CN106180140B - A kind of minimizing technology of Heavy Metal Pollution in Municipal Solid Waste object - Google Patents
A kind of minimizing technology of Heavy Metal Pollution in Municipal Solid Waste object Download PDFInfo
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- CN106180140B CN106180140B CN201610565027.4A CN201610565027A CN106180140B CN 106180140 B CN106180140 B CN 106180140B CN 201610565027 A CN201610565027 A CN 201610565027A CN 106180140 B CN106180140 B CN 106180140B
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- heavy metal
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- water
- polycarbonate
- sulfuric acid
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- 229910001385 heavy metal Inorganic materials 0.000 title claims abstract description 71
- 239000010813 municipal solid waste Substances 0.000 title claims abstract description 39
- 238000005516 engineering process Methods 0.000 title claims abstract description 16
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 44
- KRKNYBCHXYNGOX-UHFFFAOYSA-N citric acid Chemical compound OC(=O)CC(O)(C(O)=O)CC(O)=O KRKNYBCHXYNGOX-UHFFFAOYSA-N 0.000 claims abstract description 42
- 229920005989 resin Polymers 0.000 claims abstract description 33
- 239000011347 resin Substances 0.000 claims abstract description 33
- 229920000515 polycarbonate Polymers 0.000 claims abstract description 30
- 239000004417 polycarbonate Substances 0.000 claims abstract description 30
- PPBRXRYQALVLMV-UHFFFAOYSA-N Styrene Chemical compound C=CC1=CC=CC=C1 PPBRXRYQALVLMV-UHFFFAOYSA-N 0.000 claims abstract description 20
- 229920002239 polyacrylonitrile Polymers 0.000 claims abstract description 17
- 238000000108 ultra-filtration Methods 0.000 claims abstract description 16
- 238000006243 chemical reaction Methods 0.000 claims abstract description 15
- 238000010521 absorption reaction Methods 0.000 claims abstract description 14
- 150000001875 compounds Chemical class 0.000 claims abstract description 14
- 238000009300 dissolved air flotation Methods 0.000 claims abstract description 11
- 230000002378 acidificating effect Effects 0.000 claims abstract description 10
- NWUYHJFMYQTDRP-UHFFFAOYSA-N 1,2-bis(ethenyl)benzene;1-ethenyl-2-ethylbenzene;styrene Chemical compound C=CC1=CC=CC=C1.CCC1=CC=CC=C1C=C.C=CC1=CC=CC=C1C=C NWUYHJFMYQTDRP-UHFFFAOYSA-N 0.000 claims abstract description 9
- 239000003729 cation exchange resin Substances 0.000 claims abstract description 9
- 230000000536 complexating effect Effects 0.000 claims abstract description 7
- 239000000706 filtrate Substances 0.000 claims abstract description 6
- PTMHPRAIXMAOOB-UHFFFAOYSA-N phosphoramidic acid Chemical group NP(O)(O)=O PTMHPRAIXMAOOB-UHFFFAOYSA-N 0.000 claims abstract description 6
- 235000012489 doughnuts Nutrition 0.000 claims abstract 2
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 claims description 100
- 239000012528 membrane Substances 0.000 claims description 42
- 229920002678 cellulose Polymers 0.000 claims description 25
- 239000001913 cellulose Substances 0.000 claims description 25
- 229910052751 metal Inorganic materials 0.000 claims description 21
- 239000002184 metal Substances 0.000 claims description 21
- MEYZYGMYMLNUHJ-UHFFFAOYSA-N tunicamycin Natural products CC(C)CCCCCCCCCC=CC(=O)NC1C(O)C(O)C(CC(O)C2OC(C(O)C2O)N3C=CC(=O)NC3=O)OC1OC4OC(CO)C(O)C(O)C4NC(=O)C MEYZYGMYMLNUHJ-UHFFFAOYSA-N 0.000 claims description 16
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 claims description 15
- 239000000243 solution Substances 0.000 claims description 15
- 229910052718 tin Inorganic materials 0.000 claims description 15
- 239000012510 hollow fiber Substances 0.000 claims description 14
- 239000007788 liquid Substances 0.000 claims description 14
- IAZDPXIOMUYVGZ-UHFFFAOYSA-N Dimethylsulphoxide Chemical compound CS(C)=O IAZDPXIOMUYVGZ-UHFFFAOYSA-N 0.000 claims description 10
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 claims description 10
- ATJFFYVFTNAWJD-UHFFFAOYSA-N Tin Chemical compound [Sn] ATJFFYVFTNAWJD-UHFFFAOYSA-N 0.000 claims description 10
- 125000000218 acetic acid group Chemical group C(C)(=O)* 0.000 claims description 10
- 229960001760 dimethyl sulfoxide Drugs 0.000 claims description 10
- 150000002500 ions Chemical class 0.000 claims description 10
- 230000003647 oxidation Effects 0.000 claims description 10
- 238000007254 oxidation reaction Methods 0.000 claims description 10
- 238000002360 preparation method Methods 0.000 claims description 10
- GETQZCLCWQTVFV-UHFFFAOYSA-N trimethylamine Chemical compound CN(C)C GETQZCLCWQTVFV-UHFFFAOYSA-N 0.000 claims description 10
- 239000007864 aqueous solution Substances 0.000 claims description 9
- 229910021645 metal ion Inorganic materials 0.000 claims description 9
- SZYJELPVAFJOGJ-UHFFFAOYSA-N trimethylamine hydrochloride Chemical compound Cl.CN(C)C SZYJELPVAFJOGJ-UHFFFAOYSA-N 0.000 claims description 9
- 239000005703 Trimethylamine hydrochloride Substances 0.000 claims description 8
- -1 glassware Substances 0.000 claims description 8
- 239000002734 clay mineral Substances 0.000 claims description 6
- BRLQWZUYTZBJKN-UHFFFAOYSA-N Epichlorohydrin Chemical compound ClCC1CO1 BRLQWZUYTZBJKN-UHFFFAOYSA-N 0.000 claims description 5
- 229920002488 Hemicellulose Polymers 0.000 claims description 5
- 230000004888 barrier function Effects 0.000 claims description 5
- 239000011449 brick Substances 0.000 claims description 5
- 239000002131 composite material Substances 0.000 claims description 5
