CN106565051A - Novel non-degradable industrial sewage treatment method - Google Patents

Novel non-degradable industrial sewage treatment method Download PDF

Info

Publication number
CN106565051A
CN106565051A CN201510645075.XA CN201510645075A CN106565051A CN 106565051 A CN106565051 A CN 106565051A CN 201510645075 A CN201510645075 A CN 201510645075A CN 106565051 A CN106565051 A CN 106565051A
Authority
CN
China
Prior art keywords
sending
industrial sewage
salt
product
carrying
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
CN201510645075.XA
Other languages
Chinese (zh)
Inventor
胡华
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to CN201510645075.XA priority Critical patent/CN106565051A/en
Publication of CN106565051A publication Critical patent/CN106565051A/en
Pending legal-status Critical Current

Links

Abstract

The invention discloses a novel non-degradable industrial sewage treatment method. The method comprises the following steps: inputting industrial sewage to a boiler, heating the industrial sewage to 120-150 DEG C, adding fly ash, an iron salt, an aluminum salt and a magnesium salt, mixing and stirring the sewage and above added substances to obtain a first pre-made material, sending the first pre-made material to an electromagnetic field, extracting magnetic substances, purifying the extracted material, sterilizing the extracted material, filtering the purified material, sending the filtered material to an aeration biological filter tank provided with a microbial agent, biodegrading the filtered material, sending the biodegraded material to a resin adsorption reactor, adsorbing organic matters through magnetic ion exchange resin in a stirring state, sending a product obtained after the adsorption to an ultrafiltration device, carrying out ultrafiltration on the product, sending the ultrafiltered product to a reverse osmosis device, carrying out reverse osmosis treatment, sending the treated product to a regeneration system, carrying out sodium chloride water adsorption, sending the obtained product to an electrolytic oxidation process, carrying out electrolytic oxidation, and processing obtained electrolytic waste liquid through a sodium filter membrane assembly to realize standard-reaching discharge of wastewater. The method has the advantages of low cost, no secondary pollution and extremely high treatment ability.

