CN100556831C - The environmental protection of stainless steel acid-washing waste liquid utilizes method - Google Patents

The environmental protection of stainless steel acid-washing waste liquid utilizes method Download PDF

Info

Publication number
CN100556831C
CN100556831C CNB2007100241737A CN200710024173A CN100556831C CN 100556831 C CN100556831 C CN 100556831C CN B2007100241737 A CNB2007100241737 A CN B2007100241737A CN 200710024173 A CN200710024173 A CN 200710024173A CN 100556831 C CN100556831 C CN 100556831C
Authority
CN
China
Prior art keywords
waste liquid
stainless steel
filtrate
precipitation
environmental protection
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.)
Expired - Fee Related
Application number
CNB2007100241737A
Other languages
Chinese (zh)
Other versions
CN101100341A (en
Inventor
王水平
丁四宜
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.)
DING SIYI WANG SHUIPING
Original Assignee
DING SIYI WANG SHUIPING
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 DING SIYI WANG SHUIPING filed Critical DING SIYI WANG SHUIPING
Priority to CNB2007100241737A priority Critical patent/CN100556831C/en
Publication of CN101100341A publication Critical patent/CN101100341A/en
Application granted granted Critical
Publication of CN100556831C publication Critical patent/CN100556831C/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Abstract

The environmental protection of stainless steel acid-washing waste liquid utilizes method, waste liquid is dropped into feed ammonia in the reaction vessel, and reacted mixed solution filters; In the nickel ammine filtrate that produces, feed hydrogen sulfide, generate nickel sulphide precipitation and Neutral ammonium fluoride, ammonium nitrate mixed solution and free ammonia, the sedimentation and filtration washing is obtained the nickelous sulfide product; In filtrate, drop into calcium hydroxide and generate Calcium Fluoride (Fluorspan) precipitation and nitrocalcite.Advantage of the present invention is can the waste liquid environmental protection treatment is free from environmental pollution, but valuable ingredients in the efficient recovery waste liquid again has higher society and economy benefit.