- 239000002361 compost Substances 0.000 claims description 5
- 239000012153 distilled water Substances 0.000 claims description 5
- 239000000835 fiber Substances 0.000 claims description 5
- 239000011888 foil Substances 0.000 claims description 5
- 238000006703 hydration reaction Methods 0.000 claims description 5
- 229910052759 nickel Inorganic materials 0.000 claims description 5
- 239000002957 persistent organic pollutant Substances 0.000 claims description 5
- 229920003023 plastic Polymers 0.000 claims description 5
- 239000004033 plastic Substances 0.000 claims description 5
- 229920002635 polyurethane Polymers 0.000 claims description 5
- 239000004814 polyurethane Substances 0.000 claims description 5
- 238000006479 redox reaction Methods 0.000 claims description 5
- 239000007787 solid Substances 0.000 claims description 5
- 238000010129 solution processing Methods 0.000 claims description 5
- 239000007921 spray Substances 0.000 claims description 5
- 239000004575 stone Substances 0.000 claims description 5
- 238000001914 filtration Methods 0.000 claims description 3
- 239000004743 Polypropylene Substances 0.000 claims description 2
- 230000000694 effects Effects 0.000 claims description 2
- 150000002825 nitriles Chemical class 0.000 claims description 2
- 229920001155 polypropylene Polymers 0.000 claims description 2
- PXGOKWXKJXAPGV-UHFFFAOYSA-N Fluorine Chemical compound FF PXGOKWXKJXAPGV-UHFFFAOYSA-N 0.000 claims 1
- OHBTULDTCSOWOY-UHFFFAOYSA-N [C].C=C Chemical group [C].C=C OHBTULDTCSOWOY-UHFFFAOYSA-N 0.000 claims 1
- 229910052802 copper Inorganic materials 0.000 claims 1
- 239000011737 fluorine Substances 0.000 claims 1
- 229910052731 fluorine Inorganic materials 0.000 claims 1
- 238000002347 injection Methods 0.000 claims 1
- 239000007924 injection Substances 0.000 claims 1
- 150000003839 salts Chemical class 0.000 claims 1
- 239000002910 solid waste Substances 0.000 claims 1
- 238000000034 method Methods 0.000 abstract description 22
- 239000000356 contaminant Substances 0.000 abstract description 7
- 238000001179 sorption measurement Methods 0.000 abstract description 5
- 239000002699 waste material Substances 0.000 abstract description 5
- 238000010327 methods by industry Methods 0.000 abstract 1
- 239000002351 wastewater Substances 0.000 description 11
- 150000004696 coordination complex Chemical class 0.000 description 8
- 239000000839 emulsion Substances 0.000 description 8
- 230000008569 process Effects 0.000 description 8
- 239000002689 soil Substances 0.000 description 8
- 239000006260 foam Substances 0.000 description 7
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 6
- 229910052799 carbon Inorganic materials 0.000 description 6
- 230000015556 catabolic process Effects 0.000 description 5
- 150000001768 cations Chemical class 0.000 description 5
- 238000006731 degradation reaction Methods 0.000 description 5
- 238000012545 processing Methods 0.000 description 5
- 239000002033 PVDF binder Substances 0.000 description 4
- 230000003197 catalytic effect Effects 0.000 description 4
- PCHJSUWPFVWCPO-UHFFFAOYSA-N gold Chemical compound [Au] PCHJSUWPFVWCPO-UHFFFAOYSA-N 0.000 description 4
- 229910052737 gold Inorganic materials 0.000 description 4
- 239000010931 gold Substances 0.000 description 4
- 230000006872 improvement Effects 0.000 description 4
- 239000012535 impurity Substances 0.000 description 4
- 229910052742 iron Inorganic materials 0.000 description 4
- 239000000203 mixture Substances 0.000 description 4
- 239000002245 particle Substances 0.000 description 4
- 229920002981 polyvinylidene fluoride Polymers 0.000 description 4
- 238000000746 purification Methods 0.000 description 4
- 238000012360 testing method Methods 0.000 description 3
- NLHHRLWOUZZQLW-UHFFFAOYSA-N Acrylonitrile Chemical compound C=CC#N NLHHRLWOUZZQLW-UHFFFAOYSA-N 0.000 description 2
- 239000010791 domestic waste Substances 0.000 description 2
- 239000003344 environmental pollutant Substances 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 150000002894 organic compounds Chemical class 0.000 description 2
- 231100000719 pollutant Toxicity 0.000 description 2
- 238000003723 Smelting Methods 0.000 description 1
- 230000002159 abnormal effect Effects 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 229910052793 cadmium Inorganic materials 0.000 description 1
- BDOSMKKIYDKNTQ-UHFFFAOYSA-N cadmium atom Chemical compound [Cd] BDOSMKKIYDKNTQ-UHFFFAOYSA-N 0.000 description 1
- 239000000149 chemical water pollutant Substances 0.000 description 1
- 229910017052 cobalt Inorganic materials 0.000 description 1
- 239000010941 cobalt Substances 0.000 description 1
- GUTLYIVDDKVIGB-UHFFFAOYSA-N cobalt atom Chemical compound [Co] GUTLYIVDDKVIGB-UHFFFAOYSA-N 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 238000001514 detection method Methods 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 235000013399 edible fruits Nutrition 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 239000010793 electronic waste Substances 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 150000002148 esters Chemical class 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 238000011010 flushing procedure Methods 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- 230000036541 health Effects 0.000 description 1
- 238000007654 immersion Methods 0.000 description 1
- JEIPFZHSYJVQDO-UHFFFAOYSA-N iron(III) oxide Inorganic materials O=[Fe]O[Fe]=O JEIPFZHSYJVQDO-UHFFFAOYSA-N 0.000 description 1
