CN109810744B - A kind of method for preparing biological lubricating oil catalyzed by acidic polymeric ionic liquid - Google Patents
A kind of method for preparing biological lubricating oil catalyzed by acidic polymeric ionic liquid Download PDFInfo
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- 239000002608 ionic liquid Substances 0.000 title claims abstract description 78
- 230000002378 acidificating effect Effects 0.000 title claims abstract description 60
- 239000010687 lubricating oil Substances 0.000 title claims abstract description 38
- 238000000034 method Methods 0.000 title claims abstract description 18
- 238000006243 chemical reaction Methods 0.000 claims abstract description 65
- 239000004593 Epoxy Substances 0.000 claims abstract description 61
- 239000003054 catalyst Substances 0.000 claims abstract description 52
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims abstract description 29
- 150000004702 methyl esters Chemical class 0.000 claims abstract description 14
- 238000002360 preparation method Methods 0.000 claims abstract description 7
- 235000019387 fatty acid methyl ester Nutrition 0.000 claims description 21
- 239000000047 product Substances 0.000 claims description 19
- 238000006116 polymerization reaction Methods 0.000 claims description 15
- 238000003756 stirring Methods 0.000 claims description 13
- 125000000391 vinyl group Chemical group [H]C([*])=C([H])[H] 0.000 claims description 13
- 229920002554 vinyl polymer Polymers 0.000 claims description 13
- RTZKZFJDLAIYFH-UHFFFAOYSA-N Diethyl ether Chemical compound CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 claims description 10
- 125000003903 2-propenyl group Chemical group [H]C([*])([H])C([H])=C([H])[H] 0.000 claims description 9
- ZMXDDKWLCZADIW-UHFFFAOYSA-N N,N-Dimethylformamide Chemical compound CN(C)C=O ZMXDDKWLCZADIW-UHFFFAOYSA-N 0.000 claims description 9
- OZAIFHULBGXAKX-UHFFFAOYSA-N 2-(2-cyanopropan-2-yldiazenyl)-2-methylpropanenitrile Chemical compound N#CC(C)(C)N=NC(C)(C)C#N OZAIFHULBGXAKX-UHFFFAOYSA-N 0.000 claims description 8
- XEKOWRVHYACXOJ-UHFFFAOYSA-N Ethyl acetate Chemical compound CCOC(C)=O XEKOWRVHYACXOJ-UHFFFAOYSA-N 0.000 claims description 6
- KFZMGEQAYNKOFK-UHFFFAOYSA-N Isopropanol Chemical compound CC(C)O KFZMGEQAYNKOFK-UHFFFAOYSA-N 0.000 claims description 6
- LRHPLDYGYMQRHN-UHFFFAOYSA-N N-Butanol Chemical compound CCCCO LRHPLDYGYMQRHN-UHFFFAOYSA-N 0.000 claims description 6
- ZXEKIIBDNHEJCQ-UHFFFAOYSA-N isobutanol Chemical compound CC(C)CO ZXEKIIBDNHEJCQ-UHFFFAOYSA-N 0.000 claims description 6
- 235000012424 soybean oil Nutrition 0.000 claims description 6
- 239000003549 soybean oil Substances 0.000 claims description 6
- OSSNTDFYBPYIEC-UHFFFAOYSA-N 1-ethenylimidazole Chemical compound C=CN1C=CN=C1 OSSNTDFYBPYIEC-UHFFFAOYSA-N 0.000 claims description 4
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 4
- 239000007795 chemical reaction product Substances 0.000 claims description 4
- XLXCHZCQTCBUOX-UHFFFAOYSA-N 1-prop-2-enylimidazole Chemical compound C=CCN1C=CN=C1 XLXCHZCQTCBUOX-UHFFFAOYSA-N 0.000 claims description 3
- 239000004359 castor oil Substances 0.000 claims description 3
- 235000019438 castor oil Nutrition 0.000 claims description 3
- 238000006555 catalytic reaction Methods 0.000 claims description 3
- ZEMPKEQAKRGZGQ-XOQCFJPHSA-N glycerol triricinoleate Natural products CCCCCC[C@@H](O)CC=CCCCCCCCC(=O)OC[C@@H](COC(=O)CCCCCCCC=CC[C@@H](O)CCCCCC)OC(=O)CCCCCCCC=CC[C@H](O)CCCCCC ZEMPKEQAKRGZGQ-XOQCFJPHSA-N 0.000 claims description 3
- PNDIQUWDKYFMKR-UHFFFAOYSA-N 1-but-1-enylimidazole Chemical compound CCC=CN1C=CN=C1 PNDIQUWDKYFMKR-UHFFFAOYSA-N 0.000 claims description 2
- 235000019484 Rapeseed oil Nutrition 0.000 claims description 2
- 239000003999 initiator Substances 0.000 claims description 2
- 229910052757 nitrogen Inorganic materials 0.000 claims description 2
- MHYFEEDKONKGEB-UHFFFAOYSA-N oxathiane 2,2-dioxide Chemical compound O=S1(=O)CCCCO1 MHYFEEDKONKGEB-UHFFFAOYSA-N 0.000 claims description 2
- BDERNNFJNOPAEC-UHFFFAOYSA-N propan-1-ol Chemical compound CCCO BDERNNFJNOPAEC-UHFFFAOYSA-N 0.000 claims description 2
- ITMCEJHCFYSIIV-UHFFFAOYSA-N triflic acid Chemical compound OS(=O)(=O)C(F)(F)F ITMCEJHCFYSIIV-UHFFFAOYSA-N 0.000 claims description 2
- 229910006069 SO3H Inorganic materials 0.000 claims 2
- DLMHOMJRXAAYSG-UHFFFAOYSA-N butane-1-sulfonate 3-ethenyl-1H-imidazol-3-ium Chemical compound C=C[n+]1cc[nH]c1.CCCCS([O-])(=O)=O DLMHOMJRXAAYSG-UHFFFAOYSA-N 0.000 claims 2
- 239000012295 chemical reaction liquid Substances 0.000 claims 2
- 238000001291 vacuum drying Methods 0.000 claims 2
- 238000005406 washing Methods 0.000 claims 2
- 238000001816 cooling Methods 0.000 claims 1
- 238000010438 heat treatment Methods 0.000 claims 1
- 239000012263 liquid product Substances 0.000 claims 1
- 238000007142 ring opening reaction Methods 0.000 abstract description 18
- 230000015572 biosynthetic process Effects 0.000 abstract description 6
- 238000003786 synthesis reaction Methods 0.000 abstract description 6
- 229920000642 polymer Polymers 0.000 abstract description 5
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical group [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 abstract description 3
