CN104351726A - Chicken powder and automatic production technology thereof - Google Patents
Chicken powder and automatic production technology thereof Download PDFInfo
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- CN104351726A CN104351726A CN201410627669.3A CN201410627669A CN104351726A CN 104351726 A CN104351726 A CN 104351726A CN 201410627669 A CN201410627669 A CN 201410627669A CN 104351726 A CN104351726 A CN 104351726A
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- chicken
- chicken powder
- compound
- raw material
- amino acid
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- NEGYEDYHPHMHGK-UHFFFAOYSA-N para-methoxyamphetamine Chemical compound COC1=CC=C(CC(C)N)C=C1 NEGYEDYHPHMHGK-UHFFFAOYSA-N 0.000 title claims abstract description 42
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 32
- 238000005516 engineering process Methods 0.000 title abstract description 6
- 241000287828 Gallus gallus Species 0.000 claims abstract description 42
- 239000002994 raw material Substances 0.000 claims abstract description 33
- 239000003963 antioxidant agent Substances 0.000 claims abstract description 23
- 230000003078 antioxidant effect Effects 0.000 claims abstract description 23
- 239000000463 material Substances 0.000 claims abstract description 19
- IIZPXYDJLKNOIY-JXPKJXOSSA-N 1-palmitoyl-2-arachidonoyl-sn-glycero-3-phosphocholine Chemical compound CCCCCCCCCCCCCCCC(=O)OC[C@H](COP([O-])(=O)OCC[N+](C)(C)C)OC(=O)CCC\C=C/C\C=C/C\C=C/C\C=C/CCCCC IIZPXYDJLKNOIY-JXPKJXOSSA-N 0.000 claims abstract description 17
- RQFCJASXJCIDSX-UUOKFMHZSA-N guanosine 5'-monophosphate Chemical compound C1=2NC(N)=NC(=O)C=2N=CN1[C@@H]1O[C@H](COP(O)(O)=O)[C@@H](O)[C@H]1O RQFCJASXJCIDSX-UUOKFMHZSA-N 0.000 claims abstract description 17
- 235000013928 guanylic acid Nutrition 0.000 claims abstract description 17
- 239000004226 guanylic acid Substances 0.000 claims abstract description 17
- 235000010445 lecithin Nutrition 0.000 claims abstract description 17
- 239000000787 lecithin Substances 0.000 claims abstract description 17
- 229940067606 lecithin Drugs 0.000 claims abstract description 17
- WQZGKKKJIJFFOK-GASJEMHNSA-N Glucose Natural products OC[C@H]1OC(O)[C@H](O)[C@@H](O)[C@@H]1O WQZGKKKJIJFFOK-GASJEMHNSA-N 0.000 claims abstract description 14
- 239000008103 glucose Substances 0.000 claims abstract description 14
- 150000001875 compounds Chemical class 0.000 claims description 38
- 230000001954 sterilising effect Effects 0.000 claims description 36
- 238000004659 sterilization and disinfection Methods 0.000 claims description 36
- 235000001014 amino acid Nutrition 0.000 claims description 25
- 150000001413 amino acids Chemical class 0.000 claims description 25
- 210000000988 bone and bone Anatomy 0.000 claims description 23
- 239000000084 colloidal system Substances 0.000 claims description 20
- 239000000839 emulsion Substances 0.000 claims description 20
- 238000000227 grinding Methods 0.000 claims description 20
- 239000000796 flavoring agent Substances 0.000 claims description 19
- QXNVGIXVLWOKEQ-UHFFFAOYSA-N Disodium Chemical compound [Na][Na] QXNVGIXVLWOKEQ-UHFFFAOYSA-N 0.000 claims description 15
- 239000002773 nucleotide Substances 0.000 claims description 15
- 125000003729 nucleotide group Chemical group 0.000 claims description 15
- 150000003839 salts Chemical class 0.000 claims description 15
- 238000003860 storage Methods 0.000 claims description 15
- CEYULKASIQJZGP-UHFFFAOYSA-L disodium;2-(carboxymethyl)-2-hydroxybutanedioate Chemical compound [Na+].[Na+].[O-]C(=O)CC(O)(C(=O)O)CC([O-])=O CEYULKASIQJZGP-UHFFFAOYSA-L 0.000 claims description 13
- 239000007788 liquid Substances 0.000 claims description 13
- 238000000926 separation method Methods 0.000 claims description 13
- 239000007787 solid Substances 0.000 claims description 13
- 239000000203 mixture Substances 0.000 claims description 11
- DHMQDGOQFOQNFH-UHFFFAOYSA-N Glycine Chemical compound NCC(O)=O DHMQDGOQFOQNFH-UHFFFAOYSA-N 0.000 claims description 10
- 235000015228 chicken nuggets Nutrition 0.000 claims description 10
- 239000006185 dispersion Substances 0.000 claims description 10
- 238000010008 shearing Methods 0.000 claims description 10
- 239000002002 slurry Substances 0.000 claims description 10
- 238000009835 boiling Methods 0.000 claims description 9
- LPUQAYUQRXPFSQ-DFWYDOINSA-M monosodium L-glutamate Chemical compound [Na+].[O-]C(=O)[C@@H](N)CCC(O)=O LPUQAYUQRXPFSQ-DFWYDOINSA-M 0.000 claims description 8
- 235000013923 monosodium glutamate Nutrition 0.000 claims description 8
- 239000004223 monosodium glutamate Substances 0.000 claims description 8
- 238000004140 cleaning Methods 0.000 claims description 6
- 238000003756 stirring Methods 0.000 claims description 6
- 239000004475 Arginine Substances 0.000 claims description 5
- WHUUTDBJXJRKMK-UHFFFAOYSA-N Glutamic acid Natural products OC(=O)C(N)CCC(O)=O WHUUTDBJXJRKMK-UHFFFAOYSA-N 0.000 claims description 5
