CN1421525A - Hygrophilous monad and its application - Google Patents
Hygrophilous monad and its application Download PDFInfo
- Publication number
- CN1421525A CN1421525A CN 01134576 CN01134576A CN1421525A CN 1421525 A CN1421525 A CN 1421525A CN 01134576 CN01134576 CN 01134576 CN 01134576 A CN01134576 A CN 01134576A CN 1421525 A CN1421525 A CN 1421525A
- Authority
- CN
- China
- Prior art keywords
- acid
- producing
- aeromonas hydrophila
- hygrophilous
- multipolymer
- 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
Links
Landscapes
- Preparation Of Compounds By Using Micro-Organisms (AREA)
- Micro-Organisms Or Cultivation Processes Thereof (AREA)
Abstract
The present invention is hygrophilous aeromonad and its application in producing 3-hydroxy butyric acid and 3-hydroxy caproic acid copolymer. The hygrophilous aeromonad of the present invention is hygrophilous aeromonad 45/90 CGMCC No.0650 and its mutant or variant. The production process of the copolymer is the fermentation with the hygrophious aeromonad in culture medium with soybean oil and/or peanut oil. In order ot promote the synthesis of 3-hydroxy butyric acid and 3-hydroxy caproic acid copolymer in the hygrophilous aeromonad, one or several kinds of the nitrogen source, phosphorus source and oxygen supply can be limited, and lauric acid may be added into the culture medium. The present invention makes it possible to produce biodegradable material 3-hydroxy butyric acid and 3-hydroxy caproic acid copolymer in industrial scale.
Description
Technical field
The present invention relates to a Hygrophilous monad and application thereof, particularly relate to a Hygrophilous monad and utilize this bacterium to produce the method for 3-hydroxybutyric acid and 3-hydroxycaproic acid multipolymer.
Background technology
3-hydroxybutyric acid and 3-hydroxycaproic acid multipolymer [Poly (3-hydroxybutyrate-co-3-hydroxyhexanoate), PHBHHx] are by polyester in a kind of born of the same parents of bacterium synthetic, be particulate state with the inclusion form and exist in the bacterium born of the same parents.The heat that PHBHHx possessed becomes plasticity, and mechanical property is similar to the plastics of widely applying at present that obtain with petrochemical materials, but PHBHHx has biodegradability, is considered to a kind of " new bio degradation material ", therefore extremely people's attention.At present, the production method of PHBHHx mainly is to utilize to have a liking for the aqueous vapor sporangium and ferment in for the substratum of sole carbon source in lauric acid and obtain.But, limited the large-scale industrial production of PHBHHx under leavening temperature owing to reasons such as lauric acid cost an arm and a leg, separate with the product difficulty back of bubbling in a large number, ferment in feed supplement difficulty (because being insoluble in water), the fermenting process.
Summary of the invention
The purpose of this invention is to provide the Aeromonas hydrophila that a strain can be used for large-scale industrial production 3-hydroxybutyric acid and 3-hydroxycaproic acid multipolymer.
Aeromonas hydrophila provided by the invention is Aeromonas hydrophila (Aeromonas hydrophila) 45/90CGMCC № 0650 and mutant or varient.
Aeromonas hydrophila (Aeromonas hydrophila) 45/90 is deposited in China Committee for Culture Collection of Microorganisms common micro-organisms center November 12 calendar year 2001, and it abbreviates CGMCC as, and deposit number is CGMCC № 0650.
Aeromonas hydrophila of the present invention separates in by the soil of petroleum pollution from the oil field, huge port and obtains, and has and utilizes carbohydrate to produce the characteristic of acid.This bacterium can grow on Luria-Bertani (LB) (composition: 10g/L peptone, 5g/L yeast extract paste, 5g/L sodium-chlor) substratum, and is light yellow, circular bacterium colony, and neat in edge, growth is fast.
Another object of the present invention provides the method for utilizing above-mentioned Aeromonas hydrophila low cost production 3-hydroxybutyric acid and 3-hydroxycaproic acid multipolymer.
