CN105502682A - Water purifier adopted in nitrile rubber production and wastewater treatment method - Google Patents

Water purifier adopted in nitrile rubber production and wastewater treatment method Download PDF

Info

Publication number
CN105502682A
CN105502682A CN201510942293.XA CN201510942293A CN105502682A CN 105502682 A CN105502682 A CN 105502682A CN 201510942293 A CN201510942293 A CN 201510942293A CN 105502682 A CN105502682 A CN 105502682A
Authority
CN
China
Prior art keywords
water
waste water
bacterium powder
stir
hour
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
CN201510942293.XA
Other languages
Chinese (zh)
Inventor
尤晓明
王显涛
张新平
曹佃波
冯小波
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Yongtai Shandong Group Co Ltd
Original Assignee
Yongtai Shandong Group Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Yongtai Shandong Group Co Ltd filed Critical Yongtai Shandong Group Co Ltd
Priority to CN201510942293.XA priority Critical patent/CN105502682A/en
Publication of CN105502682A publication Critical patent/CN105502682A/en
Pending legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F3/00Biological treatment of water, waste water, or sewage
    • C02F3/34Biological treatment of water, waste water, or sewage characterised by the microorganisms used
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2103/00Nature of the water, waste water, sewage or sludge to be treated
    • C02F2103/34Nature of the water, waste water, sewage or sludge to be treated from industrial activities not provided for in groups C02F2103/12 - C02F2103/32
    • C02F2103/36Nature of the water, waste water, sewage or sludge to be treated from industrial activities not provided for in groups C02F2103/12 - C02F2103/32 from the manufacture of organic compounds
    • C02F2103/38Polymers

Landscapes

  • Life Sciences & Earth Sciences (AREA)
  • Microbiology (AREA)
  • Biodiversity & Conservation Biology (AREA)
  • Hydrology & Water Resources (AREA)
  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
  • Micro-Organisms Or Cultivation Processes Thereof (AREA)

Abstract

The invention belongs to the technical field of rubber wastewater treatment, and particularly relates to a water purifier adopted in nitrile rubber production and a wastewater treatment method. The water purifier is composed of a solid adsorption material, a microorganism water purifier and an enzymic preparation. The solid adsorption material is prepared from, by weight, 10-25 parts of medical stone, 10-20 parts of slag and 5-20 parts of polyacrylamide. The microorganism water purifier is prepared from, by weight, 0.5-2.0 parts of sphingomonas paucimobilis powder, 0.5-1.5 parts of sulfate reducting bacterium powder, 0.2-1.0 part of rhodococcus ruber powder and 0.5-1.5 parts of paracoccus aminovorans powder. The enzymic preparation is prepared from, by weight, 0.05-0.1 part of thioesterase, 0.04-0.15 part of aldehyde dehydrogenase, 0.03-0.2 part of mannose and 0.02-0.1 part of lipoxygenase. The solid water purifier, the composite microbial agent and the enzymic preparation act on wastewater together, secondary pollution caused by chemical treatment is avoided, sewage discharge is reduced, and the quality of wastewater is improved; by the adoption of the method, CODcr discharge meets the national standard.

