CN113897318A - Method for co-culturing protein degradation by using acetoacidophilic protein bacterium and sulfur reducing geobacillus - Google Patents

Method for co-culturing protein degradation by using acetoacidophilic protein bacterium and sulfur reducing geobacillus Download PDF

Info

Publication number
CN113897318A
CN113897318A CN202111278813.3A CN202111278813A CN113897318A CN 113897318 A CN113897318 A CN 113897318A CN 202111278813 A CN202111278813 A CN 202111278813A CN 113897318 A CN113897318 A CN 113897318A
Authority
CN
China
Prior art keywords
acetoacidophilic
protein
bacterium
culturing
solution
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
CN202111278813.3A
Other languages
Chinese (zh)
Other versions
CN113897318B (en
Inventor
刘倩
陈加娇
林辉
吕斯濠
杨立辉
郭膘虎
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.)
Dongguan University of Technology
Original Assignee
Dongguan University of Technology
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 Dongguan University of Technology filed Critical Dongguan University of Technology
Priority to CN202111278813.3A priority Critical patent/CN113897318B/en
Publication of CN113897318A publication Critical patent/CN113897318A/en
Application granted granted Critical
Publication of CN113897318B publication Critical patent/CN113897318B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Classifications

    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12NMICROORGANISMS OR ENZYMES; COMPOSITIONS THEREOF; PROPAGATING, PRESERVING, OR MAINTAINING MICROORGANISMS; MUTATION OR GENETIC ENGINEERING; CULTURE MEDIA
    • C12N1/00Microorganisms, e.g. protozoa; Compositions thereof; Processes of propagating, maintaining or preserving microorganisms or compositions thereof; Processes of preparing or isolating a composition containing a microorganism; Culture media therefor
    • C12N1/20Bacteria; Culture media therefor
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F3/00Biological treatment of water, waste water, or sewage
    • C02F3/34Biological treatment of water, waste water, or sewage characterised by the microorganisms used
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2101/00Nature of the contaminant
    • C02F2101/30Organic compounds
    • C02F2101/38Organic compounds containing nitrogen

Landscapes

  • Life Sciences & Earth Sciences (AREA)
  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Microbiology (AREA)
  • Organic Chemistry (AREA)
  • Health & Medical Sciences (AREA)
  • Biotechnology (AREA)
  • Zoology (AREA)
  • Bioinformatics & Cheminformatics (AREA)
  • Wood Science & Technology (AREA)
  • Genetics & Genomics (AREA)
  • Tropical Medicine & Parasitology (AREA)
  • Biomedical Technology (AREA)
  • Virology (AREA)
  • Biochemistry (AREA)
  • General Engineering & Computer Science (AREA)
  • General Health & Medical Sciences (AREA)
  • Medicinal Chemistry (AREA)
  • Biodiversity & Conservation Biology (AREA)
  • Hydrology & Water Resources (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Micro-Organisms Or Cultivation Processes Thereof (AREA)
  • Preparation Of Compounds By Using Micro-Organisms (AREA)

Abstract

The invention discloses a method for co-culturing and degrading protein by using acetoacidophilic protein bacteria and sulfur-reducing geobacillus, which comprises the following specific steps: s1, inoculating acetoacidophilic proteophile and thioredoxin in the culture solution; s2 protein degradation effect: the degradation effect of the protein of the mixed bacteria at different days and different inoculation ratios is observed, and the result shows that: the co-culture of the two bacteria is far superior to the degradation effect of pure culture of the acetoacidophilic protein bacteria on protein; the degraded acetoacidophilic protein bacterium is a protein degradation bacterium and can generate acetic acid, the acetic acid can be used as a substrate of the thioreducing Bacillus, compared with other protein degradation bacteria, the mixed system can degrade more proteins, and the operation is simple and convenient.

