CN105622666A - Glyphosate synthesis technology - Google Patents
Glyphosate synthesis technology Download PDFInfo
- Publication number
- CN105622666A CN105622666A CN201410620303.3A CN201410620303A CN105622666A CN 105622666 A CN105622666 A CN 105622666A CN 201410620303 A CN201410620303 A CN 201410620303A CN 105622666 A CN105622666 A CN 105622666A
- Authority
- CN
- China
- Prior art keywords
- reaction
- liquid
- glyphosate
- condensation
- depolymerization
- 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
Links
Landscapes
- Agricultural Chemicals And Associated Chemicals (AREA)
Abstract
The invention discloses a glyphosate synthesis technology. The glyphosate synthesis technology comprises a depolymerization reaction process, an addition reaction process, a condensation reaction process, a hydrolysis reaction process and a crystallization process. The glyphosate synthesis technology solves the problem that the glyphosate synthesis condensation reaction cannot occur under the waterless conditions. In the addition reaction and condensation reaction processes, the reaction liquid is dehydrated through a dehydration device so that reaction product moisture is reduced, dimethyl phosphite consumption is reduced, a reaction yield is improved, raw materials are saved and a cost is reduced.
Description
Technical field
The invention belongs to technical field of chemical synthesis, be specifically related to the synthesis technique of a kind of glyphosate.
Background technology
Glyphosate reaches also known as glyphosate, agriculture, careless dry phosphine, the sweet acid of phosphine. Sterling is non-volatile white solid, and proportion is 0.5, is approximately in about 230 DEG C fusings, and with decomposing. When 25 DEG C, the dissolubility in water is 1.2%, and insoluble in common organic solvents, its isopropyl amine salt is dissolved completely in water. Glyphosate is non-combustible, do not explode, and storage at normal temperature is stable, and medium carbon steel, tin plate (tinplate) are had corrosiveness. Glyphosate is usually used in preventing and kill off the weeds in apple orchard, vineyard and tea place. In current glyphosate synthesis process approach, technological process is not easy to implement, and the glyphosate finished product purity of generation is low, and reactant conversion per pass is low, and manufacturing process is complicated, and production efficiency is low and cost high, is not suitable for large-scale production.
Summary of the invention
For the above-mentioned technical problem overcoming prior art to exist, it is an object of the invention to, it is provided that the synthesis technique of a kind of glyphosate, the present invention not only manufacturing process is simple, improve work efficiency, and the glyphosate products purity generated is greatly, is suitable for industrialized production.
The synthesis technique of glyphosate provided by the invention, comprises the following steps:
(1) depolymerization reaction: methanol, triethylamine and paraformaldehyde are carried out depolymerization reaction 55-70 minute at 35-40 DEG C, obtains depolymerization liquid;
(2) additive reaction: after being cooled to 32-52 DEG C, adds glycine in depolymerization liquid and carries out additive reaction, react 15-25 minute and clarify to additive reaction liquid at 42-44 DEG C, solids disappeared;
(3) dehydration cycle processes the regeneration with dehydrant: while the additive reaction liquid of clarification is proceeded additive reaction, processes with 3A or 4A molecular sieve dehydration cycle, obtains dehydration addition liquid; The nitrogen of 100-350 DEG C of 3A or 4A molecular sieve carries out Regeneration Treatment, the condensed recovery methanol of nitrogen after process and triethylamine, tail gas emptying process;
(4) condensation reaction: add dimethylphosphite in dehydration addition liquid, condensation reaction is carried out at 52-54 DEG C, condensation reaction solution is carried out the dehydration cycle described in step (3) simultaneously and processes the regeneration with dehydrant by reaction, react 50-100 minute, condensation reaction completes, and obtains dehydrating condensation liquid;
(5) hydrolysis; Adding mass fraction content after dehydrating condensation liquid is cooled to less than 25 DEG C is the hydrochloric acid of 28-32%;
(6) crystallization: temperature is down to less than 30 DEG C, spontaneous nucleation at least 4 hours, filters, washing, dry obtains glyphosate.