Description

Water purification agent used and method of wastewater treatment in paracril production
Technical field
The invention belongs to Rubber Industrial Wastewater processing technology field, be specifically related to water purification agent used and method of wastewater treatment in the production of a kind of paracril.
Background technology
Wastewater source in paracril mainly SS, COD, pull open powder, divinyl, vinyl cyanide etc., in above-mentioned waste component, pulling open powder is the anion surfactant containing a naphthalene nucleus, main component is 1,2-dibutyl-6-sodium naphthalene sulfonate, is a kind of branched chain type anion surfactant, a large amount of foams can be produced in water, reduce reoxygenation speed and the oxygenation degree of water, suppress and kill microorganism, causing great difficulty to biological wastewater treatment.Pull open the structure quite stable of powder, biological degradability is poor, is difficult to decompose, because adopt the process of conventional physics, chemical process (as absorption, flocculating settling, chemical oxidation, biological degradation etc.), is all difficult to obtain satisfied effect.
Therefore, need to process for above-mentioned waste water, and its effect of single physical sedimentation is unsatisfactory, chemical treatment method easily brings new pollution, produces other chemical substance.
Summary of the invention
In order to solve above-mentioned technical problem, the invention provides a kind of water purification agent be made up of solid-state water purification agent, complex micro organism fungicide and zymin, additionally provide the method adopting above-mentioned water purification agent process paracril factory effluent, the method is without the need to adding a large amount of chemical reagent, environmentally friendly, and its purifying water effect is good.
The present invention is realized by following technical scheme:
Water purification agent used in paracril production, is made up of solid adsorbant material, microbial water-purifying agent and zymin, and its parts by weight are as follows respectively:
Solid adsorbant material is: medical stone 10-30, slag 10-20, polyacrylamide 5-20;
Microbial water-purifying agent is: sphingomonas paucimobilis bacterium powder 0.5-2.0, sulphate reducing bacteria bacterium powder 0.5-1.5, Rhodococcus ruber bacterium powder 0.2-1.0, bite ammonia secondary coccus bacterium powder 0.5-1.5;
Zymin is: thioesterase 0.05-0.1, aldehyde dehydrogenase 0.04-0.15, mannase 0.03-0.2, lipoxygenase 0.02-0.1.
Preferably, above-mentioned solid adsorbant material is: medical stone 24, slag 15, polyacrylamide 15;
Microbial water-purifying agent is: sphingomonas paucimobilis bacterium powder 1.5, sulphate reducing bacteria bacterium powder 0.9, Rhodococcus ruber bacterium powder 0.6, bite ammonia secondary coccus bacterium powder 1.2;
Zymin is: thioesterase 0.08, aldehyde dehydrogenase 0.09, mannase 0.06, lipoxygenase 0.06.
The method of waste water in above-mentioned water purification agent process paracril production, comprises following step:
In waste water, first add solid adsorbant material, stir with the rotating speed of 10-20 rev/min, stir 0.2-1 hour, leave standstill 2-5 hour, waste water is layered as upper strata clear water and lower sediment; Solid adsorbant material is: medical stone 10-30, slag 10-20, polyacrylamide 5-20;
Release the upper strata clear water in above-mentioned waste water, the deposit fouling thing of removing bottom, adds microbial water-purifying agent, stirs with the rotating speed of 10-20 rev/min in the clear water of upper strata, stirs 0.2-1 hour, leaves standstill 2-6 hour; Microbial water-purifying agent is: sphingomonas paucimobilis bacterium powder 0.5-2.0, sulphate reducing bacteria bacterium powder 0.5-1.5, Rhodococcus ruber bacterium powder 0.2-1.0, bite ammonia secondary coccus bacterium powder 0.5-1.5;
Again the waste water of above-mentioned steps is regulated pH to 4.5-6.0, the temperature keeping waste water is 35-45 DEG C, zymin is added again in above-mentioned waste water, stir with the rotating speed of 10-20 rev/min, stir 0.2-1 hour, leave standstill 3-8 hour, zymin is thioesterase 0.05-0.1, aldehyde dehydrogenase 0.04-0.15, mannase 0.03-0.2, lipoxygenase 0.02-0.1.
Preferably, the method for waste water in paracril production, comprises following step:
In waste water, first add solid adsorbant material, stir with the rotating speed of 15 revs/min, stir 0.6 hour, leave standstill 3 hours, waste water is layered as upper strata clear water and lower sediment; Solid adsorbant material is: medical stone 24, slag 15, polyacrylamide 15;
Release the upper strata clear water in above-mentioned waste water, the deposit fouling thing of removing bottom, adds microbial water-purifying agent, stirs with the rotating speed of 15 revs/min, stir 0.5 hour in the clear water of upper strata, leaves standstill 4 hours; Microbial water-purifying agent is: sphingomonas paucimobilis bacterium powder 1.5, sulphate reducing bacteria bacterium powder 0.9, Rhodococcus ruber bacterium powder 0.6, bite ammonia secondary coccus bacterium powder 1.2;
Again the waste water of above-mentioned steps is regulated pH to 5, the temperature keeping waste water is 37 DEG C, zymin is added again in above-mentioned waste water, stir with the rotating speed of 15 revs/min, stir 0.6 hour, leave standstill 6 hours, thioesterase 0.08, aldehyde dehydrogenase 0.09, mannase 0.06, lipoxygenase 0.06.
Preferably, the method for waste water in paracril production, comprises following step:
In waste water, first add solid adsorbant material, stir with the rotating speed of 10 revs/min, stir 0.2 hour, leave standstill 2 hours, waste water is layered as upper strata clear water and lower sediment; Solid adsorbant material is: medical stone 10, slag 10, polyacrylamide 5;
Release the upper strata clear water in above-mentioned waste water, the deposit fouling thing of removing bottom, adds microbial water-purifying agent, stirs with the rotating speed of 10 revs/min, stir 0.2 hour in the clear water of upper strata, leaves standstill 2 hours; Microbial water-purifying agent is: sphingomonas paucimobilis bacterium powder 0.5, sulphate reducing bacteria bacterium powder 0.5, Rhodococcus ruber bacterium powder 0.2, bite ammonia secondary coccus bacterium powder 0.5;
Again the waste water of above-mentioned steps is regulated pH to 4.5, the temperature keeping waste water is 35 DEG C, zymin is added again in above-mentioned waste water, stir with the rotating speed of 10 revs/min, stir 0.2 hour, leave standstill 3 hours, zymin is thioesterase 0.05, aldehyde dehydrogenase 0.04, mannase 0.03, lipoxygenase 0.02.
Preferably, the method for waste water in paracril production, comprises following step:
In waste water, first add solid adsorbant material, stir with the rotating speed of 20 revs/min, stir 1 hour, leave standstill 5 hours, waste water is layered as upper strata clear water and lower sediment; Solid adsorbant material is: medical stone 25, slag 20, polyacrylamide 15;
Release the upper strata clear water in above-mentioned waste water, the deposit fouling thing of removing bottom, adds microbial water-purifying agent, stirs with the rotating speed of 20 revs/min, stir 1 hour in the clear water of upper strata, leaves standstill 6 hours; Microbial water-purifying agent is: sphingomonas paucimobilis bacterium powder 2.0, sulphate reducing bacteria bacterium powder 1.5, Rhodococcus ruber bacterium powder 1.0, bite ammonia secondary coccus bacterium powder 1.5;
Again the waste water of above-mentioned steps is regulated pH to 6.0, the temperature keeping waste water is 45 DEG C, zymin is added again in above-mentioned waste water, stir with the rotating speed of 20 revs/min, stir 1 hour, 2 leave standstill 8 hours, and zymin is thioesterase 0.1, aldehyde dehydrogenase 0.15, mannase 0.2, lipoxygenase 0.1.
Beneficial effect of the present invention is, waste water in adopting water purification agent of the present invention and adopting above-mentioned water purification agent to produce paracril processes, adopt solid water purifier and complex micro organism fungicide, zymin acting in conjunction in waste water, avoid the secondary pollution that chemical treatment produces, decrease the quantity discharged of sewage, improve the water quality of waste water; And complex microorganism bacterial classification of the present invention can improve the ability of system anti-shock loading, to deal with the too high situation of organic substance load; Method of the present invention makes the quantity discharged of CODcr reach state specified standards.
Embodiment
Below in conjunction with specific embodiment, the present invention is further described, so that those skilled in the art more understands the present invention, but does not therefore limit the present invention.
