CN105124516A - Astaxanthin containing penaeus orientalis juice production method - Google Patents
Astaxanthin containing penaeus orientalis juice production method Download PDFInfo
- Publication number
- CN105124516A CN105124516A CN201510571551.8A CN201510571551A CN105124516A CN 105124516 A CN105124516 A CN 105124516A CN 201510571551 A CN201510571551 A CN 201510571551A CN 105124516 A CN105124516 A CN 105124516A
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- CN
- China
- Prior art keywords
- citric acid
- acid
- prawn
- hydrolysis
- prawn head
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
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- JEBFVOLFMLUKLF-IFPLVEIFSA-N Astaxanthin Natural products CC(=C/C=C/C(=C/C=C/C1=C(C)C(=O)C(O)CC1(C)C)/C)C=CC=C(/C)C=CC=C(/C)C=CC2=C(C)C(=O)C(O)CC2(C)C JEBFVOLFMLUKLF-IFPLVEIFSA-N 0.000 title claims abstract description 30
- MQZIGYBFDRPAKN-ZWAPEEGVSA-N astaxanthin Chemical compound C([C@H](O)C(=O)C=1C)C(C)(C)C=1/C=C/C(/C)=C/C=C/C(/C)=C/C=C/C=C(C)C=CC=C(C)C=CC1=C(C)C(=O)[C@@H](O)CC1(C)C MQZIGYBFDRPAKN-ZWAPEEGVSA-N 0.000 title claims abstract description 30
- 239000001168 astaxanthin Substances 0.000 title claims abstract description 30
- 229940022405 astaxanthin Drugs 0.000 title claims abstract description 30
- 235000013793 astaxanthin Nutrition 0.000 title claims abstract description 30
- 235000011389 fruit/vegetable juice Nutrition 0.000 title claims abstract description 26
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 20
- 241001223363 Fenneropenaeus orientalis Species 0.000 title abstract 5
- KRKNYBCHXYNGOX-UHFFFAOYSA-N citric acid Chemical compound OC(=O)CC(O)(C(O)=O)CC(O)=O KRKNYBCHXYNGOX-UHFFFAOYSA-N 0.000 claims abstract description 376
- 239000002253 acid Substances 0.000 claims abstract description 105
- 238000006460 hydrolysis reaction Methods 0.000 claims abstract description 91
- 230000007062 hydrolysis Effects 0.000 claims abstract description 77
- 239000000047 product Substances 0.000 claims abstract description 67
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 claims abstract description 62
- 239000002994 raw material Substances 0.000 claims abstract description 50
- 239000007788 liquid Substances 0.000 claims abstract description 32
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- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims abstract description 11
- CZMRCDWAGMRECN-UGDNZRGBSA-N Sucrose Chemical compound O[C@H]1[C@H](O)[C@@H](CO)O[C@@]1(CO)O[C@@H]1[C@H](O)[C@@H](O)[C@H](O)[C@@H](CO)O1 CZMRCDWAGMRECN-UGDNZRGBSA-N 0.000 claims abstract description 11
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- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 54
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- DSOWAKKSGYUMTF-GZOLSCHFSA-M sodium;(1e)-1-(6-methyl-2,4-dioxopyran-3-ylidene)ethanolate Chemical compound [Na+].C\C([O-])=C1/C(=O)OC(C)=CC1=O DSOWAKKSGYUMTF-GZOLSCHFSA-M 0.000 claims description 4
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- CYDMQBQPVICBEU-XRNKAMNCSA-N chlortetracycline Chemical compound C1=CC(Cl)=C2[C@](O)(C)[C@H]3C[C@H]4[C@H](N(C)C)C(O)=C(C(N)=O)C(=O)[C@@]4(O)C(O)=C3C(=O)C2=C1O CYDMQBQPVICBEU-XRNKAMNCSA-N 0.000 description 1
- 229960004475 chlortetracycline Drugs 0.000 description 1
- 235000019365 chlortetracycline Nutrition 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- KWGRBVOPPLSCSI-UHFFFAOYSA-N d-ephedrine Natural products CNC(C)C(O)C1=CC=CC=C1 KWGRBVOPPLSCSI-UHFFFAOYSA-N 0.000 description 1
- 238000009795 derivation Methods 0.000 description 1
- 238000000586 desensitisation Methods 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 230000018109 developmental process Effects 0.000 description 1
- 235000005911 diet Nutrition 0.000 description 1
- 230000000378 dietary effect Effects 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 229960002179 ephedrine Drugs 0.000 description 1
- 238000000855 fermentation Methods 0.000 description 1
- 230000004151 fermentation Effects 0.000 description 1
- 239000003337 fertilizer Substances 0.000 description 1
- 102000034240 fibrous proteins Human genes 0.000 description 1
- 108091005899 fibrous proteins Proteins 0.000 description 1
- 235000013373 food additive Nutrition 0.000 description 1
- 239000002778 food additive Substances 0.000 description 1
- 235000019249 food preservative Nutrition 0.000 description 1
- 239000005452 food preservative Substances 0.000 description 1
- 235000019253 formic acid Nutrition 0.000 description 1
- 210000004051 gastric juice Anatomy 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 239000000174 gluconic acid Substances 0.000 description 1
- 235000012208 gluconic acid Nutrition 0.000 description 1
- 239000003292 glue Substances 0.000 description 1
- 235000011187 glycerol Nutrition 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- XMBWDFGMSWQBCA-UHFFFAOYSA-N hydrogen iodide Chemical compound I XMBWDFGMSWQBCA-UHFFFAOYSA-N 0.000 description 1
- 239000000413 hydrolysate Substances 0.000 description 1
- 230000009610 hypersensitivity Effects 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- ICIWUVCWSCSTAQ-UHFFFAOYSA-M iodate Chemical compound [O-]I(=O)=O ICIWUVCWSCSTAQ-UHFFFAOYSA-M 0.000 description 1
- 210000003734 kidney Anatomy 0.000 description 1
- 239000001630 malic acid Substances 0.000 description 1
- 235000011090 malic acid Nutrition 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 150000007522 mineralic acids Chemical class 0.000 description 1
- NJTGANWAUPEOAX-UHFFFAOYSA-N molport-023-220-454 Chemical compound OCC(O)CO.OCC(O)CO NJTGANWAUPEOAX-UHFFFAOYSA-N 0.000 description 1
- 230000035772 mutation Effects 0.000 description 1
- 229910017604 nitric acid Inorganic materials 0.000 description 1
- 235000016709 nutrition Nutrition 0.000 description 1
- 230000035764 nutrition Effects 0.000 description 1
- 235000008935 nutritious Nutrition 0.000 description 1
- 150000007524 organic acids Chemical class 0.000 description 1
- 235000020636 oyster Nutrition 0.000 description 1
- 229920001184 polypeptide Polymers 0.000 description 1
- 230000005195 poor health Effects 0.000 description 1
- 102000004196 processed proteins & peptides Human genes 0.000 description 1
- 235000019260 propionic acid Nutrition 0.000 description 1
- IUVKMZGDUIUOCP-BTNSXGMBSA-N quinbolone Chemical compound O([C@H]1CC[C@H]2[C@H]3[C@@H]([C@]4(C=CC(=O)C=C4CC3)C)CC[C@@]21C)C1=CCCC1 IUVKMZGDUIUOCP-BTNSXGMBSA-N 0.000 description 1
- 230000035484 reaction time Effects 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 239000004576 sand Substances 0.000 description 1
- 235000015067 sauces Nutrition 0.000 description 1
- 239000013535 sea water Substances 0.000 description 1
- 230000001953 sensory effect Effects 0.000 description 1
- ZNCPFRVNHGOPAG-UHFFFAOYSA-L sodium oxalate Chemical compound [Na+].[Na+].[O-]C(=O)C([O-])=O ZNCPFRVNHGOPAG-UHFFFAOYSA-L 0.000 description 1
- 229940039790 sodium oxalate Drugs 0.000 description 1
- 238000001228 spectrum Methods 0.000 description 1
- 230000002269 spontaneous effect Effects 0.000 description 1
- 230000001954 sterilising effect Effects 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 235000019605 sweet taste sensations Nutrition 0.000 description 1
- 239000011975 tartaric acid Substances 0.000 description 1
