in restaurants, catering facilities and kitchens, including central kitchens and household kitchens | Crude protein Crude fat Crude ash Moisture if > 8 % |
| 9.10.1 | Collagen (2) | Protein-based product derived from animal bones, hides, skins and tendons | Crude protein Moisture if > 8 % |
| 9.11.1 | Feather meal | Product obtained by drying and grinding feathers of slaughtered animals | Crude protein Moisture if > 8 % |
| 9.12.1 | Gelatine (2) | Natural, soluble protein, gelling or non-gelling, obtained by the partial hydrolysis of collagen produced from bones, hides and skins, tendons and sinews of animals | Crude protein Moisture if > 8 % |
| 9.13.1 | Greaves (2) | Product obtained from the manufacture of tallow, lard and other extracted or physically removed fats of animal origin, fresh, frozen or dried. If extracted with solvents, may contain up to 0,1 % hexane | Crude protein Crude fat Crude ash Moisture if > 8 % |
| 9.14.1 | Products of animal origin (1) | Former foodstuff containing animal products; with or without treatment such as fresh, frozen, dried | Crude protein Crude fat Moisture if > 8 % |
| 9.15.1 | Eggs | Whole eggs of Gallus gallus L. with or without shells | |
| 9.15.2 | Albumen | Product obtained from eggs after the separation of shells and yolk, pasteurised and possibly denatured | Crude protein Method of denaturation, if applicable |
| 9.15.3 | Egg products, dried | Products consisting of pasteurised dried eggs, without shells or a mixture of different proportions of dried albumen and dried egg yolk | Crude protein Crude fat Moisture if > 5 % |
| 9.15.4 | Egg powder, sugared | Dried whole or parts of eggs, sugared | Crude protein Crude fat Moisture if > 5 % Total sugars, calculated as sucrose |
| 9.15.5 | Egg shells, dried | Product obtained from poultry eggs, after the content (yolk and albumen) has been removed. Shells are dried | Crude ash |
| 9.16.1 | Terrestrial invertebrates (1) , live | Live terrestrial invertebrates, in all their life stages, other than species having adverse effects on plant, animals and human health | |
| 9.16.2 | Terrestrial invertebrates (1) , dead | Dead terrestrial invertebrates, other than species having adverse effects on plant, animals and human health, in all their life stages, with or without treatment but not processed as referred to in Regulation (EC) No 1069/2009 | Crude protein Crude fat Crude ash |
| 9.17.1 | Cholesterol from woolgrease | Product obtained from woolgrease (lanolin) by saponification, separations and crystallization. Minimum content of (3β)-cholest-5-en-3-ol, C27H46O: 90 % | |
| (1) Without prejudice to mandatory requirements concerning labelling, 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) and if the Catalogue is used for labelling purposes, the name shall be replaced as appropriate to provide adequate information, by: — the animal species and — the part of the animal product (e.g. liver, meat (only if skeletal muscle)), and/or — the life stage (e.g. larvae) 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 to provide adequate information, by: — the animal species and/or — the part of the animal product (e.g. liver, meat (only if skeletal muscle)), and/or — the life stage (e.g. larvae) 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 labelling, 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) and Regulation 999/2001, Annex IV, and if the Catalogue is used for labelling purposes, the name shall be supplemented as appropriate to provide adequate information, by: — the animal species processed (e.g. porcine, ruminant, avian, insect) and/or — the life stage (e.g. larvae) 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). (3) The name shall be replaced by the name of the specific product, as appropriate. |
Feed materials in this chapter shall fulfil the requirements of Regulation (EC) No 1069/2009 and Regulation (EU) No 142/2011 and may be subject to restrictions in use according to Regulation (EC) No 999/2001.
| Number | Name (1) | Description | Compulsory declarations |
|---|---|---|---|
| 10.1.1 | Aquatic invertebrates (1) | Whole or parts of marine or freshwater invertebrates, in all their life stages, other than species pathogenic to humans and animals | Crude protein Crude fat Crude ash |
| 10.2.1 | By-products from aquatic animals (21) | Originating from establishments or plants preparing or manufacturing products for human consumption | Crude protein Crude fat Crude ash |
| 10.3.1 | Crustacea meal (2) | Product obtained by heating, pressing and drying whole or parts of crustacean including wild and farmed shrimp | Calcium Ash insoluble in HCl if > 5 % |
| 10.4.1 | Fish (1) | Whole or parts of fish: fresh, frozen, cooked, acid treated or dried | Crude protein Moisture if > 8 % |
| 10.4.2 | Fish meal (1) | Product obtained by heating, pressing and drying whole or parts of fish and to which fish solubles may have been re-added prior to drying | Crude protein Crude fat Crude ash, if > 20 % Moisture if > 8 % |
| 10.4.3 | Fish solubles | Condensed product obtained during manufacture of fishmeal which has been separated and stabilised by acidification or drying | Crude protein Crude fat Moisture if > 5 % |
| 10.4.4 | Fish protein, hydrolysed | Proteins obtained by hydrolysis of whole or parts of fish, which can be concentrated by drying | Crude protein Crude fat Crude ash, if > 20 % Moisture if > 8 % |
| 10.4.5 | Fishbone meal | Product obtained by heating, pressing and drying parts of fish. It consists principally of fishbone | Crude ash |
| 10.4.6 | Fish oil | Oil obtained from fish or parts of fish followed by centrifugation to remove water (may include species specific details e.g. cod liver oil) | Crude fat Moisture if > 1 % |
| 10.4.7 | Fish oil, hydrogenated | Oil obtained from hydrogenation of fish oil | Moisture if > 1 % |
| 10.4.8 | Fish oil stearine [Winterized fish oil] | Fraction of fish oil with a high content of saturated fats obtained during the refining of crude fish oil to refined fish oil using the process winterization in which the saturated fats are congealed and subsequently collected | Crude fat Moisture if > 1 % |
| 10.5.1 | Krill oil | Oil obtained from cooked and pressed marine planktonic krill followed by centrifugation to remove water | Moisture if > 1 % |
| 10.5.2 | Krill protein concentrate, hydrolysed | Product obtained by the enzymatic hydrolysis of whole or parts of krill, often concentrated by drying | Crude protein Crude fat Crude ash, if > 20 % Moisture if > 8 % |
| 10.6.1 | Marine annelid meal | Product obtained by heating and drying whole or parts of marine annelids, including Nereis virens M. Sars | Crude fat Ash if > 20 % Moisture if > 8 % |
| 10.7.1 | Marine zooplankton meal | Product obtained by heating, pressing and drying marine zooplankton e.g. krill | Crude protein Crude fat Crude ash, if > 20 % Moisture if > 8 % |
| 10.7.2 | Marine zooplankton oil | Oil obtained from cooked and pressed marine zooplankton followed by centrifugation to remove water | Moisture if > 1 % |
| 10.8.1 | Mollusc meal | Product obtained by heating and drying whole or parts of molluscs including squid and bi-valves | Crude protein Crude fat Crude ash, if > 20 % Moisture if > 8 % |
| 10.9.1 | Squid meal | Product obtained by heating, pressing and drying whole squid or parts of squid | Crude protein Crude fat Crude ash, if > 20 % Moisture if > 8 % |
| 10.10.1 | Starfish meal [sea star meal] | Product obtained by heating, pressing and drying whole Asteroidea or parts of Asteroide | Crude protein Crude fat Crude ash, if > 20 % Moisture if > 8 % |
| 10.11.1 | Marine invertebrates (1) meal | Product obtained by heating, pressing and drying whole or parts of marine invertebrates | Crude protein Crude fat Crude ash, if > 20 % Moisture if > 8 % |
| (1) The name shall be supplemented by the animal species. (2) The name shall be supplemented by the animal species, when produced from farmed fish/crustacean, as relevant. |
Feed materials in this chapter containing animal by-products shall fulfil the requirements of Regulation (EC) No 1069/2009 and Regulation (EU) No 142/2011 and may be subject to restrictions in use according to Regulation (EC) No 999/2001.
