CN111995026A - Environment-friendly efficient composite biological flocculant and preparation method thereof - Google Patents
Environment-friendly efficient composite biological flocculant and preparation method thereof Download PDFInfo
- Publication number
- CN111995026A CN111995026A CN202010600402.0A CN202010600402A CN111995026A CN 111995026 A CN111995026 A CN 111995026A CN 202010600402 A CN202010600402 A CN 202010600402A CN 111995026 A CN111995026 A CN 111995026A
- Authority
- CN
- China
- Prior art keywords
- flocculant
- preparation
- environment
- stirring
- microbial
- 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
- 239000002131 composite material Substances 0.000 title claims abstract description 59
- 238000002360 preparation method Methods 0.000 title claims abstract description 35
- 239000000243 solution Substances 0.000 claims abstract description 49
- 230000000813 microbial effect Effects 0.000 claims abstract description 47
- 238000003756 stirring Methods 0.000 claims abstract description 41
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 claims abstract description 36
- 238000000855 fermentation Methods 0.000 claims abstract description 34
- 230000004151 fermentation Effects 0.000 claims abstract description 34
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 28
- 239000008394 flocculating agent Substances 0.000 claims abstract description 26
- 229920000161 Locust bean gum Polymers 0.000 claims abstract description 23
- 239000000711 locust bean gum Substances 0.000 claims abstract description 23
- 235000010420 locust bean gum Nutrition 0.000 claims abstract description 23
- 239000000203 mixture Substances 0.000 claims abstract description 18
- 239000006228 supernatant Substances 0.000 claims abstract description 18
- HRPVXLWXLXDGHG-UHFFFAOYSA-N Acrylamide Chemical group NC(=O)C=C HRPVXLWXLXDGHG-UHFFFAOYSA-N 0.000 claims abstract description 17
- 239000002351 wastewater Substances 0.000 claims abstract description 17
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims abstract description 16
- FEWJPZIEWOKRBE-UHFFFAOYSA-N Tartaric acid Natural products [H+].[H+].[O-]C(=O)C(O)C(O)C([O-])=O FEWJPZIEWOKRBE-UHFFFAOYSA-N 0.000 claims abstract description 14
- 239000011975 tartaric acid Substances 0.000 claims abstract description 14
- 235000002906 tartaric acid Nutrition 0.000 claims abstract description 14
- 238000007789 sealing Methods 0.000 claims abstract description 13
- 238000001035 drying Methods 0.000 claims abstract description 12
- 230000001954 sterilising effect Effects 0.000 claims abstract description 12
- 239000007864 aqueous solution Substances 0.000 claims abstract description 11
- 235000013527 bean curd Nutrition 0.000 claims abstract description 11
- ZPWVASYFFYYZEW-UHFFFAOYSA-L dipotassium hydrogen phosphate Chemical compound [K+].[K+].OP([O-])([O-])=O ZPWVASYFFYYZEW-UHFFFAOYSA-L 0.000 claims abstract description 11
- 238000007710 freezing Methods 0.000 claims abstract description 11
- 230000008014 freezing Effects 0.000 claims abstract description 11
- 238000005406 washing Methods 0.000 claims abstract description 8
- 239000008367 deionised water Substances 0.000 claims abstract description 7
- 229910021641 deionized water Inorganic materials 0.000 claims abstract description 7
- 239000003999 initiator Substances 0.000 claims abstract description 7
- FEWJPZIEWOKRBE-JCYAYHJZSA-N Dextrotartaric acid Chemical compound OC(=O)[C@H](O)[C@@H](O)C(O)=O FEWJPZIEWOKRBE-JCYAYHJZSA-N 0.000 claims abstract description 6
- 239000007787 solid Substances 0.000 claims abstract description 6
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims abstract description 5
- 241001225321 Aspergillus fumigatus Species 0.000 claims description 16
- 244000063299 Bacillus subtilis Species 0.000 claims description 16
- 235000014469 Bacillus subtilis Nutrition 0.000 claims description 16
- 241000187561 Rhodococcus erythropolis Species 0.000 claims description 16
- 229940091771 aspergillus fumigatus Drugs 0.000 claims description 16
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 claims description 14
- 238000006243 chemical reaction Methods 0.000 claims description 12
- 244000005700 microbiome Species 0.000 claims description 10
- QKIUAMUSENSFQQ-UHFFFAOYSA-N dimethylazanide Chemical compound C[N-]C QKIUAMUSENSFQQ-UHFFFAOYSA-N 0.000 claims description 6
- 238000000227 grinding Methods 0.000 claims description 6
- 230000001678 irradiating effect Effects 0.000 claims description 6
- 238000001291 vacuum drying Methods 0.000 claims description 4
- 238000004659 sterilization and disinfection Methods 0.000 claims description 3
- 238000011049 filling Methods 0.000 claims description 2
- 238000011081 inoculation Methods 0.000 claims description 2
- 229910052757 nitrogen Inorganic materials 0.000 claims description 2
- 238000001556 precipitation Methods 0.000 claims description 2
- 230000003698 anagen phase Effects 0.000 claims 1
- 238000005189 flocculation Methods 0.000 abstract description 30
- 230000016615 flocculation Effects 0.000 abstract description 30
- 239000007788 liquid Substances 0.000 abstract description 9
- 231100000252 nontoxic Toxicity 0.000 abstract description 4
- 230000003000 nontoxic effect Effects 0.000 abstract description 4
- 238000013329 compounding Methods 0.000 abstract description 3
- 229910001873 dinitrogen Inorganic materials 0.000 abstract 1
- 230000000694 effects Effects 0.000 description 23
- 230000000052 comparative effect Effects 0.000 description 20
- 238000012360 testing method Methods 0.000 description 20
- 239000000047 product Substances 0.000 description 17
- RMBLTWUTZAFABA-XVSDJDOKSA-N (5z,8z,11z,14z)-icosa-5,8,11,14-tetraenoic acid;sodium Chemical compound [Na].CCCCC\C=C/C\C=C/C\C=C/C\C=C/CCCC(O)=O RMBLTWUTZAFABA-XVSDJDOKSA-N 0.000 description 10
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 description 10
- 150000004676 glycans Chemical class 0.000 description 9
- 229920001282 polysaccharide Polymers 0.000 description 9
- 239000005017 polysaccharide Substances 0.000 description 9
- 238000002835 absorbance Methods 0.000 description 8
- 239000002244 precipitate Substances 0.000 description 7
- 239000010865 sewage Substances 0.000 description 7
- 239000005995 Aluminium silicate Substances 0.000 description 6
- 238000012258 culturing Methods 0.000 description 6
- 229910000396 dipotassium phosphate Inorganic materials 0.000 description 6
- 235000019797 dipotassium phosphate Nutrition 0.000 description 6
- 239000002054 inoculum Substances 0.000 description 6
- LWIHDJKSTIGBAC-UHFFFAOYSA-K potassium phosphate Substances [K+].[K+].[K+].[O-]P([O-])([O-])=O LWIHDJKSTIGBAC-UHFFFAOYSA-K 0.000 description 6
- 235000012211 aluminium silicate Nutrition 0.000 description 5
- NLYAJNPCOHFWQQ-UHFFFAOYSA-N kaolin Chemical compound O.O.O=[Al]O[Si](=O)O[Si](=O)O[Al]=O NLYAJNPCOHFWQQ-UHFFFAOYSA-N 0.000 description 5
- 239000000178 monomer Substances 0.000 description 5
- 239000000725 suspension Substances 0.000 description 5
- 239000012043 crude product Substances 0.000 description 4
- 239000012153 distilled water Substances 0.000 description 4
- 238000000034 method Methods 0.000 description 4
- 238000002156 mixing Methods 0.000 description 4
- 229920005615 natural polymer Polymers 0.000 description 4
- 238000000746 purification Methods 0.000 description 4
- 238000007385 chemical modification Methods 0.000 description 3
- 150000001875 compounds Chemical class 0.000 description 3
- 238000011161 development Methods 0.000 description 3
- 229920001519 homopolymer Polymers 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- 238000005303 weighing Methods 0.000 description 3
- 241000282414 Homo sapiens Species 0.000 description 2
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 description 2
- 125000003178 carboxy group Chemical group [H]OC(*)=O 0.000 description 2
- 238000007334 copolymerization reaction Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 235000013305 food Nutrition 0.000 description 2
- 125000001165 hydrophobic group Chemical group 0.000 description 2
