Movatterモバイル変換


[0]ホーム

URL:


CN102874983A - Method for treating N-Phosphonomethyl iminodiacetic acid (PMIDA) mother liquid - Google Patents

Method for treating N-Phosphonomethyl iminodiacetic acid (PMIDA) mother liquid
Download PDF

Info

Publication number
CN102874983A
CN102874983ACN2012103848583ACN201210384858ACN102874983ACN 102874983 ACN102874983 ACN 102874983ACN 2012103848583 ACN2012103848583 ACN 2012103848583ACN 201210384858 ACN201210384858 ACN 201210384858ACN 102874983 ACN102874983 ACN 102874983A
Authority
CN
China
Prior art keywords
mother liquor
mother liquid
pmida98
pmida
treatment process
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
CN2012103848583A
Other languages
Chinese (zh)
Other versions
CN102874983B (en
Inventor
孙国庆
李志清
姚红霞
侯永生
陈桂元
邹宗加
凌晓光
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.)
Shandong Weifang Rainbow Chemical Co Ltd
Original Assignee
Shandong Weifang Rainbow Chemical 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 Shandong Weifang Rainbow Chemical Co LtdfiledCriticalShandong Weifang Rainbow Chemical Co Ltd
Priority to CN201210384858.3ApriorityCriticalpatent/CN102874983B/en
Publication of CN102874983ApublicationCriticalpatent/CN102874983A/en
Application grantedgrantedCritical
Publication of CN102874983BpublicationCriticalpatent/CN102874983B/en
Activelegal-statusCriticalCurrent
Anticipated expirationlegal-statusCritical

Links

Landscapes

Abstract

The invention relates to a method for treating an N-Phosphonomethyl iminodiacetic acid (PMIDA) mother liquid which is obtained by producing glyphosate by an iminodiacetic acid method. The method includes adding alkaline substances into the PMIDA mother liquid, adjusting potential of hydrogen (pH) of the mother liquid to be in a range from 9 to 12, subjecting the mother liquid to multiple-effect evaporation and concentration, filtering to obtain a filter cake and a filter liquid, washing the filter cake to remove organic matters to obtain inorganic salt, and burning the filter liquid to obtain pyrophosphate. The method for treating the PMIDA mother liquid has the advantages that chlorine containing substances and phosphorus containing substances in the mother liquid can be recycled in a high yield coefficient mode, the process is simple, the environment-friendly benefit is remarkable, and the method is suitable for popularization and usage in industrial mass production.

