CN1057471A - The production method of epoxy grease plasticizer - Google Patents

The production method of epoxy grease plasticizer Download PDF

Info

Publication number
CN1057471A
CN1057471A CN 90105315 CN90105315A CN1057471A CN 1057471 A CN1057471 A CN 1057471A CN 90105315 CN90105315 CN 90105315 CN 90105315 A CN90105315 A CN 90105315A CN 1057471 A CN1057471 A CN 1057471A
Authority
CN
China
Prior art keywords
epoxy
production method
soybean oil
oleum gossypii
gossypii semen
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
CN 90105315
Other languages
Chinese (zh)
Inventor
王利生
阎秀莲
王长华
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.)
PLASTIC ASSISTANTS CHEMICAL PLANT OF LELING CITY
Original Assignee
PLASTIC ASSISTANTS CHEMICAL PLANT OF LELING CITY
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 PLASTIC ASSISTANTS CHEMICAL PLANT OF LELING CITY filed Critical PLASTIC ASSISTANTS CHEMICAL PLANT OF LELING CITY
Priority to CN 90105315 priority Critical patent/CN1057471A/en
Publication of CN1057471A publication Critical patent/CN1057471A/en
Pending legal-status Critical Current

Links

Landscapes

  • Beans For Foods Or Fodder (AREA)
  • Medicines Containing Plant Substances (AREA)

Abstract

A kind of production method of epoxy grease plasticizer.Be under the condition that does not add any solvent, make raw material with Oleum Gossypii semen or soybean oil, hydrogen peroxide, Glacial acetic acid and the vitriol oil with lower concentration, synthetic epoxy grease plasticizer under conditions such as certain temperature, time, proportioning, it is the softening agent that is used for polyvinyl chloride, in the polyvinyl chloride course of processing, do not produce toxic smog contaminate environment and injury human body.

