CN109111020A - City sewage deep treatment method - Google Patents
City sewage deep treatment method Download PDFInfo
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- CN109111020A CN109111020A CN201810956539.2A CN201810956539A CN109111020A CN 109111020 A CN109111020 A CN 109111020A CN 201810956539 A CN201810956539 A CN 201810956539A CN 109111020 A CN109111020 A CN 109111020A
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- Prior art keywords
- sewage
- parts
- processing
- sludge
- mud
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- 239000010865 sewage Substances 0.000 title claims abstract description 49
- 238000000034 method Methods 0.000 title claims abstract description 38
- 239000010802 sludge Substances 0.000 claims abstract description 63
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 61
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 45
- 239000003795 chemical substances by application Substances 0.000 claims abstract description 38
- 238000004659 sterilization and disinfection Methods 0.000 claims abstract description 26
- 238000001223 reverse osmosis Methods 0.000 claims abstract description 24
- 238000004821 distillation Methods 0.000 claims abstract description 21
- 239000013505 freshwater Substances 0.000 claims abstract description 20
- 238000001179 sorption measurement Methods 0.000 claims abstract description 19
- 230000000813 microbial effect Effects 0.000 claims abstract description 14
- 230000008569 process Effects 0.000 claims abstract description 14
- 239000013078 crystal Substances 0.000 claims abstract description 12
- 150000003839 salts Chemical class 0.000 claims abstract description 12
- 239000000203 mixture Substances 0.000 claims description 37
- 239000000843 powder Substances 0.000 claims description 33
- 238000003756 stirring Methods 0.000 claims description 25
- 239000000463 material Substances 0.000 claims description 21
- 241000894006 Bacteria Species 0.000 claims description 20
- 235000008331 Pinus X rigitaeda Nutrition 0.000 claims description 20
- 235000011613 Pinus brutia Nutrition 0.000 claims description 20
- 241000018646 Pinus brutia Species 0.000 claims description 20
- 229920001495 poly(sodium acrylate) polymer Polymers 0.000 claims description 20
- NNMHYFLPFNGQFZ-UHFFFAOYSA-M sodium polyacrylate Chemical compound [Na+].[O-]C(=O)C=C NNMHYFLPFNGQFZ-UHFFFAOYSA-M 0.000 claims description 20
- 230000001954 sterilising effect Effects 0.000 claims description 20
- 229920002472 Starch Polymers 0.000 claims description 19
- 239000004411 aluminium Substances 0.000 claims description 19
- 229910052782 aluminium Inorganic materials 0.000 claims description 19
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 claims description 19
- 239000010881 fly ash Substances 0.000 claims description 19
- 239000011734 sodium Substances 0.000 claims description 19
- 229910052708 sodium Inorganic materials 0.000 claims description 19
- 235000019698 starch Nutrition 0.000 claims description 19
- 239000008107 starch Substances 0.000 claims description 19
- 239000004575 stone Substances 0.000 claims description 19
- 229910052613 tourmaline Inorganic materials 0.000 claims description 19
- 229940070527 tourmaline Drugs 0.000 claims description 19
- 239000011032 tourmaline Substances 0.000 claims description 19
- 229910052902 vermiculite Inorganic materials 0.000 claims description 19
- 239000010455 vermiculite Substances 0.000 claims description 19
- 235000019354 vermiculite Nutrition 0.000 claims description 19
- UMPKMCDVBZFQOK-UHFFFAOYSA-N potassium;iron(3+);oxygen(2-) Chemical compound [O-2].[O-2].[K+].[Fe+3] UMPKMCDVBZFQOK-UHFFFAOYSA-N 0.000 claims description 17
- 239000002994 raw material Substances 0.000 claims description 16
- 238000002360 preparation method Methods 0.000 claims description 15
- 238000004062 sedimentation Methods 0.000 claims description 15
- 239000007788 liquid Substances 0.000 claims description 14
- 238000002156 mixing Methods 0.000 claims description 14
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 claims description 12
- 239000012528 membrane Substances 0.000 claims description 12
- 238000001035 drying Methods 0.000 claims description 10
- 238000010438 heat treatment Methods 0.000 claims description 9
- 239000008367 deionised water Substances 0.000 claims description 8
- 229910021641 deionized water Inorganic materials 0.000 claims description 8
- 239000000706 filtrate Substances 0.000 claims description 7
- 238000003825 pressing Methods 0.000 claims description 7
- 239000006228 supernatant Substances 0.000 claims description 7
- 238000007598 dipping method Methods 0.000 claims description 6
- 239000000047 product Substances 0.000 claims description 6
- 238000010792 warming Methods 0.000 claims description 6
- 238000004140 cleaning Methods 0.000 claims description 3
- 239000012153 distilled water Substances 0.000 claims description 3
- 238000004108 freeze drying Methods 0.000 claims description 3
- 230000007935 neutral effect Effects 0.000 claims description 3
- 239000007787 solid Substances 0.000 claims description 3
- 239000012265 solid product Substances 0.000 claims description 3
- 229910052799 carbon Inorganic materials 0.000 claims 1
- 238000004519 manufacturing process Methods 0.000 claims 1
- 238000001914 filtration Methods 0.000 abstract description 7
- 238000010521 absorption reaction Methods 0.000 abstract description 6
- JEGUKCSWCFPDGT-UHFFFAOYSA-N h2o hydrate Chemical compound O.O JEGUKCSWCFPDGT-UHFFFAOYSA-N 0.000 abstract description 3
- 238000004064 recycling Methods 0.000 abstract description 3
- 229910001385 heavy metal Inorganic materials 0.000 description 7
- 150000002500 ions Chemical class 0.000 description 6
- IOVCWXUNBOPUCH-UHFFFAOYSA-M Nitrite anion Chemical compound [O-]N=O IOVCWXUNBOPUCH-UHFFFAOYSA-M 0.000 description 5
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- 230000001376 precipitating effect Effects 0.000 description 2
- 229910052903 pyrophyllite Inorganic materials 0.000 description 2
- 238000011084 recovery Methods 0.000 description 2
- PXFBZOLANLWPMH-UHFFFAOYSA-N 16-Epiaffinine Natural products C1C(C2=CC=CC=C2N2)=C2C(=O)CC2C(=CC)CN(C)C1C2CO PXFBZOLANLWPMH-UHFFFAOYSA-N 0.000 description 1
- VHUUQVKOLVNVRT-UHFFFAOYSA-N Ammonium hydroxide Chemical compound [NH4+].[OH-] VHUUQVKOLVNVRT-UHFFFAOYSA-N 0.000 description 1
