CN1147016A - Method for treatment of alpha, omega dibasic acid fermentation liquor - Google Patents
Method for treatment of alpha, omega dibasic acid fermentation liquor Download PDFInfo
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- CN1147016A CN1147016A CN 95116450 CN95116450A CN1147016A CN 1147016 A CN1147016 A CN 1147016A CN 95116450 CN95116450 CN 95116450 CN 95116450 A CN95116450 A CN 95116450A CN 1147016 A CN1147016 A CN 1147016A
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- dibasic acid
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Abstract
A process for separating alpha, omega-biatomic acid from fermented liquid of alpha, omega-biatomic acid comprises directly heating said fermented liquid, filtering to remove bacteria, hot acid crystallizing, filtering and drying, and features high purity of product and low cost of operation.
Description
The present invention relates to a kind of method of from the normal alkane fermented liquid, extracting α, omega-dibasic acid.
α, omega-dibasic acid are to utilize microorganism fermentation n-paraffins, particularly long-chain normal alkane and the meta-bolites that obtains.Its fermented liquid is the heterogeneous system of a complexity, contains the intact normal alkane (Residual oil) of unreacted, microorganism cells, the water and the oil-water emulsion body of meta-bolites and the various substratum that do not utilized.As seen the processing of α, omega-dibasic acid fermented liquid has very big difficulty than other fermented liquid.Therefore, selecting which kind of treatment process is to influence α, omega-dibasic acid quality product, and yield and even whole technique are through one of key of economy.Nippon Mining Co. Ltd. has proposed to separate the method for α, omega-dibasic acid, and has applied for patent JP56-260193, JP56-260194.Its treatment process is to stop fermented liquid to leave standstill under alkaline condition, and bactofugation adds diatomite adsorption unreacted reactant and byproduct of reaction, filters, and the acid out crystallization is filtered, and drying obtains α, omega-dibasic acid crystal at last.The subject matter that aforesaid method exists is that the fermented liquid alkalization is left standstill and had the somatic cells self-dissolving, intracellular protein is flowed in the fermented liquid, thereby influence product purity, and because the cell adhesiveness increase, increased the difficulty of filtering separation.The cold conditions acid out is adopted in crystallization, the method for rising temperature for dissolving then, and crystal size is little, and difficulty in filtration is big, and product color is difficult to remove.
The objective of the invention is in order to overcome above-mentioned shortcoming, find a kind of simple and effectively α, omega-dibasic acid stop the processing and the separation method of fermented liquid, separating thallus fast and effeciently, the step that simplifies the operation improves product yield and quality.
The present invention finishes by following steps:
1, will stop α, omega-dibasic acid fermented liquid direct heating earlier to 50-100 ℃ of breakdown of emulsion, after constant temperature leaves standstill 3～5 hours, be cooled to 30～40 ℃, after leaving standstill again 3 hours, the Separation and Recovery unreacted reactant.
2, separated the flocculating aids that adds 2～5% (W/W) in the fermented liquid of unreacted reactant, under 30～40 ℃ of temperature, the back press filtration that stirs, filter finish after, wash the bacterium cake with water to neutral, and washing lotion be recovered in the filtrate.
3, second filtrate that obtains of step is heated to 60～95 ℃, with the mineral acid of 4～10N transfer PH to 4 or below, the acid out nucleation of α, omega-dibasic acid is led to cooling water temperature to 20～40 ℃ then, can obtain the crystal than volume particle size.
4, the brilliant liquid filtered while hot that the 3rd step was obtained, being washed with water to filtrate PH afterwards is 5～7, the α that obtains wetting, omega-dibasic acid filter cake.
5, under 40～80 ℃ of temperature, use the warm air drying filter cake, obtain that outward appearance is white in color, the α of purity＞95%, omega-dibasic acid product.
In this fermented liquid, extract before α, the omega-dibasic acid, reclaim Residual oil at first fully to reduce the loss in subsequent step.Before this termination fermented liquid did not deal with, Residual oil and water existed with the form of emulsified body, and directly separation is very difficult, reclaims Residual oil so must carry out breakdown of emulsion by pre-treatment.The present invention is with the termination fermented liquid, is heated to 50-100 ℃, and preferably 80～100 ℃, constant temperature left standstill 3 hours, was cooled to 30～40 ℃ then, left standstill 3 hours again.Oil in water emulsion and water can be emanated well like this, and its Oil residue recuperation rate can reach more than 95%.