| Number | Name (1) | Description | Compulsory declarations |
|---|---|---|---|
| 11.1.1 | Calcium carbonate (1) [limestone] | Product obtained by grinding sources of calcium carbonate (CaCO3), such as limestone or by precipitation from acid solution. May contain up to 0,25 % propylene glycol. May contain up to 0,1 % grinding aids | Calcium Ash insoluble in HCl if > 5 % |
| 11.1.2 | Calcareous marine shells | Product of natural origin, obtained from marine shells, ground or granulated, such as oyster shells or seashells | Calcium Ash insoluble in HCl if > 5 % |
| 11.1.3 | Calcium and magnesium carbonate | Natural mixture of calcium carbonate (CaCO3) and magnesium carbonate (MgCO3). May contain up to 0,1 % grinding aids | Calcium Magnesium Ash insoluble in HCl if > 5 % |
| 11.1.4 | Maerl | Product of natural origin obtained from calcareous marine algae, ground or granulated | Calcium Ash insoluble in HCl if > 5 % |
| 11.1.5 | Lithothamn | Product of natural origin obtained from calcareous marine algae (Phymatolithon calcareum (Pall.)), ground or granulated | Calcium Ash insoluble in HCl if > 5 % |
| 11.1.6 | Calcium chloride | Calcium chloride (CaCl2) and its hydrate froms. May contain up to 0,2 % barium sulphate | Calcium Ash insoluble in HCl if > 5 % |
| 11.1.7 | Calcium hydroxide (2) | Calcium hydroxide (Ca(OH)2). May contain up to 0,1 % grinding aids | Calcium Ash insoluble in HCl if > 5 % |
| 11.1.8 | Calcium sulphate anhydrous | Calcium sulphate anhydrous (CaSO4) obtained by grinding calcium sulphate anhydrous or dehydration of calcium sulphate dihydrate | Calcium Ash insoluble in HCl if > 5 % |
| 11.1.9 | Calcium sulphate hemihydrate | Calcium sulphate hemihydrate (CaSO4 × ½ H2O) obtained by partially dehydrating calcium sulphate dihydrate | Calcium Ash insoluble in HCl if > 5 % |
| 11.1.10 | Calcium sulphate dihydrate | Calcium sulphate dihydrate (CaSO4 × 2H2O) obtained by grinding calcium sulphate dihydrate or hydration of calcium sulphate hemihydrate | Calcium Ash insoluble in HCl if > 5 % |
| 11.1.11 | Calcium salts of organic acids (3) | Calcium salts of edible organic acids with at least 4 carbon atoms (4) | Calcium Organic acid |
| 11.1.12 | Calcium oxide | Calcium oxide (CaO) obtained from calcination of naturally occurring limestone. May contain up to 0,1 % grinding aids | Calcium Ash insoluble in HCl if > 5 % |
| 11.1.13 | Calcium gluconate | Calcium salt of gluconic acid generally expressed as Ca(C6H11O7)2 and its hydrated forms | Calcium Ash insoluble in HCl if > 5 % |
| 11.1.14 | Calcium chelates (5) | Ca(x)1-3 x nH2O (x) = anion of amino acids from soya protein hydrolysate or synthetic amino acids authorised as feed additive. The chelation of the cation is proven by a maximum of 10 % molecules exceeding 1 500 Daltons and adequate analytical method proving the chelated structure of the feed material. May contain up to 40 % chloride | Calcium Ash insoluble in HCl if > 5 % |
| 11.1.15 | Calcium sulphate/carbonate | Product obtained during the manufacturing of sodium carbonate | Calcium Ash insoluble in HCl if > 5 % |
| 11.1.16 | Calcium pidolate | Calcium L-pidolate (C10H12CaN2O6 ). May contain up to 5 % glutamic acid | Calcium Ash insoluble in HCl if > 5 % |
| 11.1.17 | Calcium carbonate-magnesium oxide | Product obtained by heating of natural calcium and magnesium containing substances like dolomite. May contain up to 0,1 % grinding aids | Calcium Magnesium |
| 11.1.18 | Calcium nitrate double salt | 5 Ca(NO3)2 x NH4NO3x10 H2O. Derives from a chemical synthesis of calcium carbonate rock and nitric acid | Calcium Nitrogen |
| 11.2.1 | Magnesium oxide | Calcined magnesium oxide (MgO), not less than 70 % MgO | Magnesium Ash insoluble in HCl if > 15 %, Iron content as Fe2O3 if > 5 %. |
| 11.2.2 | Magnesium sulphate heptahydrate | Magnesium sulphate (MgSO4 × 7 H2O) | Magnesium Sulphur Ash insoluble in HCl if > 15 % |
| 11.2.3 | Magnesium sulphate monohydrate | Magnesium sulphate (MgSO4 × H2O) | Magnesium Sulphur Ash insoluble in HCl if > 15 % |
| 11.2.4 | Magnesium sulphate anhydrous | Anhydrous magnesium sulphate (MgSO4) | Magnesium Sulphur Ash insoluble in HCl if > 10 % |
| 11.2.5 | Magnesium propionate | Magnesium propionate (C6H10MgO4) | Magnesium |
| 11.2.6 | Magnesium chloride | Magnesium chloride (MgCl2) or solution obtained by natural concentration of sea water after deposit of sodium chloride | Magnesium Chlorine Ash insoluble in HCl if > 10 % |
| 11.2.7 | Magnesium carbonate | Natural magnesium carbonate (MgCO3) | Magnesium Ash insoluble in HCl if > 10 % |
| 11.2.8 | Magnesium hydroxide | Magnesium hydroxide (Mg(OH)2) | Magnesium Ash insoluble in HCl if > 10 % |
| 11.2.9 | Magnesium potassium sulphate | Magnesium potassium sulphate (K2Mg(SO4)2 x nH2O, n= 4,6) | Magnesium Potassium Ash insoluble in HCl if > 10 % |
| 11.2.10 | Magnesium salts of organic acids (3) | Magnesium salts of edible organic acids with at least 4 carbon atoms (4) | Magnesium Organic acid |
| 11.2.11 | Magnesium gluconate | Magnesium salt of gluconic acid generally expressed as Mg(C6H11O7)2 and its hydrated forms | Magnesium Ash insoluble in HCl if > 5 % |