Description

The environmental protection of stainless steel acid-washing waste liquid utilizes method
Technical field
The present invention relates to the environment-friendly treatment method of trade effluent, especially the treatment process of the spent pickle liquor that produces in the stainless steel product production process.
Background technology
Generally can use pickling in the stainless steel product production process, remove grey black etc. such as the tempering rear surface, after the pickling in the waste liquid except that containing a large amount of hydrofluoric acid, nitric acid, iron, chromium, also contain the higher nickel of a certain amount of utility value.Processing to stainless steel acid-washing waste liquid mainly is to adopt lime that heavy metal precipitation is got off simply at present, and ignored in the waste liquid ammonia nitrogen to the pollution of water body, thereby stainless steel acid-washing waste liquid is failed to obtain preferably environmental protection treatment and the severe contamination water body environment for a long time, the Taihu Lake blue-green algae wreaked havoc and caused Wuxi urbanite water consumption difficulty last stage, because of the stainless steel production in several small towns in Wuxi, the Changzhou in ring Taihu Lake very flourishing, as Wuxi Luo She town, Luoyang, Changzhou town etc., stainless steel acid-washing waste liquid also is one of pollution factor of wherein outbalance.
Goal of the invention
The objective of the invention is the spent pickle liquor that produces in the stainless steel product production, provide a kind of pollution-free and can also reclaim and wherein have the environmental protection of the stainless steel acid-washing waste liquid that utilizes the composition that is worth to utilize method.
The technical scheme that realizes above-mentioned purpose is as follows:
The environmental protection of stainless steel acid-washing waste liquid utilizes method, comprises the steps:
A drops into stainless steel acid-washing waste liquid and feeds ammonia in the reaction vessel, to pH value between 8-9, reacted mixed solution filtered obtains ferrochrome precipitation of hydroxide and nickel ammine filtrate;
B feeds hydrogen sulfide in the nickel ammine filtrate that preceding step produces, generate nickel sulphide precipitation and Neutral ammonium fluoride, ammonium nitrate mixed solution and free ammonia, and the sedimentation and filtration washing is obtained the nickelous sulfide product;
C, the b step is filtered out drop into calcium hydroxide in the filtrate of post precipitation and slowly be heated to the 60-80 degree, under this temperature, will distill out ammonia, and reaction generates Calcium Fluoride (Fluorspan) precipitation and nitrocalcite, dry after filtering again the Calcium Fluoride (Fluorspan) product, filtrate technology is routinely made the nitrocalcite product.
Stir and to add again that sulfuric acid stirs and adding water in the ferrochrome precipitation of hydroxide that produces in the aforesaid a step to PH3.5 ± 0.1, and be heated to more than 80 degree, again filter residue is carried out filtration washing, filter residue is an ironic hydroxide, can get iron oxide product to its heating, the filtrate condensing crystal can be got the basic chromium sulfate product.
The ammonia that distills out in the aforementioned c step can feed recycle in the stainless steel acid-washing waste liquid.
For ease of understanding technical solution of the present invention, sketch principle below in conjunction with reaction equation.
Because siderochrome and hydrofluoric acid can form more stable complex compound in the waste liquid, be difficult to destroy their stability according to a conventional method, they are separated from solution effectively, we find FeF according to experiment 6 3-, CrF 6 3-Under alkaline condition, can complete hydrolysis also generate ironic hydroxide and the chromium hydroxide polymkeric substance that is insoluble in water, and be easy to filtering separation, select for use under the ammonia environment and nickel to be generated nickel ammine soluble in water and separate with siderochrome and in filtrate, lead to hydrogen sulfide then, make nickel generate the nickel sulphide precipitation that is insoluble in water, the mother liquor behind the separation nickelous sulfide adds calcium hydroxide again and distills out the ammonia recycle utilization that reaction generates; In PH3.5 ± 0.1, ferric ion does not react, and chromium ion reacts, thereby can realize the separation with siderochrome oxyhydroxide, thereby has realized effective utilization of each effective constituent.
Chemical equation can be expressed as follows:
FeF 6 3+NH 3-→Fe(OH) 3↓+NH 4F
CrF 6 3-+NH 3-→Cr(OH) 3↓+NH 4F
Ni(NO 3) 2+NH 3-→Ni(NH 3) 4NO 3
Ni(NH 3) 4NO 3+H 2S-→NiS↓+NH 4NO 3+NH 3
NH 4NO 3+NH 4F+Cr(OH) 3-→CaF 2↓+Ca(NO 3) 2+NH 3
Cr (OH) 3+ H 2SO 4-→ Cr (OH) SO 4(pH value 3.5 ± 0.1)
Fe(OH) 3-→Fe 2O 3+H 2O
Advantage of the present invention is effectively to handle the spent pickle liquor that forms in the stainless steel product Industrial processes, can the waste liquid environmental protection treatment is free from environmental pollution, but valuable ingredients in the efficient recovery waste liquid again has higher society and economy benefit.
Description of drawings
Fig. 1 is the process flow sheet in the specific embodiment of the invention.
Embodiment
Below in conjunction with description of drawings the specific embodiment of the present invention:
Stainless steel acid-washing waste liquid dropped into feeds ammonia in the reaction vessel, to pH value 8, reacted mixed solution filtered obtains ferrochrome precipitation of hydroxide and nickel ammine filtrate; In nickel ammine filtrate, feed hydrogen sulfide, generate nickel sulphide precipitation and Neutral ammonium fluoride, ammonium nitrate mixed solution and free ammonia, the sedimentation and filtration washing is obtained the nickelous sulfide product; In filtrate, drops into calcium hydroxide and slowly be heated to 70 degree, under this temperature, will distill out ammonia, and reaction generates Calcium Fluoride (Fluorspan) precipitation and nitrocalcite, dry after filtering again the Calcium Fluoride (Fluorspan) product, filtrate is made the nitrocalcite product by condensing crystal.Ammonia is by recycle in the squirt pump suction stainless steel acid-washing waste liquid.
Adding water in the ferrochrome precipitation of hydroxide stirs and to add that sulfuric acid stirs and to PH3.5 again, and be heated to 90 the degree, again remaining filter residue is carried out filtration washing, filter residue is not for participating in the ironic hydroxide of reaction under this sour environment, can get iron oxide product to its heating, the filtrate condensing crystal can be got the basic chromium sulfate product.

