CN1415738A - Drying production technique of fluidized bed by starch adsorption of dry oceanic rhodotorula - Google Patents

Drying production technique of fluidized bed by starch adsorption of dry oceanic rhodotorula Download PDF

Info

Publication number
CN1415738A
CN1415738A CN02139178A CN02139178A CN1415738A CN 1415738 A CN1415738 A CN 1415738A CN 02139178 A CN02139178 A CN 02139178A CN 02139178 A CN02139178 A CN 02139178A CN 1415738 A CN1415738 A CN 1415738A
Authority
CN
China
Prior art keywords
rhodotorula
starch
ocean rhodotorula
culture
production technique
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.)
Granted
Application number
CN02139178A
Other languages
Chinese (zh)
Other versions
CN1322109C (en
Inventor
姚娟
谭斌
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.)
Angel Yeast Co Ltd
Original Assignee
Angel Yeast Co Ltd
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 Angel Yeast Co Ltd filed Critical Angel Yeast Co Ltd
Priority to CNB021391785A priority Critical patent/CN1322109C/en
Publication of CN1415738A publication Critical patent/CN1415738A/en
Application granted granted Critical
Publication of CN1322109C publication Critical patent/CN1322109C/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12MAPPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
    • C12M25/00Means for supporting, enclosing or fixing the microorganisms, e.g. immunocoatings
    • C12M25/16Particles; Beads; Granular material; Encapsulation
    • C12M25/20Fluidized bed
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A40/00Adaptation technologies in agriculture, forestry, livestock or agroalimentary production
    • Y02A40/80Adaptation technologies in agriculture, forestry, livestock or agroalimentary production in fisheries management
    • Y02A40/81Aquaculture, e.g. of fish
    • Y02A40/818Alternative feeds for fish, e.g. in aquacultures

Landscapes

  • Micro-Organisms Or Cultivation Processes Thereof (AREA)

Abstract

A starch-adsorption fluidized-bed process for drying the solid marine rhodotorula features use of continuous stream plus deep aeration culture and starch-adsorption fluidized-bed. The resultant has high concentration of rhodotorula cells (5-10 billions/g), high output and high living cell percentage (30%). It can be used to raise prawn and marine crab with high survial rate, health level and raising efficiency.