- 238000002386 leaching Methods 0.000 description 1
- QSHDDOUJBYECFT-UHFFFAOYSA-N mercury Chemical compound [Hg] QSHDDOUJBYECFT-UHFFFAOYSA-N 0.000 description 1
- 229910052753 mercury Inorganic materials 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 239000012466 permeate Substances 0.000 description 1
- 238000000053 physical method Methods 0.000 description 1
- 238000011954 pollution control method Methods 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 238000009270 solid waste treatment Methods 0.000 description 1
- 239000004071 soot Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000010998 test method Methods 0.000 description 1
- 238000003911 water pollution Methods 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B09—DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
- B09B—DISPOSAL OF SOLID WASTE NOT OTHERWISE PROVIDED FOR
- B09B3/00—Destroying solid waste or transforming solid waste into something useful or harmless
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B09—DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
- B09B—DISPOSAL OF SOLID WASTE NOT OTHERWISE PROVIDED FOR
- B09B3/00—Destroying solid waste or transforming solid waste into something useful or harmless
- B09B3/10—Destroying solid waste or transforming solid waste into something useful or harmless involving an adsorption step
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B09—DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
- B09B—DISPOSAL OF SOLID WASTE NOT OTHERWISE PROVIDED FOR
- B09B5/00—Operations not covered by a single other subclass or by a single other group in this subclass
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08B—POLYSACCHARIDES; DERIVATIVES THEREOF
- C08B3/00—Preparation of cellulose esters of organic acids
- C08B3/06—Cellulose acetate, e.g. mono-acetate, di-acetate or tri-acetate
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J5/00—Manufacture of articles or shaped materials containing macromolecular substances
- C08J5/18—Manufacture of films or sheets
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L33/00—Compositions of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and only one being terminated by only one carboxyl radical, or of salts, anhydrides, esters, amides, imides or nitriles thereof; Compositions of derivatives of such polymers
- C08L33/18—Homopolymers or copolymers of nitriles
- C08L33/20—Homopolymers or copolymers of acrylonitrile
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L69/00—Compositions of polycarbonates; Compositions of derivatives of polycarbonates
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J2333/00—Characterised by the use of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and only one being terminated by only one carboxyl radical, or of salts, anhydrides, esters, amides, imides, or nitriles thereof; Derivatives of such polymers
- C08J2333/18—Homopolymers or copolymers of nitriles
- C08J2333/20—Homopolymers or copolymers of acrylonitrile
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J2369/00—Characterised by the use of polycarbonates; Derivatives of polycarbonates
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J2433/00—Characterised by the use of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and only one being terminated by only one carboxyl radical, or of salts, anhydrides, esters, amides, imides, or nitriles thereof; Derivatives of such polymers
- C08J2433/18—Homopolymers or copolymers of nitriles
- C08J2433/20—Homopolymers or copolymers of acrylonitrile
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J2469/00—Characterised by the use of polycarbonates; Derivatives of polycarbonates
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Polymers & Plastics (AREA)
- Health & Medical Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Medicinal Chemistry (AREA)
- Organic Chemistry (AREA)
- Environmental & Geological Engineering (AREA)
- Manufacturing & Machinery (AREA)
- Materials Engineering (AREA)
- Life Sciences & Earth Sciences (AREA)
- Biochemistry (AREA)
- Treatment Of Water By Ion Exchange (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
The invention discloses a kind of minimizing technologies of Heavy Metal Pollution in Municipal Solid Waste object, the described method comprises the following steps:(1) not available waste is sorted out, crushes plus house refuse homogenate is made in suitable quantity of water homogenate;(2) four layers of macroporous absorption film reaction tank of rubbish homogenate multipass, the heavy metal contaminants in Adsorption rubbish homogenate;(3) it is 2~3 that PH is adjusted after being diluted with water, and adds citric acid, cycles through strongly acidic styrene type cation exchange resin column, then pass through polycarbonate doughnut and the compound ultrafiltration membrance filter of polyacrylonitrile;(4) by step (3) resulting filtrate by pressurized dissolved air flotation, by air-float technology except the oil film and oil droplet in decontaminated water, then by removing unadsorbed heavy metal ion again containing amino-phosphonic acid functional groups complexing resin;Entire process engineering of the invention is reasonable, easy to operate, at low cost, can be widely applied to the removal of heavy metal contaminants in house refuse.
Description
Technical field
The present invention relates to field of solid waste treatment, and in particular to the removal side of heavy metal in a kind of domestic waste
Method.
