CN102584565A - Preparation method for 2,4,5-trifluoro benzene acetic acid - Google Patents

Preparation method for 2,4,5-trifluoro benzene acetic acid Download PDF

Info

Publication number
CN102584565A
CN102584565A CN2012100263281A CN201210026328A CN102584565A CN 102584565 A CN102584565 A CN 102584565A CN 2012100263281 A CN2012100263281 A CN 2012100263281A CN 201210026328 A CN201210026328 A CN 201210026328A CN 102584565 A CN102584565 A CN 102584565A
Authority
CN
China
Prior art keywords
trifluoro
benzene
acid
acetic acid
reaction
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
CN2012100263281A
Other languages
Chinese (zh)
Other versions
CN102584565B (en
Inventor
张鹏翔
张月成
李志陵
刘细建
刘劲松
孙海丽
王建柏
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.)
CANGZHOU SENARY CHEMICAL TECHNOLOGY Co Ltd
Original Assignee
CANGZHOU SENARY CHEMICAL TECHNOLOGY 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 CANGZHOU SENARY CHEMICAL TECHNOLOGY Co Ltd filed Critical CANGZHOU SENARY CHEMICAL TECHNOLOGY Co Ltd
Priority to CN 201210026328 priority Critical patent/CN102584565B/en
Publication of CN102584565A publication Critical patent/CN102584565A/en
Application granted granted Critical
Publication of CN102584565B publication Critical patent/CN102584565B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Landscapes

  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Catalysts (AREA)

Abstract

The invention discloses a preparation method for 2,4,5-trifluoro benzene acetic acid, which belongs to the field of organic chemical synthesis and comprises the steps of (1) dissolving 1,2,4-trifluoro benzene acetic acid in a solvent, and then performing fourier alkylate reaction with chloroacetonitrile under the catalysis of lewis acid to obtain 2,4,5-trifluoro benzene acetonitrile; (2) enabling the 2,4,5-trifluoro benzene acetonitrile to perform hydrolysis reaction with acid, cooling and crystallizing to achieve the 2,4,5-trifluoro benzene acetic acid. The preparation method doesn't use toxic cyanide and avoids using a lot of concentrated sulfuric acid, thereby having the advantages of being low in pollution, short in line, capable of reducing equipment investment, low in cost, high in yield and the like.

