CN101519371B - Preparation method of cartap hydrochloride intermediate, i.e., 2-N, N-dimethyl-1, 3-dithio-cyano propane - Google Patents

Preparation method of cartap hydrochloride intermediate, i.e., 2-N, N-dimethyl-1, 3-dithio-cyano propane Download PDF

Info

Publication number
CN101519371B
CN101519371B CN200810062030XA CN200810062030A CN101519371B CN 101519371 B CN101519371 B CN 101519371B CN 200810062030X A CN200810062030X A CN 200810062030XA CN 200810062030 A CN200810062030 A CN 200810062030A CN 101519371 B CN101519371 B CN 101519371B
Authority
CN
China
Prior art keywords
dimethyl
thiocyanide
reaction
isomer
cartap
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.)
Active
Application number
CN200810062030XA
Other languages
Chinese (zh)
Other versions
CN101519371A (en
Inventor
沈新良
吴华龙
徐黎婷
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.)
Zhejiang Yulong Biotechnology Co., Ltd
Original Assignee
HANGZHOU UDRAGON 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 HANGZHOU UDRAGON CHEMICAL CO Ltd filed Critical HANGZHOU UDRAGON CHEMICAL CO Ltd
Priority to CN200810062030XA priority Critical patent/CN101519371B/en
Publication of CN101519371A publication Critical patent/CN101519371A/en
Application granted granted Critical
Publication of CN101519371B publication Critical patent/CN101519371B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Abstract

The invention relates to a preparation method for cartap hydrochloride intermediate, i.e., 2-N, N-dimethyl-1, 3-dithio-cyano propane, which takes 1-N, N-dimethyl-2, 3- propylamine dihalide, thiocyanate as the raw material, obtains the mixture of 2-N, N-dimethyl-1, 3-dithio-cyano propane and 3-N, N-dimethyl-1, 2-dithio-cyano propane by reaction with the existence of a solvent, and obtains 2-N, N-dimethyl-1, 3-dithio-cyano propane with high content by separation; simultaneously, 3-N, N-dimethyl-1, 2-dithio-cyano propane isomer participates the reaction circularly, thus having high yield, good product quality, small amount of three wastes, and better industrial application prospect.

