CN106008349A - Crystallization treating technology for pyraclostrobin - Google Patents
Crystallization treating technology for pyraclostrobin Download PDFInfo
- Publication number
- CN106008349A CN106008349A CN201610525011.0A CN201610525011A CN106008349A CN 106008349 A CN106008349 A CN 106008349A CN 201610525011 A CN201610525011 A CN 201610525011A CN 106008349 A CN106008349 A CN 106008349A
- Authority
- CN
- China
- Prior art keywords
- pyraclostrobin
- solution
- crystallization
- transferred
- filtrate
- 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
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07D—HETEROCYCLIC COMPOUNDS
- C07D231/00—Heterocyclic compounds containing 1,2-diazole or hydrogenated 1,2-diazole rings
- C07D231/02—Heterocyclic compounds containing 1,2-diazole or hydrogenated 1,2-diazole rings not condensed with other rings
- C07D231/10—Heterocyclic compounds containing 1,2-diazole or hydrogenated 1,2-diazole rings not condensed with other rings having two or three double bonds between ring members or between ring members and non-ring members
- C07D231/14—Heterocyclic compounds containing 1,2-diazole or hydrogenated 1,2-diazole rings not condensed with other rings having two or three double bonds between ring members or between ring members and non-ring members with hetero atoms or with carbon atoms having three bonds to hetero atoms with at the most one bond to halogen, e.g. ester or nitrile radicals, directly attached to ring carbon atoms
- C07D231/18—One oxygen or sulfur atom
- C07D231/20—One oxygen atom attached in position 3 or 5
- C07D231/22—One oxygen atom attached in position 3 or 5 with aryl radicals attached to ring nitrogen atoms
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Saccharide Compounds (AREA)
Abstract
The invention discloses a crystallization treating technology for pyraclostrobin. The treating technology is characterized by comprising the following steps that 1, a pyraclostrobin crude solution is rectified, filtered and washed and then is transferred to a liquid storage device on a metering pump, the flow speed of the metering pump is set, the flowing-out solution is subjected to column separation through a silicagel column, column separation is repeatedly carried out for 3-4 times, and the separated solution is collected for high-pressure suction filtration; 2, an isopropanol solvent and normal heptane are used for crystallizing filtrate obtained after high-pressure suction filtration in the step 1; 3, centrifugal mother liquor is recycled, centrifugal solid is washed with water and dried, and therefore the purified pyraclostrobin can be obtained. By carrying out column separation on the roughly-treated filtrate, the purity of pyraclostrobin can be improved; the flow speed needed during column separation is controlled through the metering pump, and therefore the product purity is further improved; isopropanol and normal heptane are added during crystallization operation, and a crystallized crystal nucleus of pyraclostrobin can be formed at normal temperature.
Description
Technical field
The present invention relates to the crystallization treatment technique of a kind of pyraclostrobin.
Background technology
Pyraclostrobin is the methoxy acrylic bactericide having pyrrazole structure concurrently, 1993
Year is found by BASF Aktiengesellschaft, and calendar year 2001 registers and lists, and has been used for more than 100 at present
Plant on crop.2009, its sales volume reached 7.35 hundred million dollars, was only second to Fluoxastrobin, became
For world's second largest antibacterial.Pyraclostrobin wide spectrum, efficiently, toxicity low, raw to non-target
Thing safety, friendly to user and environment all safety, it is market in strobilurin series bactericidal agent
The staple product that prospect is preferable, patent will be expired.
Sum up to get up to be divided into two to the synthetic route of pyraclostrobin the most both at home and abroad:
Article 1, route is by ortho-methylnitrobenzene, first obtains adjacent nitrobenzyl through Benzylphosphonium Bromide
Bromine, o-nitrobenzyl bromide is condensed to yield 2-[(N-4-chlorobenzene with 1-(4-chlorphenyl)-3-hydroxypyrazoles
Base)-3-pyrazoles epoxide methyl] Nitrobenzol, then obtain N-hydroxy-n-2-[(N-4-through reduction
Chlorphenyl)-3-pyrazoles epoxide methyl]-aniline, then with methylchloroformate reaction obtains N-hydroxyl
-N-2-[(N-rubigan)-3-pyrazoles epoxide methyl] carbanilate, last and sulphuric acid
Dimethyl ester reaction obtains pyraclostrobin.
