CN103833155A - Chromium-containing wastewater treatment technology - Google Patents

Chromium-containing wastewater treatment technology Download PDF

Info

Publication number
CN103833155A
CN103833155A CN201210471314.0A CN201210471314A CN103833155A CN 103833155 A CN103833155 A CN 103833155A CN 201210471314 A CN201210471314 A CN 201210471314A CN 103833155 A CN103833155 A CN 103833155A
Authority
CN
China
Prior art keywords
chromium
tank
chrome
press filtration
hours
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
CN201210471314.0A
Other languages
Chinese (zh)
Inventor
郭俊
李朝永
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.)
ZHONGNIU GROUP Co Ltd
Original Assignee
ZHONGNIU GROUP Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by ZHONGNIU GROUP Co Ltd filed Critical ZHONGNIU GROUP Co Ltd
Priority to CN201210471314.0A priority Critical patent/CN103833155A/en
Publication of CN103833155A publication Critical patent/CN103833155A/en
Pending legal-status Critical Current

Links

Landscapes

  • Inorganic Compounds Of Heavy Metals (AREA)

Abstract

A chromium-containing wastewater treatment technology is characterized in that precipitation separation of chromium-containing wastewater generated in a chrome tanning operation is carried out under a certain acidity, a chromium-free supernatant is reused in a liming workshop section, chromium ions form a solid substance with other precipitates, separation filtration is carried out to remove impurities, and acid dissolution ageing reaction is carried out to prepare a recyclable chrome tanning agent which can be directly reused in production or can be stored for later use. The technology realizes the comprehensive utilization of a resource, reduction of the discharge amount of a heavy metal chromium, production auxiliary material saving, and reduction of the treatment cost of chromium-containing sludge, recyclable chromium used in production can save 20% of a water resource, and the full scale and the handle of leather are better than full scale and the handle realized by raw chromium powder.

Description

Process for processing chromate-containing waste water
Technical field
The present invention relates to process for processing chromate-containing waste water.
Background technology
The chrome waste liquid that in tanning production, a tanner order produces is more difficult, and processing costs is high.Effect is undesirable, and employing alkaline precipitation makes the chromium ion in waste water form precipitated powder together with plaster and after hydraulic pressure, forms chromium-bearing sludge, belongs to dangerous and pollutes.
Summary of the invention
The object of the invention is to overcome the above problems, process for processing chromate-containing waste water is provided.
The present invention realizes by following manufacture craft: process for processing chromate-containing waste water, the chrome waste liquid that chrome tanning process produces is precipitate and separate under certain potential of hydrogen condition, Chrome-free supernatant fluid reuse is in liming workshop section, chromium ion forms solid matter with other throw out, remove impurity through separating and filtering, acid-soluble ageing is reacted, and produces the chrome tanning agent of recoverable, direct reuse is for subsequent use in producing or storing, and concrete steps are as follows:
The first step, tanning workshop set gradually to Chrome Tanning Wastewater collecting tank drainageway: planar grille 15mm, 10mm and mechanical grille 3mm, 2mm, remove macrobead scurf, hair slag, wood chip etc.
The waste water of second step, collecting tank pumps into reaction tank by pump, for further removing impurity, hydraulic screen is set.
The 3rd step, in reaction tank, add liquid caustic soda (sodium hydroxide) to adjust pH value between 10-10.5, reaction end pH value is 8-9.5, makes being converted into precipitation and separating in Chrome Tanning Wastewater, and pneumatic blending is set in reaction tank, fully reacts more than 2 hours.
The 4th step, completely reacted mixture pump into settling tank, add appropriate polyacrylamide simultaneously, and the residence time, more than 2 hours mud adopted pressure filter press filtration, after the press filtration of chromium mud is good, then with clear water washing one side, to improve chromium mud purity.
The 5th step, chromium mud acid are dissolved in reactor and carry out, and sulfuric acid used is dilute sulphuric acid.First the vitriol oil is mixed with to certain density dilute sulphuric acid.After 90C-100C is incubated 3 hours, cools to 40-50C, press filtration obtains chrome liquor.
The 6th step, press filtration obtain chrome liquor and flow into transfer tank, temporary storage.
The 7th step, concentrated, chrome liquor pumps into concentration kettle by transfer tank, by concentrating under reduced pressure, chrome liquor solid content is brought up to more than 45%, obtains containing chromium retanning agent.
Beneficial effect of the present invention is: both realized the comprehensive utilization of resource, reduce again the quantity discharged of heavy metal chromium, save production auxiliary materials and reduce again the outer expense of processing of chromium-bearing sludge, through life-time service, can react for the production of the water resources that not only can save 20% by reuse chromium, point full scale, the feel of leather are better than former chromium powder simultaneously.
Embodiment
Process for processing chromate-containing waste water, completes by following processing step:
The first step, tanning workshop set gradually to Chrome Tanning Wastewater collecting tank drainageway: planar grille 15mm, 10mm and mechanical grille 3mm, 2mm, remove macrobead scurf, hair slag, wood chip etc.
The waste water of second step, collecting tank pumps into reaction tank by pump, for further removing impurity, hydraulic screen is set.
The 3rd step, in reaction tank, add liquid caustic soda (sodium hydroxide) to adjust pH value 10.2, reaction end pH value is 9.1, makes being converted into precipitation and separating in Chrome Tanning Wastewater, and pneumatic blending is set in reaction tank, fully reacts 4 hours.
The 4th step, completely reacted mixture pump into settling tank, add appropriate polyacrylamide simultaneously, and 3 hours residence time, mud adopts pressure filter press filtration, after the press filtration of chromium mud is good, then with clear water washing one side, to improve chromium mud purity.
The 5th step, chromium mud acid are dissolved in reactor and carry out, and sulfuric acid used is dilute sulphuric acid, first the vitriol oil are mixed with to certain density dilute sulphuric acid, and after 95 ° of C are incubated 3 hours, cool to 45 ° of C, press filtration obtains chrome liquor.
The 6th step, press filtration obtain chrome liquor and flow into transfer tank, temporary storage.
The 7th step, concentrated, chrome liquor pumps into concentration kettle by transfer tank, by concentrating under reduced pressure, chrome liquor solid content is brought up to more than 45%, obtains containing chromium retanning agent.