Description

Method for co-culturing protein degradation by using acetoacidophilic protein bacterium and sulfur reducing geobacillus
Technical Field
The invention relates to the technical field of microorganisms, in particular to a method for co-culturing and degrading proteins by using acetoacidophilic protein bacteria and sulfur-reducing geobacillus.
Background
Acetoacidophilic protein bacteria (proteoliophiles TB107T) are gram-negative and anaerobic protein-degrading bacteria, which were first isolated from granular sludge from the treatment of beer wastewater and are capable of degrading yeast extract, peptone, pyruvic acid and other complex substrates to produce volatile fatty acid acetic acid and the like, and thiobacillus thioredoxin (Geobacter sulfurlowers PCA) is also an anaerobic bacteria capable of using acetic acid, propionic acid and the like as substrates.
As the number of sewage treatment plants is increased on a large scale, a large amount of domestic sewage and a large amount of sludge are generated, the sewage and the sludge contain a large amount of protein besides a large amount of pollutants, the sewage is rich in a large amount of protein resources, amino acids and growth factors, due to the difficulty in resource recovery, the random discharge of high-protein sewage wastes resources and certain damage to the ecological environment, and therefore, the full recovery and degradation of the resources are urgently needed.
The existing methods for recovering and degrading proteins in sewage and sludge include protein extraction, degradation and differentiation treatment, and direct protein degradation in sewage and sludge, such as thermal acid hydrolysis, thermal alkali hydrolysis and wet oxygen hydrolysis in chemical hydrolysis; ultrasonic methods among physical methods; biological processes such as enzymatic hydrolysis; a combined method such as an ultrasonic combined enzyme method, an ultrasonic combined acid method and the like, for example, Chinese patent document CN109400671A adopts an alkaline low-temperature hydrolysis method to treat sludge, break biological cell walls, release protein, and adopts macroporous exchange resin to refine filtrate so as to obtain a higher degradable protein solution; however, these methods are complicated, expensive, unstable in treatment effect, long in running time, and only remove them, thereby wasting a lot of valuable nutrients.
Disclosure of Invention
The present invention aims at providing the method for co-culturing the acetoacidophilic protein-producing bacteria and the sulfur-reducing bacillus to degrade the protein, so as to solve the problems in the background technology.
In order to solve the technical problems, the invention provides the following technical scheme:
the method comprises the following steps:
s1, inoculating acetoacidophilic proteophile and thioredoxin in the culture solution;
s2: and (3) taking the bacterial liquid, centrifuging at a high speed for 8min, filtering the centrifuged supernatant through a filter membrane, adding the BCA working solution and water into the filtered supernatant, standing at 37 ℃ for 20min, and measuring the absorbance of the sample at 562 nm.
Further, the preparation method of the culture solution comprises the following steps:
a: adding polypeptone, yeast extract, tryptone, glucose, ammonium chloride, calcium chloride, potassium chloride, sodium dihydrogen phosphate, dipotassium hydrogen phosphate, vitamin solution and trace element solution into water;
b: heating in water bath until dissolving, and adjusting pH to 6.9-7.0 with sodium hydroxide solution;
c: introducing mixed gas of nitrogen and hydrogen, aerating for 20min, sterilizing at 121 deg.C for 20min, and ultraviolet irradiating to obtain culture solution.
Further, the inoculation ratio of the protein acetophilic bacteria to the Acinetobacter thioredoxin in the step S1 is (1-4): (1-8).
Further, the inoculation time interval of the acetoacidophilic protein bacteria and the sulfur reducing bacteria in the step S1 is 0-3 days.
5. The method for degrading proteins by co-culturing the acetoacidophilic bacterium and the thioreductic bacterium according to claim 1, wherein: the inoculation amount of the mixed bacterium liquid of the acetoacidophilic proteophile and the sulfur reducing geobacillus is 3-6%, the culture temperature is 34 ℃, and the culture time is 7-9 days.
Further, the materials required for the culture solution include: 2.5-3g/L of polypeptone, 5.0-6g/L of yeast extract, 2.5-3g/L of tryptone, 10.0-12g/L of glucose, 1.5-3g/L of ammonium chloride, 0.024-0.2g/L of calcium chloride, 0.1-0.3g/L of potassium chloride, 0.64-0.8g/L of sodium dihydrogen phosphate, 0.04-0.1g/L of dipotassium hydrogen phosphate, 5-8mL of vitamin solution, 5-8mL of trace element solution and water with constant volume of 1L.
Further, the vitamin solution comprises the following materials: 2-5mg of biotin, 2-5mg of folic acid, 10-15mg of vitamin B6 pyridoxine-hydrochloric acid, 5-8mg of thiamine-hydrochloric acid, 5-8mg of riboflavin, 35-8mg of vitamin B, 5-8mg of D-calcium pantothenate, 120.1-0.3 mg of vitamin B, 5-8mg of p-aminobenzoic acid and 5-8mg of lipoic acid, and the volume of water is fixed to 1L.