Background technique
With the expansion of city size, municipal refuse yield is growing day by day.Since China's majority municipal refuse is non-classified
It collects, a large amount of electronic wastes, which enter soot, causes refuse landfill heavy metal pollution serious.These heavy metals pass through food simultaneously
Object chain enters human body and constitutes a serious threat to the health of resident.Since heavy metal has relative stability and difficult to degrade in the environment
Property, it cannot be degraded by microorganisms, be difficult to clear out from environment, so that Heavy Metal Pollution Control is very difficult.Therefore city
Rubbish Heavy Metal Pollution Control has become key subjects urgently to be solved in the development process of current city.
Due to continuous improvement of people's living standards, the heavy metal in daily necessities be increased, while a large amount of electricity
Sub- product abandonment object is unprocessed to be stacked together with house refuse, and heavy metals in garbage is caused to increase.Heavy metal one in rubbish
Aspect is to stacking and Soil Surrounding pollutes, and another aspect landfill leachate is discharged into river or the water that permeates the ground, and causes ground
Lower water pollution.
Heavy metal pollution is different from the pollution of other organic compounds.Many organic compounds can pass through nature itself
Physics, chemical or biological purification makes harmfulness reduce or release.And heavy metal has enriching, is difficult in the environment
Degradation.Nowadays China is due to causing many heavy metals such as lead, mercury, cadmium, cobalt etc. in the exploitation, smelting, process of heavy metal
Cause serious environmental pollution into big gas and water, soil.Such as with useless
Domestic and foreign scholars have conducted extensive research heavy metal pollution of soil improvement for a long time, achieve certain improvement
Effect.Currently used Heavy Metal Pollution Control method has physical method(Soil improvement by importing soil from other places, leaching method, absorption fixation), chemistry side
Method(Biological reducing, complexing extraction)And vitrifying, soil flushing and electro reclamation etc., but these methods engineering amounts are big, investment
Valuableness, rehabilitation cost is high, needs to bother soil texture, can only small area pollution control, be difficult to be widely applied.At this
It needs directly to handle rubbish under kind background, reduces pollution of the heavy metal in rubbish to soil.
Summary of the invention
The technical problem to be solved in the present invention is to provide a kind of simple processes, and design is rationally, at low cost, are used for urban life
The method of heavy metals in garbage removal.
A kind of minimizing technology of Heavy Metal Pollution in Municipal Solid Waste object, includes the following steps:
(1)It is not available solid that consumer garbage compost is rejected into plastic foil, Fibre Bag, metal, glassware, brick and tile stone
Body waste is sorted out, in mass ratio 1 after then crushing residual refuse:1 is added water, is placed in homogenized on refiner and is made
House refuse homogenate;
(2)Four layers of macroporous absorption film reaction tank of rubbish homogenate multipass, the first tunic of reactor tank are package sulfuric acid
Macroreticular resin exchange membrane, wrap up heavy metal Zn in the H+ and homogenate in the sulfuric acid in the macroreticular resin exchange membrane of sulfuric acid, Cu,
Redox reaction occurs for Co, Ni, Sn, Fe, generates Zn2+, Cu2+, Co2+, Ni2+, Sn2+, Fe2+, makes the gold in homogenate
Category all exists in a manner of metal ion;Second tunic of reactor tank is the poly-vinylidene-fluoride composite film for being enclosed with active carbon,
Third tunic is the microporous barrier that modified cellulose and polyurethane are combined, and wherein the content of modified cellulose is 5%;4th layer
Film is the macroporous absorption film of clay mineral;
(3)Being diluted with water to after concentration is 20% to processed homogenate and adding PH regulator adjusting PH is 2 ~ 3, so
The citric acid that the concentration measured relative to 0.2 times of homogenate is 0.3mol/L is added thereto afterwards, is 200 ~ 300r/min in revolving speed
Shaking table on shake 2 ~ 3h after cycle through strongly acidic styrene type cation exchange resin column, then by polycarbonate and poly-
The compound hollow fiber ultrafiltration membrane filtering of acrylonitrile;
(4)By step(3)Resulting filtrate by pressurized dissolved air flotation, by air-float technology except in decontaminated water oil film and
Oil droplet and other organic pollutants, it is then unadsorbed by being removed again containing amino-phosphonic acid functional groups complexing resin
Heavy metal ion, so that the heavy metal contaminants content in liquid reaches discharge standard.
Further, the macroreticular resin exchange membrane house refuse homogenate of the package sulfuric acid can be rapidly from macrovoid
It passes through, but since heavy metal partial size is excessive, so metal cannot pass through, simultaneously when passing through in homogenate containing heavy metal
The sulfuric acid wrapped up in the exchange membrane of sulfuric acid can react with heavy metal, generate heavy metal ion, then metal then passes through
The macroreticular resin exchange membrane for wrapping up sulfuric acid can save the dosage of sulfuric acid, and sulfuric acid with the macroreticular resin exchange membrane of package sulfuric acid
It is big with metal contact surface, it reacts more complete.
Further, the preparation process of the modified cellulose is:Concentrated hydrochloric acid is reacted with trimethylamine generates front three amine salt
Hydrochlorate, then cellulose cation-exchanger made from trimethylamine hydrochloride and epichlorohydrin reaction is added to immersion hemicellulose
In the dimethyl sulphoxide solution of element, NaOH solution processing is then added, acetyl progress acetyl is then added and is modified, it is made
Standby unmodified cellulose molecule amount is high, palliating degradation degree is low, adsorption capacity is strong.
Further, the mass concentration of the sulfuric acid is 45 ~ 55%.
Further, the citric acid that is added into rubbish homogenate is since citric acid and metal ion are complexed
Metal complex is generated after reaction, metal complex contains lone pair electrons pair, exchanges and sets by strongly acidic styrene's cation
Rouge column can be combined with the cation of resin column to be haved the function that recycle heavy metal.
