CN105669443A - Method of preparing tributyl citrate with nano-scale intercalated hydrotalcite catalyst - Google Patents

Method of preparing tributyl citrate with nano-scale intercalated hydrotalcite catalyst Download PDF

Info

Publication number
CN105669443A
CN105669443A CN201511012936.7A CN201511012936A CN105669443A CN 105669443 A CN105669443 A CN 105669443A CN 201511012936 A CN201511012936 A CN 201511012936A CN 105669443 A CN105669443 A CN 105669443A
Authority
CN
China
Prior art keywords
nanoscale
catalyst
tributyl citrate
intercalated houghite
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.)
Pending
Application number
CN201511012936.7A
Other languages
Chinese (zh)
Inventor
陈祥
杨旭忠
张勇
赵重光
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.)
JIANGSU RUIJIA CHEMICAL CO Ltd
Original Assignee
JIANGSU RUIJIA 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 JIANGSU RUIJIA CHEMICAL CO Ltd filed Critical JIANGSU RUIJIA CHEMICAL CO Ltd
Priority to CN201511012936.7A priority Critical patent/CN105669443A/en
Publication of CN105669443A publication Critical patent/CN105669443A/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

Abstract

The invention discloses a method of preparing tributyl citrate with a nano-scale intercalated hydrotalcite catalyst. The method includes the steps of: A) material addition: adding the nano-scale intercalated hydrotalcite catalyst, citric acid, and excessive butyl alcohol into a container with uniform stirring; B) esterification reaction: heating the container in oil bath, and performing reflux condensation for separating water generated in the reaction, wherein the esterification reaction time is 6-10 h; C) purification, when the esterification reaction is finished, filtering the nano-scale intercalated hydrotalcite catalyst away, and neutralizing, water-washing, dealcoholizing and decoloring, and purifying reaction products to obtain the tributyl citrate. Through the method, the conversion rate on the citric acid is increased and the purity of the product is improved with the nano-scale intercalated hydrotalcite catalyst for producing the tributyl citrate. The whole catalytic reaction is easy to operate, the reaction temperature is easy to control, and the catalyst can be reused after filtration.