| 11.2.12 | Magnesium chelates (5) | formula Mg(x)1-3 x nH2O (x) = anion of amino acids from soya protein hydrolysate or synthetic amino acids authorised as feed additive. The chelation of the cation is proven by a maximum of 10 % molecules exceeding 1 500 Daltons and adequate analytical method proving the chelated structure of the feed material. May contain up to 55 % chloride and/or sulphate | Magnesium Ash insoluble in HCl if > 5 % |
| 11.2.13 | Magnesium pidolate | Magnesium L-pidolate (C10H12MgN2O6). May contain up to 5 % glutamic acid | Magnesium Ash insoluble in HCl if > 5 % |
| 11.3.1 | Dicalcium phosphate (6) (7) [calcium hydrogen orthophosphate] | Calcium monohydrogen phosphate obtained from bones or inorganic sources (CaHPO4 × nH2O, n = 0 or 2). Ca/P > 1,2. May contain up to 3 % chloride expressed as NaCl | Calcium Total phosphorus P insoluble in 2 % citric acid if > 10 % Ash insoluble in HCl if > 5 % |
| 11.3.2 | Monodicalcium phosphate | Product composed of dicalcium phosphate and monocalcium phosphate (CaHPO4 × Ca(H2PO4)2 × nH2O, n = 0 or 1) 0,8 < Ca/P < 1,3 | Total phosphorus, Calcium P insoluble in 2 % citric acid if > 10 % |
| 11.3.3 | Monocalcium phosphate; [calcium tetrahydrogen diorthophosphate] | Calcium-bis dihydrogenphosphate (Ca(H2PO4)2 × nH2O, n=0 or 1) Ca/P < 0,9 | Total phosphorus Calcium P insoluble in 2 % citric acid if > 10 % |
| 11.3.4 | Tricalcium phosphate (7) [tricalcium orthophosphate] | Tricalcium phosphate from bones or inorganic sources (Ca3(PO4)2 × H2O) or hydroxyl apatite (Ca5(PO4)3OH) Ca/P > 1,3 | Calcium Total phosphorus P insoluble in 2 % citric acid if > 10 % Ash insoluble in HCl if > 5 % |
| 11.3.5 | Calcium-magnesium phosphate | Calcium-magnesium phosphate (Ca3Mg3(PO4)4). | Calcium Magnesium Total phosphorus P insoluble in 2 % citric acid if > 10 % |
| 11.3.6 | Defluorinated phosphate | Product obtained from inorganic sources, calcined and further heat treated. | Total phosphorus Calcium Sodium P insoluble in 2 % citric acid if > 10 % Ash insoluble in HCl if > 5 % |
| 11.3.7 | Dicalcium pyrophosphate; [Dicalcium diphosphate] | Dicalcium pyrophosphate (Ca2P2O7) from bones or inorganic sources. | Total phosphorus Calcium P insoluble in 2 % citric acid if > 10 % |
| 11.3.8 | Magnesium phosphate | Product consisting of monobasic and/or di-basic and/or tri-basic magnesium phosphate. | Total phosphorus Magnesium P insoluble in 2 % citric acid if > 10 % Ash insoluble in HCl if > 10 % |
| 11.3.9 | Sodium-calcium-magnesium phosphate | Product consisting of sodium-calcium-magnesium phosphate. | Total phosphorus Magnesium Calcium Sodium P insoluble in 2 % citric acid if > 10 % |
| 11.3.10 | Monosodium phosphate; [Sodium dihydrogen orthophosphate] | Monosodium phosphate. (NaH2PO4 × nH2O ; n = 0, 1 or 2) | Total phosphorus Sodium P insoluble in 2 % citric acid if > 10 % |
| 11.3.11 | Disodium phosphate; [Disodium hydrogen orthophosphate] | Disodium phosphate (Na2HPO4 × nH2O ; n = 0, 2, 7 or 12) | Total phosphorus Sodium P insoluble in 2 % citric acid if > 10 % |
| 11.3.12 | Trisodium Phosphate; [Trisodium orthophosphate] | Trisodium phosphate (Na3PO4 × nH2O ; n = 0, 1/2, 1, 6, 8 or 12) | Total phosphorus Sodium P insoluble in 2 % citric acid if > 10 % |
| 11.3.13 | Sodium pyrophosphate; [Tetrasodium diphosphate] | Sodium pyrophosphate (Na4P2O7× nH2O ; n = 0 or 10) | Total phosphorus Sodium P insoluble in 2 % citric acid if > 10 % |
| 11.3.14 | Monopotassium phosphate; [Potassium dihydrogen orthophosphate] | Monopotassium phosphate (KH2PO4) | Total phosphorus Potassium P insoluble in 2 % citric acid if > 10 % |
| 11.3.15 | Dipotassium phosphate; [Di-potassium hydrogen orthophosphate] | Dipotassium phosphate (K2HPO4 × nH2O; n= 0, 3 or 6) | Total phosphorus Potassium P insoluble in 2 % citric acid if > 10 % |
| 11.3.16 | Calcium sodium phosphate | Calcium sodium phosphate (CaNaPO4) | Total phosphorus Calcium Sodium P insoluble in 2 % citric acid if > 10 % |
| 11.3.17 | Monoammonium phosphate; [Ammonium dihydrogen orthophosphate] | Monoammonium phosphate (NH4H2PO4) | Total nitrogen Total phosphorus P insoluble in 2 % citric acid if > 10 % |
| 11.3.18 | Diammonium phosphate; [Diammonium hydrogen orthophosphate] | Diammonium phosphate ((NH4)2HPO4) | Total nitrogen Total phosphorus P insoluble in 2 % citric acid if > 10 % |
| 11.3.19 | Sodium tripolyphosphate; [Penta sodium triphosphate] | Sodium tripolyphosphate (Na5P3O10 × nH2O ; n = 0 or 6) | Total phosphorus Sodium P insoluble in 2 % citric acid if > 10 % |
| 11.3.20 | Sodium magnesium phosphate | Sodium-magnesium phosphate (MgNaPO4) | Total phosphorus Magnesium Sodium P insoluble in 2 % citric acid if > 10 % |
| 11.3.21 | Magnesium hypophosphite | Magnesium hypophosphite (Mg(H2PO2)2 × 6H2O) | Magnesium Total phosphorus P insoluble in 2 % citric acid if > 10 % |
| 11.3.22 | Degelatinised bone meal | Degelatinised, sterilised and ground bones from which the fat has been removed. | Total phosphorus Calcium Ash insoluble in HCl if > 10 % |
| 11.3.23 | Bone ash | Mineral residues from the incineration, combustion or gasification of animal by-products. | Total phosphorus Calcium Ash insoluble in HCl if > 10 % |
| 11.3.24 | Calcium polyphosphate | Heterogeneous mixtures of calcium salts of condensed polyphosphoric acids of general formula H(n+2)PnO(3n+1) where ‘n’ is not less than 2. | Total phosphorus Calcium P insoluble in 2 % citric acid if > 10 % |
