CN102653437B - Method for treating yellow sludge obtained in neutralization of steel pickling waste water lime - Google Patents

Method for treating yellow sludge obtained in neutralization of steel pickling waste water lime Download PDF

Info

Publication number
CN102653437B
CN102653437B CN 201110446622 CN201110446622A CN102653437B CN 102653437 B CN102653437 B CN 102653437B CN 201110446622 CN201110446622 CN 201110446622 CN 201110446622 A CN201110446622 A CN 201110446622A CN 102653437 B CN102653437 B CN 102653437B
Authority
CN
China
Prior art keywords
value
mud
lime
aeration
heating bath
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.)
Active
Application number
CN 201110446622
Other languages
Chinese (zh)
Other versions
CN102653437A (en
Inventor
卢玉柱
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.)
Lu Shukun
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 CN 201110446622 priority Critical patent/CN102653437B/en
Publication of CN102653437A publication Critical patent/CN102653437A/en
Application granted granted Critical
Publication of CN102653437B publication Critical patent/CN102653437B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Landscapes

  • Removal Of Specific Substances (AREA)
  • Treatment Of Sludge (AREA)

Abstract

The invention relates to a method for treating yellow sludge obtained in neutralization of steel pickling waste water lime and belongs to the technical field of waste water treatment. The method for treating the yellow sludge obtained in neutralization of the steel pickling waste water lime comprises the following steps of: adding the filtered yellow sludge into a reaction tank by use of a sludge pump; adding iron acid water which comes from a pickling workshop and has the PH value of less than 2 into the yellow sludge, carrying out aeration, adjusting the PH value to be 4.5-5.5 and then filtering again; conveying yellowish-brown oxidized sludge into a heating bath, carrying out aeration, and stirring for oxidization; adjusting the PH value to be 10.5-11.5 by lime liquor, then heating to 100-130 DEG C by steam, and carrying out heat preservation for 25-50 minutes; adding sewage which is filtered again and has the PH value of 4.5-5.5, adjusting the PH value to be 6.5-7.5, and finishing the reaction; and finally, cooling to 45-55 DEG C, and filtering to obtain black magnetic iron-containing sludge. The method has the advantages of being simple in technology, convenient in operation, easy to control, low in processing cost and high in treatment efficiency, avoiding environmental pollution, changing a pollution source into a renewable resource, and the like.