Description

A kind of method of nanoscale intercalated houghite catalyst preparing tributyl citrate
Technical field
The present invention relates to chemical catalysis method, be specifically related to a kind of method utilizing hydrotalcite catalyst to prepare tributyl citrate.
Background technology
Tri-n-butyl citrate, chemical name 3-hydroxyl-3-carboxyl 1,3-propanedicarboxylic acid tributyl, is a kind of ester type compound, and water white transparency high boiling liquid is slightly soluble in water, dissolves each other with most organic solvents. Industrial general reaction with n-butyl alcohol by citric acid forms, and can be directly used for plasticizer, it is possible to be further processed into the plasticizer tributyl 2-acetylcitrate of function admirable. Tributyl citrate (TBC) nontoxic odorless, plasticizing efficiency is high, it is widely used in the fields such as packaging material for food, medical apparatus, toy for children and personal hygiene article, becomes " green " substitute products of phthalic ester plasticizer, have wide market prospect.
In commercial production, citric acid generates tributyl citrate with n-butyl alcohol at catalyst and effect under water preparation exists of holding under the arm, obtains product through operations such as dealcoholysis, neutralization, washing, stripping, decolouring, filter pressings. Conventional catalyst is inorganic or organic acid, and holding water preparation under the arm is n-butyl alcohol itself.
The catalyst adopted in conventional synthesis TBC method mostly is concentrated sulphuric acid, and the method exists that esterifying efficiency is low, equipment corrosion serious, easily produces side reaction and produce the shortcomings such as substantial amounts of acid waste water, contaminated environment. In recent years, the catalyst finding replacement concentrated sulphuric acid has become the focus in commercial production research.
" new method of Catalytic Synthesis of Tri-n-butyl Citrate " (Zheng Yu, Wang Jiye, Tan Mingchuan, Zheng Shiqing, " organic chemical industry and catalysis ", in April, 2004) literary composition have studied the reaction with butyl titanate for catalyst synthesizing citric acid tributyl.
The domestic article also having some research solid acid catalyst synthesizing citric acid tributyls at present, if Period In Maoming institute chemistry and Life Science College Qiao Yan brightness etc. are at solid super-strong acid S2O8 2-/SnO2-SiO2Catalysis under, with citric acid and the n-butyl alcohol tributyl citrate that has been Material synthesis. Changjiang University's chemistry with Environmental Engineering School in soldier river etc. with complex solid superacid SO4 2-/ZrO2-TiO2Synthesize tributyl citrate for catalyst, investigate the impact on reaction of catalyst amount, rate of charge and reaction end temperature.
But in above-mentioned numerous researchs all rare have utilize polyacid to be inserted into hydrotalcite catalyst to carry out the research of catalytic citric acid tributyl.
Hydrotalcite intercalation material (LDHs) is the novel nano inorganic functional material that a class has layer structure, and it is similar to that shepardite, and composition formula can be expressed as: [M2+ 1-xM3+ x(OH)2]x+(An-) x/n mH2O, wherein M2+And M3+The respectively metal cation of bivalence and trivalent in laminate, as: Mg2+、Ni2+、Co2+、Zn2+、Cu2+And Al3+、Cr3+、Fe3+Deng; An-It is interlayer anion, as: CO3 2-、NO3 -、Cl-、OH-、SO4 2-、PO4 3-、C6H4(COO)2 2-, heteropolyanion etc.; X is M3+/ (M2++M3+) molar ratio, its value is typically between 0.1~0.5; M is the number of intermediary water molecule. Metal cation on LDHs laminate, due to the impact by the minimum effect of lattice energy and lattice orientation effect thereof, is uniformly distributed in a certain way on laminate so that in the construction unit that on laminate, each is small, and its chemical composition and structure is constant. Simultaneously, being positioned at the divalent metal on laminate can in certain proportion scope by the close trivalent metal cation isomorphous substitution of ionic radius, the Modulatory character of this chemical composition and the microscopic uniformity of structure so that it is become composite structure and form the good precursor material of uniform metal composite oxide.
Polyacid compound is the poly-metal deoxide that a class contains the metals such as V, Mo, W. Being same polyanionic by what oxyacid radical ion condensation of the same race was formed, isopolyacid is in its acid. Being heteropolyanion by what different types of oxygen-containing acid group anionic condensation was formed, heteropoly acid is in its acid. The atom being currently known nearly 70 kinds of elements can as the hetero atom in heteropoly acid, including whole First Series transition elements, second and third series transition elements most, adds B, Al, Ga, Si, Ge, Sn, P, As, Sb, Bi, Se, Te, I etc. And every kind of hetero atom often can different valence state be present in heteropolyanion, so kind is quite various.
Polyacid intercalation hydrotalcite catalyst is as active high with selectivity, the advantage such as corrosivity is little and reaction condition is gentle of catalyst, but its reaction condition is bad to be groped, in present specification namely novelty utilize polyacid intercalation hydrotalcite catalyst to carry out catalytic reaction to prepare tributyl citrate.
Summary of the invention