Further, the pressurized dissolved air flotation facture is exactly to be passed through air into waste water in hyperbaric environment, so
Air is precipitated from water in the form of micro-bubble afterwards becomes carrier, makes the pollutants such as oil emulsion, the small suspended particulate in waste water
Matter is adhered on bubble, is floated to the water surface with bubble, is formed foam-gas and water, particle(Oil)Three-phase mixture passes through receipts
Collection foam or dross achieve the purpose that separate impurity, remove oil film and oil droplet.The method is mainly used to handle to be leaned in rubbish homogenate
Natural subsidence or floating are difficult to the oil emulsion removed or relative density close to 1 small suspended particulate.
Further, the preparation process of the polycarbonate and the compound hollow fiber ultrafiltration membrane of polyacrylonitrile is poly- carbon
Acid esters issues raw hydration reaction in organic oxidation tin catalytic action, using organic oxidation tin is filtered out, obtains polycarbonate water
Then polycarbonate aqueous solution is mixed to obtain film liquid with the dimethyl sulphoxide solution of polyacrylonitrile by solution, then by film liquid with it is interior
It is to form a film in the bath of outer inner gel media gel that gel media passes through spray head to inject with distilled water simultaneously, that is, obtains polycarbonate and gather
The compound hollow fiber ultrafiltration membrane of acrylonitrile.
The beneficial effects of the present invention are embodied in:The method of heavy metal contaminants in removal domestic waste of the invention
Simple process, it is easy to operate, it is at low cost, it can be reduced in heavy metal processing using the macroreticular resin exchange membrane of package sulfuric acid in the process
Cost, and metal and sulfuric acid contact face are big, react more complete, then pass through active carbon, modified cellulose, clay mineral absorption
Heavy metal ion, and repeatedly recycled in reactor tank, removal metal pollutant is more thorough;It can be removed using pressurized dissolved air flotation
Oil film and oil droplet in rubbish go removing heavy metals more complete to subsequent.Entire technical process continuous operation, to removal life rubbish
Heavy metal in rubbish is complete, and not will cause secondary pollution.
Specific embodiment
Embodiment 1:A kind of minimizing technology of Heavy Metal Pollution in Municipal Solid Waste object, includes the following steps:
(1)It is not available solid that consumer garbage compost is rejected into plastic foil, Fibre Bag, metal, glassware, brick and tile stone
Body waste is sorted out, in mass ratio 1 after then crushing residual refuse:1 is added water, is placed in homogenized on refiner and is made
House refuse homogenate;
(2)Four layers of macroporous absorption film reaction tank of rubbish homogenate multipass, the first tunic of reactor tank are package sulfuric acid
Macroreticular resin exchange membrane, wrap up heavy metal Zn in the H+ and homogenate in the sulfuric acid in the macroreticular resin exchange membrane of sulfuric acid, Cu,
Redox reaction occurs for Co, Ni, Sn, Fe, generates Zn2+, Cu2+, Co2+, Ni2+, Sn2+, Fe2+, makes the gold in homogenate
Category all exists in a manner of metal ion;Second tunic of reactor tank is the poly-vinylidene-fluoride composite film for being enclosed with active carbon,
Third tunic is the microporous barrier that modified cellulose and polyurethane are combined, and wherein the content of modified cellulose is 5%;4th layer
Film is the macroporous absorption film of clay mineral;
(3)Being diluted with water to after concentration is 20% to processed homogenate and adding PH regulator adjusting PH is 2, then
The citric acid that the concentration measured relative to 0.2 times of homogenate is 0.3mol/L is added thereto, in the shaking table that revolving speed is 200r/min
Strongly acidic styrene type cation exchange resin column is cycled through after upper shake 2h, it is then multiple by polycarbonate and polyacrylonitrile
The hollow fiber ultrafiltration membrane of conjunction filters;
(4)By step(3)Resulting filtrate by pressurized dissolved air flotation, by air-float technology except in decontaminated water oil film and
Oil droplet and other organic pollutants, it is then unadsorbed by being removed again containing amino-phosphonic acid functional groups complexing resin
Heavy metal ion, so that the heavy metal contaminants content in liquid reaches discharge standard.
Wherein, the macroreticular resin exchange membrane house refuse homogenate of the package sulfuric acid can be worn from macrovoid rapidly
It crosses, but since heavy metal partial size is excessive, so metal cannot pass through when passing through in homogenate containing heavy metal, wraps simultaneously
Wrapping up in the sulfuric acid in the exchange membrane of sulfuric acid can react with heavy metal, generate heavy metal ion, then metal then passes through packet
The macroreticular resin exchange membrane for wrapping up in sulfuric acid can save the dosage of sulfuric acid with the macroreticular resin exchange membrane of package sulfuric acid, and sulfuric acid with
Metal contact surface is big, reacts more complete.
Wherein, the mass concentration of the sulfuric acid is 45%.
Wherein, the preparation process of the modified cellulose is:Concentrated hydrochloric acid is reacted with trimethylamine generates trimethylamine hydrochloride,
Cellulose cation-exchanger made from trimethylamine hydrochloride and epichlorohydrin reaction is added to again and impregnates hemicellulose
In dimethyl sulphoxide solution, NaOH solution processing is then added, acetyl progress acetyl is then added and is modified, prepared by
Unmodified cellulose molecule amount is high, palliating degradation degree is low, adsorption capacity is strong.
Wherein, the citric acid that is added into rubbish homogenate is since complex reaction occurs for citric acid and metal ion
After generate metal complex, metal complex contains lone pair electrons pair, passes through strongly acidic styrene type cation exchange resin column
It can be combined with the cation of resin column and have the function that recycle heavy metal.
