CN104193045A - Active turquoise blue dye production wastewater reclamation process - Google Patents

Active turquoise blue dye production wastewater reclamation process Download PDF

Info

Publication number
CN104193045A
CN104193045A CN201410330442.2A CN201410330442A CN104193045A CN 104193045 A CN104193045 A CN 104193045A CN 201410330442 A CN201410330442 A CN 201410330442A CN 104193045 A CN104193045 A CN 104193045A
Authority
CN
China
Prior art keywords
waste water
neutralization reaction
filter
wastewater
dyestuff
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.)
Granted
Application number
CN201410330442.2A
Other languages
Chinese (zh)
Other versions
CN104193045B (en
Inventor
赵立红
沈也红
李永明
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.)
Tangshan minzhou science and Technology Co., Ltd.
Original Assignee
NAIMAN MINGZHOU CHEMICAL 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 NAIMAN MINGZHOU CHEMICAL TECHNOLOGY Co Ltd filed Critical NAIMAN MINGZHOU CHEMICAL TECHNOLOGY Co Ltd
Priority to CN201410330442.2A priority Critical patent/CN104193045B/en
Publication of CN104193045A publication Critical patent/CN104193045A/en
Application granted granted Critical
Publication of CN104193045B publication Critical patent/CN104193045B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Landscapes

  • Removal Of Specific Substances (AREA)
  • Separation Of Suspended Particles By Flocculating Agents (AREA)

Abstract

The invention discloses an active turquoise blue dye production wastewater reclamation process, which comprises the following steps: (1) directly transferring dye wastewater which is no more than 50 times in chromaticity to a wastewater collection tank, feeding dye wastewater which is more than 50 times in chromaticity to a decolorizing pool, physically decolorizing the dye wastewater in the decolorizing pool, and transferring the processed dye wastewater into the wastewater collection tank once again; (2) adding the dye wastewater in the wastewater collection tank of the step (1) into a neutralization kettle, and slowly adding lime milk while stirring uniformly; and stopping reaction when pH value is 7.0-8.5; (3) filter-pressing through a filter press to obtain filtrate I and a filter cake I; (4) adding the obtained filtrate I to a replacement kettle, and adding sodium carbonate for a replacement reaction; and (5) filter-pressing materials in the replacement kettle of the step (4) through the press filter to obtain filtrate II and a filter cake II. The wastewater processed by the process can be completely reclaimed for production of active turquoise blue dye, thus realizing a goal of clean production in a dye production process.