- 235000002906 tartaric acid Nutrition 0.000 description 1
- 229960003080 taurine Drugs 0.000 description 1
- 229940063650 terramycin Drugs 0.000 description 1
- 229960002180 tetracycline Drugs 0.000 description 1
- 235000019364 tetracycline Nutrition 0.000 description 1
- 229930101283 tetracycline Natural products 0.000 description 1
- 150000003522 tetracyclines Chemical class 0.000 description 1
- 238000004448 titration Methods 0.000 description 1
- 231100000419 toxicity Toxicity 0.000 description 1
- 230000001988 toxicity Effects 0.000 description 1
Classifications
-
- 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
- Meat, Egg Or Seafood Products (AREA)
Abstract
The present invention uses citric acid to hydrolyze penaeus orientalis heads to produce astaxanthin containing penaeus orientalis juice. The production method solves the utilization problems of a huge number of the penaeus orientalis heads; overcomes all the problems produced by using hydrochloric acid to conduct hydrolysis; solves the protein denaturation problems due to freezing and long storage of aquatic products; and solves the allergic problems that penaeus orientalis proteins cause to parts of human body. The product contains a lot of magnesium which can help prevent hypertension and myocardial infarction, and a large amount of astaxanthin which can effectively reverse aging. The production method originally creates a formula to calculate the use amount of acid; solves the smelly problems of sea (freshwater) aquatic products; uses unique product recipes; deduces the calculation formula of product expected yield; solves the product filtration problem; and solves the product sedimentation problem. The production method comprises the following steps: (1) pretreating raw materials; (2) hydrolyzing; (3) neutralizing; (4) precipitating for 3 to 4 hours; (5) extracting supernatant, adding salt and sucrose according to the recipe of expected yield, and stirring to dissolve; (6) repeatedly filtering all of the liquids through a diatomite filtering machine; (7) blending according to the recipe; (8) ultrafiltrating using microporous membranes; and (9) filling.
Description
Technical field
The present invention relates to the method utilizing prawn head to produce astaxanthin prawn juice, belong to the technical field that sea food seasoning is produced.
Background technology
Prawn mainly originates in the Bohai and Yellow Seas of China, fine and tender taste, and delicious flavour is nutritious, easy to digest, in poor health and need the people taken good care of to be fabulous food after being ill.And containing abundant magnesium, it well can protect cardiovascular system, reduce blood cholesterol level, prevent artery sclerosis, be conducive to preventing hypertension and myocardial infarction.The potent antioxidation of its tool, effectively could reverse aging also containing a large amount of astaxanthin! Also has the element of a large amount of needed by human.
2012 end of the year, China produced prawn about 1,700,000 tons according to statistics, and exported product, based on peeled shrimp, must remove shrimp head.And shrimp head accounts for 30% of whole shrimp, nearly tens0000 tons every year.Shrimp head through we divide terminate an agreement containing 50% meat and 50% shell.Because it is difficult to process, so also do not seen which producer can extract shrimp head meat containing so how rough-and-tumble shell.So resource of high-quality, China does not effectively utilize for a long time, and except being used on a small quantity produce except chitin (removing meat) or fertilizer, major part is thrown away as rubbish.So not only cause the serious waste of resource, and contaminated environment! How scientifically to develop prawn head, improve its economic worth, become current problem demanding prompt solution!
Many people one eat shrimps, and appearance protein allergy reaction in various degree will occur, and major part shows as some position of health (face, leg, arm, even whole body) and plays pimple with pruritis.Common anaphylactogen has pollen, medicine, dirt mite, Shrimp waste food etc.
The production method of existing flavouring is as follows:
1, the traditional processing technology of soy sauce adopts dregs of beans or cereal fermented soy to form, and the production cycle is long, and efficiency is very low.
2, salt marsh spontaneous fermentation taked by shrimp sauce, and the production cycle is long, and efficiency is low, and working condition is poor, grows bacterium in a large number, and salt content is high especially, do not meet contemporary health requirement!
3, concentrated hydrochloric acid hydrolysis method production efficiency is high, and fragrance is good.But it is smelly to there is hydrolysis, serious environment pollution and air! Also may produce carcinogenic trichloropropanol!
4, enzyme hydrolysis method.Reaction time is long, and hydrolysis is not easily complete, and the peptide produced has bad allergic reaction to part human body, and product is difficult to filter.
5, we want the acid hydrolysis adopting other, but acid hydrolysis (comprising hydrochloric acid hydrolysis) method main bugbear is the computational problem by acid amount.Catalytic theory from textbook: hydrolysis constant K=α N δ, α are the catalysic coefficient of acid, and N is molar concentration, and δ becomes positive correlation within the specific limits with hydrolysis temperature T, time t.In other words, hydrolysis effect increases with the increase of the molar concentration N (mol/L) of acid in solution-is directly proportional.
This catalytic theory is defective.When 1. just beginning one's study, we are the same with many people, take for as mentioned above: hydrolysis effect is directly proportional to acid concentration in hydrating solution, using it as a leading indicator.But: in solution, acid concentration not only increases with the increase of sour consumption---and this is conducive to hydrolysis; And increase with the minimizing of amount of water---this does not only increase, and reduces hydrolysis effect on the contrary.Because do not increase by acid amount; Added water is fewer, and the acid concentration of solution is higher, now due to common-ion effect, suppresses mutually, and have impact on hydrogen atom ionization, reduce hydrolysis effect, this illustrates that this theory is defective.In fact; Amount of water is very large to hydrolysis potency due, but solution is too dense or too rarely all can reduce hydrolysis effect.2. this theory could not reflect the sour consumption of hydrolysis and the different nitrogen content of certain class hydrolysate (Pinctada martensii, cristaria plicata, scallop, prawn, various fish ...) relation.3. this theory could not reflect the relation of the sour consumption of hydrolysis and variety classes protein (fish, meat, cartilage, tendon, hair, silk).Therefore, this theory is disabled.
Hydrolysis constant K=α N δ formula accordingly; Present many patents declare or paper when writing acid hydrolysis conditions, usually only write in hydrating solution the molar concentration N being hydrolyzed acid, do not write liquor capacity, how does this know by how many acid amount? this is flicker people!