Description

Cartap midbody 2-N, N-dimethyl--1, the preparation method of 3-dithiocyano propane
Technical field
The present invention relates to a kind of cartap midbody 2-N, N-dimethyl--1, the preparation method of 3-dithiocyano propane.
Technical background
2-N; N-dimethyl--1,3-dithiocyano propane (abbreviation thiocyanide) are the necessary midbodys of preparation sterilant cartap, US3332943, denomination of invention " carbamoylthio derivatives "; Relate to the method for preparing cartap by cartap midbody thiocyanide; And relate to positive structure body of midbody thiocyanide and isomer, and corresponding positive structure body of cartap and the cartap isomer of obtaining after the hydrolysis, structural formula is following:
Figure S200810062030XD00011
Formula A:2-N, N-dimethyl--1,3-dithiocyano propane (the positive structure body of thiocyanide); Formula B: the positive structure body of cartap
Figure S200810062030XD00012
Formula C:3-N, N-dimethyl--1,2-dithiocyano propane (thiocyanide isomer)
Formula D: cartap isomer
It almost all is positive structure body that the former medicine of the required cartap of existing market demand requires, and because of the disosultap of low levels has more isomer, it is lower to obtain thiocyanide content through cyanogenation, does not generally adopt.For obtaining high-load cartap, be through of the sodium cyanide reaction of high-load benthiocarb at present with severe toxicity, prepare cartap midbody thiocyanide earlier; The thiocyanide content that obtains like this is higher, almost all is positive structure body, obtains high-load cartap through hydrolysis then; Resulting cartap almost all is positive structure body; Useless cartap isomer impurities content is less, and higher advantage is arranged on the quality product, and reaction formula is following:
Figure S200810062030XD00013
But in preparation during thiocyanide, separating with hypertoxic sodium cyanide reaction solution, in the washing operation, not only having poor working environment, poison dangerous greatly, and produce a large amount of cyanide wastewater, processing cost is high.CN1060913C, denomination of invention " preparation method of cartap "; Disclose a kind of by improving one's methods for the feedstock production cartap such as benthiocarb, sodium cyanide, methyl alcohol, hydrogen chloride gas; Though in operation, improvement has been arranged, but has not avoided using the sodium cyanide raw material of severe toxicity.CN1830957A, denomination of invention " 2-N, N-dimethyl--1,3-two sulfhedryl propane new preparation processes " disclose a kind of with 1-N; N-dimethyl--2,3-dichloro-propyl-amine hydrochloride (abbreviation muriate) is a raw material, is neutralized into free alkali with alkali earlier; Add aromatic solvent according to a certain ratio, the proportioning of muriate and aromatic hydrocarbons is 1: 500-1000 (mol: L), drip the Sodium Thiocyanate 99 alcoholic solution for preparing; Reaction obtains 2-N, N-dimethyl--1,3-dithiocyano propane.Patent does not disclose the content of positive structure body of midbody thiocyanide and isomer; Low about 50%~60% through experiment showed, according to the positive structure body burden of patent CN1830957A gained midbody thiocyanide, gained cartap content is lower behind hydrolysis reaction; Contain more cartap isomer impurities; The positive structure body of cartap yield is lower, and gained cartap effective constituent is lower like this, does not have industrial applications to be worth.Adopt non-cyaniding route to synthesize thiocyanide; The more thiocyanide isomer of inevitable generation; Though can through change reaction conditions as: reduce measures such as temperature of reaction, improve the positive structure body burden of thiocyanide, the yield of thiocyanide can be lower; And the content of thiocyanide do not reach the requirement of doing high-load cartap yet, and product does not just have the industriallization meaning like this.In order to overcome above shortcoming, the present invention provides the preparation method of the thiocyanide of a kind of high-content, high yield, and quantity of three wastes is few, and process implementing is convenient, has the industrial applications prospect, and the gained thiocyanide obtains the cartap of the high yield of high-content through hydrolysis.
Summary of the invention
Purpose of design: avoid the weak point in the background technology, design a kind of cartap midbody 2-N of the thiocyanide of a kind of high-content, high yield, N-dimethyl--1, the preparation method of 3-dithiocyano propane.
Plan: in order to realize above-mentioned purpose of design.The present invention is with 1-N, N-dimethyl--2, and 3-dihalo propylamine is a raw material, structural formula is following:
Figure S200810062030XD00021
Wherein X is halogen (Cl; Br I) reacts the mixture (formula two) of the thiocyanide that obtains containing positive structure, isomery, according to conditions such as different solvents, reaction times in the presence of solvent with thiocyanate-; The positive structure body burden of thiocyanide is generally 40~80%, and structural formula is following:
Figure S200810062030XD00022
The thiocyanide mixture obtains the positive structure body of high-content thiocyanide through separation; The thiocyanide isomer of separating simultaneously returns next reaction system, and recycled is under processing condition of the present invention; Find that positive structure body of thiocyanide and isomer reach a running balance; The positive structure body of thiocyanide total recovery increases substantially like this, has also solved simultaneously the low levels thiocyanide and has got into next step hydrolysis reaction, converts the cartap isomer to and reduces yield; Reduce the shortcoming of quality product, have very high industriallization application prospect.
