CN1184306C - Method for producing single cell protein using residue in extracting steroid sepogenin - Google Patents
Method for producing single cell protein using residue in extracting steroid sepogenin Download PDFInfo
- Publication number
- CN1184306C CN1184306C CNB031173187A CN03117318A CN1184306C CN 1184306 C CN1184306 C CN 1184306C CN B031173187 A CNB031173187 A CN B031173187A CN 03117318 A CN03117318 A CN 03117318A CN 1184306 C CN1184306 C CN 1184306C
- Authority
- CN
- China
- Prior art keywords
- yeast
- residue
- cell protein
- bacterial classification
- single cell
- 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
Links
Landscapes
- Micro-Organisms Or Cultivation Processes Thereof (AREA)
- Preparation Of Compounds By Using Micro-Organisms (AREA)
Abstract
The present invention discloses a method for producing single cell protein by using residue in extracting steroid sepogenin, which comprises strain selection, strain production and single cell protein production. The method is characterized in that the following yeast group of strain pseudocyst yeast, trichocyst yeast, candida, grease yeast, Hansenula yeast, Endomycopsis fibuligera yeast and alcohol yeast is selected as strains. After the strains are enlarged and cultivated by an agar slant culture-medium, a test tube, an erlenmeyer flask and a malt extract medium, the strains are cultured by a mother tank, a breeding tank and a workshop in an enlargement mode to obtain producing strains. After all the strains are mixed, the strains are added to residue sterilized by high pressure as solid for fermentation at a temperature from 28 to 32 DEG C. The obtained material is discharged in 5 to 7 days, and the single cell protein is obtained after ripening and puff drying. The single cell protein uses residue for producing steroid sapogenin, the environment pollution of the waste residue is reduced, and waste changes into valuable. The high quality single cell protein is produced through residue.
Description
Technical field:
The present invention relates to a kind of method for producing protein, especially a kind of method of utilizing the residue manufacture order cell protein that extracts steroid sapogenines.
Background technology:
In producing the steroid sapogenines process, can produce the residue of larger amt as everyone knows, contain a large amount of starch and other nutritive substance in this residue, past, this polytrophic material completely was abandoned, not only waste resource in a large number, but also contaminate environment, single cell protein is the best protein source of feeding animals simultaneously, therefore how using tankage in a large amount of depleted steroid saponin production processes to produce single cell protein paid close attention to by people, people also once carried out repaying examination in this respect, but because the problem that selection and process aspect exist is not seen the report that success is arranged always.
Content of the present invention:
The objective of the invention is to overcome the prior art deficiency, a kind of method of utilizing the residue manufacture order cell protein that extracts steroid sapogenines is provided, the object of the invention realizes by following technical proposals:
1. select following yeast flora to make bacterial classification
False capsule yeast Eremotnecium trichosporon Trichosporon.spp
Candiyeast Candida utilis saccharomyces oleaginosus Lipomyces.spp
Spore yeast Endomycopsis in debaryomyces hansenii Hansenula.spp button capsule is intended
Distillery yeast Alcoholyeast
2. bacterial classification production, above-mentioned each bacterial classification is obtained the production bacterial classification through mother's jar cultivation, the cultivation of breeding jar, workshop enlarged culturing respectively again after agar slant culture-medium, test tube, triangular flask, malt extract medium enlarged culturing, female jar, breeding jar and workshop enlarged culturing are all used improved malt extract medium; It is the residue that adds the 10-50% weight part in the malt extract medium, the residue that adds the 10-20% weight part in wherein female jar substratum, the residue that adds the 30-40% weight part in the breeding jar substratum, the residue of adding 50% weight part in the Workshop Production bacterium culture medium.Bacterial classification is produced routinely the yeast production technique and is carried out, and each stage incubation time was at 18-36 hour, and temperature is carried out under 25-32 ℃ of condition.Bacterial classification content is generally at 20-30 hundred million/ml, with the above-mentioned bacterial classification mixing for standby use of respectively producing.Each bacterial classification mixing consumption is false capsule yeast: trichosporon: false trichosporon: saccharomyces oleaginosus: debaryomyces hansenii: buckle capsule and intend interior spore yeast: the clear yeast of wine=1: 0.9-1.2: 0.9-1.2: 0.9-1.2: 0.9-1.2: 0.9-1.2: the 0.9-1.2 weight ratio,
3. single cell protein production, the residue that steroid saponin is produced is behind autoclaving, add composite bacteria, mix the back and add cold boiling water, and transfer PH to 5-5.5, residue: bacterial classification: cold boiling water=100: 4-6 with 10% hydrochloric acid solution: the 60-80 weight ratio, insert in the fermentation tower with the wet temperature control of control and make solid fermentation, temperature is 28-32 ℃, and the time is 5-7 days.When viable count reaches hundred million of 20-30/gram, get final product discharging, be single cell protein behind slaking, the explosion puffing drying, can make the feed of feeding animals, consider transportation, storage and easy to use, can with above-mentioned single cell protein again row pulverize the back and make by shaper.