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 1
- 229920002488 Hemicellulose Polymers 0.000 description 1
- BPQQTUXANYXVAA-UHFFFAOYSA-N Orthosilicate Chemical compound [O-][Si]([O-])([O-])[O-] BPQQTUXANYXVAA-UHFFFAOYSA-N 0.000 description 1
- 229910019142 PO4 Inorganic materials 0.000 description 1
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 description 1
- 238000005411 Van der Waals force Methods 0.000 description 1
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- 150000002484 inorganic compounds Chemical class 0.000 description 1
- 229910010272 inorganic material Inorganic materials 0.000 description 1
- 239000011229 interlayer Substances 0.000 description 1
- 229910000462 iron(III) oxide hydroxide Inorganic materials 0.000 description 1
- 239000011159 matrix material Substances 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- IJGRMHOSHXDMSA-UHFFFAOYSA-N nitrogen Substances N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 1
- 231100000252 nontoxic Toxicity 0.000 description 1
- 230000003000 nontoxic effect Effects 0.000 description 1
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- 239000013618 particulate matter Substances 0.000 description 1
- 239000002957 persistent organic pollutant Substances 0.000 description 1
- NBIIXXVUZAFLBC-UHFFFAOYSA-K phosphate Chemical compound [O-]P([O-])([O-])=O NBIIXXVUZAFLBC-UHFFFAOYSA-K 0.000 description 1
- 239000010452 phosphate Substances 0.000 description 1
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- 231100000614 poison Toxicity 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
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- -1 rare earth ion Chemical class 0.000 description 1
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- 231100000331 toxic Toxicity 0.000 description 1
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Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F9/00—Multistage treatment of water, waste water or sewage
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F11/00—Treatment of sludge; Devices therefor
- C02F11/12—Treatment of sludge; Devices therefor by de-watering, drying or thickening
- C02F11/121—Treatment of sludge; Devices therefor by de-watering, drying or thickening by mechanical de-watering
- C02F11/122—Treatment of sludge; Devices therefor by de-watering, drying or thickening by mechanical de-watering using filter presses
-
- 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
- C02F1/001—Processes for the treatment of water whereby the filtration technique is of importance
-
- 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
- C02F1/02—Treatment of water, waste water, or sewage by heating
- C02F1/04—Treatment of water, waste water, or sewage by heating by distillation or evaporation
-
- 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
- C02F1/28—Treatment of water, waste water, or sewage by sorption
- C02F1/281—Treatment of water, waste water, or sewage by sorption using inorganic sorbents
-
- 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
- C02F1/28—Treatment of water, waste water, or sewage by sorption
- C02F1/283—Treatment of water, waste water, or sewage by sorption using coal, charred products, or inorganic mixtures containing them
-
- 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
- C02F1/28—Treatment of water, waste water, or sewage by sorption
- C02F1/285—Treatment of water, waste water, or sewage by sorption using synthetic organic sorbents
-
- 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
- C02F1/28—Treatment of water, waste water, or sewage by sorption
- C02F1/286—Treatment of water, waste water, or sewage by sorption using natural organic sorbents or derivatives thereof
-
- 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
- C02F1/30—Treatment of water, waste water, or sewage by irradiation
- C02F1/32—Treatment of water, waste water, or sewage by irradiation with ultraviolet light
-
- 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
- C02F1/44—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
- C02F1/441—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis by reverse osmosis
-
- 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
- C02F1/50—Treatment of water, waste water, or sewage by addition or application of a germicide or by oligodynamic treatment
-
- 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
- C02F1/5236—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities using inorganic agents
-
- 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
- C02F1/5263—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities using natural chemical compounds
-
- 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
- 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
- C02F1/72—Treatment of water, waste water, or sewage by oxidation
-
- 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
- C02F2001/007—Processes including a sedimentation step
-
- 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
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/34—Biological treatment of water, waste water, or sewage characterised by the microorganisms used
Abstract
The present invention provides a kind of city sewage deep treatment method, sewage-mud is handled by using novel sewage-treating agent, arrange in pairs or groups again activated carbon adsorption processing, filtration treatment, Microbial denitrogenation processing, ultraviolet-sterilization processing, reverse osmosis treatment and distillation processing etc. treatment process, directly sewage-mud is handled as mud cake, fresh water and crystal salt, and the sludge-based activated carbon with excellent absorption property has been made in resulting mud cake;The present invention handles resulting fresh water water quality and has had reached the standard recycled, can direct recycling and reusing, resulting crystal salt can send processing outside.Sewage-mud processing is carried out using sewage water treatment method of the invention, return water rate is improved, realizes the zero-emission of sewage, realize the resource utilization of sewage and sludge, meet the requirement of sustainable development.
Description
Technical field
The present invention relates to water-treatment technology fields, and in particular to a kind of city sewage deep treatment method.