Description

The treatment process of the yellow mud in the steel pickling waste liquor lime and back
Technical field
The invention belongs to the steel pickling waste liquor processing technology field, particularly relate in a kind of steel pickling waste liquor lime and the treatment process of back yellow mud.
Background technology
At present, produce a large amount of poaching wastewaters in the iron and steel processing enterprise acid cleaning process, the main component of waste water is the aqueous solution that contains FeCl2 or the FeS04 of sour pH value≤2, oxidation by air forms the iron protoxide red precipitate of trivalent when the air of waste water and occurring in nature contacts, and causes the muddy polluted source of water.
Pickling iron and steel enterprise pickling waste waters generally adopts cheap basic treatment agent lime (calcium oxide) that acid-bearing wastewater is carried out neutralizing treatment in sewage treatment process, treatment process is lime to be blunged dissolve in the back formation calcium hydroxide adding acid-bearing wastewater, make neutrality that the acid waste water pH value reaches 6-8 by filter and press filtration after sewage again through pipe network enter advanced treatment and reclamation or discharging equation be FeCl2+Ca (OH) 2=Fe (OH) 2 ↓+CaClOOH do not dissolve in the neutralization reaction process fully because the solubleness of calcium oxide in water is very little, therefore produced that a large amount of oxide compounds can not be dissolved in the water and coated by ferrous ion and to form Fe (OH) 3a-FeOOH, the industrial sludge that mud mixture produces after press filtration becomes the tawny pollutent, in the middle of depositing and transporting, can produce polluting the second time of environment, do not have because the iron content magnitude is low utility value at present existing treating method be to handle the back landfill by the producer that has qualification to handle, brought serious economical load and to the pollution of environment to enterprise.
Summary of the invention
The technical problem of the present invention for existing in the solution known technology, and provide in a kind of steel pickling waste liquor lime and the treatment process of back yellow mud.
The purpose of this invention is to provide that a kind of to have technology simple, easy to operate, control easily, stable performance, process is reliable, the processing efficiency height has reached the pollution that the purpose that turns waste into wealth has been avoided environment, source of pollution has been become in the steel pickling waste liquor lime of characteristics such as renewable resource and the treatment process of the yellow mud in back.
The present invention is on the basis of the original sewage disposal of pickling iron and steel enterprise, utilize after the neutralizing treatment the tawny oxidized sludge with contain the iron waste water synthetic high iron content black magnetic breeze raw material of heating, recovery technology is simple, easy to operate, environment is not produced pollution, realized recycling economy at environment protection treating, the change source of pollution are renewable resource, for smelting iron and steel provides main raw material.
Treating processes of the present invention: will be lower than 2 Fe-laden acid wastewater from pickling workshop pH value and squeeze in the reaction tank with acid proof pump, add lime and make its acid-base neutralisation, simultaneously to carrying out aeration agitation in the reaction tank, regulate pH value=8, aeration oxidation 1 hour, the sewage after will neutralizing then filters with filter.Tawny oxidized sludge after the filtration is put in the reaction tank again with pump, adds to be lower than 2 iron content sour water from pickling workshop pH value, and regulate pH value and equal 5, aeration oxidation and then filtration, filtered sewage turns back to reaction tank and waits for next step processing.Tawny oxidized sludge after the filtration (filter cake is put in the heating bath also will (to contain crystal water 60%) after the available pressure filter press filtration) joins in the heating bath with slush pump, add in the reaction tank iron waste water that contains that pH value after filtering equals 5 in the heating bath according to the concentration of tawny oxidized sludge, open air aeration heating bath is carried out the oxidation stirring, regulating PH in the heating bath with lime liquid again equals 12 and treats that mud stops aeration agitation when being stirred to the pasty state of thickness with air aeration, the unlatching steam valve is heated, close most of steam when spending and keep micro-steam by carrying out insulation reaction 30 minutes when the mud temperature reaches 100, observing the mud color is that chocolate can not appear in pure black, and the detection iron-holder reaches 50% and is reaction end.The steam off valve stops heating, with water pump PH in the reaction tank is equaled 5 the iron waste water that contains and joins in the heating bath and to regulate pH value and equal reaction in 7 o'clock and finish.Opening the air aeration valve carries out aeration to heating bath and is cooled to 50 and squeezes into the water discharging filter cake that plate-and-frame filter press carries out after the press filtration press filtration with surge pump when spending and obtain black magnetic Z 250 mud.