- 230000000694 effects Effects 0.000 abstract description 3
- 230000005484 gravity Effects 0.000 abstract description 3
- 239000002994 raw material Substances 0.000 abstract description 3
- 238000004062 sedimentation Methods 0.000 abstract 1
- 239000002253 acid Substances 0.000 description 20
- 239000010410 layer Substances 0.000 description 17
- 239000000178 monomer Substances 0.000 description 6
- 239000003225 biodiesel Substances 0.000 description 5
- 239000007788 liquid Substances 0.000 description 4
- LSNNMFCWUKXFEE-UHFFFAOYSA-M Bisulfite Chemical group OS([O-])=O LSNNMFCWUKXFEE-UHFFFAOYSA-M 0.000 description 3
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 3
- 238000006317 isomerization reaction Methods 0.000 description 3
- 239000000314 lubricant Substances 0.000 description 3
- KBPLFHHGFOOTCA-UHFFFAOYSA-N 1-Octanol Chemical compound CCCCCCCCO KBPLFHHGFOOTCA-UHFFFAOYSA-N 0.000 description 2
- 102000004190 Enzymes Human genes 0.000 description 2
- 108090000790 Enzymes Proteins 0.000 description 2
- 238000007259 addition reaction Methods 0.000 description 2
- 150000001298 alcohols Chemical class 0.000 description 2
- 125000003342 alkenyl group Chemical group 0.000 description 2
- 230000003197 catalytic effect Effects 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 238000006735 epoxidation reaction Methods 0.000 description 2
- 239000003921 oil Substances 0.000 description 2
- 235000019198 oils Nutrition 0.000 description 2
- 239000000376 reactant Substances 0.000 description 2
- 230000035484 reaction time Effects 0.000 description 2
- 238000004064 recycling Methods 0.000 description 2
- 238000011160 research Methods 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 235000015112 vegetable and seed oil Nutrition 0.000 description 2
- 239000008158 vegetable oil Substances 0.000 description 2
- 125000004975 3-butenyl group Chemical group C(CC=C)* 0.000 description 1
- AMQJEAYHLZJPGS-UHFFFAOYSA-N N-Pentanol Chemical compound CCCCCO AMQJEAYHLZJPGS-UHFFFAOYSA-N 0.000 description 1
- 239000011831 acidic ionic liquid Substances 0.000 description 1
- 150000001335 aliphatic alkanes Chemical class 0.000 description 1
- 125000000217 alkyl group Chemical group 0.000 description 1
- -1 allyl imidazolium Chemical compound 0.000 description 1
- 239000002199 base oil Substances 0.000 description 1
- 238000007385 chemical modification Methods 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 238000004821 distillation Methods 0.000 description 1
- 125000003700 epoxy group Chemical group 0.000 description 1
- 150000002148 esters Chemical class 0.000 description 1
- 238000006266 etherification reaction Methods 0.000 description 1
- 238000004880 explosion Methods 0.000 description 1
- 239000010794 food waste Substances 0.000 description 1
- 230000007062 hydrolysis Effects 0.000 description 1
- 238000006460 hydrolysis reaction Methods 0.000 description 1
- 238000009776 industrial production Methods 0.000 description 1
- 239000011229 interlayer Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000010907 mechanical stirring Methods 0.000 description 1
- 229910044991 metal oxide Inorganic materials 0.000 description 1
- 150000004706 metal oxides Chemical class 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000002105 nanoparticle Substances 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000003444 phase transfer catalyst Substances 0.000 description 1
- 229920002006 poly(N-vinylimidazole) polymer Polymers 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 238000010992 reflux Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 238000005809 transesterification reaction Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
Classifications
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- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/50—Improvements relating to the production of bulk chemicals
- Y02P20/584—Recycling of catalysts
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- Lubricants (AREA)
Abstract
本申请公开了一种酸性聚合离子液体催化制备生物润滑油的方法,属于生物润滑油制备领域。本发明将酸性聚合离子液体作为反应的催化剂,催化环氧甲酯与短链醇在60‑80℃下反应10‑20小时,得反应液,将反应液冷却至室温,重力沉降,产物与酸性聚合离子液体分层,本发明将碳链长度不同的离子液体聚合物用于催化环氧甲酯开环制备生物润滑油。反应原料广泛,反应条件相对温和,操作简便,并且酸性可循环使用且催化剂活性高;合成方便。The application discloses a method for preparing biological lubricating oil catalyzed by an acidic polymeric ionic liquid, and belongs to the field of biological lubricating oil preparation. In the present invention, the acidic polymeric ionic liquid is used as a catalyst for the reaction, and the reaction of the epoxy methyl ester and the short-chain alcohol is catalyzed at 60-80° C. for 10-20 hours to obtain a reaction solution, which is cooled to room temperature, and subjected to gravity sedimentation. The polymerized ionic liquid is layered, and the present invention uses ionic liquid polymers with different carbon chain lengths to catalyze the ring-opening of epoxy methyl esters to prepare biological lubricating oils. The reaction raw materials are extensive, the reaction conditions are relatively mild, the operation is simple, the acidity can be recycled and the catalyst activity is high, and the synthesis is convenient.
