CN108947022A - A kind of technique for treating industrial wastewater - Google Patents

A kind of technique for treating industrial wastewater Download PDF

Info

Publication number
CN108947022A
CN108947022A CN201811033880.7A CN201811033880A CN108947022A CN 108947022 A CN108947022 A CN 108947022A CN 201811033880 A CN201811033880 A CN 201811033880A CN 108947022 A CN108947022 A CN 108947022A
Authority
CN
China
Prior art keywords
technique
industrial wastewater
treating industrial
pond
reaction solution
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
CN201811033880.7A
Other languages
Chinese (zh)
Inventor
罗万香
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.)
Hanyuan City Of Victoria Zinc Germanium Technology Co Ltd
Original Assignee
Hanyuan City Of Victoria Zinc Germanium Technology 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 Hanyuan City Of Victoria Zinc Germanium Technology Co Ltd filed Critical Hanyuan City Of Victoria Zinc Germanium Technology Co Ltd
Priority to CN201811033880.7A priority Critical patent/CN108947022A/en
Publication of CN108947022A publication Critical patent/CN108947022A/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
    • C02F9/00Multistage treatment of water, waste water or sewage
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/001Processes for the treatment of water whereby the filtration technique is of importance
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/52Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/66Treatment of water, waste water, or sewage by neutralisation; pH adjustment
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/72Treatment of water, waste water, or sewage by oxidation
    • C02F1/74Treatment of water, waste water, or sewage by oxidation with air
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F2001/007Processes including a sedimentation step
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2301/00General aspects of water treatment
    • C02F2301/08Multistage treatments, e.g. repetition of the same process step under different conditions

Landscapes

  • Life Sciences & Earth Sciences (AREA)
  • Hydrology & Water Resources (AREA)
  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Removal Of Specific Substances (AREA)
  • Separation Of Suspended Particles By Flocculating Agents (AREA)

Abstract

The invention belongs to technical field of waste water processing, provide a kind of technique for treating industrial wastewater.The technique for treating industrial wastewater includes: successively to discharge waste water behind pond through conditioning tank, neutralization pond, aeration oxidation pool, coagulation reaction tank, sedimentation basin, filtering ponds, pH readjustment, it is characterised in that: the pH that the lime after pulp is added in coagulation reaction tank adjusts reaction solution is 7-10.The technique for treating industrial wastewater reduces the sulfur content in waste residue, reduces the discharge of sulfide, reduces the usage amount of filter cloth, has saved SO2Raw material and labour cost;Improve environmental pollution, it is energy-saving, alleviate staff labor intensity;So that economic benefit gets a promotion.