Through above thermal treatment, albumen is subjected to thermocoagulation in the thalline bag, makes the easier filtration of fermented liquid after the oil removing.The present invention adds the flocculating aids of 2～5% (W/W) in the oil removing fermented liquid, 100～200 purpose pearlite filtering aids particularly, 30～40 ℃ of temperature, 0.1-0.2MPa down, press filtration, particularly by microfiltration membrane during as filtration medium, its unit surface filtration velocity is filtered than alternate manner and is improved 1～2 times at least, and filtrate is as clear as crystal.
Filtrate after the degerming is alkalescence, and α, omega-dibasic acid are present in the filtrate with the form of salt (main sodium salt).In order to be easy to filter after obtaining the higher α of purity, omega-dibasic acid and making the acid out crystallization, the present invention is under 60～95 ℃ of conditions, hot acid out nucleation, PH reduce to 4 or below, preferably 3.5, however cooling is reduced to 20～40 ℃, preferably 35 ℃, crystallization obtains the higher α of purity, omega-dibasic acid crystal, and crystal size is bigger 8～10 times than direct acid out under the normal temperature, makes the product filtration velocity improve greatly like this.After product filtered and finishes, being washed with water to the filtrate pH value was 5～7, promptly obtains α, omega-dibasic acid wet cake.This wet cake is after extrusion, section or fragmentation, and is dry down 40～80 ℃ of temperature, is preferably 50～80 ℃.
Handle through above method, obtain at last that outward appearance is white in color, purity is greater than 95% α, omega-dibasic acid product.
Compared with the prior art the present invention has following advantage:
1. α, omega-dibasic acid are stopped fermented liquid and adopt direct-fired method, make that albumen is subjected to thermocoagulation in the thalline bag, avoided " water-based albumen " cytoclasis and flow in the fermented liquid, thereby influence quality product.
2. be subjected to thermoset somatic cells,, make the thalline filtering separation be more prone to because of its rigidity increases, even under low pressure (＜0.2MPa) also can realize quick filtration.
3. to removing the filtrate of thalline, adopt hot acid out nucleation, the method that cools, the granularity of α, omega-dibasic acid increases, and is easy to filter, and the processing of need not decolouring, and can obtain outward appearance the be white in color higher α of purity, omega-dibasic acid product.
Specify the present invention below by embodiment.
Embodiment 1:
Make substrate with the n-tridecane hydrocarbon, produce the termination fermented liquid of α, ω-tridecanyldicarboxylic acid with the fermentation of candida tropicalis variant.Unreacted reactant content is 11.5% in the fermented liquid, and bacteria concentration is 10g/L, and acid concentration is 105g/L, and pH value is 7.6.Get 1000 milliliters of above-mentioned fermented liquids, be heated to 95 ℃, constant temperature left standstill 3.5 hours, was cooled to 38 ℃, reclaimed the upper strata unreacted reactant then.Separated in the fermented liquid of unreacted reactant, added 20 gram pearlite filtering aids, the back that stirs 5-10 μ m microporous membrane filtered while hot, starting pressure is 0.02MPa, boosts to 0.2MPa after 5 minutes.After filtering end, wash to reclaim α, the ω-tridecanyldicarboxylic acid salt in the bacterium cake with 300 ml waters.Above-mentioned filtrate is put into crystallizer for 500 milliliters, be heated to 90 ℃, slowly add the acid of 6N stream, make pH value reduce to 3.5, be cooled to 36 ℃ again, filtered while hot, use the tap water washing leaching cake to neutral afterwards, promptly obtaining purity is 95.3%, the α that outward appearance is white in color, ω-tridecanyldicarboxylic acid product.Embodiment 1 the results are shown in Table 1.