Description

A kind of 2,4, the preparation method of 5-trifluoro benzene acetic acid
Technical field
The present invention relates to the synthetic field of organic chemistry, relate in particular to a kind of 2,4, the preparation method of 5-trifluoro benzene acetic acid.
Background technology
Sitagliptin phosphate is a kind of novel antidiabetic drug dipeptidyl peptidase-4 (DPP-4) suppressor factor, can improve the ability that human body self reduces too high blood glucose level.Sitagliptin phosphate (
Figure 64175DEST_PATH_IMAGE001
) English name: Sitagliptin phosphate monohydrate, chemical name: 7-[(3R)-and 3-amino-1-oxo-4-(2,4, the 5-trifluorophenyl) butyl]-5; 6,7,8-tetrahydrochysene-3-Trifluoromethyl-1,2; 4-triazolo [4,3-a] pyrazine phosphoric acid salt, molecular formula is C 16H 15F 6N 5O H 3PO 4, on October 17th, 2006, Merck & Co., Inc. announced FDA's approved sitagliptin phosphate (Sitagliptin phosphata).This medicine becomes only up to now dipeptidyl peptidase-4 (DDP-4) the suppressor factor class medicine that is used to treat diabetes B of American market.
The sitagliptin of bibliographical information synthetic all is key intermediate 2,4, and 5-trifluoro benzene acetic acid (II) raw material is synthetic through long route, therefore how can the advantages of simplicity and high efficiency Synthetic 2, and 4, the 5-trifluoro benzene acetic acid is just very crucial.
Figure 816230DEST_PATH_IMAGE002
The synthetic route of the trifluoro benzene acetic acid of reporting in the document probably has following several kinds, but be aimed at suitability for industrialized production part not fully up to expectations is arranged all.
Route 1:
This route is with 2,4, and the 5-trifluorobromobenzene is a starting raw material, reacts under strong alkaline condition with diethyl oxalate, and right hydrolysis obtains product, and this route is had relatively high expectations to reaction conditions, is inappropriate for suitability for industrialized production.
Route 2:
This route is equally with 2,4, and the 5-trifluorobromobenzene is a starting raw material, generates grignard reagent earlier, replaces with allyl bromide 98 then, and oxidation obtains trifluoro benzene acetic acid under catalyst action at last.Anhydrous the having relatively high expectations of this route using form reaction pair, and the catalyzer and the oxygenant that use cost an arm and a leg, and is not suitable for suitability for industrialized production.
Route 3:
This route uses trifluoro-benzene to be raw material, carries out acetylize earlier, Willgerodt-kindler reacted sulfo-trifluoro benzene acetic acid acid amides then, and hydrolysis obtains trifluoro benzene acetic acid then.Willgerodt-kindler reaction yield in this route is lower, and produces a large amount of stench sulfide in the reaction process, and environmental pollution is bigger, and aftertreatment is purified comparatively difficult, is difficult for realizing industriallization.
Route 4:
Figure 905726DEST_PATH_IMAGE004
this route is a starting raw material with a trifluoro-benzene; Utilize chloromethylation to obtain three fluorobenzyl chlorides; Use hypertoxic sodium cyanide to obtain the trifluoro-benzene acetonitrile then, obtained trifluoro benzene acetic acid through hydrolysis again.This route has used a large amount of vitriol oils when carrying out chloromethylation, and uses the prussiate of severe toxicity, and environment is caused great pressure.
Route 5:
This route is starting raw material equally with the trifluoro-benzene, carries out chloromethylation equally earlier, carries out grignard reaction then, and logical carbonic acid gas finally obtains trifluoro benzene acetic acid in grignard reagent.This route on a route, the sodium cyanide of having avoided using severe toxicity of success, but shortcoming such as grignard reaction has difficult the initiation, and is wayward, the utmost point is unfavorable for industriallization.