The present invention is based on the analysis of the production method of tributyl citrate of the prior art, and the research of polyacid intercalation hydrotalcite catalyst performance, creationary proposition utilizes polyacid intercalation hydrotalcite catalyst to carry out the production of catalytic citric acid tributyl, and grope concrete working condition, the preparation method obtaining maturation. This preparation method can effectively carry out the production to tributyl citrate, final products finished product colourity is in 5#-10#(Pt-Co colorimetry), citric acid conversion ratio >=99%, compared with the production method of the tributyl citrate of prior art, has significant technological progress.
For realizing said method, technical scheme disclosed by the invention is as follows:
A kind of method of nanoscale intercalated houghite catalyst preparing tributyl citrate, comprises the steps:
Step a, reinforced: addition nanoscale intercalated houghite catalyst, citric acid, excessive butanol toward container in, stir;
Step b, esterification: oil bath is heated, the water that condensing reflux separating reaction generates; The time of esterification is 6h-10h;
Step c, purification: after reaction to be esterified terminates, filter nanoscale intercalated houghite catalyst, is then passed through neutralization, washing, dealcoholysis decolouring, purification step obtain finished lemon/lime acid tributyl.
Preferably, time reinforced in step a, the mol ratio of citric acid and butanol is 1:(4-6).
Preferably, described citric acid is 1:(0.03 ~ 0.05 with the mass ratio of nanoscale intercalated houghite catalyst).
Preferably, in step b, oil bath is heated, and maintains reaction temperature between 130-140 DEG C.
Preferably, in step c, esterification terminates rear system and is cooled in 75-80 DEG C of backward container and adds 5-10%Na2CO3Solution is neutralized reaction, controls system pH=8 ~ 9; Neutralization reaction performs twice at.
Preferably, described nanoscale hydrotalcite catalyst is introducing the 3rd metal component M in brucite laminate, improves carrier acid-resisting, and it consists of MMgAl-LDHs type intercalation catalyst. In the present invention, the 3rd described metal component M is Zn.
Preferably, described nanoscale intercalated houghite catalyst is the one of the magnesium aluminum-hydrotalcite of polyacid intercalation, zinc-aluminum hydrotalcite.
Preferably, the chemical formula of the anion of described polyacid is [XM11CoO39]n-, wherein X=P or Si; M=W or Mo; N is valence number, n=5-6.
By introducing the 3rd metal component M in brucite laminate in the present invention, improving carrier acid-resisting, it consists of MMgAl-LDHs type intercalation catalyst; And this MMgAl-LDHs type intercalation catalyst is nm-class catalyst, it is ensured that the accessibility of dispersion, reactant and substrate.
In the present invention, nanoscale intercalation catalyst is reusable edible after filtering, and activating component not easily runs off, long service life.
The present invention utilizes nanoscale intercalated houghite catalyst preparing tributyl citrate, after catalyst completes in the reaction, can reuse after filtration, compared with liquid catalyst, not only convenient recovery uses, and eliminate remove impurity operation, and avoid the possible side reaction brought in liquid catalyst.
The invention has the beneficial effects as follows: the employing nanoscale intercalated houghite of the invention does catalyst preparing tributyl citrate, not only increase citric acid conversion ratio >=99%, and the product purity prepared is higher, finished product colourity is 5#-10#(Pt-Co colorimetry); And whole catalytic reaction is easily operated, temperature is easily controllable, and catalyst may filter that rear Reusability, is greatly saved cost, improves production efficiency.
Detailed description of the invention
Below presently preferred embodiments of the present invention is described in detail, so that advantages and features of the invention can be easier to be readily appreciated by one skilled in the art, thus protection scope of the present invention being made apparent clear and definite defining.
Embodiment 1: a kind of method of nanoscale intercalated houghite catalyst preparing tributyl citrate, comprises the steps:
Step a, reinforced: addition nanoscale intercalated houghite catalyst, citric acid, excessive butanol toward container in, stir; Time reinforced, the mol ratio of citric acid and butanol is 1:(4-6); The mass ratio of citric acid and nanoscale intercalated houghite catalyst is 1:(0.03 ~ 0.05);
Step b, esterification: oil bath is heated, maintain reaction temperature between 130-140 DEG C; The water that condensing reflux separating reaction generates; The time of esterification is 6h-10h;
Step c, purification: after reaction to be esterified terminates, filter nanoscale intercalated houghite catalyst, is then passed through neutralization, washing, dealcoholysis decolouring, purification step obtain finished lemon/lime acid tributyl.
Nanoscale hydrotalcite catalyst described in the present embodiment is introducing the 3rd metal component M in brucite laminate, improves carrier acid-resisting, and it consists of MMgAl-LDHs type intercalation catalyst;Described nanoscale intercalated houghite catalyst is the one of the magnesium aluminum-hydrotalcite of polyacid intercalation, zinc-aluminum hydrotalcite.
Embodiment 2: the present embodiment and embodiment 1 are different in that, in the present embodiment, in step c, it is the Na of 5-10% that esterification terminates that rear system be cooled in 75-80 DEG C of backward container to add mass fraction2CO3Solution is neutralized reaction, controls system pH=8 ~ 9; Neutralization reaction performs twice at.
