CN100537513C - Preparation technology of monomethyl fumarate - Google Patents
Preparation technology of monomethyl fumarate Download PDFInfo
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- CN100537513C CN100537513C CNB2004100515790A CN200410051579A CN100537513C CN 100537513 C CN100537513 C CN 100537513C CN B2004100515790 A CNB2004100515790 A CN B2004100515790A CN 200410051579 A CN200410051579 A CN 200410051579A CN 100537513 C CN100537513 C CN 100537513C
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- monomethyl fumarate
- maleic anhydride
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- NKHAVTQWNUWKEO-UHFFFAOYSA-N fumaric acid monomethyl ester Natural products COC(=O)C=CC(O)=O NKHAVTQWNUWKEO-UHFFFAOYSA-N 0.000 title claims abstract description 49
- 238000002360 preparation method Methods 0.000 title claims abstract description 14
- NKHAVTQWNUWKEO-NSCUHMNNSA-N monomethyl fumarate Chemical compound COC(=O)\C=C\C(O)=O NKHAVTQWNUWKEO-NSCUHMNNSA-N 0.000 title claims description 36
- 229940005650 monomethyl fumarate Drugs 0.000 title claims description 29
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 claims abstract description 33
- FPYJFEHAWHCUMM-UHFFFAOYSA-N maleic anhydride Chemical compound O=C1OC(=O)C=C1 FPYJFEHAWHCUMM-UHFFFAOYSA-N 0.000 claims abstract description 24
- NKHAVTQWNUWKEO-IHWYPQMZSA-N methyl hydrogen fumarate Chemical compound COC(=O)\C=C/C(O)=O NKHAVTQWNUWKEO-IHWYPQMZSA-N 0.000 claims abstract description 13
- 239000003054 catalyst Substances 0.000 claims abstract description 7
- 229910000039 hydrogen halide Inorganic materials 0.000 claims abstract description 6
- 239000012433 hydrogen halide Substances 0.000 claims abstract description 6
- 239000012454 non-polar solvent Substances 0.000 claims abstract description 4
- 238000007142 ring opening reaction Methods 0.000 claims abstract description 4
- 238000006243 chemical reaction Methods 0.000 claims description 17
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 claims description 11
- 229910000041 hydrogen chloride Inorganic materials 0.000 claims description 7
- IXCSERBJSXMMFS-UHFFFAOYSA-N hydrogen chloride Substances Cl.Cl IXCSERBJSXMMFS-UHFFFAOYSA-N 0.000 claims description 7
- 230000017105 transposition Effects 0.000 claims description 6
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 4
- 230000032050 esterification Effects 0.000 claims description 3
- 238000005886 esterification reaction Methods 0.000 claims description 3
- 238000004519 manufacturing process Methods 0.000 abstract description 6
- 238000000034 method Methods 0.000 abstract description 5
- -1 monomethyl fumerate Chemical compound 0.000 abstract description 4
- VZCYOOQTPOCHFL-OWOJBTEDSA-N Fumaric acid Chemical compound OC(=O)\C=C\C(O)=O VZCYOOQTPOCHFL-OWOJBTEDSA-N 0.000 description 17
- VZCYOOQTPOCHFL-UHFFFAOYSA-N trans-butenedioic acid Natural products OC(=O)C=CC(O)=O VZCYOOQTPOCHFL-UHFFFAOYSA-N 0.000 description 11
- 239000002904 solvent Substances 0.000 description 9
- 239000001530 fumaric acid Substances 0.000 description 8
- RTZKZFJDLAIYFH-UHFFFAOYSA-N Diethyl ether Chemical compound CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 description 6
- 230000035484 reaction time Effects 0.000 description 5
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 3
- 239000002253 acid Substances 0.000 description 3
- 239000011203 carbon fibre reinforced carbon Substances 0.000 description 3
- 239000003208 petroleum Substances 0.000 description 3
- 239000000047 product Substances 0.000 description 3
- 239000002994 raw material Substances 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- OFOBLEOULBTSOW-UHFFFAOYSA-N Propanedioic acid Natural products OC(=O)CC(O)=O OFOBLEOULBTSOW-UHFFFAOYSA-N 0.000 description 2