Description

A kind of new non-degradable industrial sewage processing method
Technical field
The present invention relates to technical field of sewage, more particularly to a kind of new non-degradable industrial sewage process side Method.
Background technology
The pollutant levels of trade effluent are big, poisonous and harmful substance species is more, therefore waste water raw water is directly entered life Thing system can constitute serious suppression to microorganism, in order to solve this problem, generally adopt compared with multiple enterprises both at home and abroad With direct dilution method or the reflux dilution method of process water outlet, although reclaimed in sewage by physical separation effect Undissolved suspended contaminant, this centrifugation can be divided into Gravity Separation, centrifugation and sieving retention point From this method can only make some simple sewage disposals, but process dangerous, it is difficult to reach discharge standard.
Current chemical treatment method is allowed to and the pollutant in water by various flocculant are put into in waste water Chemically reactive, generates water-fast compound, separates out precipitation, as pollutant are simply condensed into greatly Block and depart from from water, Organic substance itself effectively do not degraded, and causes a large amount of sludge flcos so that run High cost and generation secondary pollution.
The content of the invention
The present invention proposes a kind of new non-degradable industrial sewage processing method, and low cost of the present invention does not have two Secondary pollution, and disposal ability is extremely strong.
A kind of new non-degradable industrial sewage processing method proposed by the present invention, comprises the steps:
S1, by trade effluent be input into boiler in, be warming up to 120-150 DEG C, add flyash, iron salt, aluminium salt, Magnesium salt is mixed, and mixing time is 40-80min, obtains the first prefabricated material;
S2, the first prefabricated material is sent into magnetic field extract magnetisable material, purify, sterilization is filtered, and feeding contains The BAF for having microbial bacterial agent carries out biodegradation, and microbial bacterial agent is wished by dynamic glue bacterium, middle angstrom
Salmonella, unwrapping wire shape Nocard's bacilluss, bacillus cereuss, Sphaerotilus natans composition, move glue bacterium, centre angstrom and wish Salmonella, unwrapping wire shape Nocard's bacilluss, bacillus cereuss, the weight ratio of Sphaerotilus natans are 1-2∶0.5-1.5∶1-4∶2-6∶2-5;
S3, the material for obtaining S2 are sent in resin absorption reactor, are handed over by magnetic ion under stirring Resin absorption Organic substance is changed, wherein mixing speed is 100-150r/min, and whipping temp is 40-60 DEG C, is sent Enter ultrafiltration apparatus to the product ultrafiltration after absorption, send into reverse osmosis unit reverse-osmosis treated, be re-fed into regeneration system System carries out sodium chloride brine absorption, sends into electrolytic oxidation operation electrolytic oxidation, by sodium filter membrane component to electrolysis Liquid waste processing, final discharged wastewater met the national standard.
Preferably, in S1, trade effluent is input in boiler, 130-145 DEG C is warming up to, addition flyash, Iron salt, aluminium salt, magnesium salt are mixed, and mixing time is 60-75min, obtains the first prefabricated material.
Preferably, in S2, move glue bacterium, middle Escherichia, unwrapping wire shape Nocard's bacilluss, bacillus cereuss, floating The weight ratio of trip football shirt bacterium is 1.5-1.8: 1-1.4: 2-3.5: 3-5: 3-4.
Preferably, in S3, mixing speed is 120-145r/min, and whipping temp is 50-55 DEG C.
In the present invention, can Organic substance in efficient absorption degrading waste water, hardly degraded organic substance concentration significantly drops Low, biodegradability is greatly improved, and the water after purification can reach discharge standard, wherein the micro- life for adding The high-efficiency strain that the characteristics of thing microbial inoculum is non-degradable industrial sewage is screened, microbial inoculum strong adaptability, to difficult degradation, Strong containing the more waste treatment capacity of phenyl ring, heterocyclic material, technique is into cost, and no secondary pollution, It is suitable to large-scale use.
Specific embodiment
Below, technical scheme is described in detail by specific embodiment.
Embodiment 1
A kind of new non-degradable industrial sewage processing method, comprises the steps:
S1, by trade effluent be input into boiler in, be warming up to 120 DEG C, add flyash, iron salt, aluminium salt, magnesium Salt is mixed, and mixing time is 80min, obtains the first prefabricated material;
