CN1149627A - Reagent peptone formula and production process thereof - Google Patents
Reagent peptone formula and production process thereof Download PDFInfo
- Publication number
- CN1149627A CN1149627A CN 95112530 CN95112530A CN1149627A CN 1149627 A CN1149627 A CN 1149627A CN 95112530 CN95112530 CN 95112530 CN 95112530 A CN95112530 A CN 95112530A CN 1149627 A CN1149627 A CN 1149627A
- Authority
- CN
- China
- Prior art keywords
- soup
- slag
- hydrochloric acid
- pancreas
- peptone
- 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.)
- Pending
Links
- 239000001888 Peptone Substances 0.000 title claims abstract description 15
- 108010080698 Peptones Proteins 0.000 title claims abstract description 15
- 235000019319 peptone Nutrition 0.000 title claims abstract description 15
- 239000003153 chemical reaction reagent Substances 0.000 title claims abstract description 13
- 238000004519 manufacturing process Methods 0.000 title claims description 10
- 238000009472 formulation Methods 0.000 title abstract description 5
- 235000014347 soups Nutrition 0.000 claims abstract description 46
- 238000000034 method Methods 0.000 claims abstract description 22
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 claims abstract description 20
- 210000000496 pancreas Anatomy 0.000 claims abstract description 10
- 239000002893 slag Substances 0.000 claims abstract description 10
- 241001465754 Metazoa Species 0.000 claims abstract description 8
- 108010019160 Pancreatin Proteins 0.000 claims abstract description 8
- 230000007062 hydrolysis Effects 0.000 claims abstract description 8
- 238000006460 hydrolysis reaction Methods 0.000 claims abstract description 8
- NLYAJNPCOHFWQQ-UHFFFAOYSA-N kaolin Chemical compound O.O.O=[Al]O[Si](=O)O[Si](=O)O[Al]=O NLYAJNPCOHFWQQ-UHFFFAOYSA-N 0.000 claims abstract description 8
- 229940055695 pancreatin Drugs 0.000 claims abstract description 8
- 235000013372 meat Nutrition 0.000 claims abstract description 6
- 238000001291 vacuum drying Methods 0.000 claims abstract description 4
- 210000001835 viscera Anatomy 0.000 claims abstract description 4
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims abstract description 3
- 238000001914 filtration Methods 0.000 claims abstract description 3
- 239000004927 clay Substances 0.000 claims abstract 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 7
- 210000004185 liver Anatomy 0.000 claims description 3
- 244000144972 livestock Species 0.000 claims description 3
- 238000012856 packing Methods 0.000 claims description 3
- 244000144977 poultry Species 0.000 claims description 3
- 238000010025 steaming Methods 0.000 claims description 3
- 108090000790 Enzymes Proteins 0.000 claims description 2
- 102000004190 Enzymes Human genes 0.000 claims description 2
- 229960000074 biopharmaceutical Drugs 0.000 claims description 2
- 229940088598 enzyme Drugs 0.000 claims description 2
- 239000000843 powder Substances 0.000 claims description 2
- 239000000463 material Substances 0.000 abstract description 7
- 239000000203 mixture Substances 0.000 abstract description 6
- 230000008901 benefit Effects 0.000 abstract description 5
- 239000002699 waste material Substances 0.000 abstract description 3
- 239000002994 raw material Substances 0.000 abstract description 2
- 239000005995 Aluminium silicate Substances 0.000 abstract 1
- 235000012211 aluminium silicate Nutrition 0.000 abstract 1
- 230000015572 biosynthetic process Effects 0.000 abstract 1
- 230000029087 digestion Effects 0.000 abstract 1
- 238000007689 inspection Methods 0.000 abstract 1
- 238000004806 packaging method and process Methods 0.000 abstract 1
- 238000002360 preparation method Methods 0.000 abstract 1
- 238000003786 synthesis reaction Methods 0.000 abstract 1
- 210000000988 bone and bone Anatomy 0.000 description 8
- 238000001035 drying Methods 0.000 description 7
- 239000000047 product Substances 0.000 description 7
- 241000282898 Sus scrofa Species 0.000 description 6
- 238000009835 boiling Methods 0.000 description 6
- 241000272525 Anas platyrhynchos Species 0.000 description 4
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 4
- 239000012467 final product Substances 0.000 description 4