The synthesis technique of glyphosate provided by the invention, it has the beneficial effects that, overcoming prior art, to prepare operation in glyphosate technical process more, and the problem that workload is big improves work efficiency; Improve the conversion per pass of reactant and the productivity of product.
Detailed description of the invention
Below in conjunction with an embodiment, the synthesis technique of glyphosate provided by the invention is described in detail.
Embodiment
The synthesis technique of the glyphosate of the present embodiment, comprises the following steps:
(1) depolymerization reaction: methanol, triethylamine and paraformaldehyde are carried out depolymerization reaction 55 minutes at 40 DEG C, obtains depolymerization liquid;
(2) additive reaction: after being cooled to 52 DEG C, adds glycine in depolymerization liquid and carries out additive reaction, react 25 minutes and clarify to additive reaction liquid at 42 DEG C, solids disappeared;
(3) dehydration cycle processes the regeneration with dehydrant: while the additive reaction liquid of clarification is proceeded additive reaction, processes with 3A or 4A molecular sieve dehydration cycle, obtains dehydration addition liquid; 3A or 4A molecular sieve carries out Regeneration Treatment with the nitrogen of 250 DEG C, the condensed recovery methanol of nitrogen after process and triethylamine, tail gas emptying process;
(4) condensation reaction: add dimethylphosphite in dehydration addition liquid, carrying out condensation reaction at 54 DEG C, condensation reaction solution is carried out the dehydration cycle described in step (3) simultaneously and processes the regeneration with dehydrant by reaction, reacts 100 minutes, condensation reaction completes, and obtains dehydrating condensation liquid;
(5) hydrolysis; Be cooled to by dehydrating condensation liquid after 20 DEG C adding mass fraction content is the hydrochloric acid of 32%;
(6) crystallization: temperature is down to 20 DEG C, spontaneous nucleation 4 hours, filters, washing, dry obtains glyphosate.
The synthesis technique of glyphosate, it is not necessary to loaded down with trivial details post-reaction treatment, operation simple possible, and also environmentally friendly pollution-free, technological process is easy to implement, it is achieved that the industrialized production of product.
Claims (1)
1. the synthesis technique of a glyphosate, it is characterised in that: said method comprising the steps of:
(1) depolymerization reaction: methanol, triethylamine and paraformaldehyde are carried out depolymerization reaction 55-70 minute at 35-40 DEG C, obtains depolymerization liquid;
(2) additive reaction: after being cooled to 32-52 DEG C, adds glycine in depolymerization liquid and carries out additive reaction, react 15-25 minute and clarify to additive reaction liquid at 42-44 DEG C, solids disappeared;
(3) dehydration cycle processes the regeneration with dehydrant: while the additive reaction liquid of clarification is proceeded additive reaction, processes with 3A or 4A molecular sieve dehydration cycle, obtains dehydration addition liquid; The nitrogen of 100-350 DEG C of 3A or 4A molecular sieve carries out Regeneration Treatment, the condensed recovery methanol of nitrogen after process and triethylamine, tail gas emptying process;
(4) condensation reaction: add dimethylphosphite in dehydration addition liquid, condensation reaction is carried out at 52-54 DEG C, condensation reaction solution is carried out the dehydration cycle described in step (3) simultaneously and processes the regeneration with dehydrant by reaction, react 50-100 minute, condensation reaction completes, and obtains dehydrating condensation liquid;
(5) hydrolysis; Adding mass fraction content after dehydrating condensation liquid is cooled to less than 25 DEG C is the hydrochloric acid of 28-32%;