Embodiment 3: the present embodiment and embodiment 1 are different in that, in the present embodiment, the chemical formula of the anion of described polyacid is [XM11CoO39]n-, wherein X=P or Si; M=W or Mo; N is valence number, n=5-6.
Embodiment 4:A kind of method of nanoscale intercalated houghite catalyst preparing tributyl citrate, comprises the steps:
Step a, reinforced: addition nanoscale intercalated houghite catalyst, citric acid, excessive butanol toward container in, stir; Time reinforced, the mol ratio of citric acid and butanol is 1:4; The mass ratio of citric acid and nanoscale intercalated houghite catalyst is 1:0.03;
Step b, esterification: oil bath is heated, maintain reaction temperature between 135-140 DEG C; The water that condensing reflux separating reaction generates; The time of esterification is 6h;
Step c, purification: after reaction to be esterified terminates, filter nanoscale intercalated houghite catalyst, is then passed through neutralization, washing, dealcoholysis decolouring, purification step obtain finished lemon/lime acid tributyl;
Nanoscale hydrotalcite catalyst described in the present embodiment is introducing the 3rd metal component Zn in brucite laminate, improves carrier acid-resisting, and it consists of ZnMgAl-LDHs type intercalation catalyst; The chemical formula of the anion of the polyacid wherein adopted in polyacid intercalation in this nanoscale intercalated houghite catalyst is [PW11CoO39]5-
Final products finished product colourity is in 8#-10#(Pt-Co colorimetry), citric acid conversion ratio >=99%, finished product acid number≤0.02%.
Embodiment 5:A kind of method of nanoscale intercalated houghite catalyst preparing tributyl citrate, comprises the steps:
Step a, reinforced: addition nanoscale intercalated houghite catalyst, citric acid, excessive butanol toward container in, stir; Time reinforced, the mol ratio of citric acid and butanol is 1:5; The mass ratio of citric acid and nanoscale intercalated houghite catalyst is 1:0.04;
Step b, esterification: oil bath is heated, maintain reaction temperature between 130-135 DEG C; The water that condensing reflux separating reaction generates; The time of esterification is 8h;
Step c, purification: after reaction to be esterified terminates, filter nanoscale intercalated houghite catalyst, is then passed through neutralization, washing, dealcoholysis decolouring, purification step obtain finished lemon/lime acid tributyl.
The chemical formula of the anion of the polyacid wherein adopted in polyacid intercalation in this nanoscale intercalated houghite catalyst is [SiMo11CoO39]6-;
Final products finished product colourity is in 5#-8#(Pt-Co colorimetry), citric acid conversion ratio >=99%, finished product acid number≤0.03%.
Embodiment 6:A kind of method of nanoscale intercalated houghite catalyst preparing tributyl citrate, comprises the steps:
Step a, reinforced: addition nanoscale intercalated houghite catalyst, citric acid, excessive butanol toward container in, stir; Time reinforced, the mol ratio of citric acid and butanol is 1:6; The mass ratio of citric acid and nanoscale intercalated houghite catalyst is 1:0.05;
Step b, esterification: oil bath is heated, maintain reaction temperature between 135-140 DEG C;The water that condensing reflux separating reaction generates; The time of esterification is 10h;
Step c, purification: after reaction to be esterified terminates, filter nanoscale intercalated houghite catalyst, is then passed through neutralization, washing, dealcoholysis decolouring, purification step obtain finished lemon/lime acid tributyl.
The chemical formula of the anion of the polyacid wherein adopted in polyacid intercalation in this nanoscale intercalated houghite catalyst is [SiW11CoO39]6-;
Final products finished product colourity is in 5#-10#(Pt-Co colorimetry), citric acid conversion ratio >=99%, finished product acid number≤0.02%.
Embodiment 7:A kind of method of nanoscale intercalated houghite catalyst preparing tributyl citrate, comprises the steps:
Step a, reinforced: addition nanoscale intercalated houghite catalyst, citric acid, excessive butanol toward container in, stir; Time reinforced, the mol ratio of citric acid and butanol is 1:6; The mass ratio of citric acid and nanoscale intercalated houghite catalyst is 1:0.04;
Step b, esterification: oil bath is heated, maintain reaction temperature between 135-140 DEG C; The water that condensing reflux separating reaction generates; The time of esterification is 9h;
Step c, purification: after reaction to be esterified terminates, filter nanoscale intercalated houghite catalyst, is then passed through neutralization, washing, dealcoholysis decolouring, purification step obtain finished lemon/lime acid tributyl.
The chemical formula of the anion of the polyacid wherein adopted in polyacid intercalation in this nanoscale intercalated houghite catalyst is [PMo11CoO39]6-;
Final products finished product colourity is in 5#-9#(Pt-Co colorimetry), citric acid conversion ratio >=99%, finished product acid number≤0.01%.
The foregoing is only embodiments of the invention; not thereby the scope of the claims of the present invention is limited; every equivalent structure utilizing description of the present invention to make or equivalence flow process conversion; or directly or indirectly it is used in other relevant technical fields, all in like manner include in the scope of patent protection of the present invention.