The technical scheme that the treatment process of the yellow mud in the steel pickling waste liquor lime of the present invention and back is taked for the problem that solves the prior art existence is:
The treatment process of the yellow mud in the steel pickling waste liquor lime and back, the Fe-laden acid wastewater in pickling workshop is squeezed in the reaction tank with acid proof pump, add lime and make its acid-base neutralisation, through aeration, accent PH, filtration treatment, be characterized in: the Fe-laden acid wastewater pH value of regulating the pickling workshop with yellow mud is 4.5-5.5, aeration oxidation and then filtration; Tawny oxidized sludge after the filtration is transported in the heating bath, carries out the aeration agitation oxidation, and regulating pH value with liquor calcis is 10.5-11.5, heats to 100-130 ℃ of mud temperature with steam then, is incubated 25-50 minute; The sewage that adds pH value after filtration and be 4.5-5.5 cools off in heating bath, regulates pH value and equals 6.5-7.5, and reaction finishes; Be cooled to 45-55 ℃, filter and obtain the black magnetic iron containing sludge.
The treatment process of the yellow mud in the steel pickling waste liquor lime of the present invention and back can also adopt following technical measures:
The treatment process of the yellow mud in the described steel pickling waste liquor lime and back, be characterized in: the tawny oxidized sludge volume of water content after the filtration is 50%-85%.
The treatment process of the yellow mud in the described steel pickling waste liquor lime and back, be characterized in: be incubated after 25-50 minute, the mud color is black, and iron level reaches at 50% o'clock, adding when filtering again pH value be that the sewage of 4.5-5.5 is in heating bath.
The treatment process of the yellow mud in the described steel pickling waste liquor lime and back is characterized in: after regulating pH value and be 10.5-11.5 with liquor calcis, treat to stop aeration agitation when mud is stirred to the pasty state of thickness with air aeration, heat with steam then.
The treatment process of the yellow mud in the described steel pickling waste liquor lime and back, be characterized in: after reaction finishes, utilize pH value after filtration to cool off in heating bath for the sewage of 4.5-5.5, open the air aeration valve simultaneously heating bath is carried out the aeration cooling, squeeze into plate-and-frame filter press with surge pump when being cooled to 45-55 ℃ and carry out press filtration, filter cake obtains black magnetic Z 250 mud.
The treatment process of the yellow mud in the described steel pickling waste liquor lime and back, be characterized in: filter cake obtains the black magnetic Z 250 mud that iron level is 50%-60%.
Advantage and positively effect that the present invention has are:
The treatment process of the yellow mud in the steel pickling waste liquor lime and back is owing to adopted brand-new technology scheme of the present invention, compared with prior art, it is simple that the treatment process of the yellow mud in the steel pickling waste liquor lime and back has technology, easy to operate, control is easy, stable performance, process is reliable, the processing efficiency height has reached the pollution that the purpose that turns waste into wealth has been avoided environment, source of pollution has been become advantages such as renewable resource.
Description of drawings
Fig. 1 is in the steel pickling waste liquor lime of the present invention and the treatment process process flow sheet of the yellow mud in back;
Fig. 2 is process innovation part process flow sheet of the present invention.
Embodiment
For further understanding technology contents of the present invention, characteristics and effect, exemplify following examples now, and be described with reference to the accompanying drawings as follows:
Consult accompanying drawing 1 and Fig. 2.
Embodiment 1