| 11.3.25 | Calcium dihydrogen diphosphate | Monocalcium dihydrogen pyrophosphate(CaH2P2O7) | Total phosphorus Calcium P insoluble in 2 % citric acid if > 10 % |
| 11.3.26 | Magnesium acid pyrophosphate | Magnesium acid pyrophosphate (MgH2P2O7.) Produced from purified phosphoric acid and purified magnesium hydroxide or magnesium oxide by evaporation of water and condensation of the orthophosphate to diphosphate. | Total phosphorus Magnesium P insoluble in 2 % citric acid if > 10 % |
| 11.3.27 | Disodium dihydrogen diphosphate | Disodium dihydrogen diphosphate (Na2H2P2O7) | Total phosphorus Sodium P insoluble in 2 % citric acid if > 10 % |
| 11.3.28 | Trisodium diphosphate | Trisodium monohydrogen diphosphate (anhydrous: Na3HP2O7; monohydrate: Na3HP2O7 × nH2O; n = 0, 1 or 9) | Total phosphorus Sodium P insoluble in 2 % citric acid if > 10 % |
| 11.3.29 | Sodium polyphosphate; [Sodium hexametaphosphate] | Heterogeneous mixtures of sodium salts of linear condensed polyphosphoric acids of general formula H(n + 2)PnO(3n + 1) where ‘n’ is not less than 2. | Total phosphorus Sodium P insoluble in 2 % citric acid if > 10 % |
| 11.3.30 | Tripotassium phosphate | Tripotassium monophosphate ( K3PO4 × nH2O; n = 0, 1, 3, 7 or 9) | Total phosphorus Potassium P insoluble in 2 % citric acid if > 10 % |
| 11.3.31 | Tetrapotassium di-phosphate | Tetrapotassium pyrophosphate (K4P2O7 × nH2O; n = 0, 1 or 3) | Total phosphorus Potassium P insoluble in 2 % citric acid if > 10 % |
| 11.3.32 | Pentapotassium tri-phosphate | Pentapotassium tri-polyphosphate (K5P3O10) | Total phosphorus Potassium P insoluble in 2 % citric acid if > 10 % |
| 11.3.33 | Potassium polyphosphate | Heterogeneous mixtures of potassium salts of linear condensed polyphosphoric acids of general formula H(n + 2)PnO(3n + 1) where ‘n’ is not less than 2 | Total phosphorus Potassium P insoluble in 2 % citric acid if > 10 % |
| 11.3.34 | Calcium sodium polyphosphate | Calcium sodium polyphosphate | Total phosphorus Sodium Calcium P insoluble in 2 % citric acid if > 10 % |
| 11.4.1 | Sodium chloride (1) | Sodium chloride (NaCl) or product obtained by evaporative crystallisation from brine (saturated or depleted in another process) (vacuum salt) or evaporation of seawater (marine salt and solar salt) or grinding rock salt | Sodium Ash insoluble in HCl if > 10 % |
| 11.4.2 | Sodium bicarbonate [sodium hydrogencarbonate] | Sodium bicarbonate (NaHCO3) | Sodium Ash insoluble in HCl if > 10 % |
| 11.4.3 | Sodium/ammonium (bi)carbonate [sodium/ammonium (hydrogen)carbonate] | Product obtained during the production of sodium carbonate and sodium bicarbonate, with traces of ammonium bicarbonate (ammonium bicarbonate max. 5 %) | Sodium Ash insoluble in HCl if > 10 % |
| 11.4.4 | Sodium carbonate | Sodium carbonate (Na2CO3) | Sodium Ash insoluble in HCl if > 10 % |
| 11.4.5 | Sodium sesquicarbonate [trisodium hydrogendicarbonate] | Sodium sesquicarbonate (Na3H(CO3)2) | Sodium Ash insoluble in HCl if > 10 % |
| 11.4.6 | Sodium sulphate | Sodium sulphate (Na2SO4) May contain up to 0,3 % methionine | Sodium Ash insoluble in HCl if > 10 % |
| 11.4.7 | Sodium salts of organic acids (3) (8) | Sodium salts of edible organic acids with at least 4 carbon atoms (27) | Sodium Organic acid |
| 11.4.8 | Sodium gluconate | Sodium salt of gluconic acid generally expressed as Na(C6H11O7) and its hydrated forms. | Sodium Ash insoluble in HCl if > 10 % |
| 11.5.1 | Potassium chloride | Potassium chloride (KCl) or product obtained by evaporation of seawater or grinding natural sources of potassium chloride | Potassium Ash insoluble in HCl if > 10 % |
| 11.5.2 | Potassium sulphate | Potassium sulphate (K2SO4) | Potassium Ash insoluble in HCl if > 10 % |
| 11.5.3 | Potassium carbonate | Potassium carbonate (K2CO3) | Potassium Ash insoluble in HCl if > 10 % |
| 11.5.4 | Potassium bicarbonate [potassium hydrogen carbonate] | Potassium bicarbonate (KHCO3) | Potassium Ash insoluble in HCl if > 10 % |
| 11.5.5 | Potassium salts of organic acids (3) (9) | Potassium salts of edible organic acids with at least 4 carbon atoms (4) | Potassium Organic acid |
| 11.5.6 | Potassium pidolate | Potassium L-pidolate (C5H6KNO3). May contain up to 5 % glutamic acid | Potassium Ash insoluble in HCl if > 5 % |
| 11.6.1 | Flower of sulphur | Powder obtained from natural deposits of the mineral. Also, product obtained from oil refinery production as practised by sulphur manufacturers | Sulphur |
| 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 (SiO2) obtained from the re-crystallisation of quartz May contain up to 0,1 % grinding aids | |
| 11.8.1 | Ammonium sulphate | Ammonium sulphate ((NH4)2SO4) obtained by chemical synthesis. May be presented in the form of an aqueous solution | Nitrogen Sulphur |
| 11.8.3 | Ammonium salts of organic acids (3) | Ammonium salts of edible organic acids with at least 4 carbon atoms (4) | Nitrogen Organic acid |
| 11.8.4 | Ammonium lactate (2) | Ammonium lactate (CH3CHOHCOONH4). Includes the Ammonium lactate produced by fermentation with Lactobacillus delbrueckii ssp. bulgaricus, Lactococcus lactis ssp., Leuconostoc mesenteroides, Streptococcus thermophilus, Lactobacillus spp, or Bifidobacterium spp., containing not less than 7 % nitrogen. May contain up to 2 % phosphorus, 2 % potassium, 0,7 % magnesium, 2 % sodium, 2 % sulphates 0,5 % chlorides, 5 % sugars and 0,1 % silicone antifoam | Nitrogen Crude ash Potassium if > 1,5 % Magnesium if > 1,5 %, sodium if > 1,5 % |