- 239000006260 foam Substances 0.000 description 4
- 238000010438 heat treatment Methods 0.000 description 4
- 238000005070 sampling Methods 0.000 description 4
- 239000000126 substance Substances 0.000 description 4
- 239000012141 concentrate Substances 0.000 description 3
- 238000010411 cooking Methods 0.000 description 3
- 229910001220 stainless steel Inorganic materials 0.000 description 3
- 239000010935 stainless steel Substances 0.000 description 3
- 238000005266 casting Methods 0.000 description 2
- 229910052571 earthenware Inorganic materials 0.000 description 2
- 235000021050 feed intake Nutrition 0.000 description 2
- 239000008187 granular material Substances 0.000 description 2
- 235000012149 noodles Nutrition 0.000 description 2
- 210000000056 organ Anatomy 0.000 description 2
- 229910052573 porcelain Inorganic materials 0.000 description 2
- 238000000247 postprecipitation Methods 0.000 description 2
- 238000011027 product recovery Methods 0.000 description 2
- 238000004062 sedimentation Methods 0.000 description 2
- 239000011265 semifinished product Substances 0.000 description 2
- 239000000377 silicon dioxide Substances 0.000 description 2
- 239000002002 slurry Substances 0.000 description 2
- 239000007858 starting material Substances 0.000 description 2
- 241000282894 Sus scrofa domesticus Species 0.000 description 1
- 229940036811 bone meal Drugs 0.000 description 1
- 239000002374 bone meal Substances 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000001963 growth medium Substances 0.000 description 1
- 210000004072 lung Anatomy 0.000 description 1
- 235000012054 meals Nutrition 0.000 description 1
- 238000009629 microbiological culture Methods 0.000 description 1
- 235000015277 pork Nutrition 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
Images
Landscapes
- Meat, Egg Or Seafood Products (AREA)
- Fodder In General (AREA)
Abstract
A reagent peptone formulation and its preparation method, the formulation is the aggregate of beasts and birds 0.06-80%, animal skin, meat, viscera 15-20%, animal pancreas 4-8%, hydrochloric acid 0.4-0.6%, kaolin 0.7-1%, alcohol, the process is to charge material → high-temperature digestion → discharge soup, discharge oil and slag → pancreatin hydrolysis → hydrochloric acid synthesis → burning soup add pottery clay → skimming slag → fine filtration → concentration → vacuum drying → inspection → pulverize packaging. Its advantages are wide raw material source, half of original process cycle, high output rate increased by 25%, utilization of waste and high economic and social benefits.
Description
The present invention relates to microbiological culture media and biochemical product technical field, know a kind of peptone formula and production technique thereof particularly well.
The prescription of producing peptone only uses the pig bone now, ox bone, and whole dead pig carries out enzymolysis as raw material, whole process needs 76 hours from being dosed into out product, and twice boiling that feed intake put soup twice, mix concentrate drying for twice, all will remove cooking pressure and just can put soup, product recovery rate only 6.8%.This Recipe makes material source, source face narrow, the acquisition cost height, and the process time is tediously long, and product production is low, and recovery rate is low.Product cost height like this, economic benefit is low.
The objective of the invention is to develop a kind of starting material wide material sources, but the prescription of utilization of waste material and production technique, short, the high reagent peptone of producing of output of cycle.
The prescription of reagent peptone of the present invention is:
Livestock and poultry animal aggregate 60～80%.
Animal skin, meat, internal organs official, the bio-pharmaceuticals heart, lung quarrel gurry etc. 15～20%.
The tankage pancreas slag 4～8% of animal pancreas or second enzyme powder manufacturer.
Hydrochloric acid 0.4～0.6%, white bole 0.7～1.0%, alcohol remainder.
Its production technique is as follows:
1, feeds intake
(1) aggregate of two or more livestock and poultry animals is as pig bone, ox bone 60～80%.