More than comprehensive, the technology of existing production trifluoro benzene acetic acid all exists some deficiency, especially lacks the consideration to environment, therefore design a raw material be simple and easy to, simple to operate, cost is low, yield is high, and is and very necessary to the little route of environmental stress.
Summary of the invention
It is a kind of 2,4 that the present invention provides, the preparation method of 5-trifluoro benzene acetic acid, method of the present invention is not used hypertoxic prussiate, and avoids the use of a large amount of vitriol oils, have pollute low, route short, reduce facility investment, low, the yield advantages of higher of cost.
The technical scheme that the present invention taked is:
A kind of 2,4, the preparation method of 5-trifluoro benzene acetic acid,
Its preparation route is following:
The preparation method comprises the steps:
(1) with 1,2, the 4-trifluoro-benzene dissolves in solvent, under Louis acid catalysis, carries out the Fu Shi alkylated reaction with chloromethyl cyanide then, obtains 2,4,5-trifluoro-benzene acetonitrile;
(2) 2,4,5-trifluoro-benzene acetonitrile and the acid reaction that is hydrolyzed, crystallisation by cooling obtains 2,4, the 5-trifluoro benzene acetic acid.
Wherein, in the step (1) 1,2, the molar ratio of 4-trifluoro-benzene and chloromethyl cyanide is 1:1-2.5; Lewis acid is aluminum chloride, boron trifluoride, zinc chloride, iron(ic)chloride, tin tetrachloride; The Lewis acid consumption is 1,2, the 3%-30% of 4-trifluoro-benzene mole number; Reaction solvent is methylene dichloride, trichloromethane, tetracol phenixin, 1, and the 2-ethylene dichloride; Solvent load is 1,2,4-trifluoro-benzene (quality)/solvent (volume)=1:3-10; Temperature of reaction is 40-85 ℃, and the reaction times is 2-4 hour.
Used acid is one or more in concentrated hydrochloric acid, the vitriol oil, SPA and the Glacial acetic acid min. 99.5 in the step (2); Temperature of reaction is 60-150 ℃; Reaction times is 1-6 hour; 2,4,5-trifluoro-benzene acetonitrile is 2,4 with the ratio of the charging capacity of acid, 5-trifluoro-benzene acetonitrile (quality)/acid (volume)=1:1-1:10.
Optimal scheme is: in the step (1) 1,2, the ingredient proportion of 4-trifluoro-benzene and chloromethyl cyanide is 1:1.2-1.5; Lewis acid is aluminum chloride and zinc chloride; The Lewis acid consumption is 1,2,4-trifluoro-benzene mole number be 5%-10%; Said reaction solvent is methylene dichloride and trichloromethane; Solvent load is 1,2,4-trifluoro-benzene (quality)/solvent (volume)=1:4-6.
Temperature of reaction is 100-140 ℃ in the step (2); Reaction times is 3-4 hour; 2,4,5-trifluoro-benzene acetonitrile is 2,4 with the ratio of the charging capacity of acid, 5-trifluoro-benzene acetonitrile (quality)/acid (volume)=1:2-3.
Concentrated hydrochloric acid, the vitriol oil, SPA and Glacial acetic acid min. 99.5 are industrial concentrated hydrochloric acid, the vitriol oil, SPA and Glacial acetic acid min. 99.5 in the reaction, and mass concentration is respectively 37%, 98%, 85% and 99%.
Adopt the beneficial effect that technique scheme produced to be:
1. the use of having avoided hypertoxic prussiate of success, and avoided in the chloromethylation process use of a large amount of vitriol oils is polluted lowly, greatly reduces the pressure to environment.
2. compared with prior art, shortened reaction scheme, significantly reduced facility investment, reduced cost, and yield is high, is easy to realize suitability for industrialized production.
Embodiment
1-5 is 2,4 in following examples, the preparation of 5-trifluoro-benzene acetonitrile, and 6-10 is 2,4, the preparation of 5-trifluoro benzene acetic acid.
Embodiment 1
2,4, the preparation of 5-trifluoro-benzene acetonitrile
In the 1L reaction flask, add 132g1,2, the 4-trifluoro-benzene adds the dissolving of 396ml methylene dichloride, adds 8.05g iron(ic)chloride then, and the 75g chloromethyl cyanide is heated to 40 ℃, refluxes stopped reaction 4 hours.Be cooled to room temperature, filter, solvent is reclaimed in the filtrate decompression distillation, distill then 2,4,5-trifluoro-benzene acetonitrile 124g, yield 72.5%.
Embodiment 2