- CREMABGTGYGIQB-UHFFFAOYSA-N carbon carbon Chemical compound C.C CREMABGTGYGIQB-UHFFFAOYSA-N 0.000 description 2
- HNEGQIOMVPPMNR-IHWYPQMZSA-N citraconic acid Chemical compound OC(=O)C(/C)=C\C(O)=O HNEGQIOMVPPMNR-IHWYPQMZSA-N 0.000 description 2
- 239000013078 crystal Substances 0.000 description 2
- 239000006185 dispersion Substances 0.000 description 2
- 235000013305 food Nutrition 0.000 description 2
- 230000000855 fungicidal effect Effects 0.000 description 2
- 239000000417 fungicide Substances 0.000 description 2
- VZCYOOQTPOCHFL-UPHRSURJSA-N maleic acid Chemical compound OC(=O)\C=C/C(O)=O VZCYOOQTPOCHFL-UPHRSURJSA-N 0.000 description 2
- 239000011976 maleic acid Substances 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- UMGDCJDMYOKAJW-UHFFFAOYSA-N thiourea Chemical compound NC(N)=S UMGDCJDMYOKAJW-UHFFFAOYSA-N 0.000 description 2
- KPYCVQASEGGKEG-UHFFFAOYSA-N 3-hydroxyoxolane-2,5-dione Chemical class OC1CC(=O)OC1=O KPYCVQASEGGKEG-UHFFFAOYSA-N 0.000 description 1
- 229930195730 Aflatoxin Natural products 0.000 description 1
- XWIYFDMXXLINPU-UHFFFAOYSA-N Aflatoxin G Chemical compound O=C1OCCC2=C1C(=O)OC1=C2C(OC)=CC2=C1C1C=COC1O2 XWIYFDMXXLINPU-UHFFFAOYSA-N 0.000 description 1
- 241000894006 Bacteria Species 0.000 description 1
- 240000004808 Saccharomyces cerevisiae Species 0.000 description 1
- XSQUKJJJFZCRTK-UHFFFAOYSA-N Urea Natural products NC(N)=O XSQUKJJJFZCRTK-UHFFFAOYSA-N 0.000 description 1
- 239000005409 aflatoxin Substances 0.000 description 1
- 230000000844 anti-bacterial effect Effects 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 125000002915 carbonyl group Chemical group [*:2]C([*:1])=O 0.000 description 1
- 238000006555 catalytic reaction Methods 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 239000002131 composite material Substances 0.000 description 1
- 239000012043 crude product Substances 0.000 description 1
- 238000002425 crystallisation Methods 0.000 description 1
- 230000008025 crystallization Effects 0.000 description 1
- LDCRTTXIJACKKU-ONEGZZNKSA-N dimethyl fumarate Chemical compound COC(=O)\C=C\C(=O)OC LDCRTTXIJACKKU-ONEGZZNKSA-N 0.000 description 1
- 229960004419 dimethyl fumarate Drugs 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000012847 fine chemical Substances 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 230000002401 inhibitory effect Effects 0.000 description 1
- 231100001231 less toxic Toxicity 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 238000006140 methanolysis reaction Methods 0.000 description 1
- 125000002496 methyl group Chemical group [H]C([H])([H])* 0.000 description 1
- 235000013379 molasses Nutrition 0.000 description 1
- AOJFQRQNPXYVLM-UHFFFAOYSA-N pyridin-1-ium;chloride Chemical compound [Cl-].C1=CC=[NH+]C=C1 AOJFQRQNPXYVLM-UHFFFAOYSA-N 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 239000007858 starting material Substances 0.000 description 1
- 230000003335 steric effect Effects 0.000 description 1
- QAOWNCQODCNURD-UHFFFAOYSA-N sulfuric acid Substances OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 1
- 238000010189 synthetic method Methods 0.000 description 1
- 230000009466 transformation Effects 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
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- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
Description
技术领域 technical field
本发明涉及一种作为粮食、食品和饲料的高效广谱防霉杀菌剂反丁烯二酸单甲酯的制备工艺。The invention relates to a preparation process of monomethyl fumarate as a high-efficiency broad-spectrum anti-mold and fungicide for grain, food and feed.
