CN1524962A - Microorganism catalysis method for producing acrylamide - Google Patents
Microorganism catalysis method for producing acrylamide Download PDFInfo
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- CN1524962A CN1524962A CNA031155367A CN03115536A CN1524962A CN 1524962 A CN1524962 A CN 1524962A CN A031155367 A CNA031155367 A CN A031155367A CN 03115536 A CN03115536 A CN 03115536A CN 1524962 A CN1524962 A CN 1524962A
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Abstract
The invention relates to the field of microorganism technology, wherein a microbiological catalytic process is disclosed for preparing acrylic amide. The process according to the invention realizes the preparation of propanoic acid stick bacillus or its mutagenesis strain cell containing nitrile hydratase through fermentation, then vinyl cyanide water is catalyzed through free cell method or immobilization cell method for synthesizing acrylic amide.
Description
Technical field:
The invention belongs to microbial technology field.Be specifically related to a kind of microorganism catalysis method and produce acrylamide.
Background technology:
Acrylamide is a kind of broad-spectrum Organic Chemicals.
The cyanogen ammonia company of the U.S. in 1964 has at first developed the technology that sulfuric acid hydration process is produced acrylamide, has realized the suitability for industrialized production of acrylamide.But there are problems such as complex process, product purification difficulty, environmental pollution be serious in this technology.The Japan and the U.S. developed simultaneously based on all kinds of process for catalytic hydration of copper and produced acrylamide the beginning of the seventies, and it has compared many advantages with sulfuric acid process, and product purity, transformation efficiency all improve a lot, and be low in the pollution of the environment, and cost is low.
1985, Japanese Ri Dong company adopts the achievement of Kyoto Univ Japan hillside plot research department, has built the type approval test device that first microbial method is in the world produced acrylamide.A strain nitrile hydratase production is also found in 1986 in the Shanghai Pesticide Research Institute from the soil in Mount Taishan bacterial strain, and begun the research that microbial method is produced acrylamide.Microbial method has greater advantage than the copper catalysis method, microbial method can save vinyl cyanide recycle section and copper centrifugal station in whole production technology, and reaction is carried out at normal temperatures and pressures, reduced energy consumption, improved the security of production process, the transformation efficiency of vinyl cyanide can reach 99.99%, does not almost have by product.
Summary of the invention:
The technical problem that solves under the present invention is to overcome above-mentioned weak point, designs the method that a kind of using microbe technology prepares acrylamide.
The invention provides a kind of microorganism catalysis method and produce the method for acrylamide, this method is propionic acid rod bacillus or its mutagenic strain cell that contains Nitrile hydratase by fermentative production, become acrylamide with free cell method or the hydration of immobilized cell method catalyzing propone nitrile under certain condition, then obtain highly purified acrylamide product by comparatively simple aftertreatment.
The specific embodiment of the present invention is as follows:
(1) preparation of zymogenic cells:
Carry out the cultivation of ferment-seeded earlier, the an amount of seed culture medium (10-70%) of in triangular flask or seeding tank, packing into, a certain amount of bacterial classification (1-10%) is inserted in the sterilization back, under 20-40 ℃, in the rotary shaking table (100-400rpm) shaking culture 30-120 hour, perhaps use 50L-2M
3Seeding tank, the inclined-plane seed is inserted in real jar of sterilization back, air flux is 1: 0.2-1: 1 (V.V.M), stirring velocity is 10-400rpm, tank pressure remains on 0.03-0.06mPa, temperature is 20-40 ℃, cultivates 30-200 hour.Then at 50L-20m
3Its fermention medium Intake Quantity of fermentor tank be 40%-70%, the seed liquor of 2-7% is inserted in real jar of sterilization back, at air flow 1: 0.2-1: 1 (V.V.M); Mixing speed: 50-400rpm; Tank pressure 0.03-0.06MP; Temperature: 20-40 ℃.Fermented 30-200 hour;
Seed culture medium is formed: 0.5-2% glucose, 0.2-1% yeast extract paste, 0.05-0.15%Nacl, 0.05-0.3%K
2HPO
4, 0.01-0.03%MgSo
4, urea 0.1-1%, PH7.0-7.5;
Fermention medium: 1-2.5% glucose, 0.2-1% yeast extract paste, 0.1-2% urea, 0.03-0.1%K
2HPO
4, 0.03-0.1%KH
2PO
4, 0.03-0.1%MgSO
4, 2-20ppmCoCl
2, monosodium glutamate 0.04-0.2%, PH6.5-7.5;
(2) cell fixation metallization processes:
With the centrifugal supernatant that goes of fermented liquid, being mixed with bacteria containing amount with sodium alginate soln is 10-35%, sodium alginate is the uniform sizing material of 0.5-4%, splash into the calcium chloride solution of 0.1-0.5M through Fitz chilsonator, at low temperatures after solidifying in 24 hours, clean 2-4 time with distilled water, immobilized cell, the about 1-5mm of diameter, at 4 ℃ of following low temperature stored refrigerated;