Further, the materials required by the trace element liquid comprise: 1.5-3g of nitrilotriacetic acid, 3-5g of magnesium sulfate heptahydrate, 0.5-1g of manganese sulfate monohydrate, 1-3g of sodium chloride, 0.1-0.3g of ferrous sulfate heptahydrate, 0.1-0.3g of cobalt chloride hexahydrate, 0.76-1g of calcium chloride, 0.1-0.3g of zinc sulfate heptahydrate, 0.01-0.05g of copper sulfate pentahydrate, 0.02-0.05g of aluminum potassium sulfate dodecahydrate, 0.01-0.03g of boric acid, 0.01-0.03g of sodium molybdate, and the volume of water is up to 1L.
Further, the acetoacidophilic proteobacteria belong to the genus proteus species.
Further, the thioreductioned geobacter is a strain belonging to the genus geobacter.
Compared with the prior art, the invention has the following beneficial effects: firstly, the protein degradation of the microorganism can be carried out under mild conditions, and the defects of pollution, high energy consumption and complex operation caused by protein treatment by a physical and chemical method can be avoided.
Secondly, the strains used in the invention all belong to anaerobic mode bacteria, and can better degrade protein compared with other anaerobic bacteria, and the operation is simple and convenient because an anaerobic incubator is not required to be degraded.
Thirdly, the mixed bacteria promote the degradation of protein under the anaerobic condition, the efficiency is high, the period is short, the sulfur-reducing geobacillus can utilize the generated acetic acid under the condition that the pure bacteria of the acetotropic bacteria can degrade the protein, thereby reducing the adverse effect of product accumulation on the growth of bacteria, opening up a new way for the treatment of the protein in the sewage, and further providing a new way for the resource treatment of the protein wastewater.
Fourthly, the influence of the inoculation sequence and time of the bacterial liquid on the degradation of the protein is researched, firstly, the acetoacidophilic proteus can convert the protein into acetic acid, and the sulfur-reducing geobacillus can take acetic acid molecules as substrates to carry out self growth and metabolism, so that the acetoacidophilic proteus is inoculated for self growth and metabolism, then the sulfur-reducing geobacillus is inoculated, and meanwhile, orthogonal experiments show that the acetoacidophilic proteus and the sulfur-reducing geobacillus are inoculated simultaneously, and the degradation effect of the protein is better than that of the acetoacidophilic proteus for 2-3 days and then the sulfur-reducing geobacillus.
Drawings
The accompanying drawings, which are included to provide a further understanding of the invention and are incorporated in and constitute a part of this specification, illustrate embodiments of the invention and together with the description serve to explain the principles of the invention and not to limit the invention. In the drawings:
FIG. 1 shows the protein degradation of examples A1-A4 and comparative example 1;
FIG. 2 shows the protein degradation of example B1-B4 and comparative example 2;
FIG. 3 shows the growth of the mixed bacterial liquid of examples B1-B4 and comparative example 2;
FIG. 4 shows the use of acetic acid in the mixed bacterial liquid of examples B1-B4 and comparative example 2.
Detailed Description
The technical solutions in the embodiments of the present invention will be clearly and completely described below with reference to the drawings in the embodiments of the present invention, and it is obvious that the described embodiments are only a part of the embodiments of the present invention, and not all of the embodiments. All other embodiments, which can be derived by a person skilled in the art from the embodiments given herein without making any creative effort, shall fall within the protection scope of the present invention.
Taking example a1 as an example:
s1 Co-culture of two bacteria:
a: preparing a culture solution: adding 500mL of distilled water into a 1L triangular flask, and dividingRespectively adding polypeptone 2.5g/L, yeast extract 5.0g/L, tryptone 2.5g/L, glucose 10.0g/L, ammonium chloride 1.5g/L, calcium chloride 0.024g/L, potassium chloride 0.1g/L, sodium dihydrogen phosphate 0.64g/L, dipotassium hydrogen phosphate 0.04g/L, vitamin solution 5mL, and trace element solution 5mL, adding pure water to constant volume to 1L, heating in water bath to dissolve, adding NaOH dropwise to adjust pH to 6.9, filling into a bottle, inserting aeration needle into the bottle, introducing 80% N, adding sodium hydroxide, sodium hydroxide2And 20% of H2Aerating the mixed gas for 20min, quickly covering the rubber stopper, placing the narrow-mouth bottle in an autoclave, sterilizing at 121 ℃ for 20min, and then transferring to a super clean bench for ultraviolet irradiation for later use;