Article 2 route, by ortho-methylnitrobenzene, obtains o-methyl-phenyl-azanol through reduction,
Obtain N-hydroxy-n-toluidino methyl formate with methylchloroformate reaction again, then with sulphuric acid two
Methyl ester reaction obtains N-methoxy-. N-methyl phenylcarbamate.N-methoxyl group-N-first
Base phenylcarbamate obtains pyrazoles pyrazoles ether with 1-(4-chlorphenyl)-3-hydroxypyrazoles again
Bacterium ester.
The traditional method of mix reagent crystallization is when solvent degree is fine in certain solvent for Organic substance,
First carrying out heating for dissolving with this solvent of minimum, the another kind reheating dissolubility slightly worse is molten
Agent, reduces this organic dissolubility, and then cooling separates out crystal.Or at reflux state
Lower with the solvent of minimal amount of favorable solubility by product dissolve, then add molten from condensing tube
The solvent that solution property is relatively low, to solution Hun Chi, then backflow is dripped clear, and cooling separates out.But this side
Method can make product crystallization not exclusively, and solvent recovery is not thorough, thus affects the yield of product, increases
Add post processing cost.
Summary of the invention
For the deficiencies in the prior art, the invention provides the crystallization treatment of a kind of pyraclostrobin
Technique.
The present invention can be achieved through the following technical solutions:
A kind of crystallization treatment technique of pyraclostrobin, it is characterised in that process technique include with
Lower step:
(1) pretreatment: by the pyraclostrobin crude product solution of 1 weight portion through rectification, filtration,
After washing, transferring in the device for storing liquid on dosing pump, the flow velocity arranging dosing pump is
10mL/min, the solution of outflow carried out post through silicagel column and separated, repeated post and separate 3-4
Secondary, regather the solution after separation and carry out high pressure sucking filtration;
(2) crystallization: the filtrate after step 1 high pressure sucking filtration is transferred to the knot of enamel material
In brilliant still, then it is slowly added dropwise isopropanol solvent, carries out stirring at normal temperature, when filtrate no longer presents oil
Shape, continues dropping isopropanol, and system is that yellow is muddy, then it is clear to drip several normal heptane backflows droplet,
Stopping stirring, stand and make system layering, upper strata is red, transparent liquid, and lower floor is yellow crystal
Solid;
(3) it is fully transferred in centrifuge be centrifuged by the material after layering in step 2,
Centrifuge mother liquor recycles in being transferred to disposing mother liquor still, and centrifugal solids is after washing and drying, i.e.
Available pyraclostrobin after purification.
The invention have the benefit that 1) divide by the filtrate after preliminary treatment was carried out post
From, the purity of pyraclostrobin can be improved;2) flow velocity during post was controlled by dosing pump,
The more thorough of magazins' layout can be made, thus improve product purity further;3) crystallization operation
Time, by adding isopropanol and normal heptane, the crystallization that can form pyraclostrobin under room temperature is brilliant
Core;4) disposing mother liquor still is used can to reclaim various solvent, it is achieved recycling of resource,
Cost-effective, the most environmentally friendly.
Detailed description of the invention:
By embodiment, the detailed description of the invention of the present invention is made an explanation below.
Embodiment
A kind of crystallization treatment technique of pyraclostrobin, it is characterised in that process technique include with
Lower step: (1) by the pyraclostrobin crude product solution of 1 weight portion through rectification, filter, wash
After, to transfer in the device for storing liquid on dosing pump, the flow velocity arranging dosing pump is 10mL/min,
The solution flowed out carried out post through silicagel column and separated, and repeated post and separates 3-4 time, at regulation stream
Speed descended post to separate, and can make the more thorough of magazins' layout, thus improve product pyraclostrobin
Purity, regather the solution after separation and carry out high pressure sucking filtration;(2) by step 1 high pressure sucking filtration
After filtrate be transferred in the crystallization kettle of enamel material, then be slowly added dropwise isopropanol solvent, enter
Row stirring at normal temperature, when filtrate no longer presents oily, continues dropping isopropanol, and system is that yellow is muddy
Turbid, then drip several normal heptane, stopping stirring, stand and make system layering, upper strata is red saturating
Prescribed liquid, lower floor is yellow crystalline solid;(3) material after layering in step 2 is all turned
Moving to be centrifuged in centrifuge, centrifuge mother liquor recycles in being transferred to disposing mother liquor still, from
Heart solid, after washing and drying, i.e. can get pyraclostrobin after purification.