(6) crystallization: temperature is down to less than 30 DEG C, spontaneous nucleation at least 4 hours, filters, washing, dry obtains glyphosate.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201410620303.3A CN105622666A (en) | 2014-11-07 | 2014-11-07 | Glyphosate synthesis technology |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201410620303.3A CN105622666A (en) | 2014-11-07 | 2014-11-07 | Glyphosate synthesis technology |
Publications (1)
Publication Number | Publication Date |
---|---|
CN105622666A true CN105622666A (en) | 2016-06-01 |
Family
ID=56038048
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201410620303.3A Pending CN105622666A (en) | 2014-11-07 | 2014-11-07 | Glyphosate synthesis technology |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN105622666A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106279273A (en) * | 2016-08-13 | 2017-01-04 | 安徽东至广信农化有限公司 | A kind of production technology of glyphosate technicals |
CN107325126A (en) * | 2017-07-13 | 2017-11-07 | 安徽东至广信农化有限公司 | A kind of acidizing process of glyphosate production technique |
CN113402549A (en) * | 2021-07-14 | 2021-09-17 | 安徽东至广信农化有限公司 | Preparation method of glyphosate technical |
-
2014
- 2014-11-07 CN CN201410620303.3A patent/CN105622666A/en active Pending
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106279273A (en) * | 2016-08-13 | 2017-01-04 | 安徽东至广信农化有限公司 | A kind of production technology of glyphosate technicals |
CN107325126A (en) * | 2017-07-13 | 2017-11-07 | 安徽东至广信农化有限公司 | A kind of acidizing process of glyphosate production technique |
CN113402549A (en) * | 2021-07-14 | 2021-09-17 | 安徽东至广信农化有限公司 | Preparation method of glyphosate technical |
CN113402549B (en) * | 2021-07-14 | 2024-05-31 | 安徽东至广信农化有限公司 | Preparation method of glyphosate raw medicine |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
RU2591703C2 (en) | Method for preparation of 3,3-dimethylbutyraldehyde | |
CN108530404B (en) | Method for co-producing furfural, cellulose and lignin by depolymerizing biomass | |
JP5579192B2 (en) | Process for producing a compound having a nitrile group | |
CN109721545B (en) | Preparation method of azoxystrobin intermediate | |
CN103467245B (en) | Method for complexing and removing water contained in ethanol and water mixed solution by utilizing eutectic solvent | |
CN105622666A (en) | Glyphosate synthesis technology | |
CN105498801A (en) | Preparation method of sulfated carbonized corn cob catalyst and method for preparing furfural from xylose in presence of catalyst | |
EP3587431A1 (en) | Method for preparing levoglucosenone by catalytic pyrolysis of biomass | |
KR101140649B1 (en) | Process for preparing alkyl lactate from fermentation-derived ammonium lactate | |
CN101993455B (en) | Glyphosate synthesis process | |
CN111574358A (en) | Preparation process of potassium diformate | |
CN104262390A (en) | Continuous production method of high-efficiency and low-toxicity pesticide-acephate | |
CN104892444A (en) | Method for synthesizing D-p-hydroxyphenylglycine methyl ester | |
JP2017534660A (en) | Process for obtaining formate from reaction mixture | |
CN102321489B (en) | Method for catalyzing and liquefying agricultural wastes by using ion liquid | |
CN101704842A (en) | Process for preparing glyphosate by using glycine | |
CN104072369B (en) | A kind of technique preparing Diisopropyl malonate | |
CN105523783A (en) | Method for producing high-additional value chemical co-production slow release fertilizer by straws | |
CN102924346B (en) | Method for synthesizing methyl sulfone base dibromo toluene | |
CN105461580A (en) | Synthesis method of metolachlor | |
CN102757367A (en) | Splitting process of racemic ethyl benzene sulfonic acid | |
CN102766160A (en) | Novel process for preparing glyphosate by utilizing glycine method | |
CN103012475B (en) | A kind of preparation method of glyphosate | |
CN104058930A (en) | Method for synthesizing sorbic acid through real-time splitting decomposition of acetic acid | |
CN103467324A (en) | Preparation method of N, N-dimethylglycine for industrial production |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C06 | Publication | ||
PB01 | Publication | ||
WD01 | Invention patent application deemed withdrawn after publication | ||
WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20160601 |