(2) pork skin, internal organs, heart quarrel, liver quarrel are mixed use 15～20%.
More than grain mixture behind the order elder generation bone that feeds intake of two things, be convenient to the soup of draining the oil.
2, Jia Shui
About 1.5 times the water that in material, adds weight of material.
3, high temperature steaming
Must not put into the steam of four kilograms of overpressures in the pot body, the intravital pressure of pot must not surpass 2Kg, 6～8 hours pressure cooking time.
4, put soup, drain the oil, deslagging.
Boiling finishes, and keeps 2Kg pressure in the pot body, and band presses soup, drains the oil, and after soup oil drains, removes pot body pressure, and deslagging, soup are done the reagent peptone, but oil refinery worker oil, and slag can be made albumen animal-feed bone meal.
5, pancreatin hydrolysis
(1) with the fresh or bright Pancreas Sus domestica 50Kg that freezes, rub into pancreas slurry, add 6～8% industrial spirit of pancreas weight, place in the earthenware porcelain receptacle, left with 6～24 hours.Made pancreatin like this.
When (2) soup is reduced to 50 ℃, add pancreatin 5% hydrolysis.Hydrolysis whole process soup temperature remains 50 ℃ (± 2 ℃), in the enzymolysis process should every 15 minutes with up and down twist of soup, in order to thorough enzymolysis, enzymolysis time was generally 4 hours.
6, hydrochloric acid is comprehensive:
After enzymolysis finishes, add hydrochloric acid 0.4～0.6%, soup is stirred adding gradually, the pH value of soup is transferred to till 5～7.
7, burn soup, add white bole, cast aside foam
After comprehensively finishing, heating burning soup is promptly cast aside the noodle soup foamy slag to boiling, and the burning soup time was generally 15 minutes, and foam promptly adds white bole 0.7～1% after casting aside totally, allows the soup boiling promptly turn off the heating admission valve in 1 minute again.Make soup natural sedimentation half an hour, make white bole adsorb its silica-based and be deposited at the bottom of the pond.
8, filter just:
The soup of post precipitation is flowed in the filter duck sieve naturally, and filter duck is that general white canvas gets final product.Canvas places compass screen surface, and soup is put into canvas.
9, smart filter:
Through the soup of just considering, by the smart filter of stainless steel sheet frame strainer.
10 concentrate:
Soup after the smart filter enters in the stainless steel concentrating pan, carries out 80 ℃ of cryoconcentration, after cryoconcentration reaches water content and is 40～50%, promptly emits paste.
1, vacuum-drying:
Paste packed into carry out drying in the drying tray, drying temperature is 80 ℃, vacuum tightness 0.8～1.2 negative pressure.Be dried to the work in-process water content and be lower than 5%, get final product outlet.
12, acceptance sampling
Semifinished product warehouse is advanced in i.e. pack behind the work in-process outlet, and sampling chemical examination, reagent peptone must be criticized chemical examination, meet national standard.
13, crushing packing warehouse-in.
Salable product can be ground into diameter less than 3 mm granules shapes, can pack warehouse-in.
Reagent peptone formula of the present invention and production technique advantage are that starting material are very extensive, inexhaustible, and be utilization of waste material, the production technique cycle is short, only needs 36 hours from being dosed into out product, shorten the process cycle time over half, improve output.The product recovery rate also is greatly improved, and improves originally about 25%, and level is in a leading position, technology is very reasonable, saves great amount of manpower and material resources, the energy, and production cost is low, output is 2.5 times of existing producer under the equal conditions, very considerable economic and social benefit.
Below in conjunction with accompanying drawing embodiment is elaborated:
Fig. 1 is for producing the reagent peptone process flow sheet.
Shown in process flow sheet:
1, feed intake:
(1) pig bone, ox bone amount to 800Kg
(2) pigskin, meat, dirty, organ, conscience quarrel mixture 200Kg
More than two kinds of things throw bones earlier in steam cooker, pigskin, meat, dirty, organ, the heart, liver quarrel mixture are dropped in the back.