| 11.8.5 | Ammonium acetate (2) | Ammonium acetate (CH3COONH4) in aqueous solution, containing not less than 55 % Ammonium acetate | Nitrogen |
| 11.9.1 | Flint grit (gizzard) | Product obtained by crushing naturally occurring mineral in the form of gravel | Particle size |
| 11.9.2 | Redstone (gizzard) | Product obtained by crushing and milling of products derived from the burning of clay | Particle size Moisture if > 2 % |
| (1) The nature of the source may be indicated additionally in the name or replace it. (2) May be placed on the market and used until 30 May 2028 in accordance with Article 3 of Regulation (EU) 2022/1104. (3) The name shall be amended or supplemented to specify the fatty and/or organic acid, as appropriate (4) This does not preclude that specific salts of organic acids are classified as feed additives (5) The name shall be supplemented by the amino acid or the source of amino acids used. (6) The manufacturing process may be included in the name. (7) The name shall be supplemented by ‘from bones’, where appropriate. (8) Sodium citrates may be placed on the market and used until 30 May 2028 in accordance with Article 3 of Regulation (EU) 2022/1104. (9) Potassium citrates may be placed on the market and used until 30 May 2028 in accordance with Article 3 of Regulation (EU) 2022/1104. |
Feed materials whose number starts with ‘12.1’ are fermentation products obtained from whole micro-organisms or their parts. Feed materials whose number starts with ‘12.2’ are fermentation co-products mainly consisting of microbial biomass and those whose number starts with ‘12.3’ are other fermentation co-products.
Feed materials whose number starts with ‘12.1’ or ‘12.2’ may contain up to 0,3 % antifoaming agents, 1,5 % filtration/clarifying agents and 2,9 % propionic acid. Feed materials whose number starts with ‘12.3’ may contain up to 0,6 % antifoaming agents, 0,5 % antiscaling agents and 0,2 % sulphites.
All microorganisms (including germinable spores) used for fermentation shall be inactivated resulting in absence of viable micro-organisms in the feed materials.
Feed materials in this chapter produced from genetically modified micro-organisms shall be compliant with Regulation (EC) No 1829/2003 on genetically modified food and feed.
| Number | Name (1) | Description | Compulsory declarations |
|---|---|---|---|
| 12.1.5 | Yeasts, inactivated [brewers' yeast, inactivated, if appropriate] | Whole yeasts (1) and parts (2) thereof obtained from Saccharomyces bayanus, Saccharomyces cerevisiae, Saccharomyces pastorianus, Saccharomyces carlsbergensis, Kluyveromyces lactis, Kluyveromyces marxianus, Metschnikowia pulcherrima, Metschnikowia fructicola, Torulaspora delbrueckii, Cyberlindnera jadinii (3), Saccharomycodes ludwigii, Wickerhamomyces anomalus, Debaryomyces hansenii, Pichia guilliermondii, Yarrowia lypolitica or Brettanomyces ssp. on substrate/culture medium consisting of a carbon source mostly of vegetal origin, a nitrogen source of vegetal or chemical origin, vitamins and minerals | Moisture if < 75 % or > 97 % If moisture < 75 %: Crude protein Propionic acid if > 0,5 % |
| 12.1.9 | Single cell proteins from fungi (4) | Fermentation product obtained from culture of Aspergillus oryzae, Paecilomyces varioti or Trichoderma viride 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 | Crude protein Crude ash Propionic acid if > 0,5 % |
| 12.1.10 | Product from Bacillus subtilis rich in protein | Fermentation product obtained from culture of Bacillus subtilis 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 | Crude protein Crude ash Propionic acid if > 0,5 % |
| 12.1.12 | Yeasts products | All yeasts (32) and parts (1) thereof obtained by cracking and/or fractionation of yeast cells from Saccharomyces bayanus, Saccharomyces cerevisiae, Saccharomyces pastorianus, Saccharomyces carlsbergensis, Kluyveromyces lactis, Kluyveromyces marxianus, Metschnikowia pulcherrima, Metschnikowia fructicola, Torulaspora delbrueckii, Cyberlindnera jadinii (2), Saccharomycodes ludwigii, Wickerhamomyces anomalus, Debaryomyces hansenii, Pichia guilliermondii, Yarrowia lypolitica or Brettanomyces ssp. on substrate/culture medium consisting of a carbon source mostly of vegetal origin, a nitrogen source of vegetal or chemical origin, vitamins and minerals | Moisture if < 75 % or > 97 % |
| 12.1.13 | Single cell proteins from bacteria (4) | Protein products obtained by fermentation with bacteria on a substrate/culture medium consisting of methanol (fermented with Methylophilus methylotrophus) or natural gas (fermented with Methylococcus capsulatus, Alcaligenes acidovorans, Aneurinibacillus danicus (previously known as Bacillus brevis) and/or Bacillus firmus) as carbon source, a nitrogen source of vegetal or chemical origin, vitamins and minerals | Crude protein Crude ash |