Background technique
Municipal sewage treatment be the municipal sewage that will be discharged in city and factory discharge sewage focus on, also
It is to say that municipal sewage includes sanitary sewage and trade effluent.These sewage due to long-time accumulate, inside containing a large amount of mud,
The harmful substances such as bacterium, heavy metal ion, inorganic compound and organic compound, if being directly discharged to water body without processing
Among, heavy pressure can be brought to water environment, it will the drinking-water health of serious people makes limited water resource by serious
It threatens, or even threatens the survival and development environment of people.Existing sewage treatment method is mostly based on qualified discharge, seldom meeting
In view of waste resource recovery utilizes, although this mode also can be realized the processing of sewage, it be easy to cause the very big wave of resource
Take, and does not meet requirement of the modern society for sustainable development.
Therefore, it in order to meet the requirement of sustainable development, realizes that waste resource recovery utilizes, needs to develop a kind of novel dirt
Method for treating water can be better achieved the resource utilization of gained waste after sewage treatment, improve while efficient water purification
The reuse ratio of gained waste after sewage treatment.
Summary of the invention
In view of this, the present invention provides a kind of sewage water treatment method of high-efficiency environment friendly, using having both flocculation, adsorb, go out
The sewage-treating agent combination activated carbon adsorption processing of the multi-functionals such as bacterium, microorganism denitration process, ultraviolet-sterilization handle, are reverse osmosis
The techniques such as processing and distillation processing, improve the water quality of gained fresh water after processing, are convenient for recycling and reusing, to greatly mention
High return water rate, realizes sewage zero-discharge, meanwhile, the sewage-treating agent that treatment process uses is also very advantageous in by sludge system
It is standby at the sludge-based activated carbon with excellent absorption property, so that the resource utilization of sludge be better achieved.
City sewage deep treatment method provided by the invention, includes the following steps:
It (1) is that multi-functional sewage-treating agent is added into the sewage-mud of mixing by 1g:1L by mass volume ratio, with
It after the revolving speed stir process 12h of 155r/min, stands wait settle, after the completion of sedimentation, supernatant liquor is taken to carry out at activated carbon adsorption
Reason is collected simultaneously in sedimentation gained sludge to sludge collecting pit;
(2) Microbial denitrogenation processing is carried out to the liquid after adsorption treatment, be filtered later, gained filtrate carried out purple
Outer sterilization processing is collected simultaneously in gained filter residue to sludge collecting pit;
(3) reverse osmosis treatment is carried out to the liquid after sterilization processing, collects resulting fresh water, and carry out to resulting concentrated water
Distillation gained fresh water and crystal salt are collected in distillation processing respectively later;
(4) filters pressing processing is carried out to the sludge in sludge collecting pit, and sludge-based activated carbon is made in gained mud cake, simultaneously
Gained sewage is added in sewage-mud to be processed;
In the step (1), the multi-functional sewage-treating agent of use by weight, including the following raw material component:
24~27 parts of aluminium polychloride, 16~18 parts of sodium carboxymethyl starch, 25~30 parts of Sodium Polyacrylate, potassium ferrate 8
~10 parts, 15~20 parts of corncob, 10~12 parts of pine tree sawdust, 13~15 parts of medical stone, 18~20 parts of flyash, vermiculite 10~
12 parts, 8~10 parts of tourmaline powder, 13~15 parts of pyrophillite;
Further, in the step (4), the preparation method of sludge-based activated carbon includes the following steps:
A, mud cake is dried to moisture content≤5%, is then 10g:20mL into resulting dry mud cake by mass volume ratio
The liquor zinci chloridi that concentration is 5mol/L is added, stirs dipping;
B, dipping mud cake is placed in Muffle furnace, is warming up to 600 DEG C with the heating rate of 10 DEG C/min, handle 60min, then
850 DEG C are warming up to the heating rate of 5 DEG C/min, handles 120min, when temperature is down to 100 DEG C or less, is taken out resulting solid
Body product;
C, the product of taking-up is put into 0.1mol/L hydrochloric acid solution, 15~20min is boiled in heating, then uses 0.1mol/L
Hydrochloric acid solution rinses 5~7 times, then being cleaned repeatedly with distilled water to raffinate is solid product drying that is neutral, will finally cleaning, i.e.,
For sludge-based activated carbon obtained;
Further, in the step (3), low pressure or middle pressure reverse osmosis membrane of the reverse osmosis treatment using resistance tocrocking;
Further, the sewage-treating agent by weight, including the following raw material component:
25 parts of aluminium polychloride, 17 parts of sodium carboxymethyl starch, 28 parts of Sodium Polyacrylate, 9 parts of potassium ferrate, corncob 18
Part, 11 parts of pine tree sawdust, 14 parts of medical stone, 19 parts of flyash, 11 parts of vermiculite, 9 parts of tourmaline powder, 14 parts of pyrophillite;
Further, the preparation method of the sewage-treating agent, includes the following steps:
1) after mixing medical stone, flyash, vermiculite, tourmaline powder and pyrophillite, it is ground into fine powder, adding granularity is
The corncob and pine tree sawdust of the drying of 50~100 mesh, stir and evenly mix, obtain mixture I;
2) after impregnating mixture I with deionized water, aluminium polychloride, sodium carboxymethyl starch and Sodium Polyacrylate is added,
It is stirred 1~1.5h under the revolving speed of 120~150r/min, obtains solidliquid mixture II, then to resulting solidliquid mixture
II carries out freeze-drying process, obtains dried material;
3) dried material obtained in step 2) is ground into granularity is addition potassium ferrate after 50~100 mesh powders,
It stirs and evenly mixs as the multi-functional Environment-friendlysewage sewage treatment agent.