2,4, the preparation of 5-trifluoro-benzene acetonitrile
Add 132g 1,2 in the 1L reaction flask, the 4-trifluoro-benzene adds the dissolving of 1320ml trichloromethane, adds the 13.2g aluminum chloride then, and the 187.5g chloromethyl cyanide is heated to 60 ℃, refluxes stopped reaction 3 hours.Be cooled to room temperature, filter, solvent is reclaimed in the filtrate decompression distillation earlier, distill then 2,4,5-trifluoro-benzene acetonitrile 130g, yield 76.0%.
Embodiment 3
2,4, the preparation of 5-trifluoro-benzene acetonitrile
Add 132g 1,2 in the 1L reaction flask, the 4-trifluoro-benzene adds the dissolving of 528ml tetracol phenixin, adds the 20.4g boron trifluoride then, and the 112.5g chloromethyl cyanide is heated to 80 ℃, refluxes stopped reaction 2 hours.Be cooled to room temperature, filter, solvent is reclaimed in the filtrate decompression distillation earlier, distill then 2,4,5-trifluoro-benzene acetonitrile 132g, yield 77.2%.
Embodiment 4
2,4, the preparation of 5-trifluoro-benzene acetonitrile
Add 132g 1,2 in the 1L reaction flask, the 4-trifluoro-benzene adds 792ml 1, and the dissolving of 2-ethylene dichloride adds the 7.77g tin tetrachloride then, and the 80g chloromethyl cyanide is heated to 85 ℃, refluxes stopped reaction 2 hours.Be cooled to room temperature, filter, solvent is reclaimed in the filtrate decompression distillation earlier, distill then 2,4,5-trifluoro-benzene acetonitrile 135g, yield 78.9%.
Embodiment 5
2,4, the preparation of 5-trifluoro-benzene acetonitrile
Add 132g 1,2 in the 1L reaction flask, the 4-trifluoro-benzene adds 792ml 1, and the dissolving of 2-ethylene dichloride adds the 18g zinc chloride then, and the 150g chloromethyl cyanide is heated to 85 ℃, refluxes stopped reaction 2 hours.Be cooled to room temperature, filter, solvent is reclaimed in the filtrate decompression distillation earlier, distill then 2,4,5-trifluoro-benzene acetonitrile 133g, yield 77.8%.
Embodiment 6
2,4, the preparation of 5-trifluoro benzene acetic acid
(1) in the 1L reaction flask, add 100g trifluoro-benzene acetonitrile, add the 100ml vitriol oil, be heated to 100 ℃, and under this temperature, reacted 3 hours, reaction solution is poured in the 5L frozen water, and a large amount of white solids are separated out, and cross and filter 2,4,5-trifluoro benzene acetic acid 106, yield 95.5%.
Embodiment 7
2,4, the preparation of 5-trifluoro benzene acetic acid
In the 1L reaction flask, add 100g trifluoro-benzene acetonitrile, add the 200ml concentrated hydrochloric acid, be heated to 80 ℃, and under this temperature, reacted 4 hours, reaction solution is poured in the 5L frozen water, and a large amount of white solids are separated out, and cross and filter 2,4,5-trifluoro benzene acetic acid 100g, yield 90.1%.
Embodiment 8
2,4, the preparation of 5-trifluoro benzene acetic acid
Add 100g trifluoro-benzene acetonitrile in the 1L reaction flask, add the 250ml SPA, 50ml acetic acid is heated to 60 ℃; And under this temperature, reacted 1 hour, reaction solution is poured in the 5L frozen water, and a large amount of white solids are separated out, and cross and filter 2; 4,5-trifluoro benzene acetic acid 110g, yield 99.1%.
Embodiment 9
2,4, the preparation of 5-trifluoro benzene acetic acid
Add 100g trifluoro-benzene acetonitrile in the 1L reaction flask, add the 400ml Glacial acetic acid min. 99.5,200ml hydrochloric acid is heated to 150 ℃; And under this temperature, reacted 2 hours, reaction solution is poured in the 5L frozen water, and a large amount of white solids are separated out, and cross and filter 2; 4,5-trifluoro benzene acetic acid 103g, yield 92.8%.
Embodiment 10
2,4, the preparation of 5-trifluoro benzene acetic acid
Add 100g trifluoro-benzene acetonitrile in the 1L reaction flask, add the 700ml concentrated hydrochloric acid, 300ml acetic acid is heated to 140 ℃; And under this temperature, reacted 6 hours, reaction solution is poured in the 5L frozen water, and a large amount of white solids are separated out, and cross and filter 2; 4,5-trifluoro benzene acetic acid 105g, yield 94.6%.