- 239000004471 Glycine Substances 0.000 claims description 5
- QNAYBMKLOCPYGJ-REOHCLBHSA-N L-alanine Chemical compound C[C@H](N)C(O)=O QNAYBMKLOCPYGJ-REOHCLBHSA-N 0.000 claims description 5
- CKLJMWTZIZZHCS-REOHCLBHSA-N L-aspartic acid Chemical compound OC(=O)[C@@H](N)CC(O)=O CKLJMWTZIZZHCS-REOHCLBHSA-N 0.000 claims description 5
- KZSNJWFQEVHDMF-BYPYZUCNSA-N L-valine Chemical compound CC(C)[C@H](N)C(O)=O KZSNJWFQEVHDMF-BYPYZUCNSA-N 0.000 claims description 5
- 239000004472 Lysine Substances 0.000 claims description 5
- KDXKERNSBIXSRK-UHFFFAOYSA-N Lysine Natural products NCCCCC(N)C(O)=O KDXKERNSBIXSRK-UHFFFAOYSA-N 0.000 claims description 5
- MTCFGRXMJLQNBG-UHFFFAOYSA-N Serine Natural products OCC(N)C(O)=O MTCFGRXMJLQNBG-UHFFFAOYSA-N 0.000 claims description 5
- AYFVYJQAPQTCCC-UHFFFAOYSA-N Threonine Natural products CC(O)C(N)C(O)=O AYFVYJQAPQTCCC-UHFFFAOYSA-N 0.000 claims description 5
- 239000004473 Threonine Substances 0.000 claims description 5
- KZSNJWFQEVHDMF-UHFFFAOYSA-N Valine Natural products CC(C)C(N)C(O)=O KZSNJWFQEVHDMF-UHFFFAOYSA-N 0.000 claims description 5
- 235000004279 alanine Nutrition 0.000 claims description 5
- ODKSFYDXXFIFQN-UHFFFAOYSA-N arginine Natural products OC(=O)C(N)CCCNC(N)=N ODKSFYDXXFIFQN-UHFFFAOYSA-N 0.000 claims description 5
- 235000003704 aspartic acid Nutrition 0.000 claims description 5
- OQFSQFPPLPISGP-UHFFFAOYSA-N beta-carboxyaspartic acid Natural products OC(=O)C(N)C(C(O)=O)C(O)=O OQFSQFPPLPISGP-UHFFFAOYSA-N 0.000 claims description 5
- 238000001035 drying Methods 0.000 claims description 5
- 235000013922 glutamic acid Nutrition 0.000 claims description 5
- 239000004220 glutamic acid Substances 0.000 claims description 5
- 239000008187 granular material Substances 0.000 claims description 5
- 238000010438 heat treatment Methods 0.000 claims description 5
- 238000009413 insulation Methods 0.000 claims description 5
- 238000002156 mixing Methods 0.000 claims description 5
- 210000003205 muscle Anatomy 0.000 claims description 5
- 238000004806 packaging method and process Methods 0.000 claims description 5
- 238000012856 packing Methods 0.000 claims description 5
- 239000002245 particle Substances 0.000 claims description 5
- 230000002093 peripheral effect Effects 0.000 claims description 5
- 150000008442 polyphenolic compounds Chemical class 0.000 claims description 5
- 235000013824 polyphenols Nutrition 0.000 claims description 5
- 235000020748 rosemary extract Nutrition 0.000 claims description 5
- 238000007789 sealing Methods 0.000 claims description 5
- 239000002893 slag Substances 0.000 claims description 5
- 239000007921 spray Substances 0.000 claims description 5
- 229910001220 stainless steel Inorganic materials 0.000 claims description 5
- 239000010935 stainless steel Substances 0.000 claims description 5
- 239000004474 valine Substances 0.000 claims description 5
- 239000003205 fragrance Substances 0.000 abstract description 6
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 abstract description 4
- 239000011575 calcium Substances 0.000 abstract description 4
- 229910052791 calcium Inorganic materials 0.000 abstract description 4
- 230000000050 nutritive effect Effects 0.000 abstract description 3
- 102000004169 proteins and genes Human genes 0.000 abstract description 3
- 108090000623 proteins and genes Proteins 0.000 abstract description 3
- TVLJNOHNHRBUBC-SIHAWKHTSA-J [Na+].[Na+].[Na+].[Na+].O[C@@H]1[C@@H](COP([O-])([O-])=O)O[C@H]([C@@H]1O)n1cnc2c(O)ncnc12.Nc1nc2n(cnc2c(=O)[nH]1)[C@@H]1O[C@H](COP([O-])([O-])=O)[C@@H](O)[C@H]1O Chemical compound [Na+].[Na+].[Na+].[Na+].O[C@@H]1[C@@H](COP([O-])([O-])=O)O[C@H]([C@@H]1O)n1cnc2c(O)ncnc12.Nc1nc2n(cnc2c(=O)[nH]1)[C@@H]1O[C@H](COP([O-])([O-])=O)[C@@H](O)[C@H]1O TVLJNOHNHRBUBC-SIHAWKHTSA-J 0.000 abstract 2
- 235000013888 disodium 5'-ribonucleotide Nutrition 0.000 abstract 2
- 239000004193 disodium 5'-ribonucleotide Substances 0.000 abstract 2
- -1 small-molecule amino acid Chemical class 0.000 abstract 2
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 abstract 1
- 238000004364 calculation method Methods 0.000 abstract 1
- 235000002639 sodium chloride Nutrition 0.000 abstract 1
- 239000011780 sodium chloride Substances 0.000 abstract 1
- 239000001509 sodium citrate Substances 0.000 abstract 1
- NLJMYIDDQXHKNR-UHFFFAOYSA-K sodium citrate Chemical compound O.O.[Na+].[Na+].[Na+].[O-]C(=O)CC(O)(CC([O-])=O)C([O-])=O NLJMYIDDQXHKNR-UHFFFAOYSA-K 0.000 abstract 1
- 238000000034 method Methods 0.000 description 8
- 230000008569 process Effects 0.000 description 8
- 230000007613 environmental effect Effects 0.000 description 4
- 238000002474 experimental method Methods 0.000 description 4
- 235000019634 flavors Nutrition 0.000 description 4
- 230000007774 longterm Effects 0.000 description 4
- 238000005520 cutting process Methods 0.000 description 3
- 230000000249 desinfective effect Effects 0.000 description 3