Description

A kind of starch absorption fluidised bed drying production technique of solid ocean rhodotorula
Technical field
The present invention relates to a kind of production method of ocean rhodotorula, particularly a kind of starch absorption fluidised bed drying production technique of solid ocean rhodotorula.
Background technology
Ocean rhodotorula is widely used at present as a kind of biological feed in growing seedlings of fishery products such as shrimps, crab class, shellfish and the adult breed.Chinese patent discloses a kind of denomination of invention and has been " live single-cell sea red-yeast ecological bait and production method thereof ", and publication number is CN1146290A, and open day is on April 24th, 1997.This invention discloses the production method of ocean rhodotorula yeast culture and liquid product in specification sheets, this method relates to a kind of ocean rhodotorula separates, makes after once feed intake liquid fermenting, the post-processed liquid product from occurring in nature method.This method exists the speed of growth of ocean rhodotorula slow, and the production cycle is long, and the cell concn of the ocean rhodotorula that of fermenting is low, and the final liquid product quality guaranteed period is short, needs refrigeration to wait the shortcoming that is unfavorable for scale operation, prolonged preservation and long-distance transport.
Summary of the invention
The purpose of this utility model is exactly the starch absorption fluidised bed drying production technique that a kind of solid ocean rhodotorula will be provided, its adopts the ventilate method of continuous feeding culture ocean rhodotorula of deep liquid, improved the output of ocean rhodotorula, made it can carry out industrialized production.And on post-processed, adopt starch absorption fluid-bed drying, can obtain having certain active ocean rhodotorula solid phase prod, thereby the quality guaranteed period of ocean rhodotorula product is prolonged, reach the purpose of convenient transportation.
The purpose of this utility model is achieved in that
The microorganism of using
The microbial strains that is used for producing ocean rhodotorula solid phase prod of the present invention is for sticking rhodotorula, and the Latin formal name used at school is Rhodotorula glutinis.The bacterial classification purposes is food and fodder yeast.Bacterial classification is available from Chinese industrial microbial strains preservation center, and deposit number is CGMCC No.2.703.
Glutinous rhodotorula bacterial strain has following character
1, morphological specificity
Circle or oval, individual less, be about 3-4.2*4-5.4um.Microscopically can be seen typical yeast vacuole.
2, the feature on substratum
30 ℃ cultivate inoculation after, observed in 24 hours, in wort liquid is cultivated,, and do not break away from after the polygon budding of cell if it is very slow to leave standstill then growth, a circle Pu shape thing is arranged in the place near liquid level, shake bottle or air agitation fermentation microscopy and then mostly be individual cells.
30 ℃ cultivate inoculation after, observed in 48 hours, the chromatogram (nineteen fifty-seven version) of publishing with Science Press is as the standard of color description.Be the circular bacterium colony of scarlet on the wort agar substratum, the surface is glossy, and neat in edge is opaque, and is long to the few middle bump that has of later stage bacterium.
3, physiological and biochemical property
(1) fermenting carbohydrate: glucose-maltose-semi-lactosi-sucrose-lactose-Mi disaccharides-melizitose-synanthrin-Zulkovsky starch-
(2) assimilation carbon source: glucose+lactose-ethanol-maltose+sucrose+Zulkovsky starch-semi-lactosi-Mi disaccharides-L-arabinose-
(3) assimilation nitrogenous source: saltpetre+ammonium sulfate+urea+Sodium Nitrite-L-Methionin+
(4) assimilation inositol :-
(5) produce the kind of starch compound :-
(6) decomposing urea :+
(7) produce the ester reaction :-
(8) anti-height oozes reaction: 50% glucose+60% glucose-
(9) anti-ethanol: 3%
(10) fatal temperature: 56 ℃
4, utilization of carbon source
Glucose maltose sucrose
The production technique of solid ocean rhodotorula of the present invention may further comprise the steps:
(1) going down to posterity of bacterial classification: bacterial classification adopts the inclined-plane to go down to posterity, and substratum is the wort agar substratum of 8-12Be, and culture temperature is 26 ℃-31 ℃, and incubation time is 26-72 hour, to growing pink circular bacterium colony; Colony diameter is 1-2mm;
(2) strain expanded culture: the bacterial classification of (1) step is connected in the triangular flask of the wort nutrient solution that the sterilized 8-12Be of 150ml is housed, at 26 ℃-31 ℃, carried out under the 100-250rpm condition shake-flask culture 36-48 hour, insert then in the Ka Shi jar of two wort aseptic culture fluids that 20 liters of 8-12Be respectively are housed, 26 ℃ of-31 ℃ of magnetic agitation were cultivated 36-48 hour, again two Ka Shi jar bacterial classifications are inserted in the pure culture fermentor tank that 3-5 ton substratum is housed of having sterilized, 26 ℃ of-31 ℃ of aeration-agitations were cultivated 36-48 hour, and air flow is controlled at 90-130m 3/ hr;
