CN1151145C - Double-function catalyst for synthesizing cyclic carbonate and methyl carbonate - Google Patents

Double-function catalyst for synthesizing cyclic carbonate and methyl carbonate Download PDF

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CN1151145C
CN1151145C CNB021447349A CN02144734A CN1151145C CN 1151145 C CN1151145 C CN 1151145C CN B021447349 A CNB021447349 A CN B021447349A CN 02144734 A CN02144734 A CN 02144734A CN 1151145 C CN1151145 C CN 1151145C
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methylcarbonate
och
carbonate
schiff base
synthesizing annular
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CN1416953A (en
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吕小兵
何仁
张英菊
王辉
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Dalian University of Technology
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    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
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Abstract

The present invention provides a double-function catalyst for synthesizing cyclic carbonate and methyl carbonate, and relates to a method for effectively catalyzing carbon dioxide, epoxyalkane and methanol to react and synthesize cyclic carbonate and methyl carbonate. A main catalyst is quadridentate Schiff base aluminum complex (R1) (R2) SalenAlX, wherein R1 and R2 are groups of H, 1-6 carbon alkyl group, alkoxy, Cl, Br, NO2, etc; X is monovalent anions of Cl, Br, I, OR, NO3, CH3COO, ClO4, BF4, BPh4, etc. A cocatalyst is an organic compound with a chemical formula of YR3, wherein Y is an element of the fifth main group, and R is alkyl groups and aryls with 2 to 12 carbon atoms. The molar ratio of the quadridentate Schiff base aluminum complex of the main catalyst to the cocatalyst is 1: 1 to 1: 20. The present invention can catalyze the epoxy compound and the carbon dioxide to react and synthesize the cyclic carbonate in a high efficiency way, and can also effectively catalyze the cyclic carbonate and methanol ester to carry out exchange reaction to synthesize methyl carbonate.

Description

The dual-function catalyst that is used for synthesizing annular carbonate and methylcarbonate
Technical field
The present invention relates to cycloaddition reaction and catalyst for ester exchange reaction, particularly a kind of be used for epoxy alkane by with the dual-function catalyst of carbonic acid gas and methyl alcohol reaction synthesizing annular carbonate and methylcarbonate.
Background technology
Cyclic carbonate is the high polar organic solvent of the high boiling point of excellent property, in field widespread uses such as organic synthesis, makeup, gas delivery, battery dielectric substance and metal extractions.In recent years, many urea production producer as decarburizer, heightens its demand propylene carbonate.In addition, cyclic carbonate is the intermediate of the synthetic green solvent-methylcarbonate of ester-interchange method, and the market requirement is bigger.The synthetic method of cyclic carbonate mainly contains phosgenation, ester-interchange method and epoxy compounds and carbonic acid gas cycloaddition etc.Be a low pollution, eco-friendly technological line by catalysis epoxy alkane and carbon dioxide reaction synthesizing annular carbonate wherein, its research and development are subjected to generally paying attention to.The catalyzer of having reported that is used for epoxy alkane and carbonic acid gas cycloaddition reaction has an alkali metal salt, quaternary ammonium salt Huo quaternary alkylphosphonium salt, KI/ polyoxyethylene glycol, KI/ZnO, MgO, MgO-Al 2O 3The metalphthelein mountain valley with clumps of trees and bamboo and ionic liquid etc. (McMullen, US 4314945; Sachs et al, US 4786741; Harvey et al, US 4841072; Kisch et al, Chem.Ber., 1986,119,1090; Stone is sensible etc., and CN 85100162; Yamaguchi K.et al, J.Am.Chem.Soc., 1999,121,4526; Ji D.F.et al, Appl.Catal.A, 2000,203,329; The Deng You congruence, CN 1343668).Although the catalyst type of report is a lot, mostly catalytic activity is not high, often need be in the presence of high temperature, high pressure and high concentration catalyst catalysis epoxy alkane and carbon dioxide reaction synthesize corresponding cyclic carbonate effectively.