Description
技术领域technical field
本发明涉及一种酸性聚合离子液体催化环氧开环异构化反应的方法,具体的涉及一种酸性聚合离子液体催化制备生物润滑油的方法。The invention relates to a method for catalyzing an epoxy ring-opening isomerization reaction by an acidic polymeric ionic liquid, in particular to a method for preparing a biological lubricating oil catalyzed by an acidic polymeric ionic liquid.
背景技术Background technique
生物柴油主要由脂肪酸甲酯的混合物(FAMEs)组成,通过环氧化反应脂肪酸甲酯的分子结构中就会具有化学性质不稳定的环氧键,由于环氧基团具有较强的张力,环氧键可以与多种物质发生反应,如在酸性条件下会发生水解反应、与金属氧化物会发生聚合引起爆炸,因此需要对环氧生物柴油进行化学改性。对环氧键开环进行加成反应是生物柴油制取生物润滑油的一条合理的路线。采用对生物柴油进行化学改性的方式合成润滑油基础油,可以提高生物柴油的附加值,提高其市场竞争力。目前研究最多的就是用有机醇类物质与环氧基团接合。Biodiesel is mainly composed of mixtures of fatty acid methyl esters (FAMEs). Through epoxidation, the molecular structure of fatty acid methyl esters will have chemically unstable epoxy bonds. Oxygen bonds can react with a variety of substances, such as hydrolysis under acidic conditions, and polymerization with metal oxides to cause explosions. Therefore, it is necessary to chemically modify epoxy biodiesel. The addition reaction of ring-opening epoxy bond is a reasonable route for biodiesel to prepare biolubricating oil. Synthesis of lubricating oil base oil by chemical modification of biodiesel can increase the added value of biodiesel and improve its market competitiveness. At present, the most research is to use organic alcohols to combine with epoxy groups.
环氧脂肪酸甲酯开环生成生物润滑油的反应中,催化剂有着很重要的作用,对环氧脂肪酸甲酯的转化率,生物润滑油的收率都有影响。此外,催化剂的回收问题在工业化生产中也是必须要考虑的问题随意丢弃催化剂会对生态环境造成极大的破坏。就目前催化剂发展的形式来说,绿色催化剂逐渐受到人们的关注,这些绿色催化剂包括:纳米粒子催化剂,离子液体催化剂,夹层催化剂,酶或仿酶催化剂,相转移催化剂等。其中离子液体催化剂因具有易化学稳定性和热稳定性好等优点,越来越受到研究者的重视,但是离子液体不易回收,分离困难阻碍了它的广泛应用。研究将离子液体聚合既能保持它的高催化活性又方便回收是未来催化剂研究中的重点方向。In the reaction of epoxy fatty acid methyl ester ring-opening to generate biological lubricating oil, the catalyst plays an important role, which affects the conversion rate of epoxy fatty acid methyl ester and the yield of biological lubricating oil. In addition, the recycling of catalysts is also a problem that must be considered in industrial production. Randomly discarding catalysts will cause great damage to the ecological environment. As far as the current form of catalyst development is concerned, green catalysts have gradually attracted people's attention. These green catalysts include: nanoparticle catalysts, ionic liquid catalysts, interlayer catalysts, enzyme or imitated enzyme catalysts, phase transfer catalysts, etc. Among them, ionic liquid catalysts have been paid more and more attention by researchers due to their advantages of easy chemical stability and good thermal stability. It is the key direction of future catalyst research to study the polymerization of ionic liquid to maintain its high catalytic activity and facilitate recycling.
发明内容SUMMARY OF THE INVENTION
本发明要解决的技术问题是是提供一种酸性聚合离子液体催化制备生物润滑油的方法,以克服公知技术中存在的缺陷。The technical problem to be solved by the present invention is to provide a method for catalyzing the preparation of biological lubricating oil by an acidic polymeric ionic liquid, so as to overcome the defects existing in the known technology.
为实现上述目的,本发明提供的酸性聚合离子液体催化制备生物润滑油的方法,其步骤为:In order to achieve the above object, the method for preparing biological lubricating oil catalyzed by the acidic polymeric ionic liquid provided by the invention, the steps are:
A)将酸性聚合离子液体作为反应的催化剂,催化环氧甲酯与有机醇在60-80℃下反应10-20小时;A) The acidic polymeric ionic liquid is used as a catalyst for the reaction to catalyze the reaction of epoxy methyl ester and organic alcohol at 60-80° C. for 10-20 hours;
酸性聚合离子液体的聚合单体可以选择乙烯基,烯丙基或烯丁基咪唑离子液体中的一种。The polymerized monomer of the acidic polymerized ionic liquid can be selected from vinyl, allyl or allyl imidazolium ionic liquid.