- 125000002887 hydroxy group Chemical group [H]O* 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 229920000642 polymer Polymers 0.000 description 2
- 229910052700 potassium Inorganic materials 0.000 description 2
- 239000011591 potassium Substances 0.000 description 2
- 230000028327 secretion Effects 0.000 description 2
- 238000001179 sorption measurement Methods 0.000 description 2
- 238000006467 substitution reaction Methods 0.000 description 2
- 238000004448 titration Methods 0.000 description 2
- 102000053602 DNA Human genes 0.000 description 1
- 108020004414 DNA Proteins 0.000 description 1
- 241000196324 Embryophyta Species 0.000 description 1
- WQZGKKKJIJFFOK-GASJEMHNSA-N Glucose Natural products OC[C@H]1OC(O)[C@H](O)[C@@H](O)[C@@H]1O WQZGKKKJIJFFOK-GASJEMHNSA-N 0.000 description 1
- 102000003886 Glycoproteins Human genes 0.000 description 1
- 108090000288 Glycoproteins Proteins 0.000 description 1
- 241001465754 Metazoa Species 0.000 description 1
- ISWSIDIOOBJBQZ-UHFFFAOYSA-N Phenol Chemical compound OC1=CC=CC=C1 ISWSIDIOOBJBQZ-UHFFFAOYSA-N 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 238000004220 aggregation Methods 0.000 description 1
- 230000002776 aggregation Effects 0.000 description 1
- 238000003556 assay Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000003054 catalyst Substances 0.000 description 1
- 125000002091 cationic group Chemical group 0.000 description 1
- 210000004027 cell Anatomy 0.000 description 1
- 239000001913 cellulose Substances 0.000 description 1
- 229920002678 cellulose Polymers 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 238000010790 dilution Methods 0.000 description 1
- 239000012895 dilution Substances 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 239000008103 glucose Substances 0.000 description 1
- 239000010842 industrial wastewater Substances 0.000 description 1
- 239000008235 industrial water Substances 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 239000011159 matrix material Substances 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 239000013618 particulate matter Substances 0.000 description 1
- 239000002846 particulate organic matter Substances 0.000 description 1
- OQUKIQWCVTZJAF-UHFFFAOYSA-N phenol;sulfuric acid Chemical compound OS(O)(=O)=O.OC1=CC=CC=C1 OQUKIQWCVTZJAF-UHFFFAOYSA-N 0.000 description 1
- 229920002401 polyacrylamide Polymers 0.000 description 1
- 230000037048 polymerization activity Effects 0.000 description 1
- 102000004169 proteins and genes Human genes 0.000 description 1
- 108090000623 proteins and genes Proteins 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 229930000044 secondary metabolite Natural products 0.000 description 1
- 210000001082 somatic cell Anatomy 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- QAOWNCQODCNURD-UHFFFAOYSA-N sulfuric acid Substances OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 1
- 229920001059 synthetic polymer Polymers 0.000 description 1
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/52—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
- C02F1/54—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities using organic material
- C02F1/56—Macromolecular compounds
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12N—MICROORGANISMS OR ENZYMES; COMPOSITIONS THEREOF; PROPAGATING, PRESERVING, OR MAINTAINING MICROORGANISMS; MUTATION OR GENETIC ENGINEERING; CULTURE MEDIA
- C12N1/00—Microorganisms, 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
- C12N1/14—Fungi; Culture media therefor
- C12N1/145—Fungal isolates
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12N—MICROORGANISMS OR ENZYMES; COMPOSITIONS THEREOF; PROPAGATING, PRESERVING, OR MAINTAINING MICROORGANISMS; MUTATION OR GENETIC ENGINEERING; CULTURE MEDIA
- C12N1/00—Microorganisms, 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
- C12N1/20—Bacteria; Culture media therefor
- C12N1/205—Bacterial isolates
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12P—FERMENTATION OR ENZYME-USING PROCESSES TO SYNTHESISE A DESIRED CHEMICAL COMPOUND OR COMPOSITION OR TO SEPARATE OPTICAL ISOMERS FROM A RACEMIC MIXTURE
- C12P1/00—Preparation of compounds or compositions, not provided for in groups C12P3/00 - C12P39/00, by using microorganisms or enzymes
- C12P1/02—Preparation of compounds or compositions, not provided for in groups C12P3/00 - C12P39/00, by using microorganisms or enzymes by using fungi
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12P—FERMENTATION OR ENZYME-USING PROCESSES TO SYNTHESISE A DESIRED CHEMICAL COMPOUND OR COMPOSITION OR TO SEPARATE OPTICAL ISOMERS FROM A RACEMIC MIXTURE
- C12P1/00—Preparation of compounds or compositions, not provided for in groups C12P3/00 - C12P39/00, by using microorganisms or enzymes
- C12P1/04—Preparation of compounds or compositions, not provided for in groups C12P3/00 - C12P39/00, by using microorganisms or enzymes by using bacteria
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/66—Treatment of water, waste water, or sewage by neutralisation; pH adjustment
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2303/00—Specific treatment goals
- C02F2303/04—Disinfection
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12R—INDEXING SCHEME ASSOCIATED WITH SUBCLASSES C12C - C12Q, RELATING TO MICROORGANISMS
- C12R2001/00—Microorganisms ; Processes using microorganisms
- C12R2001/01—Bacteria or Actinomycetales ; using bacteria or Actinomycetales
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12R—INDEXING SCHEME ASSOCIATED WITH SUBCLASSES C12C - C12Q, RELATING TO MICROORGANISMS
- C12R2001/00—Microorganisms ; Processes using microorganisms
- C12R2001/01—Bacteria or Actinomycetales ; using bacteria or Actinomycetales
- C12R2001/07—Bacillus
- C12R2001/125—Bacillus subtilis ; Hay bacillus; Grass bacillus
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12R—INDEXING SCHEME ASSOCIATED WITH SUBCLASSES C12C - C12Q, RELATING TO MICROORGANISMS
- C12R2001/00—Microorganisms ; Processes using microorganisms
- C12R2001/645—Fungi ; Processes using fungi
- C12R2001/66—Aspergillus
- C12R2001/68—Aspergillus fumigatus
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Zoology (AREA)
- Health & Medical Sciences (AREA)
- Wood Science & Technology (AREA)
- Genetics & Genomics (AREA)
- Bioinformatics & Cheminformatics (AREA)
- Biotechnology (AREA)
- Mycology (AREA)
- General Health & Medical Sciences (AREA)
- General Engineering & Computer Science (AREA)
- Biochemistry (AREA)
- Microbiology (AREA)
- Medicinal Chemistry (AREA)
- Tropical Medicine & Parasitology (AREA)
- Biomedical Technology (AREA)
- Virology (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Botany (AREA)
- Hydrology & Water Resources (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Separation Of Suspended Particles By Flocculating Agents (AREA)
Abstract
The invention discloses an environment-friendly efficient composite biological flocculant and a preparation method thereof, and relates to the technical field of flocculant preparation. The preparation method of the environment-friendly efficient composite bioflocculant comprises the following steps: adding dipotassium hydrogen phosphate into the bean curd wastewater, stirring and sterilizing to obtain a fermentation culture solution; inoculating microbial seed liquid, sealing, fermenting, centrifuging, taking supernatant, adding absolute ethyl alcohol, stirring and freezing to obtain various microbial flocculants. Dissolving sodium hydroxide and tartaric acid solid in deionized water, adding acrylamide monomer and locust bean gum aqueous solution, stirring, adjusting pH value, charging nitrogen gas, then adding initiator, standing after ultraviolet irradiation, washing, purifying, and drying to obtain the modified natural polymeric flocculant. And compounding the modified natural polymeric flocculant and the microbial flocculant mixture to obtain the environment-friendly high-efficiency composite biological flocculant. The composite biological flocculant has high flocculation performance, can reduce the dosage of the flocculant, and is safe, nontoxic and free of secondary pollution.