For realizing this purpose, the present invention is by the following technical solutions: a kind of method of producing 3-hydroxybutyric acid and 3-hydroxycaproic acid multipolymer, be that Aeromonas hydrophila is fermented in conventional substratum, described Aeromonas hydrophila is Aeromonas hydrophila 45/90 CGMCC № 0650 and mutant or varient; The carbon source of described substratum comprises soybean oil or peanut oil or their mixture.
Experiment shows, specifically utilize soybean oil or peanut oil or the sort of material of their mixture to be carbon source, to the not influence of output of 3-hydroxybutyric acid and 3-hydroxycaproic acid multipolymer, therefore can select the carbon source of proper raw material according to the practical situation of grown place as fermentation.
In order to promote 3-hydroxybutyric acid and 3-hydroxycaproic acid multipolymer synthesizing in Aeromonas hydrophila 45/90, adopt in restriction nitrogenous source, phosphorus source or three kinds of measures of oxygen supply one or more in the described culturing process.
In order to improve 3-hydroxybutyric acid and the accumulation of 3-hydroxycaproic acid multipolymer in Aeromonas hydrophila 45/90, obtain the 3-hydroxybutyric acid and the 3-hydroxycaproic acid multipolymer of high yield, also be added with lauric acid in the described substratum.
Described lauric acid accounts for the 20-40% of carbon source.
The culture temperature that is fit among the present invention is 28-37 ℃; The pH value that is fit to is 6.0-8.0.
The present invention serves as to produce bacterial strain with Aeromonas hydrophila 45/90 CGMCC № 0650 and mutant thereof or varient, utilize soybean oil or peanut oil or their mixture to be carbon source dexterously, thoroughly solved when using lauric acid as sole carbon source, bubble in a large number in cost height, the fermenting process, problem such as is separated in feed supplement difficulty, fermentation back with the product difficulty under the leavening temperature, thereby can obtain 3-hydroxybutyric acid and 3-hydroxycaproic acid multipolymer at an easy rate.Adopt restriction nitrogenous source, phosphorus source or oxygen supply simultaneously again, in substratum, add measures such as lauric acid, promote 3-hydroxybutyric acid and 3-hydroxycaproic acid multipolymer synthesizing in Aeromonas hydrophila 45/90, the output of 3-hydroxybutyric acid and 3-hydroxycaproic acid multipolymer is further improved, cost further descends, and makes the large-scale industrial production of new bio degradation material 3-hydroxybutyric acid and 3-hydroxycaproic acid multipolymer become possibility.
The present invention will be further described below in conjunction with specific embodiment.
Embodiment
In the following embodiments, the prescription of substratum is as shown in table 1, and used bacterial classification is Aeromonas hydrophila 45/90CGMCC № 0650.
The culture medium prescription nutritive element (g/L) of different culture condition among table 1 embodiment
*Embodiment 1 embodiment 2 embodiment 3 embodiment 4 embodiment 5 soybean oil 100 50 80 70 peanut oil 50 100 20 (NH
4)
2SO
413 13 3 13 13NaH
2PO
42H
2O 3.8 0.84 0.84 3.8 0.84KH
2PO
42.6 0.89 0.89 2.6 0.89MgSO
47H
2O
D1.2 1.2 1.2 1.2 1.2 yeast powders, 11111 trace element solutions
*8ml/L 8ml/L 8ml/L 8ml/L 8ml/L lauric acid 000 20 10
*: 1 liter of trace element solution contains (g): 20 FeCl
36H
2O, 10 CaCl
2H
2O, 0.03 CuSO
45H
2O, 0.05MnCl
24H
2O, 0.1 ZnSO
47H
2O, 0.5mol HCl.
Fermentation under embodiment 1, the no nutrition restricted condition
Under 30 ℃ of conditions, the 150ml seed liquor is inoculated in 6.5 liters of automatic fermentor tanks of NBS that contain the 3L fermented liquid, air flow is 3L/min, and the pH value is set at 7.0, initial stirring 150rpm, dissolved oxygen is set to 10%, along with the growth of cell, stirring constantly increases, at last to 900rpm, but dissolved oxygen is kept all the time and is higher than 10%, and fermentation was carried out 24 hours altogether.No foaming phenomenon in the fermenting process.After the fermentation ends,, washing centrifugal, analyze the content obtain dry cell weight and PHBHHx to sample.