b: inoculation: inoculating acetoacidophilic proteophile and then thioredoxin, wherein the inoculation ratio of the acetoacidophilic proteophile to the thioredoxin is 1:4, and the two are co-cultured for 8 days, and the inoculation amount is 5%;
s2: protein degradation effect:
taking 8 days as a period, taking 1mL of bacterial liquid at the same time every day, centrifuging for 8min at 10000r/min, filtering the supernatant obtained after centrifugation through a PES filter membrane of 0.22 mu m, taking 200 mu L of filtered supernatant 20 mu L, BCA working solution (BCA protein concentration determination kit produced by Fuzhou Feijing Biotechnology Co., Ltd.), adding water to fix the volume to 2.2mL, placing the prepared sample at 37 ℃ for 20min, measuring the absorbance of the sample at the wavelength of 562nm by using an ultraviolet-visible spectrophotometer, and taking the culture solution of the non-inoculated acetogenium and the thioredoxin as a blank group.
The preparation method of the vitamin solution comprises the following steps: mixing biotin 2.00mg, folic acid 2.00mg, vitamin B6 pyridoxine-hydrochloric acid 10.00mg, thiamine-hydrochloric acid 5.00mg, riboflavin 5.00mg, and vitamin B35.00mg, 5.00mg of calcium D-pantothenate, vitamin B120.100mg, 5.00mg of p-aminobenzoic acid and 5.00mg of lipoic acid are uniformly mixed, and then the mixture is added with water to be constant volume to 1L.
The preparation method of the trace element liquid comprises the following steps: 1.50g of nitrilotriacetic acid, 3.00g of magnesium sulfate heptahydrate, 0.50g of manganese sulfate monohydrate, 1.00g of sodium chloride, 0.10g of ferrous sulfate heptahydrate, 0.10g of cobalt chloride hexahydrate, 0.76g of calcium chloride, 0.10g of zinc sulfate heptahydrate, 0.01g of copper sulfate pentahydrate, 0.02g of aluminum potassium sulfate dodecahydrate, 0.01g of boric acid and 0.01g of sodium molybdate are uniformly mixed, and then water is used for fixing the volume to 1L.
Examples A1-A4: the specific data obtained by changing the inoculation time in example A1 are shown in Table 1, and the specific data obtained by measuring the protein degradation rate of the mixed bacterial liquid are shown in Table 2.
TABLE 1 example A1-A4 Mixed bacterial liquid inoculation time
A1 A2 A3 A4
Time of inoculation 0 1 2 3
Comparative example 1: in contrast to example 1, the culture broth was inoculated with a Propionibacterium acetogenium.
TABLE 2 Effect of different inoculation times on protein degradation rates in examples A1-A4
Figure BDA0003330546530000051
Figure BDA0003330546530000052
Taking example B1 as an example:
s1 Co-culture of two bacteria:
a: preparing a culture solution: adding 500mL of distilled water into a 1L triangular flask, respectively adding polypeptone 2.5g/L, yeast extract 5.0g/L, tryptone 2.5g/L, glucose 10.0g/L, ammonium chloride 1.5g/L, calcium chloride 0.024g/L, potassium chloride 0.1g/L, sodium dihydrogen phosphate 0.64g/L, dipotassium hydrogen phosphate 0.04g/L, vitamin solution 5mL and microelement solution 5mL, adding pure water to a constant volume of 1L, heating in water bath to dissolve, dropwise adding NaOH to adjust pH to 7.0, packaging into a narrow-mouth bottle, inserting an aeration needle into the narrow-mouth bottle, introducing 80% N2And 20% of H2Aerating the mixed gas for 20min, quickly covering the rubber stopper, placing the narrow-mouth bottle in an autoclave, sterilizing at 121 ℃ for 20min, and then transferring to a super clean bench for ultraviolet irradiation for later use;
b: inoculation: inoculating acetoacidophilic proteophile, inoculating thioredoxin after 2 days, and co-culturing for 8 days with the inoculation amount of 5%;
s2: protein degradation effect:
taking 8 days as a period, taking 1mL of bacterial liquid at the same time every day, centrifuging for 8min at 10000r/min, filtering the supernatant obtained after centrifugation through a PES filter membrane of 0.22 mu m, taking 200 mu L of filtered supernatant 20 mu L, BCA working solution (BCA protein concentration determination kit produced by Fuzhou Feijing Biotechnology Co., Ltd.), adding water to fix the volume to 2.2mL, placing the prepared sample at 37 ℃ for 20min, measuring the absorbance of the sample at the wavelength of 562nm by using an ultraviolet-visible spectrophotometer, and taking the culture solution of the non-inoculated acetogenium and the thioredoxin as a blank group.
The preparation method of the vitamin solution comprises the following steps: 2.00mg of biotin, 2.00mg of folic acid, 10.00mg of vitamin B6 pyridoxine-hydrochloric acid, 5.00mg of thiamine-hydrochloric acid, 5.00mg of riboflavin, 35.00mg of vitamin B, 5.00mg of D-calcium pantothenate, 120.100mg of vitamin B, 5.00mg of p-aminobenzoic acid and 5.00mg of lipoic acid are uniformly mixed, and then the volume is fixed to 1L by water.
