CN1069180C - Process for low-salt solid closed circulation fermentation of soy sauce - Google Patents

Process for low-salt solid closed circulation fermentation of soy sauce Download PDF

Info

Publication number
CN1069180C
CN1069180C CN97125865A CN97125865A CN1069180C CN 1069180 C CN1069180 C CN 1069180C CN 97125865 A CN97125865 A CN 97125865A CN 97125865 A CN97125865 A CN 97125865A CN 1069180 C CN1069180 C CN 1069180C
Authority
CN
China
Prior art keywords
soy sauce
residue
soya
hydrolyzate
technology
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.)
Expired - Fee Related
Application number
CN97125865A
Other languages
Chinese (zh)
Other versions
CN1183240A (en
Inventor
蔡木易
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
CHINESE FOOD FERMENT INDUSTRIAL INST
Original Assignee
CHINESE FOOD FERMENT INDUSTRIAL INST
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by CHINESE FOOD FERMENT INDUSTRIAL INST filed Critical CHINESE FOOD FERMENT INDUSTRIAL INST
Priority to CN97125865A priority Critical patent/CN1069180C/en
Publication of CN1183240A publication Critical patent/CN1183240A/en
Application granted granted Critical
Publication of CN1069180C publication Critical patent/CN1069180C/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Landscapes

  • Soy Sauces And Products Related Thereto (AREA)
  • Preparation Of Compounds By Using Micro-Organisms (AREA)

Abstract

The present invention belongs to the preparation of food or foodstuff, namely, a process for the low-salt solid closed circulation fermentation of soy sauce. The process is characterized in that the process is combined with the existing process for biodegradation protein of soy sauce raw materials; small quantities of salt in soy residues, residual protein and certain quantities of fermented intermediate products are returned to the production as secondary raw materials for changing waste into valuables; therefore, resource waste and environmental pollution are reduced, and the yield and the utilization rate of raw materials are increased. The color, the mouth feel and the amino acid components of the soy sauce produced by the present invention are all superior to those of the soy sauce produced by the existing process.