Description

Reactive turquoise blue waste water in dye production is recycled technique
Technical field
The present invention relates to reactive turquoise blue waste water in dye production and recycle technique.
Background technology
In the synthetic production process of dyestuff, can produce a large amount of mother liquor waste waters and washes, because of its COD value and colourity higher, as not treated direct discharge, the destruction that can cause water ecological setting, serious environment pollution.At present, existing a lot of documents are reported the improvement technology of waste water in dye production, as adsorption decoloring method, catalytic oxidation, biochemical process, Fe-C Micro Electrolysis Method etc.These methods all obtain certain effect to the improvement of waste water from dyestuff, but waste water recovery not.The area that waste water reclamation is applied mechanically for water scarcity seems particularly important, yet there are no the report that relevant reactive turquoise blue waste water in dye production recovery reaches process water zero release.
Summary of the invention
The problem existing for solving above-mentioned prior art, the present invention proposes a kind of reactive turquoise blue waste water in dye production and recycles technique, waste water after this art breading can fully recovering in reactive turquoise blue DYE PRODUCTION, realized the green production target of cleaner production and the energy-saving and emission-reduction of DYE PRODUCTION process.
Technical scheme of the present invention is achieved in that
Reactive turquoise blue waste water in dye production is recycled a technique, comprises the following steps:
(1) waste water from dyestuff is processed respectively according to the difference of colourity, the waste water from dyestuff of colourity≤50 times directly enters wastewater collection tank, colourity >50 waste water from dyestuff doubly, enters decolouring pond and carries out physical decolorization processing, and after processing, waste water from dyestuff enters wastewater collection tank again;
By step (1) wastewater collection tank waste water from dyestuff add in neutralization reaction still, then slowly add milk of lime, stir while adding evenly, detect in real time the pH value in neutralization reaction still simultaneously, when pH value is 7.0~8.5, stop adding milk of lime;
By step (2) the material in neutralization reaction still adopt pressure filter to carry out press filtration, obtain filtrate I and filter cake I;
By step (3) gained filtrate I join in replacement reaction kettle, add sodium carbonate to carry out replacement(metathesis)reaction;
By step (4) the material in replacement reaction kettle adopt pressure filter to carry out press filtration, obtain filtrate II and filter cake II.
Further, the filtrate II reuse (5) of described step is to DYE PRODUCTION process, can be used as sulfonation operation bath water and condensation operation at the bottom of water use, certainly also can be used as ice making water and filter cake rinse water; Filter cake II reuse is carried out neutralization reaction to neutralization reaction still.
Further, in described decolouring pond, be provided with the molecular sieve that filter screen and main component are silicon-dioxide, described filter screen Mu Shuo≤200 order.
Further, (2) described step detects the pH value in neutralization reaction still in real time, when pH value is 7.5~8.5, stops adding milk of lime, is conducive to so follow-up replacement(metathesis)reaction.
Further, described step is (2) after waste water from dyestuff neutralization reaction, according to polyacrylamide with in and in still liquid mass ratio be 0.5~1:10 4ratio, in neutralization reaction still, add polyacrylamide solid, can accelerate like this speed of pressure filter press filtration.
Further, described replacement(metathesis)reaction adopts sodium carbonate to carry out, and the object of carrying out replacement(metathesis)reaction is that the existence of calcium salt in reactive turquoise blue dyestuff is larger to the salt tolerant alkalescence of dyestuff and solubleness Index Influence.
Waste water from dyestuff colourity of the present invention is measured and is drawn according to extension rate method, described extension rate method refers to get a certain amount of sewage sample and is placed in 100mL or 50mL colorimetric cylinder, till being repeatedly diluted to and just can't see color with distilled water, i.e. color the same as distilled water, the multiple of dilution water is the colourity of water sample, unit is that doubly the method is applicable to the contaminated surface water and industrial sewage color measurenent.
Beneficial effect of the present invention:
Reactive turquoise blue waste water in dye production recovery method of the present invention, the processing of first waste water from dyestuff being decoloured, can effectively avoid the post precipitation thing treatment step that need to decolour, and has saved program, and the waste water after decolouring is approaching with tap water, colourity≤50 times; After adopting lime slurry neutralization to process, the COD value of waste water, lower than 100mg/L, adopts lime slurry neutralization rather than neutralization with lime, is that the pH value after neutralization is more accurate because the pH of lime slurry neutralization reaction more easily controls; After neutralization, by pressure filter press filtration, obtain filtrate I and filter cake I, filter cake I main component is calcium sulfate, can be for adjusting the additive of cement index; Filtrate I is not directly discharged into sewage work, but through SPC-D replacement(metathesis)reaction, and carry out pressure filter press filtration and obtain filtrate II and filter cake II, filtrate II reuse is to DYE PRODUCTION process, filter cake II is that calcium carbonate reuse is carried out neutralization reaction to neutralization reaction still, has realized the complete-reclaiming of waste water and dregs.
Embodiment
Embodiment 1