2, Jia Shui:
In the pot body that material is housed, put into the water that weight is 1500Kg.
3, high temperature steaming:
Steam, the pot body internal pressure of four kilograms of overpressures of must not put in the pot body must not surpass 2Kg, and the pressure cooking time is 7 hours.
4, put soup, drain the oil, deslagging.
Boiling finishes, and protects 2Kg pressure in the pot body, after band presses soup, drains the oil, soup oil drains, removes a pot body pressure, deslagging.But soup is made reagent peptone, oil refinery worker oil, and slag can be done albumen animal-feed meat meal tankage.
5, pancreatin hydrolysis:
(1) with fresh pig pancreas 50Kg, rubs into the pancreas slurry, add the industrial spirit of 4 kilogram of 95% concentration, place in the earthenware porcelain receptacle, left with 12 hours.Make pancreatin like this.
When (2) soup is reduced to 50 ℃, add pancreatin 50Kg hydrolysis.Hydrolysis whole process soup temperature remains 50 ℃ (± 2 ℃), in the enzymolysis process should every 15 minutes with up and down twist of soup, in order to thorough enzymolysis, enzymolysis time is 4 hours.
6, hydrochloric acid is comprehensive:
(1) technical hydrochloric acid seals by adding 5Kg pig hair per ton, with vessel port and deposits more than 7 days and can use.
(2) after enzymolysis finishes, add above-mentioned hydrochloric acid soln 6Kg, add in the soup gradually, and stir soup, the pH value of soup is transferred to till 5～7.
7, burn soup, add carclazyte, cast aside foam
After comprehensively finishing, heating is burnt soup to boiling, promptly casts aside the noodle soup foamy slag, and the burning soup time was generally 15 minutes, foam promptly adds white bole 10Kg after casting aside totally, allows soup seethe with excitement again 10 minutes, promptly turn off the heating admission valve, make soup natural sedimentation half an hour, make white bole adsorb its silica-based and be deposited at the bottom of the pond.
8, filter just:
The soup of post precipitation is flowed in the filter duck sieve naturally, and filter duck is that general white canvas gets final product.Canvas places compass screen surface, and soup is put into canvas.
9, smart filter:
Through the soup of just filtering, by the smart filter of stainless steel sheet frame strainer.
10, concentrate
Soup after the smart filter enters in the stainless concentrating pan, carries out 80 ℃ of cryoconcentration, after a temperature is lower than 80 ℃ of cryoconcentration and reaches water content and be 45% in the pot, promptly emits paste.
11, vacuum-drying:
Paste packed into carry out drying in the drying tray, drying temperature is lower than 80 ℃, and vacuum tightness 0.8～1.2 negative pressure is dried to the work in-process water content and is lower than 5% and gets final product outlet.
12, acceptance sampling:
Behind the work in-process outlet, i.e. pack enters semifinished product warehouse.The sampling chemical examination, the reagent peptone must be criticized chemical examination, meets national standard.
13, crushing packing warehouse-in.
Salable product can be ground into diameter less than 3 mm granules shapes, can pack warehouse-in.