酸性离子液体单体的结构式为The structural formula of the acidic ionic liquid monomer is
其中,R为-CH=CH2、-CH2-CH=CH2或-CH2-CH2-CH=CH2 Wherein, R is -CH=CH 2 , -CH 2 -CH=CH 2 or -CH 2 -CH 2 -CH=CH 2
所述的反应物为环氧甲酯和有机醇,其中环氧甲酯与有机醇摩尔比为1:1至1:6;Described reactant is epoxy methyl ester and organic alcohol, and wherein epoxy methyl ester and organic alcohol mol ratio are 1:1 to 1:6;
所述酸性聚合离子液体质量与环氧甲酯的质量比为1:4至1:60。The mass ratio of the acidic polymeric ionic liquid to the epoxy methyl ester is 1:4 to 1:60.
B)将步骤A制得的反应液冷却至室温,重力沉降,产物与酸性聚合离子液体作分层,并将上层液体减压脱除未反应有机醇,得到产物。B) The reaction solution obtained in step A is cooled to room temperature, and gravity settled, the product is layered with the acidic polymeric ionic liquid, and the upper layer liquid is decompressed to remove unreacted organic alcohol to obtain the product.
其中,步骤B中分离出的酸性聚合离子液体重复用于反应。Wherein, the acidic polymeric ionic liquid separated in step B is repeatedly used for the reaction.
其中,步骤A中原料为植物油酯交换环氧化制得环氧甲酯的;醇类为甲醇、乙醇、丙醇、异丙醇、正丁醇、异丁醇、戊醇、辛醇中的一种或几种。Wherein, in step A, the raw material is obtained by transesterification and epoxidation of vegetable oil to obtain epoxy methyl ester; the alcohols are methanol, ethanol, propanol, isopropanol, n-butanol, isobutanol, amyl alcohol, and octanol. one or more.
与背景技术相比,本发明取得的技术进步是:Compared with the background technology, the technical progress achieved by the present invention is:
本发明创新性的提出将碳链长度不同的B酸离子液体聚合物用于催化环氧甲酯开环制备生物润滑油。该类型离子液体由可调碳链长度酸性基团聚合而成,而聚合度可控,可调,在反应器中高效实现多相体系中的催化反应;因此,可利用其酸性和表面活性促进开环反应连续进行。本发明的催化剂能作为生物润滑油合成的催化剂,进行环氧开环异构醚化反应过程,酸性离子液体聚合物在生物润滑油生产领域具有极大的应用潜力,为促进可降解润滑油在国内推广奠定基础。其具体优点如下:The invention innovatively proposes to use B acid ionic liquid polymers with different carbon chain lengths to catalyze the ring-opening of epoxy methyl esters to prepare biological lubricants. This type of ionic liquid is polymerized by acid groups with adjustable carbon chain length, and the degree of polymerization is controllable and adjustable, and the catalytic reaction in the heterogeneous system can be efficiently realized in the reactor; therefore, its acidity and surface activity can be used to promote The ring-opening reaction proceeds continuously. The catalyst of the invention can be used as a catalyst for the synthesis of biological lubricating oil to carry out the epoxy ring-opening isomerization etherification reaction process. The acid ionic liquid polymer has great application potential in the field of biological lubricating oil production. Lay the foundation for domestic promotion. Its specific advantages are as follows:
1、反应原料广泛,为植物油脂、废弃餐饮废油等衍生产物环氧脂肪酸甲酯。1. Wide range of reaction raw materials, such as vegetable oil, waste food waste oil and other derivative products of epoxy fatty acid methyl ester.
2、反应条件相对温和,操作简便。2. The reaction conditions are relatively mild and the operation is simple.
3、反应产物相与催化剂相不互溶而自动分层,且易分离。3. The reaction product phase and the catalyst phase are immiscible and automatically stratified, and are easy to separate.
4、催化剂为酸性聚合离子液体,结构可控可调、性能稳定、酸性无流失、可循环使用且催化剂活性高;合成方便,原子经济好。4. The catalyst is an acidic polymeric ionic liquid with controllable and adjustable structure, stable performance, no acid loss, recyclable use and high catalyst activity; convenient synthesis and good atomic economy.
5、克服背景技术中存在的普通催化剂液体分离较难,催化活性弱的问题。5. Overcoming the problems of difficult liquid separation and weak catalytic activity of common catalysts in the background art.
6、制备工艺无废水排放,多余反应物可多次回收利用,属环境友好工艺路线。6. There is no waste water discharge in the preparation process, and excess reactants can be recycled for multiple times, which is an environmentally friendly process route.
具体实施方式Detailed ways
本发明提供的酸性聚合离子液体催化制备生物润滑油的方法,是将酸性聚合离子液体用于催化环氧甲酯开环异构化反应,为生物润滑油的制备提供了一条环境友好的工艺路线。The method for preparing biological lubricating oil catalyzed by the acidic polymeric ionic liquid provided by the invention is that the acidic polymeric ionic liquid is used to catalyze the ring-opening isomerization reaction of epoxy methyl ester, and an environment-friendly process route is provided for the preparation of biological lubricating oil. .
