CN107353193A - A kind of preparation method of anhydrous formic acid - Google Patents

A kind of preparation method of anhydrous formic acid Download PDF

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Publication number
CN107353193A
CN107353193A CN201710582138.0A CN201710582138A CN107353193A CN 107353193 A CN107353193 A CN 107353193A CN 201710582138 A CN201710582138 A CN 201710582138A CN 107353193 A CN107353193 A CN 107353193A
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formic acid
methyl formate
preparation
hydrolysis
anhydrous formic
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罗秋
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Hengyang Yishun Chemical Co Ltd
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Hengyang Yishun Chemical Co Ltd
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    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C51/00Preparation of carboxylic acids or their salts, halides or anhydrides
    • C07C51/09Preparation of carboxylic acids or their salts, halides or anhydrides from carboxylic acid esters or lactones
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C51/00Preparation of carboxylic acids or their salts, halides or anhydrides
    • C07C51/42Separation; Purification; Stabilisation; Use of additives
    • C07C51/43Separation; Purification; Stabilisation; Use of additives by change of the physical state, e.g. crystallisation
    • C07C51/44Separation; Purification; Stabilisation; Use of additives by change of the physical state, e.g. crystallisation by distillation
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C67/00Preparation of carboxylic acid esters
    • C07C67/36Preparation of carboxylic acid esters by reaction with carbon monoxide or formates

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Crystallography & Structural Chemistry (AREA)
  • Carbon And Carbon Compounds (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

The present invention relates to a kind of preparation method of anhydrous formic acid, comprise the following steps:(1) methanol and carbon monoxide are transported into reactor, it is lower to be reacted in the presence of catalyst, produce methyl formate mixed liquor;(2) sodium carbonate liquor is added into methyl formate mixed liquor, methyl formate is purified;(3) by methyl formate hydrolysis, the mixed solution containing formic acid is obtained;(4) mixed solution is delivered to rectifying in rectifying column, obtains formic acid;(5) boric acid fine powder is added in formic acid, be evaporated under reduced pressure, collected 22 25 DEG C/12 18mm fractions, be anhydrous formic acid.The preparation method of anhydrous formic acid provided by the invention, concise in technology, hydrolysis rate are fast, formic acid purity is high, formic acid purity can reach 99.5%, without other byproducts, can directly prepare anhydrous formic acid, water Han Liang≤0.02% of anhydrous formic acid.