Methylcarbonate is a kind of novel environment-friendly organic chemicals, severe toxicity such as both alternative phosgene, methyl-sulfate and methyl halide or carcinogens are as methylating and carbonylation agent, also alternative methyl tertiary butyl ether is as fuel oil additive, improving oil product octane value and oxygen level, aspects such as reduction pollutant emission demonstrate good performance.Simultaneously, it is the important source material of synthetic other carbonic acid dialkyl ester still, and market demand increases year by year.The main method of Synthesis of dimethyl carbonate has phosgenation, methyl alcohol liquid phase or gas-phase oxidation/carbonylation and ester-interchange method.Wherein, phosgenation is owing to the phosgene that will use severe toxicity, and is superseded substantially now; Methyl alcohol liquid phase or gas-phase oxidation/carbonylation method must strictness be controlled the mol ratio of carbon monoxide and oxygen, otherwise are easy to blast.And the transesterify rule is a kind of method of production methylcarbonate as safe as a house.The patent of this respect is a lot, reports that wherein the catalyzer of cyclic carbonate and methyl alcohol transesterification reaction has KOH, Tl 2CO 3, Bu 3MePI, MgO/Al 2O 3, H 4SiW 12O 40, triphenylphosphine, rare earth oxide, basic metal or alkaline earth metal carbonate, polymkeric substance load trivalent phosphine compound, Zeo-karb and quaternary ammonium functional group resin etc. (DE 4129316, Ger Offen 2740251, JP 8110141, EP 4781073, US 4734518, US5430170, CN 1380140, US 5214182, and JP 80238043, and US 4691041), temperature of reaction is generally between 100-150 ℃, the transformation efficiency of cyclic carbonate is 20-70%, and the productive rate of methylcarbonate is 16-55%, and the selectivity of methylcarbonate all is higher than 93%.
Yet, in cycloaddition reaction catalyzer of being reported and catalyst for ester exchange reaction, seldom have the catalyzer can the catalysis carbonic acid gas and the cycloaddition reaction of epoxy alkane, again the effective transesterification reaction of catalysis cyclic carbonate and methyl alcohol.To be catalyzer with TiOH, NaI reacted 2 hours under 160 ℃, 10MPa condition in propositions such as Josef, by oxyethane, carbonic acid gas and methyl alcohol one-step synthesis methylcarbonate, its productive rate is 20% (Ger Offen 2748718).James etc. are catalyzer with the triphenylphosphine, make propylene oxide, carbonic acid gas and methyl alcohol 130 ℃ of single step reactions 3 hours, 89% propylene oxide is converted into propylene carbonate, 8% methanol conversion is methylcarbonate (WO 8403701), but the consumption of triphenylphosphine is too big, up to 5% of propylene oxide in the system and methyl alcohol total mass.
Summary of the invention
But purpose of the present invention just provide a kind of can be under relative mild conditions both efficient catalytic epoxy compounds and carbon dioxide reaction synthesizing annular carbonate, the effective dual-function catalyst of catalysis cyclic carbonate and methyl alcohol transesterification reaction Synthesis of dimethyl carbonate again.
Technical solution of the present invention is, is used for the dual-function catalyst of synthesizing annular carbonate and methylcarbonate, it is characterized in that, is made up of Primary Catalysts and promotor;
Primary Catalysts is tetradentate schiff base aluminum complex (R 1) (R 2) SalenAlX, its structural formula is:
Wherein, R 1, R 2Be H, 1-6 carbon alkyl, alkoxyl group, Cl, Br, NO 2Deng group; R 3, R 4For-(CH 2) 4-, H, CH 3, Ph ,-(C H) 4-; Axial ligand X is the monovalence negative ion;
Promotor is that chemical formula is YR 3Organic compound, Y is the 5th main group element in the formula;
The mol ratio of Primary Catalysts tetradentate schiff base aluminum complex and promotor is 1: 1 to 1: 20.
Chemical formula is YR 3Promotor, Y is a nitrogen in the formula, R is a 2-12 carbon alkyl.