The treatment process of the yellow mud in the steel pickling waste liquor lime and back, the Fe-laden acid wastewater in pickling workshop is squeezed in the reaction tank with acid proof pump, adds lime and makes its acid-base neutralisation, through aeration, accent PH, filtration treatment.The Fe-laden acid wastewater pH value of regulating the pickling workshop with filter cake is 4.5-5.5, aeration oxidation and then filtration; Filtration back water-content is that the tawny oxidized sludge of 50%-85% is transported in the heating bath, carry out the aeration agitation oxidation, regulating pH value with liquor calcis is 10.5-11.5, treat that mud stops aeration agitation when being stirred to the pasty state of thickness with air aeration, heat to 100-130 ℃ of mud temperature with steam then, be incubated 25-50 minute; The mud color is black, and ferrous components content reaches at 50% o'clock, adds that to filter pH value again be that the sewage of 4.5-5.5 cools off in heating bath, regulates pH value simultaneously and equals 6.5-7.5, and reaction finishes; Open the air aeration valve heating bath is carried out the aeration cooling, squeeze into plate-and-frame filter press with surge pump when being cooled to 45-55 ℃ and carry out press filtration, filter cake obtains the black magnetic Z 250 mud that iron level is 50%-60%.
The concrete operations implementation process of present embodiment:
The treatment process of the yellow mud in the steel pickling waste liquor lime and back, to be lower than 2 Fe-laden acid wastewater from pickling workshop pH value and squeeze in the reaction tank with acid proof pump, and add lime and make its acid-base neutralisation, stir carrying out the aeration oxidation in the reaction tank simultaneously, regulate pH value=8, aeration oxidation 1 hour.Sewage after will neutralizing then filters with filter, tawny oxidized sludge after the filtration is put in the reaction tank with pump again, adding is lower than 2 iron content sour water from pickling workshop pH value, regulate pH value and equal 5, aeration oxidation and then filtration, filtered sewage turn back to reaction tank and wait for next step processing.
Tawny oxidized sludge after the filtration (filter cake is put in the heating bath also will (to contain crystal water 60%) after the available pressure filter press filtration) joins in the heating bath with sludge pump, concentration according to the tawny oxidized sludge adds through filtering the iron waste water that contains that the back pH value equals 5 last time in heating bath, open air aeration heating bath is stirred oxidation, the PH that regulates in the heating bath with lime liquid equals 12 again, treat that mud stops aeration agitation when being stirred to the pasty state of thickness with air aeration, the unlatching steam valve is heated, when the mud temperature reaches 100 ℃, close most of steam and keep micro-steam by carrying out insulation reaction 30 minutes, observing the mud color is that chocolate can not appear in pure black, and detection mud iron-holder reaches 50% and is reaction end.The steam off valve stops heating, with water pump PH in the reaction tank is equaled 5 the iron waste water that contains and joins to cool off in the heating bath and regulate pH value simultaneously and equal reaction in 7 o'clock and finish.Open the air aeration valve heating bath is carried out the aeration cooling, when being cooled to 50 ℃, squeeze into plate-and-frame filter press with surge pump and carry out press filtration, water discharging filter cake after the press filtration obtains the iron mud of iron content 50%, the raw material that is used for smelting iron and steel, stopped yellow mud after the sewage disposal to the pollution of environment and be recovered to the higher-grade iron containing sludge, source of pollution have been become renewable resource.
Embodiment 2
The treatment process of the yellow mud in the steel pickling waste liquor lime and back, technological process is with embodiment 1, wherein, the pickling mud of moisture 85% after 10 cubes of filtrations is joined in the heating bath with sludge pump, adjust pH value with liquor calcis and equal 12, open steam valve the mud in the heating bath is heated 2.5 hours vapor pressure 0.2 MPas, when the mud temperature reaches more than 100 ℃, the steam off valve adds the iron waste water that contains of PH=5 again in the heating bath, regulates PH=7 in the heating bath.The sewage gas that to heat in the pond with the air stripping tube is mentioned the mud storage pool then, joins with pneumatic diaphragm pump and carries out press filtration in the plate-and-frame filter press.Sewage discharge after the press filtration, filter cake obtains the magnetic ferroferric oxide mud of 2 cubes of black moisture 60% after the press filtration.
Present embodiment has described positively effect and advantage.