(3) free cell catalytic hydration production process:
With fermented liquid in separation factor 〉=3000, centrifugation, remove supernatant liquor, in the damping fluid of deionized water or pure water or PH7.0-8.0, the scale dimension of fermented liquid and reaction solution is held in 〉=1% with cell suspension, under 5-55 ℃ temperature, carry out enzymic catalytic reaction under the stirring velocity of 50-300rpm, in the reaction process, add vinyl cyanide by stream and make concentration of substrate be controlled at 0.001%-10%, through the reaction of 1-24h, obtain concentration at the acrylamide soln more than 10%.Its product solution is accumulated to behind the finite concentration that (〉=10%) is disposable to go out jar, and final transformation efficiency is 〉=99%, vinylformic acid, propenal concentration≤0.0001% in the solution;
(4) immobilized cell catalytic hydration production process:
The immobilized cell that obtains is joined in the damping fluid of deionized water or pure water or PH7.0-8.0, the scale dimension of the immobilized cell and the aqueous solution is held in 〉=and 1%, under 5-55 ℃ temperature, carry out enzymic catalytic reaction under the stirring velocity of 50-300rpm, in the reaction process, add vinyl cyanide by stream and make concentration of substrate be controlled at 0.001%-10%,, obtain concentration at the acrylamide soln more than 10% through the reaction of 1-24h.Its product solution is accumulated to behind the finite concentration that (〉=10%) is disposable to go out jar, and final transformation efficiency is 〉=99%, vinylformic acid, propenal concentration≤0.0001% in the solution.
The Nitrile hydratase that the present invention uses propionic acid rod bacillus and mutagenesis bacterial classification thereof to produce changes into acrylamide with vinyl cyanide, and its operating process is simple, reaction conditions is gentle, reduce environmental pollution, and it is simple to separate purification, the product purity height.
The present invention compared with prior art has following characteristics:
It mainly is the bacterium of Rhod that prior art is used for the bacterial strain that the catalysis nitrile becomes acid amides, and the present invention adopts is propionic acid rod bacillus and through the bacterial classification of mutagenesis.This bacterial classification is contained by this place to separate in the soil of nitrile and obtains, and is propionic acid rod bacillus through preliminary evaluation.This bacterial strain has been stored in China Committee for Culture Collection of Microorganisms common micro-organisms center on January 23rd, 2003, the approaching excellent bacillus Corynebacterium propinguum of classification called after that preservation is registered on the books and is numbered this bacterial strain of CGMCC No.0886..This strain enzyme-producing ability is strong, can obtain higher biomass under fermentation condition of the present invention, reaches as high as 40 mg/ml fermented liquids, thereby total enzyme of its unit volume fermented liquid is alive also higher, reaches as high as 2,400 ten thousand units per ml fermented liquids.(annotate: the enzyme unit definition of living was converted into the vinyl cyanide of 1 microgram the enzyme amount of acrylamide, unit in one hour: microgram/hour).
Embodiment:
Embodiment 1,
At 1m
3Seeding tank in add 60% substratum, after the real jar of sterilization, insert the slant strains of 1 eggplant bottle, the air flow of earlier fermentation is 1: 0.3, stirring velocity is 50rpm, and the air flow in later stage is 1: 0.5, and stirring velocity is 100rpm, tank pressure 0.05mp, 28 ℃ of temperature were cultivated 50 hours.
At 10m
3Fermentor tank in add 60% fermention medium, 5% seed liquor is inserted in real jar of sterilization back, at air flow 1: 0.5 (V.V.M); Tank pressure 0.05MP; Mixing speed: the early stage 180rpm, later stage 100rpm; Temperature: 28 ℃.Fermented 60 hours.
Seed culture medium is formed: 0.6% glucose, 0.4% yeast extract paste, 0.05%K
2HPO
4, 0.05%MgSo
4, 0.05%KH
2PO
4, urea 0.1%, PH7.2
Fermention medium: 2.1% glucose, 0.4% yeast extract paste, 0.9% urea, 0.05%K
2HPO
4, 0.05%KH
2PO
4, 0.1%MgSO
4, 10ppm CoCl
2, monosodium glutamate 0.075%, PH7.5
Embodiment 2,
Is 3500 with 1 ton of fermented liquid at separation factor, centrifugation.Remove supernatant liquor, obtain the cell of about 150kg (weight in wet base).In deionized water, the scale dimension of fermented liquid and reaction solution volume is held in 5% (v/v) with cell suspension.Under 20 ℃ temperature, carry out enzymic catalytic reaction under the stirring velocity of 80rpm.Adding vinyl cyanide by stream maintains about 0.1% concentration of substrate.The ending stage in reaction reduces concentration of substrate thereby no longer add substrate gradually, trends towards zero.After reaction finished, the acrylamide soln concentration that obtains was 32% (w/v), and transformation efficiency is 99.99%.