Chemical formula is YR 3Promotor, Y is a phosphorus in the formula, R is an aryl.
In the Primary Catalysts, be to react the tetradentate schiff base part that obtains by salicylic aldehyde homologue and diamine compounds with the aluminum ion coordination.
Diamine compounds is a quadrol, 1,2-propylene diamine, O-Phenylene Diamine, cyclohexanediamine and 1,2-diphenyl ethylene diamine etc.
In the Primary Catalysts, be to react the tetradentate schiff base part that obtains by salicylic aldehyde homologue and three aminated compoundss with the aluminum ion coordination.
Three aminated compoundss are diethylenetriamines.
The contained substituting group of salicylic aldehyde homologue is the tertiary butyl, methoxyl group, Cl, Br, NO 2Deng group.
The axial ligand X of Primary Catalysts tetradentate schiff base aluminum complex is Cl, Br, I, NO 3, CH 3COO, C1O 4, BF 4, BPh 4Etc. the monovalence negative ion.
The axial ligand X of Primary Catalysts tetradentate schiff base aluminum complex is an alkoxyl group.
Alkoxyl group is OCH 3, OCH 2CH 3, OCH 2CH 2(OCH 2CH 2) 2Cl, OCH 2CH (CH 3) [OCH 2OCH (CH 3)] 2Cl, OCH 2CH 2(OCH 2CH 2) 2OCH 3Deng.
Promotor is tri-n-butylamine, triethylamine, 1-Methylimidazole, triphenylphosphine etc.
The mol ratio of tetradentate schiff base aluminum complex and promotor is 1: 5 to 1: 15.
These tetradentate schiff base aluminum complexes are easy to synthesize, and yield is very high.
In the reaction of carbonic acid gas, epoxy alkane and methyl alcohol synthesizing annular carbonate and methylcarbonate, temperature is 100-150 ℃, is preferably 110-130 ℃; Feed the carbonic acid gas constant voltage and be controlled at 0.1-6MPa, preferably 0.6-2.0MPa; The mol ratio of tetradentate schiff base aluminum complex and epoxy alkane is 1: 100 to 1: 5000, preferably 1: 200 to 1: 1000; The mol ratio of epoxy alkane and methyl alcohol is 1: 1 to 1: 10, preferably 1: 4 to 1: 8; The mol ratio of promotor and tetradentate schiff base metal complexes is 1: 1 to 1: 20, preferably 1: 5 to 1: 15.
The invention has the beneficial effects as follows, but both efficient catalytic epoxy compounds and carbon dioxide reaction synthesizing annular carbonate, effectively catalysis cyclic carbonate and methyl alcohol transesterification reaction Synthesis of dimethyl carbonate again.
Embodiment
The present invention is further illustrated below in conjunction with embodiment,
Embodiment 1
Permitted under carbon-dioxide protecting, to add 1 mole of refining methyl alcohol, 0.25 moles of ethylene oxide, 0.5 * 10 successively in the woods gram bottle one -3Mole SalenAlCl (R 1=R 2=R 3=R 4=H) with 2.5 * 10 -3The mole tri-n-butylamine is stirred to SalenAlCl and dissolves fully.By syringe, be displaced downwardly in the stainless steel autoclave that effective volume is 200ml then at carbon-dioxide protecting.
Temperature is controlled at 120 ℃, in autoclave, adds carbonic acid gas simultaneously so that keep the 1.0MPa constant pressure.After under agitation reacting 2 hours, stop logical carbonic acid gas, autoclave speed is chilled to about 0 ℃, slowly bleed off the carbonic acid gas in the autoclave.
Form by the gas chromatographic analysis liquid mixture products, find to contain 10.1 gram NSC 11801,11.9 gram methylcarbonates and 8.1 gram ethylene glycol, the productive rate of methylcarbonate is 53%, and the transformation efficiency of oxyethane is higher than 98%.