The factory effluent of Qu Naiman Mingzhou Chemical Industry Science Co., Ltd reactive turquoise blue 21 carries out colorimetric detection, and colourity is 210 times, puts it into decolouring pond and carries out decolorization filtering.Decolouring pond comprises order number 200 object filter screens, and on filter screen, having main component is the molecular sieve of silicon-dioxide.Wastewater collection after decolouring is to wastewater collection tank, after collection, waste water in wastewater collection tank is joined in the neutralization reaction still of 10 tons, then slowly add milk of lime, stir while adding evenly, detect in real time the pH value in neutralization reaction still simultaneously, when pH value is 7.5, stop adding milk of lime.Then, adopt pressure filter to carry out press filtration the material in neutralization reaction still, obtain filtrate I and filter cake I, filter cake I is for adjusting the additive of cement index, and filtrate I joins replacement reaction kettle and sodium carbonate carries out replacement(metathesis)reaction; Then, adopt pressure filter to carry out press filtration the material in replacement reaction kettle, obtain filtrate II and filter cake II, filter cake II can reuse carry out neutralization reaction to neutralization reaction still, filtrate II naked eyes look the same with tap water, and colourity is 40 times after testing, and COD value is 90mg/L.Filtrate II is all for reactive turquoise blue 21 production processes, and products obtained therefrom solubleness reaches 155 grams per liters, and Salt And Alkali Tolerance index reaches 16 minutes, reaches the production standard of reactive turquoise blue dyestuff 21 completely.
Embodiment 2
The factory effluent of Qu Naiman Mingzhou Chemical Industry Science Co., Ltd reactive turquoise blue 14 carries out colorimetric detection, colourity is 40 times, collected wastewater collection tank, after collection, the waste water in wastewater collection tank is joined in the neutralization reaction still of 10 tons, then slowly add milk of lime, stir while adding evenly, detect in real time the pH value in neutralization reaction still simultaneously, when pH value is 7.0, stop adding milk of lime.Then, to add in neutralization reaction still according to polyacrylamide with in and in still liquid mass than being 0.5:10 4ratio add polyacrylamide solid; Then, adopt pressure filter to carry out press filtration, obtain filtrate I and filter cake I, filter cake I is for adjusting the additive of cement index, and filtrate I joins replacement reaction kettle and sodium carbonate carries out replacement(metathesis)reaction; Then, adopt pressure filter to carry out press filtration the material in replacement reaction kettle, obtain filtrate II and filter cake II, filter cake II can reuse carry out neutralization reaction to neutralization reaction still, filtrate II naked eyes look the same with tap water, and colourity is 40 times after testing, and COD value is 100mg/L.Filtrate II is all for reactive turquoise blue 14 production processes, and products obtained therefrom solubleness reaches 150 grams per liters, reaches the production standard of reactive turquoise blue dyestuff 14 completely.
Embodiment 3
The factory effluent of Qu Naiman Mingzhou Chemical Industry Science Co., Ltd reactive turquoise blue 72 carries out colorimetric detection, and colourity is 160 times, puts it into decolouring pond and carries out decolorization filtering.Decolouring pond comprises order number 300 object filter screens, and on filter screen, having main component is the molecular sieve of silicon-dioxide.Wastewater collection after decolouring is to wastewater collection tank, after collection, waste water in wastewater collection tank is joined in the neutralization reaction still of 10 tons, then slowly add milk of lime, stir while adding evenly, detect in real time the pH value in neutralization reaction still simultaneously, when pH value is 8.0, stop adding milk of lime.Then, to add in neutralization reaction still according to polyacrylamide with in and in still liquid mass than being 1:10 4ratio add polyacrylamide solid; Then, adopt pressure filter to carry out press filtration, obtain filtrate I and filter cake I, filter cake I is for adjusting the additive of cement index, and filtrate I joins replacement reaction kettle and sodium carbonate carries out replacement(metathesis)reaction; Then, adopt pressure filter to carry out press filtration the material in replacement reaction kettle, obtain filtrate II and filter cake II, filter cake II can reuse carry out neutralization reaction to neutralization reaction still, filtrate II naked eyes look the same with tap water, and colourity is 30 times after testing, and COD value is 85mg/L.Filtrate II is all for reactive turquoise blue 72 production processes, and products obtained therefrom solubleness reaches 165 grams per liters, reaches the production standard of reactive turquoise blue dyestuff 72 completely.
Embodiment 4
The factory effluent of Qu Naiman Mingzhou Chemical Industry Science Co., Ltd reactive turquoise blue 21 carries out colorimetric detection, colourity is 40 times, collected wastewater collection tank, after collection, the waste water in wastewater collection tank is joined in the neutralization reaction still of 10 tons, then slowly add milk of lime, stir while adding evenly, detect in real time the pH value in neutralization reaction still simultaneously, when pH value is 8.5, stop adding milk of lime.Then, to add in neutralization reaction still according to polyacrylamide with in and in still liquid mass than being 0.8:10 4ratio add polyacrylamide solid; Then, adopt pressure filter to carry out press filtration, obtain filtrate I and filter cake I, filter cake I is for adjusting the additive of cement index, and filtrate I joins replacement reaction kettle and sodium carbonate carries out replacement(metathesis)reaction; Then, adopt pressure filter to carry out press filtration the material in replacement reaction kettle, obtain filtrate II and filter cake II, filter cake II can reuse carry out neutralization reaction to neutralization reaction still, filtrate II naked eyes look the same with tap water, and colourity is 40 times after testing, and COD value is 80mg/L.Filtrate II is all for reactive turquoise blue 21 production processes, and products obtained therefrom solubleness reaches 155 grams per liters, and Salt And Alkali Tolerance index reaches 16 minutes, reaches the production standard of reactive turquoise blue dyestuff 21 completely.