S2, the first prefabricated material is sent into magnetic field extract magnetisable material, purify, sterilization is filtered, and feeding contains The BAF for having microbial bacterial agent carries out biodegradation, and microbial bacterial agent is wished by dynamic glue bacterium, middle angstrom Salmonella, unwrapping wire shape Nocard's bacilluss, bacillus cereuss, Sphaerotilus natans composition, move glue bacterium, middle Escherichia, Unwrapping wire shape Nocard's bacilluss, bacillus cereuss, the weight ratio of Sphaerotilus natans are 1: 1.5: 1: 6: 2;
S3, the material for obtaining S2 are sent in resin absorption reactor, are handed over by magnetic ion under stirring Resin absorption Organic substance is changed, wherein mixing speed is 150r/min, and whipping temp is 40 DEG C, sends into ultrafiltration dress Put to the product ultrafiltration after absorption, send into reverse osmosis unit reverse-osmosis treated, being re-fed into regenerative system carries out chlorine Change natrium brine absorption, send into electrolytic oxidation operation electrolytic oxidation, by sodium filter membrane component to electrolysis waste solution process, Final discharged wastewater met the national standard.
Embodiment 2
A kind of new non-degradable industrial sewage processing method, comprises the steps:
S1, by trade effluent be input into boiler in, be warming up to 150 DEG C, add flyash, iron salt, aluminium salt, magnesium Salt is mixed, and mixing time is 40min, obtains the first prefabricated material;
S2, the first prefabricated material is sent into magnetic field extract magnetisable material, purify, sterilization is filtered, and feeding contains The BAF for having microbial bacterial agent carries out biodegradation, and microbial bacterial agent is wished by dynamic glue bacterium, middle angstrom Salmonella, unwrapping wire shape Nocard's bacilluss, bacillus cereuss, Sphaerotilus natans composition, move glue bacterium, middle Escherichia, Unwrapping wire shape Nocard's bacilluss, bacillus cereuss, the weight ratio of Sphaerotilus natans are 2: 0.5: 4: 2: 5;
S3, the material for obtaining S2 are sent in resin absorption reactor, are handed over by magnetic ion under stirring Resin absorption Organic substance is changed, wherein mixing speed is 100r/min, and whipping temp is 60 DEG C, sends into ultrafiltration dress Put to the product ultrafiltration after absorption, send into reverse osmosis unit reverse-osmosis treated, being re-fed into regenerative system carries out chlorine Change natrium brine absorption, send into electrolytic oxidation operation electrolytic oxidation, by sodium filter membrane component to electrolysis waste solution process, Final discharged wastewater met the national standard.
Embodiment 3
A kind of new non-degradable industrial sewage processing method, comprises the steps:
S1, by trade effluent be input into boiler in, be warming up to 140 DEG C, add flyash, iron salt, aluminium salt, magnesium Salt is mixed, and mixing time is 70min, obtains the first prefabricated material;
S2, the first prefabricated material is sent into magnetic field extract magnetisable material, purify, sterilization is filtered, and feeding contains The BAF for having microbial bacterial agent carries out biodegradation, and microbial bacterial agent is wished by dynamic glue bacterium, middle angstrom Salmonella, unwrapping wire shape Nocard's bacilluss, bacillus cereuss, Sphaerotilus natans composition, move glue bacterium, middle Escherichia, Unwrapping wire shape Nocard's bacilluss, bacillus cereuss, the weight ratio of Sphaerotilus natans are 1.6: 1.3: 3.2: 4: 3.5;
S3, the material for obtaining S2 are sent in resin absorption reactor, are handed over by magnetic ion under stirring Resin absorption Organic substance is changed, wherein mixing speed is 140r/min, and whipping temp is 53 DEG C, sends into ultrafiltration dress Put to the product ultrafiltration after absorption, send into reverse osmosis unit reverse-osmosis treated, being re-fed into regenerative system carries out chlorine Change natrium brine absorption, send into electrolytic oxidation operation electrolytic oxidation, by sodium filter membrane component to electrolysis waste solution process, Final discharged wastewater met the national standard.
Treatment effect:To containing Organic substance, (COD9500mg/L, BOD/COD sewage 0.14) adopts above-mentioned process After method, supernatant is analyzed to discharge water sampling, after standing, the COD of purified water is 145-160 Mg/L, by the assay to final water sample, the content for finally discharging the float in water is substantially reduced, Final water quality can meet the requirement of environmental protection.
The above, the only present invention preferably specific embodiment, but protection scope of the present invention not office Be limited to this, any those familiar with the art the invention discloses technical scope in, according to this The technical scheme of invention and its inventive concept in addition equivalent or change, should all cover the protection in the present invention Within the scope of.