| 12.1.14 | Inactivated bacteria and parts thereof (4) | Whole bacteria or their parts (1) obtained from Bifidobacterium spp., Lactobacillus acidophilus, Lactobacillus delbrueckii ssp. bulgaricus, Lacticaseibacillus casei, Limosilactobacillus fermentum (formerly known as Lactobacillus fermentum), Lacticaseibacillus paracasei (formerly known as Lactobacillus paracasei), Lactiplantibacillus plantarum (formerly known as Lactobacillus plantarum), Limosilactobacillus reuteri (formerly known as Lactobacillus reuteri), Lacticaseibacillus rhamnosus (formerly known as Lactobacillus rhamnosus), Lactobacillus helveticus or Streptococcus thermophiles or other species of bacteria authorised as feed additives fermented on substrate/culture medium consisting of a carbon source mostly of vegetal origin, a nitrogen source of vegetal or chemical origin, vitamins and minerals | Crude ash |
| 12.2.8 | Bacterial biomass rich in protein (4) | Protein rich co-products obtained from the production of amino acids, vitamins, organic acids, enzymes and/or their salts obtained by fermentation with Bacillus coagulans, Bacillus subtilis, Bacillus velezensis, Bacillus licheniformis, Bacillus smithii, Corynebacterium casei, Corynebacterium glutamicum, Corynebacterium melassecola, Ensifer adhaerens, Enterococcus faecium, Escherichia coli K12 or Lactobacillaceae on substrate/culture medium consisting of a carbon source mostly of vegetal origin, a nitrogen source of vegetal or chemical origin, vitamins and minerals. The product may be hydrolysed | Crude protein Crude ash |
| 12.2.9 | Fungal biomass (4) | Protein rich co-products obtained from the production of products such as enzymes, vitamins and/or organic acids obtained by fermentation with Ashbya gossypii, Aspergillus niger, Aspergillus tubingensis, Aspergillus sojae, Neurospora intermedia, Neurospora tetrasperma, Trichoderma viride, Trichoderma longibrachiatum or Trichoderma reesei on substrate/culture medium consisting of a carbon source mostly of vegetal origin, a nitrogen source of vegetal or chemical origin, vitamins and minerals | Crude protein Crude ash |
| 12.3.1 | Vinasses [condensed molasses soluble] | Co-products derived from the industrial processing of musts/worts issued from microbial fermentation processes such as alcohol, organic acids or yeast manufacture. They are composed of the liquid/paste fraction obtained after the separation of the fermentation musts/worts. They may also include dead cells and/or parts (1) thereof of the fermentation micro-organisms used | Crude protein Substrate and indication of production process as appropriate |
| 12.3.2 | Co-products of (salts of) amino-acids production (4) | Co-products from the production of amino acids and their salts by fermentation with Escherichia coli K12, Corynebacterium casei, Corynebacterium glutamicum or Corynebacterium melassecola on substrate/culture medium consisting of a carbon source mostly of vegetal origin, a nitrogen source of vegetal or chemical origin, vitamins and minerals | Crude protein Crude ash |
| 12.3.3 | Co-products of enzymes production (4) | Co-products from the production of enzymes by fermentation with Aspergillus niger, Aspergillus tubingensis, Aspergillus oryzae, Aspergillus sojae, Neurospora intermedia, Trichoderma longibrachiatum, Trichoderma viride or Trichoderma reesei on substrate/culture medium consisting of a carbon source of vegetal origin, a nitrogen source of vegetal or chemical origin, vitamins and minerals | Crude protein Crude ash |
| 12.3.4 | Bacterial product rich in polyhydroxybutyrate | Product containing 3-hydroxybutyrate and 3-hydroxyvalerate, produced via fermentation with Cupriavidus necator, and non-viable bacterial protein meal remaining from the producing bacteria and fermentation broth | Butyrate |
| 12.3.5 | Bacterial product rich in ammonium lactate (4) | Ammonium lactate (CH3CHOHCOONH4) rich product from fermentation with Lactobacillus delbrueckii ssp. bulgaricus and other Lactobacillaceae, Lactococcus lactis, Leuconostoc mesenteroides, Streptococcus thermophiles or Bifidobacterium spp., containing not less than 5,6 % nitrogen | Nitrogen Crude ash Potassium if > 1,5 % Magnesium if > 1,5 %, sodium if > 1,5 % |
| 12.3.6 | Co-product from the production of glucono-delta-lactone, rich in gluconic acid (4) | Liquid co-product from the cristallisation of food grade glucono-delta-lactone obtained by fermentation with Gluconobacter oxydans or Aspergillus niger. It contains a minimum of 50 % of gluconic acid | Gluconic acid |
| (1) The used name of the yeast strains may vary from the scientific taxonomy. Therefore, synonyms of the yeast strains listed could also be used. (2) Parts means any soluble and insoluble fractions of the microorganism including from the membrane or the inner parts of the cell. (3) Shall not be cultivated on n-alkanes (Annex III to Regulation (EU) No 767/2009, as amended). (4) The species of microorganism(s) shall be indicated with the name of the feed material, and the term ‘inactivated’ may be added (i.e. ‘name as in the catalogue’ + ‘name of the species’; examples (i) ‘Single cell proteins from Methylococcus capsulatus’, (ii) ‘Inactivated Lactobacillus acidophilus’). |
Feed materials in this chapter containing animal by-products shall fulfil the requirements of Regulation (EC) No 1069/2009 and Regulation (EU) No 142/2011 and may be subject to restrictions in use according to Regulation (EC) No 999/2001.