Description

Process for low-salt solid closed circulation fermentation of soy sauce
The invention belongs to the preparation of food or foodstuff, i.e. flavoring soy sauce preparation technology.
Soy sauce is as China's traditional condiment, and the technology that present domestic most factories adopt is the exclusive low salt solid state fermentation of China.This technology is bacterial classification with aspergillus oryzae shanghai brewing 3042, and defatted soybean, wheat bran are raw material, under solid state fermentation conditions, adds 15% salt solution and makes the sauce unstrained spirits.After the fermentation of sauce unstrained spirits, after three pouring systems, obtain soy sauce crude oil.Crude oil obtains finished product after the allotment sterilization, residue of soya is as waste discharge.In fact, in residue of soya, contain many compositions that are not decomposed.Contain the bulk fermentation intermediate product simultaneously.And at present, the soy sauce industry is directly discharged residue of soya as discarded object owing to there is not rational treatment process, has not only wasted resource but also cause environmental pollution.
Purpose of the present invention is exactly on the basis of existing technology, make full use of and contain a small amount of salt, residual protein and a certain amount of fermentation intermediate product in the residue of soya, residue of soya is carried out chemistry and biological dual processing, making residue of soya return to be used for producing as secondary raw material goes, turn waste into wealth, to reduce the waste and the environmental pollution of resource, improved original zymotechnique greatly, improved raw material availability and yield rate.
The technology of the present invention solution is: the existing raw material biodegradation of soy sauce protein technology is combined with residue of soya acid protein hydrolysats matter technology, the residue of soya that produces behind the sauce fermentation through resulting protein hydrolyzate after the acid hydrolysis again after carrying out a biological disposal upon secondary enter in the sweat the carrying out that participates in fermentation, and then form optimum close circulation technology.
Technological process of the present invention is as follows: accompanying drawing is soy sauce low-salt solid close circulation technology flow chart one, soy sauce preparation technology:
With defatted soybean, wheat bran is raw material, and with 6: 4 or ratio mixing in 5: 5, general ratio was 6: 4.According to this ratio, can calculate the basis (seeing Table 1) of soy sauce mixed material by the normal composition of dregs of beans and wheat bran.
Table 1 raw materials of soy sauce fundamental component
Unit Dregs of beans Wheat bran 6: 4 mixed materials
Moisture content 10 12 10.8
Crude protein 46 15 33.6
Crude fat 1.5 4.7 2.78
Crude fibre 5.4 9.0 6.84
NFE 32.6 5.5 21.76
Ash 5 6.6 5.64
Dregs of beans is mixed → material moistening → steaming material → cooling → inoculation (aspergillus oryzae 3042 → triangular flask → koji tray expansion) → koji → Cheng Qu → pulverizing → system unstrained spirits → heat-preservation fermentation → ripe sauce unstrained spirits → head with wheat bran and drench oil, two pouring oil, three pouring oil (residue of soya).
Above technology is prior art, its technological parameter, condition, and inoculum concentration is known.Two, residue of soya is handled:
All kinds of nutrition compositions are complete in the residue of soya, and protein content is higher, and existing fermentation intermediate product has excessive albuminate again in the protein component.(the residue of soya composition sees Table 2)
Table 2 residue of soya composition
Project Unit Content Project Unit Content
Moisture content 14 Glycine mg/100g 1242.92
Crude protein 29.5 Alanine mg/100g 1443.21
Crude fibre 15.2 The figured silk fabrics nitronic acid mg/100g 449.43
Crude fat 1.82 Methionine mg/100g 1542.36
NFE 32.32 Isoleucine mg/100g 1108.26
Calcium 0.7 Leucine mg/100g 2329.62
Phosphorus 0.57 Tyrosine mg/100g 1094.83
Taurine mg/100g 110.01 Phenylalanine mg/100g 1509.61
Asparatate mg/100g 2653.14 Ornithine mg/100g 136.41
Threonine mg/100g 1094.60 Lysine mg/100g 1406.66
Serine mg/100g 1297.87 Histidine mg/100g 518.07
Glutamic acid mg/100g 4099.74 Tryptophan mg/100g /
Proline mg/100g 1312.64 Arginine mg/100g 1296.00
1. residue of soya is entered in the hydrolytic reaction pot, with concentration be 36% hydrochloric acid allocate to the reactant liquor concentration of hydrochloric acid be 10%, feed Steam Heating, treat that cold air arrange closed reactor afterwards.2. work as reacting kettle inner pressure and rise to 1.2kg/cm 2Back pressurize, reaction temperature are 110-125 ℃, and the reaction time is 24 hours.Question response finishes to stop heating, feeds cooling water, reduces to room temperature.3. hydrolyzate is filtered with being pumped in the diaphragm pressing machine, filtrate is sent into neutralization bucket, uses NaCO 3Or NaOH is neutralized to PH4.8-5.4, and water content is in the use that acts as a fuel of 45% filter cake, and filtrate enters next step biological treatment.4. be that bacterial classification leaves standstill cultivation 7-15 days with the above-mentioned amino acid hydrolyticsolution of producing from the acid hydrolysis mode under 30 ℃ with the soy sauce aroma-producing yeasts, carry out a biological disposal upon.5. hydrolyzate adds finished product Daqu heat-preservation fermentation, and fermentation condition is with existing technology.Be fermentation time 25 days, early stage, the product temperature was 48-50 ℃, 41-45 ℃ of later stage product temperature.6. ripe sauce unstrained spirits drenches oily method with existing technology.7. residue of soya returns in the production as secondary raw material through the present invention's processing and goes, and forms a benign cycle zymotechnique.8. filter the humus that obtains after the residue of soya hydrolysis and can be used as fuel.Residue of soya hydrolyzate amino acid composition sees Table 3.
