CN102992982A - Synthesis method of p-hydroxybenzaldehyde - Google Patents

Synthesis method of p-hydroxybenzaldehyde Download PDF

Info

Publication number
CN102992982A
CN102992982A CN2012105343723A CN201210534372A CN102992982A CN 102992982 A CN102992982 A CN 102992982A CN 2012105343723 A CN2012105343723 A CN 2012105343723A CN 201210534372 A CN201210534372 A CN 201210534372A CN 102992982 A CN102992982 A CN 102992982A
Authority
CN
China
Prior art keywords
hydroxybenzaldehyde
phenol
synthetic method
reaction
reagent
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
CN2012105343723A
Other languages
Chinese (zh)
Other versions
CN102992982B (en
Inventor
刘鹏
郭龙龙
吴文雷
马韵升
史庆苓
门振
高洪奎
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.)
Shandong Jingbo Agrochemical Technology Co ltd
Original Assignee
Chambroad Chemical Industry Research Institute 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 Chambroad Chemical Industry Research Institute Co Ltd filed Critical Chambroad Chemical Industry Research Institute Co Ltd
Priority to CN201210534372.3A priority Critical patent/CN102992982B/en
Publication of CN102992982A publication Critical patent/CN102992982A/en
Application granted granted Critical
Publication of CN102992982B publication Critical patent/CN102992982B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Landscapes

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

Abstract

The invention provides a synthesis method of p-hydroxybenzaldehyde. Phenol used as a raw material reacts with a Vilsmeier reagent to synthesize p-hydroxybenzaldehyde. The invention has advantages of easily available raw materials, short reaction period, simple operation, mild reaction conditions, safe reaction process and low requirement on equipment, and is more suitable for industrial production of p-hydroxybenzaldehyde compared to other synthesis method of p-hydroxybenzaldehyde; no by-product is generated in the synthesis process, and separation and purification in a post treatment process is simple, so as to lower the cost of post treatment, and enhance yield and purity of the target product p-hydroxybenzaldehyde, wherein the yield is higher than 90%, and the purity is above 98%; and the synthesis method resolves problems in existing phenol method for p-hydroxybenzaldehyde synthesis, such as difficulties in separation and purification in post treatment, low yield of p-hydroxybenzaldehyde and high cost.