本发明使用的酸性聚合离子液体,是磺酸基功能化烷基聚乙烯咪唑磺酸,其合成过程如下所示,其中,聚合单体可以选择乙烯基,烯丙基,烯丁基咪唑离子液体。聚合度可控可调。The acidic polymeric ionic liquid used in the present invention is a sulfonic acid group-functionalized alkyl polyvinylimidazole sulfonic acid, and its synthesis process is as follows, wherein the polymerization monomers can be selected from vinyl, allyl, and allyl imidazole ionic liquids . The degree of polymerization is controllable and adjustable.
酸性聚合乙烯基离子液体催化剂其具体合成步骤为:The specific synthesis steps of the acid polymerization vinyl ionic liquid catalyst are:
本发明使用的酸性聚合乙烯基离子液体可以通过以下方法制得:The acidic polymerized vinyl ionic liquid used in the present invention can be prepared by the following methods:
在0℃下,向烧瓶中缓慢加入1-乙烯基咪唑、丁烷磺内酯于室温下搅拌24h,最后用乙醚洗涤产物,并真空干燥(25℃,6h),得1-乙烯基咪唑丁烷磺酸。在0℃下,向圆底烧瓶中缓慢加入等摩尔的三氟甲烷磺酸和1-乙烯基咪唑丁烷磺酸,于60℃下反应12h,得[VIm(CH2)4SO3H][CF3SO3]。反应产物用乙醚洗涤,并真空干燥(50℃,2h)。取一定量的[VIm(CH2)4SO3H][CF3SO3]加入到N,N一二甲基甲酰胺(DMF),通过搅拌使其完全溶解后,加入一定量的引发剂偶氮二异丁腈(AIBN),在氮气保护下升温至60℃,并持续搅拌反应24h。反应结束后,向反应液中加入乙酸乙酯,促使产物析出,得酸性聚合乙烯基离子液体催化剂。At 0 °C, slowly add 1-vinylimidazole and butane sultone to the flask, stir at room temperature for 24 h, and finally wash the product with diethyl ether, and vacuum dry (25 °C, 6 h) to obtain 1-vinylimidazobutine Alkane sulfonic acid. At 0 °C, slowly add equimolar trifluoromethanesulfonic acid and 1-vinylimidazobutanesulfonic acid to the round-bottomed flask, and react at 60 °C for 12 h to obtain [VIm(CH 2 ) 4 SO 3 H] [CF 3 SO 3 ]. The reaction product was washed with ether and dried in vacuo (50°C, 2h). A certain amount of [VIm(CH 2 ) 4 SO 3 H][CF 3 SO 3 ] was added to N,N-dimethylformamide (DMF), and after it was completely dissolved by stirring, a certain amount of initiator was added Azobisisobutyronitrile (AIBN) was heated to 60°C under nitrogen protection, and the reaction was continuously stirred for 24h. After the reaction is completed, ethyl acetate is added to the reaction solution to promote the precipitation of the product to obtain an acidic polymerization vinyl ionic liquid catalyst.
酸性聚合烯丙基离子液体或酸性聚合烯丁基离子液体催化剂的制备方法和条件与上述相同,区别在于,将其中1-乙烯基咪唑换成1-烯丙基咪唑或1-丁烯基咪唑基团,反应后分别得到酸性聚合烯丙基离子液体或酸性聚合烯丁基离子液体催化剂。The preparation method and conditions of the acid polymerized allyl ionic liquid or the acid polymerized allyl ionic liquid catalyst are the same as above, except that 1-vinylimidazole is replaced with 1-allylimidazole or 1-butenylimidazole After the reaction, an acidic polymeric allyl ionic liquid or an acidic polymeric allyl ionic liquid catalyst is obtained, respectively.
所述酸性聚合烯丙基离子液体催化剂的结构式如下所示:The structural formula of the acidic polymeric allyl ionic liquid catalyst is as follows:
酸性聚合烯丁基离子液体催化剂的结构式如下所示:The structural formula of the acidic polymerized alkenyl ionic liquid catalyst is as follows:
本发明是将制得催化剂催化环氧脂肪酸甲酯与有机醇开环反应后,重力沉降,产物和催化剂分层,反应产物液体减压蒸除易挥发物,制得生物润滑油,而酸性聚合离子液体催化剂回收后可重复使用。In the present invention, after the prepared catalyst catalyzes the ring-opening reaction of epoxy fatty acid methyl ester and organic alcohol, gravity settles, the product and the catalyst are layered, and the reaction product liquid is decompressed to remove volatile matter, so as to prepare biological lubricating oil, and acid polymerization The ionic liquid catalyst can be reused after recovery.
采用上述制备的催化剂催化环氧脂肪酸甲酯中环氧键开环进行加成反应合成生物润滑油步骤为:Adopt the above-mentioned catalyst to catalyze the epoxy bond ring-opening in the epoxy fatty acid methyl ester to carry out the addition reaction to synthesize the biological lubricating oil step as follows:
生物润滑油的制备:在配有磁力搅拌器或机械搅拌、回流冷凝管和温度计的三口瓶内,加入一定配比的环氧甲酯、有机醇、上述酸性聚合离子液体催化剂,其中环氧甲酯与有机醇的摩尔比为1:1至1:6,酸性聚合离子液体质量与环氧甲酯的质量比为1:4至1:60。升温至反应温度开始反应计时,至预定反应时间后,停止反应,反应液冷却静置后产物与酸性聚合离子液体分层,下层分离出的聚合物离子液体简单处理后可重复使用,将上层反应产物液体蒸馏脱除有机醇得到生物润滑油产品。Preparation of biological lubricating oil: In a three-necked flask equipped with a magnetic stirrer or mechanical stirring, a reflux condenser and a thermometer, add a certain proportion of epoxy methyl ester, organic alcohol, and the above-mentioned acidic polymerized ionic liquid catalyst, among which epoxy methyl ester The molar ratio of ester to organic alcohol is 1:1 to 1:6, and the mass ratio of acidic polymeric ionic liquid to epoxy methyl ester is 1:4 to 1:60. The temperature is raised to the reaction temperature to start the reaction timing. After the predetermined reaction time, the reaction is stopped. After the reaction solution is cooled and allowed to stand, the product is layered with the acidic polymer ionic liquid. The polymer ionic liquid separated from the lower layer can be reused after simple treatment. The upper layer is reacted The organic alcohol is removed by distillation of the product liquid to obtain a biological lubricating oil product.