Claims (8)

1. the method for a nanoscale intercalated houghite catalyst preparing tributyl citrate, it is characterised in that comprise the steps:
Step a, reinforced: addition nanoscale intercalated houghite catalyst, citric acid, excessive butanol toward container in, stir;
Step b, esterification: oil bath is heated, the water that condensing reflux separating reaction generates; The time of esterification is 6h-10h;
Step c, purification: after reaction to be esterified terminates, filter nanoscale intercalated houghite catalyst, is then passed through neutralization, washing, dealcoholysis, decolouring, purification step obtain finished lemon/lime acid tributyl.
2. the method for nanoscale intercalated houghite catalyst preparing tributyl citrate according to claim 1, it is characterised in that time reinforced in step a, the mol ratio of citric acid and butanol is 1:(4-6).
3. the method for nanoscale intercalated houghite catalyst preparing tributyl citrate according to claim 1, it is characterised in that the mass ratio of described citric acid and nanoscale intercalated houghite catalyst is 1:(0.03 ~ 0.05).
4. the method for nanoscale intercalated houghite catalyst preparing tributyl citrate according to claim 1, it is characterised in that in step b, oil bath is heated, and maintains reaction temperature between 130-140 DEG C.
5. the method for nanoscale intercalated houghite catalyst preparing tributyl citrate according to claim 1, it is characterised in that in step c, esterification terminate rear system be cooled in 75-80 DEG C of backward container add mass fraction be the Na of 5-10%2CO3Solution is neutralized reaction, controls system pH=8 ~ 9;Neutralization reaction performs twice at.
6. the method for nanoscale intercalated houghite catalyst preparing tributyl citrate according to claim 1, it is characterized in that, described nanoscale hydrotalcite catalyst is introducing the 3rd metal component M in brucite laminate, improving carrier acid-resisting, it consists of MMgAl-LDHs type intercalation catalyst.
7. the method for nanoscale intercalated houghite catalyst preparing tributyl citrate according to claim 6, it is characterised in that described nanoscale intercalated houghite catalyst is the one of the magnesium aluminum-hydrotalcite of polyacid intercalation, zinc-aluminum hydrotalcite.
8. the method for nanoscale intercalated houghite catalyst preparing tributyl citrate according to claim 7, it is characterised in that the chemical formula of the anion of described polyacid is [XM11CoO39]n-, wherein X=P or Si; M=W or Mo; N is valence number, n=5-6.
CN201511012936.7A 2015-12-31 2015-12-31 Method of preparing tributyl citrate with nano-scale intercalated hydrotalcite catalyst Pending CN105669443A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201511012936.7A CN105669443A (en) 2015-12-31 2015-12-31 Method of preparing tributyl citrate with nano-scale intercalated hydrotalcite catalyst

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201511012936.7A CN105669443A (en) 2015-12-31 2015-12-31 Method of preparing tributyl citrate with nano-scale intercalated hydrotalcite catalyst

Publications (1)

Publication Number Publication Date
CN105669443A true CN105669443A (en) 2016-06-15

Family

ID=56189698

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201511012936.7A Pending CN105669443A (en) 2015-12-31 2015-12-31 Method of preparing tributyl citrate with nano-scale intercalated hydrotalcite catalyst

Country Status (1)

Country Link
CN (1) CN105669443A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106366009A (en) * 2016-08-26 2017-02-01 安徽金邦医药化工有限公司 Preparation method of chemical intermediate benzocaine

Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1762969A (en) * 2005-09-28 2006-04-26 华东师范大学 Method for preparing tributyl citrate using mesoporous molecular sieve as catalyst
CN101092360A (en) * 2007-07-03 2007-12-26 华东师范大学 Method for catalyzing and synthesizing tri-butyl citrate from methylal naphthalene sulfonic acid
CN101391957A (en) * 2008-11-05 2009-03-25 江南大学 Method for preparing tributyl citrate by using rare-earth salt binary complex type solid acid as catalyst
CN102320970A (en) * 2011-06-10 2012-01-18 四川大学 With the modified cation-exchange resin is the method for Preparation of Catalyst tributyl citrate
CN102584591A (en) * 2011-12-23 2012-07-18 蚌埠丰原医药科技发展有限公司 Method for preparing tributyl citrate through diatomite immobilized titanium sulfate used as catalyst
CN103706403A (en) * 2013-12-23 2014-04-09 北京化工大学 Application of polyacid intercalated hydrotalcite catalyst in preparing glyceryl triacetate
CN104447306A (en) * 2014-10-23 2015-03-25 西安元创化工科技股份有限公司 Method for synthesizing tributyl citrate
CN104437637A (en) * 2014-10-31 2015-03-25 常州大学 Epoxy resin loaded phosphotungstic acid catalyst as well as preparation method and application thereof

