CN101735254B - A kind of synthetic method of borate - Google Patents
A kind of synthetic method of borate Download PDFInfo
- Publication number
- CN101735254B CN101735254B CN2008101621263A CN200810162126A CN101735254B CN 101735254 B CN101735254 B CN 101735254B CN 2008101621263 A CN2008101621263 A CN 2008101621263A CN 200810162126 A CN200810162126 A CN 200810162126A CN 101735254 B CN101735254 B CN 101735254B
- Authority
- CN
- China
- Prior art keywords
- ionic liquid
- alcohol
- boric acid
- borate
- 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.)
- Expired - Fee Related
Links
- BTBUEUYNUDRHOZ-UHFFFAOYSA-N Borate Chemical compound [O-]B([O-])[O-] BTBUEUYNUDRHOZ-UHFFFAOYSA-N 0.000 title claims abstract description 11
- 238000010189 synthetic method Methods 0.000 title claims description 7
- 239000002608 ionic liquid Substances 0.000 claims abstract description 57
- 238000006243 chemical reaction Methods 0.000 claims abstract description 41
- KGBXLFKZBHKPEV-UHFFFAOYSA-N boric acid Chemical compound OB(O)O KGBXLFKZBHKPEV-UHFFFAOYSA-N 0.000 claims abstract description 37
- 239000004327 boric acid Substances 0.000 claims abstract description 35
- -1 cycloalkyl alcohol Chemical compound 0.000 claims abstract description 31
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims abstract description 23
- 238000005886 esterification reaction Methods 0.000 claims abstract description 19
- 239000003960 organic solvent Substances 0.000 claims abstract description 19
- 239000011831 acidic ionic liquid Substances 0.000 claims abstract description 15
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 claims abstract description 12
- RAXXELZNTBOGNW-UHFFFAOYSA-N imidazole Natural products C1=CNC=N1 RAXXELZNTBOGNW-UHFFFAOYSA-N 0.000 claims abstract description 12
- JUJWROOIHBZHMG-UHFFFAOYSA-N Pyridine Chemical compound C1=CC=NC=C1 JUJWROOIHBZHMG-UHFFFAOYSA-N 0.000 claims abstract description 8
- 239000000126 substance Substances 0.000 claims abstract description 5
- UMJSCPRVCHMLSP-UHFFFAOYSA-N pyridine Natural products COC1=CC=CN=C1 UMJSCPRVCHMLSP-UHFFFAOYSA-N 0.000 claims abstract description 4
- 150000003242 quaternary ammonium salts Chemical class 0.000 claims abstract description 4
- 238000001308 synthesis method Methods 0.000 claims abstract 2
- 239000005416 organic matter Substances 0.000 claims description 15
- RTZKZFJDLAIYFH-UHFFFAOYSA-N ether Substances CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 claims description 12
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 claims description 6
- APRRQJCCBSJQOQ-UHFFFAOYSA-N 4-amino-5-hydroxynaphthalene-2,7-disulfonic acid Chemical compound OS(=O)(=O)C1=CC(O)=C2C(N)=CC(S(O)(=O)=O)=CC2=C1 APRRQJCCBSJQOQ-UHFFFAOYSA-N 0.000 claims description 4
- 238000010438 heat treatment Methods 0.000 claims description 4
- 238000004508 fractional distillation Methods 0.000 claims description 3
- 239000000203 mixture Substances 0.000 claims description 3
- 230000018044 dehydration Effects 0.000 claims description 2
- 238000006297 dehydration reaction Methods 0.000 claims description 2
- 125000001495 ethyl group Chemical group [H]C([H])([H])C([H])([H])* 0.000 claims description 2
- 125000001449 isopropyl group Chemical group [H]C([H])([H])C([H])(*)C([H])([H])[H] 0.000 claims description 2
- 125000002496 methyl group Chemical group [H]C([H])([H])* 0.000 claims description 2
- 125000004108 n-butyl group Chemical group [H]C([H])([H])C([H])([H])C([H])([H])C([H])([H])* 0.000 claims description 2
- 125000001436 propyl group Chemical group [H]C([*])([H])C([H])([H])C([H])([H])[H] 0.000 claims description 2
- 125000001033 ether group Chemical group 0.000 claims 1
- 238000000638 solvent extraction Methods 0.000 claims 1
- 238000005406 washing Methods 0.000 claims 1
- 238000000034 method Methods 0.000 abstract description 17
- 238000000926 separation method Methods 0.000 abstract description 9
- 239000002904 solvent Substances 0.000 abstract description 5
- 239000003054 catalyst Substances 0.000 abstract description 3
- 238000003912 environmental pollution Methods 0.000 abstract description 3
- 238000002360 preparation method Methods 0.000 abstract description 3
- DNIAPMSPPWPWGF-GSVOUGTGSA-N (R)-(-)-Propylene glycol Chemical compound C[C@@H](O)CO DNIAPMSPPWPWGF-GSVOUGTGSA-N 0.000 abstract 1
- 125000000217 alkyl group Chemical group 0.000 abstract 1
- 239000010410 layer Substances 0.000 description 33
- IVDFJHOHABJVEH-UHFFFAOYSA-N pinacol Chemical compound CC(C)(O)C(C)(C)O IVDFJHOHABJVEH-UHFFFAOYSA-N 0.000 description 22
- 238000004445 quantitative analysis Methods 0.000 description 15
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 15
- 239000000047 product Substances 0.000 description 13
- 238000004451 qualitative analysis Methods 0.000 description 13
- 238000003756 stirring Methods 0.000 description 13
- HPXRVTGHNJAIIH-UHFFFAOYSA-N cyclohexanol Chemical compound OC1CCCCC1 HPXRVTGHNJAIIH-UHFFFAOYSA-N 0.000 description 12
- 230000032050 esterification Effects 0.000 description 12
- 238000002290 gas chromatography-mass spectrometry Methods 0.000 description 12
- 239000007788 liquid Substances 0.000 description 12
- RVEJOWGVUQQIIZ-UHFFFAOYSA-N 1-hexyl-3-methylimidazolium Chemical compound CCCCCCN1C=C[N+](C)=C1 RVEJOWGVUQQIIZ-UHFFFAOYSA-N 0.000 description 6
- ISWSIDIOOBJBQZ-UHFFFAOYSA-N Phenol Chemical compound OC1=CC=CC=C1 ISWSIDIOOBJBQZ-UHFFFAOYSA-N 0.000 description 5
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 4
- 239000003208 petroleum Substances 0.000 description 4
- 238000013517 stratification Methods 0.000 description 4
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 description 2
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- KFZMGEQAYNKOFK-UHFFFAOYSA-N Isopropanol Chemical compound CC(C)O KFZMGEQAYNKOFK-UHFFFAOYSA-N 0.000 description 2
- LRHPLDYGYMQRHN-UHFFFAOYSA-N N-Butanol Chemical compound CCCCO LRHPLDYGYMQRHN-UHFFFAOYSA-N 0.000 description 2