Claims (5)

1. reactive turquoise blue waste water in dye production is recycled a technique, it is characterized in that, comprises the following steps:
(1) waste water from dyestuff is processed respectively according to the difference of colourity, the waste water from dyestuff of colourity≤50 times directly enters wastewater collection tank, colourity >50 waste water from dyestuff doubly, enters decolouring pond and carries out physical decolorization processing, and after processing, waste water from dyestuff enters wastewater collection tank again;
By step (1) wastewater collection tank waste water from dyestuff add in neutralization reaction still, then slowly add milk of lime, stir while adding evenly, detect in real time the pH value in neutralization reaction still simultaneously, when pH value is 7.0~8.5, stop adding milk of lime;
By step (2) the material in neutralization reaction still adopt pressure filter to carry out press filtration, obtain filtrate I and filter cake I;
By step (3) gained filtrate I join in replacement reaction kettle, add sodium carbonate to carry out replacement(metathesis)reaction;
By step (4) the material in replacement reaction kettle adopt pressure filter to carry out press filtration, obtain filtrate II and filter cake II.
2. waste water reclamation according to claim 1 utilizes technique, it is characterized in that, the filtrate II reuse (5) of described step is to DYE PRODUCTION process, and filter cake II reuse is carried out neutralization reaction to neutralization reaction still.
3. waste water reclamation according to claim 1 and 2 utilizes technique, it is characterized in that, is provided with the molecular sieve that filter screen and main component are silicon-dioxide in described decolouring pond, described filter screen Mu Shuo≤200 order.
4. waste water reclamation according to claim 1 and 2 utilizes technique, it is characterized in that, (2) described step detects the pH value in neutralization reaction still in real time, when pH value is 7.5~8.5, stops adding milk of lime.
5. waste water reclamation according to claim 1 and 2 utilizes technique, it is characterized in that, described step is (2) after waste water from dyestuff neutralization reaction, according to polyacrylamide with in and in still liquid mass than being the ratio of 0.5~1:104, in neutralization reaction still, add polyacrylamide solid.
CN201410330442.2A 2014-07-11 2014-07-11 Active bright blue waste water in dye production recycles technique Active CN104193045B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201410330442.2A CN104193045B (en) 2014-07-11 2014-07-11 Active bright blue waste water in dye production recycles technique

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201410330442.2A CN104193045B (en) 2014-07-11 2014-07-11 Active bright blue waste water in dye production recycles technique

Publications (2)

Publication Number Publication Date
CN104193045A true CN104193045A (en) 2014-12-10
CN104193045B CN104193045B (en) 2016-06-01

Family

ID=52078467

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201410330442.2A Active CN104193045B (en) 2014-07-11 2014-07-11 Active bright blue waste water in dye production recycles technique

Country Status (1)

Country Link
CN (1) CN104193045B (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104674570A (en) * 2015-02-13 2015-06-03 绍兴文理学院 Recycling dyeing method of dyeing wastewater of reactive dyes
CN105836921B (en) * 2016-05-04 2019-06-25 浙江闰土研究院有限公司 A kind of processing method of dye wash waste water

Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61141995A (en) * 1984-12-14 1986-06-28 Shinyuu Kasei Kk Treatment of waste water containing water-soluble dye
CN1562774A (en) * 2004-04-14 2005-01-12 南京大学 Method for treatng wastewater of producing reactive dyes in class of bromamine acid, and for reclaiming resources
WO2010133734A1 (en) * 2009-05-22 2010-11-25 Universitat Politècnica De Catalunya Use of biopolymer chitosan for the removal of colour from wastewater using a combined coagulation-flocculation and adsorption process
US20110017098A1 (en) * 2009-07-03 2011-01-27 Board Of Regents, The University Of Texas System Removal and recovery of dye waste from effluents using clay
CN103214116A (en) * 2013-03-15 2013-07-24 浙江闰土股份有限公司 Recycling method of sulfuric acid-containing wastewater from disperse dye production
CN103588318A (en) * 2012-08-17 2014-02-19 浙江中辉皮草有限公司 Processing method used for multiple recycling of fur dyeing effluent
CN103880210A (en) * 2014-03-14 2014-06-25 浙江迪邦化工有限公司 Treating and recycling process of acid wastewater generated in disperse dye production