Description

The production method of epoxy grease plasticizer
A kind of production method of epoxy grease plasticizer.
Technical field under the present invention is the synthetic of organic compound.
Before the present invention, in the suitability for industrialized production technology of synthesizing epoxy Oleum Gossypii semen and epoxy soybean oil, all use hydrogen peroxide, Glacial acetic acid and the sulfuric acid of high density and Oleum Gossypii semen or soybean oil as reactive material, most technologies need add certain solvent, as: benzene, acetone, ethyl acetate etc., so that reaction is easy to carry out.This method is produced epoxy Oleum Gossypii semen and epoxy soybean oil, often is subjected to the restriction in high density hydrogen peroxide source, moreover remaining in the product of being produced a spot of noxious solvent is arranged, caused in the polyvinyl chloride course of processing of using this product, produce toxic smog, contaminate environment, injury human body.
The present invention has proposed new technical scheme in order to overcome the deficiency of above-mentioned prior art.Purpose of the present invention just is to seek under the condition that does not add any solvent, Oleum Gossypii semen or soybean oil are carried out the novel process of epoxidation reaction with lower concentration hydrogen peroxide, Glacial acetic acid and the vitriol oil, shorten technology to reach, reduce cost the purpose of each factor of decontamination product.
In order to achieve the above object, the invention provides a kind of epoxy Oleum Gossypii semen of totally nontoxic and the production method of epoxy soybean oil.It is by adopting the hydrogen peroxide of lower concentration, condition such as proportioning raw materials such as hydrogen peroxide, organic acid and mineral acid and temperature of reaction, time in the conditioned reaction system, realized under the condition that no any solvent exists, with lower concentration hydrogen peroxide, Glacial acetic acid and the vitriol oil respectively with handle or untreated Oleum Gossypii semen or soybean oil are carried out the novel process of building-up reactions; The excess acid of , Can Liu in system when reaction finishes neutralizes with the aqueous sodium carbonate of 1-30%.
Concrete grammar of the present invention is:
To Oleum Gossypii semen or soybean oil handling: with unpurified Oleum Gossypii semen or soybean oil, use the 2-40% aqueous sodium hydroxide solution, under 20-80 ℃, fully stir, carry out neutralizing treatment, then with centrifugal soap machine separating out fat acid sodium-salt and the moisture of taking off.
1, the epoxy Oleum Gossypii semen is synthetic:
To handle or 100 parts of undressed Oleum Gossypii semens hydrogen peroxide solution 50-85 part of 25-30%, Glacial acetic acid 10-30 part, vitriol oil 0.50-5 part in 35-70 ℃ temperature range, is fully stirred, epoxidation reaction was carried out 5-40 hour, and standing demix is told sour water.
Sodium carbonate solution with 1-30% neutralizes to above-mentioned system, uses 50-90 ℃ hot wash 2-6 time again, removes the moisture of Can Liu then with decompression.The oxirane value of the epoxy Oleum Gossypii semen that present method makes is between 4.0-5.5, and iodine number is below 6.
The epoxy Oleum Gossypii semen of producing in this way with its plastifying polyvinyl chloride test piece, records its mechanical property, transparency and heat aging performance, and the epoxy soybean oil of producing with prior art is suitable.
2, epoxy soybean oil is synthetic:
To handle or 100 parts of undressed soybean oil, hydrogen peroxide solution 60-95 part of 25-30%, Glacial acetic acid 10-30 part, vitriol oil 0.50-5 part in 35-70 ℃ of scope, is fully stirred, and epoxidation reaction was carried out 5-40 hour, and standing demix is told sour water.
Sodium carbonate solution with 1-30% neutralizes to above-mentioned system, uses 50-90 ℃ hot wash 2-6 time again, removes the moisture of Can Liu then with decompression.The oxirane value of the epoxy soybean oil that present method makes is between 6.0-7.0, and iodine number is below 6.
The epoxy soybean oil of producing in this way, with its plastifying polyvinyl chloride test piece, the epoxy soybean oil that records the production of its mechanical property, transparency and heat aging performance and prior art is suitable.
Show through toxicity test in order to prepared epoxy Oleum Gossypii semen of last method and epoxy soybean oil: the LD50 value:
Rat (oral)>20ml/kg
Rabbit (subcutaneous injection)>20ml/kg
Epoxy Oleum Gossypii semen and epoxy soybean oil are nontoxic softening agent of a class and stablizer, and their volatility is little, and resistance to migration is good, especially can improve light, the thermostability of polrvinyl chloride product; It is the softening agent that can be used for packaging material for food that a class is generally acknowledged.The production method of epoxy grease plasticizer of the present invention, advantage compared with the prior art is: prior art adopts the hydrogen peroxide of high density, and this raw material is subject to certain restrictions, the domestic production amount seldom, its production technique adopts solubilizing agent to promote reaction to carry out more; And production method of the present invention is to adopt the hydrogen peroxide of lower concentration, and abundant raw material need not add any solvent in the production process, thereby has obtained simplification technology, the technique effect that reduces cost; In the product that prior art is produced,, thereby caused in the polyvinyl chloride course of processing, emitting toxic smog because there is a small amount of noxious solvent, contaminate environment, the injury person, when using, then there are not these defectives in the product that the present invention produced.
Embodiments of the invention:
Embodiment 1: 100 parts of the Oleum Gossypii semens of handling, 75 parts in 27% hydrogen peroxide, 15 parts in Glacial acetic acid, 1.5 parts of the vitriol oils, under 50-60 ℃, reacted 10 hours, standing demix neutralizes with 15% sodium carbonate solution, with 60 ℃ washings 4 times, moisture is removed in decompression, and the oxirane value of its product epoxy Oleum Gossypii semen is 5.0, and iodine number is 3.2.
Embodiment 2: 100 parts of the soybean oil of handling, 85 parts in 27% hydrogen peroxide, 18 parts in Glacial acetic acid, 2 parts of the vitriol oils reacted 12 hours down at 55-60 ℃, standing demix, with the neutralization of 15% sodium carbonate solution, with 50 ℃ washings 3 times, moisture is removed in decompression, the oxirane value of its product epoxy soybean oil is 6.5, iodine number 5.0.
Embodiment 3: 100 parts of untreated Oleum Gossypii semens, 80 parts in 25% hydrogen peroxide, 15 parts in Glacial acetic acid, 4 parts of the vitriol oils, under 55-60 ℃, reacted 7 hours, standing demix neutralizes with 15% sodium carbonate solution, with 55 ℃ washings 2 times, moisture is removed in decompression, and the oxirane value of its product epoxy Oleum Gossypii semen is 4.5, iodine number 4.0.