The present invention has chosen that thalli growth speed is fast in the steroid sapogenines residue, fecundity is strong, the productive rate height, and the synthetic protein ability is strong, the protein content height, omnivory is strong, can make full use of in the residue nutrition and have the barms that adapts to the low substratum of PH.
The residue that the present invention has not only utilized steroid sapogenines to produce, the waste residue environmental pollution of minimizing is turned waste into wealth, and the single cell protein quality height of producing by residue.Single cell protein nutrition such as table 1 and each seed amino acid produced of the present invention after testing, vitamin contents sees Table 2.
Table 1 composite yeast bacterium manufacture order cell protein nutrition table
Composition | Moisture content | Crude protein | Crude fat | But digestibility | Robust fibre | Ash content |
Quantity (g/100g) | 6 | 41 | 2.3 | 35.1 | 5.6 | 7.3 |
Amino acid, the vitamin contents table of table 2 composite yeast manufacture order cell protein
Title | Content (amino acid g/100g) (VITAMIN mg/kg) | Title | Content (amino acid g/100g) (VITAMIN mg/kg) |
Aspartic acid | 5.3 | Isoleucine | 2.4 |
Threonine | 2.9 | Leucine | 4 |
Serine | 2.3 | Tyrosine | 1.6 |
L-glutamic acid | 7.8 | Phenylalanine | 2.1 |
Glycine | 2.6 | Methionin | 3.3 |
L-Ala | 4.5 | Histidine | 1.01 |
Gelucystine | 0.35 | Arginine | 3.01 |
Xie Ansuan | 4.2 | Tryptophane | 0.43 |
Methionine(Met) | 1.1 | Proline(Pro) | 1.2 |
Vitamins B 1 | 6.1 | Vitamin B6 | 17 |
Vitamins B 2 | 46.8 | Vitamin B7 | 1.4 |
Vitamins B 3 | 69 | Folic acid | 3.1 |
Vitamins B 4 | 2853 | Vitamins B 12 | 0.06 |
Vitamin PP | 485 |
Embodiment:
Embodiment 1:
1, choose and cultivate the capable enlarged culturing of bacterial classification, choose false capsule yeast, trichosporon, candiyeast, saccharomyces oleaginosus, debaryomyces hansenii, spore yeast in the button capsule is intended, distillery yeast is made the bacterial classification provenance, each bacterial classification respectively earlier on the plain agar slant medium 30 ℃ cultivate 24 hours after, be inoculated into enlarged culturing in test tube and the triangular flask malt extract medium successively, bacterial classification after the enlarged culturing is by little female jar, big female jar and breeding jar be enlarged culturing again, be to produce by the workshop enlarged culturing at last and use bacterial classification, little female jar, big female jar, breeding jar and workshop enlarged culturing, all use improved malt extract medium, add 10% weight part residue in the little female jar of malt extract medium, add 20% weight part residue in the big female jar of wort, the breeding jar adds and adds 30-40% weight part residue in the malt extract medium, add wort 50% weight part residue in the substratum of Workshop Production, every kind of cultivation was all cultivated 18-36 hour at 30 ℃, present embodiment selects for use female jar to cultivate 18 hours, and breeding jar was cultivated 24 hours workshop enlarged culturing 36 hours.
2, various cultured production bacterial classifications are pressed 1: 0.9-1.2: 0.9-1.2: 0.9-1.2: 0.9-1.2: 0.9-1.2: 0.9-1.2 weight ratio, it is standby that compound bacterial classification is made in mixing, and it is 1: 0.9: 1.2 that present embodiment is selected weight ratio for use: 1.2: 1.1: 0.9: 1.2.