The raw materials used 1-N of the present invention, N-dimethyl--2,3-dihalo propylamine normally obtains aminate by propenyl chloride and n n dimetylaniline reaction; Through the acidifying salify, halogenation obtains corresponding 1-N again, N-dimethyl--2,3-dihalo propylamine hydrogen salt; Halogenation can be chlorination, bromination or iodate, is preferably chlorination, and the gained hydrochloride is neutralized into 1-N with alkali; N-dimethyl--2, the 3-dichloro-propyl-amine, directly or be used for the thiocyanation reaction after the layering.
The raw materials used thiocyanate-of the present invention, available Sodium Thiocyanate 99, Rhocya, ammonium thiocyanide etc. preferably use Sodium Thiocyanate 99.Thiocyanate-and 1-N, N-dimethyl--2, the consumption proportion of 3-dihalo propylamine are 2~3: 1 (mol ratio), and consumption is many to be improved not quite reaction yield, and optimum ratio is 2.0~2.5: 1 (mol ratio).
Described reaction solvent in the scope of the invention, available alcohols, as: methyl alcohol, ethanol, propyl alcohol, Virahol, butanols, isopropylcarbinol, sec-butyl alcohol etc.; The benzene class, as: benzene, toluene, ethylbenzene, YLENE, chlorobenzene etc.; The ester class, as: ETHYLE ACETATE, propyl acetate, butylacetate etc.; Ketone, as: acetone, butanone, pentanone etc.; Ethers: propyl ether, isopropyl ether, butyl ether etc.; Nitrile, as: acetonitrile, butyronitrile etc.; Halogenated hydrocarbon, as: ethylene dichloride, trichloromethane, tetracol phenixin etc.; The aprotic polar solvent class, as: N, DMSO 99.8MIN., THF, N-Methyl pyrrolidone etc.Solvent load is 1-N, N-dimethyl--2, and 1~10 times (weight) of 3-dihalo propylamine raw material, solvent is many with causing unnecessary loss, preferably uses 2~6 times (weight); Described separate sulfur prussiate carries out in solvent in the scope of the invention, is to utilize the thiocyanide isomer; Cooling back preferential crystallization is separated out in solvent, thereby separates the thiocyanide isomer earlier, and cover capable of circulation is used for reaction next time; The solvent filtrating that obtains after the separation is the positive structure body of high-load thiocyanide; According to different solvents, can from solvent, separate the positive structure body of thiocyanide and obtain the positive structure body of high-load thiocyanide product through freezing and crystallizing, the precipitation or add methods such as elutriation goes out of reducing pressure; Also can in solvent, directly be used for next step hydrolysis reaction.Described separation solvent in the scope of the invention can be with a kind of solvent with reaction solvent, also homogeneous solvent not; Solvent load is 1-N, N-dimethyl--2,1~10 times (weight) of 3-dihalo propylamine raw material; Solvent is many preferably to use 2~6 times (weight) with causing unnecessary loss, and the reaction back is steamed earlier and removed reaction solvent; Obtain the positive isomer mixture of thiocyanide, add another kind of solvent again and carry out Crystallization Separation, for simplifying the operation; The present invention reaction with separates solvent and preferably uses with a kind of solvent, alcohols, benzene class, ketones solvent especially are suitable as and react and separate solvent; The said temperature of reaction of the scope of the invention is carried out under 45~85 ℃, carries out under preferred 60~75 ℃; Reaction times is generally 2~10 hours (in 2~10 hours scopes value and comprise end value) arbitrarily; Reaction times is too short; Yield can reduce, and the reaction times is long, can produce some side reactions; Yield is corresponding can be reduced, preferred 3~6 hours (in 3~6 hours scopes value and comprise end value) arbitrarily.
Described preparation method in the scope of the invention, reaction system can allow the existence of water, helps the dissolving of thiocyanate-, can shorten the reaction times, but the water yield can influence reaction yield and product separating effect more for a long time; Reaction system can allow the existence of phase-transfer catalyst simultaneously, and the existence of phase-transfer catalyst can be shortened the reaction times.
The present invention compares with background technology, and the one, the positive structure body burden of gained thiocyanide >=98% has positive structure body yield height, and gained cartap product content >=98% has the industrial applications prospect after the hydrolysis; The 2nd, quantity of three wastes is few, and process implementing is convenient, has the industrial applications prospect, and the gained thiocyanide obtains the cartap of the high yield of high-content through hydrolysis.
Embodiment
Embodiment 1: drop into the 400g propyl carbinol in the reaction flask, Sodium Thiocyanate 99 115g, 110g content are 95% 1-N, N-dimethyl--2,3-dichloro-propyl-amine; Heat up 45~85 ℃ (in 45~85 ℃ of scopes value and comprise end value) arbitrarily, insulation reaction 5 hours, thiocyanide just, isomer proportion: positive structure body 51%; Isomer 48% filters the sodium-chlor inorganic salt that elimination generates, and crystallization is separated out in the filtrating cooling; Filtration obtains thiocyanide isomer solid crystal (positive structure body 5%, isomer 94%), the 57g that gives money as a gift, filtrating freezing and crystallizing; Filtration obtains the positive structure body of thiocyanide (positive structure body 97%, isomer 2%), the 54g that gives money as a gift, the positive structure body of thiocyanide yield 39%.