Table 1.
| The Oil residue recuperation rate | Thalline micro-filtration speed | The product filtering velocity | DC13 purity | Product yield |
| ????％(V/V) | ??L/m 2.h | ??L/m 2.h | ??％(w/w) | ??％(w/w) |
| ????95.2 | ????50 | ????90 | ????96 | ????94 |
Embodiment 2:
Handle α, ω-mixed dibasic acid.Stopping fermentation unreacted reactant content is 10%, and bacterium is dense to be 15g/L, and acid is dense to be 110g/L, and pH value is 7.8.Get above-mentioned fermented liquid 1000ml, be heated to 75 ℃, after constant temperature leaves standstill 4 hours, be cooled to 30 ℃, reclaim the upper strata unreacted reactant then.Add the 25g perlite in having reclaimed the fermented liquid of unreacted reactant, with 10～20 μ m micro-pore-film filtrations, operation steps is with embodiment 1 after stirring.Above-mentioned filtrate 500ml is put into crystallizer be heated to 75 ℃, crystallisation process is operated with embodiment 1.The wet cake that crystallization obtains is dry under 50 ℃, and promptly obtaining purity is 94.7%, the α that outward appearance is white in color, ω-mixed dibasic acid product.Embodiment 2 the results are shown in Table 2.
Table 2.
Embodiment 3:
| The Oil residue recuperation rate | Thalline micro-filtration speed | The product filtering velocity | DC 13Purity | Product yield |
| ????％(V/V) | ????L/mU.h | ??L/m 2.h | ??％(w/w) | ????％(w/w) |
| ????93.6 | ????65 | ????86 | ????94.7 | ????92.9 |
Handle α, ω-ten four-carbon dicarboxylic acids.Stopping fermentation unreacted reactant content is 9%, and bacterium is dense to be 13g/L, and acid is dense to be 95g/L, and pH value is 8.0.Get above-mentioned fermented liquid 1000ml, be heated to 60 ℃, after constant temperature leaves standstill 4 hours, be cooled to 30 ℃, reclaim the upper strata unreacted reactant then.Add the 25g perlite in having reclaimed the fermented liquid of unreacted reactant, with 10～20 μ m micro-pore-film filtrations, operation steps is with embodiment 1 after stirring.Above-mentioned filtrate 500ml is put into crystallizer be heated to 60 ℃, crystallisation process is operated with embodiment 1.The wet cake that crystallization obtains is dry under 50 ℃, and promptly obtaining purity is 94.7%, the α that outward appearance is white in color, ω-mixed dibasic acid product.Embodiment 3 the results are shown in Table 3.
Table 3.
| The Oil residue recuperation rate | Thalline micro-filtration speed | The product filtering velocity | DC 13Purity | Product yield |
| ????％(V/V) | ????L/m 2.h | ????L/m 2.h | ％(w/w) | ％(w/w) |
| ????94.4 | ????64 | ????102.3 | ????95.8 | ????93.9 |
The present invention shows: α, omega-dibasic acid are stopped fermented liquid Residual oil system, adopt aforesaid method, can fully reclaim the Residual oil in the fermented liquid, simultaneously through steps such as heat filtering degerming, can fast and effeciently isolate α, omega-dibasic acid product, simplify treatment step, reduced processing costs, be undoubtedly a kind of desirable method.
Claims (6)
1, a kind of method of handling α, omega-dibasic acid fermented liquid is characterized in that: a, α, omega-dibasic acid are stopped fermented liquid be heated to 50-100 ℃ and carry out breakdown of emulsion, separate unreacted reactant, filtration sterilization; B, 60-95 ℃ of acid out crystallization; C, brilliant liquid filter; D, product drying.
2,, it is characterized in that it is 80 ℃-100 ℃ that a step stops the fermentation liquor pretreatment temperature according to the method for claim 1.
3, according to the method for claim 1, when it is characterized in that b step acid out crystallization, temperature is 80-95 ℃, transfer again PH to 4 or below, cool then to 20～40 ℃.
4, according to the method for claim 1, when it is characterized in that c step is filtered α, omega-dibasic acid crystal, wash to the filtrate pH value be 5～7.
5, according to the method for claim 1, when it is characterized in that the d step is dry, temperature is between 40～80 ℃.