(3) the continuous feeding culture of fermentation deep ventilation: under aseptic condition, the seed liquor of turning out is inserted fermentor tank, 26 ℃-31 ℃ of controlled temperature, aeration-agitation was cultivated 30-48 hour, and air flow is controlled at 90-130m 3/ hr, continuing to flow simultaneously adds carbon source and nitrogenous source.Carbon source is sucrose or glucose, and concentration is 2%-5% (weight ratio), and nitrogenous source is urea, ammonium sulfate or saltpetre, and concentration is 0.1%-0.3% (weight ratio);
(4) separating, washing concentrates: under the separating machine of 3000-5000rpm rotating speed fermented liquid is concentrated, yeast-lactic after concentrating concentrates after dissolving with tap water once more, to with ocean rhodotorula thalline washes clean, the storage tank cryopreservation of the yeast-lactic behind the thickening and washing;
(5) drying: the ocean rhodotorula breast with W-Gum or yam starch and after concentrating is by 2: 1-3: the physical condition homogeneous is mixed, is stirred to 2 (weight ratios); making granularity by nodulizer is 10-60 purpose small-particle; by fluidized-bed in 70 ℃-90 ℃ wind-warm syndrome rapid drying 5-20 minute, get product then.
The culture medium prescription of pure culture fermentor tank and big fermentor tank is: (weight ratio)
Glucose 2-5%
Magnesium sulfate heptahydrate 0.05-0.25%
Yeast extract 0.1-0.3%
Potassium primary phosphate 0.5-1%
Urea 0.1-0.3%
Ammonium sulfate 0.05-0.2%
Saltpetre 0.05-0.2%
PH value 4.0-6.0
The temperature of medium sterilization is 121 ℃, and the time is 30 minutes.
The solid ocean rhodotorula that adopts the present invention to produce has following feature:
1, shape: be by W-Gum or yam starch and the red granules shape material that mixes of the ocean rhodotorula breast after concentrating.
2, size: granularity is the 10-60 order.
3, form: W-Gum or yam starch content are 85%-95% (weight ratio) in the product, and ocean rhodotorula content is 5%-15% (weight ratio).
4, biological activity: the ocean rhodotorula cell concn is 50-100 hundred million/gram in the product, and cytoactive is 10%-30%.
The present invention is owing to adopt the ventilate production method of continuous feeding culture ocean rhodotorula of deep liquid, so that the output of ocean rhodotorula increases substantially, bring up to 20-30 hundred million/ml by original 5-10 hundred million/ml; Owing to adopt starch absorption fluid-bed drying, the liquid ocean rhodotorula after concentrating is dried to the solid ocean rhodotorula again, is keeping having improved the preservation period of product on the certain active basis of ocean rhodotorula like this, and be convenient to transportation.The product that the present invention produces by the result of use in prawn culturing as can be seen, it has improved the state of health of prawn, reduces the mortality ratio of prawn, has improved the quality of prawn, for the shrimp farming has brought economic benefit.
Below with regard to manufacturing of the present invention, the test example illustrate.
Production Example 1
At substratum is on the wort agar substratum test tube slant of 8Be, will stick the rhodotorula bacterial classification and be inoculated on aseptic condition in this substratum, and the control culture temperature is 30 ℃, cultivates 48 hours, and to grow pink circular bacterium colony, colony diameter is 1.5mm.Then above-mentioned bacterial classification is connected under aseptic condition in two 500ml triangular flasks, (dress 150ml wort nutrient solution in the triangular flask) carries out enlarged culturing, 30 ℃ of control culture temperature, and shake-flask culture is 48 hours under 200rpm.Above-mentioned triangular flask bacterial classification is inserted respectively in the Ka Shi jar of two wort aseptic culture fluids that 20 liters of 8Be respectively are housed, 30 ℃ of magnetic agitation were cultivated 48 hours again.At last above-mentioned cultured Ka Shi jar seed is inserted the aerobic fermentation that once feeds intake in the pure culture jar that 5 tons of substratum are housed of having sterilized and cultivate, controlled temperature is 27 ℃, and air flow is 100m 3/ hr, cultivated 48 hours, culture medium prescription is: glucose 2%, magnesium sulfate heptahydrate 0.25%, yeast extract 0.2%, potassium primary phosphate 0.5%, urea 0.3%, ammonium sulfate 0.05%, saltpetre 0.05%, PH are 4.0-6.0, and substratum was sterilized 30 minutes down at 121 ℃.
With 5 tons in above-mentioned seed, all insert in 100 tons the fermentor tank and carry out continuous feeding culture, 27 ℃ of control culture temperature, air flow is 100m 3/ hr, Continuous Flow adds 2% sucrose and 0.3% urea in the cultivation, cultivates 48 hours.Culture medium prescription is: glucose 2%, magnesium sulfate heptahydrate 0.25%, yeast extract 0.2%, potassium primary phosphate 0.5%, urea 0.3%, ammonium sulfate 0.05%, saltpetre 0.05%, PH are 4.0-6.0, and substratum was sterilized 30 minutes down at 121 ℃.After the fermentation ends, fermented liquid is pumped into the high speed butterfly chip separating machine (model is FEUX510, ALFA-LAVAL produce) of import, under the rotating speed of 4000rpm, fermented liquid is concentrated, yeast-lactic after concentrating concentrates after dissolving