Claims (4)

1. a kind of new non-degradable industrial sewage processing method, it is characterised in that comprise the steps:
S1, by trade effluent be input into boiler in, be warming up to 120-150 DEG C, add flyash, iron salt, aluminum Salt, magnesium salt are mixed, and mixing time is 40-80min, obtains the first prefabricated material;
S2, the first prefabricated material is sent into magnetic field extract magnetisable material, purify, sterilization is filtered, and feeding contains The BAF for having microbial bacterial agent carries out biodegradation, and microbial bacterial agent is wished by dynamic glue bacterium, middle angstrom Salmonella, unwrapping wire shape Nocard's bacilluss, bacillus cereuss, Sphaerotilus natans composition, move glue bacterium, middle Escherichia, Unwrapping wire shape Nocard's bacilluss, bacillus cereuss, the weight ratio of Sphaerotilus natans are 1-2: 0.5-1.5: 1-4: 2-6: 2-5;
S3, the material for obtaining S2 are sent in resin absorption reactor, are handed over by magnetic ion under stirring Resin absorption Organic substance is changed, wherein mixing speed is 100-150r/min, and whipping temp is 40-60 DEG C, is sent Enter ultrafiltration apparatus to the product ultrafiltration after absorption, send into reverse osmosis unit reverse-osmosis treated, be re-fed into regeneration system System carries out sodium chloride brine absorption, sends into electrolytic oxidation operation electrolytic oxidation, by sodium filter membrane component to electrolysis Liquid waste processing, final discharged wastewater met the national standard.
2. new non-degradable industrial sewage processing method according to claim 1, it is characterised in that S1 In, by trade effluent be input into boiler in, be warming up to 130-145 DEG C, add flyash, iron salt, aluminium salt, Magnesium salt is mixed, and mixing time is 60-75min, obtains the first prefabricated material.
3. new non-degradable industrial sewage processing method according to claim 1, it is characterised in that S2 In, move glue bacterium, middle Escherichia, unwrapping wire shape Nocard's bacilluss, bacillus cereuss, the weight of Sphaerotilus natans Than for 1.5-1.8: 1-1.4: 2-3.5: 3-5: 3-4.
4. new non-degradable industrial sewage processing method according to claim 1, it is characterised in that S3 In, mixing speed is 120-145r/min, and whipping temp is 50-55 DEG C.
CN201510645075.XA 2015-10-09 2015-10-09 Novel non-degradable industrial sewage treatment method Pending CN106565051A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201510645075.XA CN106565051A (en) 2015-10-09 2015-10-09 Novel non-degradable industrial sewage treatment method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201510645075.XA CN106565051A (en) 2015-10-09 2015-10-09 Novel non-degradable industrial sewage treatment method

Publications (1)

Publication Number Publication Date
CN106565051A true CN106565051A (en) 2017-04-19

Family

ID=58507116

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201510645075.XA Pending CN106565051A (en) 2015-10-09 2015-10-09 Novel non-degradable industrial sewage treatment method

Country Status (1)

Country Link
CN (1) CN106565051A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108396155A (en) * 2018-03-05 2018-08-14 云南驰宏锌锗股份有限公司 A kind of process of Zinc electrolysis electrolysis waste solution purification production high quality zinc
CN109231601A (en) * 2018-11-13 2019-01-18 清远市兆成环保包装纸制品有限公司 A kind of circulation utilization method of paper waste
CN110482786A (en) * 2019-08-12 2019-11-22 广东长海建设工程有限公司 The method of municipal sewage treatment

Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS57122991A (en) * 1981-01-23 1982-07-31 Mitsubishi Heavy Ind Ltd Treatment of waste water containing sludge and hydrazine
CN1715217A (en) * 2004-07-02 2006-01-04 桂林工学院 Process for removing nitrogen and phosphor from sewage capable of being built by separate periods
CN101343132A (en) * 2008-08-28 2009-01-14 杭州水处理技术研究开发中心有限公司 Treatment method for wastewater of polyvinyl chloride (PVC) anticentripetal mother solution
CN101428947A (en) * 2008-12-18 2009-05-13 南京中电联环保股份有限公司 Advanced treatment method for acrylic fibre wet-process industrial wastewater with two-step method
CN101665311A (en) * 2009-09-24 2010-03-10 中南大学 Catalysis and micro-electrolysis combined technology for high-concentration refractory organic wastewater
US20100059437A1 (en) * 2008-09-11 2010-03-11 University Of Central Florida Research Foundation, Inc. Passive Underground Drainfield For Septic Tank Nutrient Removal Using Functionalized Green Filtration Media
CN101905931A (en) * 2010-02-11 2010-12-08 南京大学 Advanced treating method of biochemical tail water based on magnetic resin