Description

A kind of technique for treating industrial wastewater
Technical field
The invention belongs to technical field of waste water processing, specifically, being related to a kind of technique for treating industrial wastewater.
Background technique
Zinc hydrometallurgy can give off a large amount of washes when smelting.The acid relatively strong, heavy metal ion of washes compared with More, especially lead, zinc, cadmium plasma severely exceed.Smelting most important pollutant in factory production waste water is acid.The prior art In, commonly used treatment process is legal in using handled, comprising: neutralizer is added in industrial wastewater, will give up The pH of water is adjusted to 6-8, is subsequently added into collecting agent vulcanized sodium to remove the metallic elements such as zinc, lead, cadmium, then passes through precipitating, filtering Means are isolated.Legal progress wastewater treatment has the disadvantage in that sulphur is easily exceeded in water after processing, has black in Color attachment is attached in chute, it is difficult to be cleared up;Sulfur-bearing is high in the waste residue that water after processing generates, large viscosity, difficult filters pressing, pressure The filter cloth of filter consumes high;The hydrogen sulfide gas that charging reaction generates is easy to make operative employee's poisoning and pollution environment.
Summary of the invention
For deficiency above-mentioned in the prior art, the object of the present invention is to provide a kind of technique for treating industrial wastewater; The technique for treating industrial wastewater reduces the sulfur content in waste residue, reduces the discharge of sulfide, reduces the usage amount of filter cloth, Sulfur dioxide (SO is saved2) raw material and labour cost;Improve environmental pollution, it is energy-saving, alleviate staff labor intensity;Make Economic benefit is obtained to be significantly improved.
In order to achieve the above object, the solution that the present invention uses is:
A kind of technique for treating industrial wastewater, comprising: waste water is successively anti-through conditioning tank, neutralization pond, aeration oxidation pool, coagulation Ying Chi, sedimentation basin, filtering ponds, pH readjustment discharge behind pond, it is characterised in that: the lime tune after pulp is added in coagulation reaction tank The pH for saving reaction solution is 7-10.
A kind of beneficial effect of technique for treating industrial wastewater provided by the invention is:
This kind of technique for treating industrial wastewater provided by the invention is led to by generating the compound of indissoluble under alkaline condition PH value is overregulated to keep the pollutant load for being difficult to react in industrial wastewater up to standard, so that treated, water reaches three classes surface water Discharge standard.The technique for treating industrial wastewater reduces the sulfur content in waste residue, reduces the discharge of sulfide, reduces filter The usage amount of cloth, has saved SO2Raw material and labour cost;Improve environmental pollution, it is energy-saving, alleviate staff labor intensity; So that economic benefit gets a promotion.
Specific embodiment
It in order to make the object, technical scheme and advantages of the embodiment of the invention clearer, below will be in the embodiment of the present invention Technical solution be clearly and completely described.The person that is not specified actual conditions in embodiment, according to normal conditions or manufacturer builds The condition of view carries out.Reagents or instruments used without specified manufacturer is the conventional production that can be obtained by commercially available purchase Product.
A kind of technique for treating industrial wastewater provided in an embodiment of the present invention is specifically described below.
A kind of technique for treating industrial wastewater, comprising the following steps: by waste water successively through conditioning tank, neutralization pond, aerating oxidation Pond, coagulation reaction tank, sedimentation basin, filtering ponds, pH readjustment discharge behind pond, it is characterised in that: pulp is added in coagulation reaction tank The pH that lime afterwards adjusts reaction solution is 7-10.
Wherein, paddle enables to the purity of lime higher, reacts more abundant.It should be noted that in the present embodiment In, it is further 80 mesh that the partial size of lime, which is 70-90 mesh, so that reaction is more abundant.
In the present embodiment, further, when containing zinc in reaction solution, the pH for adjusting reaction solution is 7-8;Work as reaction solution In contain cadmium when, further, adjust reaction solution pH be 8-9.Inventors have found that due to the metal ions such as zinc, cadmium be difficult to Hydroxyl, which combines, generates precipitating, it is therefore desirable to be properly increased and be reacted according to the combination complexity of metal ion and hydroxide ion The content of hydroxide ion in liquid, sufficiently to remove metal ion.
It should be noted that pH readjustment pond in need to adjust filtered fluid to pH be 6-9, due to the pH in coagulation reaction tank Value it is higher, reaction solution in alkalinity, precipitate filtered filtered fluid be also in alkalinity, therefore, it is necessary to filtered fluid carry out acidity Being adjusted to pH is 6-9, to meet the discharge standard of three classes surface water.In the present embodiment, to avoid introducing new impurity, into one Step ground, the acidity adjustment of liquid is filtered using sulfuric acid.
Feature and performance of the invention are described in further detail with reference to embodiments.
Embodiment 1
Present embodiments provide a kind of technique for treating industrial wastewater, comprising: by waste water successively through conditioning tank, neutralization pond, exposure Gas oxidation pond, coagulation reaction tank, sedimentation basin, filtering ponds, pH readjustment discharge behind pond: where detect and contain zinc in waste water, mixed Partial size after pulp is added in solidifying reaction tank is that the pH of the lime adjusting reaction solution of 70 mesh is 7;Sulfuric acid is used in pH readjustment pond Adjust filtered fluid to pH be 6.
Embodiment 2
Present embodiments provide a kind of technique for treating industrial wastewater, comprising: by waste water successively through conditioning tank, neutralization pond, exposure Gas oxidation pond, coagulation reaction tank, sedimentation basin, filtering ponds, pH readjustment discharge behind pond: where detect and contain zinc in waste water, mixed Partial size after pulp is added in solidifying reaction tank is that the pH of the lime adjusting reaction solution of 90 mesh is 8;Sulfuric acid is used in pH readjustment pond Adjust filtered fluid to pH be 9.
Embodiment 3
Present embodiments provide a kind of technique for treating industrial wastewater, comprising: by waste water successively through conditioning tank, neutralization pond, exposure Gas oxidation pond, coagulation reaction tank, sedimentation basin, filtering ponds, pH readjustment discharge behind pond: where detect and contain cadmium in waste water, mixed Partial size after pulp is added in solidifying reaction tank is that the pH of the lime adjusting reaction solution of 80 mesh is 9;Sulfuric acid is used in pH readjustment pond Adjust filtered fluid to pH be 7.
Embodiment 4
Present embodiments provide a kind of technique for treating industrial wastewater, comprising: by waste water successively through conditioning tank, neutralization pond, exposure Gas oxidation pond, coagulation reaction tank, sedimentation basin, filtering ponds, pH readjustment discharge behind pond: where and it detects and contains zinc and cadmium in waste water, Partial size after pulp is added in coagulation reaction tank is that the pH of the lime adjusting reaction solution of 80 mesh is 10;It is used in pH readjustment pond Sulfuric acid adjust filtered fluid to pH be 8.
Comparative example 1
This comparative example provides a kind of technique for treating industrial wastewater, comprising: by waste water successively through conditioning tank, neutralization pond, exposure Gas oxidation pond, coagulation reaction tank, sedimentation basin, filtering ponds, pH readjustment discharge behind pond: where and it detects and contains zinc and cadmium in waste water, Partial size after pulp is added in coagulation reaction tank is that the pH of the lime adjusting reaction solution of 100 mesh is 10;It is adopted in pH readjustment pond It is 8 with sulfuric acid adjusting filtered fluid to pH.
Comparative example 2
This comparative example provides a kind of technique for treating industrial wastewater, comprising: by waste water successively through conditioning tank, neutralization pond, exposure Gas oxidation pond, coagulation reaction tank, sedimentation basin, filtering ponds, pH readjustment discharge behind pond: where and it detects and contains zinc and cadmium in waste water, It is 7 that common lime is added in coagulation reaction tank and adjusts the pH of reaction solution.
Comparative example 3
This comparative example provides a kind of technique for treating industrial wastewater, comprising: by waste water successively through conditioning tank, neutralization pond, exposure Gas oxidation pond, coagulation reaction tank, sedimentation basin, filtering ponds, pH readjustment discharge behind pond: where detect and contain cadmium in waste water, mixed Partial size after pulp is added in solidifying reaction tank is that the pH of the lime adjusting reaction solution of 80 mesh is 7;Sulfuric acid is used in pH readjustment pond Adjust filtered fluid to pH be 8.
Experimental example 1
Experimental method: experimental group 1-7 is set by embodiment 1-4 and comparative example 1-3, detects and crosses filter residue in embodiment 1-7 In sulfur content, the results are shown in Table 1:
Table 1
Group number 1 2 3 4 5 6 7
Sulfur content (%) 0.32 0.33 0.28 0.29 0.8 96.3 1.2
Containing in filter residue the result shows that, is crossed using technique for treating industrial wastewater gained provided in an embodiment of the present invention by table 1 Sulphur can be down to 0.3% or so, have dropped about 96% than original process.
Experimental example 2
Experimental method: setting experimental group 1-7 for embodiment 1-4 and comparative example 1-3, and it is real that routine techniques detection is respectively adopted The content for applying in a 1-7 zinc and cadmium in waste water and filtered fluid before and after the processing, the results are shown in Table shown in 2:
Table 2
From the data in table 2, it can be seen that using in filtered fluid obtained by technique for treating industrial wastewater provided in an embodiment of the present invention Zinc and cadmium content significantly reduce.
In conclusion using technique for treating industrial wastewater provided by the invention;The technique for treating industrial wastewater reduces useless Sulfur content in slag reduces the discharge of sulfide;The usage amount for reducing filter cloth, has saved SO2Raw material and labour cost;Improve Environmental pollution, it is energy-saving, alleviate staff labor intensity;So that economic benefit is significantly improved.
The foregoing is only a preferred embodiment of the present invention, is not intended to restrict the invention, for the skill of this field For art personnel, the invention may be variously modified and varied.All within the spirits and principles of the present invention, made any to repair Change, equivalent replacement, improvement etc., should all be included in the protection scope of the present invention.