- 239000002253 acid Substances 0.000 description 2
- 150000007513 acids Chemical class 0.000 description 2
- 150000004945 aromatic hydrocarbons Chemical class 0.000 description 2
- 239000003795 chemical substances by application Substances 0.000 description 2
- 238000011161 development Methods 0.000 description 2
- 238000012423 maintenance Methods 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 239000012299 nitrogen atmosphere Substances 0.000 description 2
- 239000012044 organic layer Substances 0.000 description 2
- 239000012429 reaction media Substances 0.000 description 2
- 230000035484 reaction time Effects 0.000 description 2
- FAQYAMRNWDIXMY-UHFFFAOYSA-N trichloroborane Chemical compound ClB(Cl)Cl FAQYAMRNWDIXMY-UHFFFAOYSA-N 0.000 description 2
- 238000006220 Baeyer-Villiger oxidation reaction Methods 0.000 description 1
- ACCQAHOGVBNWCP-UHFFFAOYSA-N CC1(C)OB(OC2CCCCC2)OC1(C)C Chemical compound CC1(C)OB(OC2CCCCC2)OC1(C)C ACCQAHOGVBNWCP-UHFFFAOYSA-N 0.000 description 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 208000005156 Dehydration Diseases 0.000 description 1
- 238000005698 Diels-Alder reaction Methods 0.000 description 1
- 238000005727 Friedel-Crafts reaction Methods 0.000 description 1
- 229920001967 Metal rubber Polymers 0.000 description 1
- 238000007171 acid catalysis Methods 0.000 description 1
- 238000007259 addition reaction Methods 0.000 description 1
- 239000002318 adhesion promoter Substances 0.000 description 1
- 150000001298 alcohols Chemical class 0.000 description 1
- 150000001336 alkenes Chemical class 0.000 description 1
- 239000013556 antirust agent Substances 0.000 description 1
- 239000002216 antistatic agent Substances 0.000 description 1
- 229910052786 argon Inorganic materials 0.000 description 1
- 239000011830 basic ionic liquid Substances 0.000 description 1
- 239000007767 bonding agent Substances 0.000 description 1
- 229910021538 borax Inorganic materials 0.000 description 1
- 150000001642 boronic acid derivatives Chemical class 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- CREMABGTGYGIQB-UHFFFAOYSA-N carbon carbon Chemical compound C.C CREMABGTGYGIQB-UHFFFAOYSA-N 0.000 description 1
- 239000011203 carbon fibre reinforced carbon Substances 0.000 description 1
- 239000000969 carrier Substances 0.000 description 1
- 238000009903 catalytic hydrogenation reaction Methods 0.000 description 1
- 238000006555 catalytic reaction Methods 0.000 description 1
- 239000007809 chemical reaction catalyst Substances 0.000 description 1
- 239000003153 chemical reaction reagent Substances 0.000 description 1
- 239000002131 composite material Substances 0.000 description 1
- 238000005859 coupling reaction Methods 0.000 description 1
- 230000032798 delamination Effects 0.000 description 1
- JKWMSGQKBLHBQQ-UHFFFAOYSA-N diboron trioxide Chemical compound O=BOB=O JKWMSGQKBLHBQQ-UHFFFAOYSA-N 0.000 description 1
- 238000004090 dissolution Methods 0.000 description 1
- 239000003995 emulsifying agent Substances 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 239000003822 epoxy resin Substances 0.000 description 1
- 239000000945 filler Substances 0.000 description 1
- 239000003063 flame retardant Substances 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 229910002804 graphite Inorganic materials 0.000 description 1
- 239000010439 graphite Substances 0.000 description 1
- 238000007037 hydroformylation reaction Methods 0.000 description 1
- 230000003301 hydrolyzing effect Effects 0.000 description 1
- 239000011261 inert gas Substances 0.000 description 1
- 239000003999 initiator Substances 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- 238000011031 large-scale manufacturing process Methods 0.000 description 1
- 239000000314 lubricant Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000008204 material by function Substances 0.000 description 1
- 238000010327 methods by industry Methods 0.000 description 1
- 239000002086 nanomaterial Substances 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 229920000647 polyepoxide Polymers 0.000 description 1
- 239000003755 preservative agent Substances 0.000 description 1
- 230000005855 radiation Effects 0.000 description 1
- 238000006722 reduction reaction Methods 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 239000003566 sealing material Substances 0.000 description 1
- 239000004328 sodium tetraborate Substances 0.000 description 1
- 235000010339 sodium tetraborate Nutrition 0.000 description 1
- 239000004449 solid propellant Substances 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 239000004094 surface-active agent Substances 0.000 description 1
- 230000002194 synthesizing effect Effects 0.000 description 1
- 231100000331 toxic Toxicity 0.000 description 1
- 230000002588 toxic effect Effects 0.000 description 1
- 238000005809 transesterification reaction Methods 0.000 description 1
- LGQXXHMEBUOXRP-UHFFFAOYSA-N tributyl borate Chemical compound CCCCOB(OCCCC)OCCCC LGQXXHMEBUOXRP-UHFFFAOYSA-N 0.000 description 1
- AVBGNFCMKJOFIN-UHFFFAOYSA-N triethylammonium acetate Chemical class CC(O)=O.CCN(CC)CC AVBGNFCMKJOFIN-UHFFFAOYSA-N 0.000 description 1
- NHDIQVFFNDKAQU-UHFFFAOYSA-N tripropan-2-yl borate Chemical compound CC(C)OB(OC(C)C)OC(C)C NHDIQVFFNDKAQU-UHFFFAOYSA-N 0.000 description 1
- 238000007039 two-step reaction Methods 0.000 description 1
Classifications
-
- 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
- Y02P20/54—Improvements relating to the production of bulk chemicals using solvents, e.g. supercritical solvents or ionic liquids
Abstract
Description
技术领域 technical field
本发明涉及硼酸酯的制备方法。具体为以对水稳定的、水溶性的酸性离子液体为反应介质和催化剂,制备硼酸酯。The present invention relates to the preparation method of borate. Specifically, the boric acid ester is prepared by using a water-stable and water-soluble acidic ionic liquid as a reaction medium and a catalyst.