The preparation method of the trace element liquid comprises the following steps: 1.50g of nitrilotriacetic acid, 3.00g of magnesium sulfate heptahydrate, 0.50g of manganese sulfate monohydrate, 1.00g of sodium chloride, 0.10g of ferrous sulfate heptahydrate, 0.10g of cobalt chloride hexahydrate, 0.76g of calcium chloride, 0.10g of zinc sulfate heptahydrate, 0.01g of copper sulfate pentahydrate, 0.02g of aluminum potassium sulfate dodecahydrate, 0.01g of boric acid and 0.01g of sodium molybdate are uniformly mixed, and then water is used for fixing the volume to 1L.
Examples B1-B4: the specific data obtained by replacing the inoculation ratio in example B1 are shown in Table 3, and the specific data obtained by measuring the protein degradation rate of the mixed bacterial liquid are shown in Table 4.
TABLE 3 example B1-B4 inoculation ratio of mixed bacterial liquid
Figure BDA0003330546530000061
Comparative example 2: in contrast to example 2, the culture broth was inoculated with a Propionibacterium acetogenium.
TABLE 4 Effect of different inoculation ratios on protein degradation rates in examples B1-B4
Figure BDA0003330546530000062
Figure BDA0003330546530000063
Experimental data
Mixed culture growth (OD 600): 2mL of the culture solution was taken, and the absorbance (blank was a culture solution of non-inoculated bacteria) was measured at 600nm once a day.
Acetic acid utilization: centrifuging 1mL of bacterial liquid at 10000r/min and room temperature for 8min, filtering the supernatant obtained after centrifugation through a PES filter membrane of 0.22 mu m, adding 0.9mL of methanol into 0.1mL of the filtered supernatant, centrifuging at 10000r/min and room temperature for 5min, adding 0.15mL of the supernatant into pure water to dilute the pure water by 10 times, and performing analysis and detection on the obtained solution, namely a sample solution, in an ion chromatography, wherein a culture solution of non-inoculated bacteria is used as a blank, and the blank solution is treated in the same way as the sample.
TABLE 5 Effect of different inoculation times on protein degradation rates in examples A1-A4
Figure BDA0003330546530000071
Figure BDA0003330546530000081
TABLE 6 Effect of different inoculation ratios on protein degradation rates in examples B1-B4
Figure BDA0003330546530000082
Figure BDA0003330546530000091
TABLE 7 results of experiments in examples B1-B4 and comparative example 2OD600
B1 B2 B3 B4 Comparative example 2
0d 0 0 0 0 0
1d 0 0 0 0 0
2d 0.078 0.078 0.078 0.078 0.06
3d 0.268 0.281 0.36 0.282 0.139
4d 0.302 0.407 0.361 0.285 0.232
5d 0.277 0.371 0.327 0.277 0.275
6d 0.272 0.371 0.319 0.277 0.254
7d 0.262 0.323 0.327 0.251 0.251
8d 0.270 0.338 0.274 0.312 0.217
TABLE 8 utilization of acetic acid in examples B1-B4 and comparative example 2
Figure BDA0003330546530000092
Figure BDA0003330546530000101
And (4) conclusion: as can be seen from tables 2 and 4, the protein degradation rate of the sulfur-reducing Bacillus strain inoculated at different inoculation times and different inoculation ratios is higher than that of the control group, the acetoacidophilic Propionibacterium is inoculated for 2 days and then the thioreducing Bacillus strain is inoculated, the protein degradation rate is highest when the inoculation ratio is 1:4, the protein degradation rate is accelerated after the thioreducing Bacillus strain is inoculated, the mixed culture is more favorable for the degradation of the protein, Table 7 shows that the mixed growth condition is best when the biomass of the mixed culture is higher than that of the comparative example 2 and 1:4, the bacterial growth condition and the protein degradation rate are in a positive relationship, Table 8 shows that the acetic acid content of the comparative example 2 is in an ascending trend and is finally higher than that of the mixed strain, while the acetic acid concentrations under different inoculation ratios in the mixed strain are closer, the acetic acid content is obviously reduced after the thioreducing Bacillus strain is added, the change of acetic acid and the protein degradation rate do not form a positive-negative relationship.
It is noted that, herein, relational terms such as first and second, and the like may be used solely to distinguish one entity or action from another entity or action without necessarily requiring or implying any actual such relationship or order between such entities or actions. Also, the terms "comprises," "comprising," or any other variation thereof, are intended to cover a non-exclusive inclusion, such that a process, method, article, or apparatus that comprises a list of elements does not include only those elements but may include other elements not expressly listed or inherent to such process, method, article, or apparatus.
Finally, it should be noted that: although the present invention has been described in detail with reference to the foregoing embodiments, it will be apparent to those skilled in the art that changes may be made in the embodiments and/or equivalents thereof without departing from the spirit and scope of the invention. Any modification, equivalent replacement, or improvement made within the spirit and principle of the present invention should be included in the protection scope of the present invention.