Description

A kind of preparation method of anhydrous formic acid
Technical field
The present invention relates to chemical production technical field, and in particular to a kind of preparation method of anhydrous formic acid.
Background technology
Formic acid, also referred to as formic acid, molecular formula HCOOH.Formic acid is colourless and has penetrating odor, and is corrosive, Ren Leipi Can bubble redness after skin contact.Formic acid has the property of acid and aldehyde simultaneously.In chemical industry, formic acid be used for rubber, medicine, Dyestuff, the industry of leather species.
Formic acid covered by J.-L. earliest-and Gay-Lussac oxalic acid decomposes and is made.1855~1856 years M. Bei Teluo sodium hydroxides Sodium formate is directly made with carbon monoxide, formic acid is made from sodium formate with the method for hydrolysis at first in T. Ge De-Schmidt.This method in Start within 1896 to be used for industrial production in Europe, small lot production so far is still with this method.American science Chevron Research Company (CRC), primary in 1980 Li Heng iron companies and Leo Nader company succeed in developing the method for methanol carbonyl metaplasia production formic acid, and have produced formic acid 20kt per year Factory go into operation.Obtained in addition, formic acid can also be aoxidized to reclaim in the accessory substance of acetic acid processed by light oil.
In traditional formic acid preparation method, the not purified direct hydrolysis of methyl formate obtains formic acid, and hydrolysis rate is relatively low, system It is not high for the formic acid purity gone out, waste more water resource.A kind of concise in technology is now provided, hydrolysis rate is fast, and formic acid purity is high, Without other byproducts, the preparation method of the anhydrous formic acid of anhydrous formic acid can be directly prepared.
The content of the invention
The technical problems to be solved by the invention are:Fast a kind of concise in technology, hydrolysis rate, formic acid purity height, nothing are provided Other byproducts, can directly prepare anhydrous formic acid anhydrous formic acid preparation method.
In order to solve the above technical problems, the technical scheme is that:A kind of preparation method of anhydrous formic acid, its feature exist In comprising the following steps:.
(1) methanol and carbon monoxide are transported into reactor, in the presence of catalyst, control temperature at 65-80 DEG C, Reacted under pressure 2.5-6.0MPa, produce methyl formate mixed liquor;
(2) in the presence of gas-liquid separator, sodium carbonate liquor, methanol soluble are added into the methyl formate mixed liquor In the sodium carbonate liquor, methyl formate is insoluble, and methyl formate is purified;
(3) by the methyl formate hydrolysis, 115-125 DEG C of hydrolysis temperature, the weight ratio of water and methyl formate is 2-3:1, Hydrolysis time is 1-3h, and pressure is the saturated vapor pressure of hydrolysis reaction system, obtains the mixed solution containing formic acid;
(4) mixed solution is delivered to rectifying in rectifying column, obtains formic acid;
(5) boric acid is put and gets rid of Shanghai high temperature and be dehydrated to bubble is no longer produced, gained fused mass is poured on iron plate one, puts drying Cooled down in device, be then ground to powder, boric acid fine powder is added in the formic acid, place 72h, form lump, separate clear thorough liquid It is evaporated under reduced pressure, collects 22-25 DEG C/12-18mm fractions, be anhydrous formic acid.
Preferably, the catalyst described in step (1) is sodium methoxide, and the addition of the sodium methoxide is the methanol weight 5%.
Preferably, the reaction time of step (1) is 1-2h.
Preferably, the hydrolysis temperature is 120 DEG C, and the weight ratio of water and the methyl formate is 2:1, the hydrolysis time For 1.5h.
Preferably, the method for step (4) described rectifying is, by the mixed solution and phthalic anhydride mixing infinite reflux 6h, then carry out rectifying.
Preferably, described be evaporated under reduced pressure of step (5) collects 23 DEG C/16mm fractions.
By adopting the above-described technical solution, the beneficial effects of the invention are as follows:
Methanol and carbon monoxide synthesize methyl formate in the presence of catalyst sodium methoxide;
Methyl formate purifies under sodium carbonate liquor, and methanol is dissolved in sodium carbonate liquor, methanol can be passed through into steaming after purification Purification is evaporated, is reused;
Methyl formate is after purification, it is ensured that the amount of formic acid is continuously increased in hydrolytic process, will not be due to remnants first Alcohol reduces the hydrolysis rate of methyl formate;
Boric acid is used in the preparation process of anhydrous formic acid, boric acid can reach the purpose of recycling by heating.