技术背景 technical background
反丁烯二酸单甲酯又叫富马酸单甲酯,英文名称为:mono-methylfurmarate,简称MMF,MMF能广泛而有效地抑制环境中霉菌的滋生,可抑制的细菌及酵母菌达30多种,其中尤其对黄曲霉素有强烈的抑制作用。同时MMF的抗菌性不受pH值的影响,与富马酸二甲酯DMF相比,若要达到同样的防霉效果,则MMF的消耗量只为DMF消耗量的五分之三。另外,MMF的毒性和刺激性远远低于DMF。因此MMF是一种较理想的粮食、食品和饲料的防霉杀菌防蛀剂。Monomethyl fumarate is also called monomethyl fumarate, the English name is: mono-methylfurmarate, MMF for short, MMF can widely and effectively inhibit the growth of mold in the environment, and the bacteria and yeasts that can be inhibited reach 30 A variety of them, especially aflatoxin has a strong inhibitory effect. At the same time, the antibacterial property of MMF is not affected by the pH value. Compared with dimethyl fumarate DMF, if the same anti-mold effect is to be achieved, the consumption of MMF is only three-fifths of the consumption of DMF. In addition, MMF is far less toxic and irritating than DMF. Therefore, MMF is an ideal anti-mildew, fungicide and anti-moth agent for grain, food and feed.
目前,MMF的制备方法有如下两种途径:一是富马酸法,即以富马酸(反丁烯二酸,延胡索酸)为原料,在浓硫酸或BF3催化下与甲醇反应而制得。另一种途径是以顺丁烯二酸酐(又叫失水苹果酸酐,或马来酸酐)为原料,其路线又包括两种,两种路线的步骤分别如下:At present, the preparation method of MMF has the following two ways: one is the fumaric acid method, that is, using fumaric acid (fumaric acid, fumaric acid) as raw material, reacting with methanol under the catalysis of concentrated sulfuric acid or BF3 . Another kind of approach is to be raw material with maleic anhydride (being called dehydrated malic anhydride again, or maleic anhydride), and its route comprises two kinds again, and the steps of two kinds of routes are respectively as follows:
其一,顺丁烯二酸酐→顺丁烯二酸→反丁烯二酸→反丁烯二酸单甲酯(即富马酸单甲酯)。First, maleic anhydride → maleic acid → fumaric acid → monomethyl fumarate (ie monomethyl fumarate).
另一路线是顺丁烯二酸酐→顺丁烯二酸单甲酯→反丁烯二酸单甲酯。Another route is maleic anhydride → monomethyl maleate → monomethyl fumarate.
富马酸在自然界存在不多,它由马来酸水溶液经硫脲催化而制得,或从糖蜜发酵而制得但绝大多数富马酸均由顺丁烯二酸酐转化而来。因此直接由富马酸制备富马酸单甲酯其起始原料仍然是顺丁烯二酸酐。Fumaric acid does not exist much in nature. It is produced from maleic acid aqueous solution catalyzed by thiourea, or fermented from molasses, but the vast majority of fumaric acid is converted from maleic anhydride. Therefore, the starting material for preparing monomethyl fumarate directly from fumaric acid is still maleic anhydride.