Beneficial effects of the present invention:
The present invention is handled sewage-mud by using novel sewage-treating agent, then at activated carbon adsorption of arranging in pairs or groups
The treatment process such as reason, filtration treatment, Microbial denitrogenation processing, ultraviolet-sterilization processing, reverse osmosis treatment and distillation processing, directly
Sewage-mud is handled as mud cake, fresh water and crystal salt, and the dirt with excellent absorption property has been made in resulting mud cake
Mud matrix activated carbon;The present invention handle resulting fresh water water quality had reached recycle standard, can direct recycling and reusing, institute
The crystal salt obtained can send processing outside.Sewage-mud processing is carried out using sewage water treatment method of the invention, improves return water rate, it is real
The zero-emission for having showed sewage realizes the resource utilization of sewage and sludge, meets the requirement of sustainable development.
The sewage-treating agent that the present invention uses has both the multi-functionals such as flocculation, oxidation, absorption, sterilizing, can not only be efficient
Ground removes harmful organic substance, inorganic substances and heavy metal ion in sewage, additionally it is possible to effectively kill the bacterium in water
Equal microorganisms, avoid it from excessively breeding and cause the more serious pollution of water body, handle sewage-mud using it, can greatly improve
Water quality that treated;Meanwhile dirt is being carried out containing raw materials such as a large amount of plant and minerals in sewage-treating agent of the invention
It after water process, can directly be deposited in sludge, to increase significantly the content of carbohydrate and minerals in sludge, have
Conducive to sludge to be preferably prepared into the sludge-based activated carbon haveing excellent performance, to realize the resource utilization of sludge.
Sewage-treating agent provided by the invention uses aluminium polychloride, sodium carboxymethyl starch, Sodium Polyacrylate, ferric acid
The raw material components such as potassium, corncob, pine tree sawdust, medical stone, flyash, vermiculite, tourmaline powder and pyrophillite are closed by specific dosage
System is compounded, and in the preparation, is realized between each raw material component by way of stirring immersion in deionized water fully
Dispersion Fusion can be such that water-soluble aluminium polychloride, sodium carboxymethyl starch and Sodium Polyacrylate sufficiently saws with corncob, pine tree
End, medical stone, flyash, vermiculite, tourmaline powder and pyrophillite are mixed, and part can also be absorbed into these originals
In the hole of material, then moisture sharp freezing is evaporated using Freeze Drying Technique (for the prior art, details are not described herein), it can
To keep the abundant fusion of each raw material component in the case where not damaging raw material mix and performance, sent out convenient for subsequent each raw material component
Mutual synergistic effect is waved, realizes the complementation and enhancing of performance.
Wherein, contain a large amount of cellulose, hemicellulose in corncob and pine tree sawdust, by means of porous structure, surface
Product is big, has many advantages, such as affine adsorptivity, can help dissolubility pollutant matter and free heavy metal ion in water removal,
Also contain Fungicidal substance in pine tree sawdust, it can be except the harmful microorganism in decontaminated water;Medical stone has porous structure and huge
Specific surface area, can not only adsorb in water dissociate heavy metal ion and harmful organic substance, additionally it is possible in absorption effluent
The harmful microorganisms such as bacterium;Flyash is in porous type cellular tissue, and specific surface area is larger, adsorption activity with higher;
Vermiculite is the silicate of layer structure, has the characteristics that porosity height, large specific surface area, adsorption capacity is big, can remove in water
Ammonia nitrogen, heavy metal element, phosphate, rare earth ion, organic pollutant etc.;Between adjacent two crystal layer of pyrophyllite layer structure only
It is connected with Van der Waals force, structure is easy to along damage layer, and anions and canons can enter interlayer, therefore pyrophyllite has natural suction
Attached activity;Tourmaline powder can not only cross the various harmful elements in drainage, remove the chlorine in water, additionally it is possible to release bear from
Son kills the harmful microorganism in water;Potassium ferrate has excellent performance, and collection is aoxidized, adsorbed, flocculating, precipitating, sterilizing, disappearing
The features such as poison, decoloration, deodorization;Aluminium polychloride has the performances such as absorption, cohesion, precipitating, has to water-borne glue body and particulate matter
Height charge neutrality and bridge linking effect, and can strongly remove micro- Toxic and heavy metal ion;Sodium carboxymethyl starch have chelating, from
The functions such as son exchange, flocculation;Carboxyl on Sodium Polyacrylate strand is due to electrostatic repulsion effect, so that the polymer chain to circumnutate
Stretching, extension, facilitates the functional group with adsorptivity to be exposed on surface, since these active sites adsorb suspended particles in the solution
On, form interparticle bridge formation, to accelerate the sedimentation of suspended particles, and Sodium Polyacrylate can with the above metal of divalent from
Son reaction forms its insoluble salt, to be conducive to the heavy metal ion gone in water removal.
In addition, each raw material component used in water treatment agent of the invention is from a wealth of sources, cheap, property is stablized, and
It is nontoxic environmentally friendly material, can guarantees the safety of water quality after processing, and reduces processing cost simultaneously.