3, will extract the white tankage of steroid sapogenines after sterilising treatment, add composite bacteria and cold water, sterilized water is better, and with extract spent acid solution that steroid saponin produced transfer PH in 5 (with 10% hydrochloric acid also can), tankage: composite bacteria: water=100: 5: 70 weight ratios mix in the fermentation tower that is placed on the wet temperature control of control and make solid fermentation, fermentation humidity is controlled at 85-90%, and leavening temperature is controlled at 30 ℃, and fermentation time is 6 days.General mensuration gets final product discharging when total viable count reaches hundred million of 20-30/gram, steam slaking in 1 hour through 100 ℃ again, insert the bulking machine explosion puffing drying again and be single cell protein, consider transportation and easy to use, the single cell protein that present embodiment is good with drying is pulverized and is granulated.
Embodiment 2:
1, choose and cultivate the capable enlarged culturing of bacterial classification, choose false capsule yeast, trichosporon, candiyeast, saccharomyces oleaginosus, debaryomyces hansenii, spore yeast in the button capsule is intended, distillery yeast is made the bacterial classification provenance, each bacterial classification respectively earlier on the plain agar slant medium 32 ℃ cultivate 24 hours after, be inoculated into enlarged culturing in test tube and the triangular flask malt extract medium successively, bacterial classification after the enlarged culturing is by little female jar, little female jar, big female jar, breeding jar and workshop enlarged culturing, all use improved malt extract medium, add 10% weight part residue in the little female jar of malt extract medium, add 20% weight part residue in the big female jar of wort, the breeding jar adds and adds 30-40% weight part residue in the malt extract medium, add wort 50% weight part residue in the substratum of Workshop Production, big female jar and breeding jar enlarged culturing, be to produce by the workshop enlarged culturing at last and use bacterial classification, every kind of cultivation was all cultivated 18-36 hour at 32 ℃, present embodiment selects for use female jar to cultivate 20 hours, and breeding jar was cultivated 36 hours workshop enlarged culturing 24 hours.
2, with various cultured production bacterial classifications by 1: 1.2: 0.9: 0.9: 0.9: 1.1: 1.2 weight ratios mixed that to make compound bacterial classification standby.
3, will extract the white tankage of steroid sapogenines after sterilising treatment, add composite bacteria and cold water, and with extract spent acid solution that steroid saponin produced transfer PH in 5.5 (with 10% hydrochloric acid also can), tankage: composite bacteria: water=100: 6: 80 weight ratios, mix in the fermentation tower that is placed on the wet temperature control of control and make solid fermentation, fermentation humidity is controlled at 85-90%, and leavening temperature is controlled at 30 ℃, and fermentation time is 6 days.General mensuration when total viable count reaches hundred million of 20-30/gram gets final product discharging, through 100 ℃ of steamings slaking in 1 hour, inserts the bulking machine explosion puffing drying again and is single cell protein again.
Embodiment 3:
1, choose and cultivate the capable enlarged culturing of bacterial classification, choose false capsule yeast, trichosporon, candiyeast, saccharomyces oleaginosus, debaryomyces hansenii, spore yeast in the button capsule is intended, distillery yeast is made the bacterial classification provenance, each bacterial classification earlier on the plain agar slant medium 25 ℃ cultivate 24 hours after, be inoculated into enlarged culturing in test tube and the triangular flask malt extract medium successively, bacterial classification after the enlarged culturing is by little female jar, big mother's jar and breeding jar cultivation, be to produce by the workshop enlarged culturing at last and use bacterial classification, little female jar, big female jar, breeding jar and workshop enlarged culturing, all use improved malt extract medium, add 10% weight part residue in the little female jar of malt extract medium, add 20% weight part residue in the big female jar of wort, the breeding jar adds and adds 30-40% weight part residue in the malt extract medium, add wort 50% weight part residue in the substratum of Workshop Production, every kind of cultivation was all cultivated 18-36 hour at 25 ℃, present embodiment selects for use female jar to cultivate 18 hours, and breeding jar was cultivated 24 hours workshop enlarged culturing 36 hours.
2, with various cultured production bacterial classifications by 1: 1.1: 1.1: 1.2: 1.1: 1.2: 0.9 weight ratio mixed that to make compound bacterial classification standby.