Summary of the invention
The invention provides a kind of production method of astaxanthin prawn juice.Citric acid hydrolysis is that we create, and is used for being hydrolyzed prawn head and produces " astaxanthin prawn juice ", solves and strips the Utilizing question that peeled shrimp outlet leaves rough-and-tumble prawn head hundreds of thousands ton every year; Overcome and produce problem such as hydrolysis smelly, carcinogenic trichloropropanol and contaminated environment etc. with hydrochloric acid hydrolysis; Add citric acid first and make the freezing protein denaturant stored for a long time of water resistant product, improve recovery rate; Shrimp protein matter is hydrolyzed into amino acid, solves the allergic problem of shrimp protein confrontation part human body; Product contains a large amount of magnesium, and it can reduce blood cholesterol level, is conducive to preventing hypertension and myocardial infarction.Also containing a large amount of astaxanthin, the potent antioxidation of its tool, effectively can reverse aging; The calculating hydrolysis acid amount formula of original creation; Solve the fishy smell problem of sea (light) aquatic products; Use and allow the formula of the strong fresh fragrance of product tool, taste is excellent; Derive the computing formula of product estimated output; Solve a filtration difficult problem for product; Solve a precipitation difficult problem for product.
Technical scheme:
The production method of astaxanthin prawn juice, adopts citric acid hydrolysis prawn head to produce, comprises the steps:
1, pretreatment of raw material
Annual nine, October is important season of Bohai Sea autumn flood shrimping, collects prawn head, sort out wherein foreign material and shrimp head palpus when taking advantage of processing peeled shrimp.Add the citric acid of raw material 2 ~ 4% as the agent of anti-protein freeze denaturation
[A], save backup in fish freezer less than-20 DEG C cryogenic freezings, can recovery rate be improved.Citric acid does not produce Mei La get reaction when pyrohydrolysis, make the product of production have scarlet color.
Darker dark reddish brown will be had, so can not with citric acid as the agent of anti-protein freeze denaturation for production baste.
2, be hydrolyzed
Citric acid C is used in hydrolysis
6h
8o
7192.125, commercially available product is Citric Acid Mono, containing citric acid 91.43%, containing the crystallization water 8.57%.General citric acid purity 98%, 2% impurity, now containing citric acid 89.6%, containing the crystallization water 8.4%, is called lemon acid crystals.
Prawn head according to decomposition, containing protein 9.3%.Containing calcium carbonate 2.25%.
Charging: Σ=M
prawn headwater gaging+the M such as+prawn head
lemon acid crystals.The citric acid added has two parts, and M represents weight, herewith later.
To different hydrolysis devices.
(1) use 5000mL erlenmeyer flask, adopt citric acid, back hydrolysis prawn head
The water of raw material that step 1 obtains and raw material equivalent is added in erlenmeyer flask.The citric acid added has two parts.
1. hydrolyzable moiety.See
[B]middle formula (I-1), selects CC=1.2.。
hydrolysism
citric acid=M
prawn head× this kind of material protein content × CC × 2.1947=M
prawn head× 9.3% × 1.2 × 2.1947=M
prawn head× 0.2449.
2. prawn shell need consume citric acid containing dissolution of calcium carbonate
2C
6H
8O
7+3CaCO
3——→Ca
3(C
6H
5O
7)
2↓+3H
2O+3CO
2↑
384.251300.267498.443
dissolvem
citric acid=(384.251 ÷ 300.267) × M
calcium carbonate, prawn head=(384.251 ÷ 300.267) × M
prawn head× C
calcium carbonate, prawn head
=1.2797 × 2.25% × M
prawn head=M
prawn head× 0.0288 ... (IV).Prawn head is containing calcium carbonate C
calcium carbonate, prawn head=2.25%.
alwaysm
citric acid=
hydrolysism
citric acid+
dissolvem
citric acid=M
prawn head× 0.2449+M
prawn head× 0.0288=M
prawn head× 0.2737,
Use Citric Acid Mono--lemon acid crystals:
alwaysm
lemon acid crystals=
alwaysm
citric acid÷ 0.896=M
prawn head× 0.3055.
The lemon acid crystals Freezing preservation agent of the raw material 3% added should be reduced:
addm
lemon acid crystals=M
prawn head× 3%.
Now actually add lemon acid crystals:
add in factm
lemon acid crystals=
alwaysm
lemon acid crystals-
addm
lemon acid crystals=M
prawn head× 0.3055-M
prawn head× 3%=M
prawn head× 0.2755.
Back hydrolysis 12 ~ 16 hours
(2) use reactor hydrolysis, adopt citric acid, hydrolysis prawn head
Add the water of raw material that step 1 obtains and raw material equivalent in a kettle..The citric acid added equally has two parts:
1. hydrolyzable moiety.See
[B]middle formula (I-1), selects CC=1.1.
hydrolysism
citric acid=raw material weight × this kind of material protein content × CC × 2.1947=raw material weight × 9.3% × 1.1 × 2.1947
=M
prawn head× 0.2245.
2. prawn head need consume citric acid containing dissolution of calcium carbonate, the same;
dissolvem
citric acid=M
prawn head× 0.0288.
alwaysm
citric acid=
hydrolysism
citric acid+
dissolvem
citric acid=M
prawn head× 0.2245+M
prawn head× 0.0288=M
prawn head× 0.2533,
Use Citric Acid Mono--lemon acid crystals:
alwaysm
lemon acid crystals=
alwaysm
citric acid÷ 0.896=M
prawn head× 0.2827.
The lemon acid crystals Freezing preservation agent of the raw material 3% added should be reduced:
addm
lemon acid crystals=M
prawn head× 3%.
Now actually add lemon acid crystals:
add in factm
lemon acid crystals=
alwaysm
lemon acid crystals-
addm
lemon acid crystals=M
prawn head× 0.2827-M
prawn head× 3%=M
prawn head× 0.2527.
112 ~ 118 DEG C of hydrolysis 12 ~ 16 hours.
3, neutralize
With the food-grade limestone vegetation of citric acid weight 59 ~ 65% of hydrolysis to PH>=8, see
[C]formula (II-1), citric acid weight is shown in step 2.
4, precipitate
Liquid after neutralization is injected storage tank, precipitates 3 ~ 4 hours.
5, with salt and sucrose
Supernatant after extraction step 4 precipitates, by the weight percent (g/100mL or Kg/100L) of the precalculated volume output of product astaxanthin prawn juice, adds
[E]18% salt, stirring and dissolving; Add and to state
[E]3% sucrose, stirring and dissolving.The precalculated volume output of astaxanthin prawn juice is shown in
[F]middle formula (III).
6, the whole liquid of diatomite filtration
Liquid step 5 obtained uses diatomite filter repeatedly to filter, and reaches liquid completely limpid, till can't see suspended particulate.
7, modulate
1. by filtered Zi Lai Shui ‥ filtered water, liquid step 6 obtained is adjusted to nitrogen content 0.31 ~ 0.32 (g/100mL or Kg/100L).
2. regulate with food grade hydrochloric acid, liquid is reached
[D]pH4.4 ~ 4.6, so that the fishy smell removing marine product.
3. the precalculated volume output of product astaxanthin prawn juice is pressed
[F]weight percent (g/100mL or Kg/100L), add batch formula
[E]in each component modulate.
8, microporous barrier ultrafiltration
Liquid membrane aperture after step 7 being modulated is that the microporous barrier of 0.1 μm ~ 0.3 μm carries out ultrafiltration, removes bacterium.
9, filling
By filling for the liquid 250mL bottle after step 8 ultrafiltration.Filling bucket, bottle placer and filling bottle, lid use Ozone Water washed all in advance.