- 230000006872 improvement Effects 0.000 description 2
- 235000018102 proteins Nutrition 0.000 description 2
- 239000000654 additive Substances 0.000 description 1
- 230000000996 additive effect Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 230000008034 disappearance Effects 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- 230000000813 microbial effect Effects 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 235000021049 nutrient content Nutrition 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 235000013599 spices Nutrition 0.000 description 1
Classifications
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23L—FOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
- A23L27/00—Spices; Flavouring agents or condiments; Artificial sweetening agents; Table salts; Dietetic salt substitutes; Preparation or treatment thereof
- A23L27/20—Synthetic spices, flavouring agents or condiments
- A23L27/21—Synthetic spices, flavouring agents or condiments containing amino acids
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23L—FOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
- A23L27/00—Spices; Flavouring agents or condiments; Artificial sweetening agents; Table salts; Dietetic salt substitutes; Preparation or treatment thereof
- A23L27/20—Synthetic spices, flavouring agents or condiments
- A23L27/26—Meat flavours
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23V—INDEXING SCHEME RELATING TO FOODS, FOODSTUFFS OR NON-ALCOHOLIC BEVERAGES AND LACTIC OR PROPIONIC ACID BACTERIA USED IN FOODSTUFFS OR FOOD PREPARATION
- A23V2002/00—Food compositions, function of food ingredients or processes for food or foodstuffs
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Health & Medical Sciences (AREA)
- Nutrition Science (AREA)
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Food Science & Technology (AREA)
- Polymers & Plastics (AREA)
- Proteomics, Peptides & Aminoacids (AREA)
- Coloring Foods And Improving Nutritive Qualities (AREA)
- Meat, Egg Or Seafood Products (AREA)
Abstract
The invention discloses chicken powder and an automatic production technology thereof. The chicken powder is prepared from the following raw materials by mass percent: 90-92% of chicken raw material, 0.03-0.05% of an antioxidant, 0.02-0.03% of sodium citrate, 1-2% of table salt, 0.5-0.7% of guanylic acid, 3-4% of edible glucose, 0.5-1% of disodium 5'-ribonucleotide, 1-2% of small-molecule amino acid and 1-2% of lecithin. According to the chicken powder prepared by the invention, the content of the chicken raw material reaches about 90%, and the chicken raw material is matched with the auxiliary materials such as guanylic acid, disodium 5'-ribonucleotide, small-molecule amino acid, lecithin, calcium and the like, so that the nutritive value of the product is greatly improved; the prepared chicken powder is rich in fresh fragrance, thus being very good in mouth feel; the prepared chicken powder is very high in contents of protein and calcium, thus having very high marketing values; furthermore, the automatic production technology of the chicken powder is improved, and especially, accurate calculation and yield control are carried out in all production processes, so that the safety of the production line is effectively improved; after the automatic production technology is used, the chicken powder can be continuously produced, the production is uninterrupted, the utilization rate of production equipment can be improved, and intelligence and automation of the production line can be realized; the production cost of products can be lowered, and the market competitiveness of the products can be improved.
Description
Technical field
The present invention relates to food processing field technology, refer in particular to a kind of chicken powder and automatic production process thereof.
Background technology
On existing market, so-called chicken powder is compound chicken powder, it is for raw material with the powder of edible salt, monosodium glutamate, chicken, chicken bone or its concentrated extract, monosodium glutamate and other auxiliary materials, add or do not add the fumet such as spice or flavorant, through being mixed and processed, there is the strong fragrance of chicken and the compound seasoner of delicious flavour.This series products obtains liking of consumer in recent years, but in order to the current compound chicken powder on the market of the freshness improving product, the additive such as monosodium glutamate, edible salt of higher proportion is contained in capital, make its local flavor that should exist strong not and abundant, mouthfeel is fineless and smooth, and existing automatic production process exists complex process and cannot continuous seepage, and easily cause microbial contamination, easily cause flavor components to lose, cause chicken powder fragrance not strong.