with tap water once more, can be with ocean rhodotorula thalline washes clean.Yeast-lactic behind the thickening and washing is delivered to the storage tank cryopreservation with transferpump.Ocean rhodotorula breast after 2 tons of W-Gums and 1 ton concentrated mixes; be stirred to the physical condition homogeneous; (model is FLG120 by one-step-granulating method again; luxuriant source pharmaceutical machine factory produces) to make granularity be 30 purpose small-particles; (model is HF20 by fluidized-bed at last; changzhou city medical matters drying plant factory produces); rapid drying is 20 minutes in 70 ℃ wind-warm syndrome; can obtain 2.2 tons of solid ocean rhodotorulas; wherein W-Gum contains 91% (weight ratio); ocean rhodotorula contains 9% (weight ratio); the activity of ocean rhodotorula is 30% in this product, and cell concn reaches 10,000,000,000/gram.
The said products is bundled into 500 gram or 10 kilograms products, is put in shady and cool dry place, can effectively preserve 2 years.
Production Example 2
At substratum is on the wort agar substratum test tube slant of 10Be, will stick the rhodotorula bacterial classification and be inoculated on aseptic condition in this substratum, and the control culture temperature is 26 ℃, cultivates 26 hours, and to grow pink circular bacterium colony, colony diameter is 1mm.Then above-mentioned bacterial classification is connected under aseptic condition in two 500ml triangular flasks, (dress 150ml wort nutrient solution in the triangular flask) carries out enlarged culturing, 26 ℃ of control culture temperature, and shake-flask culture is 36 hours under 100rpm.Above-mentioned triangular flask bacterial classification is inserted respectively in the Ka Shi jar of two wort aseptic culture fluids that 20 liters of 8Be respectively are housed, 26 ℃ of magnetic agitation were cultivated 36 hours again.At last above-mentioned cultured Ka Shi jar seed is inserted the aerobic fermentation that once feeds intake in the pure culture jar that 3 tons of substratum are housed of having sterilized and cultivate, controlled temperature is 26 ℃, and air flow is 90m 3/ hr, cultivated 36 hours, culture medium prescription is: glucose 3.5%, magnesium sulfate heptahydrate 0.15%, yeast extract 0.1%, potassium primary phosphate 0.75%, urea 0.2%, ammonium sulfate 0.1%, saltpetre 0.1%, PH are 4.0-6.0, and substratum was sterilized 30 minutes down at 121 ℃.
With 3 tons in above-mentioned seed, all insert in 100 tons the fermentor tank and carry out continuous feeding culture, 26 ℃ of control culture temperature, air flow is 90m 3/ hr, Continuous Flow adds 3% sucrose and 0.2% urea in the cultivation, cultivates 30 hours.Culture medium prescription is: glucose 3.5%, magnesium sulfate heptahydrate 0.15%, yeast extract 0.1%, potassium primary phosphate 0.75%, urea 0.2%, ammonium sulfate 0.1%, saltpetre 0.1%, PH are 4.0-6.0, and substratum was sterilized 30 minutes down at 121 ℃.After the fermentation ends, fermented liquid is pumped into the high speed butterfly chip separating machine (model is FEUX510, ALFA-LAVAL produce) of import, under the rotating speed of 3000rpm, fermented liquid is concentrated, yeast-lactic after concentrating concentrates after dissolving with tap water once more, can be with ocean rhodotorula thalline washes clean.Yeast-lactic behind the thickening and washing is delivered to the storage tank cryopreservation with transferpump.Ocean rhodotorula breast after 3 tons of W-Gums and 2 tons are concentrated mixes; be stirred to the physical condition homogeneous; (model is FLG120 by one-step-granulating method again; luxuriant source pharmaceutical machine factory produces) to make granularity be 10 purpose small-particles; (model is HF20 by fluidized-bed at last; changzhou city medical matters drying plant factory produces); rapid drying is 10 minutes in 80 ℃ wind-warm syndrome; can obtain 3.4 tons of solid ocean rhodotorulas; wherein W-Gum contains 85% (weight ratio); ocean rhodotorula contains 15% (weight ratio); the activity of ocean rhodotorula is 20% in this product, and cell concn reaches 9,000,000,000/gram.
The said products is bundled into 500 gram or 10 kilograms products, is put in shady and cool dry place, can effectively preserve 2 years.
Production Example 3
At substratum is on the wort agar substratum test tube slant of 12Be, will stick the rhodotorula bacterial classification and be inoculated on aseptic condition in this substratum, and the control culture temperature is 31 ℃, cultivates 72 hours, and to grow pink circular bacterium colony, colony diameter is 2mm.Then above-mentioned bacterial classification is connected under aseptic condition in two 500ml triangular flasks, (dress 150ml wort nutrient solution in the triangular flask) carries out enlarged culturing, 31 ℃ of control culture temperature, and shake-flask culture is 45 hours under 250rpm.Above-mentioned triangular flask bacterial classification is inserted respectively in the Ka Shi jar of two wort aseptic culture fluids that 20 liters of 8Be respectively are housed, 31 ℃ of magnetic agitation were cultivated 45 hours again.At last above-mentioned cultured Ka Shi jar seed is inserted the aerobic fermentation that once feeds intake in the pure culture jar that 4 tons of substratum are housed of having sterilized and cultivate, controlled temperature is 31 ℃, and air flow is 130m 3/ hr, cultivated 45 hours, culture medium prescription is: glucose 5%, magnesium sulfate heptahydrate 0.05%, yeast extract 0.3%, potassium primary phosphate 1.0%, urea 0.1%, ammonium sulfate 0.2%, saltpetre 0.2%, PH are 4.0-6.0, and substratum was sterilized 30 minutes down at 121 ℃.