Claims (3)

1, the environmental protection of stainless steel acid-washing waste liquid utilizes method, it is characterized in that: comprise the steps:
A drops into stainless steel acid-washing waste liquid and feeds ammonia in the reaction vessel, to the pH value between 8-9, reacted mixed solution is filtered the filtrate that obtains the ferrochrome precipitation of hydroxide and contain nickel ammine;
B feeds hydrogen sulfide in the filtrate of containing nickel ammine that preceding step produces, generate nickel sulphide precipitation and Neutral ammonium fluoride, ammonium nitrate mixed solution and free ammonia, and the sedimentation and filtration washing is obtained the nickelous sulfide product;
C, the b step is filtered out drop into calcium hydroxide in the filtrate of post precipitation and slowly be heated to the 60-80 degree, under this temperature, will distill out ammonia, and reaction generates Calcium Fluoride (Fluorspan) precipitation and nitrocalcite, dry after filtering again the Calcium Fluoride (Fluorspan) product, filtrate technology is routinely made the nitrocalcite product.
2, the environmental protection of stainless steel acid-washing waste liquid according to claim 1 utilizes method, it is characterized in that: add water in the ferrochrome precipitation of hydroxide that produces in the described a step and stir and to add again that sulfuric acid stirs and to pH3.5 ± 0.1, and be heated to more than 80 degree, again filter residue is carried out filtration washing, filter residue is an ironic hydroxide, to its heat iron oxide product, the filtrate condensing crystal is got the basic chromium sulfate product.
3, the environmental protection of stainless steel acid-washing waste liquid according to claim 1 and 2 utilizes method, it is characterized in that: the ammonia that distills out in the described c step feeds recycle in the stainless steel acid-washing waste liquid.
CNB2007100241737A 2007-07-18 2007-07-18 The environmental protection of stainless steel acid-washing waste liquid utilizes method Expired - Fee Related CN100556831C (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CNB2007100241737A CN100556831C (en) 2007-07-18 2007-07-18 The environmental protection of stainless steel acid-washing waste liquid utilizes method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CNB2007100241737A CN100556831C (en) 2007-07-18 2007-07-18 The environmental protection of stainless steel acid-washing waste liquid utilizes method

Publications (2)

Publication Number Publication Date
CN101100341A CN101100341A (en) 2008-01-09
CN100556831C true CN100556831C (en) 2009-11-04

Family

ID=39034824

Family Applications (1)

Application Number Title Priority Date Filing Date
CNB2007100241737A Expired - Fee Related CN100556831C (en) 2007-07-18 2007-07-18 The environmental protection of stainless steel acid-washing waste liquid utilizes method

Country Status (1)

Country Link
CN (1) CN100556831C (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2020076315A1 (en) * 2018-10-10 2020-04-16 Lixivia, Inc. Compositions and methods for purification of metals from steel making waste streams