Description

A kind for the treatment of process of pmida98 mother liquor
Technical field
The present invention relates to a kind for the treatment of process of pmida98 mother liquor, particularly a kind of iminodiacetic acid (salt) acid system is produced the treatment process of the pmida98 mother liquor that glyphosate obtains.
Technical background
Glyphosate is as the steriland herbicide of a kind of efficient, wide spectrum, low toxicity, range of application is more and more extensive, become the present in the world weedicide of consumption maximum, the method that Present Domestic prepares glyphosate is a lot, dialkyl phosphite method and the iminodiacetic acid (salt) acid systems of adopting more, can produce the acid mother liquid of the Multiple components such as chloride ion-containing, sodium ion, pmida98 when adopting the iminodiethanoic acid route to prepare glyphosate, in present production process, process comparatively difficulty of this kind mother liquor, usually fall as wastewater treatment, not only waste resource, but also contaminate environment.
Only the sodium-chlor in the waste water is recycled in the patent application of Chinese patent CN1422275A and CN1837105A, pmida98 is utilized; Recycled the pmida98 in the waste water in the patent application of Chinese patent CN101041527A, but complex process wastes time and energy; Chinese patent CN101348266A adopts the nanofiltration membrane concentrated mother liquor, reclaim the pmida98 in the concentrated solution, light liquid is through evaporative crystallization, and roasting, dephosphorization are processed and obtained refining sodium-chlor, although reclaimed pmida98 and byproduct sodium chloride, but the rate of recovery is also not bery high, from the data of embodiment 1, it only is 91.2% that pmida98 reclaims, and the sodium-chlor rate of recovery does not reach 90%.And treatment step is comparatively loaded down with trivial details, and processing cost is not low yet.
Now, seek a kind of can be high yield reclaim Recyclable in the mother liquor, can reduce again waste water and discharge, alleviate environmental protection pressure, the treatment process that can produce higher secondary benefit and the simple pmida98 mother liquor of technique simultaneously is the problem that the industry needs to be resolved hurrily.
Summary of the invention
In order to solve the problems of the technologies described above, the invention provides the treatment process that a kind of iminodiacetic acid (salt) acid system is produced the PMIDA synthesis mother liquor that glyphosate obtains.The present invention can effectively reclaim the material in the pmida98 mother liquor, and technique is simple, and is easy to operate.
Concrete technical scheme of the present invention is as follows:
A kind for the treatment of process of pmida98 mother liquor may further comprise the steps:
(1) in the pmida98 mother liquor, add alkaline matter, make the mother liquor pH regulator to 9-12, concentrated through multiple-effect evaporation, filter, get filter cake and filtrate;
(2) get filter cake, remove organic substance through washing, namely get inorganic salt;
(3) get filtrate, through burning, namely get pyrophosphate salt.Further, also comprise waste heat and the solid that reclaims in the incineration flue gas.
Described pmida98 mother liquor is when adopting the standby glyphosate of iminodiethanoic acid legal system, the acid mother liquid of synthetic pmida98 gained.
In the above-mentioned steps (1), alkaline matter is sodium hydroxide, potassium hydroxide, calcium hydroxide or calcium oxide.Inventing used alkaline matter is pH adjusting agent, and its state, concentration are not particularly limited, for considering of wastewater flow rate and processing cost, and preferred solid sodium hydroxide.
In the above-mentioned steps (3), multiple-effect evaporation is concentrated into 60 ~ 90% of former weight.
In the above-mentioned steps (3), incineration temperature is 600 ~ 900 ℃.
Adopting the present invention to process PMIDA synthesis mother liquor has the following advantages:
(1) technique is simple, efficient, the chlorion transformation efficiency is more than 98%, step (2) gained waste water is after biochemical system is processed, the waste water COD of discharging is less than 20mg/L, TP is less than 0.5mg/L, and ammonia nitrogen has been realized the zero release of waste water substantially less than 10mg/L, efficiently solve the processing problem of pmida98 mother liquor, environmental benefit of the present invention is outstanding;
(2) gained pyrophosphate salt content is more than 95%, and the phosphorus containg substances transformation efficiency reaches more than 98%;
(3) the gained Industrial Salt can be used for the industries such as chemical industry, papermaking, building, and the trisodium phosphate of gained can be used for chemical industry, plating, wool spinning, paper industry, so economic benefit of the present invention is outstanding.
Embodiment