Claims (7)

1, a kind of production method of epoxy grease plasticizer is characterized in that reacting with Oleum Gossypii semen or soybean oil respectively with lower concentration hydrogen peroxide, Glacial acetic acid and the vitriol oil without any in the presence of the solvent, generates epoxy Oleum Gossypii semen or epoxy soybean oil.
2, according to the production method of claim 1 said epoxy grease plasticizer, it is characterized in that concentration is that the consumption of the hydrogen peroxide of 25-30% is the 50-85% of Oleum Gossypii semen consumption, be the 60-95% of soybean oil consumption.
3,, it is characterized in that used Glacial acetic acid amount is the 10-30% of Oleum Gossypii semen or soybean oil consumption according to the production method of claim 1 or 2 said epoxy grease plasticizers.
4,, it is characterized in that used vitriol oil amount is the 0.5-5% of Oleum Gossypii semen or soybean oil consumption according to the production method of claim 1 or 2 said epoxy grease plasticizers.
5,, it is characterized in that temperature of reaction is 35-70 ℃ according to the production method of claim 1 said epoxy grease plasticizer.
6,, it is characterized in that the reaction times is 5-40 hour according to the production method of claim 1 said epoxy grease plasticizer.
7, according to the production method of claim 1 said epoxy grease plasticizer, it is characterized in that epoxidation reaction finishes after, with in the sodium carbonate solution of 1-30% and excessive acid.
CN 90105315 1990-06-15 1990-06-15 The production method of epoxy grease plasticizer Pending CN1057471A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 90105315 CN1057471A (en) 1990-06-15 1990-06-15 The production method of epoxy grease plasticizer

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN 90105315 CN1057471A (en) 1990-06-15 1990-06-15 The production method of epoxy grease plasticizer

Publications (1)

Publication Number Publication Date
CN1057471A true CN1057471A (en) 1992-01-01

Family

ID=4879140

Family Applications (1)

Application Number Title Priority Date Filing Date
CN 90105315 Pending CN1057471A (en) 1990-06-15 1990-06-15 The production method of epoxy grease plasticizer

Country Status (1)

Country Link
CN (1) CN1057471A (en)

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101225236B (en) * 2007-12-19 2010-06-16 江苏飞翔化工股份有限公司 Composition used for polychloroethylene resin plasticizer and method of use thereof
CN101824368A (en) * 2010-04-14 2010-09-08 太仓市天盈化工有限公司 Method for preparing epoxidized soybean oil
CN102250688A (en) * 2011-06-21 2011-11-23 广州市新锦龙实业有限公司 Method for dynamically separating epoxidized soybean oil at high speed
CN102250693A (en) * 2011-06-21 2011-11-23 广州市新锦龙实业有限公司 Process flow for preparing epoxidized soybean oil by using crude soybean oil
CN102617888A (en) * 2011-12-09 2012-08-01 江南大学 Preparation of environment friendly calcium-zinc composite heat stabilizer and its application in PVC (polrvinyl chloride)
CN103044755A (en) * 2012-11-25 2013-04-17 安徽六方重联机械股份有限公司 Preparation method of package-purposed plastic-based film containing modified nano celestite powder
CN103044741A (en) * 2012-11-25 2013-04-17 安徽六方重联机械股份有限公司 Preparation method of package-purposed plastic-based film containing dibutyl maleate
CN114907750A (en) * 2022-04-15 2022-08-16 书香门地集团股份有限公司 Flame retardant, preparation method thereof and application of flame retardant in preparation of flame-retardant floor