Above-mentioned particular content is as follows:
The freezing protein denaturant stored for a long time of [A] water resistant product, is called for short Freezing preservation agent.Protein denaturation refers to that protein its specific space conformation under some physics and chemistry factor effect is changed, thus causes the change of its physicochemical property and bioactive forfeiture, and this phenomenon is called protein denaturation.Marine product cryogenic freezing is preserved, of long duration will produce the permanent sex change of protein, greatly reduce amino acid whose recovery rate, the agent of anti-protein freeze denaturation must be added.Generally be divided into following a few class: carbohydrate, amino acids, carboxylic acid, EDTA etc.
[B] acid hydrolysis problem.
1, we are to the derivation of " calculating hydrolysis acid amount formula ".The H of hydrolysis ability only and in hydrolysis acid molecule
+ion is relevant.To polyacid Y, an acid molecule has Y H atom to be ionized into H
+ion.So; Hydrolysis effect is relevant with hydrolysis acid equivalent number.Hydrolysis object is that the nitrogen molecular polypeptide chain in raw material is broken into free amino acid, and raw material nitrogen molecular number is more, needs more hydrolysis acid equivalent numbers, and this is a proportional relation, and being write as equation is:
Hydrolysis acid equivalent number=raw material nitrogen molecular number × CC ... 1., proportionality coefficient aunt CC is called hydrolysis coefficient of intensification.
Hydrolysis acid equivalent number=hydrolysis acid molecule number × Y, ∵ hydrolysis acid molecule number=be hydrolyzed sour weight/hydrolysis acid molecule amount;
Hydrolysis acid equivalent number=hydrolysis acid molecule number × Y=(being hydrolyzed sour weight × Y)/hydrolysis acid molecule amount ... 2.;
Raw material nitrogen molecular number=raw material nitrogen quantity/molecular weight nitroxide 14.0067 ... 3..
Will 2. formula and 3. formula substitute into 1. formula:
(being hydrolyzed sour weight × Y)/hydrolysis acid molecule amount=(raw material nitrogen quantity/14.0067) × CC.
∴ is hydrolyzed sour weight=(hydrolysis acid molecule amount/14.0067) × raw material nitrogen quantity × CC ÷ Y
=(hydrolysis acid molecule amount/14.0067) × material protein quality × 16% × CC ÷ Y ... (I
0).
Raw material nitrogen quantity=material protein quality × 16%=raw material weight × this kind of material protein content × protein nitrogen content 16%.
The protein nitrogen content of general general meat, fowl, egg, fish, shellfish is 16%, and pearl imagination is also similar.
Sulfuric acid is binary acid, Y=2.We once used sulphuric acid hydrolysis, because mouthfeel is not good, and danger close, therefore use less as far as possible.
Polyacid except the sulfuric acid overwhelming majority be all weak acid, 2nd ~ 3 yuan of acid not easily ionizable, does not work very much, still regard as unit acid Y=1.Now: be hydrolyzed sour weight=(hydrolysis acid molecule amount/14.0067) × material protein quality × 16% × CC ... (I).
Wherein, Various material protein content can be found from food composition table or upper internet.
The size that hydrolysis coefficient of intensification CC selects with used be hydrolyzed sour catalysic coefficient relevant, also with to be hydrolyzed protein amounts contained by object relevant with type.The catalysic coefficient of strong acid is generally higher than weak acid.Catalysic coefficient α general alignment order is: acid iodide, bromic acid, hydrochloric acid, sulfuric acid, phosphoric acid, oxalic acid, sulfurous acid, citric acid, lactic acid, acetic acid ...When adopting the acid that catalysic coefficient is large, hydrolysis coefficient of intensification CC can with less, and with the acid that catalysic coefficient is little, CC can with large.Scleroprotein composition bone, cartilage, tendon, angle, hair, silk etc., not facile hydrolysis, hydrolysis coefficient of intensification CC can with large.Hydrolysis effect becomes positive correlation with hydrolysis temperature T, time t in general usual range, and also dispel the heat relevant with temperature height and container, but impact is less, these can suitably adjust.Such as: back hydrolysis, temperature is lower, and CC can with larger, and reactor is hydrolyzed, and temperature is higher, and CC can with smaller.Hydrolysis time t is shorter, and CC can with larger; Hydrolysis time t is longer, and CC can with smaller.About the selection of hydrolysis coefficient of intensification CC value.It is for reference that we propose following table from experience, and reader can improve in practice further!
Table 1 is hydrolyzed some reference values of coefficient of intensification CC
# shrimp shell, containing calcium carbonate, dissolves and needs consumption acids.
2, acid hydrolysis uses and inquires into.Strong acid is inorganic acid entirely; Iodate and bromate are dangerous material or carcinogen; Nitric acid stimulates very much, can explode; After phosphoric acid hydrolysis, after neutralization, reaction is very slow, and precipitation is bonded at chamber wall difficulty and removes, and product is the smell of burning.These acid all can not be used for being hydrolyzed.
The most general is hydrochloric acid, and its catalysic coefficient α is large, can obtain food grade hydrochloric acid from electrolytic seawater, good and cheap.Hydrochloric acid is the composition of human body hydrochloric acid in gastric juice, and the acid after hydrolysis is by soda ash Na
2cO
3be neutralized into salt, be well suited for making flavouring, mouthfeel is pretty good.Japanese has invented chemical soy sauce with hydrochloric acid hydrolysis soybean during World War II, propagates its belief on a large scale! But hydrochloric acid hydrolysis is hydrolyzed smelly as consumption too much can produce, in Shandong, a food factory met for we.Good unpleasant! The stainless steel cauldron of a 3000L, due to excessive hydrochloric acid, even also has burnt by they! This is the first problem that hydrochloric acid hydrolysis is dealt with improperly.
Before and after 1992 last century, carcinogenic substance---the chloropropyl alcohol content overproof in some soy sauce that China produces, for this reason, European Union's restriction soy sauce exports to European market, large quantities of return of goods.In chloropropyl alcohol, the harm of trichloropropanol to human body is maximum, it is that soybean fat hydrolysis of rupturing under strong acid forms glycerine, and glycerine (glycerine) reacts under strong acid or hot conditions, HCl substituted alcohols hydroxyl and generate chloropropyl alcohol, based on 3-chlorine-1,2-propylene glycol.
Why there will be this problem? this is that the soy sauce of outlet is the blended soy sauce being mixed with hydrochloric acid hydrolysis dregs of beans mostly because the production efficiency that makes soy sauce is very low.This is the Second Problem that hydrochloric acid hydrolysis deals with appearance improperly.
Besides utilizing hydrochloric acid hydrolysis can cause severe contamination to air, this is a pretty troublesome thing! The stink of hydrochloric acid all is filled the air in the whole workshop of thousands of square metres, extremely feels bad when Shandong food factory produces seafood soy-sauce with hydrochloric acid hydrolysis! This is the 3rd problem that hydrochloric acid hydrolysis occurs.
The catalysic coefficient of sulfuric acid is comparatively large, is again binary strong acid, can remove the heavy metal of product by chelating.Seabed, Zhejiang has " Haiti melon " of a kind of similar sea cucumber, allegedly the similar sea cucumber of nutrition, but toxicity is large, and containing heavy metal, local fisherman dare not eat.We once became Haiti melon hydrolyzate with sulphuric acid hydrolysis It, and through medical college of Zhongshan University, acute toxicity test proves hypotoxicity.Wherein content of beary metal (mg/L): As0.009 is checked through Guangzhou Institute of Analysis; Cd0.052; Hg7.8 × 10
-4; Pb0.18.All reach the food standard of country.Total number of bacteria, coliform, pathogenic bacteria etc. all reach standard through the inspection of Food Hygiene Supervision and Inspection Institute of Guangdong Province.Amino acid and taurine summation reach 12815mg/100g, are close with the 14892.44mg/100g of our oyster hydrolyzate.Visible Haiti melon still has Development volue.Put off until some time later mouthfeel also not so good, sulfurous acid is also like this but sulfuric acid is too strong, accidentally with regard to hurting people or smashing objects, very fearful!