Claims (6)

  1. In the steel pickling waste liquor lime and the back yellow mud treatment process, the Fe-laden acid wastewater in pickling workshop is squeezed in the reaction tank with acid proof pump, add lime and make its acid-base neutralisation, through aeration, accent PH, filtration treatment, it is characterized in that: the Fe-laden acid wastewater pH value of regulating the pickling workshop with yellow mud is 4.5-5.5, aeration oxidation and then filtration; Tawny oxidized sludge after the filtration is transported in the heating bath, add the iron waste water that contains that filtration back pH value equals 5 in heating bath, carry out the aeration agitation oxidation, regulating pH value with liquor calcis is 10.5-11.5, heat to 100-130 ℃ of mud temperature with steam then, be incubated 25-50 minute; The adding pH value is that the iron content sewage of 4.5-5.5 cools off in heating bath, regulates the pH value and equals 6.5-7.5, and reaction finishes; Be cooled to 45-55 ℃, filter and obtain the black magnetic iron containing sludge.
  2. 2. according to the treatment process of the yellow mud in the described steel pickling waste liquor lime of claim 1 and back, it is characterized in that: the tawny oxidized sludge volume of water content after the filtration is 50%-85%.
  3. According in the described steel pickling waste liquor lime of claim 1 and the back yellow mud treatment process, it is characterized in that: be incubated after 25-50 minute, the mud color is black, and iron level reaches at 50% o'clock, and the sewage that adds pH value when filtering again and be 4.5-5.5 carries out hypothermic response in heating bath.
  4. According in claim 1, the 2 or 3 described steel pickling waste liquor lime and the back yellow mud treatment process, it is characterized in that: after being 10.5-11.5 with liquor calcis adjusting pH value, treat to stop aeration agitation when mud is stirred to the pasty state of thickness with air aeration, heat with steam then.
  5. According in claim 1, the 2 or 3 described steel pickling waste liquor lime and the back yellow mud treatment process, it is characterized in that: after reaction finishes, be that the iron content sewage of 4.5-5.5 is lowered the temperature with pH value in the heating bath, open the air aeration valve simultaneously heating bath is carried out the aeration cooling, squeeze into plate-and-frame filter press with surge pump when being cooled to 45-55 ℃ and carry out press filtration, filter cake obtains black magnetic Z 250 mud.
  6. 6. according to the treatment process of the yellow mud in the described steel pickling waste liquor lime of claim 5 and back, it is characterized in that: filter cake obtains the black magnetic Z 250 mud that iron level is 50%-60%.
CN 201110446622 2011-09-20 2011-12-28 Method for treating yellow sludge obtained in neutralization of steel pickling waste water lime Active CN102653437B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 201110446622 CN102653437B (en) 2011-09-20 2011-12-28 Method for treating yellow sludge obtained in neutralization of steel pickling waste water lime

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
CN201110278314.4 2011-09-20
CN2011102783144A CN102358648A (en) 2011-09-20 2011-09-20 Technology for recycling of sludge obtained after neutralizing treatment of steel and iron pickling wastewater and recycling ferroferric oxide
CN 201110446622 CN102653437B (en) 2011-09-20 2011-12-28 Method for treating yellow sludge obtained in neutralization of steel pickling waste water lime

Publications (2)

Publication Number Publication Date
CN102653437A CN102653437A (en) 2012-09-05
CN102653437B true CN102653437B (en) 2013-07-17

Family

ID=45584035

Family Applications (2)

Application Number Title Priority Date Filing Date
CN2011102783144A Pending CN102358648A (en) 2011-09-20 2011-09-20 Technology for recycling of sludge obtained after neutralizing treatment of steel and iron pickling wastewater and recycling ferroferric oxide
CN 201110446622 Active CN102653437B (en) 2011-09-20 2011-12-28 Method for treating yellow sludge obtained in neutralization of steel pickling waste water lime

Family Applications Before (1)

Application Number Title Priority Date Filing Date
CN2011102783144A Pending CN102358648A (en) 2011-09-20 2011-09-20 Technology for recycling of sludge obtained after neutralizing treatment of steel and iron pickling wastewater and recycling ferroferric oxide

Country Status (1)

Country Link
CN (2) CN102358648A (en)