With 4 tons in above-mentioned seed, all insert in 100 tons the fermentor tank and carry out continuous feeding culture, 31 ℃ of control culture temperature, air flow is 130m 3/ hr, Continuous Flow adds 5% sucrose and 0.1% urea in the cultivation, cultivates 45 hours.Culture medium prescription is: glucose 5%, magnesium sulfate heptahydrate 0.05%, yeast extract 0.3%, potassium primary phosphate 1.0%, urea 0.1%, ammonium sulfate 0.2%, saltpetre 0.2%, PH are 4.0-6.0, and substratum was sterilized 30 minutes down at 121 ℃.After the fermentation ends, fermented liquid is pumped into the high speed butterfly chip separating machine (model is FEUX510, ALFA-LAVAL produce) of import, under the rotating speed of 4000rpm, fermented liquid is concentrated, yeast-lactic after concentrating concentrates after dissolving with tap water once more, can be with ocean rhodotorula thalline washes clean.Yeast-lactic behind the thickening and washing is delivered to the storage tank cryopreservation with transferpump.Ocean rhodotorula breast after 2.5 tons of W-Gums and 1.5 tons are concentrated mixes; be stirred to the physical condition homogeneous; (model is FLG120 by one-step-granulating method again; luxuriant source pharmaceutical machine factory produces) to make granularity be 60 purpose small-particles; (model is HF20 by fluidized-bed at last; changzhou city medical matters drying plant factory produces); rapid drying is 5 minutes in 90 ℃ wind-warm syndrome; can obtain 2.8 tons of solid ocean rhodotorulas; wherein W-Gum contains 95% (weight ratio); ocean rhodotorula contains 5% (weight ratio); the activity of ocean rhodotorula is 10% in this product, and cell concn reaches 5,000,000,000/gram.
The said products is bundled into 500 gram or 10 kilograms products, is put in shady and cool dry place, can effectively preserve 2 years.
Test the effect test of routine product solid ocean rhodotorula of the present invention in Penaeus vannamei is cultured.
Ocean rhodotorula is except that rich in proteins, also have astaxanthin (carotenoid a kind of) and a large amount of unsaturated fatty acidss, be used for aquaculture, can obviously improve the survival rate of output, fishes and shrimps and improve body colour, and can avoid residual in human body of the edible chemical pigment of tradition in culturing, microbiotic and the harm that brings.In order to understand the effect of product solid ocean rhodotorula of the present invention in prawn culturing, we test on the shrimp pool that North Sea group woods biotechnology company limited provides, and situation is as follows:
One, materials and methods
1, experiment pool and contrast pond: select 2 of test tanks, the pond number is 15 #, 16 #, area is respectively 9 mu, 10 mu.2 in pond of contrast, the pond number is 17 #, 18 #, being respectively 9 mu, 11 mu, shrimp pond auxiliary facility and cultivating condition are basic identical.
2, breed variety and putting in a suitable place to breed: breed variety is a Penaeus vannamei, and the shrimp seedling is from local seedling field, puts the date in a suitable place to breed and density sees Table 1
Table 1 test tank is put situation in a suitable place to breed with the contrast pond
Pond number Area Put the date (month, day) in a suitable place to breed Put quantity (ten thousand tails) in a suitable place to breed Mu is put (ten thousand tails)
The contrast pond ????17 # ????9 August 4 calendar year 2001 ????22.5 ????2.5
????18 # ????11 August 4 calendar year 2001 ????27.5 ????2.5
Test tank ????15 # ????9 August 4 calendar year 2001 ????22.5 ????2.5
????16 # ????10 August 4 calendar year 2001 ????25 ????2.5
3, cultural method: press the 2% interpolation product solid ocean rhodotorula of the present invention of feed grain in the daily ration of test tank every day, control group does not add, and other aquaculture management measure is identical.
Two, interpretation of result
A) results situation (seeing Table 2):
Each pond results situation of table 2
Pond number The breed fate (my god) Gross output (kilogram) Per mu yield (kilogram) Survival rate (%) Specification (tail/kilogram)
The contrast pond ????17 # ????101 ????1350 ????150 ????50 ????66
????18 # ????102 ????1672 ????152 ????52 ????67
Test tank ????15 # ????95 ????1440 ????160 ????56 ????60
????16 # ????96 ????1630 ????163 ????58 ????59
B) Economic and Efficiency Analysis: the test tank comparison is according to 10 kilograms of the average mu volume increase in pond, about 6.7%.
C) surviving rate situation analysis: as can be seen from Table 2, volume increase is mainly reflected in the surviving rate raising, illustrates that rhodotorula is strengthening the prawn vigor, has very strong effect on the surviving rate of raising prawn.
D) mature stage analysis: can find out obviously that from table 2 becoming the shrimp specification preferably under the situation, about 6 days of mature stage are shortened in test tank average specific contrast pond.