背景技术 Background technique
硼酸酯是一种无机酸酯类化合物,其本身和衍生物可以应用在众多领域中。如可作为高效环保型润滑剂,防锈剂,改性纳米材料橡胶填充剂,表面活性剂,固体推进剂中的键合剂,复合石墨密封材料,环氧树脂固化促进剂,汽车制动液,金属-橡胶粘合促进剂,抗静电剂,阻燃剂,乳化剂,光引发及热引发剂,防腐剂以及抗中子辐射材料等。Boric acid ester is a kind of inorganic acid ester compound, itself and its derivatives can be applied in many fields. For example, it can be used as an efficient and environmentally friendly lubricant, antirust agent, modified nanomaterial rubber filler, surfactant, bonding agent in solid propellant, composite graphite sealing material, epoxy resin curing accelerator, automobile brake fluid, Metal-rubber adhesion promoters, antistatic agents, flame retardants, emulsifiers, photoinitiators and thermal initiators, preservatives and anti-neutron radiation materials, etc.
传统制备硼酸酯的方法主要有五种:(1)三氯化硼与醇或酚的反应,(2)硼酸与醇或酚反应,(3)硼酐与醇或酚反应,(4)硼砂与醇或酚在酸催化下的反应,(5)酯交换反应。第一种方法用到活泼、较贵的三氯化硼,不适用于大量生产。第二种方法,以大量的芳烃类化合物作为溶剂和带水剂,因而会对环境有较大的危害。第三种方法会产生较多的副产物,收率不高。第四种方法,用到腐蚀性硫酸等强酸,对设备的使用和维护费用要求较高,且对环境造成污染。第五种方法,有两步反应,先制备一种简单易得的硼酸酯,再与醇或酚发生交换反应得到相应的硼酸酯。所以该方法生产效率不高。There are five main methods for traditionally preparing boric acid esters: (1) the reaction of boron trichloride and alcohol or phenol, (2) the reaction of boric acid and alcohol or phenol, (3) the reaction of boric anhydride and alcohol or phenol, (4) The reaction of borax with alcohol or phenol under acid catalysis, (5) transesterification reaction. The first method uses lively and expensive boron trichloride, which is not suitable for mass production. The second method uses a large amount of aromatic hydrocarbons as solvent and water-carrying agent, which will cause greater harm to the environment. The third method can produce more by-products, and the yield is not high. The fourth method uses strong acids such as corrosive sulfuric acid, which requires high equipment use and maintenance costs and pollutes the environment. The fifth method has a two-step reaction. Firstly, a simple and easy-to-obtain borate is prepared, and then exchanged with alcohol or phenol to obtain the corresponding borate. Therefore, the production efficiency of this method is not high.
离子液体自被合成出来以后,人们一直在探索它在化学、化工中的应用,近年来离子液体呈现出多功能化的发展趋势,合成出了各种功能化的离子,如手性离子液体,酸性离子液体,碱性离子液体负载型离子液体催化剂和试剂以及目标分子载体的离子液体等。离子液体在化学领域中的应用也日趋广泛,如在烯烃、醇的氧化,Baeyer-Villiger反应,酯化反应,还原反催化加氢应(,Friedel-Crafts反应,Diels-Alder反应,碳-碳偶联反应(Heck,Suzuki),加成反应(Knovenagel,Michael),氢甲酰化反应,取代反应等。此外,离子液体研究的发展已不仅仅局限在合成化学和催化反应中的应用,已扩展到过程工程,功能材料,环境工程以及生命科学等诸多领域。利用离子液体选择性溶解的特性,BASF公司在2002年成功开发了制备烷基苯基瞵的工艺,该工艺被业界认为是离子液体实现规模化应用最早的实例。Since the ionic liquid was synthesized, people have been exploring its application in chemistry and chemical industry. In recent years, ionic liquids have shown a multifunctional development trend, and various functional ions have been synthesized, such as chiral ionic liquids. Acidic ionic liquids, basic ionic liquids, supported ionic liquid catalysts and reagents, and ionic liquids for target molecular carriers, etc. The application of ionic liquids in the chemical field is also becoming more and more extensive, such as oxidation of olefins and alcohols, Baeyer-Villiger reaction, esterification reaction, reduction and reverse catalytic hydrogenation reaction (, Friedel-Crafts reaction, Diels-Alder reaction, carbon-carbon Coupling reaction (Heck, Suzuki), addition reaction (Knovenagel, Michael), hydroformylation reaction, substitution reaction, etc. In addition, the development of ionic liquid research is not limited to the application in synthetic chemistry and catalytic reaction, has been Expanded to many fields such as process engineering, functional materials, environmental engineering and life sciences. Utilizing the selective dissolution characteristics of ionic liquids, BASF successfully developed a process for the preparation of alkylphenylsulfone in 2002, which is considered by the industry to be an ionic The earliest example of large-scale application of liquid.
发明内容 Contents of the invention
本发明所有解决的技术问题是针对传统制备无机硼酸与醇的酯化方法中存在的问题,以水溶性酸性离子液体为反应介质和催化剂,开发出一种新的硼酸酯的合成方法,该方法与传统方法相比,具有操作简单、反应时间短、分离容易,避免使用芳烃作为溶剂,对环境污染小,适用于规模化生产。All the technical problems solved by the present invention are aimed at the problems existing in the traditional esterification method for preparing inorganic boric acid and alcohol, and develop a new synthetic method of boric acid ester with water-soluble acidic ionic liquid as reaction medium and catalyst. Compared with the traditional method, the method has the advantages of simple operation, short reaction time, easy separation, avoids the use of aromatic hydrocarbons as solvents, has little environmental pollution, and is suitable for large-scale production.
本发明解决上述技术问题所采用的技术方案为:一种硼酸酯的合成方法,其特征在于在酸性离子液体中,催化硼酸与醇的酯化反应而获得硼酸酯;所用的酸性离子液体采用咪唑类离子液体、吡啶类离子液体或季铵盐类离子液体,酸性离子液体为如下所示的一种,可为咪唑类离子液体(I-1),吡啶类离子液体(I-2)或季铵盐类离子液体(I-3):The technical solution adopted by the present invention to solve the above-mentioned technical problems is: a synthetic method of boric acid ester, which is characterized in that in acidic ionic liquid, the esterification reaction of boric acid and alcohol is catalyzed to obtain boric acid ester; the acidic ionic liquid used Using imidazole ionic liquid, pyridine ionic liquid or quaternary ammonium salt ionic liquid, the acidic ionic liquid is one of the following, which can be imidazole ionic liquid (I-1), pyridine ionic liquid (I-2) Or quaternary ammonium salt ionic liquid (I-3):
其中,R1的含义为H,或磺酸丙基;R2的含义为H,或磺酸丙基;X的含义为HSO4,BF4,o-CH3C6H5SO3,或者CH3COO。Wherein, the meaning of R 1 is H, or sulfonic acid propyl group; the meaning of R 2 is H, or sulfonic acid propyl group; the meaning of X is HSO 4 , BF 4 , o-CH 3 C 6 H 5 SO 3 , or CH3COO .