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101225236B (en) * 2007-12-19 2010-06-16 江苏飞翔化工股份有限公司 Composition used for polychloroethylene resin plasticizer and method of use thereof
CN101824368A (en) * 2010-04-14 2010-09-08 太仓市天盈化工有限公司 Method for preparing epoxidized soybean oil
CN102250688A (en) * 2011-06-21 2011-11-23 广州市新锦龙实业有限公司 Method for dynamically separating epoxidized soybean oil at high speed
CN102250693A (en) * 2011-06-21 2011-11-23 广州市新锦龙实业有限公司 Process flow for preparing epoxidized soybean oil by using crude soybean oil
CN102250693B (en) * 2011-06-21 2013-12-11 广州市新锦龙实业有限公司 Process flow for preparing epoxidized soybean oil by using crude soybean oil
CN102617888A (en) * 2011-12-09 2012-08-01 江南大学 Preparation of environment friendly calcium-zinc composite heat stabilizer and its application in PVC (polrvinyl chloride)
CN103044755A (en) * 2012-11-25 2013-04-17 安徽六方重联机械股份有限公司 Preparation method of package-purposed plastic-based film containing modified nano celestite powder
CN103044741A (en) * 2012-11-25 2013-04-17 安徽六方重联机械股份有限公司 Preparation method of package-purposed plastic-based film containing dibutyl maleate
CN103044755B (en) * 2012-11-25 2016-03-02 安徽六方重联机械股份有限公司 A kind of preparation method of the packaging plastic substrate film containing modified Nano celestite powder
CN114907750A (en) * 2022-04-15 2022-08-16 书香门地集团股份有限公司 Flame retardant, preparation method thereof and application of flame retardant in preparation of flame-retardant floor

Similar Documents

Publication Publication Date Title
CN1057471A (en) The production method of epoxy grease plasticizer
KR970009896B1 (en) Method of preparing intermediate as starch esters in aqueous solution
Nakajima et al. ϵ-N-Trimethyl-l-δ-hydroxylysine phosphate and its nonphosphorylated compound in diatom cell walls
KR830007654A (en) 5-Aroylation Method of 1,2-dihydro-3H-pyrrolo [1,2-a] pytone-1-carboxylate
CN101914076A (en) Method for preparing non-toxic environmental-friendly epoxy plasticizer
MY102444A (en) Process for the production of color-stable, light colored, aqueous salt pastes of wash-active (alpha)- sulfofatty acid esters
ATE71412T1 (en) METHOD OF RECOVERING RHODIUM.
CN1064370C (en) Process for extraction of plant protein and use thereof
ATE315339T1 (en) LATE ADDING OF POLYUNSATURATED FATTY ACIDS IN AN INFANT FOOD PRODUCTION PROCESS
CN104938763A (en) Method for separating proteins from corn original pulp
CN86104989A (en) A kind of production method of epoxy soybean oil
FI66195B (en) FOERFARANDE FOER NEDSAETTNING AV KCENTRATION AV EN FOERORENING
CN112473181A (en) Method for removing odor of biological extract
CN1173998A (en) Compound feed antifermenting and antioxidizing agent and its production process
US4401811A (en) Process for the production of a cation exchanger: tree bark treated with alkali and sulfuric acid for waste water treatment
CN111100896A (en) Preparation method of protein peptide molybdenum chelate suitable for ruminant animals
IE51018B1 (en) Stabilization of pleuromutilin derivatives against oxidation by sodium hypochlorite in aqueous solution
ATE124063T1 (en) USE OF AQUEOUS SOLUTIONS OR DISPERSIONS OF OLIGOURETHANES CONTAINING (METH)-ACRYLOYL GROUPS FOR THE PRODUCTION OF COATING AGENTS AND SUITABLE AQUEOUS SOLUTIONS OR DISPERSIONS FOR THIS.
KR100719481B1 (en) Preparation method of anion degreasing agent using the lard oil
US3082222A (en) Steroid acid-esters and salts thereof, and method of making the same
JPS5538363A (en) Preparation of optically active n-mercaptoacyl-imino acid
CN1057052A (en) After-treatment of methyl glucoside
JPS62148449A (en) Production of oleic acid
CN116693390A (en) Composition of cetostearyl alcohol and fatty acid, and preparation method and application thereof
SE8205619L (en) PROCEDURE FOR THE PREPARATION OF ARSENIC 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
C01 Deemed withdrawal of patent application (patent law 1993)
WD01 Invention patent application deemed withdrawn after publication