Specific embodiment
The following are specific embodiments:
Embodiment one
City sewage deep treatment method provided in this embodiment, includes the following steps:
It (1) is that multi-functional sewage-treating agent is added into the sewage-mud of mixing by 1g:1L by mass volume ratio, with
It after the revolving speed stir process 12h of 155r/min, stands wait settle, after the completion of sedimentation, supernatant liquor is taken to carry out at activated carbon adsorption
Reason is collected simultaneously in sedimentation gained sludge to sludge collecting pit;
(2) Microbial denitrogenation processing is carried out to the liquid after adsorption treatment, be filtered later, gained filtrate carried out purple
Outer sterilization processing is collected simultaneously in gained filter residue to sludge collecting pit;
(3) reverse osmosis treatment is carried out to the liquid after sterilization processing, collects resulting fresh water, and carry out to resulting concentrated water
Distillation gained fresh water and crystal salt are collected in distillation processing respectively later;
(4) filters pressing processing is carried out to the sludge in sludge collecting pit, and sludge-based activated carbon is made in gained mud cake, simultaneously
Gained sewage is added in sewage-mud to be processed;
In the step (1), the multi-functional sewage-treating agent of use by weight, including the following raw material component:
25 parts of aluminium polychloride, 17 parts of sodium carboxymethyl starch, 28 parts of Sodium Polyacrylate, 9 parts of potassium ferrate, corncob 18
Part, 11 parts of pine tree sawdust, 14 parts of medical stone, 19 parts of flyash, 11 parts of vermiculite, 9 parts of tourmaline powder, 14 parts of pyrophillite;
In the step (2), Microbial denitrogenation processing includes that (such as nitrite bacteria and nitrification are thin using aerobic bacteria processing
Bacterium) and using anaerobic bacteria processing (such as denitrifying bacteria), using the prior art, details are not described herein;
In the step (2), ultraviolet-sterilization processing carries out sterilization processing using ultraviolet light, using the prior art,
Details are not described herein;
It is 0.22 μm that membrane aperture is selected in the step (2), when filtering, and material is PVDF (Kynoar) hollow fibre
Dimension;
In the step (3), low pressure or middle pressure reverse osmosis membrane of the reverse osmosis treatment using resistance tocrocking;
In the step (3), distillation processing is the prior art.
In the present embodiment, in the step (4), the preparation method of sludge-based activated carbon includes the following steps:
A, mud cake is dried to moisture content≤5%, is then 10g:20mL into resulting dry mud cake by mass volume ratio
The liquor zinci chloridi that concentration is 5mol/L is added, stirs dipping;
B, dipping mud cake is placed in Muffle furnace, is warming up to 600 DEG C with the heating rate of 10 DEG C/min, handle 60min, then
850 DEG C are warming up to the heating rate of 5 DEG C/min, handles 120min, when temperature is down to 100 DEG C or less, is taken out resulting solid
Body product;
C, the product of taking-up is put into 0.1mol/L hydrochloric acid solution, 15~20min is boiled in heating, then uses 0.1mol/L
Hydrochloric acid solution rinses 5~7 times, then being cleaned repeatedly with distilled water to raffinate is solid product drying that is neutral, will finally cleaning, i.e.,
For sludge-based activated carbon obtained.
In the present embodiment, the preparation method of the sewage-treating agent includes the following steps:
1) after mixing medical stone, flyash, vermiculite, tourmaline powder and pyrophillite, it is ground into fine powder, adding granularity is
The corncob and pine tree sawdust of the drying of 50~100 mesh, stir and evenly mix, obtain mixture I;
2) after impregnating mixture I with deionized water, aluminium polychloride, sodium carboxymethyl starch and Sodium Polyacrylate is added,
It is stirred 1h under the revolving speed of 150r/min, obtains solidliquid mixture II, then freeze to resulting solidliquid mixture II
It is dried, obtains dried material;
3) dried material obtained in step 2) is ground into granularity is addition potassium ferrate after 50~100 mesh powders,
It stirs and evenly mixs as the multi-functional Environment-friendlysewage sewage treatment agent.
Embodiment two
City sewage deep treatment method provided in this embodiment, includes the following steps:
It (1) is that multi-functional sewage-treating agent is added into the sewage-mud of mixing by 1g:1L by mass volume ratio, with
It after the revolving speed stir process 12h of 155r/min, stands wait settle, after the completion of sedimentation, supernatant liquor is taken to carry out at activated carbon adsorption
Reason is collected simultaneously in sedimentation gained sludge to sludge collecting pit;
(2) Microbial denitrogenation processing is carried out to the liquid after adsorption treatment, be filtered later, gained filtrate carried out purple
Outer sterilization processing is collected simultaneously in gained filter residue to sludge collecting pit;
(3) reverse osmosis treatment is carried out to the liquid after sterilization processing, collects resulting fresh water, and carry out to resulting concentrated water
Distillation gained fresh water and crystal salt are collected in distillation processing respectively later;
(4) filters pressing processing is carried out to the sludge in sludge collecting pit, and sludge-based activated carbon is made in gained mud cake, simultaneously
Gained sewage is added in sewage-mud to be processed;
In the step (1), the multi-functional sewage-treating agent of use by weight, including the following raw material component:
24 parts of aluminium polychloride, 18 parts of sodium carboxymethyl starch, 25 parts of Sodium Polyacrylate, 10 parts of potassium ferrate, corncob 15
Part, 12 parts of pine tree sawdust, 13 parts of medical stone, 20 parts of flyash, 12 parts of vermiculite, 10 parts of tourmaline powder, 13 parts of pyrophillite;
In the step (2), Microbial denitrogenation processing includes that (such as nitrite bacteria and nitrification are thin using aerobic bacteria processing
Bacterium) and using anaerobic bacteria processing (such as denitrifying bacteria), using the prior art, details are not described herein;
In the step (2), ultraviolet-sterilization processing carries out sterilization processing using ultraviolet light, using the prior art,
Details are not described herein;
It is 0.22 μm that membrane aperture is selected in the step (2), when filtering, and material is PVDF (Kynoar) hollow fibre
Dimension;
In the step (3), low pressure or middle pressure reverse osmosis membrane of the reverse osmosis treatment using resistance tocrocking;
In the step (3), distillation processing is the prior art.
In the present embodiment, the preparation method of sludge-based activated carbon is the same as embodiment one.