Embodiment 1
Following waste water takes from certain rubber production producer, this waste water is specially the waste water that above-mentioned producer produces when producing paracril, more suspended substance is had in the water body of waste water, water body has peculiar smell, adopts method of the present invention to carry out following process (the waste water sample got in following embodiment 2,3 is same batch):
In waste water, first add solid adsorbant material, stir with the rotating speed of 15 revs/min, stir 0.6 hour, leave standstill 3 hours, waste water is layered as upper strata clear water and lower sediment; Solid adsorbant material is: medical stone 24, slag 15, polyacrylamide 15;
Release the upper strata clear water in above-mentioned waste water, the deposit fouling thing of removing bottom, adds microbial water-purifying agent, stirs with the rotating speed of 15 revs/min, stir 0.5 hour in the clear water of upper strata, leaves standstill 4 hours; Microbial water-purifying agent is: sphingomonas paucimobilis bacterium powder 1.5, sulphate reducing bacteria bacterium powder 0.9, Rhodococcus ruber bacterium powder 0.6, bite ammonia secondary coccus bacterium powder 1.2;
Again the waste water of above-mentioned steps is regulated pH to 5, the temperature keeping waste water is 37 DEG C, zymin is added again in above-mentioned waste water, stir with the rotating speed of 15 revs/min, stir 0.6 hour, leave standstill 6 hours, thioesterase 0.08, aldehyde dehydrogenase 0.09, mannase 0.06, lipoxygenase 0.06.
Waste water after treatment, detects its each index as follows:
CODcr value is 45mg/L;
PH value is about 7.23;
SS is 18.5mg/L, reaches the emission standard of national regulation.
Embodiment 2
In waste water, first add solid adsorbant material, stir with the rotating speed of 10 revs/min, stir 0.2 hour, leave standstill 2 hours, waste water is layered as upper strata clear water and lower sediment; Solid adsorbant material is: medical stone 10, slag 10, polyacrylamide 5;
Release the upper strata clear water in above-mentioned waste water, the deposit fouling thing of removing bottom, adds microbial water-purifying agent, stirs with the rotating speed of 10 revs/min, stir 0.2 hour in the clear water of upper strata, leaves standstill 2 hours; Microbial water-purifying agent is: sphingomonas paucimobilis bacterium powder 0.5, sulphate reducing bacteria bacterium powder 0.5, Rhodococcus ruber bacterium powder 0.2, bite ammonia secondary coccus bacterium powder 0.5;
Again the waste water of above-mentioned steps is regulated pH to 4.5, the temperature keeping waste water is 35 DEG C, zymin is added again in above-mentioned waste water, stir with the rotating speed of 10 revs/min, stir 0.2 hour, leave standstill 3 hours, zymin is thioesterase 0.05, aldehyde dehydrogenase 0.04, mannase 0.03, lipoxygenase 0.02.
Waste water after treatment, detects its each index as follows:
CODcr value is 54mg/L,
PH value is about 7.28;
SS is 21.3mg/L, reaches the emission standard of national regulation.
Embodiment 3
In waste water, first add solid adsorbant material, stir with the rotating speed of 20 revs/min, stir 1 hour, leave standstill 5 hours, waste water is layered as upper strata clear water and lower sediment; Solid adsorbant material is: medical stone 25, slag 20, polyacrylamide 15;
Release the upper strata clear water in above-mentioned waste water, the deposit fouling thing of removing bottom, adds microbial water-purifying agent, stirs with the rotating speed of 20 revs/min, stir 1 hour in the clear water of upper strata, leaves standstill 6 hours; Microbial water-purifying agent is: sphingomonas paucimobilis bacterium powder 2.0, sulphate reducing bacteria bacterium powder 1.5, Rhodococcus ruber bacterium powder 1.0, bite ammonia secondary coccus bacterium powder 1.5;
Again the waste water of above-mentioned steps is regulated pH to 6.0, the temperature keeping waste water is 45 DEG C, zymin is added again in above-mentioned waste water, stir with the rotating speed of 20 revs/min, stir 1 hour, 2 leave standstill 8 hours, and zymin is thioesterase 0.1, aldehyde dehydrogenase 0.15, mannase 0.2, lipoxygenase 0.1.
Waste water after treatment, detects its each index as follows:
CODcr value is 58mg/L,
PH value is about 7.24;
SS is 23.5mg/L, reaches the emission standard of national regulation.

