WO2018039848A1 - Recovery process for tetrahydrofuran - Google Patents
Recovery process for tetrahydrofuran Download PDFInfo
- Publication number
- WO2018039848A1 WO2018039848A1 PCT/CN2016/097112 CN2016097112W WO2018039848A1 WO 2018039848 A1 WO2018039848 A1 WO 2018039848A1 CN 2016097112 W CN2016097112 W CN 2016097112W WO 2018039848 A1 WO2018039848 A1 WO 2018039848A1
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- WO
- WIPO (PCT)
- Prior art keywords
- tetrahydrofuran
- oil
- vacuum pump
- water content
- solution
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- 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.)
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D3/00—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
- B01D3/34—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping with one or more auxiliary substances
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07D—HETEROCYCLIC COMPOUNDS
- C07D307/00—Heterocyclic compounds containing five-membered rings having one oxygen atom as the only ring hetero atom
- C07D307/02—Heterocyclic compounds containing five-membered rings having one oxygen atom as the only ring hetero atom not condensed with other rings
- C07D307/04—Heterocyclic compounds containing five-membered rings having one oxygen atom as the only ring hetero atom not condensed with other rings having no double bonds between ring members or between ring members and non-ring members
- C07D307/06—Heterocyclic compounds containing five-membered rings having one oxygen atom as the only ring hetero atom not condensed with other rings having no double bonds between ring members or between ring members and non-ring members with only hydrogen atoms or radicals containing only hydrogen and carbon atoms, directly attached to ring carbon atoms
- C07D307/08—Preparation of tetrahydrofuran
Definitions
- the invention relates to a compound herbicide, belonging to the field of chemical substance recovery and treatment.
- Tetrahydrofuran is an organic solvent with excellent performance and is widely used in pharmaceutical and chemical production.
- the industrial waste liquid produced by the pharmaceutical and chemical production of tetrahydrofuran is processed by atmospheric distillation. Since tetrahydrofuran is difficult to be separated from water by azeotropy, it cannot be directly used for production; if the waste liquid is directly discharged into the sewage treatment system, It has increased the difficulty of sewage treatment, polluting the environment, and causing waste of resources.
- a variety of tetrahydrofuran recovery treatment processes have been developed in the prior art, but these processes are complicated in process, long in time and low in efficiency. Therefore, it is urgent to develop a compound herbicide with simple process, short time and high efficiency. Upon search, no technical solutions identical or similar to the present invention were found.
- the technical problem to be solved by the present invention is to provide a compound herbicide which is simple in process, short in time and high in efficiency.
- the technical solution of the present invention is: a compounding herbicide, and the innovation is that the recycling process is as follows:
- a liquid moisture detector is arranged in the vacuum distiller to detect the water content in the solution, and when the moisture is less than 5%, the operation can be stopped.
- the invention discloses a compound herbicide, and the recycling process is as follows:
- the recovery time of tetrahydrofuran in this example requires a total of 55 minutes.
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- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
Description
技术领域Technical field
本发明涉及一种复配除草剂,属于化学物质回收处理领域。The invention relates to a compound herbicide, belonging to the field of chemical substance recovery and treatment.
背景技术Background technique
四氢呋喃是一种性能优良的有机溶剂,在医药化工生产中广泛使用。以四氢呋喃为原料的医药化工生产所产生的工业废液,通过常压精馏处理,由于四氢呋喃与水共沸难以分离,不能直接用于生产使用;如将这些废液直接排入污水处理系统,加大了污水处理难度,污染环境,又造成资源的浪费。现有技术中研制了多种四氢呋喃的回收处理工艺,但是这些工艺处理过程复杂,时间长且效率低,因此急需研制一种工艺处理过程简单、时间短且效率高的一种复配除草剂,经检索,未发现与本发明相同或相似的技术方案。Tetrahydrofuran is an organic solvent with excellent performance and is widely used in pharmaceutical and chemical production. The industrial waste liquid produced by the pharmaceutical and chemical production of tetrahydrofuran is processed by atmospheric distillation. Since tetrahydrofuran is difficult to be separated from water by azeotropy, it cannot be directly used for production; if the waste liquid is directly discharged into the sewage treatment system, It has increased the difficulty of sewage treatment, polluting the environment, and causing waste of resources. A variety of tetrahydrofuran recovery treatment processes have been developed in the prior art, but these processes are complicated in process, long in time and low in efficiency. Therefore, it is urgent to develop a compound herbicide with simple process, short time and high efficiency. Upon search, no technical solutions identical or similar to the present invention were found.
发明内容Summary of the invention
本发明要解决的技术问题是提供一种工艺处理过程简单、时间短且效率高的一种复配除草剂。The technical problem to be solved by the present invention is to provide a compound herbicide which is simple in process, short in time and high in efficiency.
为解决上述技术问题,本发明的技术方案为:一种复配除草剂,其创新点在于:所述回收工艺具体如下:In order to solve the above technical problem, the technical solution of the present invention is: a compounding herbicide, and the innovation is that the recycling process is as follows:
(1)测试制备得到的四氢呋喃的浓度,当其含水量大于10%时,将四氢呋喃倒入无油真空泵中进行抽真空处理;(1) testing the concentration of the prepared tetrahydrofuran, when the water content is greater than 10%, the tetrahydrofuran is poured into an oil-free vacuum pump for vacuum treatment;
(2)向无油真空泵中加入高锰酸钾,边搅拌边进行氧化处理,搅拌时间控制为5min;(2) adding potassium permanganate to the oil-free vacuum pump, and performing oxidation treatment while stirring, the stirring time is controlled to 5 min;
(3)向氧化完成的溶液中添加催化剂,在50℃的温度下反应30min;(3) adding a catalyst to the oxidized solution, and reacting at a temperature of 50 ° C for 30 min;
(4)将溶液倒入减压蒸馏器中进行减压蒸馏,收集90%的馏分,最终得到含水量小于5%的四氢呋喃。(4) The solution was poured into a vacuum distiller for distillation under reduced pressure, and 90% of the fraction was collected to finally obtain tetrahydrofuran having a water content of less than 5%.