Families Citing this family (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101376547B (en) * 2008-10-10 2010-10-13 韩晓波 Method for recovering and processing pickling solution of refining benzene
CN102115038A (en) * 2010-12-30 2011-07-06 王莉 Method for preparing sulfides and mixed product of sodium sulfide and strontium sulfate by manganese-containing waste liquid
CN102115039A (en) * 2010-12-30 2011-07-06 王莉 Method for preparing sulfide and mixed product of sodium sulfide and ammonium sulfate by manganese-containing waste liquid
CN104098148B (en) * 2013-04-08 2015-11-18 兰州大学 A kind for the treatment of process reclaiming nickel, chromium, iron from stainless steel plant's waste residue
CN104973745A (en) * 2014-04-11 2015-10-14 河北建支铸造集团有限公司 Harmless treatment method of red sludge in after-treatment liquid of cold galvanizing
CN104805291B (en) * 2015-04-16 2016-10-05 南阳师范学院 The process of a kind of stainless steel acid-washing waste liquid and iron, chromium, the recovery method of nickel
CN108166009A (en) * 2018-02-06 2018-06-15 北海诚德镍业有限公司 The system and method for nickelous carbonate are extracted in a kind of waste mixed acid from acid-washing stainless steel
CN109554718B (en) * 2019-01-25 2020-11-13 鲍君杰 Treatment method of stainless steel pickling waste liquid
CN112520776A (en) * 2020-11-26 2021-03-19 广沣金源(北京)科技有限公司 Combined treatment method for fluorine-containing nitric acid waste liquid and hydrofluoric acid waste liquid

Non-Patent Citations (2)

* Cited by examiner, † Cited by third party
Title
硝氟酸酸洗废液的治理. 稀有金属材料与工程,第6期. 1979 *
钢铁酸洗废液的处理技术及其评价. 郑隆鳌,刘文夫.钢铁研究,第1期. 1997 *

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2020076315A1 (en) * 2018-10-10 2020-04-16 Lixivia, Inc. Compositions and methods for purification of metals from steel making waste streams

Also Published As

Publication number Publication date
CN101100341A (en) 2008-01-09

Similar Documents

Publication Publication Date Title
CN100556831C (en) The environmental protection of stainless steel acid-washing waste liquid utilizes method
CN101982433B (en) Method for harmless and recycling treatment of stainless steel acid washing waste water neutralization sludge
CN101618892B (en) Recovery and comprehensive utilization method of heavy metals in stainless steel pickling wastewater sludge
CN104628217B (en) A kind of processing method recycling waste lithium cell electrolyte and electrolyte waste water
CN102634673B (en) Method for deeply removing iron ions from chromium-containing waste residue pickle liquor
CN101428933B (en) Biological agent cooperated hydrolyzation-blowing off treatment process for nickel-ammonia wastewater
CN104018184A (en) Brand new method of producing electrolytic manganese metal
CN102492858A (en) Method for separating enriched nickel and cobalt from battery waste leaching solution
CN109867382B (en) Resource recovery method of metal ions in pickling waste liquid, product prepared by resource recovery method and application of product
CN102808082B (en) Method for selective leaching separation of cobalt, nickel and molybdenum from high grade cobalt-nickel-molybdenum waste material
CN103495589B (en) A kind of plating waste residue recoverying and utilizing method
CN113481541B (en) Method for recovering manganese metal by using electrolytic manganese slag leachate
CN108947012B (en) Method for separating and recovering ammonia from ammonia nitrogen wastewater
CN101134566B (en) Process for preparing amino-sulfonic acid nickel by nickel sulfide concentrate
CN101070564A (en) Method for recovering valuable metal in electroplated mud
Zhang et al. Recovering phosphorus and lithium separately from wastewater and brine using a novel coupled biofilm-precipitation system
CN109576494B (en) Method for preparing sodium sulfate by utilizing metal surface treatment waste
CN114560767B (en) Method for preparing ferrous oxalate by siderite
CN111162272B (en) Regeneration method of nickel cobalt lithium manganate positive electrode material of waste lithium ion battery
CN113788520A (en) Iron-chromium-aluminum pickling process, wastewater treatment method and wastewater treatment device
CN109607945B (en) Method for improving biochemical efficiency of wastewater in photovoltaic and electronic industries
CN108996752B (en) Method for recovering low-concentration nickel from nickel extraction waste water
CN101905932B (en) Process for treating and recycling wastewater generated by performing chrome-free passivation on electrolytic manganese
CN218665447U (en) Continuous production system for preparing nickel sulfate by ammonia leaching based on ammonia circulation
CN111018182A (en) Recycling process of cyaniding cadmium plating electroplating rinsing water

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
C17 Cessation of patent right
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20091104

Termination date: 20120718