Embodiment 3,
Is 3500 with 1 ton of fermented liquid at separation factor, centrifugation.Remove supernatant liquor, obtain the cell of about 150kg (weight in wet base).Cell and sodium alginate are hybridly prepared into bacteria containing amount 22%, the uniform sizing material of sodium alginate 2%.Splash into the 0.2M calcium chloride solution through Fitz chilsonator, be incubated 24 hours down at 4 ℃, then use distilled water wash twice, remove residual calcium chloride, 4 ℃ of deepfreezes are preserved.
Embodiment 4,
The immobilized cell that obtains is added in the deionized water, and the scale dimension of immobilized cell and deionized water is held in 3.6%.Under 20 ℃ temperature, carry out enzymic catalytic reaction under the stirring velocity of 80rpm.Adding vinyl cyanide by stream maintains about 0.1% concentration of substrate.The ending stage in reaction reduces concentration of substrate thereby no longer add substrate gradually, trends towards zero.After reaction finished, the acrylamide soln concentration that obtains was 32% (w/v), and transformation efficiency is 99.99%.
Claims (3)
1, a kind of microorganism catalysis method is produced the method for acrylamide, it is characterized in that this method comprises the following steps:
(1) preparation of zymogenic cells:
Carry out the cultivation of ferment-seeded earlier, the seed culture medium of the 10-70% that in triangular flask or seeding tank, packs into, the bacterial classification of 1-10% is inserted in the sterilization back, and under 20-40 ℃, in the rotary shaking table, 100-400rpm shaking culture 30-120 hour, perhaps uses 50L-2M
3Seeding tank, the inclined-plane seed is inserted in real jar of sterilization back, air flux is 1: 0.2-1: 1, V.V.M, stirring velocity is 10-400rpm, tank pressure remains on 0.03-0.06mPa, temperature is 20-40 ℃, cultivates 30-200 hour, then at 50L-20m
3Its fermention medium Intake Quantity of fermentor tank be 40%-70%, the seed liquor of 2-7% is inserted in real jar of sterilization back, at air flow 1: 0.2-1: 1, V.V.M; Mixing speed: 50-400rpm; Tank pressure 0.03-0.06MP; Temperature: 20-40 ℃, fermented 30-200 hour;
Seed culture medium is formed: 0.5-2% glucose, 0.2-1% yeast extract paste, 0.05-0.15%Nacl, 0.05-0.3%K
2HPO
4, 0.01-0.03%MgSo
4, urea 0.1-1%, PH7.0-7.5;
Fermention medium: 1-2.5% glucose, 0.2-1% yeast extract paste, 0.1-2% urea, 0.03-0.1%K
2HPO
4, 0.03-0.1%KH
2PO
4, 0.03-0.1%MgSO
4, 2-20ppmCoCl
2, monosodium glutamate 0.04-0.2%, PH6.5-7.5;
(2) free cell catalytic hydration production process:
With fermented liquid in separation factor 〉=3000, centrifugation, remove supernatant liquor, with cell suspension in the damping fluid of deionized water or pure water or PH7.0-8.0, the scale dimension of fermented liquid and reaction solution is held in 〉=and 1%, under 5-55 ℃ temperature, carry out enzymic catalytic reaction under the stirring velocity of 50-300rpm, in the reaction process, adding vinyl cyanide by stream makes concentration of substrate be controlled at 0.001%-10%, through the reaction of 1-24h, obtain concentration at the acrylamide soln more than 10%, after its product solution is accumulated to finite concentration, 〉=10%, disposablely go out jar, final transformation efficiency is 〉=99%, vinylformic acid in the solution, propenal concentration≤0.0001%.