Embodiment 2: drop into the 400g propyl carbinol in the reaction flask, and embodiment 1 gained isomer 57g, Sodium Thiocyanate 99 58g, 55g content are 95% 1-N; N-dimethyl--2, the 3-dichloro-propyl-amine, 45~85 ℃ (in 45~85 ℃ of scopes value and comprise end value) arbitrarily heat up; Insulation reaction 5 hours, thiocyanide just, isomer proportion, positive structure body 51%; Isomer 47% filters the sodium-chlor inorganic salt that elimination generates, and crystallization is separated out in the filtrating cooling; Filtration obtains thiocyanide isomer solid crystal (positive structure body 6%, isomer 93%), the 58g that gives money as a gift, filtrating freezing and crystallizing; Filtration obtains the positive structure body of thiocyanide (positive structure body 98%, isomer 1%), the 53g that gives money as a gift, the positive structure body of thiocyanide yield 77%.
Embodiment 3: drop into 500g acetone in the reaction flask, and embodiment 2 gained isomer 58g, Sodium Thiocyanate 99 58g, 55g content are 95% 1-N; N-dimethyl--2, the 3-dichloro-propyl-amine, 45~70 ℃ (in 45~70 ℃ of scopes value and comprise end value) arbitrarily heat up; Insulation reaction 5 hours, thiocyanide just, isomer proportion, positive structure body 50%; Isomer 48% filters the sodium-chlor inorganic salt that elimination generates, and crystallization is separated out in the filtrating cooling; Filtration obtains thiocyanide isomer solid crystal (positive structure body 5%, isomer 94%), the 58g that gives money as a gift, filtrating freezing and crystallizing; Filtration obtains the positive structure body of thiocyanide (positive structure body 98%, isomer 1%), the 52g that gives money as a gift, the positive structure body of thiocyanide yield 76%.
Embodiment 4: drop into 500g toluene, water 100ml, four butyl bromation amine 4g, embodiment 3 gained isomer 58g in the reaction flask; Ammonium thiocyanide 55g, 80g content are 95% 1-N, N-dimethyl--2, and 3-dibromo propylamine, 45~85 ℃ (in 45~85 ℃ of scopes value and comprise end value) arbitrarily heat up; Insulation reaction 6 hours, thiocyanide just, isomer proportion, positive structure body 52%; Isomer 47%, branch vibration layer while hot, crystallization is separated out in the solvent layer cooling; Filtration obtains thiocyanide isomer solid crystal (positive structure body 5%, isomer 94%), the 58g that gives money as a gift, filtrating freezing and crystallizing; Filtration obtains the positive structure body of thiocyanide (positive structure body 98%, isomer 1%), the 52g that gives money as a gift, the positive structure body of thiocyanide yield 75%.
Embodiment 5: drop into toluene mother liquor, water layer, the thiocyanide isomer that embodiment 4 obtains in the reaction flask, drop into Sodium Thiocyanate 99 58g, 55g content again and be 95% 1-N, N-dimethyl--2; The 3-dichloro-propyl-amine, heat up 45~85 ℃ (in 45~85 ℃ of scopes value and comprise end value) arbitrarily, insulation reaction 6 hours; Filtered while hot elimination inorganic salt, the solvent layer branch vibration layer, crystallization is separated out in the solvent layer cooling; Filtration obtains thiocyanide isomer solid crystal (positive structure body 5%, isomer 94%), the 57g that gives money as a gift, filtrating freezing and crystallizing; Filtration obtains the positive structure body of thiocyanide (positive structure body 98%, isomer 1%), the 54g that gives money as a gift, the positive structure body of thiocyanide yield 78%.
Embodiment 6: drop into methyl alcohol 200g in the reaction flask, the positive structure body of embodiment 2 gained thiocyanides 50g feeds the exsiccant hydrogen chloride gas at 10~15 ℃, to all dissolvings; Stop logical hydrogen chloride gas, be warming up to 20~25 ℃ of insulations 3 hours, lower the temperature about 10 ℃; Filter, the small amount of methanol washing gets white cartap solid crystal (positive structure body 98.4%, isomer 0.1%); Oven dry 64g, 179~181 ℃ of fusing points, yield 94%.
Comparative example 1: drop into 400g ethanol in the reaction flask, Sodium Thiocyanate 99 116g, 110g content are 95% 1-N, N-dimethyl--2; The 3-dichloro-propyl-amine heats up 65~75 ℃ insulation reaction 6 hours; After filtrate decompression steams solvent; Add elutriation and go out, filter and obtain thiocyanation materialization thing (positive structure body 50%, isomer 48%), oven dry 106g.
Comparative example 2: drop into methyl alcohol 400g in the reaction flask, comparative example 1 gained thiocyanide 100g feeds the exsiccant hydrogen chloride gas at 10~15 ℃; To all dissolving is transparent, stop logical hydrogen chloride gas, be warming up to 20~25 ℃; Be incubated 3 hours, lower the temperature about 10 ℃, filter; The small amount of methanol washing gets white cartap solid crystal, oven dry 72g (positive structure body 73%, isomer 26%).
What need understand is: though the foregoing description is to the present invention's detailed explanation of contrasting; But these explanations, just to simple declaration of the present invention, rather than limitation of the present invention; Any innovation and creation that do not exceed in the connotation of the present invention all fall into protection scope of the present invention.