Description
Technical Field
The invention belongs to the technical field of flocculant preparation, and particularly relates to an environment-friendly efficient composite biological flocculant and a preparation method thereof.
Background
Water resources are important resources indispensable to the development of the human society and to the maintenance of various animal and plant life activities. Along with the rapid growth of population, the rapid development of social economy and the accelerated promotion of industrialization process, the contradiction between the industrial wastewater production and the domestic water demand produced by population life is sharp, and the crisis of water resources is obvious and urgent. Therefore, the problem of water treatment (including raw water treatment, sewage treatment, and industrial water treatment, etc.) has become more and more severe. Flocculation is one of the most common methods for removing particulate matter and organic matter from water, and a flocculant is one of the most important factors for determining flocculation effect.
At present, the most commonly used flocculating agents in the water treatment process are mainly inorganic flocculating agents and organic synthetic polymer flocculating agents, which cause certain pollution to the environment and even influence the health of human beings. The microbial flocculant is a secondary metabolite which is generated by microorganisms and can cause suspended particles, somatic cells and colloidal particles in a water body to coagulate and precipitate, mainly contains substances such as glycoprotein, polysaccharide, protein, cellulose, deoxyribonucleic acid and the like, is a high-efficiency, non-toxic and secondary-pollution-free green water treatment agent with biodegradability and safety, and has become one of hot spots of domestic and foreign researches in recent years. However, because the production cost of the microbial flocculant is high, the fermentation production process is not mature, and the molecular structure, shape, molecular mass, carried groups and the like of the microbial flocculant influence the activity of the flocculant, so that the development of the microbial flocculant is limited to a certain extent. The search for suitable composite biological flocculants is a new direction for preparing efficient, environment-friendly and safe flocculants.
Disclosure of Invention
The invention aims to provide an environment-friendly efficient composite bioflocculant and a preparation method thereof.
The technical scheme adopted by the invention for realizing the purpose is as follows:
a preparation method of an environment-friendly efficient composite biological flocculant comprises the following steps:
s1: adjusting the pH value of the bean curd wastewater, adding dipotassium hydrogen phosphate, stirring and sterilizing to obtain a fermentation culture solution;
s2: inoculating various microorganism seed solutions into the fermentation culture solution, and performing sealed fermentation culture to obtain fermentation strain solutions; centrifuging, adding absolute ethyl alcohol into the supernatant, stirring and freezing to obtain various microbial flocculants;
s3: dissolving sodium hydroxide and tartaric acid solid in deionized water, adding acrylamide monomer and locust bean gum aqueous solution, and stirring; adjusting the pH value of the reaction solution, filling nitrogen, then adding an initiator aqueous solution, sealing, irradiating by ultraviolet light, standing and washing; purifying with N, N-dimethyl amide, drying at constant temperature until the quality is unchanged, and grinding to obtain a modified natural polymeric flocculant;
s4: and (4) dissolving the mixture of the modified natural polymeric flocculant in the step S3 and the microbial flocculants in the step S2 in water, stirring, standing, performing centrifugal precipitation, and performing vacuum drying to obtain the composite biological flocculant. The composite biological flocculant is constructed by compounding a microbial flocculant mixture and a modified natural polymeric flocculant, the microbial flocculant is non-toxic, harmless and biodegradable, and the locust bean gum serving as a matrix of the modified polymeric flocculant has high safety and is often applied to the food industry. The two are compounded to ensure the safety of the composite biological flocculant, no secondary pollution is caused, and the composite biological flocculant belongs to a green environment-friendly flocculant. The locust bean gum has great amount of hydroxyl active groups in its structure, and is used as natural polymer compound through chemical modification of grafting copolymerization and other chemical modification, so as to improve the flocculation performance and dissolving performance greatly. The polyacrylamide is grafted to the molecular chain of the locust bean gum, so that the biological solubility of the locust bean gum is improved, the molecular weight is increased, the cationic degree is improved, and the flocculation effect of the composite bioflocculant is further improved; tartaric acid is an unsaturated dibasic acid, contains active double bonds and two carboxyl groups in the molecule, is a bio-based monomer with higher polymerization activity, is grafted to the molecular chain of the locust bean gum, enhances the bridging effect and the characteristic adsorption effect, and can improve the flocculation performance of the composite bioflocculant.
Preferably, the pH value of the bean curd wastewater in the step S1 is 6.8-7, the content of dipotassium hydrogen phosphate is 4-4.2 g/L, the sterilization temperature is 120-130 ℃, and the sterilization time is 20-30 min.
Preferably, the microorganism seed solution in step S2 includes: rhodococcus erythropolis, Aspergillus fumigatus, Bacillus subtilis; the inoculation amount of each microorganism is 5-8%, the fermentation temperature is 28-37 ℃, and the culture time is 60-80 h.
Preferably, the amount of the absolute ethyl alcohol added in the step S2 is 1.5-3 times of the volume of the supernatant; the centrifugal speed is 5800-7600 r/min, the centrifugal time is 11-13 min, the freezing temperature is 2-5 ℃, and the freezing time is 25-45 h.
Preferably, the molar ratio of the sodium hydroxide to the tartaric acid in the step S3 is 0.9-1: 1; the molar ratio of the acrylamide monomer to the tartaric acid is 1-1.2: 1; the mass fraction of the locust bean gum aqueous solution is 3-5%, the content of the locust bean gum is 15-18% of the total amount of the acrylamide monomer, and the initiator is azobisisobutyrimidazoline hydrochloride, the content of the initiator is 0.06-0.08% of the total amount of the acrylamide monomer.