Table 3 residue of soya hydrolyzate amino acid analysis of components
Project Unit Content Project Unit Content
Salt g/100ml 14.15 Glycine mg/100g 172.4
Total solid g/100ml 33.59 Alanine mg/100g 185.8
Salt-less solid g/100ml 19.44 Valine mg/100g 244.8
Full nitrogen g/100ml 0.87 Methionine mg/100g 25.3
Reduced sugar g/100ml 0.24 Isoleucine mg/100g 174.2
Total acid g/100ml 0.44 Leucine mg/100g 338.5
Ammonia nitrogen g/100ml 0.456 Tyrosine mg/100g 76.5
Total amino acid content mg/100g 3267.2 Phenylalanine mg/100g 151.1
Asparatate mg/100g 293.1 Ornithine mg/100g /
Threonine mg/100g 109.8 Lysine mg/100g 111.3
Serine mg/100g 156.3 Histidine mg/100g 59.2
Glutamic acid mg/100g 556.0 Tryptophan mg/100g /
Proline mg/100g 333.4 Arginine mg/100g 199.4
Residue of soya hydrolyzate reuse secondary fermentation technology and the contrast of common process soy sauce composition see Table 4.
Table 4 residue of soya hydrolyzate reuse secondary fermentation technology and the contrast of common process soy sauce analysis of components
Project Unit Control group Test group
Salt g/100ml 12.24 14.92
Total solid g/100ml 33.0 38.7
Salt-less solid g/100ml 20.76 23.78
Full nitrogen g/100ml 1.08 1.10
Reduced sugar g/100ml 3.0 1.2
Total acid g/100ml 2.27 1.85
Ammonia nitrogen g/100ml 0.55 0.68
Total amino acid content mg/100g 3471.74 4895.11
Asparatate mg/100g 240.92 400.32
Threonine mg/100g 100.81 192.61
Serine mg/100g 152.74 249.80
Glutamic acid mg/100g 381.67 583.10
Proline mg/100g 280.20 554.82
Glycine mg/100g 66.65 120.44
Alanine mg/100g 221.20 263.69
Valine mg/100g 220.96 335.69
Methionine mg/100g 72.76 83.81
Isoleucine mg/100g 182.29 290.24
Leucine mg/100g 331.91 453.59
Tyrosine mg/100g 144.92 192.04
Phenylalanine mg/100g 213.30 312.99
Ornithine mg/100g
Lysine mg/100g 183.45 236.54
Histidine mg/100g 45.95 60.06
Tryptophan mg/100g
Arginine mg/100g 389.72 348.47
The present invention processes processing to the residue of soya in the soy sauce production, make a small amount of salt in the residue of soya, residual protein and a certain amount of fermentation intermediate product return in the production as secondary raw material and go, to reduce the waste and the environmental pollution of resource, improve original zymotechnique, improved the yield rate and the utilization rate of raw material.The present invention compares koji part technology and does not adjust with existing technology, sauce unstrained spirits fermentation part adopts the residue of soya hydrolyzate water instead of salt system unstrained spirits after biological treatment, and sauce unstrained spirits fermentation condition is identical with existing technology with pouring system technology.With the soy sauce of this explained hereafter, its colourity, mouthfeel, the amino acid composition all is better than existing technology.
The embodiment of the invention: one, the preparation of soy sauce:
Ratio in prior art dregs of beans and wheat bran is 6: 4, dregs of beans is mixed → material moistening → steaming material → cooling → inoculation (aspergillus oryzae 3042 → triangular flask → koji tray expansion) koji → Cheng Qu → pulverizing → system unstrained spirits → heat-preservation fermentation → ripe sauce unstrained spirits → head with wheat bran and drenches oil, two pouring oil, three pouring oil (residue of soya).After the above process using closed cycle, except that system unstrained spirits process using residue of soya hydrolyzate water instead of salt, other is prior art, and its consumption, technological parameter are known.Two, residue of soya is handled: 1. get residue of soya and enter in the hydrolytic reaction pot for one ton, with concentration be 36.0% food grade hydrochloric acid allocate to the reactant liquor concentration of hydrochloric acid be 10.0%, feed steam, treat that cold air arranged closed reactor afterwards.2. work as reacting kettle inner pressure and rise to 1.2kg/cm 2Back pressurize, reaction temperature are 120 ℃, and the reaction time is 24 hours.Stop heating after question response is reached home, feed cooling water and reduce to room temperature.3. hydrolyzate is filtered with being pumped in the diaphragm pressing machine, filtrate is sent into neutralization bucket, uses NaCO 3Be neutralized to PH5.0, about amount of filtrate 1.0-1.2 ton, water content is in the use that acts as a fuel of 45% filter cake (about 150kg), and filtrate enters down the step biological treatment.4. the above-mentioned amino acid hydrolyticsolution of producing from the acid hydrolysis mode being added with soy sauce aroma-producing yeasts (not lattice torulopsis Toruiopsis mogii) with 2% inoculum concentration be the Yeast Cultivation liquid of bacterial classification, leaves standstill cultivation 10 days under 30 ℃.Carry out a biological disposal upon.Soy sauce aroma-producing yeasts (not lattice torulopsis Toruiopsis mogii) is known bacterial classification, and it enlarges cultural method together
The Saccharomyces cerevisiae cultural method is a known technology.5. get 1.2 tons of hydrolyzates, add 1.5 tons in finished product Daqu, carry out heat-preservation fermentation, fermentation condition is with existing technology.Be fermentation time 25 days, early stage, the product temperature was 48 ℃, 41 ℃ of later stage product temperature.6. generate the sauce unstrained spirits and drench oil, its method is with existing technology.Respectively drench oil, two to the end and drench oil, three and drench oil, also have residue of soyas.7. the head that obtains drenches oil, two pouring oil, three drench oil and enter down the step process blended soy sauce, and residue of soya turns back in the production as secondary raw material by PROCESS FOR TREATMENT of the present invention and goes, and forms an optimum closed cycle zymotechnique.8. the humus of residue of soya is a filter cake, can be used as fuel combustion.