Organic acid only has below secondary strong acid, and catalysic coefficient α is lower, and price is more expensive, is applicable to the aquatic products of the low nitrogen of hydrolysis.Wherein formic acid, acetic acid, propionic acid threshold value are low, very bad news; Tartaric acid stimulates very much; Gluconic acid and malic acid price more expensive, catalysic coefficient α is low.We once used citric acid, oxalic acid and lactic acid to be hydrolyzed, and thought that citric acid and oxalic acid comparatively share.α is low for lactic acid catalysic coefficient, expensive again, improper.
3, citric acid and oxalic acid hydrolysis.
Citric acid and oxalic acid hydrolysis are that we initiate, and their catalysic coefficient is slightly low, and price is more expensive than hydrochloric acid, but it is free from environmental pollution, and the acid after hydrolysis can filter out with lime or nacreous layer powder neutralization, so finished product not saliferous, can produce aminoacids solution, efficiency is very high! This is great advantage.
Measuring with acid with they hydrolysis is below discussed.
(1) citric acid C
6h
8o
7(192.125), be ternary weak acid.Dissociation constant K
α 1=7.4 × 10
-4, K
α 2=1.7 × 10
-5, K
α 3=4.0 × 10
-7.Add the water of raw material and equivalent in a kettle., and following citric acid amount.From formula (I), adopt citric acid:
M
citric acid=(192.125 ÷ 14.0067) × (raw material weight × this kind of material protein content × 16%) × CC
=raw material weight × this kind of material protein content × CC × 2.1947 ... (I-1).
At 112 ~ 118 DEG C, be hydrolyzed 12 ~ 16 hours, imagination only has monoacid to ionize.
As used citric acid to make the freezing protein denaturant stored for a long time of water resistant product, using during citric acid hydrolysis and remembering to deduct this part consumption.
(2) oxalic acid H
2c
2o
4(90.036), be binary time strong acid.Dissociation constant K
α 1=5.9 × 10
-2, K
α 2=6.4 × 10
-5.Add the water of raw material and equivalent in a kettle., and following oxalic acid amount.From formula (I), adopt oxalic acid:
M
oxalic acid=(90.036 ÷ 14.0067) × (raw material weight × this kind of material protein content × 16%) × CC
=raw material weight × this kind of material protein content × CC × 1.0285 ... (I-2).
At 112 ~ 118 DEG C, be hydrolyzed 12 ~ 16 hours, imagination only has monoacid to ionize.
Oxalic acid at medical industry for the manufacture of aureomycin, terramycin, tetracycline, streptomysin, ephedrine.But oxalic acid is harmful, the acid-base value disequilibrium in human body can be made, affect the growth of children; Oxalic acid can also form calcium oxalate precipitation with the calcium of human body and cause kidney or ureteral calculi, very painful; Oxalic acid can form water-soluble complex compound with many metals.Therefore; Use oxalic acid must be very careful, be hydrolyzed and completely all must become calcium oxalate with limestone vegetation, filter remove clean! All containers must with stainless steel or glass container, in order to avoid form water-soluble complex compound with some metals.
[C] neutralizes.
1, with food-grade limestone vegetation citric acid.Food-grade lime is containing calcium hydroxide 98%.
2C
6H
8O
7+3Ca(OH)
2——→Ca
3(C
6H
5O
7)
2↓+6H
2O
384.251222.284498.443
M
calcium hydroxide=(222.284 ÷ 384.251) × M
citric acid=0.5785M
citric acid.Food-grade lime contains calcium hydroxide 98%,
M
lime=M
calcium hydroxide÷ 0.98%=0.5785M
citric acid÷ 0.98%=M
citric acid× 0.59 ... (II-1)
2, use in nacreous layer powder and citric acid.Nacreous layer powder is containing calcium carbonate 92%.
2C
6H
8O
7+3CaCO
3——→Ca
3(C
6H
5O
7)
2↓+3H
2O+3CO
2↑
384.251300.2676498.443
M
caCO3=(300.2676 ÷ 384.251) × M
citric acid=0.7814 × M
citric acid.Nacreous layer powder is containing calcium carbonate 92%
∴ M
layer powder=M
caCO3÷ 0.92%=0.8494 × M
citric acid(II-2)
3, with food-grade limestone vegetation oxalic acid.
Employing soda ash neutralizes, and form sodium oxalate solvable, not being food additives, is dangerous material, and this neutralization is unavailable.Or adopt limestone vegetation better.For preventing remaining oxalic acid, must make it fully to precipitate to filter by Zhong He Zhi≤PH8.
H
2C
2O
4+Ca(OH)
2——→CaC
2O
4↓+2H
2O
90.03674.09468128.10012
M
ca (OH) 2=(74.09468 ÷ 90.036) × M
oxalic acid=M
oxalic acid× 0.8229.Food-grade lime is containing calcium hydroxide 98%.
Use food-grade lime: M
lime=M
ca (OH) 2÷ 0.98=M
oxalic acid× 0.8397 ... (II-3).
The smelling removal of [D] marine product and the adjustment of pH value.。
What marine product was afraid of most is fishy smell, and this is easy to solve in fact.We find: when baste mouthfeel when acidity is PH4.4-4.6 is best, do not have fishy smell, and antiseptic effect, just engenders fishy smell to PH6 later, and arrived PH7-8 and eaten with regard to very bad later, this just can smell at N-process!
The adjustment of pH value.We are when playing initial adjustment, repeatedly add the change of alkali (acid) pH value little, just adjust suddenly excessive, have to acid adding (alkali) recall to again, enough tired! Just find several times that pH value has individual mutation range, investigates interrelated data as following table.
Table 2 HCl of the 0.1N of the NaOH titration 20mL of 0.1N
From PH1 → PH4.30, the NaOH adding 0.1N is needed to be 19.98mL, and from PH4.31 → PH7.00, only need the NaOH adding 0.1N to be 0.02mL, and from PH7 → PH9.7, only need the NaOH adding 0.1N to be 0.02mL, visible fast in this scope pH value hop, must carefully slowly add.Neutralization for other acid-base class also has analogue!
[E] astaxanthin prawn juice batch formula:
PH4.4 ~ 4.6, amino nitrogen 0.28 ~ 0.3%, salt 18%, sucrose 3%, monosodium glutamate 1.8%, guanylic acid GMP0.05% (or I+G--inosinicacid and guanylic acid half and half IMP+GMP0.06%), sodium succinate 0.04%, natrium citricum 0.16%, cooking wine 1%, the old vinegar 1% in Shanxi, sodium dehydroacetate 0.05 ~ 0.1%.
Here % still refers to g/100mL or Kg/100L.
Sucrose makes product have sweet taste, and for glycosuria patient, also can replace with the Sucralose of 0.005%, Sucralose sugariness is 600 times of sucrose.Guanylic acid GMP tool delicate flavour and mushroom taste, and suppress peculiar smell to make taste soft, I+G is also similar.Sodium succinate tool shellfish delicate flavour, many tastes are turbid.The old vinegar in Shanxi has special fragrance, and cooking wine is also.Sodium dehydroacetate is the extremely strong food preservative of the antibacterial power of a kind of wide spectrum class newly developed.