Preferably, the pH value of the reaction solution in the step S3 is 4.0-5.0; the ultraviolet irradiation time is 110-125 min.
Preferably, in the step S3, the standing time is 2-3 h, the washing solution is acetone, and the constant-temperature drying temperature is (60 +/-2) DEG C.
Preferably, the mixture of microbial flocculants in step S4 includes: 30-45 parts by weight of a flocculating agent obtained by fermenting rhodococcus erythropolis, 10-25 parts by weight of a flocculating agent obtained by fermenting aspergillus fumigatus and 20-35 parts by weight of a flocculating agent obtained by fermenting bacillus subtilis.
Preferably, the composite bioflocculant in step S4 includes: 70-85 parts of a microbial flocculant mixture and 15-30 parts of a natural polymer modified flocculant by weight.
Preferably, in the step S4, the stirring time is 45-60 min, and the vacuum drying temperature is 55-60 ℃.
Preferably, the sodium arachidonic acid and the absolute ethyl alcohol are added into the fermentation strain liquid of the step S2, and the mixture is stirred to obtain modified microbial flocculants; wherein the volume ratio of the mass of the arachidonic acid sodium to the fermentation strain liquid is 1-1.1 g: 30 mL; stirring for 40-50 min; the volume ratio of the absolute ethyl alcohol to the fermentation strain liquid is 0.8-1: 5. One of the main components of the macromolecular polymer secreted outside cells by microorganisms is extracellular polysaccharide which has more hydrophilic groups such as hydroxyl, carboxyl and the like, and the aggregation of a microbial flocculant and target flocculate is hindered to a certain extent. After the arachidonic acid sodium salt in the mass-volume ratio range is added, the secretion of microbial extracellular polysaccharide can be promoted, and meanwhile, the arachidonic acid sodium salt can be combined with a microbial flocculant to reduce hydrophilic groups on the surface of the microbial flocculant and increase hydrophobic groups on the surface of the microbial flocculant, so that the flocculation performance of the microbial flocculant on flocculates is improved.
The invention also discloses an environment-friendly high-efficiency composite bioflocculant prepared by the preparation method.
The invention adopts the modified natural polymeric flocculant and the microbial flocculant to compound, thereby having the following beneficial effects:
the composite biological flocculant is constructed by compounding a microbial flocculant mixture and a natural polymer modified flocculant locust bean gum, the microbial flocculant is non-toxic, harmless and biodegradable, and the polymer modified flocculant locust bean gum has high safety and is often applied to the food industry. The safety of the composite biological flocculant is ensured, no secondary pollution is caused, and the composite biological flocculant is environment-friendly. Through chemical modification such as grafting/graft copolymerization, the flocculation effect and the solubility of the natural polymeric flocculant are improved, the natural polymeric flocculant is further compounded with the microbial flocculant, the bridging effect and the characteristic adsorption effect of the microbial flocculant are enhanced, and the flocculation performance of the composite biological flocculant is further improved. The microbial flocculant is modified by adding the arachidonic acid sodium, so that the secretion of extracellular polysaccharide of the microbes is promoted, meanwhile, the hydrophobic groups on the surface of the microbes can be increased, and the flocculation performance of the microbes on flocculates is further improved. The composite biological flocculant of the invention has less addition amount and convenient operation.
Therefore, the invention provides an environment-friendly high-efficiency composite biological flocculant and a preparation method thereof.
Drawings
FIG. 1 is a comparative graph showing the results of the flocculation test on the kaolin suspension in test example 1 of the present invention;
FIG. 2 is a comparison diagram of the results of tests on flocculation effect and COD removal rate of actual papermaking wastewater in test example 2 of the present invention;
FIG. 3 is a comparison diagram of the results of the flocculation effect and COD removal rate tests on municipal sewage in test example 3 of the present invention;
FIG. 4 is a comparison of the results of the measurement of the extracellular polysaccharide content of the microorganism in test example 4 of the present invention.
Detailed Description
The technical solution of the present invention is further described in detail below with reference to the following detailed description and the accompanying drawings:
example 1:
a preparation method of an environment-friendly efficient composite biological flocculant comprises the following steps:
s1: taking 50mL of bean curd wastewater, adjusting the pH to 7, adding 0.2g of dipotassium phosphate, stirring, and sterilizing at 121 ℃ for 20min to obtain a fermentation culture solution;
s2: respectively inoculating Rhodococcus erythropolis, Aspergillus fumigatus and Bacillus subtilis to the fermentation culture solution according to the inoculum size of 6%, sealing, fermenting and culturing at 31 deg.C under shaking of 140r/min in incubator for 80 h; centrifuging at 7000r/min for 10min, collecting supernatant, adding 2 times of anhydrous ethanol, stirring, and freezing at 2 deg.C for 40min to obtain microbial flocculants;
s3: weighing sodium hydroxide and tartaric acid solids with the same molar mass, dissolving in deionized water, and mixing the components according to the weight ratio of acrylamide monomer: adding acrylamide monomer into tartaric acid at a molar mass ratio of 1.2:1, adding 3% locust bean gum aqueous solution (the content of the locust bean gum is 16% of the total amount of the acrylamide monomer), and stirring to form a uniform solution; the concentration of the catalyst is 0.1 mol.L-1Adjusting pH of the reaction solution to 5 with hydrochloric acid solution and sodium hydroxide solution, adding 0.06% azobisisobutyrimidazoline hydrochloride, rapidly sealing, placing in ultraviolet device (power of 500W, dominant wavelength of 365nm, light intensity of 1200 μ W cm)-2) Irradiating for 120min, standing and curing for 2h, extracting a product in a reaction bottle by using acetone, and washing for multiple times to obtain a crude product; then the product is subjected to Soxhlet purification by using N, N-dimethyl amide to remove homopolymerizationPlacing the mixture and unreacted monomers in an oven, drying at a constant temperature of 60 ℃ until the mass of the mixture is unchanged, and grinding to obtain a modified natural polymeric flocculant;
s4: and (2) dissolving 20 parts by weight of the modified natural polymeric flocculant in the step S3 and 80 parts by weight of the microbial flocculant mixture in the step S2 (wherein 35 parts by weight of the flocculant obtained by fermenting rhodococcus erythropolis, 20 parts by weight of the flocculant obtained by fermenting aspergillus fumigatus and 25 parts by weight of the flocculant obtained by fermenting bacillus subtilis) in water, stirring for 50min at 130rpm, standing, centrifuging, collecting precipitate, and drying in vacuum at 60 ℃ to obtain the composite biological flocculant.