Claims (7)

1. a kind of technique for treating industrial wastewater, comprising: by waste water successively through conditioning tank, neutralization pond, aeration oxidation pool, coagulating Pond, sedimentation basin, filtering ponds, pH readjustment discharge behind pond, it is characterised in that: the lime after pulp is added in the coagulation reaction tank The pH for adjusting reaction solution is 7-10.
2. technique for treating industrial wastewater according to claim 1, it is characterised in that: the partial size of the lime is 70-90 mesh.
3. technique for treating industrial wastewater according to claim 2, it is characterised in that: the partial size of the lime is 80 mesh.
4. technique for treating industrial wastewater according to claim 2, it is characterised in that: when containing zinc in the reaction solution, The pH for adjusting the reaction solution is 7-8.
5. technique for treating industrial wastewater according to claim 2, it is characterised in that: when containing cadmium in the reaction solution, The pH for adjusting the reaction solution is 8-9.
6. technique for treating industrial wastewater according to claim 1, it is characterised in that: adjust filtering in pH readjustment pond Liquid to pH be 6-9.
7. technique for treating industrial wastewater according to claim 4, it is characterised in that: carry out the filtered fluid using sulfuric acid Acidity adjustment.
CN201811033880.7A 2018-09-05 2018-09-05 A kind of technique for treating industrial wastewater Pending CN108947022A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201811033880.7A CN108947022A (en) 2018-09-05 2018-09-05 A kind of technique for treating industrial wastewater