Below by specific embodiment the present invention is further set forth, should be understood that, following explanation only is in order to explain the present invention, its particular content not to be limited.
Embodiment 1
Get pmida98 mother liquor 1000g, chlorion 13.8% is arranged after testing, total phosphorus 0.9%, add the 30wt% sodium hydroxide solution, make mother liquor pH regulator to 9 after, multiple-effect evaporation is concentrated into 60% of former weight, filter, filter cake is removed organism through washing, namely gets sodium-chlor 223.12g, the chlorion transformation efficiency is 98.1%, and waste water is COD 18mg/L after biochemical treatment, TP 0.4mg/L, ammonia nitrogen 8mg/L, filtrate namely gets trisodium phosphate 38.5g through 600 ℃ of burnings, content 98.3%, phosphorus containg substances transformation efficiency 98.0%.Reclaim simultaneously waste heat and solid in the incineration flue gas.
Embodiment 2
To containing chlorion 13.8%, add the 40wt% sodium hydroxide solution among the pmida98 mother liquor 1000g of total phosphorus 0.9%, make mother liquor pH regulator to 10 after, multiple-effect evaporation is concentrated into 70% of former weight, filters, and filter cake is removed organism through washing, namely get sodium-chlor 223.92g, the chlorion transformation efficiency is 98.5%, and waste water is COD 17mg/L after biochemical treatment, TP 0.3mg/L, ammonia nitrogen 7mg/L, filtrate namely gets trisodium phosphate 38.4g through 700 ℃ of burnings, content 98.6%, phosphorus containg substances transformation efficiency 98.1%.Reclaim simultaneously waste heat and solid in the incineration flue gas.
Embodiment 3
To containing chlorion 13.8%, add the 50wt% sodium hydroxide solution among the pmida98 mother liquor 1000g of total phosphorus 0.9%, make mother liquor pH regulator to 11 after, multiple-effect evaporation is concentrated into 80% of former weight, filters, and filter cake is removed organism through washing, namely get sodium-chlor 224.4g, the chlorion transformation efficiency is 98.7%, and waste water is COD 12mg/L after biochemical treatment, TP 0.3mg/L, ammonia nitrogen 6mg/L, filtrate namely gets trisodium phosphate 38.5g through 800 ℃ of burnings, content 98.7%, phosphorus containg substances transformation efficiency 98.4%.Reclaim simultaneously waste heat and solid in the incineration flue gas.
Embodiment 4
To containing chlorion 13.8%, add sodium hydroxide among the pmida98 mother liquor 1000g of total phosphorus 0.9%, make mother liquor pH regulator to 12 after, multiple-effect evaporation is concentrated into 90% of former weight, filters, and filter cake is removed organism through washing, namely get sodium-chlor 227.04g, the chlorion transformation efficiency is 99.8%, and waste water is COD 10mg/L after biochemical treatment, TP 0.1mg/L, ammonia nitrogen 5mg/L, filtrate namely gets trisodium phosphate 38.6g through 900 ℃ of burnings, content 99.6%., phosphorus containg substances transformation efficiency 99.6%.Waste heat and solid in the while recovered flue gas.
Embodiment 5
To containing chlorion 13.8%, add solid potassium hydroxide among the pmida98 mother liquor 1000g of total phosphorus 0.9%, make mother liquor pH regulator to 10.5 after, multiple-effect evaporation is concentrated into 75% of former weight, filters, and filter cake is removed a small amount of organism through washing, namely get Repone K 284.4g, the chlorion transformation efficiency is 98.1%, and waste water is COD 12mg/L after biochemical treatment, TP 0.4mg/L, ammonia nitrogen 8mg/L, filtrate namely gets potassium pyrophosphate 47.8g through 750 ℃ of burnings, content 98.3%, phosphorus containg substances transformation efficiency 98.1%.Waste heat and solid in the while recovered flue gas.
Embodiment 6
To containing chlorion 13.8%, add the solid hydrogen calcium oxide among the pmida98 mother liquor 1000g of total phosphorus 0.9%, make mother liquor pH regulator to 10.5 after, multiple-effect evaporation is concentrated into 75% of former weight, filters, and filter cake is removed a small amount of organism through washing, namely get calcium chloride 211.8g, the chlorion transformation efficiency is 98.2%, and waste water is COD 15mg/L after biochemical treatment, TP 0.3mg/L, ammonia nitrogen 7mg/L, filtrate namely gets Calcium Pyrophosphate 36.8g through 650 ℃ of burnings, content 98.4%, phosphorus containg substances transformation efficiency 98.1%.Waste heat and solid in the while recovered flue gas.
Embodiment 7
To containing chlorion 13.8%, add solid oxidation calcium among the pmida98 mother liquor 1000g of total phosphorus 0.9%, make mother liquor pH regulator to 10.5 after, multiple-effect evaporation is concentrated into 75% of former weight, filters, and filter cake is removed a small amount of organism through washing, namely get calcium chloride 212.4g, the chlorion transformation efficiency is 98.4%, and waste water is COD 17mg/L after biochemical treatment, TP 0.4mg/L, ammonia nitrogen 8mg/L, filtrate namely gets Calcium Pyrophosphate 36.9g through 850 ℃ of burnings, content 98.3%, phosphorus containg substances transformation efficiency 98.3%.Waste heat and solid in the while recovered flue gas.