Families Citing this family (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103408158B (en) * 2013-07-05 2015-01-14 无锡市新都环保科技有限公司 Acidic iron-containing wastewater recycling system and method for carrying out in situ modification by system
CN103553258B (en) * 2013-11-13 2014-08-06 卢玉柱 Safe recycling treatment method of waste iron/steel pickling acid
CN103553146A (en) * 2013-11-13 2014-02-05 卢玉柱 Method for preparing magnetite powder by using wasted electric lime size
CN103922516B (en) * 2014-05-07 2016-05-18 太仓东能环保设备有限公司 A kind of stainless steel acid cleaning waste water treating apparatus
CN103964660B (en) * 2014-05-20 2016-01-06 钱占虎 The acid wastewater treatment of acid-base neutralisation precipitator method process iron content produces the recovery process of mud
CN104445436B (en) * 2014-12-04 2016-03-30 黑龙江大学 A kind of take copper water-supply pipe as the method that nano ferriferrous oxide prepared by raw material
CN104671290B (en) * 2015-03-20 2016-08-24 王浩 A kind of method utilizing pickling mud to prepare iron oxide red
CN105540937A (en) * 2016-02-04 2016-05-04 卢玉柱 Treatment method of steel processing waste dangerous chemicals and product calcium-base ferrous hydroxide thereof
CN105906174A (en) * 2016-05-04 2016-08-31 卢玉柱 Method for ferric hydroxide water purifier preparation with sludge after steel pickling waste water lime neutralization
CN106379976A (en) * 2016-08-30 2017-02-08 无锡市新都环保科技有限公司 Equipment and method for preparing water treatment agent through using acidic iron-containing wastewater
CN107200447A (en) * 2017-06-20 2017-09-26 天津丰源首创环保科技有限公司 A kind of pickling iron and steel sludge quickly improves the resource utilization method after iron-holder
GB2578645B (en) * 2018-11-02 2021-11-24 Darlow Lloyd & Sons Ltd Method and apparatus for treating waste material
CN109399887A (en) * 2018-12-07 2019-03-01 中国矿业大学(北京) A kind of steel rolling pickling waste water sludge recycling processing method
CN112573580A (en) * 2020-10-12 2021-03-30 江苏荣信环保科技有限公司 Recovery treatment process of ferric trichloride sludge on surface of metal product

Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP3069515B2 (en) * 1995-11-24 2000-07-24 新キャタピラー三菱株式会社 Electromagnetic proportional relief valve
CN1807263A (en) * 2006-02-21 2006-07-26 上海宝齐氧化铁有限公司 Method for producing iron oxide black using desilicified mud cake
CN1958462A (en) * 2006-11-09 2007-05-09 武汉理工大学 Method for preparing potassium ferrate by using waste liquid from acid washing steel
JP2008188479A (en) * 2007-01-31 2008-08-21 Nisshin Steel Co Ltd Method and apparatus for treating waste acid liquid
CN201195751Y (en) * 2008-05-30 2009-02-18 陈跃星 Processing and recycling equipment for acid pickle of acid washing rolled steel
CN101649130A (en) * 2009-09-03 2010-02-17 浙江大学 Method for preparing ferric oxide yellow pigment by waste iron hydrochloric acid lotion
CN101798120A (en) * 2010-02-02 2010-08-11 东南大学 Method for producing nanometer iron oxide red by utilizing ferrous chloride recovered from waste acid washing liquor
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

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH02102787A (en) * 1988-10-13 1990-04-16 Sumitomo Metal Ind Ltd Treatment of waste pickling liquid
JPH085676B2 (en) * 1989-08-09 1996-01-24 株式会社鐵原 A method of recovering high-purity iron sulfate from the sulfuric acid pickling waste liquid of stainless steel

Patent Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP3069515B2 (en) * 1995-11-24 2000-07-24 新キャタピラー三菱株式会社 Electromagnetic proportional relief valve
CN1807263A (en) * 2006-02-21 2006-07-26 上海宝齐氧化铁有限公司 Method for producing iron oxide black using desilicified mud cake
CN1958462A (en) * 2006-11-09 2007-05-09 武汉理工大学 Method for preparing potassium ferrate by using waste liquid from acid washing steel
JP2008188479A (en) * 2007-01-31 2008-08-21 Nisshin Steel Co Ltd Method and apparatus for treating waste acid liquid
CN201195751Y (en) * 2008-05-30 2009-02-18 陈跃星 Processing and recycling equipment for acid pickle of acid washing rolled steel
CN101649130A (en) * 2009-09-03 2010-02-17 浙江大学 Method for preparing ferric oxide yellow pigment by waste iron hydrochloric acid lotion
CN101798120A (en) * 2010-02-02 2010-08-11 东南大学 Method for producing nanometer iron oxide red by utilizing ferrous chloride recovered from waste acid washing liquor
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