在现有的富马酸单甲酯合成方法中,生产周期均较长。如西南大学荣昌校区的钟国清,曾仁权报道[《精细化工》2002.19(6)343-345]以苯作溶剂,盐酸-吡啶做复合催化剂作用下反应时间要3h,收率83%;而重庆香料化工有限责任公司在合成富马酸单甲酯时,第一步,反应要用1.5-5h;第二步反应在无溶剂存在下用盐酸作催化剂,则需20-60h,如用乙酸乙酯作溶剂则需要3-8h,收率约为95%。In the existing synthetic method of monomethyl fumarate, the production cycle is all long. For example, Zhong Guoqing and Zeng Renquan of Southwest University Rongchang Campus reported ["Fine Chemical Industry" 2002.19 (6) 343-345] using benzene as a solvent and hydrochloric acid-pyridine as a composite catalyst. The reaction time will be 3h and the yield will be 83%; When Chemical Co., Ltd. synthesizes monomethyl fumarate, the first step takes 1.5-5 hours to react; the second step uses hydrochloric acid as a catalyst in the presence of no solvent, and it takes 20-60 hours. As a solvent, it takes 3-8 hours, and the yield is about 95%.
发明内容 Contents of the invention
为解决上述问题,本发明的目的是提供一种反丁烯二酸单甲酯的制备工艺,其反应时间短,收率较高,生产效率大大提高。For solving the above problems, the purpose of this invention is to provide a kind of preparation technology of monomethyl fumarate, and its reaction time is short, and yield is higher, and production efficiency improves greatly.
本发明的目的是这样实现的:一种反丁烯二酸单甲酯的制备工艺,其特征在于:首先通过甲醇将顺丁烯二酸酐醇解开环酯化为顺丁烯二酸单甲酯,然后以卤化氢作催化剂,使顺丁烯二酸单甲酯在非极性溶剂中反应,转位生成反丁烯二酸单甲酯。The object of the present invention is achieved like this: a kind of preparation technology of monomethyl fumarate is characterized in that: at first maleic anhydride alcohol is decomposed and esterified into monomethyl maleic acid by methanol, Then use hydrogen halide as a catalyst to react monomethyl maleate in a non-polar solvent to generate monomethyl fumarate.
本发明反丁烯二酸单甲酯的制备工艺简单,生产周期短,只需1-2小时即可完成反应,收率较高,可达85-90%,使生产效率得到大大提高。The preparation process of the monomethyl fumarate of the present invention is simple, the production cycle is short, the reaction can be completed in only 1-2 hours, the yield is high, up to 85-90%, and the production efficiency is greatly improved.
具体实施方式 Detailed ways
本发明是以顺丁烯二酸酐为原料,经甲醇醇解开环酯化为顺丁烯二酸单甲酯,再经转位生成富马酸单甲酯的工艺,其反应式如下:The present invention uses maleic anhydride as a raw material, undergoes methanolysis and ring-opening esterification into monomethyl maleate, and then undergoes transposition to generate monomethyl fumarate. The reaction formula is as follows:
分析顺丁烯二酸酐(I)的结构,分子中有两个羰基基团,所以很容易在甲醇的存在下进行醇解开环而甲酯化,得到顺丁烯二酸单甲酯(II),这步反应很快,而且放热,因此反应中只需加热引发反应就能持续进行。为使顺丁烯二酸酐彻底甲酯化,所以采用顺丁烯二酸酐∶甲醇=1∶1.05-1.1的投料摩尔比。在步骤②中,顺丁烯二酸酐与催化剂的摩尔比为1∶0.25-0.4,反应温度为80-95℃。在顺丁烯二酸单甲酯(II)转位为反丁烯二酸单酯(III)的过程中,由于双键不能自由旋转,因此转位过程的反应历程表现为首先是碳-碳双键的破裂进而形成碳-碳σ-键,只有σ-键才可以旋转,在顺丁烯二酸单甲酯分子中处于同侧的羧酸基团-COOH和羧酸基甲酯团-COOCH3由于存在空间效应,一旦双键破裂,这两个基团马上通过σ-键旋转为异侧,从而完成了由顺丁烯二酸单甲酯转位为反丁烯二酸单酯的过程。在这里,碳-碳双键的破裂是通过双键与卤化氢的加成而不是与卤化氢酸的加成实现的,卤氢酸在一定程度上也能与双键发生反应,但卤氢酸的水会妨碍这一反应,所以用浓盐酸作催化剂时反应时间会很长,因此在本发明中采用通入氯化氢气体作为催化剂。产品反丁烯二酸单甲酯为极性较弱的脂类化合物,当顺丁烯二酸单甲酯转化为反式结构的反丁烯二酸单甲酯时,如用与其结构相似的物质作溶剂,根据相似者相溶原理,产品从溶剂中析出结晶所需时间一定较长,如果用非极性物质作分散溶剂,则产品能很快以结晶形式从溶剂中析出,因此本发明中采用非极性物质,如石油醚,作为转位反应的溶剂,能大大缩短反应时间。