Summary of the invention
In view of this, the present invention is directed to the disappearance of prior art existence, its main purpose is to provide a kind of delicious, chicken powder that nutrient content is high and automatic production process thereof, and its automatic production process is simple, production efficiency is high; By the chicken powder of this explained hereafter, there is the strong fragrance of chicken and delicious taste.
For achieving the above object, the present invention adopts following technical scheme:
A kind of chicken powder, by percent mass hundred, includes:
Chicken raw material 90 ~ 92%
Antioxidant 0.03 ~ 0.05%
Natrium citricum 0.02 ~ 0.03%
Salt 1 ~ 2%
Guanylic acid 0.5 ~ 0.7%
Edible glucose 3 ~ 4%
5 '-flavour nucleotide disodium 0.5 ~ 1%
Small molecular amino acid/11 .1 ~ 2.5%
Lecithin 1 ~ 2%.
An automatic production process for chicken powder, includes following steps:
A, first chicken raw material is put into dicer and carry out stripping and slicing, chicken raw material is cut into the chicken nugget containing chicken bone and muscle of 2.5 ~ 4 centimetres of sizes; The stripping and slicing speed of this dicer is 1500-2000kg/h;
B, then the chicken nugget cut is put into cooker and carry out boiling, this cooker inner liner pressure is 0.1 ~ 0.3MPa, and chuck pressure is less than 0.4MPa, this cooker peripheral hardware heat-insulation layer, in establish agitating device; Adopt steam to be warmed to 121-128 DEG C, be incubated 90 minutes, and stir;
C, then well-done material is sent in bone mud mill grind, make well-done material form slurry by grinding; This bone mud mill includes three, be divided into thick, essence, thin three grades grind; Grinding rate is 1 ton/hour ~ 3 tons/hour;
D, slurry then after the grinding of bone mud mill adopt that lift is 24m, power is that the sanitary pump of 2.2Kw pumps in rotor-vibrating screen and carries out Separation of Solid and Liquid;
E, residue after rotor-vibrating screen Separation of Solid and Liquid adopt that dress slag ladle loads, colloidal solution enters in allotment sterilization tank and carries out sterilization treatment; Meanwhile, in this allotment sterilization tank, add antioxidant, monosodium glutamate, natrium citricum, salt, guanylic acid, edible glucose, 5 '-flavour nucleotide disodium, Small molecular amino acid, lecithin and calcareous; This allotment sterilization tank is pressure vessel, is with hollow heating jacket ,-0.1 ~ 0.1MPa in tank, and chuck is less than 0.25MPa, and top is provided with the band anchor formula scraper mixing device of CIP cleaning head and variable ratio frequency changer speed governing; Described anchor formula scraper plate stretches in allotment sterilization tank and is uniformly mixed the compound in tank and scrapes in the colloid mill of next step by the compound in allotment sterilization tank;
Above-mentioned compound grinds and is mixed further with the colloidal solution obtained by Step d by various auxiliary material by f, employing colloid mill further; Grinding rate is 1 ton/hour ~ 3 tons/hour;
G, pump in compound temporary storage tank by stainless steel impeller pump by colloid mill, be dispensed in each high pressure homogenizer through the compound that colloid mill is ground by automatically distributing control system in compound temporary storage tank, described high pressure homogenizer is at least 2; The volume of described high pressure homogenizer is 4000L ~ 8000L; The shearing dispersion and emulsion time of described high pressure homogenizer to compound is 0.5 ~ 1 hour;
H, send in finished product temporary storage tank store carrying out shearing the finished emulsion after dispersion and emulsion under high pressure conditions;
I, finished emulsion sent in dry spray tower by impeller pump and carries out drying, generate powdered granule;
J, dried particle sieve through vibratory sieve as required;
K, packaging, sealing, packing.
Described Small molecular amino acid relative molecular mass is less than 500 dalton; Its free amino acid is formed and ratio is: aspartic acid 11%, glutamic acid 28%, lysine 3.8%, arginine 15%, glycine 22%, alanine 1.2%, valine 7%, serine 3%, threonine 5%, trorsine 14 %.
This antioxidant is Rosmarinus officinalis extract, VE, Tea Polyphenols and in mass ratio 1:2:2 mix; Prove through long-term experiment, these antioxidants have good antioxidant effect in boiling, defibrination operation, and natural environmental-protective; Make this chicken powder and produce safety and environmental protection more.
The present invention compared with prior art has obvious advantage and beneficial effect, chicken powder prepared by the present invention, its chicken raw material reaches about 90%, and coordinate guanylic acid, 5 '-flavour nucleotide disodium, Small molecular amino acid, lecithin and the auxiliary material such as calcareous greatly to improve the nutritive value of product, the obtained fresh fragrance of chicken powder is extremely dense, excellent taste; Adopt the chicken powder of this explained hereafter, it adopts whole chicken as raw material, has not only been rich in protein, and because chicken bone is after PROCESS FOR TREATMENT of the present invention, makes calcium content in obtained chicken powder high, have market popularization value; Simultaneously, by the improvement of present invention process, particularly the precision of each production link calculates and output control, the security of effective raising production line, the continuous seepage of chicken powder can be realized simultaneously, can produce incessantly, improve the utilization rate of production equipment, realize intellectuality and the automation of production line; Reduce the production cost of product, improve the competitiveness of product in market.