Non-Patent Citations (3)

* Cited by examiner, † Cited by third party
Title
《利用钢铁酸洗废液制备高档级氧化铁黑》;崔辰霞;《河北化工》;20101130;第33卷(第11期);37-38 *
崔辰霞.《利用钢铁酸洗废液制备高档级氧化铁黑》.《河北化工》.2010,第33卷(第11期),37-38.
黄万抚,何善媛.钢铁酸洗废水处理与回收利用.《冶金丛刊》.2005,(第5期),33-39. *

Also Published As

Publication number Publication date
CN102358648A (en) 2012-02-22
CN102653437A (en) 2012-09-05

Similar Documents

Publication Publication Date Title
CN102653437B (en) Method for treating yellow sludge obtained in neutralization of steel pickling waste water lime
CN104310647B (en) Recycling method for treating stainless steel pickling acid pickle and wastewater
CN103408158B (en) Acidic iron-containing wastewater recycling system and method for carrying out in situ modification by system
CN111410345A (en) Method and system for treating comprehensive wastewater generated by anodic oxidation process
CN104909511A (en) Coating wastewater treatment method
CN104118956A (en) Method for treating sewage
CN106495215B (en) A kind of method that magnesium arsenate is produced containing arsenic waste solution
CN103626322A (en) Double-alkali neutralization treatment method of heavy metal-containing acidic wastewater
CN102887575B (en) Technology for recycling recovery of waste sulfuric acid
CN102616979B (en) Treatment method for surface treatment liquid wastewater of metal processing
CN102936074A (en) Pretreatment method of epoxy type plasticizer production wastewater
CN109721195B (en) Internal circulation catalytic oxidation method for waste water
CN104671507A (en) Comprehensive recycling method for trimanganese tetraoxide industrial wastewater
CN204224358U (en) Stainless-steel cold-rolling acid waste water treatment unit
CN104192971A (en) Method for treating industrial wastewater containing sulfuric acid
CN101665293A (en) Fractional precipitation treatment method of wastewater containing nonferrous metal of nickel, lead and cadmium
CN105254067A (en) Resource utilization method for advanced wastewater treatment Fenton method sludge
CN104926048A (en) Treatment method for waste water in coal chemical industry
CN104402145B (en) The waste water Han ferrous salt is utilized to prepare the production method of hydrated ferric oxide.
CN212403790U (en) System for treating comprehensive wastewater generated by anodic oxidation process
CN110655290B (en) Coal mine wastewater treatment method
CN108083529A (en) A kind of method that chromate waste water cooperates with processing with acid waste water
CN104310650A (en) Chromium-containing stainless steel cold-rolled wastewater treatment device and method
CN111186948A (en) Treatment method of electric desalting and decalcification wastewater
CN204224357U (en) Oil-containing stainless-steel cold-rolling wastewater treatment equipment

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C14 Grant of patent or utility model
GR01 Patent grant
TR01 Transfer of patent right
TR01 Transfer of patent right

Effective date of registration: 20170327

Address after: Caigongzhuang Daegu 301606 Tianjin city Jinghai County town east toll station

Patentee after: Tianjin Fengyuan Environmental Protection Technology Co., Ltd.

Address before: Daegu 301606 Tianjin city Jinghai County Town Village

Patentee before: Lu Yuzhu

TR01 Transfer of patent right
TR01 Transfer of patent right

Effective date of registration: 20220402

Address after: 301606 No. 39, row 3, zone 4, Datun village, Daqiuzhuang Town, Jinghai District, Tianjin

Patentee after: Lu Shukun

Address before: 301606 east of caigongzhuang toll station, Daqiuzhuang Town, Jinghai County, Tianjin

Patentee before: TIANJIN FENG YUAN ENVIRONMENTAL PROTECTION SCIENCE AND TECHNOLOGY CO.,LTD.