Description

The synthetic method of p-Hydroxybenzaldehyde
Technical field
The invention belongs to the fine chemical technology field, relate to the chemical synthetic method, be specifically related to the synthetic method of p-Hydroxybenzaldehyde.
Background technology
P-Hydroxybenzaldehyde is the important intermediate of medicine industry and perfume industry, in medicine industry, can be used for synthetic amoxycillin (amoxycilline Trihydrate bp), Trimethoprim Trimethyl phosphate (TMP), 3,4,5-TMB, to hydroxyglycine, amoxycillin cephamycin, artificial rhizoma Gastrodiae, farrerol, Ai Siluo etc.; In perfume industry for the synthesis of spices such as vanillin food grade,1000.000000ine mesh, vanirone, piperonal, syringic aldehyde, aubepine and raspberry ketones.Also be used for abroad the synthetic of pesticide herbicide bromoxynil and chloroxynil, and produce sterilant, photograph emulsifying agent, nickel plating gloss-imparting agent, liquid crystal etc.
Present industrial production p-Hydroxybenzaldehyde is the operational path take phenol, p-cresol, para-nitrotoluene etc. as raw material mainly.Existing phynol method raw material is easy to get, and manufacturing process is simpler, but the separation in later stage and purification ratio are difficult, cause the yield of p-Hydroxybenzaldehyde on the low side, and cost is higher.
Summary of the invention
The object of the present invention is to provide a kind of take phenol as raw material, by the synthetic p-Hydroxybenzaldehyde of simple technique, this synthetic method feed stock conversion is high, product yield is high, it is a kind of brand-new method for preparing p-Hydroxybenzaldehyde take phenol as raw material, namely adopt Vilsmeier reagent and phenol reactant to prepare p-Hydroxybenzaldehyde, having solved in the synthetic p-Hydroxybenzaldehyde technique of existing phynol method exists the later stage to separate and purification difficult, cause the yield of p-Hydroxybenzaldehyde on the low side, the problem that cost is higher.
The invention provides a kind of synthetic method of p-Hydroxybenzaldehyde, take phenol as raw material, adopt Vilsmeier reagent and phenol reactant to prepare p-Hydroxybenzaldehyde, reaction equation is as follows:
Figure 558521DEST_PATH_IMAGE001
Concrete steps comprise:
(1) take toluene as solvent, adding DMF and reagent I is 10~30 ℃ of lower reactions in temperature, gets Vilsmeier reagent;
(2) phenol is slowly added in the Vilsmeier reagent that generates in the step (1) and carry out insulation reaction, be cooled to 25 ℃-50 ℃, add again the water stirring reaction;
(3) add water washing, separatory, desolventizing, drying after reaction is finished, get faint yellow solid, be target product.
The composition principle of described p-Hydroxybenzaldehyde is:
Figure 295533DEST_PATH_IMAGE002
The synthetic method of the p-Hydroxybenzaldehyde that the present invention relates to is a kind of brand-new method for preparing p-Hydroxybenzaldehyde take phenol as raw material, namely adopts Vilsmeier reagent and phenol reactant to prepare p-Hydroxybenzaldehyde.From thermodynamics, Vilsmeier reagent and phenol reactant generate the contraposition product p-Hydroxybenzaldehyde of phenol at first, and at this moment aldehyde radical occupies the contraposition position of phenyl ring, and the aldehyde radical in the contraposition produces so do not have other by products so that the phenyl ring passivation.
Reagent I is POCl in the described step (1) 3Or SOCl 2Or PCl 5Or PCl 3A kind of.
The volumetric usage of the middle toluene of described step (1) is 3~10 times of DMF.
Phenol: DMF in described step (1) and the step (2): the mol ratio of reagent I is 1:1~1.2:1~1.3, and the very few reaction of raw material is incomplete, and excessive cost increases, and by product is increased.
Order of addition(of ingredients) in the described step (1) is to add reagent I in the toluene to drip DMF again, or reagent I is added drop-wise in the mixed solution of toluene and DMF.This is because the reaction in the step (1) is strong exothermal reaction, can only be that a kind of raw material is added drop-wise in the another kind of raw material, is conducive to like this temperature of reaction of the hierarchy of control.
The temperature of reaction of system is 10~30 ℃ in the described step (1).Because the reaction of system is more violent in the step (1), heat release is many, and wayward reaction during excess Temperature can make temperature moment rising that the punching material occurs, so temperature is controlled in this scope.
The adding method of phenol is adding phenol solid in the described step (2), or adds the toluene solution of phenol.
Temperature of reaction in the described step (2) is 60~110 ℃, is preferably 110 ℃.When temperature was lower than 60 ℃, the meeting augmenting response time, energy consumption increased; Because the boiling point of toluene is 110 ℃, selection toluene is solvent, and when carrying out back flow reaction, best temperature of reaction is 110 ℃.
Reaction times in the described step (2) is 30min~180min, and this is the Best Times scope of reaction, and the time is too short, causes reaction not exclusively, and product yield is excessively low, and cost increases; Overlong time can increase energy consumption, and corresponding cost also can increase.
The temperature of the water that adds in the described step (2) is 0-83 ℃, finds through the long-term a large amount of test of contriver, when the temperature of the water that adds during greater than 83 ℃, bumping even punching material phenomenon can occur.