Claims (8)

1. A method for co-culturing and degrading protein by using acidophilic protein bacteria and sulfur reducing geobacillus is characterized by comprising the following steps: the method comprises the following steps:
s1, inoculating acetoacidophilic proteophile and thioredoxin in the culture solution;
s2: and (3) taking the bacterial liquid, centrifuging at a high speed for 8min, filtering the centrifuged supernatant through a filter membrane, adding the BCA working solution and water into the filtered supernatant, standing at 37 ℃ for 20min, and measuring the absorbance of the sample at 562 nm.
2. The method for degrading proteins by co-culturing the acetoacidophilic bacterium and the thioreductic bacterium according to claim 1, wherein: the preparation method of the culture solution comprises the following steps:
a: adding polypeptone, yeast extract, tryptone, glucose, ammonium chloride, calcium chloride, potassium chloride, sodium dihydrogen phosphate, dipotassium hydrogen phosphate, vitamin solution and trace element solution into water;
b: heating in water bath until dissolving, and adjusting pH to 6.9-7.0 with sodium hydroxide solution;
c: introducing mixed gas of nitrogen and hydrogen, aerating for 20min, sterilizing at 121 deg.C for 20min, and ultraviolet irradiating to obtain culture solution.
3. The method for degrading proteins by co-culturing the acetoacidophilic bacterium and the thioreductic bacterium according to claim 1, wherein: the inoculation ratio of the protein acetophilic bacteria to the Acetobacter thioredoxin in the step S1 is (1-4): (1-8).
4. The method for degrading proteins by co-culturing the acetoacidophilic bacterium and the thioreductic bacterium according to claim 1, wherein: in the step S1, the inoculation time interval of the acetoacidophilic protein bacteria and the sulfur reducing geobacillus is 0-3 days.
5. The method for degrading proteins by co-culturing the acetoacidophilic bacterium and the thioreductic bacterium according to claim 1, wherein: the inoculation amount of the mixed bacterium liquid of the acetoacidophilic proteophile and the sulfur reducing geobacillus is 3-6%, the culture temperature is 34 ℃, and the culture time is 7-9 days.
6. The method for degrading proteins by co-culturing the acetoacidophilic bacterium and the thioreductic bacterium according to claim 2, wherein: the materials required by the culture solution comprise: 2.5-3g/L of polypeptone, 5.0-6g/L of yeast extract, 2.5-3g/L of tryptone, 10.0-12g/L of glucose, 1.5-3g/L of ammonium chloride, 0.024-0.2g/L of calcium chloride, 0.1-0.3g/L of potassium chloride, 0.64-0.8g/L of sodium dihydrogen phosphate, 0.04-0.1g/L of dipotassium hydrogen phosphate, 5-8mL of vitamin solution, 5-8mL of trace element solution and water with constant volume of 1L.
7. The method for degrading proteins by co-culturing the acetoacidophilic bacterium and the thioreductic bacterium according to claim 2, wherein: the vitamin solution comprises the following materials: 2-5mg of biotin, 2-5mg of folic acid, 10-15mg of vitamin B6 pyridoxine-hydrochloric acid, 5-8mg of thiamine-hydrochloric acid, 5-8mg of riboflavin, and vitamin B35-8mg, 5-8mg of D-calcium pantothenate, vitamin B120.1-0.3mg, 5-8mg of p-aminobenzoic acid and 5-8mg of lipoic acid, and the volume of water is fixed to 1L.
8. The method for degrading proteins by co-culturing the acetoacidophilic bacterium and the thioreductic bacterium according to claim 2, wherein: the materials required by the trace element liquid comprise: 1.5-3g of nitrilotriacetic acid, 3-5g of magnesium sulfate heptahydrate, 0.5-1g of manganese sulfate monohydrate, 1-3g of sodium chloride, 0.1-0.3g of ferrous sulfate heptahydrate, 0.1-0.3g of cobalt chloride hexahydrate, 0.76-1g of calcium chloride, 0.1-0.3g of zinc sulfate heptahydrate, 0.01-0.05g of copper sulfate pentahydrate, 0.02-0.05g of aluminum potassium sulfate dodecahydrate, 0.01-0.03g of boric acid, 0.01-0.03g of sodium molybdate, and the volume of water is up to 1L.
CN202111278813.3A 2021-10-31 2021-10-31 Method for degrading protein by co-culturing acidophilic acid-producing protein bacterium and geobacillus thioreductase Active CN113897318B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN202111278813.3A CN113897318B (en) 2021-10-31 2021-10-31 Method for degrading protein by co-culturing acidophilic acid-producing protein bacterium and geobacillus thioreductase