| Number | Name (1) | Description | Compulsory declarations |
|---|---|---|---|
| 13.1.1 | Products from the bakery and pasta industry | Products obtained during and from the production of bread, biscuits, wafers or pasta | Starch Total sugars, calculated as sucrose, Crude fat, if > 5 % |
| 13.1.2 | Products from the pastry industry | Products obtained during and from the production of pastry and cakes | Starch Total sugars, calculated as sucrose, Crude fat, if > 5 % |
| 13.1.3 | Products of the breakfast cereal manufacture | Substances or products that are intended or where it is reasonable to expect that they can be consumed by humans in their processed, partially processed or unprocessed forms | Crude protein, if > 10 % Crude fibre Crude oils/fats, if > 10 %, Starch, if > 30 % Total sugars, calculated as sucrose, if > 10 % |
| 13.1.4 | Products from the confectionery industry | Products obtained during and from the production of sweets, including chocolate goods | Starch Crude fat, if > 5 % Total sugars, calculated as sucrose |
| 13.1.5 | Products of the ice-cream industry | Products obtained during the production of ice-cream | Starch Total sugars, calculated as sucrose, Crude fat |
| 13.1.6 | Products and co-products from processing fresh fruits and vegetables (17) | Products obtained when processing fresh fruit and vegetables (including peel, whole pieces of fruit/vegetables, and mixtures thereof). They may have been frozen | Starch Crude fibre Crude fat, if > 5 % Ash insoluble in HCl, if > 3,5 % |
| 13.1.7 | Products from the processing of plants (17) | Products obtained from freezing or drying whole plants (15) or their parts | Crude Fibre |
| 13.1.8 | Products from processing of spices and seasonings (17) | Products obtained from freezing or drying spices and seasonings or their parts | Crude protein, if > 10 % Crude fibre Crude oils/fats, if > 10 %, Starch, if > 30 % Total sugars, calculated as sucrose, if > 10 % |
| 13.1.9 | Products from the processing of herbs (17) | Products obtained from crushing, grinding, freezing or drying herbs or their parts | Crude Fibre |
| 13.1.10 | Products from the potato processing industry | Products obtained when processing potatoes. They may have been frozen | Starch Crude fibre Crude fat, if > 5 % Ash insoluble in HCl, if > 3,5 % |
| 13.1.11 | Products and co-products of the sauces production | Substances from the sauces-production that are intended or where it is reasonable to expect that they can be consumed by humans in their processed, partially processed or unprocessed forms | Crude fat |
| 13.1.12 | Products and co-products from the savoury snacks industry | Products and co-products of the savoury snacks industry obtained during and from the production of savoury snacks — potato chips, potato and/or cereal based snacks (direct extruded, dough based and pelleted snacks) and nuts | Crude fat |
| 13.1.13 | Products from the ready-to-eat food industry | Products obtained during the production of ready-to-eat food (1) | Crude fat, if > 5 % |
| 13.1.14 | Plants co-products from spirits production | Solid products from plants (including berries and seeds such as anise) obtained after maceration of these plants in an alcoholic solution or after alcoholic evaporation/distillation, or both, in the elaboration of flavourings for the spirits production. These products must be distilled to eliminate the alcoholic residue | Crude protein, if > 10 % Crude fibre Crude oils/fats, if > 10 % |
| 13.1.15 | Feed beer | Product of the brewing process which is not marketable as a human beverage | Alcohol content Moisture if < 75 % |
| 13.1.16 | Sweet flavored drink | Products from the soft drink industry obtained from the production of sweet flavoured soft drinks or from unpacked non-marketable sweet-flavoured soft drinks | Total sugars, calculated as sucrose. Moisture if > 30 % |
| 13.1.17 | Fruit Syrup | Products from the fruit syrup industry obtained from the manufacture of fruit syrup for human consumption | Total sugars, calculated as sucrose Moisture if > 30 % |
| 13.1.18 | Sweet flavored syrup | Products from the sweet flavored syrup industry obtained from the production of syrup or from unpacked non-marketable syrup | Total sugars, calculated as sucrose. Moisture if > 30 % |
| 13.1.19 | Used food factory vegetable oils | Vegetable oils having been used by food business operators in accordance with Regulation (EC) No 852/2004 for cooking purposes and which have not been in contact with meat, animal fats, fish or aquatic animals | Moisture, if > 1 % |
| 13.2.1 | Caramelised sugars | Product obtained by the controlled heating of any sugar | Total sugars, calculated as sucrose |
| 13.2.2 | Dextrose | Dextrose is obtained after hydrolysis of starch and consists of purified, crystallised glucose, with or without crystal water | |
| 13.2.3 | Fructose | Fructose as purified crystalline powder. It is obtained from glucose in glucose syrup by the use of glucose isomerase and from sucrose inversion | |
| 13.2.4 | Glucose syrup | Glucose syrup is a purified and concentrated aqueous solution of nutritive saccharides obtained through hydrolysis from starch | Moisture if > 30 % |
| 13.2.5 | Glucose molasses | Product produced during refining process of glucose syrups | Total sugars, calculated as sucrose |
| 13.2.6 | Xylose | Sugar extracted from wood | |
| 13.2.7 | Lactulose | Semi-synthetic disaccharide (4-O-D-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 (Chitosamine) (2) | Amino sugar (monosaccharide) being part of the structure of the polysaccharides chitosan and chitin. Produced by the hydrolysis of crustacean and other arthropod exoskeletons or by fermentation of grain such as corn or wheat | Sodium or Potassium, as applicable |
| 13.2.9 | Xylo-oligosaccharide | Chains of xylose molecules linked with β1–4 bonds with degree of polymerization ranging from 2 to 10 and produced from enzymatic hydrolysis of various feedstocks rich in hemicellulose | Moisture if > 5 % |
| 13.2.10 | Gluco-oligosaccharide | Product obtained by either fermentation or hydrolysis and/or physical thermal treatment of glucose polymers, glucose, sucrose and maltose | Moisture if > 28 % |
| 13.2.11 | Fructo-oligosaccharides | Product obtained from sugar from sugar beet or sugar cane through an enzymatic process or from physical treatment of fresh cultivated pasture grass | Moisture if > 28 % |
| 13.2.12 | Trehalose | Non-reducing disaccharide consisting in two glucose moieties linked by an α-1,1-glucosidic bond. It is produced from liquefied starch further to multistep enzymatic process. | trehalose if < 98,0 % (on anhydrous base), moisture if > 11,0 % |
| 13.3.1 | Starch (3) | Starch | Starch |
| 13.3.2 | Starch (3) , pre-gelatinised | Product consisting of starch expanded by heat treatment | Starch |
| 13.3.3 | Starch (3) mixture | Product consisting of native and/or modified food starch obtained from different botanical sources | Starch |
| 13.3.4 | Starch (3) hydrolysates cake | Product from starch hydrolysis liquor filtration which consists of the following: protein, starch, polysaccharides, fat, oil and filter aid (e.g. diatomaceous earth, wood fibre) | Moisture if < 25 % or > 45 % If moisture < 25 %: — 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 (4) | 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 (25) | Product obtained by hydrogenation or fermentation and consisting of reduced glucose and/or fructose | |