Analyzing the structure of maleic anhydride (I), there are two carbonyl groups in the molecule, so it is easy to carry out alcohololysis ring-opening and methyl esterification in the presence of methanol to obtain monomethyl maleate (II), This step reaction is very fast and exothermic, so the reaction only needs to be heated to initiate the reaction and can continue. In order to completely methylate the maleic anhydride, a feed molar ratio of maleic anhydride:methanol=1:1.05-1.1 is used. In step ②, the molar ratio of maleic anhydride to catalyst is 1:0.25-0.4, and the reaction temperature is 80-95°C. In the process of transposition of monomethyl maleate (II) to monomethyl fumarate (III), since the double bond cannot rotate freely, the reaction process of the transposition process is firstly carbon-carbon The double bond breaks and then forms a carbon-carbon σ-bond. Only the σ-bond can be rotated. The carboxylic acid group -COOH and carboxylate methyl ester group on the same side in the monomethyl maleate molecule- Due to the steric effect of COOCH 3 , once the double bond is broken, the two groups immediately rotate to the opposite side through the σ-bond, thus completing the transformation from monomethyl maleate to fumarate monoester process. Here, the breaking of the carbon-carbon double bond is achieved by the addition of the double bond to the hydrogen halide rather than the addition of the hydrogen halide acid, which can also react with the double bond to a certain extent, but the hydrogen halide The water of acid can hinder this reaction, so reaction time can be very long when making catalyzer with concentrated hydrochloric acid, therefore adopts to feed hydrogen chloride gas as catalyzer in the present invention. The product monomethyl fumarate is a lipid compound with weak polarity. When monomethyl maleate is converted into monomethyl fumarate of trans structure, if it is Substance is used as solvent, and according to the principle of mutual solubility of similars, the time required for the crystallization of the product from the solvent must be longer. If a non-polar substance is used as the dispersion solvent, the product can be precipitated from the solvent in the form of crystals very quickly. Therefore, the present invention The use of non-polar substances, such as petroleum ether, as a solvent for the transposition reaction can greatly shorten the reaction time.
以顺丁烯二酸酐∶甲醇=1∶1.05-1.1的投料摩尔比,甲醇将顺丁烯二酸酐醇解开环酯化为顺丁烯二酸单甲酯,反应温度为45-90℃,时间为30-60min,然后以石油醚作为反应分散溶剂,通入HCl,顺丁烯二酸酐与HCl的摩尔比为1∶0.25-0.4,催化顺丁烯二酸单甲酯转位为反丁烯二酸单甲酯,即富马酸单甲酯,反应温度为80-95℃,时间为30-60min。With maleic anhydride:methanol=1:1.05-1.1 feeding molar ratio, methanol decomposes maleic anhydride and esterifies maleic anhydride into monomethyl maleic acid, the reaction temperature is 45-90°C, and the time is 30-60min, then use petroleum ether as the reaction dispersion solvent, pass through HCl, the molar ratio of maleic anhydride and HCl is 1:0.25-0.4, and catalyze the transposition of maleic acid monomethyl ester into fumadiene Acid monomethyl ester, that is, monomethyl fumarate, the reaction temperature is 80-95°C, and the reaction time is 30-60min.