The invention have the benefit that 1) divide by the filtrate after preliminary treatment was carried out post
From, the purity of pyraclostrobin can be improved;2) flow velocity during post was controlled by dosing pump,
The more thorough of magazins' layout can be made, thus improve product purity further;3) crystallization operation
Time, by adding isopropanol and normal heptane, the crystallization that can form pyraclostrobin under room temperature is brilliant
Core;4) disposing mother liquor still is used can to reclaim various solvent, it is achieved recycling of resource,
Cost-effective, the most environmentally friendly.
Claims (1)
1. the crystallization treatment technique of a pyraclostrobin, it is characterised in that process technique bag
Include following steps:
(1) pretreatment: by the pyraclostrobin crude product solution of 1 weight portion through rectification, filtration,
After washing, transferring in the device for storing liquid on dosing pump, the flow velocity arranging dosing pump is
10mL/min, the solution of outflow carried out post through silicagel column and separated, repeated post and separate 3-4
Secondary, regather the solution after separation and carry out high pressure sucking filtration;
(2) crystallization: the filtrate after step 1 high pressure sucking filtration is transferred to the knot of enamel material
In brilliant still, then it is slowly added dropwise isopropanol solvent, carries out stirring at normal temperature, when filtrate no longer presents oil
Shape, continues dropping isopropanol, and system is that yellow is muddy, then drips several normal heptane, stops stirring
Mixing, stand and make system layering, upper strata is red, transparent liquid, and lower floor is yellow crystalline solid;
(3) it is fully transferred in centrifuge be centrifuged by the material after layering in step 2,
Centrifuge mother liquor recycles in being transferred to disposing mother liquor still, and centrifugal solids is after washing and drying, i.e.
Available pyraclostrobin after purification.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201610525011.0A CN106008349A (en) | 2016-07-02 | 2016-07-02 | Crystallization treating technology for pyraclostrobin |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201610525011.0A CN106008349A (en) | 2016-07-02 | 2016-07-02 | Crystallization treating technology for pyraclostrobin |
Publications (1)
Publication Number | Publication Date |
---|---|
CN106008349A true CN106008349A (en) | 2016-10-12 |
Family
ID=57106582
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201610525011.0A Pending CN106008349A (en) | 2016-07-02 | 2016-07-02 | Crystallization treating technology for pyraclostrobin |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN106008349A (en) |
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106243040A (en) * | 2016-07-28 | 2016-12-21 | 山东康乔生物科技有限公司 | A kind of pyraclostrobin novel crystal forms V and preparation method thereof |
CN106543066A (en) * | 2016-11-11 | 2017-03-29 | 深圳市新阳唯康科技有限公司 | A kind of pyraclostrobin novel crystal forms and preparation method thereof |
CN106631965A (en) * | 2016-12-21 | 2017-05-10 | 深圳市新阳唯康科技有限公司 | Novel pyraclostrobin crystal form and preparation method thereof |
CN106866533A (en) * | 2017-03-28 | 2017-06-20 | 天津大学 | Pyraclostrobin crystal formation and preparation method |
CN106928144A (en) * | 2017-03-16 | 2017-07-07 | 上海晓明检测技术服务有限公司 | A kind of preparation method of high-purity pyraclostrobin standard items |
CN107021927A (en) * | 2017-03-28 | 2017-08-08 | 天津大学 | A kind of pyraclostrobin crystal formation and preparation method thereof |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102399190A (en) * | 2011-12-20 | 2012-04-04 | 河南中医学院 | Pyraclostrobin and method for economically synthesizing same |
CN104211641A (en) * | 2014-08-19 | 2014-12-17 | 山东康乔生物科技有限公司 | Synthetic technology for pyraclostrobin |
CN105218450A (en) * | 2015-11-06 | 2016-01-06 | 江苏托球农化股份有限公司 | A kind of green production process of pyraclostrobin |
-
2016
- 2016-07-02 CN CN201610525011.0A patent/CN106008349A/en active Pending