Claims (7)

1, a kind of solid ocean rhodotorula, it is characterized in that: it is the particulate material that is mixed by W-Gum or yam starch and spissated ocean rhodotorula breast, granularity is the 10-60 order, wherein the content of W-Gum or yam starch is 85%-95% (weight ratio), ocean rhodotorula content is 5%-15% (weight ratio), wherein the ocean rhodotorula cell concn is 50-100 hundred million/gram, and cytoactive is 10%-30%.
2, the starch of a kind of solid ocean rhodotorula according to claim 1 absorption fluidised bed drying production technique, it is characterized in that: it may further comprise the steps:
(1) going down to posterity of bacterial classification: bacterial classification adopts the inclined-plane to go down to posterity, and substratum is the wort agar substratum of 8-12Be, and culture temperature is 26 ℃-31 ℃, and incubation time is 26-72 hour, and to growing pink circular bacterium colony, colony diameter is 1-2mm;
(2) strain expanded culture: the bacterial classification of (1) step is connected in the triangular flask of the wort nutrient solution that the sterilized 8-12Be of 150ml is housed, at 26 ℃-31 ℃, carried out under the 100-250rpm condition shake-flask culture 36-48 hour, insert then in the Ka Shi jar of two wort aseptic culture fluids that 20 liters of 8-12Be respectively are housed, 26 ℃ of-31 ℃ of magnetic agitation were cultivated 36-48 hour, again two Ka Shi jar bacterial classifications are inserted in the pure culture fermentor tank that 3-5 ton substratum is housed of having sterilized, 26 ℃ of-31 ℃ of aeration-agitations were cultivated 36-48 hour, and air flow is controlled at 90-130m 3/ hr;
(3) the continuous feeding culture of fermentation deep ventilation: under aseptic condition, the seed liquor of turning out is inserted fermentor tank, 26 ℃-31 ℃ of controlled temperature, aeration-agitation was cultivated 30-48 hour, and air flow is controlled at 90-130m 3/ hr, continuing to flow simultaneously adds carbon source and nitrogenous source;
(4) separating, washing concentrates: under the separating machine of 3000-5000rpm rotating speed fermented liquid is concentrated, yeast-lactic after concentrating concentrates after dissolving with tap water once more, to with ocean rhodotorula thalline washes clean, the storage tank cryopreservation of the yeast-lactic behind the thickening and washing;
(5) drying: the ocean rhodotorula breast with W-Gum or yam starch and after concentrating is by 2: 1-3: the physical condition homogeneous is mixed, is stirred to 2 (weight ratios); making granularity by nodulizer is 10-60 purpose small-particle; by fluidized-bed in 70 ℃-90 ℃ wind-warm syndrome rapid drying 5-20 minute, get product then.
3, the starch of a kind of solid ocean rhodotorula according to claim 2 absorption fluidised bed drying production technique is characterized in that: bacterial classification is glutinous rhodotorula, and Latin is called Rhodotorule glutinis, and preserving number is CGMCC No.2.703.
4, the starch of a kind of solid ocean rhodotorula according to claim 2 absorption fluidised bed drying production technique, it is characterized in that: carbon source is sucrose or glucose, concentration is 2%-5% (weight ratio).
5, the starch of a kind of solid ocean rhodotorula according to claim 2 absorption fluidised bed drying production technique, it is characterized in that: nitrogenous source is urea, ammonium sulfate or saltpetre, concentration is 0.1%-0.3% (weight ratio).
6, the starch of a kind of solid ocean rhodotorula according to claim 2 absorption fluidised bed drying production technique, it is characterized in that: the culture medium prescription of pure culture fermentor tank and fermentor tank is: (weight ratio)
Glucose 2-5%
Magnesium sulfate heptahydrate 0.05-0.25%
Yeast extract 0.1-0.3%
Potassium primary phosphate 0.5-1%
Urea 0.1-0.3%
Ammonium sulfate 0.05-0.2%
Saltpetre 0.05-0.2%
PH value 4.0-6.0
7, according to the starch absorption fluidised bed drying production technique of claim 2 or 6 described a kind of solid ocean rhodotorulas, it is characterized in that: the temperature of medium sterilization is 121 ℃, and the time is 30 minutes.
CNB021391785A 2002-10-15 2002-10-15 Drying production technique of fluidized bed by starch adsorption of dry oceanic rhodotorula Expired - Fee Related CN1322109C (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CNB021391785A CN1322109C (en) 2002-10-15 2002-10-15 Drying production technique of fluidized bed by starch adsorption of dry oceanic rhodotorula