制备所得的硼酸酯,为如下所示任意一种,均烷基硼酸酯(II-1),均环烷基硼酸酯(II-2),混合环烷基-1,2-氧杂-烷基硼酸酯(II-3):The borates prepared are any of the following, homo-alkyl borate (II-1), homo-cycloalkyl borate (II-2), mixed cycloalkyl-1,2-oxo Hetero-alkyl borates (II-3):
其中R3为甲基,乙基,丙基,异丙基,正丁基,或者正辛基的一种。Wherein R 3 is one of methyl, ethyl, propyl, isopropyl, n-butyl, or n-octyl.
本发明提供的技术方案是,一种酸性离子液体催化合成硼酸酯的方法,具体为:The technical solution provided by the invention is a method for catalytically synthesizing boric acid ester with an acidic ionic liquid, specifically:
将离子液体、硼酸、醇按一定摩尔比(离子液体:硼酸:一元醇=0.5~10:1:3,或离子液体:硼酸:一元醇:二元醇=0.5~10:1:1:1)加入到反应瓶中,搅拌反应。反应温度可为室温~90度,反应时间为2~15小时。反应完毕,静置分层。取出上层有机层,分馏得到产品硼酸酯。对于不分层的体系,可以加入少量有机溶剂萃取硼酸酯,再分馏得到产品。下层离子液体层,经少量有机溶剂洗涤2-5次、加热减压除水、除有机物后,重复使用。Mix the ionic liquid, boric acid, and alcohol in a certain molar ratio (ionic liquid: boric acid: monohydric alcohol = 0.5-10:1:3, or ionic liquid: boric acid: monohydric alcohol: dihydric alcohol = 0.5-10:1:1:1 ) was added to the reaction flask, and the reaction was stirred. The reaction temperature can be from room temperature to 90 degrees, and the reaction time is 2 to 15 hours. After the reaction was completed, the mixture was allowed to stand for stratification. The upper organic layer was taken out, and fractional distillation was carried out to obtain the product boric acid ester. For a non-layered system, a small amount of organic solvent can be added to extract the boric acid ester, and then the product can be obtained by fractional distillation. The lower ionic liquid layer is washed 2-5 times with a small amount of organic solvent, heated and decompressed to remove water and organic matter, and then reused.
上述所用的有机溶剂可为乙醚,石油醚,苯,或甲苯等。The organic solvent used above can be diethyl ether, petroleum ether, benzene, or toluene and the like.
当制备较易吸湿水解的硼酸酯II-1时,反应和分离应在惰性气体氮气或氩气下进行;当制备水解稳定性较好的硼酸酯II-2或II-3时,反应可在空气中操作。When preparing borate II-1, which is easier to absorb moisture and hydrolyze, the reaction and separation should be carried out under inert gas nitrogen or argon; when preparing borate II-2 or II-3 with better hydrolytic stability, the reaction Can operate in air.
与现有技术相比,本发明的优点在于:(1)无须使用强腐蚀性的硫酸等强酸,减少了对环境的污染和降低了设备维护费的问题;(2)无须使用大量的有毒有害的苯类溶剂作为溶剂和带水剂,减少了对环境的污染;(3)对水稳定的酸性离子液体不断地将酯化反应过程中产生的水移出有机层,进入离子液体层,加快和促进了酯化反应进程;(4)产物分离容易;(5)酸性离子液体经简单脱水处理后,可重复使用。Compared with the prior art, the present invention has the advantages of: (1) no need to use strong acids such as highly corrosive sulfuric acid, which reduces environmental pollution and equipment maintenance costs; (2) no need to use a large amount of toxic and harmful The benzene solvent used as a solvent and water-carrying agent reduces the pollution to the environment; (3) the water-stable acidic ionic liquid constantly moves the water produced in the esterification process out of the organic layer and enters the ionic liquid layer to speed up and The progress of the esterification reaction is promoted; (4) the separation of the product is easy; (5) the acidic ionic liquid can be reused after simple dehydration treatment.
具体实施方式 Detailed ways
以下结合实施例对本发明作进一步详细描述。Below in conjunction with embodiment the present invention is described in further detail.
以下将通过实施实例对本发明的实施方式进行说明,实施实例并不限制本发明的保护范围。实施实例中所用的离子液体:质子化甲基咪唑-硫酸氢根负离子([Hmin]+HSO4 -),质子化甲基咪唑-四氟硼酸根离子([Hmim]+BF4 -,质子化三乙胺-醋酸根负离子([Et3NH]+[CH3COO-]),甲基咪唑丙磺酸-硫酸氢根负离子([(CH2)3SO3Hmin]+HSO4 -),三乙基胺基丙磺酸-硫酸氢根负离子([(CH2)3SO3HTEA]+HSO4 -),吡啶丙磺酸-硫酸氢根负离子([(CH2)3SO3HPy]+HSO4 -),质子化三乙胺-四氟硼酸根离子([Et3NH]+BF4 -),吡啶丙磺酸-对甲苯磺酸根负离子([(CH2)3SO3HPy]+[o-CH3C6H5SO3]-),吡啶丙磺酸-四氟硼酸根离子[(CH2)3SO3HPy]+BF4 -),根据公开报道的方法制备(岳彩波,魏远洋,吕敏杰,应用化学2006,23,1282-1285。H.-P.Zhu,F.Yang,J.Tang,M.-Y.He;Green Chem.,2003,5,38-39。C.-M.Wang,L.-P.Guo,H.-R.Li,Y.Wang,J.-Y.Weng,L.-H.Wu;GreenChem.,2006,8,603-607。A.C.Cole,J.L Jensen,I.Ntai,K.L.T.Tran,K.J.Weaver,D.C.Forbes,J.H.Davis,Jr.;J.Am.Chem.Soc.,2002,124,5962-5963。J.-Z.Guo,X.-H.Cong,D.Liu,X.-T.Zhang,Z.-D.Hu,Z.-L.Sun;Catal.Commun.,2004,5,473-477.C.-M.Wang,L.-P.Guo,H.-R.Li,Y.Wang,J.-Y.Weng,L.-H.Wu;Green Chem.,2006,8,603-607。王涛,刑华斌,周震寰,戴猷元,专利号CN1594280A)。The embodiments of the present invention will be described below through examples, which do not limit the protection scope of the present invention. The ionic liquid used in the implementation example: protonated methylimidazolium-hydrogensulfate anion ([Hmin] + HSO 4 - ), protonated methylimidazolium-tetrafluoroborate ion ([Hmim] + BF 4 - , protonated Triethylamine-acetate anion ([Et 3 NH] + [CH 3 COO - ]), methylimidazolium propanesulfonate-hydrogen sulfate anion ([(CH 2 ) 3 SO 3 Hmin] + HSO 4 - ), Triethylaminopropanesulfonic acid-hydrogensulfate anion ([(CH 2 ) 3 SO 3 HTEA] + HSO 4 - ), pyridinepropanesulfonic acid-hydrogensulfate anion ([(CH 2 ) 3 SO 3 HPy] + HSO 4 - ), protonated triethylamine-tetrafluoroborate ion ([Et 3 NH] + BF 4 - ), pyridine propanesulfonic acid-p-toluenesulfonate anion ([(CH 2 ) 3 SO 3 HPy] + [o-CH 3 C 6 H 5 SO 3 ] - ), pyridine propanesulfonic acid-tetrafluoroborate ion [(CH 2 ) 3 SO 3 HPy] + BF 4 - ), prepared according to published methods (Yue Caibo , Wei Yuanyang, Lu Minjie, Applied Chemistry 2006, 23, 1282-1285. H.-P.Zhu, F.Yang, J.Tang, M.-Y.He; Green Chem., 2003, 5, 38-39. C.-M. Wang, L.-P. Guo, H.-R. Li, Y. Wang, J.-Y. Weng, L.-H. Wu; Green Chem., 2006, 8, 603-607. ACCole, JL Jensen, I.Ntai, KLTTran, KJWeaver, DCForbes, JHDavis, Jr.; J.Am.Chem.Soc., 2002, 124, 5962-5963. J.-Z.Guo, X.-H.Cong , D.Liu, X.-T.Zhang, Z.-D.Hu, Z.-L.Sun; Catal.Commun., 2004, 5, 473-477.C.-M.Wang, L.-P .Guo, H.-R.Li, Y.Wang, J.-Y.Weng, L.-H.Wu; Green Chem., 2006, 8, 603-607. Wang Tao, Xing Huabin, Zhou Zhenhuan, Dai Youyuan, Patent No. CN1594280A).