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN202111278813.3A CN113897318B (en) 2021-10-31 2021-10-31 Method for degrading protein by co-culturing acidophilic acid-producing protein bacterium and geobacillus thioreductase

Publications (2)

Publication Number Publication Date
CN113897318A true CN113897318A (en) 2022-01-07
CN113897318B CN113897318B (en) 2023-12-01

Family

ID=79027191

Family Applications (1)

Application Number Title Priority Date Filing Date
CN202111278813.3A Active CN113897318B (en) 2021-10-31 2021-10-31 Method for degrading protein by co-culturing acidophilic acid-producing protein bacterium and geobacillus thioreductase

Country Status (1)

Country Link
CN (1) CN113897318B (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN114958654A (en) * 2022-04-29 2022-08-30 江南大学 Propionic acid-producing type protein-philic bacterium derived from pit mud produced by brewing white spirit and application thereof

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20120027888A1 (en) * 2009-03-30 2012-02-02 Meji Co. Ltd Method for Culturing Lactic Acid Bacterium and Method for Producing Fermented Milk
JP2014217304A (en) * 2013-05-07 2014-11-20 ドーサン・フィード・アンド・ライブストック・カンパニーリミテッドDoosan Feed &Livestock Co., Ltd. Microorganism having methanation inhibition ability in reticulo rumen of ruminant, and use thereof
CN104630292A (en) * 2015-02-09 2015-05-20 哈尔滨工业大学宜兴环保研究院 Method for preparing butyric acid by fermenting lignocellulose by using mixed flora
RU2678123C1 (en) * 2017-10-13 2019-01-23 Федеральное государственное бюджетное учреждение науки Институт клеточного и внутриклеточного симбиоза Уральского отделения Российской академии наук Nutrient environment for restoring number of anaerobic bacteria after low-temperature storage
CN110592148A (en) * 2019-09-12 2019-12-20 同济大学 Method for promoting protein-philic acetogenic bacteria to generate acetic acid
CN113151105A (en) * 2021-05-17 2021-07-23 东莞理工学院 Pure culture method of anaerobic microorganisms

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20120027888A1 (en) * 2009-03-30 2012-02-02 Meji Co. Ltd Method for Culturing Lactic Acid Bacterium and Method for Producing Fermented Milk
JP2014217304A (en) * 2013-05-07 2014-11-20 ドーサン・フィード・アンド・ライブストック・カンパニーリミテッドDoosan Feed &Livestock Co., Ltd. Microorganism having methanation inhibition ability in reticulo rumen of ruminant, and use thereof
CN104630292A (en) * 2015-02-09 2015-05-20 哈尔滨工业大学宜兴环保研究院 Method for preparing butyric acid by fermenting lignocellulose by using mixed flora
RU2678123C1 (en) * 2017-10-13 2019-01-23 Федеральное государственное бюджетное учреждение науки Институт клеточного и внутриклеточного симбиоза Уральского отделения Российской академии наук Nutrient environment for restoring number of anaerobic bacteria after low-temperature storage
CN110592148A (en) * 2019-09-12 2019-12-20 同济大学 Method for promoting protein-philic acetogenic bacteria to generate acetic acid
CN113151105A (en) * 2021-05-17 2021-07-23 东莞理工学院 Pure culture method of anaerobic microorganisms