In the present embodiment, the preparation method of the sewage-treating agent includes the following steps:
1) after mixing medical stone, flyash, vermiculite, tourmaline powder and pyrophillite, it is ground into fine powder, adding granularity is
The corncob and pine tree sawdust of the drying of 50~100 mesh, stir and evenly mix, obtain mixture I;
2) after impregnating mixture I with deionized water, aluminium polychloride, sodium carboxymethyl starch and Sodium Polyacrylate is added,
It is stirred 1.5h under the revolving speed of 120r/min, obtains solidliquid mixture II, then resulting solidliquid mixture II is carried out cold
Freeze and be dried, obtains dried material;
3) dried material obtained in step 2) is ground into granularity is addition potassium ferrate after 50~100 mesh powders,
It stirs and evenly mixs as the multi-functional Environment-friendlysewage sewage treatment agent.
Embodiment three
City sewage deep treatment method provided in this embodiment, includes the following steps:
It (1) is that multi-functional sewage-treating agent is added into the sewage-mud of mixing by 1g:1L by mass volume ratio, with
It after the revolving speed stir process 12h of 155r/min, stands wait settle, after the completion of sedimentation, supernatant liquor is taken to carry out at activated carbon adsorption
Reason is collected simultaneously in sedimentation gained sludge to sludge collecting pit;
(2) Microbial denitrogenation processing is carried out to the liquid after adsorption treatment, be filtered later, gained filtrate carried out purple
Outer sterilization processing is collected simultaneously in gained filter residue to sludge collecting pit;
(3) reverse osmosis treatment is carried out to the liquid after sterilization processing, collects resulting fresh water, and carry out to resulting concentrated water
Distillation gained fresh water and crystal salt are collected in distillation processing respectively later;
(4) filters pressing processing is carried out to the sludge in sludge collecting pit, and sludge-based activated carbon is made in gained mud cake, simultaneously
Gained sewage is added in sewage-mud to be processed;
In the step (1), the multi-functional sewage-treating agent of use by weight, including the following raw material component:
27 parts of aluminium polychloride, 16 parts of sodium carboxymethyl starch, 30 parts of Sodium Polyacrylate, 8 parts of potassium ferrate, corncob 20
Part, 10 parts of pine tree sawdust, 15 parts of medical stone, 18 parts of flyash, 12 parts of vermiculite, 8 parts of tourmaline powder, 15 parts of pyrophillite;
In the step (2), Microbial denitrogenation processing includes that (such as nitrite bacteria and nitrification are thin using aerobic bacteria processing
Bacterium) and using anaerobic bacteria processing (such as denitrifying bacteria), using the prior art, details are not described herein;
In the step (2), ultraviolet-sterilization processing carries out sterilization processing using ultraviolet light, using the prior art,
Details are not described herein;
It is 0.22 μm that membrane aperture is selected in the step (2), when filtering, and material is PVDF (Kynoar) hollow fibre
Dimension;
In the step (3), low pressure or middle pressure reverse osmosis membrane of the reverse osmosis treatment using resistance tocrocking;
In the step (3), distillation processing is the prior art.
In the present embodiment, the preparation method of sludge-based activated carbon is the same as embodiment one.
In the present embodiment, the preparation method of the sewage-treating agent includes the following steps:
1) after mixing medical stone, flyash, vermiculite, tourmaline powder and pyrophillite, it is ground into fine powder, adding granularity is
The corncob and pine tree sawdust of the drying of 50~100 mesh, stir and evenly mix, obtain mixture I;
2) after impregnating mixture I with deionized water, aluminium polychloride, sodium carboxymethyl starch and Sodium Polyacrylate is added,
It is stirred 1h under the revolving speed of 150r/min, obtains solidliquid mixture II, then freeze to resulting solidliquid mixture II
It is dried, obtains dried material;
3) dried material obtained in step 2) is ground into granularity is addition potassium ferrate after 50~100 mesh powders,
It stirs and evenly mixs as the multi-functional Environment-friendlysewage sewage treatment agent.
Example IV
City sewage deep treatment method provided in this embodiment, includes the following steps:
It (1) is that multi-functional sewage-treating agent is added into the sewage-mud of mixing by 1g:1L by mass volume ratio, with
It after the revolving speed stir process 12h of 155r/min, stands wait settle, after the completion of sedimentation, supernatant liquor is taken to carry out at activated carbon adsorption
Reason is collected simultaneously in sedimentation gained sludge to sludge collecting pit;
(2) Microbial denitrogenation processing is carried out to the liquid after adsorption treatment, be filtered later, gained filtrate carried out purple
Outer sterilization processing is collected simultaneously in gained filter residue to sludge collecting pit;
(3) reverse osmosis treatment is carried out to the liquid after sterilization processing, collects resulting fresh water, and carry out to resulting concentrated water
Distillation gained fresh water and crystal salt are collected in distillation processing respectively later;
(4) filters pressing processing is carried out to the sludge in sludge collecting pit, and sludge-based activated carbon is made in gained mud cake, simultaneously
Gained sewage is added in sewage-mud to be processed;
In the step (1), the multi-functional sewage-treating agent of use by weight, including the following raw material component:
27 parts of aluminium polychloride, 18 parts of sodium carboxymethyl starch, 30 parts of Sodium Polyacrylate, 10 parts of potassium ferrate, corncob 20
Part, 12 parts of pine tree sawdust, 15 parts of medical stone, 20 parts of flyash, 12 parts of vermiculite, 10 parts of tourmaline powder, 15 parts of pyrophillite;
In the step (2), Microbial denitrogenation processing includes that (such as nitrite bacteria and nitrification are thin using aerobic bacteria processing
Bacterium) and using anaerobic bacteria processing (such as denitrifying bacteria), using the prior art, details are not described herein;
In the step (2), ultraviolet-sterilization processing carries out sterilization processing using ultraviolet light, using the prior art,
Details are not described herein;
It is 0.22 μm that membrane aperture is selected in the step (2), when filtering, and material is PVDF (Kynoar) hollow fibre
Dimension;
In the step (3), low pressure or middle pressure reverse osmosis membrane of the reverse osmosis treatment using resistance tocrocking;
In the step (3), distillation processing is the prior art.