| 13.5.4 | Xylitol (25) | Product obtained by hydrogenation and fermentation of xylose | |
| 13.5.5 | Sorbitol (25) | Product obtained by hydrogenation of glucose | |
| 13.6.1 | Acid oils from chemical refining (5) | Product obtained during the deacidification of oils and fats of vegetable or animal origin by means of alkali, followed by an acidulation with 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, crude lecithin and fibres | Crude fat Moisture if > 1 % |
| 13.6.2 | Fatty acids esterified with glycerol (26) | Glycerides obtained by esterification of fatty acids with glycerol. May contain up to 50 ppm nickel from hydrogenation | Moisture if > 1 % Crude fat Nickel if > 20 ppm |
| 13.6.3 | Mono di and tri glycerides of fatty acids (26) | Product consisting of reaction mass of mono-, di- and triesters of glycerol with fatty acids. They may contain small amounts of free fatty acids and up to 7 % glycerol. May contain up to 50 ppm Nickel from hydrogenation | Crude fat Nickel if > 20 ppm |
| 13.6.4 | Salts of fatty acids (26) | Product obtained by reaction of fatty acids with at least 4 carbon atoms with calcium, magnesium, sodium or potassium hydroxides, oxides or salts. May contain up to 50 ppm nickel from hydrogenation | Crude fat (after hydrolysis) Moisture Ca or Na or K or Mg (when appropriate) Nickel if > 20 ppm |
| 13.6.5 | Fatty acid distillates from physical refining (3) | Product obtained during the deacidification of oils and fats of vegetable or animal origin by 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 | Crude fat Moisture if > 1 % |
| 13.6.6 | Crude fatty acids (3) (6) | Product obtained by fermentation of organic matter, by enzymatic interesterification of oil or by oil/fat splitting. By definition it consists of crude fatty acids C4-C24, aliphatic, linear, monocarboxylic, saturated and unsaturated. May contain up to 50 ppm nickel in case it has undergone hydrogenation | Crude fat Moisture if > 1 % Nickel if > 20 ppm |
| 13.6.7 | Pure distilled fatty acids (3) (4) | Product obtained by the distillation of crude fatty acids produced by fermentation of organic matter, by enzymatic interesterification of oil or by oil/fat splitting potentially plus hydrogenation. By definition it consists of pure distilled fatty acids C4-C24, aliphatic, linear, monocarboxylic, saturated and unsaturated. May contain up to 50 ppm Nickel in case it has undergone hydrogenation | Crude fat Moisture if > 1 % Nickel if > 20 ppm |
| 13.6.8 | Soap stocks (3) | Product obtained during the deacidification of vegetable oils and fats by means of aqueous calcium, magnesium, sodium or potassium hydroxide solution, containing salts of fatty acids, oils or fats and natural components of seeds, fruits or animal tissues such as mono- and diglycerides, crude lecithin and fibres | Moisture if < 40 and > 50 % Ca or Na or K or Mg, as appropriate |
| 13.6.9 | Mono- and diglycerides of fatty acids esterified with organic acids (26) | Mono- and diglycerides of fatty acids with at least 4 carbon atoms esterified with organic acids | Crude fat |
| 13.6.10 | Sucrose esters of fatty acids (26) | Esters of saccharose and fatty acids | Total sugars, calculated as sucrose Crude fat |
| 13.6.11 | Sucroglycerides of fatty acids (26) | Mixture of esters of saccharose and mono and di-glycerides of fatty acids | Total sugars, calculated as sucrose Crude fat |
| 13.6.12 | Palmitoylglucosamine | Lipid organic compound present in the roots of many plants and particularly in most leguminous plants. Palmitoylglucosamine (C22H43NO6) is produced by acylation of D-glucosamine with palmitic acid. May contain up to 0,5 % acetone | Crude fat Moisture if > 2 % |
| 13.6.13 | Salt of lactylates of fatty acids | Non-glyceride ester of fatty acids. The product can be a calcium, magnesium, sodium or potassium salt of fatty acids esterified with lactic acid. It may contain the salts of free fatty acids and lactic acid | Crude fat Moisture if > 1 % Nickel if > 20 ppm Ca or Na or K or Mg as appropriate |
| 13.6.14 | Palmitoylethanolamide | Lipid organic compound present in soy lecithin, eggs and other feed sources. Palmitoylethanolamide (C18H37NO2) is produced by synthesis from the reaction of palmitic acid with ethanolamine | Crude fat Moisture if > 2 % |
| 13.8.1 | Glycerine, crude [Glycerol, crude] | Co-product obtained from: — the oleochemical process of oil/fat splitting to obtain fatty acids and sweet water, followed by concentration of the sweet water to get crude glycerol or by 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; — saponification 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 | Glycerol Potassium if > 1,5 % Sodium if > 1,5 % Nickel if > 20 ppm |
| 13.8.2 | Glycerine [Glycerol] | Product obtained from: — the oleochemical process of (a) oil/fat splitting followed by concentration of sweet waters and refining by distillation (see part B, glossary of processes, entry 20) or ion-exchange process; (b) transesterification 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; — saponification 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 | Glycerol if < 99 % on dry matter basis Sodium if > 0,1 % Potassium if > 0,1 % Nickel if > 20 ppm |
| 13.9.1 | Methyl sulphonyl methane | Organo-sulfur compound ((CH3)2SO2) obtained by chemical synthesis which is identical to the naturally occurring source in plants | Sulphur |
| 13.10.1 | Peat | Product from the natural decomposition of plant (mainly sphagnum) in anaerobic and oligotrophic environment | Crude Fibre |
| 13.10.2 | Leonardite | Product that is a naturally occurring mineral complex of phenolic hydrocarbons, also known as humate, which originates from the decomposition of organic matter over the course of millions of years | Crude Fibre |
| 13.11.1 | Propylene glycol; [1,2-propanediol]; [propane-1,2-diol] | Organic compound (a diol or double alcohol) with formula C3H8O2. It is a viscous liquid with 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 propylene glycol and fatty acids (26) | Mono-esters of propylene glycol and fatty acids, alone or in mixtures with di-esters | Propylene glycol Crude fat |
| 13.12.1 | Hyaluronic acid (36) | Glucosamineglucan (polysaccharide) with repeating unit consisting of an amino sugar (N-acetyl-D- glucosamine) and D-glucuronic acid present in the skin, synovial fluid and the umbilical cord, produced, for example, from animal tissue or by bacterial fermentation | Sodium or Potassium, as applicable |
| 13.12.2 | Chondroitin sulphate (36) | Product obtained by extraction from tendons, bones and other animal tissues containing cartilage and soft connective tissues, or by sulphation of chondroitin isolated from microbial fermentation | Sodium |
| (1) As defined in Article 2(g) of Commission Regulation (EC) No 2073/2005 of 15 November 2005 on microbiological criteria for foodstuffs (OJ L 338, 22.12.2005, p. 1). (2) The name shall be supplemented by the words ‘from animal tissues’ or ‘from fermentation’, as appropriate. (3) The name shall be supplemented by the indication of the botanical origin. (4) With the exception of mannitol, sorbitol and xylitol. (5) The name shall be supplemented by the indication of the botanical or animal origin, as appropriate. (6) The name of the feed materials shall be supplemented by the words ‘from splitting’, ‘from fermentation’ or ‘from enzymatic transesterification’, as appropriate. |
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