Non-Patent Citations (3)

* Cited by examiner, † Cited by third party
Title
CHEN SHUANGYA等: "Proteiniphilum acetatigenes gen. nov., sp. nov., from a UASB reactor treating brewery wastewater", INTERNATIONAL JOURNAL OF SYSTEMATIC AND EVOLUTIONARY MICROBIOLOGY, vol. 55, pages 2257 *
CHYI-HOW LAY等: "Power generation in fed-batch and continuous up-flow microbial fuel cell from synthetic wastewater", ENERGY, vol. 91, pages 235 - 241 *
刘倩: "微生物电化学系统种群互作及胞外电子传递代谢调控机制", 博士电子期刊库, no. 01, pages 1 - 149 *

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN114958654A (en) * 2022-04-29 2022-08-30 江南大学 Propionic acid-producing type protein-philic bacterium derived from pit mud produced by brewing white spirit and application thereof
CN114958654B (en) * 2022-04-29 2023-09-22 江南大学 Propionic acid-producing proteophilic bacteria derived from white spirit brewing pit mud and application thereof

Also Published As

Publication number Publication date
CN113897318B (en) 2023-12-01

Similar Documents

Publication Publication Date Title
CN109055282B (en) Novel Klebsiella pneumoniae strain and separation method and application thereof
CN108298701B (en) Low-biodegradability fermentation wastewater treatment method after anaerobic treatment
CN110655198B (en) Method for treating nitrogen-containing wastewater by using heterotrophic nitrification-aerobic denitrification paracoccus strain
CN106477846B (en) Method for strengthening microbial electrolysis sludge hydrogen production and recycling struvite by adopting free nitrite
CN101225405A (en) Method for producing microbial flocculant and method of use thereof
Li et al. Hydrogen production characteristics of photoheterotrophic Rubrivivax gelatinosus L31
CN115385456B (en) Efficient denitrification sewage treatment agent and preparation method thereof
CN110656057B (en) Heterotrophic nitrification-aerobic denitrification paracoccus strain, seed liquid, preparation method and application thereof
CN115677059A (en) Application of yeast in treatment of dextran industrial wastewater
CN113897318B (en) Method for degrading protein by co-culturing acidophilic acid-producing protein bacterium and geobacillus thioreductase
CN111705089A (en) Method for promoting anaerobic fermentation of municipal excess sludge to produce volatile fatty acid
CN109504642B (en) Denitrifying bacterium and application thereof
CN113307377A (en) Method for treating fermentation exhaust gas and wastewater by coupling active microalgae
CN115159677B (en) Method for improving anaerobic digestion efficiency of organic wastewater and application thereof
CN116732111A (en) Method for promoting conversion of waste biomass energy by adopting persulfate oxidation and sulfate reduction bacteria novel system
CN107760636B (en) Denitrifying strain taking low-quality carbon source phenol as electron donor and application thereof
CN112694987B (en) Method for enriching and domesticating perchlorate reducing flora by using conductive material
CN110408658A (en) A method of polyhydroxyalkanoates is produced using white wine wastewater as matrix
CN113104991B (en) Two-stage co-anaerobic treatment process for simultaneously treating N, N-dimethylformamide and sludge
CN113444845A (en) Method for refining, detoxifying and producing acetone and butanol by fermentation of molasses
CN109762849B (en) Kasugamycin residue fermentation hydrogen production device and hydrogen production method thereof
CN113774104A (en) Method for preparing peptone and bio-organic fertilizer by using chondroitin sulfate wastewater
CN112279481A (en) Aluminum-carbon composite promoter and preparation method and application thereof
CN111607554A (en) Mixed metal salt formula for increasing biogas production amount of cassava vinasse waste liquid through fermentation
CN104609541A (en) Sebacic acid wastewater direct biochemical treatment method without desalination

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
GR01 Patent grant
GR01 Patent grant