CN103880665A - Methyl stearate production method - Google Patents

Methyl stearate production method Download PDF

Info

Publication number
CN103880665A
CN103880665A CN201210565612.6A CN201210565612A CN103880665A CN 103880665 A CN103880665 A CN 103880665A CN 201210565612 A CN201210565612 A CN 201210565612A CN 103880665 A CN103880665 A CN 103880665A
Authority
CN
China
Prior art keywords
methanol
reaction
methyl stearate
stearic acid
production method
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
CN201210565612.6A
Other languages
Chinese (zh)
Inventor
王明夫
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.)
QINGDAO SHUAIWANG OIL CHEMICAL CO Ltd
Original Assignee
QINGDAO SHUAIWANG OIL 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 QINGDAO SHUAIWANG OIL CHEMICAL CO Ltd filed Critical QINGDAO SHUAIWANG OIL CHEMICAL CO Ltd
Priority to CN201210565612.6A priority Critical patent/CN103880665A/en
Publication of CN103880665A publication Critical patent/CN103880665A/en
Pending legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C67/00Preparation of carboxylic acid esters
    • C07C67/08Preparation of carboxylic acid esters by reacting carboxylic acids or symmetrical anhydrides with the hydroxy or O-metal group of organic compounds

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

The invention discloses a methyl stearate production method. The method comprises the following steps: adding stearic acid and methanol into a reaction kettle according to a weight part ratio of 10-20:30-50, adding paratoluenesulfonic acid having an amount accounting for 1.2% of the mass of stearic acid and 1-5 parts of zinc oxide as catalysts, heating to 100DEG C, continuously adding methanol from the bottom of the reaction kettle through a drop funnel, maintaining the entrance and exit balance of methanol, reacting for 2.5-3.5h, cooling to 50DEG C after the above reaction, washing with an aqueous solution of sodium bicarbonate, washing with water to neutrality, and carrying out negative pressure distillation to remove water in order to obtain methyl stearate. The method has the advantages of less methanol consumption, small environmental pollution, energy consumption reduction, reaction efficiency improvement, substantial shortening of the reaction time, and yield improvement.

Description

A kind of production method of methyl stearate
Technical field
The present invention relates to a kind of production method of methyl stearate.
Background technology
The western purport of stearic acid first is a kind of important industrial chemicals during modern industry is produced, and has important purposes at industrial circles such as detergents and cosmetic, coating, oilfield chemistries.
Summary of the invention
Technical problem to be solved by this invention is: the production method that a kind of methyl stearate is provided.
For solving the problems of the technologies described above, the technical solution used in the present invention is:
A kind of production method of methyl stearate, by stearic acid and the methyl alcohol ratio input reactor of 10-20:30-50 by weight, add the tosic acid of stearic acid quality 1.2% and 1-5 part zinc oxide as catalyzer, be warming up to after 100 degrees Celsius, methyl alcohol is continued to add from reactor bottom by dripping night funnel, keep methyl alcohol turnover balance, reaction 2.5-3.5 hour, after reaction finishes, be cooled to 50 degrees Celsius, with sodium bicarbonate aqueous solution washing, then be washed to neutrality, then negative pressure boils off moisture, obtains methyl stearate.
The invention has the beneficial effects as follows: methanol usage is few, environmental pollution is little, has reduced energy consumption, has improved reaction efficiency, has greatly shortened the reaction times, improves productive rate.
Embodiment
Embodiment 1
A kind of production method of methyl stearate, by stearic acid and the methyl alcohol ratio input reactor of 10-20:30-50 by weight, add the tosic acid of stearic acid quality 1.2% and 1-5 part zinc oxide as catalyzer, be warming up to after 100 degrees Celsius, methyl alcohol is continued to add from reactor bottom by dripping night funnel, keep methyl alcohol turnover balance, reaction 2.5-3.5 hour, after reaction finishes, be cooled to 50 degrees Celsius, with sodium bicarbonate aqueous solution washing, then be washed to neutrality, then negative pressure boils off moisture, obtains methyl stearate.