Claims (5)

1. cartap midbody 2-N, N-dimethyl--1, the preparation method of 3-dithiocyano propane, it is by 1-N; N-dimethyl--2,3-dihalo propylamine, thiocyanate-are raw material, prepared in reaction is separating obtained in the presence of solvent, it is characterized in that: isomer products 3-N; N-dimethyl--1,2-dithiocyano propane cycles are participated in reaction, 1-N wherein, N-dimethyl--2; 3-dihalo propylamine raw material is selected from 1-N, N-dimethyl--2,3-dichloro-propyl-amine or 1-N, N-dimethyl--2; 3-dibromo propylamine or 1-N, N-dimethyl--2,3-diiodo-propylamine; Thiocyanate-is selected from Sodium Thiocyanate 99 or Rhocya or ammonium thiocyanide.
2. cartap midbody 2-N according to claim 1, N-dimethyl--1, the preparation method of 3-dithiocyano propane is characterized in that: used 1-N, N-dimethyl--2,3-dihalo propylamine raw material is 1-N, N-dimethyl--2,3-dichloro-propyl-amine.
3. cartap midbody 2-N according to claim 1, N-dimethyl--1, the preparation method of 3-dithiocyano propane is characterized in that: used thiocyanate-is a Sodium Thiocyanate 99.
4. cartap midbody 2-N according to claim 1, N-dimethyl--1, the preparation method of 3-dithiocyano propane is characterized in that: solvent is butanols, acetone or toluene.
5. cartap midbody 2-N according to claim 1, N-dimethyl--1, the preparation method of 3-dithiocyano propane is characterized in that: temperature of reaction is: 45~85 ℃, the reaction times is: 2~10 hours.
CN200810062030XA 2008-05-18 2008-05-18 Preparation method of cartap hydrochloride intermediate, i.e., 2-N, N-dimethyl-1, 3-dithio-cyano propane Active CN101519371B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN200810062030XA CN101519371B (en) 2008-05-18 2008-05-18 Preparation method of cartap hydrochloride intermediate, i.e., 2-N, N-dimethyl-1, 3-dithio-cyano propane