制备生物润滑油的机理为:The mechanism of preparing bio-lubricating oil is as follows:
下面结合实施例对本发明的方法做进一步说明,并不是本发明的限定。The method of the present invention will be further described below in conjunction with the examples, which are not limitations of the present invention.
实施例1:Example 1:
称取68g乙醇和4g酸性乙烯基离子液体单体催化剂放于带有冷凝管和温度计的四口烧瓶中,在搅拌状态下加热至80℃,然后加入200g环氧大豆油脂肪酸甲酯,测得反应体系初始的环氧值为5.46,并在该温度下进行开环反应。反应过程中每隔30min中取样,测定其环氧值,反应时间t=12h,停止反应。上述溶液冷却至室温,静置沉降,离心分离酸性乙烯基离子液体单体,发现离子液体单体催化剂使用很难分离,很难回收循环利,将反应溶液减压蒸馏,最终得到澄清透明的乙醇改性生物润滑油。生物润滑油的环氧值为1.076,转化率为80.3%,酸值为1.73(mgKOH/g),40℃运动粘度为38.49(mm2/s)。Weigh 68g of ethanol and 4g of acid vinyl ionic liquid monomer catalyst and place it in a four-necked flask with a condenser tube and a thermometer, heat to 80°C under stirring, then add 200g of epoxidized soybean oil fatty acid methyl ester, and measure The initial epoxy value of the reaction system was 5.46, and the ring-opening reaction was carried out at this temperature. During the reaction, samples were taken every 30 minutes to measure the epoxy value. The reaction time was t=12h, and the reaction was stopped. The above solution was cooled to room temperature, allowed to settle, and centrifuged to separate the acid vinyl ionic liquid monomer. It was found that the ionic liquid monomer catalyst was difficult to separate, and it was difficult to recover and recycle. The reaction solution was decompressed and distilled to finally obtain clear and transparent ethanol. Modified biological lubricants. The epoxy value of the bio-lubricating oil was 1.076, the conversion rate was 80.3%, the acid value was 1.73 (mgKOH/g), and the kinematic viscosity at 40°C was 38.49 (mm 2 /s).
实施例2:Example 2:
称取68g乙醇和4g酸性聚合乙烯基离子液体催化剂放于带有冷凝管和温度计的四口烧瓶中,在搅拌状态下加热至80℃,然后加入200g环氧大豆油脂肪酸甲酯,测得反应体系初始的环氧值为5.46,并在该温度下进行开环反应。反应过程中每隔30min中取样,测定其环氧值,当环氧值小于0.08时(t=10h),停止反应。上述溶液冷却至室温,静置沉降,产物与酸性聚合离子液体分层,下层离心分离得酸性聚合离子液体催化剂,将上层反应溶液减压蒸馏,最终得到澄清透明的乙醇改性生物润滑油。生物润滑油的环氧值为0.172,转化率为96.8%,酸值为0.95(mgKOH/g),40℃运动粘度为38.51(mm2/s)。Weigh 68g of ethanol and 4g of acidic polymerization vinyl ionic liquid catalyst and place it in a four-necked flask with a condenser tube and a thermometer, heat to 80°C under stirring, then add 200g of epoxidized soybean oil fatty acid methyl ester, and measure the reaction The initial epoxy value of the system was 5.46, and the ring-opening reaction was carried out at this temperature. During the reaction, samples were taken every 30 minutes to measure the epoxy value. When the epoxy value was less than 0.08 (t=10h), the reaction was stopped. The above solution is cooled to room temperature, allowed to settle, the product is layered with the acidic polymeric ionic liquid, the lower layer is centrifuged to obtain an acidic polymeric ionic liquid catalyst, and the upper layer reaction solution is decompressed and distilled to finally obtain a clear and transparent ethanol-modified biological lubricating oil. The epoxy value of the bio-lubricating oil was 0.172, the conversion rate was 96.8%, the acid value was 0.95 (mgKOH/g), and the kinematic viscosity at 40°C was 38.51 (mm 2 /s).