Claims (5)

CN201210384858.3A2012-10-122012-10-12Method for treating N-Phosphonomethyl iminodiacetic acid (PMIDA) mother liquidActiveCN102874983B (en)

Priority Applications (1)

Application NumberPriority DateFiling DateTitle
CN201210384858.3ACN102874983B (en)2012-10-122012-10-12Method for treating N-Phosphonomethyl iminodiacetic acid (PMIDA) mother liquid

Applications Claiming Priority (1)

Application NumberPriority DateFiling DateTitle
CN201210384858.3ACN102874983B (en)2012-10-122012-10-12Method for treating N-Phosphonomethyl iminodiacetic acid (PMIDA) mother liquid

Publications (2)

Publication NumberPublication Date
CN102874983Atrue CN102874983A (en)2013-01-16
CN102874983B CN102874983B (en)2014-03-19

Family

ID=47476547

Family Applications (1)

Application NumberTitlePriority DateFiling Date
CN201210384858.3AActiveCN102874983B (en)2012-10-122012-10-12Method for treating N-Phosphonomethyl iminodiacetic acid (PMIDA) mother liquid

Country Status (1)

CountryLink
CN (1)CN102874983B (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication numberPriority datePublication dateAssigneeTitle
CN103342398A (en)*2013-07-172013-10-09山东潍坊润丰化工有限公司Method for recovering high-purity organic salt from phosphorous-containing industrial wastewater
CN104150668A (en)*2014-07-302014-11-19常州市康瑞化工有限公司Method for multiple-effect evaporation treatment of chemical mother solution wastewater
CN104591424A (en)*2014-03-142015-05-06山东潍坊润丰化工股份有限公司IDA method glyphosate wastewater resource treatment method
CN105016515A (en)*2015-06-182015-11-04浙江新安化工集团股份有限公司Treatment method of phosphorus-containing waste produced during glufosinate ammonium production process
CN105440074A (en)*2014-09-302016-03-30北京紫光英力化工技术有限公司Recycling method for mother liquor of N-(phosphonomethyl)iminodiacetic acid
CN108059140A (en)*2018-01-232018-05-22浙江新安化工集团股份有限公司A kind of method for preparing industry trisodium phosphate using glyphosate production waste material one-step method

Citations (5)

* Cited by examiner, † Cited by third party
Publication numberPriority datePublication dateAssigneeTitle
CN1422275A (en)*2000-04-142003-06-04美国陶氏益农公司Removal of chloride from phosphonomethyliminodiacetic acid process
US6641741B2 (en)*2001-04-132003-11-04Dow Agrosciences LlcRemoval and recovery of chloride from phosphonomethyliminodiacetic acid process brine
CN101428935A (en)*2008-11-282009-05-13四川贝尔实业有限责任公司Treatment process for wastewater from N-(Phosphonomethyl)iminodiacetic acid production
CN102079605A (en)*2010-12-232011-06-01北京拓峰科技开发有限责任公司Novel process for zero discharge of glyphosate production waste water
CN102616914A (en)*2011-01-312012-08-01浙江新安化工集团股份有限公司Treatment method of phosphorus-containing waste from pesticide production and product obtained thereby

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication numberPriority datePublication dateAssigneeTitle
CN1422275A (en)*2000-04-142003-06-04美国陶氏益农公司Removal of chloride from phosphonomethyliminodiacetic acid process
US6641741B2 (en)*2001-04-132003-11-04Dow Agrosciences LlcRemoval and recovery of chloride from phosphonomethyliminodiacetic acid process brine
CN101428935A (en)*2008-11-282009-05-13四川贝尔实业有限责任公司Treatment process for wastewater from N-(Phosphonomethyl)iminodiacetic acid production
CN102079605A (en)*2010-12-232011-06-01北京拓峰科技开发有限责任公司Novel process for zero discharge of glyphosate production waste water
CN102616914A (en)*2011-01-312012-08-01浙江新安化工集团股份有限公司Treatment method of phosphorus-containing waste from pesticide production and product obtained thereby

Cited By (9)

* Cited by examiner, † Cited by third party
Publication numberPriority datePublication dateAssigneeTitle
CN103342398A (en)*2013-07-172013-10-09山东潍坊润丰化工有限公司Method for recovering high-purity organic salt from phosphorous-containing industrial wastewater
CN103342398B (en)*2013-07-172015-03-25山东潍坊润丰化工股份有限公司Method for recovering high-purity organic salt from phosphorous-containing industrial wastewater
CN104591424A (en)*2014-03-142015-05-06山东潍坊润丰化工股份有限公司IDA method glyphosate wastewater resource treatment method
CN104150668A (en)*2014-07-302014-11-19常州市康瑞化工有限公司Method for multiple-effect evaporation treatment of chemical mother solution wastewater
CN105440074A (en)*2014-09-302016-03-30北京紫光英力化工技术有限公司Recycling method for mother liquor of N-(phosphonomethyl)iminodiacetic acid
CN105440074B (en)*2014-09-302018-05-22北京紫光英力化工技术有限公司A kind of method that pmida Recycling Mother Solution is applied mechanically
CN105016515A (en)*2015-06-182015-11-04浙江新安化工集团股份有限公司Treatment method of phosphorus-containing waste produced during glufosinate ammonium production process
CN108059140A (en)*2018-01-232018-05-22浙江新安化工集团股份有限公司A kind of method for preparing industry trisodium phosphate using glyphosate production waste material one-step method
CN108059140B (en)*2018-01-232020-02-18浙江新安化工集团股份有限公司Method for preparing industrial trisodium phosphate by using glyphosate production waste through one-step method