Patent Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1762969A (en) * 2005-09-28 2006-04-26 华东师范大学 Method for preparing tributyl citrate using mesoporous molecular sieve as catalyst
CN101092360A (en) * 2007-07-03 2007-12-26 华东师范大学 Method for catalyzing and synthesizing tri-butyl citrate from methylal naphthalene sulfonic acid
CN101391957A (en) * 2008-11-05 2009-03-25 江南大学 Method for preparing tributyl citrate by using rare-earth salt binary complex type solid acid as catalyst
CN102320970A (en) * 2011-06-10 2012-01-18 四川大学 With the modified cation-exchange resin is the method for Preparation of Catalyst tributyl citrate
CN102584591A (en) * 2011-12-23 2012-07-18 蚌埠丰原医药科技发展有限公司 Method for preparing tributyl citrate through diatomite immobilized titanium sulfate used as catalyst
CN103706403A (en) * 2013-12-23 2014-04-09 北京化工大学 Application of polyacid intercalated hydrotalcite catalyst in preparing glyceryl triacetate
CN104447306A (en) * 2014-10-23 2015-03-25 西安元创化工科技股份有限公司 Method for synthesizing tributyl citrate
CN104437637A (en) * 2014-10-31 2015-03-25 常州大学 Epoxy resin loaded phosphotungstic acid catalyst as well as preparation method and application thereof

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106366009A (en) * 2016-08-26 2017-02-01 安徽金邦医药化工有限公司 Preparation method of chemical intermediate benzocaine

Similar Documents

Publication Publication Date Title
CN101580464B (en) Method for producing battery-grade ferrous oxalate by using ferrous sulfate as titanium pigment byproduct
CN101723455B (en) Method for preparing sodium metavanadate
CN104058456B (en) A kind of preparation method of ammonium meta-vanadate
CN102504028A (en) Method for preparing organic cellulose acid ester by solid acid catalysts
CN101549288A (en) Novel Dawson polyacid intercalation hydrotalcite composite material and method of preparing the same
CN101774548A (en) Recycling technology of mother solution obtained by preparing layered composition metal hydroxide by coprecipitation method
CN101722027A (en) Esterification catalyst for synthesizing ethylene/propylene glycol ether carboxylate, and preparation method thereof
CN102408338A (en) Method for synthesizing salicylate
CN102531055B (en) The preparation method of sodium metavanadate/potassium metavanadate
CN101898155A (en) Preparation method and application of sandwich type polyacid intercalated hydrotalcite composite material
CN107814939B (en) Method for synthesizing poly (ethylene glycol methyl phosphonate) by metal oxide catalysis
CN103922930B (en) Method for preparing n-propyl acetate by using multi-acid intercalated hydrotalcite catalyst
CN109772378B (en) Method for preparing high-activity iron-doped bismuth oxyhalide photo-Fenton catalyst, product and application thereof
CN105669443A (en) Method of preparing tributyl citrate with nano-scale intercalated hydrotalcite catalyst
CN1176024C (en) Process for comprehensive utilization of waste acid containing titanium oxide
CN103316696B (en) Preparation method of acetyl tri-n-butyl citrate and catalyst used in preparation method
CN103274491A (en) Method for removing vanadium in water through Mg-Al hydrotalcite
CN109912646A (en) The preparation method of bis- (diphenyl phosphoester) fire retardants of bisphenol-A-
CN110372017B (en) Separation method for preparing basic magnesium carbonate and sodium-potassium salt thereof by bittern mixed alkali method
CN102424913B (en) Method for separating vanadium and chromium from mixing solution containing vanadium (V) and chromium (VI)
CN101920994A (en) Method for preparing vanadyl sulfate
CN103111297A (en) Catalyst for glycerin monostearate synthesis and preparation method and application thereof
CN106186063A (en) A kind of preparation method of nanoscale Zinc vanadate
CN107285292B (en) Method for preparing battery-grade iron phosphate through multi-stage reaction
CN105399630A (en) Method for preparing triethyl citrate through using nanometer intercalated hydrotalcite catalyst

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
RJ01 Rejection of invention patent application after publication
RJ01 Rejection of invention patent application after publication

Application publication date: 20160615