Embodiment 2
With embodiment 1 in the same equipment that uses, under the same conditions, just the reaction times was extended for 3 hours by 2 hours.
Form by the gas chromatographic analysis liquid mixture products, find to contain 8.5 gram NSC 11801,13.5 gram methylcarbonates and 9.1 gram ethylene glycol, the productive rate of methylcarbonate is 60%, and the transformation efficiency of oxyethane is higher than 98%.
Embodiment 3
With embodiment 1 in the same equipment that uses, under the same conditions, just replace oxyethane with propylene oxide.
After 2 hours, obtain 12.7 gram propylene carbonates, 11 gram methylcarbonates and 9.2 grams, 1,2 propylene glycol 120 ℃ of reactions, the productive rate of methylcarbonate is 49%, and the transformation efficiency of propylene oxide is higher than 98%.
Embodiment 4
With embodiment 1 in the same equipment that uses, under the same conditions, just with (t-Bu) SalenAlCl (R 1=t-Bu, R 2=R 3=R 4=H) replace SalenAlCl (R 1=R 2=R 3=R 4=H).
, form by the gas chromatographic analysis liquid mixture products after 2 hours 120 ℃ of reactions, find to contain 9.6 gram NSC 11801,12.4 gram methylcarbonates and 8.4 gram ethylene glycol, the productive rate of methylcarbonate is 55%, and the transformation efficiency of oxyethane is 99%.
Embodiment 5
With embodiment 1 under the same equipment and same catalyst condition that use, just change temperature of reaction into 140 ℃ by 120 ℃.
After 2 hours, obtain 7.2 gram NSC 11801,14.8 gram methylcarbonates, 9.4 gram ethylene glycol and 0.9 gram ethylene glycol monomethyl ether in reaction under this temperature, the productive rate of methylcarbonate is 66%, and the transformation efficiency of oxyethane is 99%.
Embodiment 6
With embodiment 1 in the same equipment that uses, under the same conditions, just replace tri-n-butylamine with triphenylphosphine.
, form by the gas chromatographic analysis liquid mixture products after 2 hours 120 ℃ of reactions, find to contain 11.9 gram NSC 11801,10.1 gram methylcarbonates and 6.9 gram ethylene glycol, the productive rate of methylcarbonate is 45%, and the transformation efficiency of oxyethane is 99%.
Embodiment 7
With embodiment 1 in the same equipment that uses, under the same conditions, just with (t-Bu) 2SalenAlCl (R 1=R 2=t-Bu, R 3=R 4=Ph) replace SalenAlCl (R 1=R 2=R 3=R 4=H).
After 2 hours, obtain 11.4 gram NSC 11801,10.6 gram methylcarbonates and 7.2 gram ethylene glycol 120 ℃ of reactions, the productive rate of methylcarbonate is 47%, and the transformation efficiency of oxyethane is 98%.
Embodiment 8
With embodiment 1 in the same equipment that uses, under the same conditions, just methyl alcohol is increased to 2 molar weights by 1 mole, make that the mol ratio of oxyethane and methyl alcohol became 1: 8 by 1: 4 in the system.
After 2 hours, obtain 8.6 gram NSC 11801,13.5 gram methylcarbonates and 9.2 gram ethylene glycol 120 ℃ of reactions, the productive rate of methylcarbonate is 60%, and the transformation efficiency of oxyethane is 99%.

Claims (13)

1, is used for the dual-function catalyst of synthesizing annular carbonate and methylcarbonate, it is characterized in that, form by Primary Catalysts and promotor;
Primary Catalysts is tetradentate schiff base aluminum complex (R 1) (R 2) SalenAlX, its structural formula is:
Wherein, R 1, R 2Be H, 1-6 carbon alkyl, alkoxyl group, Cl, Br or NO 2Group; R 3, R 4For-(CH 2) 4-, H, CH 3, Ph ,-(CH) 4-; Axial ligand X is the monovalence negative ion;
Promotor is that chemical formula is YR 3Organic compound, Y is nitrogen or phosphorus in the formula; R is a 2-12 carbon alkyl or aryl;
The mol ratio of Primary Catalysts tetradentate schiff base aluminum complex and promotor is 1: 1 to 1: 20.