Example 2:
a preparation method of an environment-friendly efficient composite biological flocculant comprises the following steps:
s1: taking 50mL of bean curd wastewater, adjusting the pH to 7, adding 0.2g of dipotassium phosphate, stirring, and sterilizing at 121 ℃ for 20min to obtain a fermentation culture solution;
s2: respectively inoculating Rhodococcus erythropolis, Aspergillus fumigatus and Bacillus subtilis to the fermentation culture solution according to the inoculum size of 6%, sealing, fermenting and culturing at 31 deg.C under shaking of 140r/min in incubator for 80h to obtain fermentation strain solution; then, according to the mass-volume ratio of the arachidonic acid sodium to the fermentation strain liquid of 1 g: adding arachidonic acid sodium in an amount of 30mL, adding absolute ethyl alcohol according to the volume ratio of the absolute ethyl alcohol to the fermentation strain liquid of 1:5, and stirring for 45 min; centrifuging at 7000r/min for 10min, collecting supernatant, adding 2 times of anhydrous ethanol, stirring, and freezing at 2 deg.C for 40min to obtain modified microbial flocculants;
s3: weighing sodium hydroxide and tartaric acid solids with the same molar mass, dissolving in deionized water, and mixing the components according to the weight ratio of acrylamide monomer: adding acrylamide monomer into tartaric acid at a molar mass ratio of 1.2:1, adding 3% locust bean gum aqueous solution (the content of the locust bean gum is 16% of the total amount of the acrylamide monomer), and stirring to form a uniform solution; adjusting the pH value of the reaction solution to 5 by using hydrochloric acid solution with the concentration of 0.1 mol.L < -1 > and sodium hydroxide solution, then adding 0.06 percent of azobisisobutyrimidazoline hydrochloride, quickly sealing, placing in an ultraviolet device (the power is 500W, the dominant wavelength is 365nm, and the light intensity is 1200 mu W.cm < -2 >) for irradiating for 120min, standing and curing for 2h, extracting the product in a reaction bottle by using acetone, and washing for multiple times to obtain a crude product; performing Soxhlet purification on the product by using N, N-dimethyl amide to remove homopolymers and unreacted monomers in the product, then placing the product in an oven for drying at a constant temperature of 60 ℃ until the quality is unchanged, and grinding the product to obtain a modified natural polymeric flocculant;
s4: and (2) dissolving 20 parts by weight of the modified natural polymeric flocculant obtained in the step S3 and 80 parts by weight of the microbial flocculant mixture modified in the step S2 (wherein 35 parts by weight of the flocculant obtained by fermenting rhodococcus erythropolis, 20 parts by weight of the flocculant obtained by fermenting aspergillus fumigatus and 25 parts by weight of the flocculant obtained by fermenting bacillus subtilis) in water, stirring for 50min at 130rpm, standing, centrifuging, collecting precipitate, and drying in vacuum at 60 ℃ to obtain the composite biological flocculant.
Comparative example 1:
a preparation method of a composite biological flocculant comprises the following steps:
s1: taking 50mL of bean curd wastewater, adjusting the pH to 7, adding 0.2g of dipotassium phosphate, stirring, and sterilizing at 121 ℃ for 20min to obtain a fermentation culture solution;
s2: respectively inoculating Rhodococcus erythropolis, Aspergillus fumigatus and Bacillus subtilis to the fermentation culture solution according to the inoculum size of 6%, sealing, fermenting and culturing at 31 deg.C under shaking of 140r/min in incubator for 80 h; centrifuging at 7000r/min for 10min, collecting supernatant, adding 2 times of anhydrous ethanol, stirring, and freezing at 2 deg.C for 40min to obtain microbial flocculants; taking 35 parts by weight of a flocculant obtained by fermenting rhodococcus erythropolis, 20 parts by weight of a flocculant obtained by fermenting aspergillus fumigatus and 25 parts by weight of a flocculant obtained by fermenting bacillus subtilis, and mixing the two parts in water to obtain the microbial flocculant blend.
Comparative example 2:
a preparation method of a composite biological flocculant comprises the following steps:
s1: taking 50mL of bean curd wastewater, adjusting the pH to 7, adding 0.2g of dipotassium phosphate, stirring, and sterilizing at 121 ℃ for 20min to obtain a fermentation culture solution;
s2: respectively inoculating Rhodococcus erythropolis, Aspergillus fumigatus and Bacillus subtilis to the fermentation culture solution according to the inoculum size of 6%, sealing, fermenting and culturing at 31 deg.C under shaking of 140r/min in incubator for 80 h; centrifuging at 7000r/min for 10min, collecting supernatant, adding 2 times of anhydrous ethanol, stirring, and freezing at 2 deg.C for 40min to obtain microbial flocculants;
s3: according to the weight parts, 20 parts of locust bean gum base natural polymeric flocculant and 80 parts of each microbial flocculant mixture obtained in the step S2 (wherein, 35 parts of flocculant obtained by fermenting rhodococcus erythropolis, 20 parts of flocculant obtained by fermenting aspergillus fumigatus and 25 parts of flocculant obtained by fermenting bacillus subtilis) are dissolved in water together, stirred for 50min at 130rpm, kept stand, centrifuged to collect precipitate, and dried in vacuum at 60 ℃ to obtain the composite biological flocculant.
Comparative example 3:
a preparation method of a composite biological flocculant comprises the following steps:
s1: taking 50mL of bean curd wastewater, adjusting the pH to 7, adding 0.2g of dipotassium phosphate, stirring, and sterilizing at 121 ℃ for 20min to obtain a fermentation culture solution;
s2: respectively inoculating Rhodococcus erythropolis, Aspergillus fumigatus and Bacillus subtilis to the fermentation culture solution according to the inoculum size of 6%, sealing, fermenting and culturing at 31 deg.C under shaking of 140r/min in incubator for 80 h; centrifuging at 7000r/min for 10min, collecting supernatant, adding 2 times of anhydrous ethanol, stirring, and freezing at 2 deg.C for 40min to obtain microbial flocculants;
s3: adding acrylamide monomer into deionized water, adding 3 wt% of locust bean gum aqueous solution (the content of the locust bean gum is 16% of the total amount of the acrylamide monomer), and stirring to form a uniform solution; adjusting the pH value of the reaction solution to 5 by using hydrochloric acid solution with the concentration of 0.1 mol.L < -1 > and sodium hydroxide solution, then adding 0.06 percent of azobisisobutyrimidazoline hydrochloride, quickly sealing, placing in an ultraviolet device (the power is 500W, the dominant wavelength is 365nm, and the light intensity is 1200 mu W.cm < -2 >) for irradiating for 120min, standing and curing for 2h, extracting the product in a reaction bottle by using acetone, and washing for multiple times to obtain a crude product; performing Soxhlet purification on the product by using N, N-dimethyl amide to remove homopolymers and unreacted monomers in the product, then placing the product in an oven for drying at a constant temperature of 60 ℃ until the quality is unchanged, and grinding the product to obtain a modified natural polymeric flocculant;
s4: and (2) dissolving 20 parts by weight of the modified natural polymeric flocculant in the step S3 and 80 parts by weight of the microbial flocculant mixture in the step S2 (wherein 35 parts by weight of the flocculant obtained by fermenting rhodococcus erythropolis, 20 parts by weight of the flocculant obtained by fermenting aspergillus fumigatus and 25 parts by weight of the flocculant obtained by fermenting bacillus subtilis) in water, stirring for 50min at 130rpm, standing, centrifuging, collecting precipitate, and drying in vacuum at 60 ℃ to obtain the composite biological flocculant.