Claims (5)

1. one kind 2,4, the preparation method of 5-trifluoro benzene acetic acid is characterized in that comprising the steps:
(1) with 1,2, the 4-trifluoro-benzene dissolves in solvent, under Louis acid catalysis, carries out the Fu Shi alkylated reaction with chloromethyl cyanide then, obtains 2,4,5-trifluoro-benzene acetonitrile;
(2) 2,4,5-trifluoro-benzene acetonitrile and the acid reaction that is hydrolyzed, crystallisation by cooling obtains 2,4, the 5-trifluoro benzene acetic acid.
2. according to claim 1 a kind of 2,4, the preparation method of 5-trifluoro benzene acetic acid is characterized in that described in the step (1) 1,2, and the molar ratio of 4-trifluoro-benzene and chloromethyl cyanide is 1:1-2.5; Said Lewis acid is aluminum chloride, boron trifluoride, zinc chloride, iron(ic)chloride, tin tetrachloride; Said Lewis acid consumption is 1,2, the 3%-30% of 4-trifluoro-benzene mole number; Said reaction solvent is methylene dichloride, trichloromethane, tetracol phenixin, 1, and the 2-ethylene dichloride; Solvent load is 1,2,4-trifluoro-benzene (quality)/solvent (volume)=1:3-10; Temperature of reaction is 40-85 ℃, and the reaction times is 2-4 hour.
3. according to claim 2 a kind of 2,4, the preparation method of 5-trifluoro benzene acetic acid is characterized in that saidly 1,2, and the ingredient proportion of 4-trifluoro-benzene and chloromethyl cyanide is 1:1.2-1.5; Said Lewis acid is aluminum chloride and zinc chloride; Said Lewis acid consumption is 1,2,4-trifluoro-benzene mole number be 5%-10%; Said reaction solvent is methylene dichloride and trichloromethane; Solvent load is 1,2,4-trifluoro-benzene (quality)/solvent (volume)=1:4-6.
4. according to claim 1 a kind of 2,4, the preparation method of 5-trifluoro benzene acetic acid is characterized in that acid described in the step (2) is in concentrated hydrochloric acid, the vitriol oil, SPA and the Glacial acetic acid min. 99.5 one or more; Temperature of reaction is 60-150 ℃; Reaction times is 1-6 hour; 2,4,5-trifluoro-benzene acetonitrile is 2,4 with the ratio of the charging capacity of acid, 5-trifluoro-benzene acetonitrile (quality)/acid (volume)=1:1-1:10.
5. according to claim 4 a kind of 2,4, the preparation method of 5-trifluoro benzene acetic acid is characterized in that said temperature of reaction is 100-140 ℃; Reaction times is 3-4 hour; 2,4,5-trifluoro-benzene acetonitrile is 2,4 with the ratio of the charging capacity of acid, 5-trifluoro-benzene acetonitrile (quality)/acid (volume)=1:2-3.
CN 201210026328 2012-02-07 2012-02-07 Preparation method for 2,4,5-trifluoro benzene acetic acid Active CN102584565B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 201210026328 CN102584565B (en) 2012-02-07 2012-02-07 Preparation method for 2,4,5-trifluoro benzene acetic acid

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN 201210026328 CN102584565B (en) 2012-02-07 2012-02-07 Preparation method for 2,4,5-trifluoro benzene acetic acid

Publications (2)

Publication Number Publication Date
CN102584565A true CN102584565A (en) 2012-07-18
CN102584565B CN102584565B (en) 2013-10-02

Family

ID=46473901

Family Applications (1)

Application Number Title Priority Date Filing Date
CN 201210026328 Active CN102584565B (en) 2012-02-07 2012-02-07 Preparation method for 2,4,5-trifluoro benzene acetic acid

Country Status (1)

Country Link
CN (1) CN102584565B (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103232339A (en) * 2013-04-19 2013-08-07 重庆紫光化工股份有限公司 Preparation method of chlorinated phenylacetic acid
CN111393282A (en) * 2020-05-21 2020-07-10 湖南复瑞生物医药技术有限责任公司 Preparation method of 2,4, 5-trifluorophenylacetic acid
CN112457153A (en) * 2020-11-10 2021-03-09 杭州臻挚生物科技有限公司 Industrial preparation method of 2,4, 5-trifluoro-phenylacetic acid

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6870067B2 (en) * 2002-10-08 2005-03-22 Merck & Co., Inc. Process for the synthesis of trifluorophenylacetic acids
CN101429115A (en) * 2008-12-22 2009-05-13 浙江海翔药业股份有限公司 Process for producing trifluoro benzene acetic acid and sitagliptin
CN101659611A (en) * 2009-09-28 2010-03-03 浙江永太科技股份有限公司 Method for preparing 2, 4, 5-trifluoro-phenylacetic-acid