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CNB021391785A CN1322109C (en) 2002-10-15 2002-10-15 Drying production technique of fluidized bed by starch adsorption of dry oceanic rhodotorula

Publications (2)

Publication Number Publication Date
CN1415738A true CN1415738A (en) 2003-05-07
CN1322109C CN1322109C (en) 2007-06-20

Family

ID=4749935

Family Applications (1)

Application Number Title Priority Date Filing Date
CNB021391785A Expired - Fee Related CN1322109C (en) 2002-10-15 2002-10-15 Drying production technique of fluidized bed by starch adsorption of dry oceanic rhodotorula

Country Status (1)

Country Link
CN (1) CN1322109C (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102676408A (en) * 2012-06-13 2012-09-19 北京大北农科技集团股份有限公司 Method for producing rhodotorula benthica by subsurface fermentation of high-density liquid
CN103374530A (en) * 2012-04-23 2013-10-30 安琪酵母股份有限公司 Semi-dry yeast and preparation method thereof
CN103614307A (en) * 2013-11-13 2014-03-05 中国水产科学研究院南海水产研究所 Solid ocean red yeast preparation as well as preparation method and application thereof
CN104774900A (en) * 2015-05-05 2015-07-15 昌邑市明兴饲料有限责任公司 Technology of using ocean phaffiarodozyma for producing feed additive astaxanthin in fermentation mode
CN105502679A (en) * 2015-01-28 2016-04-20 大连玉兔岛海珍品有限公司 Preparation method for high-activity marine yeast dry powder
CN105792678A (en) * 2013-12-06 2016-07-20 帝斯曼知识产权资产管理有限公司 Biomass formulation

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102919597A (en) * 2012-11-08 2013-02-13 黑龙江省轻工科学研究院 Production method of red-enhancing feed for ornamental red parrot fish

Family Cites Families (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1050975A (en) * 1990-11-13 1991-05-01 沈阳市沈雪饲料加工厂 Refined granular yeast fodder and preparation method
CN1058989A (en) * 1991-08-28 1992-02-26 中国生物工程开发中心宜昌食用酵母基地 Process for refractory alcohol active dried yeast
CN1066290A (en) * 1992-05-21 1992-11-18 宜昌市生物技术研究开发中心 Nutritive element yeast production technique
CN1146290A (en) * 1995-09-27 1997-04-02 王世权 Live single-cell sea red-yeast ecological bait and production method
DE19819475A1 (en) * 1998-04-30 1999-11-04 Basf Ag Dry microorganism cultures and methods for their production