Comparative example 4:
a preparation method of a composite biological flocculant comprises the following steps:
s1: taking 50mL of bean curd wastewater, adjusting the pH to 7, adding 0.2g of dipotassium phosphate, stirring, and sterilizing at 121 ℃ for 20min to obtain a fermentation culture solution;
s2: respectively inoculating Rhodococcus erythropolis, Aspergillus fumigatus and Bacillus subtilis to the fermentation culture solution according to the inoculum size of 6%, sealing, fermenting and culturing at 31 deg.C under shaking of 140r/min in incubator for 80 h; centrifuging at 7000r/min for 10min, collecting supernatant, adding 2 times of anhydrous ethanol, stirring, and freezing at 2 deg.C for 40min to obtain microbial flocculants;
s3: weighing sodium hydroxide and tartaric acid solid with the same molar mass, dissolving in deionized water, adding 3% locust bean gum aqueous solution (the content of locust bean gum is 16% of total amount of tartaric acid), and stirring to form uniform solution; adjusting the pH value of the reaction solution to 5 by using hydrochloric acid solution with the concentration of 0.1 mol.L < -1 > and sodium hydroxide solution, then adding 0.06 percent of azobisisobutyrimidazoline hydrochloride, quickly sealing, placing in an ultraviolet device (the power is 500W, the dominant wavelength is 365nm, and the light intensity is 1200 mu W.cm < -2 >) for irradiating for 120min, standing and curing for 2h, extracting the product in a reaction bottle by using acetone, and washing for multiple times to obtain a crude product; performing Soxhlet purification on the product by using N, N-dimethyl amide to remove homopolymers and unreacted monomers in the product, then placing the product in an oven for drying at a constant temperature of 60 ℃ until the quality is unchanged, and grinding the product to obtain a modified natural polymeric flocculant;
s4: and (2) dissolving 20 parts by weight of the modified natural polymeric flocculant in the step S3 and 80 parts by weight of the microbial flocculant mixture in the step S2 (wherein 35 parts by weight of the flocculant obtained by fermenting rhodococcus erythropolis, 20 parts by weight of the flocculant obtained by fermenting aspergillus fumigatus and 25 parts by weight of the flocculant obtained by fermenting bacillus subtilis) in water, stirring for 50min at 130rpm, standing, centrifuging, collecting precipitate, and drying in vacuum at 60 ℃ to obtain the composite biological flocculant.
Test example 1:
testing of flocculation Effect on Kaolin suspension
1.2g of kaolin (d 44 μm 325 mesh) was accurately weighed into 300mL of distilled water to prepare a 4g/L kaolin suspension, and 3mL of 1% CaCl was added2The solution was stirred and dispersed for 15min at 700 rpm. Then adding 0.3mg of composite biological flocculant, quickly stirring for 30s at the rotating speed of 400rpm, slowly stirring for 5min at the rotating speed of 100rpm, standing for 10min, taking the supernatant, measuring the absorbance at the wavelength of 550nm, and taking the absorbance of a blank group without the composite biological flocculant as a control. The flocculation rate of the kaolin suspension is calculated according to the following formula:
Y=(A1-A2)/A1×100%
wherein, the flocculation rate of the Y-kaolin suspension is expressed in unit; a. the1-absorbance of the blank supernatant; a. the2-assay group supernatant absorbance.
The above tests were carried out for example 1, example 2, comparative example 1, comparative example 2, comparative example 3, comparative example 4, and the results of the experimental tests are shown in fig. 1. As can be seen from the figure, the flocculation performance of the composite biological flocculants prepared in the examples 1 and 2 is obviously better than that of the comparative example, and the flocculation effect can reach 99 percent at most. The flocculation effect of the composite flocculant is improved by the composite construction of the natural polymer modified flocculant and the microbial flocculant, and the flocculation effect of the composite flocculant can be further improved by modifying the structure of the microbial flocculant. The test result shows that the environment-friendly efficient composite biological flocculant prepared by the invention has high activity, excellent flocculation effect and no secondary pollution.
Test example 2:
flocculation effect on actual papermaking wastewater (main material content is shown in table 1):
TABLE 1 papermaking wastewater
Adjusting the pH value of 300mL of actual papermaking wastewater to 7.0, adding 0.3mg of composite bioflocculant, quickly stirring for 30s at the rotation speed of 400rpm, slowly stirring for 5min at the rotation speed of 100rpm, standing for 10min, measuring the absorbance of supernatant at the wavelength of 550nm, and calculating the flocculation rate; meanwhile, measuring COD by using a potassium dichromate-ferrous ammonium sulfate titration method, and calculating the removal rate of the COD.
The above tests were carried out for example 1, example 2, comparative example 1, comparative example 2, comparative example 3, comparative example 4, and the results of the experimental tests are shown in fig. 2. As can be seen from the figure, the flocculation effect and the COD removal rate of the composite biological flocculant prepared in the example 1 and the example 2 on the actual papermaking wastewater are higher than those of the comparative example. Experimental structures show that the flocculation effect of the environment-friendly efficient composite bioflocculant on actual papermaking wastewater is over 95%, and the removal rate of COD is over 85%.
Test example 3:
flocculation effect on municipal sewage (main material content shown in table 2):
TABLE 2 municipal sewage
Adjusting the pH value of 300mL of urban sewage to 7.0, adding 0.3mg of composite bioflocculant, quickly stirring for 30s at the rotation speed of 400rpm, slowly stirring for 5min at the rotation speed of 100rpm, standing for 10min, measuring the absorbance of supernatant at the wavelength of 550nm, and calculating the flocculation rate; meanwhile, measuring COD by using a potassium dichromate-ferrous ammonium sulfate titration method, and calculating the removal rate of the COD.
The above tests were carried out for example 1, example 2, comparative example 1, comparative example 2, comparative example 3, comparative example 4, and the results of the experimental tests are shown in fig. 3. As can be seen from the figure, the flocculation effect and the COD removal rate of the composite biological flocculants prepared in the examples 1 and 2 on the municipal sewage are higher than those of the comparative examples. The microbial flocculant compound has a flocculation effect on municipal sewage of more than 96 percent and a COD removal rate of more than 85 percent.
Test example 4:
and (3) detecting the extracellular polysaccharide of the microorganism:
and detecting by adopting a phenol-sulfuric acid method. The fermentation strain liquid obtained in the step S2 in the example 1 and the fermentation strain liquid obtained in the step S2 in the example 2 after the arachidonic acid sodium salt is added are respectively taken and centrifuged for 15min at the rotating speed of 1500r/min, 0.2mL of supernatant is absorbed into a 1.5mL finger-shaped tube, 0.8mL of absolute ethyl alcohol is added into the finger-shaped tube, the finger-shaped tube is placed in a refrigerator with the temperature of-4 ℃ for standing overnight after being shaken evenly, and then the finger-shaped tube is taken out and centrifuged for 15min at the speed of 3000 r/min. Removing supernatant, dissolving precipitate with 1mL distilled water, adding 0.5mL redissolved solution into 15mL test tube (provided with a blank tube, and replacing redissolved solution with distilled water), adding 0.5mL distilled water, 1mL 5% phenol and 5mL concentrated sulfuric acid, mixing, cooling to room temperature, and measuring absorbance (OD)490nm). And calculating the extracellular polysaccharide content of the fermentation liquid according to a glucose concentration-absorbance standard curve equation and the dilution condition which are measured in parallel.