3, will extract the white tankage of steroid sapogenines after sterilising treatment, add composite bacteria and cold water, and with extract spent acid solution that steroid saponin produced transfer PH in 5.3 (with 10% hydrochloric acid also can), tankage: composite bacteria: water=100: 4: 60 weight ratios, mix in the fermentation tower that is placed on the wet temperature control of control and make solid fermentation, fermentation humidity is controlled at 85-90%, and leavening temperature is controlled at 30 ℃, and fermentation time is 6 days.General mensuration when total viable count reaches hundred million of 20-30/gram gets final product discharging, through 100 ℃ of steamings slaking in 1 hour, inserts the bulking machine explosion puffing drying again and is single cell protein again.Consider transportation and easy to use, the single cell protein that present embodiment is good with drying is pulverized and is granulated.
Embodiment 4:
1, choose and cultivate the capable enlarged culturing of bacterial classification, choose false capsule yeast, trichosporon, candiyeast, saccharomyces oleaginosus, debaryomyces hansenii, spore yeast in the button capsule is intended, distillery yeast is made the bacterial classification provenance, each bacterial classification respectively earlier on the plain agar slant medium 29 ℃ cultivate 24 hours after, be inoculated into enlarged culturing in test tube and the triangular flask malt extract medium successively, bacterial classification after the enlarged culturing is by little female jar, big mother's jar and breeding jar cultivation, be to produce by the workshop enlarged culturing at last and use bacterial classification, little female jar, big female jar, breeding jar and workshop enlarged culturing, all use improved malt extract medium, add 10% weight part residue in the little female jar of malt extract medium, add 20% weight part residue in the big female jar of wort, the breeding jar adds and adds 30-40% weight part residue in the malt extract medium, add wort 50% weight part residue in the substratum of Workshop Production, every kind of cultivation was all cultivated 18-36 hour at 28 ℃, present embodiment selects for use female jar to cultivate 18 hours, and breeding jar was cultivated 24 hours workshop enlarged culturing 36 hours.
2, with various cultured production bacterial classifications by 1: 1: 1: 1: 1: 1: 1 weight ratio mixed that to make compound bacterial classification standby.
3, will extract the white tankage of steroid sapogenines after sterilising treatment, add composite bacteria and cold water, and with extract spent acid solution that steroid saponin produced transfer PH in 5.4 (with 10% hydrochloric acid also can), tankage: composite bacteria: water=100: 5: 70 weight ratios, mix in the fermentation tower that is placed on the wet temperature control of control and make solid fermentation, fermentation humidity is controlled at 85-90%, and leavening temperature is controlled at 30 ℃, and fermentation time is 6 days.General when measuring total viable count and reaching hundred million of 20-30/gram, get final product discharging, through 100 ℃ of steamings slaking in 1 hour, insert the bulking machine explosion puffing drying again and be single cell protein again.
Claims (1)
1, a kind of method of utilizing the residue manufacture order cell protein that extracts steroid sapogenines comprises bacterial classification selection, bacterial classification production and single cell protein production, it is characterized in that:
1. select following yeast flora to make bacterial classification
False capsule yeast Eremotnecium trichosporon Trichosporon.spp
Candiyeast Candida utilis saccharomyces oleaginosus Lipomyces.spp
Spore yeast Endomycopsis in debaryomyces hansenii Hansenula.spp button capsule is intended
Distillery yeast Alcoholyeast
2. bacterial classification production, with above-mentioned each bacterial classification respectively through agar slant culture-medium, test tube, triangular flask, cultivate through female jar again after the malt extract medium enlarged culturing, breeding jar cultivation, the workshop enlarged culturing is obtained the production bacterial classification, female jar, breeding jar and workshop enlarged culturing are all used improved malt extract medium, promptly female jar, add 10-20% respectively in the malt extract medium of breeding jar and workshop enlarged culturing, residue after 30-40% and 50% weight part steroid sapogenines extract, each stage incubation time was at 18-36 hour, temperature is carried out under 25-32 ℃ of condition, with the above-mentioned bacterial classification mixing for standby use of respectively producing, each bacterial classification mixing consumption is false capsule yeast: trichosporon: false trichosporon: saccharomyces oleaginosus: debaryomyces hansenii: buckle capsule and intend interior spore yeast: the clear yeast of wine=1: 0.9-1.2: 0.9-1.2: 0.9-1.2: 0.9-1.2: 0.9-1.2: 0.9-1.2 weight ratio;