The preparation method of anhydrous formic acid provided by the invention, concise in technology, hydrolysis rate are fast, formic acid purity is high, formic acid is pure Degree can reach 99.5%, without other byproducts, can directly prepare anhydrous formic acid, water Han Liang≤0.02% of anhydrous formic acid.
Embodiment
The following examples are only intended to illustrate the technical solution of the present invention more clearly, therefore is only used as example, and can not Limited the scope of the invention with this.
In following examples, the addition of sodium methoxide is the 5% of methanol weight.
Embodiment 1
The preparation method of anhydrous formic acid:
(1) methanol and carbon monoxide are transported into reactor, in the presence of sodium methoxide, control temperature is at 65 DEG C, pressure Reaction 1h is carried out under power 2.5MPa, produces methyl formate mixed liquor;
(2) in the presence of gas-liquid separator, sodium carbonate liquor is added into methyl formate mixed liquor, methanol soluble is in carbon Acid sodium solution, methyl formate is insoluble, and methyl formate is purified;
(3) by methyl formate hydrolysis, 115 DEG C of hydrolysis temperature, the weight ratio of water and methyl formate is 2:1, hydrolysis time is 1h, pressure are the saturated vapor pressure of hydrolysis reaction system, obtain the mixed solution containing formic acid;
(4) by mixed solution and phthalic anhydride mixing infinite reflux 6h, rectifying is then carried out, obtains formic acid;
(5) boric acid is put and gets rid of Shanghai high temperature and be dehydrated to bubble is no longer produced, gained fused mass is poured on iron plate one, puts drying Cooled down in device, be then ground to powder, boric acid fine powder is added in formic acid, place 72h, form lump, separated clear thorough liquid and carry out It is evaporated under reduced pressure, collects 22 DEG C/12mm fractions, be anhydrous formic acid.
The purity of resulting anhydrous formic acid is detected as 99.5, and the water content of anhydrous formic acid is 0.02%.
Embodiment 2
The preparation method of anhydrous formic acid:
(1) methanol and carbon monoxide are transported into reactor, in the presence of sodium methoxide, control temperature is at 80 DEG C, pressure Reaction 2h is carried out under power 6.0MPa, produces methyl formate mixed liquor;
(2) in the presence of gas-liquid separator, sodium carbonate liquor is added into methyl formate mixed liquor, methanol soluble is in carbon Acid sodium solution, methyl formate is insoluble, and methyl formate is purified;
(3) by methyl formate hydrolysis, 125 DEG C of hydrolysis temperature, the weight ratio of water and methyl formate is 3:1, hydrolysis time is 3h, pressure are the saturated vapor pressure of hydrolysis reaction system, obtain the mixed solution containing formic acid;
(4) by mixed solution and phthalic anhydride mixing infinite reflux 6h, rectifying is then carried out, obtains formic acid;
(5) boric acid is put and gets rid of Shanghai high temperature and be dehydrated to bubble is no longer produced, gained fused mass is poured on iron plate one, puts drying Cooled down in device, be then ground to powder, boric acid fine powder is added in formic acid, place 72h, form lump, separated clear thorough liquid and carry out It is evaporated under reduced pressure, collects 25 DEG C/18mm fractions, be anhydrous formic acid.
The purity of resulting anhydrous formic acid is detected as 99.4, and the water content of anhydrous formic acid is 0.01%.
Embodiment 3
The preparation method of anhydrous formic acid:
(1) methanol and carbon monoxide are transported into reactor, in the presence of sodium methoxide, control temperature is at 70 DEG C, pressure Reaction 1.5h is carried out under power 3MPa, produces methyl formate mixed liquor;
(2) in the presence of gas-liquid separator, sodium carbonate liquor is added into methyl formate mixed liquor, methanol soluble is in carbon Acid sodium solution, methyl formate is insoluble, and methyl formate is purified;
(3) by methyl formate hydrolysis, 120 DEG C of hydrolysis temperature, the weight ratio of water and methyl formate is 2.5:1, hydrolysis time For 2h, pressure is the saturated vapor pressure of hydrolysis reaction system, obtains the mixed solution containing formic acid;
(4) by mixed solution and phthalic anhydride mixing infinite reflux 6h, rectifying is then carried out, obtains formic acid;
(5) boric acid is put and gets rid of Shanghai high temperature and be dehydrated to bubble is no longer produced, gained fused mass is poured on iron plate one, puts drying Cooled down in device, be then ground to powder, boric acid fine powder is added in formic acid, place 72h, form lump, separated clear thorough liquid and carry out It is evaporated under reduced pressure, collects 23 DEG C/13mm fractions, be anhydrous formic acid.
The purity of resulting anhydrous formic acid is detected as 99.5, and the water content of anhydrous formic acid is 0.02%.
Embodiment 4
The preparation method of anhydrous formic acid:
(1) methanol and carbon monoxide are transported into reactor, in the presence of sodium methoxide, control temperature is at 75 DEG C, pressure Reaction 1.5h is carried out under power 3.5MPa, produces methyl formate mixed liquor;
(2) in the presence of gas-liquid separator, sodium carbonate liquor is added into methyl formate mixed liquor, methanol soluble is in carbon Acid sodium solution, methyl formate is insoluble, and methyl formate is purified;
(3) by methyl formate hydrolysis, 120 DEG C of hydrolysis temperature, the weight ratio of water and methyl formate is 2:1, hydrolysis time is 1.5h, pressure are the saturated vapor pressure of hydrolysis reaction system, obtain the mixed solution containing formic acid;
(4) by mixed solution and phthalic anhydride mixing infinite reflux 6h, rectifying is then carried out, obtains formic acid;
(5) boric acid is put and gets rid of Shanghai high temperature and be dehydrated to bubble is no longer produced, gained fused mass is poured on iron plate one, puts drying Cooled down in device, be then ground to powder, boric acid fine powder is added in formic acid, place 72h, form lump, separated clear thorough liquid and carry out It is evaporated under reduced pressure, collects 23 DEG C/16mm fractions, be anhydrous formic acid.
The purity of resulting anhydrous formic acid is detected as 99.5, and the water content of anhydrous formic acid is 0.01%.
Embodiment 5
The preparation method of anhydrous formic acid:
(1) methanol and carbon monoxide are transported into reactor, in the presence of sodium methoxide, control temperature is at 75 DEG C, pressure Reaction 1.5h is carried out under power 4MPa, produces methyl formate mixed liquor;
(2) in the presence of gas-liquid separator, sodium carbonate liquor is added into methyl formate mixed liquor, methanol soluble is in carbon Acid sodium solution, methyl formate is insoluble, and methyl formate is purified;
(3) by methyl formate hydrolysis, 121 DEG C of hydrolysis temperature, the weight ratio of water and methyl formate is 3:1, hydrolysis time is 2.5h, pressure are the saturated vapor pressure of hydrolysis reaction system, obtain the mixed solution containing formic acid;
(4) by mixed solution and phthalic anhydride mixing infinite reflux 6h, rectifying is then carried out, obtains formic acid;
(5) boric acid is put and gets rid of Shanghai high temperature and be dehydrated to bubble is no longer produced, gained fused mass is poured on iron plate one, puts drying Cooled down in device, be then ground to powder, boric acid fine powder is added in formic acid, place 72h, form lump, separated clear thorough liquid and carry out It is evaporated under reduced pressure, collects 24 DEG C/15mm fractions, be anhydrous formic acid.
The purity of resulting anhydrous formic acid is detected as 99.4, and the water content of anhydrous formic acid is 0.02%.
Embodiment 6
The preparation method of anhydrous formic acid:
(1) methanol and carbon monoxide are transported into reactor, in the presence of sodium methoxide, control temperature is at 72 DEG C, pressure Reaction 1h is carried out under power 5MPa, produces methyl formate mixed liquor;
(2) in the presence of gas-liquid separator, sodium carbonate liquor is added into methyl formate mixed liquor, methanol soluble is in carbon Acid sodium solution, methyl formate is insoluble, and methyl formate is purified;
(3) by methyl formate hydrolysis, 120 DEG C of hydrolysis temperature, the weight ratio of water and methyl formate is 2.5:1, hydrolysis time For 2.5h, pressure is the saturated vapor pressure of hydrolysis reaction system, obtains the mixed solution containing formic acid;
(4) by mixed solution and phthalic anhydride mixing infinite reflux 6h, rectifying is then carried out, obtains formic acid;
(5) boric acid is put and gets rid of Shanghai high temperature and be dehydrated to bubble is no longer produced, gained fused mass is poured on iron plate one, puts drying Cooled down in device, be then ground to powder, boric acid fine powder is added in formic acid, place 72h, form lump, separated clear thorough liquid and carry out It is evaporated under reduced pressure, collects 22 DEG C/17mm fractions, be anhydrous formic acid.
The purity of resulting anhydrous formic acid is detected as 99.4, and the water content of anhydrous formic acid is 0.01%.
Various embodiments above is merely illustrative of the technical solution of the present invention, rather than its limitations;Although with reference to foregoing each reality Example is applied the present invention is described in detail, it will be understood by those within the art that:It still can be to foregoing each Technical scheme described in embodiment is modified, and either carries out equivalent substitution to which part or all technical characteristic;And These modifications are replaced, and the essence of appropriate technical solution is departed from the scope of various embodiments of the present invention technical scheme, its It all should cover among the claim of the present invention and the scope of specification.