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201811033880.7A CN108947022A (en) 2018-09-05 2018-09-05 A kind of technique for treating industrial wastewater

Publications (1)

Publication Number Publication Date
CN108947022A true CN108947022A (en) 2018-12-07

Family

ID=64475951

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201811033880.7A Pending CN108947022A (en) 2018-09-05 2018-09-05 A kind of technique for treating industrial wastewater

Country Status (1)

Country Link
CN (1) CN108947022A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN115070352A (en) * 2022-06-16 2022-09-20 江苏伟业铝材有限公司 Aluminum profile machining process

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5370800A (en) * 1993-05-25 1994-12-06 Stevenson; Sanford M. Method for removing metal compounds from waste water
WO2007098592A1 (en) * 2006-03-01 2007-09-07 Noram Engineering And Constructors Ltd. Method for treating acidic waters using recycled acidic and basic sludges
CN101805084A (en) * 2010-03-29 2010-08-18 中钢集团马鞍山矿山研究院有限公司 Process for treating mine wastewater containing sulfur minerals, As, Pb and Cd
CN102107963A (en) * 2010-12-30 2011-06-29 天津市环境保护科学研究院 Method for treating acid-washing wastewater and metallic ions in iron and steel industry
CN105621744A (en) * 2016-03-07 2016-06-01 山东国信环境系统股份有限公司 Copper ore acid wastewater treatment and recovery device and method

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5370800A (en) * 1993-05-25 1994-12-06 Stevenson; Sanford M. Method for removing metal compounds from waste water
WO2007098592A1 (en) * 2006-03-01 2007-09-07 Noram Engineering And Constructors Ltd. Method for treating acidic waters using recycled acidic and basic sludges
CN101805084A (en) * 2010-03-29 2010-08-18 中钢集团马鞍山矿山研究院有限公司 Process for treating mine wastewater containing sulfur minerals, As, Pb and Cd
CN102107963A (en) * 2010-12-30 2011-06-29 天津市环境保护科学研究院 Method for treating acid-washing wastewater and metallic ions in iron and steel industry
CN105621744A (en) * 2016-03-07 2016-06-01 山东国信环境系统股份有限公司 Copper ore acid wastewater treatment and recovery device and method

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN115070352A (en) * 2022-06-16 2022-09-20 江苏伟业铝材有限公司 Aluminum profile machining process

Similar Documents

Publication Publication Date Title
CN103922517B (en) A kind of method containing the process of heavy metal sulfuric acid wastewater containing and recycle
CN103030233A (en) Treatment method for high-concentration arsenic waste water
CN108383272A (en) A kind of sludge recovery treatment method of waste acid that wire rope factory generates
CN105000713A (en) Desulfurization wastewater treatment system and desulfurization wastewater treatment method
CN111499029B (en) Two-stage method for quickly removing copper ions in copper ammonia complexing wastewater
CN106396163B (en) A kind of method of rare-earth smelting amine wastewater of sulphuric acid comprehensive treatment reuse
CN102311181A (en) Embrane method and acidifying combined treatment reuse cyanide barren solution technology and method
CN108975570A (en) A kind of device and method handling industrially desulfurized waste water using stack gases
CN106219807B (en) Integrated conduct method of the mine low concentration containing Effluent of cuprous cyanide
CN110577307A (en) Efficient low-cost treatment method for tungsten polymetallic ore beneficiation wastewater
CN104326620A (en) Tannery wastewater treatment method
CN108947022A (en) A kind of technique for treating industrial wastewater
JPH11314094A (en) Method for treating drainage containing arsenic and other heavy metals
CN111675295A (en) Preparation method of efficient flocculant for purifying acid mine wastewater
CA2647965C (en) Nickel sulphide precipitation processes
CN110818123B (en) Treatment method of trivalent chromium plating waste water
CN112759195A (en) Treatment device and treatment process for high ammonia nitrogen wastewater
CN104261585A (en) Method for treating metallurgy wastewater and recycling resources
JP3945216B2 (en) Waste acid gypsum manufacturing method
CN104986897B (en) Method for recovering valuable metals in wastewater
CN107487910B (en) Combined process treatment method for lead-zinc smelting industrial wastewater
CN110759511B (en) Treatment method of gun black tin-nickel alloy electroplating wastewater
CN102826677A (en) Full-cycling technology for vanadium smelting wastewater
CN110759441B (en) Treatment method of trivalent chromium passivation wastewater containing aminoacetic acid coordination agent
CN207192971U (en) Suitable for the carbon dioxide deliming system of liquid after the processing of gypsum neutralization step

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
RJ01 Rejection of invention patent application after publication

Application publication date: 20181207

RJ01 Rejection of invention patent application after publication