3. single cell protein production, the residue that steroid saponin is produced is behind autoclaving, add composite bacteria, mix the back and add cold boiling water, and transfer PH to 5-5.5, residue: bacterial classification: cold boiling water=100: 4-6: 60-80 weight ratio with 10% hydrochloric acid solution, insert in the fermentation tower with the wet temperature control of control and make solid fermentation, temperature is 28-32 ℃, and the time is discharging in 5-7 days, is single cell protein behind slaking, the explosion puffing drying.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CNB031173187A CN1184306C (en) | 2003-02-18 | 2003-02-18 | Method for producing single cell protein using residue in extracting steroid sepogenin |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CNB031173187A CN1184306C (en) | 2003-02-18 | 2003-02-18 | Method for producing single cell protein using residue in extracting steroid sepogenin |
Publications (2)
Publication Number | Publication Date |
---|---|
CN1434125A CN1434125A (en) | 2003-08-06 |
CN1184306C true CN1184306C (en) | 2005-01-12 |
Family
ID=27634333
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CNB031173187A Expired - Fee Related CN1184306C (en) | 2003-02-18 | 2003-02-18 | Method for producing single cell protein using residue in extracting steroid sepogenin |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN1184306C (en) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103849575B (en) * | 2014-03-05 | 2017-12-15 | 南昌大学 | A kind of production method of single cell protein |
-
2003
- 2003-02-18 CN CNB031173187A patent/CN1184306C/en not_active Expired - Fee Related
Also Published As
Publication number | Publication date |
---|---|
CN1434125A (en) | 2003-08-06 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US20160374364A1 (en) | Method of and system for producing a high value animal feed additive from a stillage in an alcohol production process | |
CN101074426B (en) | Method for producing bean-dregs feed containing conjugated linolic acid by plant lactobacillin fermentation | |
Nangul et al. | Microorganisms: a marvelous source of single cell proteins | |
CN102217708B (en) | Novel environment-friendly feed additive and preparation method thereof | |
CN102687792A (en) | Feeding microecologic preparation based on beer grains and rice bran meal | |
CN101940267A (en) | Method for preparing microbial fermentation feed for improving pork quality | |
Yalemtesfa et al. | Solid substrate fermentation and conversion of orange waste in to fungal biomass using Aspergillus niger KA-06 and Chaetomium Spp KC-06 | |
CN102334611A (en) | Solid-state fermentation method for bacillus natto-saccharomycete composite viable bacteria preparation with rice bran as matrix | |
CN101692869B (en) | Method for producing high protein bean pulp based on two-step microbial fermentation | |
US20200109428A1 (en) | Process for producing high protein biomass from starch-containing cereal materials by yeast strains | |
CN103468594A (en) | Candidautilis strain and application thereof | |
Rages et al. | Alkaline hydrolysis of olive fruits wastes for the production of single cell protein by Candida lipolytica | |
CN107535671A (en) | Improve the microbial fermentation yellow wine lees feed and preparation method of ruminal protein utilization rate | |
CN103820339A (en) | Dehydrated solid composite microbial agent capable of increasing albumen level of cassava residue and preparation method of dehydrated solid composite microbial agent | |
CN113243450A (en) | Method for improving quality of mushroom bran feed through multi-strain mixed fermentation | |
CN113892556B (en) | Biological protein feed prepared from waste distillers' grains of Jimo old wine and preparation method thereof | |
CN1247103C (en) | Mixed solid fermentation and straw puffing process to prepare protein feed | |
CN111248340A (en) | Traditional Chinese medicine solid fermentation product and preparation method and application thereof | |
CN1449673A (en) | Single cell protein fodder and preparation process thereof | |
CN102337225A (en) | Preparation method of high-nitrogen fresh yeast and extract | |
Ginting | Comparison of isolate dadih with yeast dadih in improving nutrition quality of Cassava Waste (CW) | |
CN101690541A (en) | Method for preparing feed protein from microbial fermented silkworms | |
Kurbanoglu | Enhancement of glycerol production with ram horn hydrolysate by yeast | |
CN116283377A (en) | Fruit and vegetable waste composting fermentation method and application thereof | |
CN1184306C (en) | Method for producing single cell protein using residue in extracting steroid sepogenin |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C06 | Publication | ||
PB01 | Publication | ||
C10 | Entry into substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
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 |