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102399190A (en) * | 2011-12-20 | 2012-04-04 | 河南中医学院 | Pyraclostrobin and method for economically synthesizing same |
CN104211641A (en) * | 2014-08-19 | 2014-12-17 | 山东康乔生物科技有限公司 | Synthetic technology for pyraclostrobin |
CN105218450A (en) * | 2015-11-06 | 2016-01-06 | 江苏托球农化股份有限公司 | A kind of green production process of pyraclostrobin |
Non-Patent Citations (1)
Title |
---|
王陈敏: "吡唑醚菌酯的合成研究", 《南京理工大学硕士学位论文》 * |
Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106243040A (en) * | 2016-07-28 | 2016-12-21 | 山东康乔生物科技有限公司 | A kind of pyraclostrobin novel crystal forms V and preparation method thereof |
CN106543066A (en) * | 2016-11-11 | 2017-03-29 | 深圳市新阳唯康科技有限公司 | A kind of pyraclostrobin novel crystal forms and preparation method thereof |
CN106543066B (en) * | 2016-11-11 | 2018-12-21 | 深圳市新阳唯康科技有限公司 | A kind of pyraclostrobin crystal form and preparation method thereof |
CN106631965A (en) * | 2016-12-21 | 2017-05-10 | 深圳市新阳唯康科技有限公司 | Novel pyraclostrobin crystal form and preparation method thereof |
CN106928144A (en) * | 2017-03-16 | 2017-07-07 | 上海晓明检测技术服务有限公司 | A kind of preparation method of high-purity pyraclostrobin standard items |
CN106866533A (en) * | 2017-03-28 | 2017-06-20 | 天津大学 | Pyraclostrobin crystal formation and preparation method |
CN107021927A (en) * | 2017-03-28 | 2017-08-08 | 天津大学 | A kind of pyraclostrobin crystal formation and preparation method thereof |
CN106866533B (en) * | 2017-03-28 | 2022-03-11 | 天津大学 | Pyraclostrobin crystal form and preparation method thereof |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN106008349A (en) | Crystallization treating technology for pyraclostrobin | |
CN105367557A (en) | Method for preparing cycloxylidin | |
JP4558870B2 (en) | Tower-type processing method and apparatus | |
CN109053492B (en) | Adiponitrile rectification and purification system and rectification and purification method thereof | |
CN108686397B (en) | Method for distilling dimethyl sulfoxide and multi-section distillation tower | |
CN108484442A (en) | A kind of process for purification of adiponitrile | |
CN106083722A (en) | A kind of Six Steps prepares the synthesis technique of pyrazoles Fluoxastrobin | |
CN110483337A (en) | A kind of separation and purification system and method for benzene dimethylene diisocyanate product | |
CN104557969A (en) | Production technique of clopidogrel hydrogen sulfate | |
CN108752415A (en) | A kind of Finasteride chiral impurity(5 β-Finasterides)Synthesis and purification process | |
CN103044323B (en) | A kind of purification process of SASP | |
CN107556213B (en) | A kind of technique of cyclohexanone oxamidinating and the technique for manufacturing caprolactam | |
CN110015986B (en) | 2-chloro-2-chloromethyl-4-cyano butyraldehyde cyclization device | |
CN204281332U (en) | A kind of continuous recovery isocyanic ester produces the device of high-content phosgene in tail gas | |
CN106928172A (en) | A kind of process for refining of dibenzofuran | |
CN106565519A (en) | Preparation method of diacetone acrylamide | |
CN106632312A (en) | Apixaban related substance, intermediate, preparation method and applications thereof | |
CN103796982B (en) | The preparation method of methacrylic acid and methacrylic ester | |
CN114272636A (en) | Device and method for separating ethylene glycol monomethyl ether and water through melt crystallization | |
CN211752616U (en) | Caprolactam device is refined in crystallization | |
CN107522718A (en) | A kind of synthetic method of Marbofloxacin | |
CN210595851U (en) | Alkane bromination reaction system | |
KR100433826B1 (en) | Solvent recovery facility by the combination of extraction and distillation | |
CN216273867U (en) | Acetone oxime's separation and purification device | |
CN111036149B (en) | Thiodicarb water washing continuous production process and device |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C06 | Publication | ||
PB01 | Publication | ||
C10 | Entry into substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
RJ01 | Rejection of invention patent application after publication |
Application publication date: 20161012 |
|
RJ01 | Rejection of invention patent application after publication |