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6870067B2 (en) * 2002-10-08 2005-03-22 Merck & Co., Inc. Process for the synthesis of trifluorophenylacetic acids
CN101429115A (en) * 2008-12-22 2009-05-13 浙江海翔药业股份有限公司 Process for producing trifluoro benzene acetic acid and sitagliptin
CN101659611A (en) * 2009-09-28 2010-03-03 浙江永太科技股份有限公司 Method for preparing 2, 4, 5-trifluoro-phenylacetic-acid

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103232339A (en) * 2013-04-19 2013-08-07 重庆紫光化工股份有限公司 Preparation method of chlorinated phenylacetic acid
CN111393282A (en) * 2020-05-21 2020-07-10 湖南复瑞生物医药技术有限责任公司 Preparation method of 2,4, 5-trifluorophenylacetic acid
CN112457153A (en) * 2020-11-10 2021-03-09 杭州臻挚生物科技有限公司 Industrial preparation method of 2,4, 5-trifluoro-phenylacetic acid

Also Published As

Publication number Publication date
CN102584565B (en) 2013-10-02

Similar Documents

Publication Publication Date Title
US20170101326A1 (en) Method for Recycling Ammonia from Low-Concentration Ammonium Chloride Wastewater
CN102584565B (en) Preparation method for 2,4,5-trifluoro benzene acetic acid
CN101333304B (en) Rubber antiager and method for preparing same
CN103058912A (en) Preparation method of 3-(4-chlorobutyl)indole-5-formonitrile
CN106008290A (en) Method for preparing tembotrions
CN103408475B (en) The preparation method of liquid antioxidant 4,6-bis-(pungent thiomethyl) ortho-cresol
CN102160956A (en) Method for absorbing and utilizing phosgene tail gas
CN102249928B (en) Synthesis method of N,N-diisopropyl quadrol
US20130281730A1 (en) Preparation of 5-aminosalicylic acid by gas phase catalytic carboxylation
CN102617312A (en) Method for preparing 2-chloro-6-fluorobenzaldehyde
CN101659611A (en) Method for preparing 2, 4, 5-trifluoro-phenylacetic-acid
CN103073458B (en) Method for recovering trifluoromethanesulfonic acid in wastewater
CN102757348B (en) Processing method of sodium citrate mother liquor
CN103112879B (en) Method for preparing cryolite and co-generating polymerized chlorination aluminum sulfate iron by using iron-containing wastewater
CN110128258B (en) Synthetic method of sitagliptin intermediate 2,4, 5-trifluorophenylacetic acid
CN101417946B (en) Method for preparing pentachlorobenzoyl chloride
TWI637913B (en) Curing manufacturing method of hexahydrate ferric chloride and curing manufacturing system thereof
CN1317268C (en) 2,6-dimethylpyridine preparation method
CN102617418B (en) Method for recovering amino acid ester from amino acid esterification mother liquor
WO2022088302A1 (en) Preparation method for isophthalamide
CN103254202A (en) Preparation method of asenapine
CN103613785A (en) Preparation method of antioxidant 224 by employing solid sulfuric acid as catalyst
CN104445441B (en) A kind of method utilizing the industrial waste sulfuric acid of purification acetylene gas generation and red mud to produce polyaluminium sulfate ferrous solution
CN108752218B (en) Route for preparing dolutegravir key intermediate 2, 4-difluorobenzylamine
CN102219716A (en) Method for purifying 5-sulfosalicylic acid

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

Denomination of invention: Double layer cyclic 4-belts filtered well

Effective date of registration: 20150707

Granted publication date: 20131002

Pledgee: Qingxian County rural credit cooperative Limited by Share Ltd

Pledgor: CANGZHOU SENARY CHEMICAL SCIENCE-TEC CO.,LTD.

Registration number: 2015990000541

PLDC Enforcement, change and cancellation of contracts on pledge of patent right or utility model
PC01 Cancellation of the registration of the contract for pledge of patent right
PC01 Cancellation of the registration of the contract for pledge of patent right

Date of cancellation: 20230418

Granted publication date: 20131002

Pledgee: Qingxian County rural credit cooperative Limited by Share Ltd

Pledgor: CANGZHOU SENARY CHEMICAL SCIENCE-TEC CO.,LTD.

Registration number: 2015990000541