Claims (2)

1. a soy sauce preparation method process for low-salt solid closed circulation fermentation of soy sauce, it is characterized in that raw materials of soy sauce biodegradation protein technology combines with residue of soya acid protein hydrolysats matter technology, residue of soya hydrolyzate after the acidolysis enters in the sweat after biological treatment once more, form optimum close circulation technology, its residue of soya technological process is as follows:
1) residue of soya enters in the hydrolytic reaction pot, with concentration be 36.0% hydrochloric acid allocate to the reactant liquor concentration of hydrochloric acid be 10.0%, feed steam, cold air arrange closed reactor afterwards;
2) reacting kettle inner pressure rises to 1.2kg/cm 2Pressurize, reaction temperature are 110-125 ℃, and the reaction time is 24 hours, and reaction finishes to stop heating, feeds cooling water, reduces to room temperature;
3) hydrolyzate filters with being pumped in the diaphragm pressing machine, and filtrate is sent into neutralization bucket, uses NaCO 3Or NaOH is neutralized to PH4.8-5.4;
4) hydrolyzate with the yeast be bacterial classification under 30 ℃, leave standstill and cultivated 7-15 days;
5) add Daqu and hydrolyzate, heat-preservation fermentation, (with existing technology);
6) ripe sauce unstrained spirits drenches system → head pouring oil, two pouring oil, three drench oily (residue of soya), with having technology now;
7) residue of soya returns in the production as secondary raw material by the present invention's processing and goes.
2. zymotechnique according to claim 1 is characterized in that: hydrolyzate adds the soy sauce aroma-producing yeasts with 2% inoculum concentration.
CN97125865A 1997-12-25 1997-12-25 Process for low-salt solid closed circulation fermentation of soy sauce Expired - Fee Related CN1069180C (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN97125865A CN1069180C (en) 1997-12-25 1997-12-25 Process for low-salt solid closed circulation fermentation of soy sauce

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN97125865A CN1069180C (en) 1997-12-25 1997-12-25 Process for low-salt solid closed circulation fermentation of soy sauce

Publications (2)

Publication Number Publication Date
CN1183240A CN1183240A (en) 1998-06-03
CN1069180C true CN1069180C (en) 2001-08-08