Also Published As

Publication numberPublication date
CN102874983B (en)2014-03-19

Similar Documents

PublicationPublication DateTitle
CN102874983B (en)Method for treating N-Phosphonomethyl iminodiacetic acid (PMIDA) mother liquid
Lei et al.Is there a precipitation sequence in municipal wastewater induced by electrolysis?
CN102874786A (en)Processing method of glyphosate mother liquor
CN102616914B (en)Treatment method of phosphorus-containing waste from pesticide production and product obtained thereby
CN103964622B (en)A kind of comprehensive treating process of industrial organophosphorus waste liquid and resource utilization method
CN105540960B (en)The processing method and system of limestone/lime-gypsum method flue gas desulfurization waste-water
CN101428935B (en) Treatment method of diglyphosate production wastewater
WO2016205303A1 (en)Carbon dioxide capture and storage electrolytic methods
CN109205876B (en)Method and device for treating desulfurization wastewater
CN104140174A (en)Combined treatment method for ammonia chloride waste water through rare earth extraction separation
CN101838288A (en)Processing method of glyphosate mother liquor
CN106082515B (en)A kind of incineration treatment technology of glyphosate mother solution
CN101985426B (en)Method for treating glyphosate mother solution
CN103224261B (en)Method for extracting inorganic salt in industrial wastewater and method for recycling industrial wastewater
WO2011143610A2 (en)Process and system for recovering phosphorus from wastewater
CN105417795A (en)Desulfurization waste water zero discharging treatment process for coal-fired power plant
CN102115281B (en)Method for pretreating wastewater generated in production of N-(Phosphonomethyl) iminodiaceticacid (PMIDA)
CN103435222B (en)Method for treating flourescent brightener wastewater with phosphorus
CN214611993U (en)Mine strong brine zero release processing system
CN213977333U (en)Zero-discharge treatment system for boiler desulfurization wastewater
CN105016515A (en)Treatment method of phosphorus-containing waste produced during glufosinate ammonium production process
CN105565342A (en)Refining agent for refining primary brine in chlorine alkali industry and application of refining agent
CN106116705B (en)A kind of many class resourcesization recycling integrated technique of glyphosate mother solution
CN103936192B (en)High-concentration ammonia-nitrogen wastewater treatment process
CN109824194A (en)A kind of processing method of high COD organic wastewater with high salt

Legal Events

DateCodeTitleDescription
C06Publication
PB01Publication
C10Entry into substantive examination
SE01Entry into force of request for substantive examination
C53Correction of patent of invention or patent application
CB02Change of applicant information

Address after:Haiyuan Binhai Economic Development Zone, Shandong province Weifang city 262737 Street No. 600

Applicant after:Shandong Weifang Rainbow Chemical Co., Ltd.

Address before:Haiyuan Binhai Economic and Technological Development Zone in Shandong province Weifang City 600 street 262737 No. 1 ranked No. 1

Applicant before:Shandong Weifang Rainbow Chemical Co., Ltd.

GR01Patent grant
GR01Patent grant
CP02Change in the address of a patent holder
CP02Change in the address of a patent holder

Address after:No. 03001, chlor alkali Road, Weifang Coastal Economic Development Zone, Shandong, Shandong

Patentee after:Shandong Weifang Rainbow Chemical Co.,Ltd.

Address before:Haiyuan Binhai Economic Development Zone, Shandong province Weifang city 262737 Street No. 600

Patentee before:Shandong Weifang Rainbow Chemical Co.,Ltd.


[8]ページ先頭

©2009-2025 Movatter.jp