实施实例1:Implementation example 1:
将1.8g(10mmol)离子液体[Hmim]+HSO4 -和0.62g(10mmol)硼酸及1.38g(30mmol)乙醇放入反应瓶中,搅拌,加热,控制温度为80℃,反应2h,反应液静置,不分层,透明溶液,氮气氛下用石油醚萃取产物硼酸三乙酯。经GC-MS定性、定量分析得到产率为74%。离子液体层,经少量有机溶剂洗涤2-5次、加热真空干燥除水、除有机物后,可重复使用。Put 1.8g (10mmol) ionic liquid [Hmim] + HSO 4 - , 0.62g (10mmol) boric acid and 1.38g (30mmol) ethanol into the reaction flask, stir, heat, control the temperature at 80°C, react for 2h, the reaction solution Stand still, no layering, transparent solution, and extract the product triethyl borate with petroleum ether under nitrogen atmosphere. Qualitative and quantitative analysis by GC-MS gave a yield of 74%. The ionic liquid layer can be reused after being washed 2-5 times with a small amount of organic solvent, heated and vacuum-dried to remove water and organic matter.
实施实例2:Implementation example 2:
将1.8g(10mmol)离子液体[Hmim]+HSO4 -和0.62g(10mmol)硼酸及1.8g(30mmol)异丙醇放入反应瓶中,搅拌,加热,控制温度为80℃,反应2h,反应液静置,分层,上层为无色澄清溶液。在氮气氛下,分出酯化产物硼酸三异丙酯。经GC-MS定性、定量分析得到产率为89.7%。下层离子液体层,经少量有机溶剂洗涤2-5次、加热真空干燥除水、除有机物后,可重复使用。Put 1.8g (10mmol) ionic liquid [Hmim] + HSO 4 - , 0.62g (10mmol) boric acid and 1.8g (30mmol) isopropanol into the reaction flask, stir, heat, control the temperature at 80°C, and react for 2h, The reaction solution was allowed to stand, and the layers were separated, and the upper layer was a colorless clear solution. Under a nitrogen atmosphere, the esterification product triisopropyl borate was separated. The yield was 89.7% by GC-MS qualitative and quantitative analysis. The lower ionic liquid layer can be reused after being washed 2-5 times with a small amount of organic solvent, heated and vacuum-dried to remove water and organic matter.
实施实例3:Implementation example 3:
将1.8g(10mmol)离子液体[Hmim]+HSO4 -和0.62g(10mmol)硼酸及2.64g(30mmol)正丁醇放入反应瓶中,搅拌,加热,控制温度为80℃,反应2h,反应液静置,分层,上下两层均为无色澄清溶液,在氮气氛下,分出酯化产物硼酸三丁酯。经GC-MS定性、定量分析得到产率为98.9%。下层离子液体层,经少量有机溶剂洗涤2-5次、加热真空干燥除水、除有机物后,可重复使用。Put 1.8g (10mmol) ionic liquid [Hmim] + HSO 4 - , 0.62g (10mmol) boric acid and 2.64g (30mmol) n-butanol into the reaction flask, stir, heat, control the temperature at 80°C, and react for 2h. The reaction solution was allowed to stand and separated into layers. The upper and lower layers were both colorless and clear solutions. Under a nitrogen atmosphere, the esterification product tributyl borate was separated. The yield was 98.9% through qualitative and quantitative analysis by GC-MS. The lower ionic liquid layer can be reused after being washed 2-5 times with a small amount of organic solvent, heated and vacuum-dried to remove water and organic matter.
实施实例4:Implementation example 4:
将1.8g(10mmol)离子液体[Hmim]+HSO4 -和0.62g(10mmol)硼酸及1g(10mmol)环己醇、频哪醇1.18(10mmol)放入反应瓶中,搅拌,加热,控制温度为80℃,反应2h,反应液静置,分层,上下两层均为淡黄色透明溶液,通过分液分出酯化产物环己醇频哪醇硼酸酯。经GC-MS定性、定量分析得到产率为73.7%。下层离子液体层,经少量有机溶剂洗涤2-5次、加热真空干燥除水、除有机物后,重复使用3次,经GC-MS定性、定量分析,产率分别为83.9%,64.87%,65.27%。Put 1.8g (10mmol) ionic liquid [Hmim] + HSO 4 - , 0.62g (10mmol) boric acid and 1g (10mmol) cyclohexanol, pinacol 1.18 (10mmol) into the reaction flask, stir, heat, and control the temperature 80°C, react for 2 hours, let the reaction solution stand still, and separate layers, the upper and lower layers are light yellow transparent solutions, and the esterification product cyclohexanol pinacol borate is separated by liquid separation. The yield was 73.7% by GC-MS qualitative and quantitative analysis. The lower ionic liquid layer was washed 2-5 times with a small amount of organic solvent, heated and vacuum-dried to remove water and organic matter, and then reused 3 times. After qualitative and quantitative analysis by GC-MS, the yields were 83.9%, 64.87%, and 65.27%, respectively. %.