实施例3:Example 3:
称取68g乙醇和4g酸性聚合乙烯基离子液体催化剂放于带有冷凝管和温度计的四口烧瓶中,在搅拌状态下加热至80℃,然后加入200g环氧大豆油脂肪酸甲酯,测得反应体系初始的环氧值为5.46,并在该温度下进行开环反应。反应过程中每隔30min中取样,测定其环氧值,当环氧值小于0.08时(t=12h),停止反应。上述溶液冷却至室温,静置沉降,产物与酸性聚合离子液体分层,下层离心分离后得酸性聚合离子液体催化剂,将上层反应溶液减压蒸馏,最终得到澄清透明的乙醇改性生物润滑油。生物润滑油的环氧值为0.069,转化率为98.7%,酸值为0.78(mgKOH/g),40℃运动粘度为38.53(mm2/s)。Weigh 68g of ethanol and 4g of acidic polymerization vinyl ionic liquid catalyst and place it in a four-necked flask with a condenser tube and a thermometer, heat to 80°C under stirring, then add 200g of epoxidized soybean oil fatty acid methyl ester, and measure the reaction The initial epoxy value of the system was 5.46, and the ring-opening reaction was carried out at this temperature. During the reaction, samples were taken every 30 minutes to measure the epoxy value. When the epoxy value was less than 0.08 (t=12h), the reaction was stopped. The above solution is cooled to room temperature, allowed to settle, the product is layered with the acidic polymeric ionic liquid, the lower layer is centrifuged to obtain an acidic polymeric ionic liquid catalyst, and the upper layer reaction solution is decompressed and distilled to finally obtain a clear and transparent ethanol-modified biological lubricating oil. The epoxy value of the bio-lubricating oil was 0.069, the conversion rate was 98.7%, the acid value was 0.78 (mgKOH/g), and the kinematic viscosity at 40°C was 38.53 (mm 2 /s).
实施例4:Example 4:
称取84.4g异丙醇和4g酸性聚合乙烯基离子液体催化剂放于带有冷凝管和温度计的四口烧瓶中,在搅拌状态下加热至70℃,然后加入200g环氧菜籽油脂肪酸甲酯,测得反应体系初始的环氧值为5.46,并在该温度下进行开环反应。反应过程中每隔30min中取样,测定其环氧值,当环氧值小于0.08时(t=14h),停止反应。上述溶液冷却至室温,静置沉降,产物与酸性聚合离子液体分层,下层,离心分离后得酸性聚合离子液体催化剂,将上层反应溶液减压蒸馏,最终得到澄清透明的异丙醇改性生物润滑油。生物润滑油的环氧值为0.068,转化率为98.8%,酸值为0.79(mgKOH/g),40℃运动粘度为37.54(mm2/s)。Weigh 84.4g of isopropanol and 4g of acid polymerization vinyl ionic liquid catalyst and place in a four-necked flask with a condenser tube and a thermometer, heat to 70°C under stirring, then add 200g of epoxy rapeseed oil fatty acid methyl ester, The initial epoxy value of the reaction system was measured to be 5.46, and the ring-opening reaction was carried out at this temperature. During the reaction, samples were taken every 30 minutes to measure the epoxy value. When the epoxy value was less than 0.08 (t=14h), the reaction was stopped. The above solution is cooled to room temperature, allowed to settle, the product is layered with the acidic polymeric ionic liquid, the lower layer is centrifuged to obtain an acidic polymeric ionic liquid catalyst, and the upper layer reaction solution is decompressed and distilled to finally obtain a clear and transparent isopropanol-modified organism. lubricating oil. The epoxy value of the bio-lubricating oil was 0.068, the conversion rate was 98.8%, the acid value was 0.79 (mgKOH/g), and the kinematic viscosity at 40°C was 37.54 (mm 2 /s).
实施例5:Example 5:
称取114.4g正丁醇和4g酸性聚合乙烯基离子液体催化剂放于带有冷凝管和温度计的四口烧瓶中,在搅拌状态下加热至70℃,然后加入200g环氧蓖麻油脂肪酸甲酯,测得反应体系初始的环氧值为5.46,并在该温度下进行开环反应。反应过程中每隔30min中取样,测定其环氧值,当环氧值小于0.08时(t=10h),停止反应。上述溶液冷却至室温,上述溶液冷却至室温,上述溶液冷却至室温,静置沉降,产物与酸性聚合离子液体分层,下层离心分离后得酸性聚合离子液体催化剂,将上层反应溶液减压蒸馏,最终得到澄清透明的正丁醇改性生物润滑油。生物润滑油的环氧值为0.075,转化率为98.6%,酸值为0.72(mgKOH/g),40℃运动粘度为34.48(mm2/s)。Weigh 114.4g of n-butanol and 4g of acidic polymerization vinyl ionic liquid catalyst and place them in a four-necked flask with a condenser tube and a thermometer, heat to 70°C under stirring, then add 200g of epoxy castor oil fatty acid methyl ester, measure The initial epoxy value of the reaction system was 5.46, and the ring-opening reaction was carried out at this temperature. During the reaction, samples were taken every 30 minutes to measure the epoxy value. When the epoxy value was less than 0.08 (t=10h), the reaction was stopped. The above solution is cooled to room temperature, the above solution is cooled to room temperature, the above solution is cooled to room temperature, allowed to settle, the product is layered with the acidic polymeric ionic liquid, the lower layer is centrifuged to obtain an acidic polymeric ionic liquid catalyst, and the upper layer reaction solution is distilled under reduced pressure, Finally, a clear and transparent n-butanol-modified biological lubricant was obtained. The epoxy value of the bio-lubricating oil was 0.075, the conversion rate was 98.6%, the acid value was 0.72 (mgKOH/g), and the kinematic viscosity at 40°C was 34.48 (mm 2 /s).