Detailed description of the invention
Embodiment 1
A kind of chicken powder, by percent mass hundred, includes:
Chicken raw material 89.95%
Antioxidant 0.03%
Natrium citricum 0.02%
Salt 2%
Guanylic acid 0.5%
Edible glucose 4%
5 '-flavour nucleotide disodium 0.5%
Small molecular amino acid 2%
Lecithin 1%.
This antioxidant is Rosmarinus officinalis extract, VE, Tea Polyphenols and in mass ratio 1:2:2 mix; Prove through long-term experiment, these antioxidants have good antioxidant effect in boiling, defibrination operation, and natural environmental-protective; Make this chicken powder and produce safety and environmental protection more.
The automatic production process of this chicken powder, includes following steps:
A, first chicken raw material is put into dicer and carry out stripping and slicing, chicken raw material is cut into the chicken nugget containing chicken bone and muscle of 2.5 ~ 4 centimetres of sizes; Because dicer cannot ensure that in the process of cutting every block chicken raw material is in the same size, the chicken raw material size that therefore the present invention adopts is mainly 2.5 ~ 4 centimetres; The stripping and slicing speed of this dicer is 1500kg/h;
B, then the chicken nugget cut is put into cooker and carry out boiling, this cooker inner liner pressure remains between 0.1 ~ 0.3MPa, and chuck pressure is less than 0.4MPa, this cooker peripheral hardware heat-insulation layer, in establish agitating device; Adopt steam to be warmed between 121 ~ 128 DEG C to float, be incubated 90 minutes, and stir;
C, then well-done material is sent in bone mud mill grind, make well-done material form slurry by grinding; This bone mud mill includes three, be divided into thick, essence, thin three grades grind; Grinding rate is 2 tons/hour;
D, slurry then after the grinding of bone mud mill adopt that lift is 24m, power is that the sanitary pump of 2.2Kw pumps in rotor-vibrating screen and carries out Separation of Solid and Liquid;
E, residue after rotor-vibrating screen Separation of Solid and Liquid adopt dress slag ladle to load, and the colloidal solution after Separation of Solid and Liquid enters in allotment sterilization tank and carries out sterilization treatment; Meanwhile, in this allotment sterilization tank, add antioxidant, monosodium glutamate, natrium citricum, salt, guanylic acid, edible glucose, 5 '-flavour nucleotide disodium, Small molecular amino acid, lecithin and calcareous; This allotment sterilization tank is pressure vessel, is with hollow heating jacket, and keep between-0.1 ~ 0.1MPa in tank, chuck is less than 0.25MPa, and this allotment sterilization tank top is provided with the band anchor formula scraper mixing device of CIP cleaning head and variable ratio frequency changer speed governing; Described anchor formula scraper plate stretches in allotment sterilization tank and is uniformly mixed the compound in tank and scrapes in the colloid mill of next step by the compound in allotment sterilization tank; In this allotment sterilization tank, carry out the allotment of a mixture ratio and disinfecting action is carried out to it; The ratio of each component of this mixture is: chicken raw material 89.95%, antioxidant 0.03%, natrium citricum 0.02%, salt 2%, guanylic acid 0.5%, edible glucose 4%, 5 '-flavour nucleotide disodium 0.5%, Small molecular amino acid 2%, lecithin 1%;
Above-mentioned compound grinds and is mixed further with the colloidal solution obtained by Step d by various auxiliary material by f, employing colloid mill further; Grinding rate is 2 tons/hour;
G, pump in compound temporary storage tank by stainless steel impeller pump by colloid mill, be dispensed in each high pressure homogenizer through the compound that colloid mill is ground by automatically distributing control system in compound temporary storage tank, described high pressure homogenizer is 2; The volume of described high pressure homogenizer is 4000LL; The shearing dispersion and emulsion time of described high pressure homogenizer to compound is 0.5 hour;
H, send in finished product temporary storage tank store carrying out shearing the finished emulsion after dispersion and emulsion under high pressure conditions;
I, finished emulsion sent in dry spray tower by impeller pump and carries out drying, generate powdered granule;
J, dried particle sieve through vibratory sieve as required; The mesh size size of this vibratory sieve is 80 orders;
K, packaging, sealing, packing.
Described Small molecular amino acid relative molecular mass is less than 500 dalton; Its free amino acid is formed and ratio is: aspartic acid 11%, glutamic acid 28%, lysine 3.8%, arginine 15%, glycine 22%, alanine 1.2%, valine 7%, serine 3%, threonine 5%, trorsine 14 %.
Embodiment 2
A kind of chicken powder, by percent mass hundred, includes:
Chicken raw material 91.23%
Antioxidant 0.04%
Natrium citricum 0.03%
Salt 1%
Guanylic acid 0.7%
Edible glucose 3%
5 '-flavour nucleotide disodium 1%
Small molecular amino acid/11 %
Lecithin 2%.
This antioxidant is Rosmarinus officinalis extract, VE, Tea Polyphenols and in mass ratio 1:2:2 mix; Prove through long-term experiment, these antioxidants have good antioxidant effect in boiling, defibrination operation, and natural environmental-protective; Make this chicken powder and produce safety and environmental protection more.