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61141995A (en) * 1984-12-14 1986-06-28 Shinyuu Kasei Kk Treatment of waste water containing water-soluble dye
CN1562774A (en) * 2004-04-14 2005-01-12 南京大学 Method for treatng wastewater of producing reactive dyes in class of bromamine acid, and for reclaiming resources
WO2010133734A1 (en) * 2009-05-22 2010-11-25 Universitat Politècnica De Catalunya Use of biopolymer chitosan for the removal of colour from wastewater using a combined coagulation-flocculation and adsorption process
US20110017098A1 (en) * 2009-07-03 2011-01-27 Board Of Regents, The University Of Texas System Removal and recovery of dye waste from effluents using clay
CN103588318A (en) * 2012-08-17 2014-02-19 浙江中辉皮草有限公司 Processing method used for multiple recycling of fur dyeing effluent
CN103214116A (en) * 2013-03-15 2013-07-24 浙江闰土股份有限公司 Recycling method of sulfuric acid-containing wastewater from disperse dye production
CN103880210A (en) * 2014-03-14 2014-06-25 浙江迪邦化工有限公司 Treating and recycling process of acid wastewater generated in disperse dye production

Non-Patent Citations (3)

* Cited by examiner, † Cited by third party
Title
刘帅霞,何松: ""高铁酸盐对染整废水脱色处理的实验研究"", 《针织工业》 *
周光勇 等: ""活性染浴残液处理与回用技术"", 《印染》 *
孙华 等: ""内电解法处理染料生产废水试验研究"", 《工业用水与废水》 *

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104674570A (en) * 2015-02-13 2015-06-03 绍兴文理学院 Recycling dyeing method of dyeing wastewater of reactive dyes
CN105836921B (en) * 2016-05-04 2019-06-25 浙江闰土研究院有限公司 A kind of processing method of dye wash waste water

Also Published As

Publication number Publication date
CN104193045B (en) 2016-06-01

Similar Documents

Publication Publication Date Title
CN102849879A (en) Treatment technology for recycling reverse osmosis concentrated water
CN101565202B (en) Silicon slag treating process in zirconyl chloride production
CN210117307U (en) Waste incineration fly ash washing water resource treatment system
CN103482784B (en) Method for processing waste water of acid leaching and deironing of potassium feldspar
CN105645643A (en) Phosphorus-containing sewage treatment method
CN104591486B (en) A kind of processing method of Low acid dye wastewater
CN104724853B (en) A kind of clothes dyeing and printing sewage processes technique
CN106414347B (en) Method and system for reducing phosphorus in effluent or filtrate
CN104193045B (en) Active bright blue waste water in dye production recycles technique
CN107585917B (en) Method for treating ceramic polishing wastewater
CN108751533A (en) A kind of processing method of the acidic rinse waste water suitable for process of metal working
CN103086542B (en) Recycling process and system for wooden activated carbon industrial wastewater
CN102502989A (en) Method for processing hexavalent chromium ions in sewage by utilizing ferrous ion obtained from waste acid
CN104086043B (en) A kind for the treatment of of dyeing wastewater reuse method
JP5224380B2 (en) Manufacturing method of low grade Ni recycled sludge
CN206692476U (en) A kind of pickling waste waters treatment for reuse system
CN104193046A (en) Method for recycling and reusing active turquoise blue dye production wastewater
CN112223909B (en) Method for cleaning printing screen for circuit board
CN103508607A (en) Method for improving water production rate of advanced wastewater treatment
CN104058570B (en) A kind of mud coagulant of diaphragm filter press and using method thereof
CN107540077B (en) Catalytic oxidation treatment method for neutralizing wastewater by 3, 3' -dichlorobenzidine hydrochloride
CN104016527A (en) Textile dyeing wastewater treatment method
CN104003555A (en) Method of pretreating dyeing and finishing wastewater
CN219991360U (en) Circulating water sand filtration backwash water treatment device
CN103663758A (en) Method for recycling wastewater produced during purified terephthalic acid production

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

Effective date of registration: 20180713

Address after: 063611 Hebei Tangshan City harbor development area, Zhongshan Avenue, north of Sinoma road.

Patentee after: Tangshan minzhou science and Technology Co., Ltd.

Address before: 028306 Tongliao City, the Inner Mongolia Autonomous Region, Naiman Banner, Da qinla town south suburb Chemical District

Patentee before: NAIMAN MINGZHOU CHEMICAL TECHNOLOGY CO., LTD.

TR01 Transfer of patent right