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN200810062030XA CN101519371B (en) 2008-05-18 2008-05-18 Preparation method of cartap hydrochloride intermediate, i.e., 2-N, N-dimethyl-1, 3-dithio-cyano propane

Publications (2)

Publication Number Publication Date
CN101519371A CN101519371A (en) 2009-09-02
CN101519371B true CN101519371B (en) 2012-06-20

Family

ID=41080193

Family Applications (1)

Application Number Title Priority Date Filing Date
CN200810062030XA Active CN101519371B (en) 2008-05-18 2008-05-18 Preparation method of cartap hydrochloride intermediate, i.e., 2-N, N-dimethyl-1, 3-dithio-cyano propane

Country Status (1)

Country Link
CN (1) CN101519371B (en)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104774167A (en) * 2014-11-27 2015-07-15 湖南昊华化工有限责任公司 Cartap intermediate 1, 3-thiocyanide normal compound preparation method
CN106748937B (en) * 2017-01-10 2018-06-19 仪征市海帆化工有限公司 The synthetic method of cartap
CN106905209B (en) * 2017-01-21 2018-10-30 宁波科诺华化工有限公司 A kind of synthesis technology of cartap intermediate
CN106905210B (en) * 2017-01-21 2018-10-30 宁波科诺华化工有限公司 A kind of preparation method of cartap intermediate

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB1264207A (en) * 1968-04-04 1972-02-16
CN1263089A (en) * 1998-09-18 2000-08-16 武田药品工业株式会社 Preparation of thiol-carbamate and sulfocyanic ester compound
CN1830957A (en) * 2005-03-09 2006-09-13 梁建忠 Novel process for preparing 2-N,-N-dimethyl-1, 3-thiocyanato propane
CN101103725A (en) * 2007-07-23 2008-01-16 江苏天容集团股份有限公司 Cartap environment-friendly type preparing method

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB1264207A (en) * 1968-04-04 1972-02-16
CN1263089A (en) * 1998-09-18 2000-08-16 武田药品工业株式会社 Preparation of thiol-carbamate and sulfocyanic ester compound
CN1830957A (en) * 2005-03-09 2006-09-13 梁建忠 Novel process for preparing 2-N,-N-dimethyl-1, 3-thiocyanato propane
CN101103725A (en) * 2007-07-23 2008-01-16 江苏天容集团股份有限公司 Cartap environment-friendly type preparing method