Obtain dry cell weight maximum value 31g/L after 24 hours, PHBHHx accounts for 30% of dry cell weight, and wherein the content of 3-hydroxycaproic acid (HHx) accounts for 10-15%.
Fermentation under the condition of embodiment 2, while phosphorus restriction and oxygen
Under 28 ℃ of conditions, the 150ml seed liquor is inoculated in 6.5 liters of automatic fermentor tanks of NBS that contain the 3L fermented liquid, and air flow is 2L/min, the pH value is set at 6.2, initial stirring 150rpm, and dissolved oxygen is set to 10%, along with the growth of cell, stirring constantly increases, at last to 900rpm, but dissolved oxygen descends gradually, after 6 hours, dissolved oxygen drops to 0, and cell enters the limit oxygen production phase, phosphoric density loss to 0 in the nutrient solution after 12 hours, cell enter the limit phosphorus stage again.No foaming phenomenon in the fermenting process was carried out in fermentation altogether 24 hours.After the fermentation ends,, washing centrifugal, analyze the dry cell weight obtain and the content of PHBHHx to sample.
Fermenting obtained dry cell weight maximum value 15g/L in 24 hours, and it is 33% that corresponding PHBHHx accounts for the dry cell weight percentage composition, and wherein the content of HHx accounts for 10-12%.
Embodiment 3, limit fermentation under the condition of nitrogen, phosphorus, oxygen simultaneously
Under 37 ℃ of conditions, the 150ml seed liquor is inoculated in 6.5 liters of automatic fermentor tanks of NBS that contain the 3L fermented liquid, and air flow is 2L/min, the pH value is set at 6.8, initial stirring 150rpm, and dissolved oxygen is set to 10%, along with the growth of cell, stirring constantly increases, at last to 900rpm.Nitrogen element, phosphoric and dissolved oxygen all drop to 0 in 12 hours secondary fermentation liquid, and cell has entered the restriction state of above-mentioned 3 kinds of elements.No foaming phenomenon in the fermenting process was carried out in fermentation altogether 24 hours.After the fermentation ends,, washing centrifugal, analyze the dry cell weight obtain and the content of PHBHHx to sample.
Fermenting obtained dry cell weight maximum value 18g/L in 24 hours, and corresponding PHBHHx accounts for 50% of dry cell weight, and wherein the content of HHx accounts for 10-12%.
Add the fermentation under the lauric acid condition in embodiment 4, the substratum
Under 30 ℃ of conditions, the 150ml seed liquor is inoculated in 6.5 liters of automatic fermentor tanks of NBS that contain the 3L fermented liquid, and air flow is 3L/min, the pH value is set at 6.8, initial stirring 150rpm, and dissolved oxygen is set to 10%, along with the growth of cell, stirring constantly increases, at last to 900rpm.Add the 20g/L lauric acid when cultivating 12 hours.Dissolved oxygen is kept all the time and is higher than 10%, and fermentation was carried out 24 hours altogether.No foaming phenomenon in the fermenting process.After the fermentation ends,, washing centrifugal, analyze the dry cell weight obtain and the content of PHBHHx to sample.
Fermenting obtained dry cell weight maximum value 42g/L in 24 hours, and corresponding PHBHHx accounts for 40% of dry cell weight, and wherein the content of HHx accounts for 10-12%.
Embodiment 5, phosphorus restriction and the fermentation under the adding lauric acid condition in substratum
Under 33 ℃ of conditions, the 150ml seed liquor is inoculated in 6.5 liters of automatic fermentor tanks of NBS that contain the 3L fermented liquid, and air flow is 3L/min, the pH value is set at 8.0, initial stirring 150rpm, and dissolved oxygen is set to 10%, along with the growth of cell, stirring constantly increases, at last to 900rpm.When cultivating 12 hours in the fermented liquid phosphoric drop to 0, add the 10g/L lauric acid.Dissolved oxygen is kept all the time and is higher than 10%, and fermentation was carried out 24 hours altogether.No foaming phenomenon in the fermenting process.After the fermentation ends,, washing centrifugal, analyze the dry cell weight obtain and the content of PHBHHx to sample.