实施例Example
将顺丁烯二酸酐98克(1mol),甲醇35.2克于搅拌下加热至50℃,顺丁烯二酸酐开始溶解。由于本反应为放热反应,因此在反应过程中可停止加热,温度可升至90℃。从50℃开始计时,于30min后加入石油醚100ml,通入HCl,在80-95℃下搅拌反应0.5-1h,控制HCl的流量使顺丁烯二酸酐与通入的HCl摩尔比为1∶0.3,过滤,干燥得反丁烯二酸单甲酯粗品,粗品用乙醇水溶液重结晶,过滤、干燥得白色反丁烯二酸单甲酯结晶,熔点142-144℃,收率为85-90%。98 grams (1 mol) of maleic anhydride and 35.2 grams of methanol were heated to 50° C. under stirring, and the maleic anhydride began to dissolve. Since this reaction is an exothermic reaction, the heating can be stopped during the reaction, and the temperature can rise to 90°C. Start timing at 50°C, add 100ml of petroleum ether after 30min, feed HCl, stir and react at 80-95°C for 0.5-1h, control the flow of HCl so that the molar ratio of maleic anhydride to HCl fed is 1: 0.3, filtered and dried to obtain the crude product of monomethyl fumarate, which was recrystallized with aqueous ethanol solution, filtered and dried to obtain white crystals of monomethyl fumarate with a melting point of 142-144°C and a yield of 85-90 %.
Claims (7)
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| EP2334378B1 (en) | 2008-08-19 | 2014-04-09 | XenoPort, Inc. | Prodrugs of methyl hydrogen fumarate, pharmaceutical compositions thereof, and methods of use |
| CN101880229A (en) * | 2009-05-08 | 2010-11-10 | 广州中医药大学 | (+)-monobornyl maleate and its preparation method and application |
| CN101823962B (en) * | 2010-05-17 | 2012-11-14 | 淮安苏瑞精细化工有限公司 | Method for preparing dimethyl maleate |
| CN101830801B (en) * | 2010-05-17 | 2012-11-14 | 淮安苏瑞精细化工有限公司 | Method for preparing monomethyl cis-butenedioic acid |
| CA2882713A1 (en) | 2012-08-22 | 2014-02-27 | Xenoport, Inc. | Methods of administering monomethyl fumarate and prodrugs thereof having reduced side effects |
| CA2882727A1 (en) | 2012-08-22 | 2014-02-27 | Xenoport, Inc. | Oral dosage forms of methyl hydrogen fumarate and prodrugs thereof |
| CN103044249A (en) * | 2012-12-31 | 2013-04-17 | 广东石油化工学院 | New method for compounding maleic diacid single low-carbon alcohol ester |
| WO2014160633A1 (en) | 2013-03-24 | 2014-10-02 | Xenoport, Inc. | Pharmaceutical compositions of dimethyl fumarate |
| WO2014197860A1 (en) | 2013-06-07 | 2014-12-11 | Xenoport, Inc. | Method of making monomethyl fumarate |
| WO2014205392A1 (en) | 2013-06-21 | 2014-12-24 | Xenoport, Inc. | Cocrystals of dimethyl fumarate |
| US9416096B2 (en) | 2013-09-06 | 2016-08-16 | Xenoport, Inc. | Crystalline forms of (N,N-Diethylcarbamoyl)methyl methyl (2E)but-2-ene-1,4-dioate, methods of synthesis and use |
| US9999672B2 (en) | 2014-03-24 | 2018-06-19 | Xenoport, Inc. | Pharmaceutical compositions of fumaric acid esters |
| CN105906505B (en) * | 2016-06-03 | 2018-06-12 | 陕西能源职业技术学院 | A kind of process for preparing fumaric monoalkylester |
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