实施实例5:Implementation example 5:
将1.8g(10mmol)离子液体[Hmim]+HSO4 -和0.62g(10mmol)硼酸及1g(10mmol)环己醇、频哪醇1.18(10mmol)放入反应瓶中,室温下(30℃)搅拌。反应2h,反应液静置,分层,上下两层均为淡黄色透明溶液,通过分液分出酯化产物环己醇频哪醇硼酸酯。经GC-MS定性、定量分析得到产率为76.48%。Put 1.8g (10mmol) ionic liquid [Hmim] + HSO 4 - and 0.62g (10mmol) boric acid and 1g (10mmol) cyclohexanol, pinacol 1.18 (10mmol) into the reaction flask, at room temperature (30°C) Stir. After reacting for 2 hours, the reaction solution was allowed to stand still and layered. The upper and lower layers were light yellow transparent solutions, and the esterification product cyclohexanol pinacol borate was separated by liquid separation. The yield was 76.48% by GC-MS qualitative and quantitative analysis.
实施实例6:Implementation example 6:
将1.7g(10mmol)离子液体[Hmim]+BF4 -和0.62g(10mmol)硼酸及1g(10mmol)环己醇、频哪醇1.18(10mmol)放入反应瓶中,搅拌,加热,控制温度为80℃,反应6h,反应液静置,不分层,为淡黄色乳状液体,用石油醚萃取,得到酯化产物环己醇频哪醇硼酸酯,经GC-MS定性、定量分析得到产率为78.56%。离子液体层经少量有机溶剂洗涤2-5次、加热真空干燥除水、除有机物后,可重复使用。Put 1.7g (10mmol) ionic liquid [Hmim] + BF 4 - , 0.62g (10mmol) boric acid and 1g (10mmol) cyclohexanol, pinacol 1.18 (10mmol) into the reaction flask, stir, heat, and control the temperature 80°C, reacted for 6 hours, the reaction solution was left standing, without stratification, it was a light yellow milky liquid, extracted with petroleum ether, and the esterification product cyclohexanol pinacol borate was obtained, which was obtained through qualitative and quantitative analysis by GC-MS The yield was 78.56%. The ionic liquid layer can be reused after being washed 2-5 times with a small amount of organic solvent, heated and vacuum-dried to remove water and organic matter.
实施实例7:Implementation example 7:
将1.61g(10mmol)离子液体[Et3NH]+[CH3COO-]和0.62g(10mmol)硼酸及1g(10mmol)环己醇、频哪醇1.18(10mmol)放入反应瓶中,搅拌,加热,控制温度为80℃,反应6h,反应液静置,不分层,为黄色液体,用石油醚萃取,得到酯化产物环己醇频哪醇硼酸酯,经GC-MS定性、定量分析得到产率为96.3%。离子液体层经少量有机溶剂洗涤2-5次、加热真空干燥除水、除有机物后,可重复使用。Put 1.61g (10mmol) ionic liquid [Et 3 NH] + [CH 3 COO - ], 0.62g (10mmol) boric acid and 1g (10mmol) cyclohexanol, pinacol 1.18 (10mmol) into the reaction flask, stir , heating, controlling the temperature at 80°C, and reacting for 6 hours. The reaction solution was allowed to stand still without delamination. Quantitative analysis gave a yield of 96.3%. The ionic liquid layer can be reused after being washed 2-5 times with a small amount of organic solvent, heated and vacuum-dried to remove water and organic matter.
实施实例8:Implementation example 8:
将3.02g(10mmol)离子液体[(CH2)3SO3Hmin]+HSO4 -和0.62g(10mmol)硼酸及1g(10mmol)环己醇、频哪醇1.18(10mmol)放入反应瓶中,搅拌,加热,控制温度为80℃,反应6h,反应液静置,分层,上下两层为黄色液体,通过分液分出酯化产物环己醇频哪醇硼酸酯,经GC-MS定性、定量分析得到产率为82.1%。离子液体层经少量有机溶剂洗涤2-5次、加热真空干燥除水、除有机物后,可重复使用。Put 3.02g (10mmol) ionic liquid [(CH 2 ) 3 SO 3 Hmin] + HSO 4 - , 0.62g (10mmol) boric acid and 1g (10mmol) cyclohexanol, pinacol 1.18 (10mmol) into the reaction flask , stirring, heating, controlling the temperature at 80°C, and reacting for 6 hours. The reaction solution was allowed to stand and separated into layers. MS qualitative and quantitative analysis gave a yield of 82.1%. The ionic liquid layer can be reused after being washed 2-5 times with a small amount of organic solvent, heated and vacuum-dried to remove water and organic matter.
实施实例9:Implementation example 9:
将3.21g(10mmol)离子液体[(CH2)3SO3HTEA]+HSO4 -和0.62g(10mmol)硼酸及1g(10mmol)环己醇、频哪醇1.18(10mmol)放入反应瓶中,搅拌,加热,控制温度为80℃,反应6h,反应液静置,分层,上下两层为澄黄色液体,通过分液分出酯化产物环己醇频哪醇硼酸酯,经GC-MS定性、定量分析得到产率为72.71%。离子液体层经少量有机溶剂洗涤2-5次、加热真空干燥除水、除有机物后,可重复使用。Put 3.21g (10mmol) ionic liquid [(CH 2 ) 3 SO 3 HTEA] + HSO 4 - and 0.62g (10mmol) boric acid and 1g (10mmol) cyclohexanol, pinacol 1.18 (10mmol) into the reaction flask , Stir, heat, control the temperature at 80°C, react for 6h, let the reaction solution stand, and separate layers. -MS qualitative and quantitative analysis obtained a yield of 72.71%. The ionic liquid layer can be reused after being washed 2-5 times with a small amount of organic solvent, heated and vacuum-dried to remove water and organic matter.
实施实例10:Implementation example 10:
将2.99g(10mmol)离子液体[(CH2)3SO3HPy]+HSO4 -和0.62g(10mmol)硼酸及1g(10mmol)环己醇、频哪醇1.18(10mmol)放入反应瓶中,搅拌,加热,控制温度为80℃,反应6h,反应液静置,分层,上层为红棕色液体,下层为黄色液体,通过分液分出酯化产物环己醇频哪醇硼酸酯,经GC-MS定性、定量分析得到产率为80.13%。离子液体层经少量有机溶剂洗涤2-5次、加热真空干燥除水、除有机物后,可重复使用。Put 2.99g (10mmol) ionic liquid [(CH 2 ) 3 SO 3 HPy] + HSO 4 - and 0.62g (10mmol) boric acid and 1g (10mmol) cyclohexanol, pinacol 1.18 (10mmol) into the reaction flask , Stir, heat, control the temperature at 80°C, react for 6h, let the reaction solution stand, and separate layers, the upper layer is a reddish-brown liquid, the lower layer is a yellow liquid, and the esterification product cyclohexanol pinacol borate is separated by liquid separation , the yield was 80.13% through GC-MS qualitative and quantitative analysis. The ionic liquid layer can be reused after being washed 2-5 times with a small amount of organic solvent, heated and vacuum-dried to remove water and organic matter.