Washing temperature is 40~80 ℃ in the described step (3), crosses when low when washing temperature, and the product in the toluene can be separated out, and when washing temperature is too high, reaches the azeotropic point of toluene and water, and is dangerous.General washing two to three times because product is dissolved in the toluene, is got the upper toluene phase, desolvation toluene under negative pressure, and recovery toluene is also applied mechanically, and gets at last faint yellow solid, and detecting the gained faint yellow solid by liquid matter and nucleus magnetic hydrogen spectrum is p-Hydroxybenzaldehyde.Separation and purification operations in the post-processed process are simple, and the solvent toluene after the recovery can be applied mechanically, and have reduced the cost of post-processed, thereby have reduced production cost.
The present invention is as raw material take phenol, prepare p-Hydroxybenzaldehyde with Vilsmeier reagent, raw material is easy to get, reaction time is short, operation steps is simple, and reaction conditions is gentle, reaction process safety, low for equipment requirements, the method for other p-Hydroxybenzaldehydes more is applicable to industrial production p-Hydroxybenzaldehyde relatively; In building-up process, there is not by product to produce, separating-purifying is simple in the post-processed process, reduced the cost of post-processed, yield and the purity of target product p-Hydroxybenzaldehyde have been improved, yield is more than 90%, and purity is more than 98%, solved in the synthetic p-Hydroxybenzaldehyde method of existing phynol method to exist the later stage to separate and purification difficult, cause the yield of p-Hydroxybenzaldehyde on the low side, the problem that cost is higher.
Embodiment
Below in conjunction with specific embodiment invention is described further, but not as to the restriction of summary of the invention, all based on purification principle of the present invention technology all belong to integral part of the present invention.
Embodiment one
The synthetic method of p-Hydroxybenzaldehyde, take phenol as raw material, concrete steps comprise:
(1) in the four-hole boiling flask of drying, adds 300mL toluene, then add 100mL DMF, measure 93.79mL SOCl 2In constant pressure funnel, in four-hole boiling flask, drip SOCl 2, temperature of reaction is 30 ℃, stirs 30min, gets Vilsmeier reagent;
(2) taking by weighing 121.68g phenol and add in the four-hole boiling flask, is 60 ℃ of lower insulation reaction 80min in temperature, cools to 50 ℃ again, and the adding volume is that 250mL, temperature are 83 ℃ water stirring 100min;
(3) solution in step (2) four-hole boiling flask is moved in the separating funnel leave standstill, cut lower floor's water, the water that adds volume and be 300mL, temperature and be 80 ℃ is washed; Then cut lower floor's water, get toluene and remove toluene under negative pressure, drying gets faint yellow solid, namely obtains p-Hydroxybenzaldehyde 143.85g, purity 98.9%, yield 91.1%.
Embodiment two
The synthetic method of p-Hydroxybenzaldehyde, take phenol as raw material, concrete steps comprise:
(1) in the four-hole boiling flask of drying, adds 100mL toluene, then add 12.05mL POCL 3, measure 10mL DMF in constant pressure funnel, in four-hole boiling flask, drip DMF, temperature of reaction is 10 ℃, stirs 45min, gets Vilsmeier reagent;
(2) taking by weighing 10.15g phenol and add in the four-hole boiling flask, is 110 ℃ of lower insulation reaction 30min in temperature, cools to 25 ℃ again, and the adding volume is that 200mL, temperature are 0 ℃ water stirring 100min;
(3) solution in step (2) four-hole boiling flask is moved in the separating funnel leave standstill, cut lower floor's water, the water that adds volume and be 280mL, temperature and be 60 ℃ is washed; Then cut lower floor's water, get toluene and remove toluene under negative pressure, drying gets faint yellow solid, namely obtains p-Hydroxybenzaldehyde 12.21g, purity 98.7%, yield 92.7%.
Embodiment three
The synthetic method of p-Hydroxybenzaldehyde, take phenol as raw material, concrete steps comprise:
(1) in the four-hole boiling flask of drying, adds 200mL toluene, then add 48.61mL PCL 5, measure 50mL DMF in constant pressure funnel, in four-hole boiling flask, drip DMF, temperature of reaction is 20 ℃, stirs 70min, gets Vilsmeier reagent;
(2) taking by weighing 60.84g phenol and be dissolved in the 100mL toluene solution and add in the four-hole boiling flask, is 85 ℃ of lower insulation reaction 180min in temperature, cools to 40 ℃ again, and addings volume is that 150mL, temperature are 40 ℃ water stirring 65min;
(3) solution in step (2) four-hole boiling flask is moved in the separating funnel leave standstill, cut lower floor's water, the water that adds volume and be 180mL, temperature and be 40 ℃ is washed; Then cut lower floor's water, get toluene and remove toluene under negative pressure, drying gets faint yellow solid, namely obtains p-Hydroxybenzaldehyde 73.18g, purity 98.4%, yield 92.7%.
Embodiment four
The synthetic method of p-Hydroxybenzaldehyde, take phenol as raw material, concrete steps comprise:
(1) in the four-hole boiling flask of drying, adds 300mL toluene, then add 60mL DMF, measure 73.33mL PCL 3In constant pressure funnel, in four-hole boiling flask, drip PCL 3, temperature of reaction is 15 ℃, stirs 70min, gets Vilsmeier reagent;
(2) taking by weighing 60.84g phenol and add in the four-hole boiling flask, is 100 ℃ of lower insulation reaction 60min in temperature, cools to 30 ℃ again, and the adding volume is that 150mL, temperature are 60 ℃ water stirring 65min;
(3) solution in step (2) four-hole boiling flask is moved in the separating funnel leave standstill, cut lower floor's water, the water that adds volume and be 200mL, temperature and be 50 ℃ is washed; Then cut lower floor's water, get toluene and remove toluene under negative pressure, drying gets faint yellow solid, namely obtains p-Hydroxybenzaldehyde 72.55g, purity 98.1%, yield 91.9%.
Can find out that from embodiment 1-4 take phenol as raw material, adopt the synthetic p-Hydroxybenzaldehyde of the present invention, the purity of gained p-Hydroxybenzaldehyde is more than 98%, yield is more than 90%.