Claims (1)

1. process for processing chromate-containing waste water, is characterized in that: it is completed by following steps:
The first step, tanning workshop set gradually to Chrome Tanning Wastewater collecting tank drainageway: planar grille 15mm, 10mm and mechanical grille 3mm, 2mm, remove macrobead scurf, hair slag, wood chip etc.;
The waste water of second step, collecting tank pumps into reaction tank by pump, for further removing impurity, hydraulic screen is set;
The 3rd step, in reaction tank, add liquid caustic soda (sodium hydroxide) to adjust pH value between 10-10.5, reaction end pH value is 8-9.5, makes being converted into precipitation and separating in Chrome Tanning Wastewater, and pneumatic blending is set in reaction tank, fully reacts more than 2 hours;
The 4th step, completely reacted mixture pump into settling tank, add appropriate polyacrylamide simultaneously, and the residence time is more than 2 hours, and mud adopts pressure filter press filtration, after the press filtration of chromium mud is good, then with clear water washing one side;
The 5th step, chromium mud acid are dissolved in reactor and carry out, and sulfuric acid used is dilute sulphuric acid;
First the vitriol oil is mixed with to certain density dilute sulphuric acid, after 90C-100C is incubated 3 hours, cools to 40-50C, press filtration obtains chrome liquor;
The 6th step, press filtration obtain chrome liquor and flow into transfer tank, temporary storage;
The 7th step, concentrated, chrome liquor pumps into concentration kettle by transfer tank, obtains containing chromium retanning agent.
CN201210471314.0A 2012-11-20 2012-11-20 Chromium-containing wastewater treatment technology Pending CN103833155A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201210471314.0A CN103833155A (en) 2012-11-20 2012-11-20 Chromium-containing wastewater treatment technology

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201210471314.0A CN103833155A (en) 2012-11-20 2012-11-20 Chromium-containing wastewater treatment technology

Publications (1)

Publication Number Publication Date
CN103833155A true CN103833155A (en) 2014-06-04

Family

ID=50797101

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201210471314.0A Pending CN103833155A (en) 2012-11-20 2012-11-20 Chromium-containing wastewater treatment technology

Country Status (1)

Country Link
CN (1) CN103833155A (en)

Cited By (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105523665A (en) * 2016-01-12 2016-04-27 武汉森泰环保股份有限公司 Method for recovering chromium from leather tanning waste water
EP3045548A3 (en) * 2014-12-22 2016-10-12 Zhang, Zhuangdou Chromium tanning process with reduced waste discharge
CN106277101A (en) * 2016-08-30 2017-01-04 陕西科技大学 A kind of method utilizing lamina sodium silicate precipitation chroming waste liquor and chromium resource to reclaim
CN106630008A (en) * 2016-03-22 2017-05-10 深圳前海中盛环保科技有限公司 Novel method for chrome tanning wastewater treatment and chrome recycling
AU2015271965B2 (en) * 2014-12-22 2017-09-07 Zhuangdou ZHANG Tannery process with effluent recycling
US9776887B2 (en) 2013-12-04 2017-10-03 Zhuangdou Zhang Tannery process with effluent recycling
CN107640848A (en) * 2016-07-22 2018-01-30 宝山钢铁股份有限公司 A kind of method of the processing of flushing waste water containing chromium
US10260115B2 (en) 2014-03-20 2019-04-16 Zhuangdou Zhang Leather production using waste liquids
CN110002564A (en) * 2019-05-13 2019-07-12 浙江海洋大学 The processing method of Chrome Tanning Wastewater
CN110923477A (en) * 2019-12-11 2020-03-27 中南大学 Method for separating and recovering chromium in tanning chromium-containing sludge
CN115465968A (en) * 2022-09-16 2022-12-13 嘉兴学院 Method for separating and recovering chromium in chrome tanning waste liquid