The adding and be careful of batching, we once found to modulate the rear the bottom of a pan and leave guanylic acid GMP or I+G valuable in a large number and precipitate, and caused waste.Dissolve so they can not directly be put in pot, precipitation loss can be formed.Filtered water, heating, stirring and dissolving must be added by another beaker.Sodium dehydroacetate also other filtered water dissolving adds.Monosodium glutamate, sodium succinate, natrium citricum, cooking wine, vinegar can directly add, and stirs.
[F] estimated output V (volume):
By definition recovery rate γ=product nitrogen content ÷ raw material nitrogen content
=[small product size V (mL) × product amino nitrogen (g/mL)] ÷ [raw material weight (g) × this kind of raw material nitrogen content %]
∴ small product size V (mL)=[raw material weight (g) × this kind of raw material nitrogen content % × γ] ÷ product amino nitrogen (g/mL)
∵ raw material nitrogen content %=material protein content % × 16%.The protein nitrogen content of meat, fish is 16%.
V (mL)=raw material weight (g) × material protein content % × 16% × γ ÷ product amino nitrogen (g/mL) ... (III)
From small product size V, measurement products amino nitrogen (g/mL), raw material weight (g) and food composition table can find protein content or the nitrogen content % of raw material, just can calculate recovery rate γ, generally 60% ~ 65%.
Shi Zhong unit (g, mL, g/mL) can be made into (Kg, L, Kg/L).
The filtration problem of [G] product.Product wants limpid bright precipitation first will solve filtration problem.The food machinery of China has been introduced since being full reform and opening-up, and history is not long, and some equipment performance manufacturer is also unclear.Our hydrolyzate comparatively filter by sticky being difficult to.When hydrolyzate is injected the duplex filter filtration of manufacturer's recommended by for the first time, filtration sieve plate is inside crushed entirely.Be originally that slag is filtered to pass by too much, pressure causes too greatly.Consult this food machinery factory factory director, he says that available filter centrifugal filters.When buying filter centrifugal, a start liquid is thrown out of entirely, or because slag is too many.Diatomite filter is used to filter also not all right.We added one precipitation operation of 3 ~ 4 hours before filtration afterwards, extracted supernatant, then filtered with diatomite filter.Essence filter at that time adopts husky core to filter, and just blocked husky core once, again consulted food machinery factory factory director and how to recover husky core function, he says and has been crossed just by husky core poach.We fall down once boiling sand, because husky core sticks with glue, once boiling.Finally find it is that diatomite filtration is not filtered, need repeatedly to filter that to reach liquid completely limpid, till can't see suspended particulate.After formula for a product modulation, use the filter of husky core essence instead microporous barrier ultrafiltration again, bacterium is also filtered.This just thoroughly solves filtration problem, also solves sterilizing problem.
The sedimentation problem of [H] product.In order to improve products taste, when its acidity being adjusted to PH4.4 ~ 4.6, mouthfeel is best, so very naturally merely hits and arrives this, being now in meta-acid state.Cause product constantly to precipitate, heavily filter after some months, cross some months and precipitate again, so when finish? also do not become with ultrafiltration.Change technique, formula, product still precipitates successively, has consulted my the relevant professor in school (department of chemistry of Ji'nan University) and has all come to nothing.This problem perplexs us for many years, finally just realizes opposition thinking! Does not is not product precipitate successively? do are we afraid of precipitation? that is just acted in a diametrically opposite way, by in the liquid after hydrolysis and to≤PH8, it is allowed to be in alkaline state, the acid salt of citric acid is made to have the sufficient time to be transformed into normal salt precipitation, cross and filter to remove all citric acid normal salt, this just solves sedimentation problem.Be transferred to PH4.4 ~ 4.6 with food grade hydrochloric acid again, solve sensory issues.
From the principle: with citric acid hydrolysis, when limestone vegetation is to PH4.4 ~ 4.6, under being in slant acidity condition, certainly exist the acid salt citric acid 4 hydrogen calcium CaH of a large amount of citric acid
4(C
6h
5o
7)
2with calcium hydrogen citrate CaHC
6h
5o
7, be long placed in and form calcium citrate Ca
3(C
6h
5o
7)
2precipitation and citric acid, as reaction equation below.This is a reversible equilibrium process, both there is citric acid 4 hydrogen calcium or the calcium hydrogen citrate on the formula left side in solution, also there is the calcium citrate precipitation on the right of formula and citric acid.If we filter, the calcium citrate precipitated on the right of formula is removed, just have the citric acid 4 hydrogen calcium on the formula left side or calcium hydrogen citrate at once and again form calcium citrate on the right of formula and citric acid, namely continue to produce precipitation, like this: filter → precipitation → filter → precipitation → filter →, be difficult to stop, our situation about in the past experiencing that Here it is.If we are by liquid Zhong He Zhi≤PH8, constantly neutralize by the citric acid generated on the right of formula, destroy the balance of reaction equation, just do not have to the reaction on the formula left side on the right of formula, the reaction only from the formula left side on the right of formula, reaches new balance, so continue, last citric acid 4 hydrogen calcium or calcium hydrogen citrate become calcium citrate all, remove after filtration, thoroughly solve sedimentation problem! Reaction needed has time enough.
For crustacean hydrolyzates such as shrimps, also can there is a large amount of chitin and be dissolved in acid solution, they also can be precipitated out through long-time storing in the basic conditions, remove by filtering.
When within 1996, we produce scallop seasoning king in Yantai with hydrochloric acid hydrolysis scallop body, use dietary alkali Na
2cO
3be neutralized to PH7, be then modulated to PH4.4 ~ 4.6 to improve mouthfeel with citric acid, result product produces a large amount of precipitation, still precipitates, filters time and again, precipitate time and again, cannot solve after filtration.Found it is because scallop body, with not examining clean shell, becomes calcium chloride CaCl through hydrochloric acid hydrolysis afterwards
2, be transferred to PH4.4 ~ 4.6 with citric acid, just define acid salt citric acid 4 hydrogen calcium CaH
4(C
6h
5o
7)
2with calcium hydrogen citrate CaHC
6h
5o
7, so that there is above-mentioned continuous filtration, constantly precipitate! Reaction equation is as 3 formulas below.When this lesson makes us understand to adopt hydrochloric acid hydrolysis, can not to think and improve mouthfeel and use citric acid to regulate pH value, pH value can only be regulated with food grade hydrochloric acid.
2HCl+CaCO
3——→CaCl
2+H
2O+CO
2↑
CaCl
2+2C
6H
8O
7——→CaH
4(C
6H
5O
7)
2+2HCl
CaCl
2+C
6H
8O
7——→CaHC
6H
5O
7+2HCl
Compared with the prior art, the present invention has following beneficial effect.
Main innovate point
1, citric acid hydrolysis is our original creation, solves and produces problem such as hydrolysis smelly, carcinogenic trichloropropanol and contaminated environment etc. with hydrochloric acid hydrolysis.
2, we are pioneering is hydrolyzed prawn head, produces " astaxanthin prawn juice ", solves the process difficult problem of shrimp head containing many rough-and-tumble shells.
3, the freezing protein stored for a long time of aquatic products raw material sex change can affect recovery rate, adds citric acid for this reason in the feed and makes the freezing protein denaturant stored for a long time of water resistant product
[A], improve recovery rate.Do not produce dark reddish brown, make product have the beautiful color of rare astaxanthin!