2, be used for synthesizing annular carbonate and methylcarbonate difunctional according to claim 1 urged agent, it is characterized in that chemical formula is YR 3Promotor, Y is a nitrogen in the formula, R is a 2-12 carbon alkyl.
3, be used for synthesizing annular carbonate and methylcarbonate difunctional according to claim 1 urged agent, it is characterized in that chemical formula is YR 3Promotor, Y is a phosphorus in the formula, R is an aryl.
4, the dual-function catalyst that is used for synthesizing annular carbonate and methylcarbonate according to claim 1 is characterized in that, diamine compounds is a quadrol, 1,2-propylene diamine, O-Phenylene Diamine, cyclohexanediamine or 1,2-diphenyl ethylene diamine.
5, the dual-function catalyst that is used for synthesizing annular carbonate and methylcarbonate according to claim 1 is characterized in that, three aminated compoundss are diethylenetriamines.
6, the dual-function catalyst that is used for synthesizing annular carbonate and methylcarbonate according to claim 1 is characterized in that, the contained substituting group of salicylic aldehyde homologue is the tertiary butyl, methoxyl group, Cl, Br or NO 2Group.
7, the dual-function catalyst that is used for synthesizing annular carbonate and methylcarbonate according to claim 1 is characterized in that, the axial ligand X of Primary Catalysts tetradentate schiff base aluminum complex is Cl, Br, I, NO 3, CH 3COO, ClO 4, BF 4Or BPh 4The monovalence negative ion.
8, the dual-function catalyst that is used for synthesizing annular carbonate and methylcarbonate according to claim 1 is characterized in that, the axial ligand X of Primary Catalysts tetradentate schiff base aluminum complex is an alkoxyl group.
9, according to claim 1 or the 8 described dual-function catalysts that are used for synthesizing annular carbonate and methylcarbonate, it is characterized in that alkoxyl group is OCH 3, OCH 2CH 3, OCH 2CH 2(OCH 2CH 2) 2Cl, OCH 2CH (CH 3) [OCH 2OCH (CH 3)] 2Cl or OCH 2CH 2(OCH 2CH 2) 2OCH 3
According to claim 1, the 2 or 3 described dual-function catalysts that are used for synthesizing annular carbonate and methylcarbonate, it is characterized in that 10, promotor is tri-n-butylamine, triethylamine, 1-Methylimidazole or triphenylphosphine.
11, the dual-function catalyst that is used for synthesizing annular carbonate and methylcarbonate according to claim 1 is characterized in that, the mol ratio of tetradentate schiff base aluminum complex and promotor is 1: 5 to 1: 15.
12, the method for a kind of synthesizing annular carbonate and methylcarbonate, it is characterized in that, claim 1 or 11 described dual-function catalysts have been used, temperature of reaction is 100-150 ℃, feed the carbonic acid gas constant voltage and be controlled at 0.1-6MPa, the mol ratio of tetradentate schiff base aluminum complex and epoxy alkane is 1: 100 to 1: 5000, and the mol ratio of epoxy alkane and methyl alcohol is 1: 1 to 1: 10.
13, the method for a kind of synthesizing annular carbonate according to claim 12 and methylcarbonate, it is characterized in that, temperature of reaction is 110-130 ℃, feed the carbonic acid gas constant voltage and be controlled at 0.6-2.0MPa, the mol ratio of tetradentate schiff base metal complexes and epoxy alkane is 1: 200 to 1: 1000, the mol ratio of tetradentate schiff base aluminum complex and promotor is 1: 5 to 1: 15, and the mol ratio of epoxy alkane and methyl alcohol is 1: 4 to 1: 8.
CNB021447349A 2002-12-06 2002-12-06 Double-function catalyst for synthesizing cyclic carbonate and methyl carbonate Expired - Fee Related CN1151145C (en)

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