实施实例11:Implementation example 11:
将2.99g(10mmol)离子液体[(CH2)3SO3HPy]+HSO4 -和0.62g(10mmol)硼酸及1g(10mmol)环己醇、频哪醇1.18(10mmol)放入反应瓶中,搅拌,加热,控制温度为80℃,反应6h,反应液静置,分层,上层为红棕色液体,下层为黄色液体,通过分液分出酯化产物环己醇频哪醇硼酸酯,经GC-MS定性、定量分析得到产率为80.13%。离子液体层经少量有机溶剂洗涤2-5次、加热真空干燥除水、除有机物后,可重复使用。Put 2.99g (10mmol) ionic liquid [(CH 2 ) 3 SO 3 HPy] + HSO 4 - and 0.62g (10mmol) boric acid and 1g (10mmol) cyclohexanol, pinacol 1.18 (10mmol) into the reaction flask , Stir, heat, control the temperature at 80°C, react for 6h, let the reaction solution stand, and separate layers, the upper layer is a reddish-brown liquid, the lower layer is a yellow liquid, and the esterification product cyclohexanol pinacol borate is separated by liquid separation , the yield was 80.13% through GC-MS qualitative and quantitative analysis. The ionic liquid layer can be reused after being washed 2-5 times with a small amount of organic solvent, heated and vacuum-dried to remove water and organic matter.
实施实例12:Implementation example 12:
将1.88g(10mmol)离子液体[Et3NH]+BF4 -和0.62g(10mmol)硼酸及1g(10mmol)环己醇、频哪醇1.18(10mmol)放入反应瓶中,搅拌,加热,控制温度为80℃,反应2h,反应液静置,不分层,淡黄色溶液,用石油醚萃取,得到酯化产物环己醇频哪醇硼酸酯,经GC-MS定性、定量分析得到产率为72.14%。离子液体层经少量有机溶剂洗涤2-5次、加热真空干燥除水、除有机物后,可重复使用。Put 1.88g (10mmol) ionic liquid [Et 3 NH] + BF 4 - and 0.62g (10mmol) boric acid and 1g (10mmol) cyclohexanol, pinacol 1.18 (10mmol) into the reaction flask, stir, heat, Control the temperature at 80°C, react for 2 hours, let the reaction solution stand still, without stratification, light yellow solution, extract with petroleum ether, and obtain the esterification product cyclohexanol pinacol borate, which is obtained by qualitative and quantitative analysis by GC-MS The yield was 72.14%. The ionic liquid layer can be reused after being washed 2-5 times with a small amount of organic solvent, heated and vacuum-dried to remove water and organic matter.
实施实例13:Implementation example 13:
将3.73g(10mmol)离子液体[PrSPy]+pTSA-和0.62g(10mmol)硼酸及1g(10mmol)环己醇、频哪醇1.18(10mmol)放入反应瓶中,搅拌,加热,控制温度为80℃,反应2h,反应液静置,不分层,红棕色溶液,用石油醚萃取,得到酯化产物环己醇频哪醇硼酸酯,经GC-MS定性、定量分析得到产率为81.37%。离子液体层经少量有机溶剂洗涤2-5次、加热真空干燥除水、除有机物后,可重复使用。3.73g (10mmol) ionic liquid [PrSPy] + pTSA - and 0.62g (10mmol) boric acid and 1g (10mmol) cyclohexanol, pinacol 1.18 (10mmol) are put into reaction flask, stir, heating, control temperature is 80°C, reacted for 2 hours, the reaction solution was allowed to stand without stratification, and the reddish-brown solution was extracted with petroleum ether to obtain the esterification product cyclohexanol pinacol borate, which was obtained by qualitative and quantitative analysis by GC-MS. 81.37%. The ionic liquid layer can be reused after being washed 2-5 times with a small amount of organic solvent, heated and vacuum-dried to remove water and organic matter.
实施实例14:Implementation example 14:
将2.89g(10mmol)离子液体[PrSPy]+BF4 -和0.62g(10mmol)硼酸及1g(10mmol)环己醇、频哪醇1.18(10mmol)放入反应瓶中,搅拌,加热,控制温度为80℃,反应2h,反应液静置,分层,上层为棕黄色溶液,下层为澄黄色液体,通过分液分出酯化产物环己醇频哪醇硼酸酯,经GC-MS定性、定量分析得到产率为54.1%。离子液体层经少量有机溶剂洗涤2-5次、加热真空干燥除水、除有机物后,可重复使用。Put 2.89g (10mmol) ionic liquid [PrSPy] + BF 4 - and 0.62g (10mmol) boric acid and 1g (10mmol) cyclohexanol, pinacol 1.18 (10mmol) into the reaction flask, stir, heat, and control the temperature 80°C, react for 2 hours, let the reaction solution stand still, separate layers, the upper layer is a brownish yellow solution, the lower layer is an orange liquid, the esterification product cyclohexanol pinacol borate is separated by liquid separation, and it is qualitative by GC-MS , Quantitative analysis obtained a yield of 54.1%. The ionic liquid layer can be reused after being washed 2-5 times with a small amount of organic solvent, heated and vacuum-dried to remove water and organic matter.