Claims (9)

1. the synthetic method of a p-Hydroxybenzaldehyde take phenol as raw material, is characterized in that: adopt Vilsmeier reagent and phenol reactant to prepare p-Hydroxybenzaldehyde, reaction equation is as follows:
Figure 290886DEST_PATH_IMAGE001
2. the synthetic method of p-Hydroxybenzaldehyde according to claim 1, it is characterized in that: concrete steps comprise:
(1) take toluene as solvent, adding DMF and reagent I is 10~30 ℃ of lower reactions in temperature, gets Vilsmeier reagent;
(2) phenol is slowly added in the Vilsmeier reagent that generates in the step (1) and carry out insulation reaction, be cooled to 25 ℃-50 ℃, add again the water stirring reaction;
(3) add water washing, separatory, desolventizing, drying after reaction is finished, get faint yellow solid, be target product.
3. the synthetic method of p-Hydroxybenzaldehyde according to claim 2 is characterized in that: reagent I is POCl in the described step (1) 3Or SOCl 2Or PCl 5Or PCl 3A kind of.
4. the synthetic method of p-Hydroxybenzaldehyde according to claim 2 is characterized in that: the volumetric usage of toluene is 3~10 times of DMF in the described step (1).
5. the synthetic method of p-Hydroxybenzaldehyde according to claim 2 is characterized in that: phenol: DMF in described step (1) and the step (2): the mol ratio of reagent I is 1:1~1.2:1~1.3.
6. the synthetic method of p-Hydroxybenzaldehyde according to claim 2 is characterized in that: the order of addition(of ingredients) in the described step (1) is to add reagent I in the toluene to drip DMF again, or reagent I is added drop-wise in the mixed solution of toluene and DMF.
7. the synthetic method of p-Hydroxybenzaldehyde according to claim 2 is characterized in that: the adding method of phenol or adds the toluene solution of phenol for adding the phenol solid in the described step (2).
8. the synthetic method of p-Hydroxybenzaldehyde according to claim 2, it is characterized in that: the temperature of reaction in the described step (2) is 60~110 ℃.
9. the synthetic method of p-Hydroxybenzaldehyde according to claim 2, it is characterized in that: the reaction times in the described step (2) is 30min~180min.
CN201210534372.3A 2012-12-12 2012-12-12 Synthesis method of p-hydroxybenzaldehyde Active CN102992982B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201210534372.3A CN102992982B (en) 2012-12-12 2012-12-12 Synthesis method of p-hydroxybenzaldehyde

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201210534372.3A CN102992982B (en) 2012-12-12 2012-12-12 Synthesis method of p-hydroxybenzaldehyde

Publications (2)

Publication Number Publication Date
CN102992982A true CN102992982A (en) 2013-03-27
CN102992982B CN102992982B (en) 2015-01-14