Claims (2)
1, a kind of reagent peptone, it is as follows to it is characterized in that filling a prescription:
Livestock and poultry aggregate: 60～80%
Animal skin, meat, internal organs official, the bio-pharmaceuticals heart, liver slag gurry: 15～20%
Animal pancreas or second enzyme powder manufacturer leftover bits and pieces pancreas slag: 4～8%
Hydrochloric acid 0.4～0.6%
White bole 0.7～1%
The alcohol remainder
2, a kind of reagent peptone is characterized in that production technique is:
Water → high temperature steaming → band 2Kg the pressure that feeds intake → add is put soup, is drained the oil, pressure relief deslagging → pancreatin hydrolysis → hydrochloric acid is comprehensive → and burn soup, add potter's clay, cast aside bubble slag → coarse filtration → essence filter → concentrated → vacuum-drying → check → crushing packing.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 95112530 CN1149627A (en) | 1995-11-08 | 1995-11-08 | Reagent peptone formula and production process thereof |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 95112530 CN1149627A (en) | 1995-11-08 | 1995-11-08 | Reagent peptone formula and production process thereof |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN1149627A true CN1149627A (en) | 1997-05-14 |
Family
ID=5079595
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 95112530 Pending CN1149627A (en) | 1995-11-08 | 1995-11-08 | Reagent peptone formula and production process thereof |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN1149627A (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1318568C (en) * | 2004-06-21 | 2007-05-30 | 锡林郭勒盟金易科工贸有限责任公司 | Protein peptone and production thereof |
| CN102827911A (en) * | 2012-09-24 | 2012-12-19 | 平凉市华科生物技术有限公司 | Preparation method of animal peptone by double-enzyme enzymolysis |
| CN103276038A (en) * | 2013-05-13 | 2013-09-04 | 贵州新华生化科技发展有限公司 | Method for producing reagent grade peptone |
-
1995
- 1995-11-08 CN CN 95112530 patent/CN1149627A/en active Pending
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1318568C (en) * | 2004-06-21 | 2007-05-30 | 锡林郭勒盟金易科工贸有限责任公司 | Protein peptone and production thereof |
| CN102827911A (en) * | 2012-09-24 | 2012-12-19 | 平凉市华科生物技术有限公司 | Preparation method of animal peptone by double-enzyme enzymolysis |
| CN103276038A (en) * | 2013-05-13 | 2013-09-04 | 贵州新华生化科技发展有限公司 | Method for producing reagent grade peptone |
| CN103276038B (en) * | 2013-05-13 | 2015-02-11 | 贵州新华生化科技发展有限公司 | Method for producing reagent grade peptone |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN1100490C (en) | Separation and extraction process of effective component in resource insect | |
| CN108285363A (en) | A kind of method of large size livestock and poultry feces harmless treatment and recycling | |
| CN101076497A (en) | Industrial olive oil mill by-products producing method and resulting products | |
| CN108244402A (en) | It is a kind of suitable for protein sources heavy metal removing agent of mussel and preparation method thereof | |
| CN1070056C (en) | Method to accelerating growth of animal and powdered composite of microbe cells contraining killed fusiform bacillus of bacteria | |
| CN109851446A (en) | A kind of anaerobic fermentation phosphorous compound additive and fermentation process | |
| CN100336832C (en) | Process for extracting comb shell polysaccharide | |
| CN107226636A (en) | A kind of retarder and preparation method thereof | |
| CN1149627A (en) | Reagent peptone formula and production process thereof | |
| CN1537445A (en) | A kind of production method of blood meal feed protein | |
| CN1958781A (en) | Reagent peptone, and preparation method | |
| RU2049084C1 (en) | Process for preparing growth biostimulant from sapropel and/or peat | |
| CN1290428C (en) | Engineered fly biological high-protein powder | |
| CN105265324B (en) | A kind of system and method suitable for the pig raising of mountainous region large-scale ecological | |
| CN1467296A (en) | Feeding spore-forming bacillus microbial preparation-glycopeptide and method for making the same | |
| CN1045276A (en) | Extraction process of drone nutritious composition and uses thereof | |
| CN1071199A (en) | A kind of method of compound zymohydrolysis of silkworm chrysalis protein | |
| CN1288125C (en) | Method of preparing calcium propionate using egg shell | |
| CN1623415A (en) | Multiple composite microbiological protein feed | |
| CN101864364A (en) | A kind of enzymatic hydrolyzate of fish waste protein as a growth regulator of spirulina | |
| RU2780463C1 (en) | Method for processing cellulose-containing waste | |
| CN1403565A (en) | Fermentation process of producing agaric and its culture medium | |
| KR20130053579A (en) | A feed additives and that contain feed composition | |
| SU1703029A1 (en) | Method for processing animal feces into protein-vitamin feed, biogas and fertilizer | |
| CN109348995A (en) | A kind of culture medium of edible fungus and preparation method thereof |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C06 | Publication | ||
| PB01 | Publication | ||
| C12 | Rejection of a patent application after its publication | ||
| RJ01 | Rejection of invention patent application after publication |