Claims (1)

1. the production method of a methyl stearate, it is characterized in that, by stearic acid and the methyl alcohol ratio input reactor of 10-20:30-50 by weight, add the tosic acid of stearic acid quality 1.2% and 1-5 part zinc oxide as catalyzer, be warming up to after 100 degrees Celsius, methyl alcohol is continued to add from reactor bottom by dripping night funnel, keep methyl alcohol turnover balance, reaction 2.5-3.5 hour, after reaction finishes, is cooled to 50 degrees Celsius, wash with sodium bicarbonate aqueous solution, be washed to neutrality, then negative pressure boils off moisture again, obtains methyl stearate.
CN201210565612.6A 2012-12-24 2012-12-24 Methyl stearate production method Pending CN103880665A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201210565612.6A CN103880665A (en) 2012-12-24 2012-12-24 Methyl stearate production method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201210565612.6A CN103880665A (en) 2012-12-24 2012-12-24 Methyl stearate production method

Publications (1)

Publication Number Publication Date
CN103880665A true CN103880665A (en) 2014-06-25

Family

ID=50949835

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201210565612.6A Pending CN103880665A (en) 2012-12-24 2012-12-24 Methyl stearate production method

Country Status (1)

Country Link
CN (1) CN103880665A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109317193A (en) * 2018-11-12 2019-02-12 上海第二工业大学 A kind of application of Fe-SAPO-34 catalyst in methyl stearate synthesis

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109317193A (en) * 2018-11-12 2019-02-12 上海第二工业大学 A kind of application of Fe-SAPO-34 catalyst in methyl stearate synthesis

Similar Documents

Publication Publication Date Title
CN101948386B (en) Method for preparing 2,2,4-trimethyl-1,3-pentanediol monoisobutyrate
CN102260174B (en) Application of solid acid catalyst in preparation of 2,5-dichloronitrobenzene
CN103086891A (en) Preparation method of plasticizer diethylene glycol dibenzoate
CN105646226A (en) Plasticizer tributyl citrate production process
CN103880665A (en) Methyl stearate production method
CN108043456A (en) A kind of polyacid class ionic-liquid catalyst, preparation method and the method for preparing cyclohexanol with its catalysis ethyl cyclohexyl ester hydrolysis
CN106083685A (en) A kind of preparation method of phenyl piracetam
CN104230716A (en) Method for enhancing nitration reaction rate of 2,5-dichloronitrobenzene
CN103113234B (en) Method for synthesizing N-methyl paranitroaniline
CN106083585A (en) A kind of method that dimethyl carbonate is prepared in indirect alcoholysis
CN102231404A (en) Technology for cleaning solar monocrystalline wafer
CN112645815A (en) Preparation method for catalytically synthesizing methyl cinnamate based on eutectic solvent
CN203507997U (en) Reaction kettle neutralization and water-washing device
CN201799201U (en) Process tail gas spray absorber
CN201959964U (en) Improved bottle washing machine
CN101671303B (en) Process for directly synthesizing caprolactam by using cyclohexanone
CN103788979A (en) Preparation of biodiesel oil by industrial sonochemical technology
CN103524336A (en) Preparation method of 2-(4-pentyloxybenzoyl) benzoic acid with high secondary-tertiary ratio
CN104475110B (en) Catalyst for preparing Guerbet alcohol and preparation method for catalyst for preparing Guerbet alcohol
CN103819338A (en) Preparation method for alpha-methyl-diglycollic acid-diethyl ester
MX2012002249A (en) Method for carboxylic acid esterification.
CN103803612A (en) Preparation method of basic magnesium sulfate
CN203866230U (en) Device for producing 3, 4-dichloroaniline through continuous kettle reaction
CN202011847U (en) Urotropine mother liquor circulating device
CN105753740A (en) Catalytic synthesis method for methyl carbamate

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C02 Deemed withdrawal of patent application after publication (patent law 2001)
WD01 Invention patent application deemed withdrawn after publication

Application publication date: 20140625