The automatic production process of this chicken powder, includes following steps:
A, first chicken raw material is put into dicer and carry out stripping and slicing, chicken raw material is cut into the chicken nugget containing chicken bone and muscle of 2.5 ~ 4 centimetres of sizes; Because dicer cannot ensure that in the process of cutting every block chicken raw material is in the same size, the chicken raw material size that therefore the present invention adopts is mainly 2.5 ~ 4 centimetres; The stripping and slicing speed of this dicer is 1800kg/h;
B, then the chicken nugget cut is put into cooker and carry out boiling, this cooker inner liner pressure remains between 0.1 ~ 0.3MPa, and chuck pressure is less than 0.4MPa, this cooker peripheral hardware heat-insulation layer, in establish agitating device; Adopt steam to be warmed between 121 ~ 128 DEG C to float, be incubated 90 minutes, and stir;
C, then well-done material is sent in bone mud mill grind, make well-done material form slurry by grinding; This bone mud mill includes three, be divided into thick, essence, thin three grades grind; Grinding rate is 2.5 tons/hour;
D, slurry then after the grinding of bone mud mill adopt that lift is 24m, power is that the sanitary pump of 2.2Kw pumps in rotor-vibrating screen and carries out Separation of Solid and Liquid;
E, residue after rotor-vibrating screen Separation of Solid and Liquid adopt dress slag ladle to load, and the colloidal solution after Separation of Solid and Liquid enters in allotment sterilization tank and carries out sterilization treatment; Meanwhile, in this allotment sterilization tank, add antioxidant, monosodium glutamate, natrium citricum, salt, guanylic acid, edible glucose, 5 '-flavour nucleotide disodium, Small molecular amino acid, lecithin and calcareous; This allotment sterilization tank is pressure vessel, is with hollow heating jacket,-0.1 ~ 0.1MPa is kept in tank, chuck is less than 0.25MPa, and this allotment sterilization tank top is provided with CIP cleaning head for cleaning this allotment sterilization tank and for stirring or the band anchor formula scraper mixing device of variable ratio frequency changer speed governing of scraper; Described anchor formula scraper plate stretches in allotment sterilization tank and is uniformly mixed the compound in tank and scrapes in the colloid mill of next step by the compound in allotment sterilization tank; In this allotment sterilization tank, carry out the allotment of a mixture ratio and disinfecting action is carried out to it; The ratio of each component of this mixture is: chicken raw material 91.23%, antioxidant 0.04%, natrium citricum 0.03%, salt 1%, guanylic acid 0.7%, edible glucose 3%, 5 '-flavour nucleotide disodium 1%, Small molecular amino acid/11 %, lecithin 2%;
Above-mentioned compound grinds and is mixed further with the colloidal solution obtained by Step d by various auxiliary material by f, employing colloid mill further; Grinding rate is 2.5 tons/hour;
G, pump in compound temporary storage tank by stainless steel impeller pump by colloid mill, be dispensed in each high pressure homogenizer through the compound that colloid mill is ground by automatically distributing control system in compound temporary storage tank, described high pressure homogenizer is 2; The volume of described high pressure homogenizer is 6000LL; The shearing dispersion and emulsion time of described high pressure homogenizer to compound is 0.8 hour;
H, send in finished product temporary storage tank store carrying out shearing the finished emulsion after dispersion and emulsion under high pressure conditions;
I, finished emulsion sent in dry spray tower by impeller pump and carries out drying, generate powdered granule;
J, dried particle sieve through vibratory sieve as required; The mesh size size of this vibratory sieve is 80 orders;
K, packaging, sealing, packing.
Described Small molecular amino acid relative molecular mass is less than 500 dalton; Its free amino acid is formed and ratio is: aspartic acid 11%, glutamic acid 28%, lysine 3.8%, arginine 15%, glycine 22%, alanine 1.2%, valine 7%, serine 3%, threonine 5%, trorsine 14 %.
Embodiment 3
A kind of chicken powder, by percent mass hundred, includes:
Chicken raw material 90.51%
Antioxidant 0.05%
Natrium citricum 0.03%
Salt 1.5%
Guanylic acid 0.6%
Edible glucose 3.5%
5 '-flavour nucleotide disodium 0.8%
Small molecular amino acid/11 .5%
Lecithin 1.5%.
This antioxidant is Rosmarinus officinalis extract, VE, Tea Polyphenols and in mass ratio 1:2:2 mix; Prove through long-term experiment, these antioxidants have good antioxidant effect in boiling, defibrination operation, and natural environmental-protective; Make this chicken powder and produce safety and environmental protection more.