Fermenting obtained dry cell weight maximum value 40g/L in 24 hours, and corresponding PHBHHx accounts for 50% of dry cell weight, and wherein the content of HHx accounts for 10-12%.
Claims (8)
1, Aeromonas hydrophila (Aeromonas hydrophila) 45/90 CGMCC № 0650 and mutant or varient.
2, a kind of method of producing 3-hydroxybutyric acid and 3-hydroxycaproic acid multipolymer, be that Aeromonas hydrophila is fermented in conventional substratum, it is characterized in that: described Aeromonas hydrophila is Aeromonas hydrophila 45/90 CGMCC № 0650 and mutant or varient; The carbon source of described substratum comprises soybean oil or peanut oil or their mixture.
3, a kind of method of producing 3-hydroxybutyric acid and 3-hydroxycaproic acid multipolymer according to claim 2 is characterized in that: one or more in the described culturing process in employing restriction nitrogenous source, phosphorus source or three kinds of measures of oxygen supply.
4, a kind of method of producing 3-hydroxybutyric acid and 3-hydroxycaproic acid multipolymer according to claim 2 is characterized in that: also be added with lauric acid in the described substratum.
5, a kind of method of producing 3-hydroxybutyric acid and 3-hydroxycaproic acid multipolymer according to claim 3 is characterized in that: also be added with lauric acid in the described substratum.
6, according to claim 4 or 5 described a kind of methods of producing 3-hydroxybutyric acid and 3-hydroxycaproic acid multipolymer, it is characterized in that: described lauric acid accounts for the 10-40% of carbon source.
7, according to claim 2 or 3 or 4 or 5 described a kind of methods of producing 3-hydroxybutyric acid and 3-hydroxycaproic acid multipolymer, it is characterized in that: described culture temperature is 28-37 ℃.
8, according to claim 2 or 3 or 4 or 5 described a kind of methods of producing 3-hydroxybutyric acid and 3-hydroxycaproic acid multipolymer, it is characterized in that: the pH value in the described culturing process is 6.0-8.0.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB011345764A CN1177036C (en) | 2001-11-28 | 2001-11-28 | Hygrophilous monad and its application |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB011345764A CN1177036C (en) | 2001-11-28 | 2001-11-28 | Hygrophilous monad and its application |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1421525A true CN1421525A (en) | 2003-06-04 |
| CN1177036C CN1177036C (en) | 2004-11-24 |
Family
ID=4672597
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNB011345764A Expired - Fee Related CN1177036C (en) | 2001-11-28 | 2001-11-28 | Hygrophilous monad and its application |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN1177036C (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101993834A (en) * | 2010-05-20 | 2011-03-30 | 上海海洋大学 | Method for separating Aeromonas molluscorum producing tetrodotoxin from Takifugu fasciatus tissue and fermentation culture method of Aeromonas molluscorum as well as detection method of produced tetrodotoxin |
| CN101696431B (en) * | 2009-10-29 | 2011-11-09 | 辽宁大学 | Method for producing copolymer PHBHHx by metabolism control of aeromonas hydrophila |
| CN101287839B (en) * | 2005-03-24 | 2015-04-08 | 帝斯曼知识产权资产管理有限公司 | Process for microbial production of a valuable compound |
| CN105039216A (en) * | 2015-07-14 | 2015-11-11 | 浙江工业大学 | Aeromonas sp. YQ and its application in enzymatic preparation of L-citrulline |
-
2001
- 2001-11-28 CN CNB011345764A patent/CN1177036C/en not_active Expired - Fee Related
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101287839B (en) * | 2005-03-24 | 2015-04-08 | 帝斯曼知识产权资产管理有限公司 | Process for microbial production of a valuable compound |
| CN101696431B (en) * | 2009-10-29 | 2011-11-09 | 辽宁大学 | Method for producing copolymer PHBHHx by metabolism control of aeromonas hydrophila |