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS57122991A (en) * 1981-01-23 1982-07-31 Mitsubishi Heavy Ind Ltd Treatment of waste water containing sludge and hydrazine
CN1715217A (en) * 2004-07-02 2006-01-04 桂林工学院 Process for removing nitrogen and phosphor from sewage capable of being built by separate periods
CN101343132A (en) * 2008-08-28 2009-01-14 杭州水处理技术研究开发中心有限公司 Treatment method for wastewater of polyvinyl chloride (PVC) anticentripetal mother solution
US20100059437A1 (en) * 2008-09-11 2010-03-11 University Of Central Florida Research Foundation, Inc. Passive Underground Drainfield For Septic Tank Nutrient Removal Using Functionalized Green Filtration Media
CN101428947A (en) * 2008-12-18 2009-05-13 南京中电联环保股份有限公司 Advanced treatment method for acrylic fibre wet-process industrial wastewater with two-step method
CN101665311A (en) * 2009-09-24 2010-03-10 中南大学 Catalysis and micro-electrolysis combined technology for high-concentration refractory organic wastewater
CN101905931A (en) * 2010-02-11 2010-12-08 南京大学 Advanced treating method of biochemical tail water based on magnetic resin

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
池振明: "《微生物生态学》", 30 June 1999, 山东大学出版社 *

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108396155A (en) * 2018-03-05 2018-08-14 云南驰宏锌锗股份有限公司 A kind of process of Zinc electrolysis electrolysis waste solution purification production high quality zinc
CN109231601A (en) * 2018-11-13 2019-01-18 清远市兆成环保包装纸制品有限公司 A kind of circulation utilization method of paper waste
CN110482786A (en) * 2019-08-12 2019-11-22 广东长海建设工程有限公司 The method of municipal sewage treatment

Similar Documents

Publication Publication Date Title
Gao et al. The present status of landfill leachate treatment and its development trend from a technological point of view
Ahmed An overview of arsenic removal technologies in Bangladesh and India
Das et al. Effluent Treatment Technologies in the Iron and Steel Industry‐A State of the Art Review: Das et al.
Suhartini et al. Influence of powdered Moringa oleifera seeds and natural filter media on the characteristics of tapioca starch wastewater
Li et al. Review on physicochemical, chemical, and biological processes for pharmaceutical wastewater
EP2421798A2 (en) Water treatment
CN102781846A (en) Apparatus and method for electrochemical treatment of wastewater
CN105923850A (en) Treatment technology of refuse leachate membrane concentration liquid
WO2013078639A1 (en) Coking wastewater treatment
CN106977013B (en) Purification treatment method of high-chlorine thallium-containing wastewater and application thereof
CN104445691A (en) Circulating powdered activated carbon and ultrafiltration combined water treatment system and application thereof
Alam et al. A critical review on treatment of saline wastewater with emphasis on electrochemical based approaches
CN103663870B (en) Sewage processing method for food entrepreneurs
Lin et al. Industrial effluent treatments using heavy-metal removing bacterial bioflocculants
CN106565051A (en) Novel non-degradable industrial sewage treatment method
CN104891714A (en) Treatment method and novel composite water purifying agent for purifying water of micro-polluted water sources
WO2013020163A2 (en) A water treatment system
Abdollahzadeh Sharghi et al. The study of organic removal efficiency and membrane fouling in a submerged membrane bioreactor treating vegetable oil wastewater
CN101486524A (en) Comprehensive processing method for furfural production wastewater
US20210292195A1 (en) Anolyte as an additive for wastewater treatment
CN105174546A (en) Industrial wastewater treatment system
CN107473316A (en) Solid-state heavy metal containing wastewater treatment agent
CN113200587A (en) System and method for utilizing, disposing and discharging salt-containing waste
Lawal et al. An Overview of Characterization and Treatment Methods of Wastewater from Iron and Steel Industries.
Estahbanati et al. Physical and physicochemical separation of microplastics and nanoplastics from water

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
DD01 Delivery of document by public notice

Addressee: Hu Hua

Document name: the First Notification of an Office Action

DD01 Delivery of document by public notice
WD01 Invention patent application deemed withdrawn after publication

Application publication date: 20170419

WD01 Invention patent application deemed withdrawn after publication