实施例6:Example 6:
称取114.4g异丁醇和4g酸性聚合乙烯基离子液体催化剂放于带有冷凝管和温度计的四口烧瓶中,在搅拌状态下加热至70℃,然后加入200g环氧蓖麻油脂肪酸甲酯,测得反应体系初始的环氧值为5.46,并在该温度下进行开环反应。反应过程中每隔30min中取样,测定其环氧值,当环氧值小于0.08时(t=10h),停止反应。上述溶液冷却至室温,上述溶液冷却至室温,上述溶液冷却至室温,静置沉降,产物与酸性聚合离子液体分层,下层离心分离后得酸性聚合离子液体催化剂,将上层反应溶液减压蒸馏,最终得到澄清透明的异丁醇改性生物润滑油。生物润滑油的环氧值为0.066,转化率为98.8%,酸值为0.79(mgKOH/g),40℃运动粘度为35.50(mm2/s)。Weigh 114.4g of isobutanol and 4g of acidic polymerization vinyl ionic liquid catalyst and place them in a four-necked flask with a condenser tube and a thermometer, heat to 70°C under stirring, then add 200g of epoxy castor oil fatty acid methyl ester, measure The initial epoxy value of the reaction system was 5.46, and the ring-opening reaction was carried out at this temperature. During the reaction, samples were taken every 30 minutes to measure the epoxy value. When the epoxy value was less than 0.08 (t=10h), the reaction was stopped. The above solution is cooled to room temperature, the above solution is cooled to room temperature, the above solution is cooled to room temperature, allowed to settle, the product is layered with the acidic polymeric ionic liquid, the lower layer is centrifuged to obtain an acidic polymeric ionic liquid catalyst, and the upper layer reaction solution is distilled under reduced pressure, Finally, a clear and transparent isobutanol-modified biological lubricating oil was obtained. The epoxy value of the bio-lubricating oil was 0.066, the conversion rate was 98.8%, the acid value was 0.79 (mgKOH/g), and the kinematic viscosity at 40°C was 35.50 (mm 2 /s).
实施例7:Example 7:
称取68g乙醇和4g酸性聚合烯丙基离子液体催化剂放于带有冷凝管和温度计的四口烧瓶中,在搅拌状态下加热至80℃,然后加入200g环氧大豆油脂肪酸甲酯,测得反应体系初始的环氧值为5.46,并在该温度下进行开环反应。反应过程中每隔30min中取样,测定其环氧值,当环氧值小于0.08时(t=10h),停止反应。上述溶液冷却至室温,静置沉降,产物与酸性聚合离子液体分层,下层离心分离后得酸性聚合离子液体催化剂,将上层反应溶液减压蒸馏,最终得到澄清透明的乙醇改性生物润滑油。生物润滑油的环氧值为0.07,转化率为98.7%,酸值为0.76(mgKOH/g),40℃运动粘度为38.32(mm2/s)。Weigh 68g of ethanol and 4g of acidic polymerized allyl ionic liquid catalyst and place it in a four-necked flask with a condenser tube and a thermometer, heat to 80°C under stirring, then add 200g of epoxidized soybean oil fatty acid methyl ester, and measure The initial epoxy value of the reaction system was 5.46, and the ring-opening reaction was carried out at this temperature. During the reaction, samples were taken every 30 minutes to measure the epoxy value. When the epoxy value was less than 0.08 (t=10h), the reaction was stopped. The above solution is cooled to room temperature, allowed to settle, the product is layered with the acidic polymeric ionic liquid, the lower layer is centrifuged to obtain an acidic polymeric ionic liquid catalyst, and the upper layer reaction solution is decompressed and distilled to finally obtain a clear and transparent ethanol-modified biological lubricating oil. The epoxy value of the bio-lubricating oil was 0.07, the conversion rate was 98.7%, the acid value was 0.76 (mgKOH/g), and the kinematic viscosity at 40°C was 38.32 (mm 2 /s).
实施例8:Example 8:
称取68g乙醇和4g酸性聚合烯丁基离子液体催化剂放于带有冷凝管和温度计的四口烧瓶中,在搅拌状态下加热至80℃,然后加入200g环氧大豆油脂肪酸甲酯,测得反应体系初始的环氧值为5.46,并在该温度下进行开环反应。反应过程中每隔30min中取样,测定其环氧值,当环氧值小于0.08时(t=10h),停止反应。上述溶液冷却至室温,静置沉降,产物与酸性聚合离子液体分层,下层离心分离酸性聚合离子液体催化剂,将上层反应溶液减压蒸馏,最终得到澄清透明的乙醇改性生物润滑油。生物润滑油的环氧值为0.069,转化率为98.7%,酸值为0.77(mgKOH/g),40℃运动粘度为38.23(mm2/s)。Weigh 68g of ethanol and 4g of acidic polymerized alkenyl ionic liquid catalyst and place them in a four-necked flask with a condenser tube and a thermometer, heat to 80°C under stirring, then add 200g of epoxidized soybean oil fatty acid methyl ester, and measure The initial epoxy value of the reaction system was 5.46, and the ring-opening reaction was carried out at this temperature. During the reaction, samples were taken every 30 minutes to measure the epoxy value. When the epoxy value was less than 0.08 (t=10h), the reaction was stopped. The above solution is cooled to room temperature, allowed to settle, the product is layered with the acidic polymeric ionic liquid, the lower layer is centrifuged to separate the acidic polymeric ionic liquid catalyst, and the upper layer of the reaction solution is decompressed and distilled to finally obtain a clear and transparent ethanol-modified biological lubricating oil. The epoxy value of the bio-lubricating oil was 0.069, the conversion rate was 98.7%, the acid value was 0.77 (mgKOH/g), and the kinematic viscosity at 40°C was 38.23 (mm 2 /s).
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