The results of the experiment are shown in FIG. 4. As can be seen from the figure, the extracellular polysaccharide content of the fermentation broth after the arachidonic acid sodium is added in the example 2 is higher than that of the example 1, which shows that the arachidonic acid sodium can promote the microorganisms to secrete the extracellular polysaccharide, and further improves the flocculation performance of the microbial flocculant.
The above description is only for the specific embodiments of the present invention, but the scope of the present invention is not limited thereto, and any person skilled in the art can easily conceive of the changes or substitutions within the technical scope of the present invention, and all the changes or substitutions should be covered within the scope of the present invention. Therefore, the protection scope of the present invention shall be subject to the protection scope of the appended claims.
Claims (10)
1. A preparation method of an environment-friendly efficient composite biological flocculant comprises the following steps:
s1: adjusting the pH value of the bean curd wastewater, adding dipotassium hydrogen phosphate, stirring and sterilizing to obtain a fermentation culture solution;
s2: inoculating various microorganism seed solutions into the fermentation culture solution, and performing sealed fermentation culture to obtain fermentation strain solutions; centrifuging, adding absolute ethyl alcohol into the supernatant, stirring and freezing to obtain various microbial flocculants;
s3: dissolving sodium hydroxide and tartaric acid solid in deionized water, adding acrylamide monomer and locust bean gum aqueous solution, and stirring; adjusting the pH value of the reaction solution, filling nitrogen, then adding an initiator aqueous solution, sealing, irradiating by ultraviolet light, standing and washing; purifying with N, N-dimethyl amide, drying at constant temperature until the quality is unchanged, and grinding to obtain a modified natural polymeric flocculant;
s4: and (4) dissolving the mixture of the modified natural polymeric flocculant in the step S3 and the microbial flocculant in the step S2 in water, stirring, standing, performing centrifugal precipitation, and performing vacuum drying to obtain the composite biological flocculant.
2. The preparation method of the environment-friendly efficient composite bioflocculant according to claim 1, wherein the preparation method comprises the following steps: in the step S1, the pH value of the bean curd waste water is 6.8-7, the content of dipotassium hydrogen phosphate is 4-4.2 g/L, and the sterilization temperature is 120-130 ℃.
3. The preparation method of the environment-friendly efficient composite bioflocculant according to claim 1, wherein the preparation method comprises the following steps: in the step S2, the microbial seed solutions are all in logarithmic growth phase, including: rhodococcus erythropolis, Aspergillus fumigatus, Bacillus subtilis; the inoculation amount of each microorganism is 5-8%, the fermentation temperature is 28-37 ℃, the rotating speed is 140-150 r/min, and the culture time is 60-80 h.
4. The preparation method of the environment-friendly efficient composite bioflocculant according to claim 1, wherein the preparation method comprises the following steps: and in the step S2, the amount of the absolute ethyl alcohol added is 1.5-3 times of the volume of the supernatant.
5. The preparation method of the environment-friendly efficient composite bioflocculant according to claim 1, wherein the preparation method comprises the following steps: the molar mass ratio of the sodium hydroxide to the tartaric acid in the step S3 is 0.9-1: 1; the molar mass ratio of the acrylamide monomer to the tartaric acid is 1-1.2: 1; the mass fraction of the locust bean gum aqueous solution is 3-5%, the content of the locust bean gum is 15-18% of the total amount of the acrylamide monomer, and the initiator is azobisisobutyrimidazoline hydrochloride, the content of the initiator is 0.06-0.08% of the total amount of the acrylamide monomer.
6. The preparation method of the environment-friendly efficient composite bioflocculant according to claim 1, wherein the preparation method comprises the following steps: the pH value of the reaction solution is 4.0-5.0; the ultraviolet irradiation time is 110-125 min.
7. The preparation method of the environment-friendly efficient composite bioflocculant according to claim 1, wherein the preparation method comprises the following steps: the mixture of microbial flocculants in step S4 includes: 30-45 parts by weight of a flocculating agent obtained by fermenting rhodococcus erythropolis, 10-25 parts by weight of a flocculating agent obtained by fermenting aspergillus fumigatus and 20-35 parts by weight of a flocculating agent obtained by fermenting bacillus subtilis.
8. The preparation method of the environment-friendly efficient composite bioflocculant according to claim 1, wherein the preparation method comprises the following steps: the composite biological flocculant in the step S4 comprises the following steps: 70-85 parts of a microbial flocculant mixture and 15-30 parts of a modified natural polymeric flocculant by weight.
9. The preparation method of the environment-friendly efficient composite bioflocculant according to claim 1, wherein the preparation method comprises the following steps: in the step S4, the stirring time is 45-60 min, and the vacuum drying temperature is 55-60 ℃.
10. The environment-friendly efficient composite biological flocculant prepared by the preparation method of claim 1.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202010600402.0A CN111995026B (en) | 2020-06-28 | 2020-06-28 | Environment-friendly efficient composite biological flocculant and preparation method thereof |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202010600402.0A CN111995026B (en) | 2020-06-28 | 2020-06-28 | Environment-friendly efficient composite biological flocculant and preparation method thereof |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN111995026A true CN111995026A (en) | 2020-11-27 |
| CN111995026B CN111995026B (en) | 2022-06-21 |
Family
ID=73466653
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202010600402.0A Active CN111995026B (en) | 2020-06-28 | 2020-06-28 | Environment-friendly efficient composite biological flocculant and preparation method thereof |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN111995026B (en) |
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113087166A (en) * | 2021-04-06 | 2021-07-09 | 江苏建筑职业技术学院 | Sewage treatment flocculant and preparation method thereof |
| CN113804788A (en) * | 2021-09-17 | 2021-12-17 | 湖南省茶叶研究所(湖南省茶叶检测中心) | Metabonomics-based method for researching action mechanism of aged Liupao tea for preventing and treating obesity |
| CN114229992A (en) * | 2021-12-16 | 2022-03-25 | 李立欣 | A kind of preparation of composite modified carrier and sewage treatment method |
| CN114478922A (en) * | 2022-02-22 | 2022-05-13 | 海南扬航实业有限公司 | Preparation process of high-solubility high-molecular-weight cationic polyacrylamide |
| CN115259209A (en) * | 2022-08-24 | 2022-11-01 | 萍乡宝海锌营养科技有限公司 | Method for producing food-grade zinc sulfate by using industrial-grade zinc sulfate as raw material |
| CN115959749A (en) * | 2022-11-18 | 2023-04-14 | 曹学深 | A kind of environment-friendly high-efficiency composite biological flocculant and preparation method thereof |
| CN116495880A (en) * | 2023-04-14 | 2023-07-28 | 海南省智慧环境投资控股有限公司 | Treatment process and application of a magnetic activated carbon aerobic granular sludge membrane bioreactor |