Family

ID=47922167

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201210534372.3A Active CN102992982B (en) 2012-12-12 2012-12-12 Synthesis method of p-hydroxybenzaldehyde

Country Status (1)

Country Link
CN (1) CN102992982B (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103787945A (en) * 2014-01-20 2014-05-14 天津市敬业精细化工有限公司 Preparation method of aromatic aldehyde
CN104230748A (en) * 2014-11-04 2014-12-24 洛阳市三诺化工有限公司 Synthetic process of copper extraction agent 5-nonyl salicylaldoxime
CN104230748B (en) * 2014-11-04 2017-01-04 洛阳市三诺化工有限公司 A kind of synthesis technique of copper extractant 5-nonyl salicyl aldooxime
CN106916051A (en) * 2017-02-21 2017-07-04 新乡学院 A kind of preparation method of the hydroxy-benzyl alcohol of 3,5 di-t-butyl 4
CN112205405A (en) * 2020-11-11 2021-01-12 浙江新安化工集团股份有限公司 Weeding composition containing vanillin and glufosinate-ammonium and herbicide
CN112616837A (en) * 2020-10-28 2021-04-09 贵州省中国科学院天然产物化学重点实验室(贵州医科大学天然产物化学重点实验室) Use of o-hydroxy-p-methoxybenzaldehyde derivatives as herbicides

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101456853A (en) * 2009-01-05 2009-06-17 江苏省农业科学院 Bionic novel series compounds 7-alkoxyl-8-(3,3'-disubstituted propyl) benzo pyran-2-ones synthesis and its application as pesticides
CN102617313A (en) * 2012-03-15 2012-08-01 华东理工大学 Sharing synthesis method for vanillin and isovanillin

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101456853A (en) * 2009-01-05 2009-06-17 江苏省农业科学院 Bionic novel series compounds 7-alkoxyl-8-(3,3'-disubstituted propyl) benzo pyran-2-ones synthesis and its application as pesticides
CN102617313A (en) * 2012-03-15 2012-08-01 华东理工大学 Sharing synthesis method for vanillin and isovanillin

Non-Patent Citations (3)

* Cited by examiner, † Cited by third party
Title
GURNOS JONES ET AL.: "The vilsmeier reaction of fully conjugated carbocycles and heterocycles", 《ORGANIC REACTIONS》, vol. 49, 31 December 1997 (1997-12-31) *
厍梦尧等: "对羟基苯甲醛的合成研究新进展", 《化学试剂》, vol. 33, no. 12, 31 December 2011 (2011-12-31), pages 1087 - 1094 *
李东凤等: "《有机化学》", 31 August 2007, article "醛、酮、醌", pages: 326 *

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103787945A (en) * 2014-01-20 2014-05-14 天津市敬业精细化工有限公司 Preparation method of aromatic aldehyde
CN104230748A (en) * 2014-11-04 2014-12-24 洛阳市三诺化工有限公司 Synthetic process of copper extraction agent 5-nonyl salicylaldoxime
CN104230748B (en) * 2014-11-04 2017-01-04 洛阳市三诺化工有限公司 A kind of synthesis technique of copper extractant 5-nonyl salicyl aldooxime
CN106916051A (en) * 2017-02-21 2017-07-04 新乡学院 A kind of preparation method of the hydroxy-benzyl alcohol of 3,5 di-t-butyl 4
CN112616837A (en) * 2020-10-28 2021-04-09 贵州省中国科学院天然产物化学重点实验室(贵州医科大学天然产物化学重点实验室) Use of o-hydroxy-p-methoxybenzaldehyde derivatives as herbicides
CN112616837B (en) * 2020-10-28 2024-03-01 贵州省中国科学院天然产物化学重点实验室(贵州医科大学天然产物化学重点实验室) Use of o-hydroxy-p-methoxybenzaldehyde derivatives as herbicides
CN112205405A (en) * 2020-11-11 2021-01-12 浙江新安化工集团股份有限公司 Weeding composition containing vanillin and glufosinate-ammonium and herbicide