Claims (8)

1. water purification agent used in paracril production, it is characterized in that, described water purification agent is made up of solid adsorbant material, microbial water-purifying agent and zymin, and its parts by weight are as follows respectively:
Described solid adsorbant material is: medical stone 10-30, slag 10-20, polyacrylamide 5-20;
Described microbial water-purifying agent is: sphingomonas paucimobilis bacterium powder 0.5-2.0, sulphate reducing bacteria bacterium powder 0.5-1.5, Rhodococcus ruber bacterium powder 0.2-1.0, bite ammonia secondary coccus bacterium powder 0.5-1.5;
Described zymin is: thioesterase 0.05-0.1, aldehyde dehydrogenase 0.04-0.15, mannase 0.03-0.2, lipoxygenase 0.02-0.1.
2. water purification agent used in paracril production as claimed in claim 1, it is characterized in that, described solid adsorbant material is: medical stone 24, slag 15, polyacrylamide 15.
3. paracril as claimed in claim 1 produce in water purification agent used, it is characterized in that, described microbial water-purifying agent is: sphingomonas paucimobilis bacterium powder 1.5, sulphate reducing bacteria bacterium powder 0.9, Rhodococcus ruber bacterium powder 0.6, bite ammonia secondary coccus bacterium powder 1.2.
4. water purification agent used in paracril production as claimed in claim 1, it is characterized in that, described zymin is: thioesterase 0.08, aldehyde dehydrogenase 0.09, mannase 0.06, lipoxygenase 0.06.
5. the method for waste water in adopting water purification agent process paracril as claimed in claim 1 to produce, comprises following step:
In waste water, first add solid adsorbant material, stir with the rotating speed of 10-20 rev/min, stir 0.2-1 hour, leave standstill 2-5 hour, waste water is layered as upper strata clear water and lower sediment; Described solid adsorbant material is: medical stone 10-30, slag 10-20, polyacrylamide 5-20;
Release the upper strata clear water in above-mentioned waste water, the deposit fouling thing of removing bottom, adds microbial water-purifying agent, stirs with the rotating speed of 10-20 rev/min in the clear water of upper strata, stirs 0.2-1 hour, leaves standstill 2-6 hour; Described microbial water-purifying agent is: sphingomonas paucimobilis bacterium powder 0.5-2.0, sulphate reducing bacteria bacterium powder 0.5-1.5, Rhodococcus ruber bacterium powder 0.2-1.0, bite ammonia secondary coccus bacterium powder 0.5-1.5;
Again the waste water of above-mentioned steps is regulated pH to 4.5-6.0, the temperature keeping waste water is 35-45 DEG C, zymin is added again in above-mentioned waste water, stir with the rotating speed of 10-20 rev/min, stir 0.2-1 hour, leave standstill 3-8 hour, described zymin is thioesterase 0.05-0.1, aldehyde dehydrogenase 0.04-0.15, mannase 0.03-0.2, lipoxygenase 0.02-0.1.
6. paracril as claimed in claim 5 produce in the method for waste water, it is characterized in that, described method comprises following step:
In waste water, first add solid adsorbant material, stir with the rotating speed of 15 revs/min, stir 0.6 hour, leave standstill 3 hours, waste water is layered as upper strata clear water and lower sediment; Described solid adsorbant material is: medical stone 24, slag 15, polyacrylamide 15;
Release the upper strata clear water in above-mentioned waste water, the deposit fouling thing of removing bottom, adds microbial water-purifying agent, stirs with the rotating speed of 15 revs/min, stir 0.5 hour in the clear water of upper strata, leaves standstill 4 hours; Described microbial water-purifying agent is: sphingomonas paucimobilis bacterium powder 1.5, sulphate reducing bacteria bacterium powder 0.9, Rhodococcus ruber bacterium powder 0.6, bite ammonia secondary coccus bacterium powder 1.2;
Again the waste water of above-mentioned steps is regulated pH to 5, the temperature keeping waste water is 37 DEG C, zymin is added again in above-mentioned waste water, stir with the rotating speed of 15 revs/min, stir 0.6 hour, leave standstill 6 hours, described thioesterase 0.08, aldehyde dehydrogenase 0.09, mannase 0.06, lipoxygenase 0.06.
7. paracril as claimed in claim 5 produce in the method for waste water, it is characterized in that, described method comprises following step:
In waste water, first add solid adsorbant material, stir with the rotating speed of 10 revs/min, stir 0.2 hour, leave standstill 2 hours, waste water is layered as upper strata clear water and lower sediment; Described solid adsorbant material is: medical stone 10, slag 10, polyacrylamide 5;
Release the upper strata clear water in above-mentioned waste water, the deposit fouling thing of removing bottom, adds microbial water-purifying agent, stirs with the rotating speed of 10 revs/min, stir 0.2 hour in the clear water of upper strata, leaves standstill 2 hours; Described microbial water-purifying agent is: sphingomonas paucimobilis bacterium powder 0.5, sulphate reducing bacteria bacterium powder 0.5, Rhodococcus ruber bacterium powder 0.2, bite ammonia secondary coccus bacterium powder 0.5;
Again the waste water of above-mentioned steps is regulated pH to 4.5, the temperature keeping waste water is 35 DEG C, zymin is added again in above-mentioned waste water, stir with the rotating speed of 10 revs/min, stir 0.2 hour, leave standstill 3 hours, described zymin is thioesterase 0.05, aldehyde dehydrogenase 0.04, mannase 0.03, lipoxygenase 0.02.
8. paracril as claimed in claim 5 produce in the method for waste water, it is characterized in that, described method comprises following step:
In waste water, first add solid adsorbant material, stir with the rotating speed of 20 revs/min, stir 1 hour, leave standstill 5 hours, waste water is layered as upper strata clear water and lower sediment; Described solid adsorbant material is: medical stone 25, slag 20, polyacrylamide 15;
Release the upper strata clear water in above-mentioned waste water, the deposit fouling thing of removing bottom, adds microbial water-purifying agent, stirs with the rotating speed of 20 revs/min, stir 1 hour in the clear water of upper strata, leaves standstill 6 hours; Described microbial water-purifying agent is: sphingomonas paucimobilis bacterium powder 2.0, sulphate reducing bacteria bacterium powder 1.5, Rhodococcus ruber bacterium powder 1.0, bite ammonia secondary coccus bacterium powder 1.5;
Again the waste water of above-mentioned steps is regulated pH to 6.0, the temperature keeping waste water is 45 DEG C, zymin is added again in above-mentioned waste water, stir with the rotating speed of 20 revs/min, stir 1 hour, 2 leave standstill 8 hours, and described zymin is thioesterase 0.1, aldehyde dehydrogenase 0.15, mannase 0.2, lipoxygenase 0.1.
CN201510942293.XA 2015-12-16 2015-12-16 Water purifier adopted in nitrile rubber production and wastewater treatment method Pending CN105502682A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201510942293.XA CN105502682A (en) 2015-12-16 2015-12-16 Water purifier adopted in nitrile rubber production and wastewater treatment method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201510942293.XA CN105502682A (en) 2015-12-16 2015-12-16 Water purifier adopted in nitrile rubber production and wastewater treatment method