The automatic production process of this chicken powder, includes following steps:
A, first chicken raw material is put into dicer and carry out stripping and slicing, chicken raw material is cut into the chicken nugget containing chicken bone and muscle of 2.5 ~ 4 centimetres of sizes; Because dicer cannot ensure that in the process of cutting every block chicken raw material is in the same size, the chicken raw material size that therefore the present invention adopts is mainly 2.5 ~ 4 centimetres; The stripping and slicing speed of this dicer is 2000kg/h;
B, then the chicken nugget cut is put into cooker and carry out boiling, this cooker inner liner pressure remains between 0.1 ~ 0.3MPa, and chuck pressure is less than 0.4MPa, this cooker peripheral hardware heat-insulation layer, in establish agitating device; Adopt steam to be warmed between 121 ~ 128 DEG C to float, be incubated 90 minutes, and stir;
C, then well-done material is sent in bone mud mill grind, make well-done material form slurry by grinding; This bone mud mill includes three, be divided into thick, essence, thin three grades grind; Grinding rate is 3 tons/hour;
D, slurry then after the grinding of bone mud mill adopt that lift is 24m, power is that the sanitary pump of 2.2Kw pumps in rotor-vibrating screen and carries out Separation of Solid and Liquid;
E, residue after rotor-vibrating screen Separation of Solid and Liquid adopt dress slag ladle to load, and the colloidal solution after Separation of Solid and Liquid enters in allotment sterilization tank and carries out sterilization treatment; Meanwhile, in this allotment sterilization tank, add antioxidant, monosodium glutamate, natrium citricum, salt, guanylic acid, edible glucose, 5 '-flavour nucleotide disodium, Small molecular amino acid, lecithin and calcareous; This allotment sterilization tank is pressure vessel, is with hollow heating jacket, and remain on-0.1 ~ 0.1MPa in tank, chuck is less than 0.25MPa, and top is provided with the band anchor formula scraper mixing device of CIP cleaning head and variable ratio frequency changer speed governing; Described anchor formula scraper plate stretches in allotment sterilization tank and is uniformly mixed the compound in tank and scrapes in the colloid mill of next step by the compound in allotment sterilization tank; In this allotment sterilization tank, carry out the allotment of a mixture ratio and disinfecting action is carried out to it; The ratio of each component of this mixture is: chicken raw material 90.51%, antioxidant 0.05%, natrium citricum 0.03%, salt 1.5%, guanylic acid 0.6%, edible glucose 3.5%, 5 '-flavour nucleotide disodium 0.8%, Small molecular amino acid/11 .5%, lecithin 1.5%;
Above-mentioned compound grinds and is mixed further with the colloidal solution obtained by Step d by various auxiliary material by f, employing colloid mill further; Grinding rate is 3 tons/hour;
G, pump in compound temporary storage tank by stainless steel impeller pump by colloid mill, be dispensed in each high pressure homogenizer through the compound that colloid mill is ground by automatically distributing control system in compound temporary storage tank, described high pressure homogenizer is 2; The volume of described high pressure homogenizer is 8000L; The shearing dispersion and emulsion time of described high pressure homogenizer to compound is 1 hour;
H, send in finished product temporary storage tank store carrying out shearing the finished emulsion after dispersion and emulsion under high pressure conditions;
I, finished emulsion sent in dry spray tower by impeller pump and carries out drying, generate powdered granule;
J, dried particle sieve through vibratory sieve as required; The mesh size size of this vibratory sieve is 80 orders;
K, packaging, sealing, packing.
Described Small molecular amino acid relative molecular mass is less than 500 dalton; Its free amino acid is formed and ratio is: aspartic acid 11%, glutamic acid 28%, lysine 3.8%, arginine 15%, glycine 22%, alanine 1.2%, valine 7%, serine 3%, threonine 5%, trorsine 14 %.
Of the present inventionly to focus on: the chicken powder prepared by the present invention, its chicken raw material reaches about 90%, and coordinating guanylic acid, 5 '-flavour nucleotide disodium, Small molecular amino acid, lecithin and the auxiliary material such as calcareous greatly to improve the nutritive value of product, the obtained fresh fragrance of chicken powder is extremely dense, excellent taste; Adopt the chicken powder of this explained hereafter, it adopts whole chicken as raw material, has not only been rich in protein, and because chicken bone is after PROCESS FOR TREATMENT of the present invention, makes calcium content in obtained chicken powder high, have market popularization value; Simultaneously, by the improvement of present invention process, particularly the precision of each production link calculates and output control, the security of effective raising production line, the continuous seepage of chicken powder can be realized simultaneously, can produce incessantly, improve the utilization rate of production equipment, realize intellectuality and the automation of production line; Reduce the production cost of product, improve the competitiveness of product in market.
The above, it is only preferred embodiment of the present invention, not technical scope of the present invention is imposed any restrictions, thus every according to technical spirit of the present invention to any trickle amendment made for any of the above embodiments, equivalent variations and modification, all still belong in the scope of technical solution of the present invention.
Claims (4)
1. a chicken powder, is characterized in that: by percent mass hundred, include:
Chicken raw material 90 ~ 92%
Antioxidant 0.03 ~ 0.05%
Natrium citricum 0.02 ~ 0.03%
Salt 1 ~ 2%
Guanylic acid 0.5 ~ 0.7%
Edible glucose 3 ~ 4%
5 '-flavour nucleotide disodium 0.5 ~ 1%
Small molecular amino acid/11 .1 ~ 2.5%
Lecithin 1 ~ 2%.