Also Published As

Publication number Publication date
CN102992982B (en) 2015-01-14

Similar Documents

Publication Publication Date Title
CN102174040B (en) Preparation method of electronic grade triglycidyl isocyanurate
CN102992982B (en) Synthesis method of p-hydroxybenzaldehyde
CN104387291B (en) Preparation method of 1,3,6-hexanetricarbonitrile
CN104788632B (en) A kind of preparation method of high-purity polyether-ether-ketone
CN106117128A (en) A kind of micro passage reaction prepares the method for pyridone chlorine addition product continuously
CN102285649A (en) Method for preparing monopotassium phosphate
CN107459472A (en) Method for refining dimethyl sulfoxide solvent in carbon fiber precursor production process
CN105503513B (en) The method of silicon dioxide carried catalysis of phosphotungstic acid synthesis 4,4 '-dichloromethyl biphenyl
CN102976929A (en) Method for synthesizing (4-chloro-2-phenoxy phenyl)-acetic acid
CN104250218B (en) A kind of tert-butyl acrylamide sulfonate production method
CN105315232A (en) Method for preparing acryloyl morpholine
CN105837791B (en) Preparation method of hydantoin epoxy resin
CN104910032A (en) Preparation method of anilino-acetate
CN103951590B (en) The preparation method of N, O-dimethyl-N '-nitro isourea
CN107253916B (en) A kind of environmentally protective new method for preparing amion acetic acid
Souza et al. Structural characterization of a new dioxamic acid derivative by experimental (FT-IR, NMR, and X-ray) analyses and theoretical (HF and DFT) investigations
CN105330605B (en) A kind of industrialized preparing process of the fluoropyrimidine of 2 first sulfydryl 4,6
CN108409768A (en) A kind of preparation method of boron trifluoride benzylamine complex compound
CN103524291A (en) Continuous synthetic method of chloralkane
CN115960133A (en) Comprehensive recovery and utilization method of alkyl dichlorophosphine production by-products
CN104117389A (en) Preparation method capable of improving yield of catalyst raw powder for methanol to olefin
CN104945234B (en) The preparation method of the methoxy benzophenone of 2,2 ' dihydroxy 4
CN103319355B (en) Separation and purification method of amino glycerol
CN205653373U (en) System for synthetic 2, 4 - dinitroanisole of serialization
CN104045525A (en) Production technology for synthesizing m-bromoanisole

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
ASS Succession or assignment of patent right

Owner name: CHAMBROAD AGROCHEMICAL TECHNOLOGY CO., LTD.

Free format text: FORMER OWNER: YELLOW RIVER DELTA JINGBO CHEMICAL RESEARCH INSTITUTE CO., LTD.

Effective date: 20141201

C41 Transfer of patent application or patent right or utility model
TA01 Transfer of patent application right

Effective date of registration: 20141201

Address after: 256500 Shandong city of Binzhou province Hu Zhen Boxing County Chen Jingbo Industrial Park Beijing Bo agricultural Polytron Technologies Inc

Applicant after: JINGBO AGROCHEMICALS TECHNOLOGY Co.,Ltd.

Address before: 256500 Boxing Economic Development Zone, Binzhou, Shandong

Applicant before: CHAMBROAD CHEMICAL INDUSTRY RESEARCH INSTITUTE Co.,Ltd.

C14 Grant of patent or utility model
GR01 Patent grant
CP03 Change of name, title or address
CP03 Change of name, title or address

Address after: 256500 Boxing County Economic Development Zone, Binzhou, Shandong

Patentee after: JINGBO AGROCHEMICALS TECHNOLOGY Co.,Ltd.

Address before: 256500 Jingbo Agrochemical Technology Co., Ltd. of Jingbo Industrial Park, Chenhu Town, Boxing County, Binzhou City, Shandong Province

Patentee before: JINGBO AGROCHEMICALS TECHNOLOGY 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: 256500 Boxing Economic Development Zone, Shandong, Binzhou

Patentee after: Shandong Jingbo Agrochemical Technology Co.,Ltd.

Address before: 256500 Boxing Economic Development Zone, Shandong, Binzhou

Patentee before: JINGBO AGROCHEMICALS TECHNOLOGY Co.,Ltd.