Publications (1)

Publication Number Publication Date
CN105502682A true CN105502682A (en) 2016-04-20

Family

ID=55711067

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201510942293.XA Pending CN105502682A (en) 2015-12-16 2015-12-16 Water purifier adopted in nitrile rubber production and wastewater treatment method

Country Status (1)

Country Link
CN (1) CN105502682A (en)

Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1611450A (en) * 2003-10-31 2005-05-04 中国石油化工股份有限公司 Waste water purifying agent, and its preparing method and use
CN104478168A (en) * 2014-12-13 2015-04-01 山东永泰化工有限公司 Treatment process for wastewater generated during recycling process of waste tire
CN104478169A (en) * 2014-12-13 2015-04-01 山东永泰化工有限公司 Water purifying agent for wastewater treatment of tire production enterprises and wastewater treatment method
CN104478096A (en) * 2014-12-13 2015-04-01 山东永泰化工有限公司 Water purifying agent for wastewater treatment in rubber accelerator production and wastewater treatment method
CN104478095A (en) * 2014-12-13 2015-04-01 山东永泰化工有限公司 Water purifying agent for wastewater treatment in rubber accelerator M production and wastewater treatment method
CN104478097A (en) * 2014-12-13 2015-04-01 山东永泰化工有限公司 Water purifying agent for sewage resulting from recovery of waste/used tires and sewage treatment method
CN104649408A (en) * 2015-03-10 2015-05-27 北京麦克安吉生物技术有限公司 Bio-enzyme preparation for aerobic section process for municipal and industrial wastewater treatment