2. an automatic production process for chicken powder, is characterized in that: include following steps:
A, first chicken raw material is put into dicer and carry out stripping and slicing, chicken raw material is cut into the chicken nugget containing chicken bone and muscle of 2.5 ~ 4 centimetres of sizes; The stripping and slicing speed of this dicer is 1500-2000kg/h;
B, then the chicken nugget cut is put into cooker and carry out boiling, this cooker inner liner pressure is 0.1 ~ 0.3MPa, and chuck pressure is less than 0.4MPa, this cooker peripheral hardware heat-insulation layer, in establish agitating device; Adopt steam to be warmed to 121-128 DEG C, be incubated 90 minutes, and stir;
C, then well-done material is sent in bone mud mill grind, make well-done material form slurry by grinding; This bone mud mill includes three, be divided into thick, essence, thin three grades grind; Grinding rate is 1 ton/hour ~ 3 tons/hour;
D, slurry then after the grinding of bone mud mill adopt that lift is 24m, power is that the sanitary pump of 2.2Kw pumps in rotor-vibrating screen and carries out Separation of Solid and Liquid;
E, residue after rotor-vibrating screen Separation of Solid and Liquid adopt that dress slag ladle loads, colloidal solution enters in allotment sterilization tank and carries out sterilization treatment; Meanwhile, in this allotment sterilization tank, add antioxidant, monosodium glutamate, natrium citricum, salt, guanylic acid, edible glucose, 5 '-flavour nucleotide disodium, Small molecular amino acid, lecithin and calcareous; This allotment sterilization tank is pressure vessel, is with hollow heating jacket ,-0.1 ~ 0.1MPa in tank, and chuck is less than 0.25MPa, and top is provided with the band anchor formula scraper mixing device of CIP cleaning head and variable ratio frequency changer speed governing; Described anchor formula scraper plate stretches in allotment sterilization tank and is uniformly mixed the compound in tank and scrapes in the colloid mill of next step by the compound in allotment sterilization tank;
Above-mentioned compound grinds and is mixed further with the colloidal solution obtained by Step d by various auxiliary material by f, employing colloid mill further; Grinding rate is 1 ton/hour ~ 3 tons/hour;
G, pump in compound temporary storage tank by stainless steel impeller pump by colloid mill, be dispensed in each high pressure homogenizer through the compound that colloid mill is ground by automatically distributing control system in compound temporary storage tank, described high pressure homogenizer is at least 2; The volume of described high pressure homogenizer is 4000L ~ 8000L; The shearing dispersion and emulsion time of described high pressure homogenizer to compound is 0.5 ~ 1 hour;
H, send in finished product temporary storage tank store carrying out shearing the finished emulsion after dispersion and emulsion under high pressure conditions;
I, finished emulsion sent in dry spray tower by impeller pump and carries out drying, generate powdered granule;
J, dried particle sieve through vibratory sieve as required;
K, packaging, sealing, packing.
3. a kind of chicken powder automatic production process according to claim 2, is characterized in that: described Small molecular amino acid relative molecular mass is less than 500 dalton; Its free amino acid is formed and ratio is: aspartic acid 11%, glutamic acid 28%, lysine 3.8%, arginine 15%, glycine 22%, alanine 1.2%, valine 7%, serine 3%, threonine 5%, trorsine 14 %.
4. a kind of chicken powder according to claim 1, is characterized in that: described antioxidant is Rosmarinus officinalis extract, VE, Tea Polyphenols and in mass ratio 1:2:2 mix.
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN106473082A (en) * | 2016-10-19 | 2017-03-08 | 湖南省嘉品嘉味生物科技有限公司 | A kind of pure chicken cream and preparation method thereof |
| CN109674004A (en) * | 2019-03-04 | 2019-04-26 | 江苏特味浓生物技术开发有限公司 | A kind of production method of pure flesh of fish powder |
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| CN102726696A (en) * | 2011-04-08 | 2012-10-17 | 成坚 | A high-protein pure chicken powder and production technology for the same |
| CN102742720A (en) * | 2012-07-27 | 2012-10-24 | 江苏海企长城股份有限公司 | Method for producing seasoning chicken bone soup, chicken meal for pets and the like by comprehensively utilizing chicken skeletons |
| CN104041788A (en) * | 2014-06-25 | 2014-09-17 | 江南大学 | Preparation method for compound chicken powder rich in flavor amino acid with high ratio and small molecular weight |
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| CN102726696A (en) * | 2011-04-08 | 2012-10-17 | 成坚 | A high-protein pure chicken powder and production technology for the same |
| CN102742720A (en) * | 2012-07-27 | 2012-10-24 | 江苏海企长城股份有限公司 | Method for producing seasoning chicken bone soup, chicken meal for pets and the like by comprehensively utilizing chicken skeletons |
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| CN106473082A (en) * | 2016-10-19 | 2017-03-08 | 湖南省嘉品嘉味生物科技有限公司 | A kind of pure chicken cream and preparation method thereof |
| CN109674004A (en) * | 2019-03-04 | 2019-04-26 | 江苏特味浓生物技术开发有限公司 | A kind of production method of pure flesh of fish powder |
| CN109674004B (en) * | 2019-03-04 | 2021-10-22 | 江苏特味浓食品股份有限公司 | Preparation method of pure fish soup powder |
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Effective date of registration: 20201217 Address after: Building e, No.3, Xingye Road, Conghua Mingzhu Industrial Park, Guangzhou, Guangdong 510931 Patentee after: GUANGZHOU HUAQI BIOLOGICAL TECHNOLOGY Co.,Ltd. Address before: Room 103, 1 / F, block 3, jiafuyuan, Hengkeng Jiahu villa, Liaobu Town, Dongguan City, Guangdong Province 523000 Patentee before: Wei Zhihua |