In the present embodiment, the preparation method of sludge-based activated carbon is the same as embodiment one.
In the present embodiment, the preparation method of the sewage-treating agent includes the following steps:
1) after mixing medical stone, flyash, vermiculite, tourmaline powder and pyrophillite, it is ground into fine powder, adding granularity is
The corncob and pine tree sawdust of the drying of 50~100 mesh, stir and evenly mix, obtain mixture I;
2) after impregnating mixture I with deionized water, aluminium polychloride, sodium carboxymethyl starch and Sodium Polyacrylate is added,
It is stirred 1.5h under the revolving speed of 120r/min, obtains solidliquid mixture II, then resulting solidliquid mixture II is carried out cold
Freeze and be dried, obtains dried material;
3) dried material obtained in step 2) is ground into granularity is addition potassium ferrate after 50~100 mesh powders,
It stirs and evenly mixs as the multi-functional Environment-friendlysewage sewage treatment agent.
Embodiment five
City sewage deep treatment method provided in this embodiment, includes the following steps:
It (1) is that multi-functional sewage-treating agent is added into the sewage-mud of mixing by 1g:1L by mass volume ratio, with
It after the revolving speed stir process 12h of 155r/min, stands wait settle, after the completion of sedimentation, supernatant liquor is taken to carry out at activated carbon adsorption
Reason is collected simultaneously in sedimentation gained sludge to sludge collecting pit;
(2) Microbial denitrogenation processing is carried out to the liquid after adsorption treatment, be filtered later, gained filtrate carried out purple
Outer sterilization processing is collected simultaneously in gained filter residue to sludge collecting pit;
(3) reverse osmosis treatment is carried out to the liquid after sterilization processing, collects resulting fresh water, and carry out to resulting concentrated water
Distillation gained fresh water and crystal salt are collected in distillation processing respectively later;
(4) filters pressing processing is carried out to the sludge in sludge collecting pit, and sludge-based activated carbon is made in gained mud cake, simultaneously
Gained sewage is added in sewage-mud to be processed;
In the step (1), the multi-functional sewage-treating agent of use by weight, including the following raw material component:
24 parts of aluminium polychloride, 16 parts of sodium carboxymethyl starch, 25 parts of Sodium Polyacrylate, 8 parts of potassium ferrate, corncob 15
Part, 10 parts of pine tree sawdust, 13 parts of medical stone, 18 parts of flyash, 10 parts of vermiculite, 8 parts of tourmaline powder, 13 parts of pyrophillite;
In the step (2), Microbial denitrogenation processing includes that (such as nitrite bacteria and nitrification are thin using aerobic bacteria processing
Bacterium) and using anaerobic bacteria processing (such as denitrifying bacteria), using the prior art, details are not described herein;
In the step (2), ultraviolet-sterilization processing carries out sterilization processing using ultraviolet light, using the prior art,
Details are not described herein;
It is 0.22 μm that membrane aperture is selected in the step (2), when filtering, and material is PVDF (Kynoar) hollow fibre
Dimension;
In the step (3), low pressure or middle pressure reverse osmosis membrane of the reverse osmosis treatment using resistance tocrocking;
In the step (3), distillation processing is the prior art.
In the present embodiment, the preparation method of sludge-based activated carbon is the same as embodiment one.
In the present embodiment, the preparation method of the sewage-treating agent includes the following steps:
1) after mixing medical stone, flyash, vermiculite, tourmaline powder and pyrophillite, it is ground into fine powder, adding granularity is
The corncob and pine tree sawdust of the drying of 50~100 mesh, stir and evenly mix, obtain mixture I;
2) after impregnating mixture I with deionized water, aluminium polychloride, sodium carboxymethyl starch and Sodium Polyacrylate is added,
It is stirred 1h under the revolving speed of 150r/min, obtains solidliquid mixture II, then freeze to resulting solidliquid mixture II
It is dried, obtains dried material;
3) dried material obtained in step 2) is ground into granularity is addition potassium ferrate after 50~100 mesh powders,
It stirs and evenly mixs as the multi-functional Environment-friendlysewage sewage treatment agent.
Certain plant effuent is handled using the processing method that the present embodiment one to embodiment five provides, before comparison processing
Water quality situation afterwards is obtained such as the following table 1:
Table 1
As shown in Table 1, the high treating effect for the sewage water treatment method that embodiment one is provided to embodiment five, obtains after processing
Fresh water water quality it is high, can be recycled and recycle.
Finally, it is stated that the above examples are only used to illustrate the technical scheme of the present invention and are not limiting, although referring to compared with
Good embodiment describes the invention in detail, those skilled in the art should understand that, it can be to skill of the invention
Art scheme is modified or replaced equivalently, and without departing from the objective and range of technical solution of the present invention, should all be covered at this
In the scope of the claims of invention.