6, according to the method for claim 1, the carbonatoms that it is characterized in that α, omega-dibasic acid is 10～18, can be α, omega-dibasic acid, also can be any mixed dibasic acid.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN95116450A CN1049688C (en) | 1995-10-05 | 1995-10-05 | Method for treatment of alpha, omega dibasic acid fermentation liquor |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN95116450A CN1049688C (en) | 1995-10-05 | 1995-10-05 | Method for treatment of alpha, omega dibasic acid fermentation liquor |
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| CN1147016A true CN1147016A (en) | 1997-04-09 |
| CN1049688C CN1049688C (en) | 2000-02-23 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN95116450A Expired - Lifetime CN1049688C (en) | 1995-10-05 | 1995-10-05 | Method for treatment of alpha, omega dibasic acid fermentation liquor |
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Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1056882C (en) * | 1996-10-09 | 2000-09-27 | 中国石油化工总公司抚顺石油化工研究院 | Process for preparing high purity long chain dicarboxylic acid and its ester |
| CN1079389C (en) * | 1998-12-03 | 2002-02-20 | 中国石油化工集团公司 | Process for refining long-chain biatomic acid |
| CN103805275A (en) * | 2012-11-08 | 2014-05-21 | 中国石油化工股份有限公司 | Fermentation carbon source recycling method |
| CN103805643A (en) * | 2012-11-07 | 2014-05-21 | 中国石油化工股份有限公司 | Production method for long-chain dicarboxylic acids |
| CN106673995A (en) * | 2015-11-09 | 2017-05-17 | 中国石油化工股份有限公司 | Method for refining long-chain dicarboxylic acids |
| CN106673996A (en) * | 2015-11-09 | 2017-05-17 | 中国石油化工股份有限公司 | Method for purifying long-chain dicarboxylic acid |
Family Cites Families (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5611797A (en) * | 1979-07-06 | 1981-02-05 | Mitsui Petrochem Ind Ltd | Purification of dicarboxylic acid |
| JPS5626193A (en) * | 1979-08-09 | 1981-03-13 | Nippon Mining Co Ltd | Removal of microbial cell from fermentation broth of long-chain dicarboxylic acid |
| JPS57102191A (en) * | 1980-12-16 | 1982-06-25 | Mitsui Petrochem Ind Ltd | Separating method of dicarboxylic acid |
| CN1026129C (en) * | 1989-04-27 | 1994-10-05 | 中国石油化工总公司 | Process for producing long-chain alpha, omega-dicarboxylic acid from orthoalkanes by microbe fermentation |
| CN1029842C (en) * | 1991-09-11 | 1995-09-27 | 中国石油化工总公司抚顺石油化工研究院 | Method for refining long-chain binary acid |
| CN1030146C (en) * | 1994-01-28 | 1995-10-25 | 中国科学院微生物研究所 | Method of preparation long chain a,w-dicarboxylic acid with microorganism fermentation n-paraffins |
-
1995
- 1995-10-05 CN CN95116450A patent/CN1049688C/en not_active Expired - Lifetime
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1056882C (en) * | 1996-10-09 | 2000-09-27 | 中国石油化工总公司抚顺石油化工研究院 | Process for preparing high purity long chain dicarboxylic acid and its ester |
| CN1079389C (en) * | 1998-12-03 | 2002-02-20 | 中国石油化工集团公司 | Process for refining long-chain biatomic acid |
| CN103805643A (en) * | 2012-11-07 | 2014-05-21 | 中国石油化工股份有限公司 | Production method for long-chain dicarboxylic acids |
| CN103805643B (en) * | 2012-11-07 | 2016-04-27 | 中国石油化工股份有限公司 | A kind of method of producing long-chain biatomic acid |
| CN103805275A (en) * | 2012-11-08 | 2014-05-21 | 中国石油化工股份有限公司 | Fermentation carbon source recycling method |
| CN103805275B (en) * | 2012-11-08 | 2016-02-03 | 中国石油化工股份有限公司 | A kind of method that fermenting carbon source is recycled |
| CN106673995A (en) * | 2015-11-09 | 2017-05-17 | 中国石油化工股份有限公司 | Method for refining long-chain dicarboxylic acids |
| CN106673996A (en) * | 2015-11-09 | 2017-05-17 | 中国石油化工股份有限公司 | Method for purifying long-chain dicarboxylic acid |
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| CN1049688C (en) | 2000-02-23 |
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Owner name: CHINA PETROCHEMICAL CORPORATION; CHINA PETROLEUM & Free format text: FORMER NAME OR ADDRESS: CHINA PETRO-CHEMICAL CORP.; FUSHUN PETROCHEMICAL INSTITUTE., CHINA PETROCHEMICAL CORP. |
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Patentee after: China Petrochemical Group Corp. Patentee after: Sinopec Group Fushun Research Institute of Petroleum and Petrochemicals Patentee before: China Petrochemical Corporation Patentee before: Fushun Research Inst. of Petroleum Processing, China Petro-chem. Corp. |
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