本发明的优点在于:The advantages of the invention are:
(1)加入特殊氧化剂,使得四氢呋喃中易氧化性指标符合质量标准,减少了蒸馏次数,降低了能耗;使用无油真空泵抽真空,得到洁净的尾气,增加尾气回收系统冷凝回收四氢呋喃,减少了污染排放,前述操作相互协同配合,最终提高了四氢呋喃的回收收率。(1) Adding a special oxidant to make the oxidizing index in tetrahydrofuran meet the quality standard, reducing the number of distillations and reducing the energy consumption; using an oil-free vacuum pump to vacuum, obtaining clean exhaust gas, and increasing the tail gas recovery system to recover and recover tetrahydrofuran, reducing The pollution discharge, the aforementioned operations cooperate with each other, and finally improve the recovery yield of tetrahydrofuran.
(2)溶液中加入催化剂,加快溶液的蒸馏速度,提高回收处理的效率。(2) Adding a catalyst to the solution accelerates the distillation speed of the solution and improves the efficiency of the recovery treatment.
(3)减压蒸馏器中设置一液体水分检测仪,可检测溶液中的含水量,当水分低于5%时,即可停止操作。(3) A liquid moisture detector is arranged in the vacuum distiller to detect the water content in the solution, and when the moisture is less than 5%, the operation can be stopped.
具体实施方式detailed description
实施例1 Example 1
本发明公开了一种一种复配除草剂,该回收工艺具体如下:The invention discloses a compound herbicide, and the recycling process is as follows:
(1)测试制备得到的四氢呋喃的浓度,当其含水量大于10%时,将四氢呋喃倒入无油真空泵中进行抽真空处理;(1) testing the concentration of the prepared tetrahydrofuran, when the water content is greater than 10%, the tetrahydrofuran is poured into an oil-free vacuum pump for vacuum treatment;
(2)向无油真空泵中加入高锰酸钾,其中高锰酸钾的加入量为四氢呋喃质量的0.02%,边搅拌边进行氧化处理,搅拌时间控制为1~5min;(2) adding potassium permanganate to the oil-free vacuum pump, wherein the potassium permanganate is added in an amount of 0.02% by mass of tetrahydrofuran, and is oxidized while stirring, and the stirring time is controlled to be 1 to 5 minutes;
(3)向氧化完成的溶液中添加二氧化锰,在20℃的温度下反应30~50min;(3) adding manganese dioxide to the oxidized solution, and reacting at a temperature of 20 ° C for 30 to 50 minutes;
(4)将溶液倒入安装有液体水分检测仪的减压蒸馏器中进行减压蒸馏,收集90%的馏分,最终得到含水量小于5%的四氢呋喃。(4) The solution was poured into a vacuum distiller equipped with a liquid moisture detector for vacuum distillation, and 90% of the fraction was collected to finally obtain tetrahydrofuran having a water content of less than 5%.
本实施例中四氢呋喃的回收时间共需55min。The recovery time of tetrahydrofuran in this example requires a total of 55 minutes.
Claims (1)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| PCT/CN2016/097112 WO2018039848A1 (en) | 2016-08-29 | 2016-08-29 | Recovery process for tetrahydrofuran |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| PCT/CN2016/097112 WO2018039848A1 (en) | 2016-08-29 | 2016-08-29 | Recovery process for tetrahydrofuran |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| WO2018039848A1 true WO2018039848A1 (en) | 2018-03-08 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| PCT/CN2016/097112 Ceased WO2018039848A1 (en) | 2016-08-29 | 2016-08-29 | Recovery process for tetrahydrofuran |
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| Country | Link |
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| WO (1) | WO2018039848A1 (en) |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1370774A (en) * | 2001-02-27 | 2002-09-25 | 天津药业集团有限公司 | Butylene oxide recovering process |
| CN101555238A (en) * | 2009-05-21 | 2009-10-14 | 广西万德药业股份有限公司 | Method for tetrahydrofuran recycling |
| CN101914077A (en) * | 2010-09-13 | 2010-12-15 | 东瑞(南通)医药科技有限公司 | Recovery process of tetrahydrofuran |
| CN102596926A (en) * | 2009-10-30 | 2012-07-18 | 株式会社日立工业设备技术 | Process and system for purification of tetrahydrofuran |
| CN103408514A (en) * | 2013-08-20 | 2013-11-27 | 江苏九天高科技股份有限公司 | Technique and device for recovering tetrahydrofuran by pervaporation method |
-
2016
- 2016-08-29 WO PCT/CN2016/097112 patent/WO2018039848A1/en not_active Ceased
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1370774A (en) * | 2001-02-27 | 2002-09-25 | 天津药业集团有限公司 | Butylene oxide recovering process |
| CN101555238A (en) * | 2009-05-21 | 2009-10-14 | 广西万德药业股份有限公司 | Method for tetrahydrofuran recycling |
| CN102596926A (en) * | 2009-10-30 | 2012-07-18 | 株式会社日立工业设备技术 | Process and system for purification of tetrahydrofuran |
| CN101914077A (en) * | 2010-09-13 | 2010-12-15 | 东瑞(南通)医药科技有限公司 | Recovery process of tetrahydrofuran |
| CN103408514A (en) * | 2013-08-20 | 2013-11-27 | 江苏九天高科技股份有限公司 | Technique and device for recovering tetrahydrofuran by pervaporation method |
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