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1611450A (en) * 2003-10-31 2005-05-04 中国石油化工股份有限公司 Waste water purifying agent, and its preparing method and use
CN104478168A (en) * 2014-12-13 2015-04-01 山东永泰化工有限公司 Treatment process for wastewater generated during recycling process of waste tire
CN104478169A (en) * 2014-12-13 2015-04-01 山东永泰化工有限公司 Water purifying agent for wastewater treatment of tire production enterprises and wastewater treatment method
CN104478096A (en) * 2014-12-13 2015-04-01 山东永泰化工有限公司 Water purifying agent for wastewater treatment in rubber accelerator production and wastewater treatment method
CN104478095A (en) * 2014-12-13 2015-04-01 山东永泰化工有限公司 Water purifying agent for wastewater treatment in rubber accelerator M production and wastewater treatment method
CN104478097A (en) * 2014-12-13 2015-04-01 山东永泰化工有限公司 Water purifying agent for sewage resulting from recovery of waste/used tires and sewage treatment method
CN104649408A (en) * 2015-03-10 2015-05-27 北京麦克安吉生物技术有限公司 Bio-enzyme preparation for aerobic section process for municipal and industrial wastewater treatment

Similar Documents

Publication Publication Date Title
CN101157510B (en) Process for treating waste water produced during biofermentation method for producing penicillin and intermediate 6-APA process
CN102649616B (en) Comprehensive treatment method for garbage leachate
CN103011526B (en) Method for treating erythromycin thiocyanate wastewater
CN103936225B (en) The method of catalyzed internal electrocatalysis coupling two-stage biofilter advanced treatment on coking wastewater
CN104150713B (en) The treatment process of waste water in rutin production process
CN101549940B (en) Technique of treating textile dyeing waste water
CN104671613B (en) A kind for the treatment of process of percolate from garbage filling field
CN102730907B (en) Deep treatment method for printing and dyeing industry production waste water
CN105217911B (en) It is a kind of to react the technique for carrying out sludge dewatering using bioleaching
CN105036312A (en) Starting method for high-salinity wastewater MBBR treatment system
CN104531783B (en) The method that copper sulphate joint alkaline pH promotes excess sludge anaerobic fermentation production short chain fatty acids
CN103708626A (en) Method for treating solid-waste anaerobic fermentation biogas slurry
CN102408172A (en) Pretreatment method for preparing polymer solution by recovering oil field produced water
CN107235553B (en) Low-temperature aerobic granular sludge rapid culture method based on sludge incineration ash
CN104556528A (en) An integrated treatment process of clindamycin alkaline wastewater
CN105000751A (en) Integrated treatment method of aceto acetanilide wastewater and diketene wastewater
CN105254035A (en) Essence production wastewater treating agent and wastewater treatment method
WO2016103949A1 (en) Treatment method and treatment device for fat and/or oil-containing waste water
CN105502682A (en) Water purifier adopted in nitrile rubber production and wastewater treatment method
CN105923888B (en) A kind of method of Fenton oxidation-MBR combined depths processing antibiotic waste water
CN104529106A (en) Method for promoting anaerobic digestion of excess sludge through copper sulfate to produce methane
CN102923903A (en) Textile printing and dyeing wastewater processing technology
CN105502683A (en) Water purifying agent used in isoprene rubber production and wastewater treatment method
CN105621576A (en) Composite aluminum-iron water purifier and production method thereof
CN112358041A (en) Granular sludge culture method for synchronous denitrification and methanogenesis and COD removal

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
RJ01 Rejection of invention patent application after publication
RJ01 Rejection of invention patent application after publication

Application publication date: 20160420