4, the desensitization of shrimp protein.Shrimp protein is breaks down into amino acids after hydrolysis, is no longer protein, there is not allergic problem.We were once hydrolyzed pollen, be afraid of that the woman physician teacher of pollen hypersensitivity detects most, prove to desensitize completely through my school.
5, product contains a large amount of magnesium, and it well can protect cardiovascular system, reduces blood cholesterol level, prevents artery sclerosis, be conducive to preventing hypertension and myocardial infarction.The potent antioxidation of its tool, effectively could reverse aging also containing a large amount of astaxanthin!
6, the calculating hydrolysis acid amount formula of original creation
[B].
7, the fishy smell problem of sea (light) aquatic products is solved
[D].Finally product is modulated to PH4.4 ~ 4.6, solves the fishy smell problem of marine product.
8, the formula of the fresh fragrance making product tool strong is used
[E], make effect more perfect, taste is excellent!
9, the computing formula of product estimated output is derived
[F].
10, a filtration difficult problem for product is solved
[G].Add before filtration and precipitated 3 ~ 4 hours together, then extracted the technique of supernatant liquid filtering, solve a filtration difficult problem.
11, a precipitation difficult problem for product is solved
[H].To be hydrolyzed, be neutralized to >=PH8 after liquid inject storage tank, precipitate 3 ~ 4 hours.Allow the acid salt of the citric acid existed in liquid: citric acid 4 hydrogen calcium CaH
4(C
6h
5o
7)
2with calcium hydrogen citrate CaHC
6h
5o
7, at alkali condition to normal salt [Ca
3(C
6h
5o
7)
2] change and be precipitated out, then passed through to filter to remove, stopped precipitation.We are in the prawn head hydrolyzate product on September 19th, 2003--and " red prawn juice ", limpid bright so far, have no precipitation!
12, enter industrialized reactor technology for hydrolyzing from the back hydrolysis technology in laboratory, this is a leap.Have many new technologies to lack this leap exactly, rest on laboratory all the time, cannot promote!
Specifically execute mode
Below in conjunction with specific embodiment, the invention will be further described.
Embodiment 1
Use 5000 milliliters of erlenmeyer flasks, adopt citric acid, back hydrolysis prawn head 1200g.Produce " astaxanthin prawn juice ".Prawn head is about containing protein 9.3%.Containing calcium carbonate 2.25%.
Charging: Σ=prawn head 1200g+ water 1200g+M
lemon acid crystals.
The citric acid added has two parts:
1. hydrolyzable moiety.See
[B]formula (I-1), select CC=1.2:
hydrolysism
citric acid=M
prawn head× this kind of material protein content × CC × 2.1947=1200 × 9.3% × 1.2 × 2.1947=293.91g.
2. dissolve and consume part.Formula (IV) from technical scheme:
dissolvem
citric acid=M
prawn head× 0.0288=1200 × 0.0288=34.56g.
Altogether need with citric acid:
alwaysm
citric acid=
hydrolysism
citric acid+
dissolvem
citric acid=293.91g+34.56g+=328.47g
Altogether need to use lemon acid crystals:
alwaysm
lemon acid crystals=
alwaysm
citric acid÷ 0.896=366.60g,
Reduce the lemon acid crystals Freezing preservation agent adding raw material 3%: 1200 × 3%=36g.The brilliant 366.6-36=330.6g of real adding citric acid.
With dry food level limestone vegetation, only need neutralizing hydrolysis acid, see
[C]formula (II-1):
M
lime=
hydrolysism
citric acid× 0.59=293.91 × 0.59=173.41g.
Estimated output V (volume), is shown in formula (III) in [F]:
V (mL)=[raw material weight (g) × this kind of material protein content % × 16% × 65% (recovery rate)] ÷ product nitrogen content (g/mL).
=1200×9.3%×16%×65%÷0.003=3868.8mL。
Astaxanthin prawn juice nitrogen content 0.003 (g/mL).
The water of 1200g prawn head and equivalent is inserted in 5000mL erlenmeyer flask, adds lemon acid crystals 330.6g, back hydrolysis 12 ~ 16 hours.>=PH8 is neutralized to dry food level lime 173.41g.Precipitate 3 ~ 4 hours.Extract supernatant, by 18% salt adding of estimated output 3869 milliliters, stirring and dissolving; Add the sucrose of 3% again, stirring and dissolving.Whole liquid diatomite filter filters repeatedly, removes the precipitation slags such as citrate, reaches liquid completely limpid, till can't see suspended particulate.Modulation.1. by filtered water, liquid is adjusted to nitrogen content 0.31 ~ 0.33 (g/100mL), in order to causing dilution because adding formula.2. regulate with food grade hydrochloric acid, make liquid reach PH4.4 ~ 4.6, to remove the fishy smell of marine product.3. press the weight percent (g/100mL) of now volume, add batch formula
[E]in each component modulate.Carry out ultrafiltration with the microporous barrier that membrane aperture is 0.1 μm ~ 0.3 μm, remove bacterium.Filling 250 milliliters of bottles.
Embodiment 2
Use 1000L all steel reactor, adopt citric acid, hydrolysis prawn head.Produce " astaxanthin prawn juice ".Prawn head is about containing protein 9.3%.Containing calcium carbonate 2.25%
Dress still: Σ=prawn head 340Kg+ water 340Kg+M
lemon acid crystals.
The citric acid added has two parts:
1. hydrolyzable moiety.See
[B]middle formula (I-1), select CC=1.1:
hydrolysism
citric acid=M
prawn head× this kind of material protein content × CC × 2.1947=340 × 9.3% × 1.1 × 2.1947=76.34Kg,
2. dissolve and consume part.From formula (IV):
dissolvem
citric acid=M
prawn head× 0.0288=340 × 0.0288=9.79kg.
Altogether need with citric acid:
alwaysm
citric acid=
hydrolysism
citric acid+
dissolvem
citric acid=76.34Kg+9.79kg=86.13Kg,
Altogether need to use lemon acid crystals:
alwaysm
lemon acid crystals=
alwaysm
citric acid÷ 0.8966=96.12Kg.
Reduce the lemon acid crystals Freezing preservation agent adding raw material 3%: 340 × 3%=10.2Kg, the brilliant 96.12-10.2=85.92Kg of real adding citric acid.
With dry food level limestone vegetation, only need neutralizing hydrolysis acid, see
[C]middle formula (II-1):
M
lime=
hydrolysism
citric acid× 0.59=76.34 × 0.59=45.03Kg.
Estimated output V (volume), is shown in
[F]middle formula (III):
V (L)=[raw material weight (Kg) × this kind of material protein content % × 16% × 65% (recovery rate)] ÷ product nitrogen content (Kg/L).
=340×9.3%×16%×65%÷0.003=1096.16L。
Astaxanthin prawn juice nitrogen content 0.003 (Kg/L).
The water of 340kg prawn head and equivalent is inserted in 1000L all steel reactor, adds lemon acid crystals 85.92Kg, 112 ~ 118 DEG C of hydrolysis 12 ~ 16 hours.With dry food level lime 45.03Kg, be neutralized to >=PH8.Precipitate 3 ~ 4 hours.Extract supernatant, by 18% salt adding of estimated output 1096L, stirring and dissolving; Add the sucrose of 3% again, stirring and dissolving.Whole liquid diatomite filter filters repeatedly, removes the precipitation slags such as citrate, reaches liquid completely limpid, till can't see suspended particulate.Modulation.1. by filtered water, liquid is adjusted to nitrogen content 0.31 ~ 0.33 (Kg/100L), in order to causing dilution because adding formula.2. regulate with food grade hydrochloric acid, make liquid reach PH4.4 ~ 4.6, to remove the fishy smell of marine product.3. press the weight percent (Kg/100L) of now volume, add batch formula
[E]in each component modulate.Carry out ultrafiltration with the microporous barrier that membrane aperture is 0.1 μm ~ 0.3 μm, remove bacterium.Filling 250mL bottle.