Also Published As

Publication number Publication date
CN101519371A (en) 2009-09-02

Similar Documents

Publication Publication Date Title
CN101519371B (en) Preparation method of cartap hydrochloride intermediate, i.e., 2-N, N-dimethyl-1, 3-dithio-cyano propane
CN102101847B (en) Method for preparing N-methyl-N'-(2-chloroethyl)piperazine
CN102659727A (en) Preparation method of benzbromarone
CN111620769B (en) Method for preparing 3,3 ', 4, 4' -biphenyl tetracarboxylic dianhydride
CN101885716B (en) Process for preparing sodium dehydroacetate
CN101239919B (en) Method for synthesizing aromatic diamines monomer
CN101823968B (en) Method for preparing 1,8-diaminonaphthalene by reducing 1,8-dinitronaphthalene with hydrazine hydrate
CN101979391B (en) Method for preparing tiotropium bromide
CN102976961A (en) Method for preparing methoxamine hydrochloride
Biffis et al. Trinuclear copper (I) complexes with triscarbene ligands: catalysis of C–N and C–C coupling reactions
CN107954882A (en) A kind of preparation method of 2- amino -2- (the 4- tert-butyl group -2- ethoxyl phenenyls) ethanol
CN102040572B (en) Production method of benzofuranone
CN102675148B (en) Preparation method of hydroxybenzyl cyanide
CN105481812B (en) Preparation method of 5-benzyloxy-4-oxo-4H-pyran-2-carboxylic acid
CN111170908B (en) Synthesis method of 2, 4-dimethyl-3-methylsulfonyl halogeno-benzene
CN107641080A (en) A kind of dihydronaphthalene ketones derivant containing spirane structure and preparation method thereof
CN101168520B (en) Method for producing 1,1'-phenylsulfonyl-4,4'-diallyl (2) ether
CN102531843A (en) Method for catalytically hydrogenating difluoroacetic acid
CN101781205A (en) Method for synthesizing substitutional crylic acid phenyl ester
CN110294694A (en) A kind of improved preparation method of intermediate DAS of paratonere 177
CN100554252C (en) A kind of preparation method of Sumatriptan Succinate
CN106083667B (en) A kind of synthetic method of 2 amino (4 ethylsulfonyl) phenol
CN102942533A (en) Preparation method of 4-(5-amino-6-hydroxy-2-benzoxazolyl) benzoic acid (ABA)
CN108129536A (en) A kind of preparation method of Dexamethasone Intermediate
CN107235873A (en) A kind of preparation method of high-purity mesna

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
ASS Succession or assignment of patent right

Owner name: ZHEJIANG BOSHIDA CROP TECHNOLOGY CO., LTD.

Free format text: FORMER OWNER: HANGZHOU UDRAGON CHEMICLAL CO., LTD.

Effective date: 20120518

C41 Transfer of patent application or patent right or utility model
COR Change of bibliographic data

Free format text: CORRECT: ADDRESS; FROM: 311106 HANGZHOU, ZHEJIANG PROVINCE TO: 314304 JIAXING, ZHEJIANG PROVINCE

TR01 Transfer of patent right

Effective date of registration: 20120518

Address after: Jiaxing City, Zhejiang province 314304 Fang Haiyan Haiyan Economic Development Zone, Tai Road No. 1

Patentee after: Zhejiang Boshida Crop Technological Co., Ltd.

Address before: 311106 Tangqi Industrial Zone, Yuhang District, Zhejiang, Hangzhou

Patentee before: Hangzhou Udragon Chemical Co., Ltd.

CP03 Change of name, title or address
CP03 Change of name, title or address

Address after: 314300 No. 1 Fangjiaduo Road, Haiyan Economic Development Zone, Jiaxing City, Zhejiang Province

Patentee after: Zhejiang Yulong Biotechnology Co., Ltd.

Address before: 314304 No. 1 Fangjiaduo Road, Haiyan Economic Development Zone, Jiaxing City, Zhejiang Province

Patentee before: Zhejiang Boshida Crop Technological Co., Ltd.

CP01 Change in the name or title of a patent holder
CP01 Change in the name or title of a patent holder

Address after: Fang Tai Road Economic Development Zone, Haiyan County, Jiaxing city of Zhejiang Province, No. 1 314300

Patentee after: Zhejiang Yulong Biotechnology Co., Ltd

Address before: Fang Tai Road Economic Development Zone, Haiyan County, Jiaxing city of Zhejiang Province, No. 1 314300

Patentee before: Zhejiang Yulong Biotechnology Co., Ltd.

PE01 Entry into force of the registration of the contract for pledge of patent right
PE01 Entry into force of the registration of the contract for pledge of patent right

Denomination of invention: Preparation of 2-N, n-dimethyl-1,3-dithiocyanopropane, an intermediate of fenitrogen

Effective date of registration: 20211222

Granted publication date: 20120620

Pledgee: Xitangqiao sub branch of Zhejiang Haiyan Rural Commercial Bank Co.,Ltd.

Pledgor: Zhejiang Yulong Biotechnology Co.,Ltd.

Registration number: Y2021330002593