| WO2025141398A1 (en) | 2023-12-27 | 2025-07-03 | Universidade De Coimbra | Bacterial biopolymer formulation suitable for the treatment of wastewater with suspended solids, methods of producing and using the same |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1142837A (en) * | 1993-12-22 | 1997-02-12 | 施托克豪森公司 | Graft copolymers of unsaturated monomers and polyhydroxy compounds, process for producing them and their use |
| US6416668B1 (en) * | 1999-09-01 | 2002-07-09 | Riad A. Al-Samadi | Water treatment process for membranes |
| CN103073680A (en) * | 2013-01-28 | 2013-05-01 | 重庆大学 | Synthetic method of ultraviolet initiated hydrophobic modified cationic polyacrylamide |
| US20140309392A1 (en) * | 2011-11-04 | 2014-10-16 | Akzo Nobel Chemicals International B.V. | Graft dendrite copolymers, and methods for producing the same |
| US20160023933A1 (en) * | 2014-07-24 | 2016-01-28 | Hong Kong Baptist University | BioFerric-Flocculant Enhanced Primary Treatment Process (BEPT) for Sewage Treatment |
| CN108793426A (en) * | 2018-06-19 | 2018-11-13 | 深圳文科园林股份有限公司 | A kind of microbial flocculant compound preparation method and its application in water treatment field |
-
2020
- 2020-06-28 CN CN202010600402.0A patent/CN111995026B/en active Active
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1142837A (en) * | 1993-12-22 | 1997-02-12 | 施托克豪森公司 | Graft copolymers of unsaturated monomers and polyhydroxy compounds, process for producing them and their use |
| US6416668B1 (en) * | 1999-09-01 | 2002-07-09 | Riad A. Al-Samadi | Water treatment process for membranes |
| US20140309392A1 (en) * | 2011-11-04 | 2014-10-16 | Akzo Nobel Chemicals International B.V. | Graft dendrite copolymers, and methods for producing the same |
| CN103073680A (en) * | 2013-01-28 | 2013-05-01 | 重庆大学 | Synthetic method of ultraviolet initiated hydrophobic modified cationic polyacrylamide |
| US20160023933A1 (en) * | 2014-07-24 | 2016-01-28 | Hong Kong Baptist University | BioFerric-Flocculant Enhanced Primary Treatment Process (BEPT) for Sewage Treatment |
| CN108793426A (en) * | 2018-06-19 | 2018-11-13 | 深圳文科园林股份有限公司 | A kind of microbial flocculant compound preparation method and its application in water treatment field |
Cited By (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113087166A (en) * | 2021-04-06 | 2021-07-09 | 江苏建筑职业技术学院 | Sewage treatment flocculant and preparation method thereof |
| CN113804788A (en) * | 2021-09-17 | 2021-12-17 | 湖南省茶叶研究所(湖南省茶叶检测中心) | Metabonomics-based method for researching action mechanism of aged Liupao tea for preventing and treating obesity |
| CN113804788B (en) * | 2021-09-17 | 2023-11-21 | 湖南省茶叶研究所(湖南省茶叶检测中心) | Metabonomics-based aged Liupu tea action mechanism research method for preventing and treating obesity |
| CN114229992A (en) * | 2021-12-16 | 2022-03-25 | 李立欣 | A kind of preparation of composite modified carrier and sewage treatment method |
| CN114229992B (en) * | 2021-12-16 | 2022-10-28 | 广州市天河区林和粤财技术服务中心 | Preparation of composite modified carrier and sewage treatment method |
| CN114478922A (en) * | 2022-02-22 | 2022-05-13 | 海南扬航实业有限公司 | Preparation process of high-solubility high-molecular-weight cationic polyacrylamide |
| CN114478922B (en) * | 2022-02-22 | 2024-02-06 | 海南扬航实业有限公司 | Preparation process of high-solubility high-molecular-weight cationic polyacrylamide |
| CN115259209A (en) * | 2022-08-24 | 2022-11-01 | 萍乡宝海锌营养科技有限公司 | Method for producing food-grade zinc sulfate by using industrial-grade zinc sulfate as raw material |
| CN115959749A (en) * | 2022-11-18 | 2023-04-14 | 曹学深 | A kind of environment-friendly high-efficiency composite biological flocculant and preparation method thereof |
| CN116495880A (en) * | 2023-04-14 | 2023-07-28 | 海南省智慧环境投资控股有限公司 | Treatment process and application of a magnetic activated carbon aerobic granular sludge membrane bioreactor |
| WO2025141398A1 (en) | 2023-12-27 | 2025-07-03 | Universidade De Coimbra | Bacterial biopolymer formulation suitable for the treatment of wastewater with suspended solids, methods of producing and using the same |
Also Published As
| Publication number | Publication date |
|---|---|
| CN111995026B (en) | 2022-06-21 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN111995026B (en) | Environment-friendly efficient composite biological flocculant and preparation method thereof | |
| CN102910721B (en) | A kind of composite biological flocculant and its preparation method and application | |
| CN105858880B (en) | A method for immobilized anammox coupled with short-range denitrification to treat municipal sewage and nitrate wastewater | |
| CN108298701A (en) | A kind of fermentation waste water processing method of low biodegradability after Anaerobic Treatment | |
| CN102532418B (en) | A graft-modified composite biological flocculant and its preparation method | |
| JP4172294B2 (en) | Organic sludge treatment method and treatment system | |
| CN105505913B (en) | A kind of anaerobic bacteria process for fixation | |
| CN1261583C (en) | Method for producing acrylamide using microbial catalyst washed with acrylic acid aqueous solution | |
| CN101805707A (en) | Producing strain for producing microbial flocculating agent by using starch wastewater and production process thereof | |
| CN110218682B (en) | Pseudomycosis bacillus and application thereof in sludge reduction | |
| CN113401997A (en) | Extracellular polysaccharide sewage treatment flocculant and preparation method thereof | |
| CN112375721A (en) | Preparation method and application of composite microbial inoculum for low-temperature treatment of rural domestic sewage | |
| CN112939417B (en) | Activated sludge conditioner for wastewater biochemical treatment and preparation method thereof | |
| CN102408146B (en) | Composite bio-flocculant grafted acrylamide flocculant and its preparation method | |
| CN104803569A (en) | Method for treating sludge through coupling of electrochemistry and flocculant | |
| CN108660178A (en) | A kind of preparation method of high flocculating rate microbial flocculant | |
| CN111235057B (en) | A kind of biological bacterial agent for treating polyacrylamide wastewater and its preparation method and application | |
| CN120172471A (en) | A recyclable composite water purifier and preparation method thereof | |
| CN1207214C (en) | Economic inorganic-organic composite flocculant | |
| CN111748057A (en) | A kind of method for synthesizing gum arabic high polymer by composite initiation system | |
| CN109734840B (en) | A kind of preparation method of natural graft flocculant based on β-CD | |
| CN111349626A (en) | Immobilized microorganism for sewage treatment and preparation method and application thereof | |
| CN101560536A (en) | Fermentation method of microbial polysaccharide flocculant | |
| CN101942407B (en) | Producing strain and production method for producing microbial flocculant from wheat starch waste water | |
| CN116462318A (en) | A kind of composite carbon source for waste water treatment and its application |
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 | ||
| TA01 | Transfer of patent application right |
Effective date of registration: 20220519 Address after: 342599 No. 18, building 2, No. 153, Hongdu Avenue, Xianghu Town, Ruijin City, Ganzhou City, Jiangxi Province Applicant after: Lai Jiping Address before: 314300 West District, 211 Yanbei Road, Wuyuan Street, Haiyan County, Jiaxing City, Zhejiang Province, 2 Blocks 102-9 Applicant before: JIAXING JUETUO TECHNOLOGY Co.,Ltd. |
|
| TA01 | Transfer of patent application right | ||
| GR01 | Patent grant | ||
| GR01 | Patent grant |