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103374530A (en) * 2012-04-23 2013-10-30 安琪酵母股份有限公司 Semi-dry yeast and preparation method thereof
CN102676408A (en) * 2012-06-13 2012-09-19 北京大北农科技集团股份有限公司 Method for producing rhodotorula benthica by subsurface fermentation of high-density liquid
CN102676408B (en) * 2012-06-13 2016-03-23 北京大北农科技集团股份有限公司 The method of ocean rhodotorula is produced in a kind of high density liquid submerged fermentation
CN103614307A (en) * 2013-11-13 2014-03-05 中国水产科学研究院南海水产研究所 Solid ocean red yeast preparation as well as preparation method and application thereof
CN105792678A (en) * 2013-12-06 2016-07-20 帝斯曼知识产权资产管理有限公司 Biomass formulation
CN105502679A (en) * 2015-01-28 2016-04-20 大连玉兔岛海珍品有限公司 Preparation method for high-activity marine yeast dry powder
CN105502679B (en) * 2015-01-28 2019-02-05 大连玉兔岛海洋生物科技有限公司 The preparation method of high-activity ocean yeast dry powder
CN104774900A (en) * 2015-05-05 2015-07-15 昌邑市明兴饲料有限责任公司 Technology of using ocean phaffiarodozyma for producing feed additive astaxanthin in fermentation mode

Also Published As

Publication number Publication date
CN1322109C (en) 2007-06-20

Similar Documents

Publication Publication Date Title
CN101611767B (en) Method for producing microbial fermentation bait for sea cucumbers
CN1264967C (en) Industrial use of marine fungus fission chytrid OUC88
CN103173371B (en) Production of saccharomyces cerevisiae and lactobacillus acidophilus composite microbe preparation used for feed
CN101078003A (en) Preparation for comprehensive treatment of cultivation water body by using multiple bacterial and manufacturing method thereof
CN108531409B (en) High-density fermentation method of rhodotorula benthica
CN101407761B (en) Liquid inocula composed of yeast fused strain, Geotrichum candidum Link and Rhizopus, and preparation and use thereof
CN114468121B (en) Method for fermenting food industry leftovers by using fermentation agent containing Bacillus belgii
CN1322109C (en) Drying production technique of fluidized bed by starch adsorption of dry oceanic rhodotorula
CN107841464B (en) Algae culture method
CN105969702A (en) Serratia marcescens RZ 21-C6 and application thereof
CN102676408B (en) The method of ocean rhodotorula is produced in a kind of high density liquid submerged fermentation
CN109609384B (en) Chlorella sorokiniana TX strain and high-density rapid culture method thereof
CN108004190B (en) Method for increasing chlorella biomass by using bacillus
CN1179036C (en) Drying production technique by bran adsorption for drying oceanic rhodotorula
CN108085283B (en) method for culturing high-density algae through symbiosis of bacteria and algae
CN1182239C (en) Drying production technique by spraying dry oceanic rhodotorula
CN107746809B (en) Method for increasing algae biomass
CN114381394B (en) Bacillus beiLeisi strain and feed raw material leavening agent for water spider
CN110800888A (en) Composition for culturing plankton, preparation method and application thereof
CN1498865A (en) Micro ecological agent for supporting water in fishing use and its prepn. method
CN104894028A (en) Fishery ocean microbial ecological preparation and preparation method thereof
CN1715399A (en) Process for preparing lichem bacillus strain for producing composite amino acid and culture amino acid liquid fertilizer
CN113136321A (en) Method and system for heterotrophic-autotrophic co-culture of photosynthetic microorganisms and method for production of biomass and bioenergy
CN113136339A (en) Method for mixotrophic-autotrophic continuous culture of photosynthetic microorganisms, culture system and application thereof
CN113136345B (en) Method for heterotrophic-autotrophic continuous cultivation of photosynthetic microorganisms, cultivation system and application thereof

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
C17 Cessation of patent right
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20070620

Termination date: 20121015