Claims (5)
1. a kind of city sewage deep treatment method, which comprises the steps of:
It (1) is that multi-functional sewage-treating agent is added into the sewage-mud of mixing by 1g:1L by mass volume ratio, with 155r/min
Revolving speed stir process 12h after, stand wait settle, after the completion of sedimentation, take supernatant liquor carry out activated carbon adsorption processing, receive simultaneously
In collection sedimentation gained sludge to sludge collecting pit;
(2) Microbial denitrogenation processing is carried out to the liquid after adsorption treatment, be filtered later, ultraviolet kill is carried out to gained filtrate
Bacterium processing is collected simultaneously in gained filter residue to sludge collecting pit;
(3) reverse osmosis treatment is carried out to the liquid after sterilization processing, collects resulting fresh water, and distill to resulting concentrated water
Distillation gained fresh water and crystal salt are collected in processing respectively later;
(4) filters pressing processing is carried out to the sludge in sludge collecting pit, and gained mud cake is made sludge-based activated carbon, while by institute
Sewage is obtained to be added in sewage-mud to be processed;
In the step (1), the multi-functional sewage-treating agent of use by weight, including the following raw material component:
24~27 parts of aluminium polychloride, 16~18 parts of sodium carboxymethyl starch, 25~30 parts of Sodium Polyacrylate, potassium ferrate 8~10
Part, 15~20 parts of corncob, 10~12 parts of pine tree sawdust, 13~15 parts of medical stone, 18~20 parts of flyash, vermiculite 10~12
Part, 8~10 parts of tourmaline powder, 13~15 parts of pyrophillite.
2. city sewage deep treatment method according to claim 1, it is characterised in that: in the step (4), sludge base
The preparation method of active carbon includes the following steps:
A, mud cake is dried to moisture content≤5%, is then that 10g:20mL is added into resulting dry mud cake by mass volume ratio
Concentration is the liquor zinci chloridi of 5mol/L, stirs dipping;
B, dipping mud cake is placed in Muffle furnace, is warming up to 600 DEG C with the heating rate of 10 DEG C/min, handles 60min, then with 5
DEG C/heating rate of min is warming up to 850 DEG C, 120min is handled, when temperature is down to 100 DEG C or less, takes out resulting solid production
Object;
C, the product of taking-up is put into 0.1mol/L hydrochloric acid solution, 15~20min is boiled in heating, then uses 0.1mol/L hydrochloric acid
Solution rinses 5~7 times, then being cleaned repeatedly with distilled water to raffinate is solid product drying that is neutral, will finally cleaning, is as made
The sludge-based activated carbon obtained.
3. city sewage deep treatment method according to claim 1, it is characterised in that: reverse osmosis in the step (3)
Low pressure or middle pressure reverse osmosis membrane of the processing using resistance tocrocking.
4. city sewage deep treatment method according to claim 1, it is characterised in that: the sewage-treating agent is by weight
Part meter, including the following raw material component:
25 parts of aluminium polychloride, 17 parts of sodium carboxymethyl starch, 28 parts of Sodium Polyacrylate, 9 parts of potassium ferrate, 18 parts of corncob, pine
Set 11 parts of sawdust, 14 parts of medical stone, 19 parts of flyash, 11 parts of vermiculite, 9 parts of tourmaline powder, 14 parts of pyrophillite.
5. city sewage deep treatment method according to claim 1, it is characterised in that: the preparation of the sewage-treating agent
Method includes the following steps:
1) by medical stone, flyash, vermiculite, tourmaline powder and pyrophillite mix after, be ground into fine powder, add granularity be 50~
The corncob and pine tree sawdust of the drying of 100 mesh, stir and evenly mix, obtain mixture I;
2) after impregnating mixture I with deionized water, aluminium polychloride, sodium carboxymethyl starch and Sodium Polyacrylate is added, 120
It is stirred 1~1.5h under the revolving speed of~150r/min, obtains solidliquid mixture II, then carry out to resulting solidliquid mixture II
Freeze-drying process obtains dried material;
3) dried material obtained in step 2) is ground into granularity is addition potassium ferrate after 50~100 mesh powders, stirring
Mixing is the multi-functional Environment-friendlysewage sewage treatment agent.
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Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
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CN110436554A (en) * | 2019-08-23 | 2019-11-12 | 河南亿群环保科技有限公司 | A kind of environment protection sewage inorganic agent and preparation method thereof |
CN114478059A (en) * | 2021-12-31 | 2022-05-13 | 西安理工大学 | Preparation method of ceramic filter material |
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CN102120575A (en) * | 2011-03-04 | 2011-07-13 | 南京工业大学 | Process for preparing active carbon from chemical sludge |
CN103102049A (en) * | 2013-03-07 | 2013-05-15 | 苏州苏净环保工程有限公司 | High-nitrogen-concentration organic wastewater treatment method |
CN107162093A (en) * | 2017-07-04 | 2017-09-15 | 合肥市大卓电力有限责任公司 | A kind of aquaculture water purifying agent and preparation method thereof |
CN107840545A (en) * | 2017-11-30 | 2018-03-27 | 重庆精创联合环保工程有限公司 | Process for treating industrial waste water |
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CN102120575A (en) * | 2011-03-04 | 2011-07-13 | 南京工业大学 | Process for preparing active carbon from chemical sludge |
CN103102049A (en) * | 2013-03-07 | 2013-05-15 | 苏州苏净环保工程有限公司 | High-nitrogen-concentration organic wastewater treatment method |
CN107162093A (en) * | 2017-07-04 | 2017-09-15 | 合肥市大卓电力有限责任公司 | A kind of aquaculture water purifying agent and preparation method thereof |
CN107840545A (en) * | 2017-11-30 | 2018-03-27 | 重庆精创联合环保工程有限公司 | Process for treating industrial waste water |
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CN110436554A (en) * | 2019-08-23 | 2019-11-12 | 河南亿群环保科技有限公司 | A kind of environment protection sewage inorganic agent and preparation method thereof |
CN114478059A (en) * | 2021-12-31 | 2022-05-13 | 西安理工大学 | Preparation method of ceramic filter material |
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Application publication date: 20190101 |