To those skilled in the art, obviously the invention is not restricted to the details of above-mentioned one exemplary embodiment, and when not deviating from spirit of the present invention or essential characteristic, the present invention can be realized in other specific forms.Therefore, no matter from which point, all should embodiment be regarded as exemplary, and be nonrestrictive, scope of the present invention is limited by claims instead of above-mentioned explanation, and all changes be therefore intended in the implication of the equivalency by dropping on claim and scope are included in the present invention.
In addition, be to be understood that, although this description is described according to embodiment, but not each embodiment comprises an independently technical scheme, this narrating mode of description is only for clarity sake, those skilled in the art should by description integrally, and in each embodiment, technical scheme also through appropriately combined, can form other embodiments that it will be appreciated by those skilled in the art that.
Claims (5)
1. the production method of astaxanthin prawn juice, is characterized in that the method adopting citric acid hydrolysis prawn head, comprises the following steps:
(1) pretreatment of raw material
Collect raw material prawn head, the citric acid adding raw material weight 2 ~ 4%, as the agent of anti-protein freeze denaturation, saves backup in fish freezer less than-20 DEG C cryogenic freezings;
(2) be hydrolyzed
Hydrolysis adopts citric acid C
6h
8o
7192.125;
Prawn head according to decomposition, containing protein 9.3%, containing calcium carbonate 2.25%;
Charging: Σ=M
prawn headwater gaging+the M such as+prawn head
lemon acid crystals; The citric acid added has two parts;
(3) neutralize
By the food-grade limestone vegetation of the citric acid weight 59 ~ 65% of the hydrolysis of liquid above to >=PH8;
(4) precipitate
Liquid after neutralization is injected storage tank, precipitates 3 ~ 4 hours;
(5) with salt and sucrose
Supernatant after extraction step 4 precipitates, by the weight percent of the precalculated volume output of product astaxanthin prawn juice, adds 18% salt, stirring and dissolving; Add 3% sucrose stated, stirring and dissolving;
(6) the whole liquid of diatomite filtration
Liquid step 5 obtained uses diatomite filter repeatedly to filter, and reaches liquid completely limpid, till can't see suspended particulate;
(7) modulate
1. by filtered Zi Lai Shui ‥ filtered water, liquid step 6 obtained is adjusted to nitrogen content 0.31 ~ 0.32g/100mL or Kg/100L;
2. regulate with food grade hydrochloric acid, make liquid reach PH4.4 ~ 4.6, to remove the fishy smell of marine product;
3. press the weight percent of the precalculated volume output of product astaxanthin prawn juice, add batch formula
]in each component modulate;
(8) microporous barrier ultrafiltration
Liquid membrane aperture after step 7 being modulated is that the microporous barrier of 0.1 μm ~ 0.3 μm carries out ultrafiltration, removes bacterium;
(9) filling.
2., according to the production method of astaxanthin prawn juice according to claim 1, it is characterized in that
Step 2 adopts 5000mL erlenmeyer flask back hydrolysis
In erlenmeyer flask, add the water of raw material that step 1 obtains and equivalent, then add two parts citric acid:
(1) hydrolyzable moiety
hydrolysism
citric acid=M
prawn head× this kind of material protein content × CC × 2.1947=M
prawn head× 9.3% × 1.2 × 2.1947=M
prawn head× 0.2449
(2) prawn head is containing calcium carbonate 2.25%, need dissolve consumption citric acid,
dissolvem
citric acid=M
prawn head× 0.0288
alwaysm
citric acid=
hydrolysism
citric acid+
dissolvem
citric acid=M
prawn head× 0.2449+M
prawn head× 0.0288=M
prawn head× 0.2737, use Citric Acid Mono--lemon acid crystals:
alwaysm
lemon acid crystals=
alwaysm
citric acid÷ 0.896=M
prawn head× 0.3055,
The lemon acid crystals Freezing preservation agent of the raw material 3% added should be reduced:
addm
lemon acid crystals=M
prawn head× 3%, now actually add lemon acid crystals:
add in factm
lemon acid crystals=
alwaysm
lemon acid crystals-
addm
lemon acid crystals=M
prawn head× 0.3055-M
prawn head× 3%=M
prawn head× 0.2755,
Back hydrolysis 12 ~ 16 hours.
3., according to the production method of astaxanthin prawn juice described in claim 1, it is characterized in that
Step 2 adopts reactor to be hydrolyzed
Add the water of raw material that step 1 obtains and raw material equivalent in a kettle., then add two parts citric acid:
(1) hydrolyzable moiety
hydrolysism
citric acid=raw material weight × this kind of material protein content × CC × 2.1947=raw material weight × 9.3% × 1.1 × 2.1947=M
prawn head× 0.2245
(2) prawn head need consume citric acid containing calcium carbonate, the same;
dissolvem
citric acid=M
prawn head× 0.0288
alwaysm
citric acid=
hydrolysism
citric acid+
dissolvem
citric acid=M
prawn head× 0.2245+M
prawn head× 0.0288=M
prawn head× 0.2533, use Citric Acid Mono--lemon acid crystals:
alwaysm
lemon acid crystals=
alwaysm
citric acid÷ 0.896=M
prawn head× 0.2827, the lemon acid crystals Freezing preservation agent of the raw material 3% added should be reduced:
addm
lemon acid crystals=M
prawn head× 3%, now actually add lemon acid crystals:
add in factm
lemon acid crystals=
alwaysm
lemon acid crystals-
addm
lemon acid crystals=M
prawn head× 0.2827-M
prawn head× 3%=M
prawn head× 0.2527,
112 ~ 118 DEG C of hydrolysis 12 ~ 16 hours.
4., according to the production method of astaxanthin prawn juice described in claim 1, it is characterized in that
Neutralization procedure
With food-grade limestone vegetation citric acid, food-grade lime is containing calcium hydroxide 98%
2C
6H
8O
7+3Ca(OH)
2——→Ca
3(C
6H
5O
7)
2↓+6H
2O
384.251222.284498.443
M
calcium hydroxide=(222.284 ÷ 384.251) × M
citric acid=0.5785M
citric acid
M
lime=M
calcium hydroxide÷ 0.98%=0.5785M
citric acid÷ 0.98%=M
citric acid× 0.59.
5., according to the production method of astaxanthin prawn juice described in claim 1, it is characterized in that
In modulation step, by the weight percent of the precalculated volume output of product astaxanthin prawn juice, adding batch formula is:
Astaxanthin prawn juice batch formula (g/100mL or Kg/100L):
PH4.4 ~ 4.6, amino nitrogen 0.28 ~ 0.3%, salt 18%, sucrose 3%, monosodium glutamate 1.8%, guanylic acid GMP0.05% (or I+G--inosinicacid and guanylic acid half and half IMP+GMP0.06%), sodium succinate 0.04%, natrium citricum 0.16%, cooking wine 1%, the old vinegar 1% in Shanxi, sodium dehydroacetate 0.05 ~ 0.1%
Here % still refers to g/100mL or Kg/100L.
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