Cited By (15)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US10501336B2 (en) 2013-12-04 2019-12-10 Zhuangdou Zhang Tannery process with effluent recycling
US11040890B2 (en) 2013-12-04 2021-06-22 Zhuangdou Zhang Tannery process with effluent recycling
US9776887B2 (en) 2013-12-04 2017-10-03 Zhuangdou Zhang Tannery process with effluent recycling
US10260115B2 (en) 2014-03-20 2019-04-16 Zhuangdou Zhang Leather production using waste liquids
EP3045548A3 (en) * 2014-12-22 2016-10-12 Zhang, Zhuangdou Chromium tanning process with reduced waste discharge
AU2015271965B2 (en) * 2014-12-22 2017-09-07 Zhuangdou ZHANG Tannery process with effluent recycling
CN105523665A (en) * 2016-01-12 2016-04-27 武汉森泰环保股份有限公司 Method for recovering chromium from leather tanning waste water
CN105523665B (en) * 2016-01-12 2018-02-09 武汉森泰环保股份有限公司 A kind of method that chromium is reclaimed from leather tanning wastewater
CN106630008A (en) * 2016-03-22 2017-05-10 深圳前海中盛环保科技有限公司 Novel method for chrome tanning wastewater treatment and chrome recycling
CN107640848A (en) * 2016-07-22 2018-01-30 宝山钢铁股份有限公司 A kind of method of the processing of flushing waste water containing chromium
CN106277101B (en) * 2016-08-30 2019-07-30 陕西科技大学 A method of chroming waste liquor is precipitated using lamina sodium silicate and chromium resource recycles
CN106277101A (en) * 2016-08-30 2017-01-04 陕西科技大学 A kind of method utilizing lamina sodium silicate precipitation chroming waste liquor and chromium resource to reclaim
CN110002564A (en) * 2019-05-13 2019-07-12 浙江海洋大学 The processing method of Chrome Tanning Wastewater
CN110923477A (en) * 2019-12-11 2020-03-27 中南大学 Method for separating and recovering chromium in tanning chromium-containing sludge
CN115465968A (en) * 2022-09-16 2022-12-13 嘉兴学院 Method for separating and recovering chromium in chrome tanning waste liquid

Similar Documents

Publication Publication Date Title
CN103833155A (en) Chromium-containing wastewater treatment technology
CN108584901B (en) Method for recovering ceramic-grade iron phosphate from polymetallic hazardous wastes
CN102153217A (en) Electroplating integrated wastewater treatment method
CN104609683A (en) Chrome tanning sludge heavy metal chromium regeneration method
CN104108814B (en) A kind of method processing Rutile type Titanium Dioxide waste water
CN103043759A (en) Method for preparing polyaluminium ferric chloride flocculating agent by pickling waste liquid and waste aluminium material
CN104445720A (en) Pickling waste liquid treatment process of steel industry
CN101648741A (en) Recycling method of heavy metal in composite waste
CN102249443B (en) Method for recycling chromium from chromium passivation wastewater of electrolytic manganese factory
CN102010082A (en) Treatment method for recycling waste dilute sulfuric acid
CN104512951A (en) Method for co-production of ploysilicate aluminium ferric sulphate and waste water treatment powder by PAC (poly aluminum chloride) residues
CN104773748A (en) Method for preparing low-iron polyaluminium sulfate by using aluminiferous waste sulfuric acid mother liquor
CN101898838B (en) Method for separating iron and steel pickling waste liquid through multistage membrane dialysis
CN110498531A (en) The devil liquor recovery of concentrated base containing aluminium utilizes method
CN102241448A (en) Comprehensive utilization method of sodium sulfate wastewater
CN102167436A (en) Electroplating wastewater treating agent
CN101628928A (en) Cleaning and producing technology of turmetic produced saponin
CN112320776B (en) Chemical waste liquid throwing and washing water regenerated acid recovery system and application thereof
CN202657995U (en) Recycling system for acid-containing wastewater
CN109516443A (en) A kind of processing method of the Waste Sulfuric Acid containing aluminium
CN108996752B (en) Method for recovering low-concentration nickel from nickel extraction waste water
CN104402145B (en) The waste water Han ferrous salt is utilized to prepare the production method of hydrated ferric oxide.
CN101905932B (en) Process for treating and recycling wastewater generated by performing chrome-free passivation on electrolytic manganese
CN102774889A (en) Method for producing poly aluminum ferric chloride (PAFC) by utilizing caustic sludge
CN102153223A (en) Sodium carboxymethylcellulose industrial sewage recycling device

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C02 Deemed withdrawal of patent application after publication (patent law 2001)
WD01 Invention patent application deemed withdrawn after publication

Application publication date: 20140604