Wherein, the pressurized dissolved air flotation facture is exactly to be passed through air into waste water in hyperbaric environment, then empty
Gas is precipitated from water in the form of micro-bubble becomes carrier, keeps the polluters such as oil emulsion, the small suspended particulate in waste water viscous
It is attached on bubble, floats to the water surface with bubble, form one gas and water of foam, particle(Oil)Three-phase mixture is steeped by collecting
Foam or dross achieve the purpose that separate impurity, the oil film in decontaminated water and oil droplet, purification waste water.It is useless that the method is mainly used to processing
The oil emulsion removed or relative density are difficult to close to 1 small suspended particulate by natural subsidence or floating in water.
Wherein, the preparation process of the polycarbonate and the compound hollow fiber ultrafiltration membrane of polyacrylonitrile is polycarbonate
Raw hydration reaction is issued in organic oxidation tin catalytic action, using organic oxidation tin is filtered out, obtains polycarbonate aqueous solution,
Then polycarbonate aqueous solution is mixed into obtain film liquid with the dimethyl sulphoxide solution of polyacrylonitrile, then film liquid and inner gel is situated between
It is to form a film in the bath of outer inner gel media gel that matter passes through spray head to inject with distilled water simultaneously, i.e. acquisition polycarbonate and polyacrylonitrile
Compound hollow fiber ultrafiltration membrane.
Embodiment 2:A kind of minimizing technology of Heavy Metal Pollution in Municipal Solid Waste object, includes the following steps:
(1)It is not available solid that consumer garbage compost is rejected into plastic foil, Fibre Bag, metal, glassware, brick and tile stone
Body waste is sorted out, in mass ratio 1 after then crushing residual refuse:1 is added water, is placed in homogenized on refiner and is made
House refuse homogenate;
(2)Four layers of macroporous absorption film reaction tank of rubbish homogenate multipass, the first tunic of reactor tank are package sulfuric acid
Macroreticular resin exchange membrane, wrap up heavy metal Zn in the H+ and homogenate in the sulfuric acid in the macroreticular resin exchange membrane of sulfuric acid, Cu,
Redox reaction occurs for Co, Ni, Sn, Fe, generates Zn2+, Cu2+, Co2+, Ni2+, Sn2+, Fe2+, makes the gold in homogenate
Category all exists in a manner of metal ion;Second tunic of reactor tank is the poly-vinylidene-fluoride composite film for being enclosed with active carbon,
Third tunic is the microporous barrier that modified cellulose and polyurethane are combined, and wherein the content of modified cellulose is 5%;4th layer
Film is the macroporous absorption film of clay mineral;
(3)Being diluted with water to after concentration is 20% to processed homogenate and adding PH regulator adjusting PH is 2.5, so
The citric acid that the concentration measured relative to 0.2 times of homogenate is 0.3mol/L is added thereto afterwards, is shaking for 250r/min in revolving speed
Strongly acidic styrene type cation exchange resin column is cycled through after shaking 2.5h on bed, then passes through polycarbonate and polypropylene
The compound hollow fiber ultrafiltration membrane filtering of nitrile;
(4)By step(3)Resulting filtrate by pressurized dissolved air flotation, by air-float technology except in decontaminated water oil film and
Oil droplet and other organic pollutants, it is then unadsorbed by being removed again containing amino-phosphonic acid functional groups complexing resin
Heavy metal ion, so that the heavy metal contaminants content in liquid reaches discharge standard.
Wherein, the macroreticular resin exchange membrane house refuse homogenate of the package sulfuric acid can be worn from macrovoid rapidly
It crosses, but since heavy metal partial size is excessive, so metal cannot pass through when passing through in homogenate containing heavy metal, wraps simultaneously
Wrapping up in the sulfuric acid in the exchange membrane of sulfuric acid can react with heavy metal, generate heavy metal ion, then metal then passes through packet
The macroreticular resin exchange membrane for wrapping up in sulfuric acid can save the dosage of sulfuric acid with the macroreticular resin exchange membrane of package sulfuric acid, and sulfuric acid with
Metal contact surface is big, reacts more complete.
Wherein, the mass concentration of the sulfuric acid is 50%.
Wherein, the preparation process of the modified cellulose is:Concentrated hydrochloric acid is reacted with trimethylamine generates trimethylamine hydrochloride,
Cellulose cation-exchanger made from trimethylamine hydrochloride and epichlorohydrin reaction is added to again and impregnates hemicellulose
In dimethyl sulphoxide solution, NaOH solution processing is then added, acetyl progress acetyl is then added and is modified, prepared by
Unmodified cellulose molecule amount is high, palliating degradation degree is low, adsorption capacity is strong.
Wherein, the citric acid that is added into rubbish homogenate is since complex reaction occurs for citric acid and metal ion
After generate metal complex, metal complex contains lone pair electrons pair, passes through strongly acidic styrene type cation exchange resin column
It can be combined with the cation of resin column and have the function that recycle heavy metal.
Wherein, the pressurized dissolved air flotation facture is exactly to be passed through air into waste water in hyperbaric environment, then empty
Gas is precipitated from water in the form of micro-bubble becomes carrier, keeps the polluters such as oil emulsion, the small suspended particulate in waste water viscous
It is attached on bubble, floats to the water surface with bubble, form one gas and water of foam, particle(Oil)Three-phase mixture is steeped by collecting
Foam or dross achieve the purpose that separate impurity, the oil film in decontaminated water and oil droplet, purification waste water.It is useless that the method is mainly used to processing
The oil emulsion removed or relative density are difficult to close to 1 small suspended particulate by natural subsidence or floating in water.