2, a kind of microorganism catalysis method is produced the method for acrylamide, it is characterized in that this method comprises the following steps:
(1) preparation of zymogenic cells:
Carry out the cultivation of ferment-seeded earlier, the seed culture medium of the 10-70% that in triangular flask or seeding tank, packs into, the bacterial classification of 1-10% is inserted in the sterilization back, and under 20-40 ℃, in the rotary shaking table, 100-400rpm shaking culture 30-120 hour, perhaps uses 50L-2M
3Seeding tank, the inclined-plane seed is inserted in real jar of sterilization back, air flux is 1: 0.2-1: 1, V.V.M, stirring velocity is 10-400rpm, tank pressure remains on 0.03-0.06mPa, temperature is 20-40 ℃, cultivates 30-200 hour, then at 50L-20m
3Its fermention medium Intake Quantity of fermentor tank be 40%-70%, the seed liquor of 2-7% is inserted in real jar of sterilization back, at air flow 1: 0.2-1: 1, V.V.M; Mixing speed: 50-400rpm; Tank pressure 0.03-0.06MP; Temperature: 20-40 ℃, fermented 30-200 hour;
Seed culture medium is formed: 0.5-2% glucose, 0.2-1% yeast extract paste, 0.05-0.15%Nacl, 0.05-0.3%K
2HPO
4, 0.01-0.03%MgSo
4, urea 0.1-1%, PH7.0-7.5;
Fermention medium: 1-2.5% glucose, 0.2-1% yeast extract paste, 0.1-2% urea, 0.03-0.1%K
2HPO
4, 0.03-0.1%KH
2PO
4, 0.03-0.1%MgSO
4, 2-20ppm CoCl
2, monosodium glutamate 0.04-0.2%, PH6.5-7.5;
(2) cell fixation metallization processes:
With the centrifugal supernatant that goes of fermented liquid, being mixed with bacteria containing amount with sodium alginate soln is 10-35%, sodium alginate is the uniform sizing material of 0.5-4%, splash into the calcium chloride solution of 0.1-0.5M through Fitz chilsonator, at low temperatures after solidifying in 24 hours, clean 2-4 time with distilled water, immobilized cell, the about 1-5mm of diameter, at 4 ℃ of following low temperature stored refrigerated;
(3) immobilized cell catalytic hydration production process:
The immobilized cell that obtains is joined in the damping fluid of deionized water or pure water or PH7.0-8.0, the scale dimension of the immobilized cell and the aqueous solution is held in 〉=and 1%, under 5-55 ℃ temperature, carry out enzymic catalytic reaction under the stirring velocity of 50-300rpm, in the reaction process, adding vinyl cyanide by stream makes concentration of substrate be controlled at 0.001%-10%, reaction through 1-24h, obtain concentration at the acrylamide soln more than 10%, after its product solution is accumulated to finite concentration, 〉=10%, disposablely go out jar, final transformation efficiency is 〉=99%, vinylformic acid in the solution, propenal concentration≤0.0001%.
3, a kind of propionic acid rod bacillus, the classification called after that it is characterized in that this bacterial strain be near excellent bacillus, Corynebacterium propinguum, and preservation is registered on the books and is numbered CGMCC No.0886.
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|---|---|---|---|
| CNB031155367A CN1308456C (en) | 2003-02-27 | 2003-02-27 | Microorganism catalysis method for producing acrylamide |
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| CNB031155367A CN1308456C (en) | 2003-02-27 | 2003-02-27 | Microorganism catalysis method for producing acrylamide |
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| CN1308456C CN1308456C (en) | 2007-04-04 |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101130795B (en) * | 2007-07-26 | 2010-05-19 | 武汉三江航天固德生物科技有限公司 | Technique for producing acrylic ester during lactic acid production by zymotechnics |
| CN102286560A (en) * | 2011-06-20 | 2011-12-21 | 山东宝莫生物化工股份有限公司 | Method for continuously producing acrylamide solution by using multi-level membrane bioreactors |
| CN106367447A (en) * | 2016-08-28 | 2017-02-01 | 山东昆达生物科技有限公司 | Preparation method of nicotinamide |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5648889A (en) * | 1979-09-28 | 1981-05-02 | Nitto Chem Ind Co Ltd | Preparation of acrylamide or methacrylamide by fermentation |
| CN1524961A (en) * | 2003-02-27 | 2004-09-01 | 上海双建生化技术发展有限公司 | Microorganism continuous catalysis method for producing acrylamide |
-
2003
- 2003-02-27 CN CNB031155367A patent/CN1308456C/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101130795B (en) * | 2007-07-26 | 2010-05-19 | 武汉三江航天固德生物科技有限公司 | Technique for producing acrylic ester during lactic acid production by zymotechnics |
| CN102286560A (en) * | 2011-06-20 | 2011-12-21 | 山东宝莫生物化工股份有限公司 | Method for continuously producing acrylamide solution by using multi-level membrane bioreactors |
| CN106367447A (en) * | 2016-08-28 | 2017-02-01 | 山东昆达生物科技有限公司 | Preparation method of nicotinamide |
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| CN1308456C (en) | 2007-04-04 |
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Granted publication date: 20070404 Termination date: 20190227 |