| CN101993834A (en) * | 2010-05-20 | 2011-03-30 | 上海海洋大学 | Method for separating Aeromonas molluscorum producing tetrodotoxin from Takifugu fasciatus tissue and fermentation culture method of Aeromonas molluscorum as well as detection method of produced tetrodotoxin |
| CN101993834B (en) * | 2010-05-20 | 2013-06-12 | 上海海洋大学 | Method for separating Aeromonas molluscorum producing tetrodotoxin from Takifugu fasciatus tissue and fermentation culture method of Aeromonas molluscorum as well as detection method of produced tetrodotoxin |
| CN105039216A (en) * | 2015-07-14 | 2015-11-11 | 浙江工业大学 | Aeromonas sp. YQ and its application in enzymatic preparation of L-citrulline |
| CN105039216B (en) * | 2015-07-14 | 2019-02-01 | 浙江工业大学 | Aeromonas YQ and the application in enzyme process preparation L-citrulline |
Also Published As
| Publication number | Publication date |
|---|---|
| CN1177036C (en) | 2004-11-24 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| Mu et al. | Microbial production of 1, 3-propanediol by Klebsiella pneumoniae using crude glycerol from biodiesel preparations | |
| Wild et al. | Lipidi iz kvasca Lipomyces starkeyi | |
| US5688674A (en) | Continuous fermentation process for the production of metabolities using a moving filter | |
| CN101735993B (en) | Method for efficiently producing cellulase | |
| Jin et al. | Rhizopus arrhizus–a producer for simultaneous saccharification and fermentation of starch waste materials to L (+)-lactic acid | |
| EP3640337A1 (en) | Method for continuously culturing aspergillus niger seeds and producing citric acid using same | |
| CN109929897B (en) | Culture medium for promoting HAU-M1 photosynthetic bacteria flora to produce hydrogen and application thereof | |
| CN101792778A (en) | Method for fermentation production of succinic acid by circulating utilization of recombinant Bacillus coli cells | |
| CN101665813A (en) | Microorganism fermentation production method of L-alanine | |
| CN100342022C (en) | Method for improving alcohol yield fermented from starch material | |
| CN101724592B (en) | Bacillus subtilis and application thereof in biocatalytic production of L-lactic acid | |
| Burgstaller et al. | The influence of different carbon sources on growth and single cell oil production in oleaginous yeasts Apiotrichum brassicae and Pichia kudriavzevii | |
| CN105543297B (en) | Hydrogenogen combines conversion of biomass and CO with alcaligenes eutrophus2The method for preparing polyhydroxyalkanoate | |
| CN102586353A (en) | Non-dependent production method of gamma-polyglutamic acid from glutamic acid | |
| CN1259424C (en) | Method for increasing long-chain biatomic acid fermentation production rate | |
| CN1177036C (en) | Hygrophilous monad and its application | |
| CN112430557B (en) | high-PHA-yield Kabayeri strain, screening method and PHA production method thereof | |
| CN101886095A (en) | Method for producing high-concentration D-lactic acid by adopting synchronous enzymolysis and fermentation on peanut meal and special culture medium thereof | |
| CN1225546C (en) | Method for preparing astaxanthin from alga cultivated by using residue of fermenting yeast | |
| CN112852891A (en) | Artificial dual-bacterium system for producing mcl-PHA and application thereof | |
| CN1952164A (en) | Process for combined fermentation production of D-lactic acid | |
| CN103952447A (en) | Method for producing succinic acid by virtue of fermentation under anaerobic conditions | |
| CN102051336B (en) | Lactobacillus casei and application of lactobacillus casei in ferment production of L-lactic acid | |
| CN1173041C (en) | Production of alcohol by fermenting by yeast tolerant to high concentrated sugar and alcohol | |
| CN1524961A (en) | Microorganism continuous catalysis method for producing acrylamide |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| 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 | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20041124 Termination date: 20141128 |
|
| EXPY | Termination of patent right or utility model |