Wherein, the preparation process of the polycarbonate and the compound hollow fiber ultrafiltration membrane of polyacrylonitrile is polycarbonate
Raw hydration reaction is issued in organic oxidation tin catalytic action, using organic oxidation tin is filtered out, obtains polycarbonate aqueous solution,
Then polycarbonate aqueous solution is mixed into obtain film liquid with the dimethyl sulphoxide solution of polyacrylonitrile, then film liquid and inner gel is situated between
It is to form a film in the bath of outer inner gel media gel that matter passes through spray head to inject with distilled water simultaneously, i.e. acquisition polycarbonate and polyacrylonitrile
Compound hollow fiber ultrafiltration membrane.
Embodiment 3:A kind of minimizing technology of Heavy Metal Pollution in Municipal Solid Waste object, includes the following steps:
(1)It is not available solid that consumer garbage compost is rejected into plastic foil, Fibre Bag, metal, glassware, brick and tile stone
Body waste is sorted out, in mass ratio 1 after then crushing residual refuse:1 is added water, is placed in homogenized on refiner and is made
House refuse homogenate;
(2)Four layers of macroporous absorption film reaction tank of rubbish homogenate multipass, the first tunic of reactor tank are package sulfuric acid
Macroreticular resin exchange membrane, wrap up heavy metal Zn in the H+ and homogenate in the sulfuric acid in the macroreticular resin exchange membrane of sulfuric acid, Cu,
Redox reaction occurs for Co, Ni, Sn, Fe, generates Zn2+, Cu2+, Co2+, Ni2+, Sn2+, Fe2+, makes the gold in homogenate
Category all exists in a manner of metal ion;Second tunic of reactor tank is the poly-vinylidene-fluoride composite film for being enclosed with active carbon,
Third tunic is the microporous barrier that modified cellulose and polyurethane are combined, and wherein the content of modified cellulose is 5%;4th layer
Film is the macroporous absorption film of clay mineral;
(3)Being diluted with water to after concentration is 20% to processed homogenate and adding PH regulator adjusting PH is 3, then
The citric acid that the concentration measured relative to 0.2 times of homogenate is 0.3mol/L is added thereto, in the shaking table that revolving speed is 300r/min
Strongly acidic styrene type cation exchange resin column is cycled through after upper shake 3h, it is then multiple by polycarbonate and polyacrylonitrile
The hollow fiber ultrafiltration membrane of conjunction filters;
(4)By step(3)Resulting filtrate by pressurized dissolved air flotation, by air-float technology except in decontaminated water oil film and
Oil droplet and other organic pollutants, it is then unadsorbed by being removed again containing amino-phosphonic acid functional groups complexing resin
Heavy metal ion, so that the heavy metal contaminants content in liquid reaches discharge standard.
Wherein, the macroreticular resin exchange membrane house refuse homogenate of the package sulfuric acid can be worn from macrovoid rapidly
It crosses, but since heavy metal partial size is excessive, so metal cannot pass through when passing through in homogenate containing heavy metal, wraps simultaneously
Wrapping up in the sulfuric acid in the exchange membrane of sulfuric acid can react with heavy metal, generate heavy metal ion, then metal then passes through packet
The macroreticular resin exchange membrane for wrapping up in sulfuric acid can save the dosage of sulfuric acid with the macroreticular resin exchange membrane of package sulfuric acid, and sulfuric acid with
Metal contact surface is big, reacts more complete.
Wherein, the mass concentration of the sulfuric acid is 55%.
Wherein, the preparation process of the modified cellulose is:Concentrated hydrochloric acid is reacted with trimethylamine generates trimethylamine hydrochloride,
Cellulose cation-exchanger made from trimethylamine hydrochloride and epichlorohydrin reaction is added to again and impregnates hemicellulose
In dimethyl sulphoxide solution, NaOH solution processing is then added, acetyl progress acetyl is then added and is modified, prepared by
Unmodified cellulose molecule amount is high, palliating degradation degree is low, adsorption capacity is strong.
Wherein, the citric acid that is added into rubbish homogenate is since complex reaction occurs for citric acid and metal ion
After generate metal complex, metal complex contains lone pair electrons pair, passes through strongly acidic styrene type cation exchange resin column
It can be combined with the cation of resin column and have the function that recycle heavy metal.
Wherein, the pressurized dissolved air flotation facture is exactly to be passed through air into waste water in hyperbaric environment, then empty
Gas is precipitated from water in the form of micro-bubble becomes carrier, keeps the polluters such as oil emulsion, the small suspended particulate in waste water viscous
It is attached on bubble, floats to the water surface with bubble, form one gas and water of foam, particle(Oil)Three-phase mixture is steeped by collecting
Foam or dross achieve the purpose that separate impurity, the oil film in decontaminated water and oil droplet, purification waste water.It is useless that the method is mainly used to processing
The oil emulsion removed or relative density are difficult to close to 1 small suspended particulate by natural subsidence or floating in water.
Wherein, the preparation process of the polycarbonate and the compound hollow fiber ultrafiltration membrane of polyacrylonitrile is polycarbonate
Raw hydration reaction is issued in organic oxidation tin catalytic action, using organic oxidation tin is filtered out, obtains polycarbonate aqueous solution,
Then polycarbonate aqueous solution is mixed into obtain film liquid with the dimethyl sulphoxide solution of polyacrylonitrile, then film liquid and inner gel is situated between
It is to form a film in the bath of outer inner gel media gel that matter passes through spray head to inject with distilled water simultaneously, i.e. acquisition polycarbonate and polyacrylonitrile
Compound hollow fiber ultrafiltration membrane.