Family

ID=5177452

Family Applications (1)

Application Number Title Priority Date Filing Date
CN97125865A Expired - Fee Related CN1069180C (en) 1997-12-25 1997-12-25 Process for low-salt solid closed circulation fermentation of soy sauce

Country Status (1)

Country Link
CN (1) CN1069180C (en)

Families Citing this family (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101756159B (en) * 2009-12-15 2012-07-04 佛山市海天调味食品股份有限公司 Soy sauce desalting method
CN103478676A (en) * 2013-09-25 2014-01-01 千禾味业食品股份有限公司 Multiple fermentation process for soybean sauce
CN104381964B (en) * 2014-12-04 2016-05-18 滕州市鼎盛酿造有限责任公司 A kind of soy sauce biological enzymolysis zymotechnique
CN104757502B (en) * 2014-12-10 2016-11-02 山东玉兔食品有限责任公司 High-salt dilute soy squeezing system and squeezing process thereof
CN112042920A (en) * 2020-10-22 2020-12-08 安徽省农业科学院农产品加工研究所 Circulating system for spraying oil in soy sauce production process

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1114868A (en) * 1994-07-14 1996-01-17 胡于鲁 Technology of production of soy by improved hydrolysis method
CN1155996A (en) * 1995-11-27 1997-08-06 王听林 Method for producing soy sauce using sauce dregs as raw material

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1114868A (en) * 1994-07-14 1996-01-17 胡于鲁 Technology of production of soy by improved hydrolysis method
CN1155996A (en) * 1995-11-27 1997-08-06 王听林 Method for producing soy sauce using sauce dregs as raw material

Also Published As

Publication number Publication date
CN1183240A (en) 1998-06-03

Similar Documents

Publication Publication Date Title
CN101012471B (en) Method for extracting rice bran protein by complex enzyme
CN100392092C (en) Soybean peptide production method
CN1026457C (en) Flavouring agent
CN111920031B (en) Brewing method of selenium-rich soy sauce with high glutamic acid content
CN103937846B (en) A kind of method utilizing cotton cake dregs to prepare Moriamin S
CN102239930A (en) Method for preparing fragrant peanut oil
CN101787382A (en) Method for recovering coin protein sugar dregs and preparing protein nitrogen sources and nitrogen-containing syrup
CN101717807B (en) Process for preparing chicken liver hydrolyzed protein with proteases
CN102212107A (en) Rice protein polypeptide and preparation method thereof
CN112674318A (en) Method for improving color, fragrance and taste of soy sauce based on soybeans and wheat
CN108902676A (en) Wheat-based polypeptide and modified starch compounding wheat analogies and preparation method thereof
CN110326770A (en) A kind of production method that improved Flaxseed cake makes functional soy sauce and salty sauce
CN1069180C (en) Process for low-salt solid closed circulation fermentation of soy sauce
CN103045705A (en) Method for producing protein peptide composed of fish protein peptide and soybean peptide
CN102086466A (en) Almond functional hybrid peptide and preparation method thereof
CN103642885A (en) Method for producing wheat biological active peptide by fermentation
CN1895661A (en) Preparation of cotton-seed polypeptide with anti-oxidant function
CN107653289A (en) A kind of industrialized production kardiseed active peptide and preparation method
CN102150806A (en) Method for producing novel ossein flavor powder through ultrasonic auxiliary spray drying
CN1235504C (en) Method for producing nutritious sauce from glutamic acid tropina
CN106497997A (en) A kind of method that haemachrome is produced by the enzymatic isolation method that interlocks
CN110973581A (en) Preparation method and application of delicious soy sauce
CN1174689C (en) Soy sauce of black wheat and its brewing process
CN1063024A (en) The production method of a kind of baste and extraction glutamic acid
CN101653234A (en) Manufacturing method of mung bean soy sauce

Legal Events

Date Code Title Description
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C06 Publication
PB01 Publication
C14 Grant of patent or utility model
GR01 Patent grant
C19 Lapse of patent right due to non-payment of the annual fee
CF01 Termination of patent right due to non-payment of annual fee