Claims (5)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN2008101621263A CN101735254B (en) | 2008-11-12 | 2008-11-12 | A kind of synthetic method of borate |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN2008101621263A CN101735254B (en) | 2008-11-12 | 2008-11-12 | A kind of synthetic method of borate |
Publications (2)
Publication Number | Publication Date |
---|---|
CN101735254A CN101735254A (en) | 2010-06-16 |
CN101735254B true CN101735254B (en) | 2012-05-16 |
Family
ID=42459329
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN2008101621263A Expired - Fee Related CN101735254B (en) | 2008-11-12 | 2008-11-12 | A kind of synthetic method of borate |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN101735254B (en) |
Families Citing this family (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103193660B (en) * | 2013-03-30 | 2015-03-04 | 浙江工业大学 | Synthetic method of 4-alkoxy phenylamine compound |
CN103910656B (en) * | 2014-03-20 | 2016-07-06 | 浙江工业大学 | Functionalized acidic ionic liquid and preparation thereof and the application in ethyl lactate synthesizes |
CN104356152A (en) * | 2014-11-07 | 2015-02-18 | 白银摩尔化工有限责任公司 | Method for producing high-purity triisopropyl borate through system external circulation reaction dehydration |
CN104844644B (en) * | 2015-03-25 | 2017-04-19 | 中国工程物理研究院化工材料研究所 | Di-hydroxyl six-membered ring borate compound, preparation method and application thereof |
CN106111203B (en) * | 2016-06-30 | 2018-06-26 | 苏州大学 | Application of two (beta-diimine base) ytterbiums in catalysis aldehyde and borine hydroboration |
CN106188119B (en) * | 2016-06-30 | 2018-06-12 | 苏州大学 | Application of two (beta-diimine base) ytterbiums in catalysis ketone and borine hydroboration |
CN108033975A (en) * | 2017-12-27 | 2018-05-15 | 安徽金善化工科技有限公司 | A kind of preparation method of butyl borate |
CN116239626B (en) * | 2023-01-13 | 2023-09-15 | 南京工业大学 | Fluorine-modified borate ester and preparation method thereof and brake fluid containing the fluorine-modified borate ester |
CN116285040A (en) * | 2023-03-30 | 2023-06-23 | 东莞市利群榕兴高分子科技有限公司 | A kind of antistatic high-strength nitrile rubber/potassium sorbate composite material and preparation method thereof |
CN117603044B (en) * | 2023-11-24 | 2025-03-07 | 浙江大学 | Method for depolymerizing and upgrading polyester into carboxylate and borate by using ionic liquid to catalyze |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1405140A (en) * | 2002-11-07 | 2003-03-26 | 华东师范大学 | Method of esterifying in ion liquid [Hmim]+ BF4- |
CN1646540A (en) * | 2002-04-05 | 2005-07-27 | 南阿拉巴马大学 | Functionalized ionic liquids, and methods of use thereof |
-
2008
- 2008-11-12 CN CN2008101621263A patent/CN101735254B/en not_active Expired - Fee Related
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1646540A (en) * | 2002-04-05 | 2005-07-27 | 南阿拉巴马大学 | Functionalized ionic liquids, and methods of use thereof |
CN1405140A (en) * | 2002-11-07 | 2003-03-26 | 华东师范大学 | Method of esterifying in ion liquid [Hmim]+ BF4- |
Non-Patent Citations (3)
Title |
---|
Dong Fang et al.Brønsted Acidic Ionic Liquids and Their Use as Dual Solvent-Catalysts for Fischer Esterifications.《Industrial & Engineering Chemistry Research》.2006,第45卷(第24期), * |
Huabing Xing et al.Novel Brønsted-Acidic Ionic Liquids for Esterifications.《Industrial & Engineering Chemistry Research》.2005,第44卷(第11期), * |
庄丽珍等.吡咯烷酮酸性离子液体中硼酸酯的催化合成.《应用化学》.2011,第28卷(第1期), * |
Also Published As
Publication number | Publication date |
---|---|
CN101735254A (en) | 2010-06-16 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN101735254B (en) | A kind of synthetic method of borate | |
McNeice et al. | Basic ionic liquids for catalysis: the road to greater stability | |
Vafaeezadeh et al. | Brønsted acidic ionic liquids: Green catalysts for essential organic reactions | |
Wang et al. | Rare earth perfluorooctanoate [RE (PFO) 3]-catalyzed condensations of indole with carbonyl Compounds | |
Lee et al. | Microwave-assisted Kabachnik-Fields reaction in ionic liquid | |
Zhang et al. | Rh‐Catalyzed C C Cleavage of Benzyl/Allylic Alcohols to Produce Benzyl/Allylic Amines or other Alcohols by Nucleophilic Addition of Intermediate Rhodacycles to Aldehydes and Imines | |
Rohaniyan et al. | Phosphomolybdic acid supported on Schiff base functionalized graphene oxide nanosheets: Preparation, characterization, and first catalytic application in the multi‐component synthesis of tetrahydrobenzo [a] xanthene‐11‐ones | |
Khedkar et al. | CO surrogates: a green alternative in palladium-catalyzed CO gas free carbonylation reactions | |
Mohammadbagheri et al. | KCC-1/Pr-SO3H as an efficient heterogeneous catalyst for production of n-butyl levulinate from furfuryl alcohol | |
Cui et al. | Catalytic use of zinc amide for transmetalation with allylboronates: general and efficient catalytic allylation of carbonyl compounds, imines, and hydrazones | |
Zhu et al. | One-pot synthesis of 3, 4-dihydro-2 (H)-pyrimidinones catalyzed by reusable acidic choline-based ionic liquids | |
Nakayama et al. | Water‐Tolerant and Reusable Catalysts for Direct Ester Condensation between Equimolar Amounts of Carboxylic Acids and Alcohols | |
Zhang et al. | Uniform acid poly ionic liquid-based large particle and its catalytic application in esterification reaction | |
CN108409772A (en) | The method for preparing borate based on aldehyde | |
CN108558925A (en) | Application of the 2,6- diisopropyl benzene amido lithiums in catalysis ketone and borine hydroboration | |
Shakourian-Fard et al. | Synthesis of α-aminophosphonates in the presence of a magnetic recyclable Fe3O4@ SiO2-2mimSO3H nanocatalyst | |
CN109704968A (en) | A kind of method that ionic liquid catalyzes synthesis of dimethyl carbonate | |
Hosseini Monfared et al. | A heterogenized vanadium oxo-aroylhydrazone catalyst for efficient and selective oxidation of hydrocarbons with hydrogen peroxide | |
Mujahid Alam et al. | Applications of polymethylhydrosiloxane (PMHS) in organic synthesis-covering up to March 2022 | |
CN101440025A (en) | Method for preparing ethylidene ether or ketal by N-methyl glyoxaline bisulphate ion liquid catalysis | |
CN105521825A (en) | Catalyst for preparing phenol by oxidation of benzene, preparation method and application thereof | |
CN102040545A (en) | Acidic room-temperature ionic liquid using acidic functional tetraalkylguanidine as cations and preparation method thereof | |
Wu et al. | Efficient synthesis of sec-butanol from sec-butyl acetate under mild conditions with the basic ionic liquid catalysts | |
Nakamura et al. | Iron (III)–Zirconium (IV) Combined Salt Immobilized on N‐(Polystyrylbutyl) pyridinium Triflylimide as a Reusable Catalyst for a Dehydrative Esterification Reaction | |
CN102786436B (en) | A kind of method of synthesizing cyanoacetate |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C06 | Publication | ||
PB01 | Publication | ||
C10 | Entry into substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
C41 | Transfer of patent application or patent right or utility model | ||
TR01 | Transfer of patent right |
Effective date of registration: 20151218 Address after: 505 B building, No. 655, bachelor Road, Yinzhou District, Zhejiang, Ningbo 315100, China Patentee after: Ningbo Jiezhong New Materials Technology Co., Ltd. Address before: 818 School of materials science and chemical engineering, Ningbo University, Fenghua Road, Zhejiang, Ningbo 315211, China Patentee before: Ningbo University |
|
DD01 | Delivery of document by public notice |
Addressee: Ningbo Jiezhong New Materials Technology Co., Ltd. Document name: Notification to Pay the Fees |
|
DD01 | Delivery of document by public notice | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20120516 Termination date: 20191112 |
|
CF01 | Termination of patent right due to non-payment of annual fee |