Specific experiment verifying
1. subjects:It is process object with the rubbish of certain city house refuse stack-up-yard, through in detection house refuse
Content of beary metal be greater than 5g/m3,
2. test method:Take 4 parts of above-mentioned house refuse, every part of 5m3, it is respectively labeled as test group 1, test group 2, test group
3, control group.It is wherein handled respectively with the method for the embodiment of the present invention 1 ~ 3 for 3 groups of experimental group, the absorption of control group routine
Method is handled.
3. after treatment heavy metals in garbage content records:
4. conclusion:As can be seen from the above data, treatment process of the invention imitates the heavy metal in processing house refuse
Fruit is obvious, and without any abnormal conditions, securely and reliably.
Finally it should be noted that:Above embodiments are only to illustrate the technical solution of the utility model, rather than its limitations;
Although the utility model is described in detail with reference to the foregoing embodiments, those skilled in the art should understand that:
It can still modify to technical solution documented by previous embodiment, or be equal to part of technical characteristic
Replacement;And these are modified or replaceed, the utility model embodiment technical solution that it does not separate the essence of the corresponding technical solution
Spirit and scope.
Claims (3)
1. a kind of minimizing technology of Heavy Metal Pollution in Municipal Solid Waste object, which is characterized in that include the following steps:
(1)By consumer garbage compost, not available solid waste therein is sorted out, the not available solid is useless
Gurry includes plastic foil, Fibre Bag, metal, glassware, brick and tile stone, in mass ratio 1 after then crushing residual refuse:1
Water is added, is placed in homogenized on refiner and house refuse homogenate is made;
(2)Four layers of macroporous absorption film reaction tank of rubbish homogenate multipass, the first tunic of reactor tank are the macropore for wrapping up sulfuric acid
Resins exchange film, the mass concentration of the sulfuric acid are 45 ~ 55%, wrap up the H in the sulfuric acid in the macroreticular resin exchange membrane of sulfuric acid
+ and the heavy metal Zn in homogenate, Cu, Co, Ni, Sn generation redox reaction, generate Zn2+、Cu2+、Co2+、Ni2+、Sn2+, make
Metal in homogenate all exists in a manner of metal ion;Second tunic of reactor tank is the poly- inclined fluorine for being enclosed with active carbon
Ethylene composite membrane;Third tunic is the microporous barrier that modified cellulose and polyurethane are combined, wherein the content of modified cellulose
It is 5%;4th tunic is the macroporous absorption film of clay mineral;The heavy metal being adsorbed and removed in rubbish homogenate for the first time;
(3)Be diluted with water to after concentration is 20% to processed homogenate add PH regulator adjust PH be 2 ~ 3, then to
The citric acid that the concentration measured relative to 0.2 times of homogenate is 0.3mol/L is wherein added, is shaking for 200 ~ 300r/min in revolving speed
Strongly acidic styrene type cation exchange resin column is cycled through after shaking 2 ~ 3h on bed, then passes through polycarbonate and polypropylene
The compound hollow fiber ultrafiltration membrane filtering of nitrile;
(4)By step(3)Resulting filtrate is by pressurized dissolved air flotation, by air-float technology except the oil film and oil droplet in decontaminated water
And other organic pollutants, then by removing a unadsorbed huge sum of money again containing amino-phosphonic acid functional groups complexing resin
Belong to ion.
2. a kind of minimizing technology of Heavy Metal Pollution in Municipal Solid Waste object as described in claim 1, which is characterized in that institute
The preparation process for the modified cellulose stated is:Concentrated hydrochloric acid is reacted with trimethylamine generates trimethylamine hydrochloride, then by trimethylamine hydrochloric acid
Cellulose cation-exchanger made from salt and epichlorohydrin reaction is added to the dimethyl sulphoxide solution for impregnating hemicellulose
In, NaOH solution processing is then added, it is modified then to add acetyl progress acetyl.
3. a kind of minimizing technology of Heavy Metal Pollution in Municipal Solid Waste object as described in claim 1, which is characterized in that institute
The preparation process of the polycarbonate the stated hollow fiber ultrafiltration membrane compound with polyacrylonitrile is that polycarbonate is urged in organic oxidation tin
Change effect issues raw hydration reaction, using organic oxidation tin is filtered out, polycarbonate aqueous solution is obtained, then by polycarbonate
Aqueous solution mixes to obtain film liquid with the dimethyl sulphoxide solution of polyacrylonitrile, and film liquid and inner gel medium are then passed through spray head simultaneously
Injection is to form a film in the bath of outer inner gel media gel with distilled water, i.e. acquisition polycarbonate and the compound doughnut of polyacrylonitrile
Ultrafiltration membrane.
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CN108929162B (en) * | 2018-08-06 | 2021-06-01 | 上海玖钬环保科技有限公司 | Treatment method for degrading and removing heavy metal from municipal domestic waste |
CN109940034B (en) * | 2019-04-24 | 2021-07-09 | 河南省岩石矿物测试中心 | Method for repairing heavy metal contaminated soil by flotation |
CN110436974A (en) * | 2019-09-05 | 2019-11-12 | 湖南人文科技学院 | A kind of non-pollution processing method and system of afforestation rubbish |
CN114057950B (en) * | 2020-07-30 | 2024-03-22 | 湖北远大生命科学与技术有限责任公司 | Spherical polyurethane grafted modified polyacrylate macroporous anion resin, preparation method thereof and application thereof in taurine production |
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