Claims (6)

1. a kind of preparation method of anhydrous formic acid, it is characterised in that comprise the following steps:
(1) methanol and carbon monoxide are transported into reactor, in the presence of catalyst, control temperature is at 65-80 DEG C, pressure Reacted under 2.5-6.0MPa, produce methyl formate mixed liquor;
(2) in the presence of gas-liquid separator, sodium carbonate liquor is added into the methyl formate mixed liquor, methanol soluble is in institute Sodium carbonate liquor is stated, methyl formate is insoluble, and methyl formate is purified;
(3) by the methyl formate hydrolysis, 115-125 DEG C of hydrolysis temperature, the weight ratio of water and methyl formate is 2-3:1, hydrolysis Time is 1-3h, and pressure is the saturated vapor pressure of hydrolysis reaction system, obtains the mixed solution containing formic acid;
(4) mixed solution is delivered to rectifying in rectifying column, obtains formic acid;
(5) boric acid is put and gets rid of Shanghai high temperature and be dehydrated to bubble is no longer produced, gained fused mass is poured on iron plate one, put in drier Cooling, is then ground to powder, boric acid fine powder is added in the formic acid, places 72h, forms lump, separates clear thorough liquid and carries out It is evaporated under reduced pressure, collects 22-25 DEG C/12-18mm fractions, be anhydrous formic acid.
2. the preparation method of anhydrous formic acid as claimed in claim 1, it is characterised in that:Catalyst described in step (1) is first Sodium alkoxide, the addition of the sodium methoxide are the 5% of the methanol weight.
3. the preparation method of anhydrous formic acid as claimed in claim 1, it is characterised in that:The reaction time of step (1) is 1-2h.
4. the preparation method of anhydrous formic acid as claimed in claim 1, it is characterised in that:The hydrolysis temperature be 120 DEG C, water and The weight ratio of the methyl formate is 2:1, the hydrolysis time is 1.5h.
5. the preparation method of anhydrous formic acid as claimed in claim 1, it is characterised in that:The method of step (4) described rectifying is, By the mixed solution and phthalic anhydride mixing infinite reflux 6h, rectifying is then carried out.
6. the preparation method of anhydrous formic acid as claimed in claim 1, it is characterised in that:Described be evaporated under reduced pressure of step (5) is collected 23 DEG C/16mm fractions.
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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109320410A (en) * 2018-11-22 2019-02-12 湖南湘硕化工有限公司 A kind of preparation method of formic acid

Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR672161A (en) * 1928-04-07 1929-12-24 Schering Kahlbaum Ag Process for preparing anhydrous formic acid
US3907884A (en) * 1973-04-06 1975-09-23 Bethlehem Steel Corp Formic acid synthesis by lower alkyl formate hydrolysis
CN1063483A (en) * 1991-01-25 1992-08-12 北京农业大学 The novel process of preparation anhydrous formic acid
CN1066442A (en) * 1992-05-25 1992-11-25 济南石油化工二厂 Novel process with preparing aminic acid by methyl formate hydrolysis
CN1085892A (en) * 1993-04-10 1994-04-27 中国科学院成都有机化学研究所 The production method of methyl-formiate and equipment
CN1396898A (en) * 2000-01-24 2003-02-12 巴斯福股份公司 Method for producing anhydrous formic acid
CN1850777A (en) * 2006-05-29 2006-10-25 孙建民 Method and device for preparing methyl formate by methanol carbonylation
CN101125795A (en) * 2007-09-30 2008-02-20 四川天一科技股份有限公司 Method for preparing formic acid

Patent Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR672161A (en) * 1928-04-07 1929-12-24 Schering Kahlbaum Ag Process for preparing anhydrous formic acid
US3907884A (en) * 1973-04-06 1975-09-23 Bethlehem Steel Corp Formic acid synthesis by lower alkyl formate hydrolysis
CN1063483A (en) * 1991-01-25 1992-08-12 北京农业大学 The novel process of preparation anhydrous formic acid
CN1066442A (en) * 1992-05-25 1992-11-25 济南石油化工二厂 Novel process with preparing aminic acid by methyl formate hydrolysis
CN1085892A (en) * 1993-04-10 1994-04-27 中国科学院成都有机化学研究所 The production method of methyl-formiate and equipment
CN1396898A (en) * 2000-01-24 2003-02-12 巴斯福股份公司 Method for producing anhydrous formic acid
CN1850777A (en) * 2006-05-29 2006-10-25 孙建民 Method and device for preparing methyl formate by methanol carbonylation
CN101125795A (en) * 2007-09-30 2008-02-20 四川天一科技股份有限公司 Method for preparing formic acid

Non-Patent Citations (4)

* Cited by examiner, † Cited by third party
Title
姚迎等主编: "《化学知识辞典》", 30 September 1995 *
程能林: "《溶剂手册 第2版》", 30 September 1994 *
章江洪等: "一氧化碳、甲醇液相羰基合成甲酸甲酯的助催化研究", 《云南化工》 *
谢克昌等主编: "《甲醇及其衍生物》", 30 September 2002 *

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109320410A (en) * 2018-11-22 2019-02-12 湖南湘硕化工有限公司 A kind of preparation method of formic acid

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