CN111517984B - Method for synthesizing cyclohexanone oxime by catalyzing cyclohexanone with titanium ammonium phosphotungstate - Google Patents
Method for synthesizing cyclohexanone oxime by catalyzing cyclohexanone with titanium ammonium phosphotungstate Download PDFInfo
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- JHIVVAPYMSGYDF-UHFFFAOYSA-N cyclohexanone Chemical compound O=C1CCCCC1 JHIVVAPYMSGYDF-UHFFFAOYSA-N 0.000 title claims abstract description 140
- VEZUQRBDRNJBJY-UHFFFAOYSA-N cyclohexanone oxime Chemical compound ON=C1CCCCC1 VEZUQRBDRNJBJY-UHFFFAOYSA-N 0.000 title claims abstract description 114
- 238000000034 method Methods 0.000 title claims abstract description 18
- 230000002194 synthesizing effect Effects 0.000 title claims abstract description 6
- ZWNZGTHTOBNSDL-UHFFFAOYSA-N N.[Ti+4] Chemical compound N.[Ti+4] ZWNZGTHTOBNSDL-UHFFFAOYSA-N 0.000 title claims description 9
- 238000006243 chemical reaction Methods 0.000 claims abstract description 105
- QGZKDVFQNNGYKY-UHFFFAOYSA-O Ammonium Chemical compound [NH4+] QGZKDVFQNNGYKY-UHFFFAOYSA-O 0.000 claims abstract description 35
- 239000003054 catalyst Substances 0.000 claims abstract description 33
- MHAJPDPJQMAIIY-UHFFFAOYSA-N Hydrogen peroxide Chemical compound OO MHAJPDPJQMAIIY-UHFFFAOYSA-N 0.000 claims abstract description 32
- 239000002904 solvent Substances 0.000 claims abstract description 19
- 235000011114 ammonium hydroxide Nutrition 0.000 claims abstract description 13
- VHUUQVKOLVNVRT-UHFFFAOYSA-N Ammonium hydroxide Chemical compound [NH4+].[OH-] VHUUQVKOLVNVRT-UHFFFAOYSA-N 0.000 claims abstract description 12
- 238000003756 stirring Methods 0.000 claims abstract description 5
- 239000000463 material Substances 0.000 claims abstract description 4
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Natural products CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 claims description 7
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 7
- 239000012074 organic phase Substances 0.000 claims description 4
- 239000007788 liquid Substances 0.000 claims description 3
- 239000012071 phase Substances 0.000 claims description 3
- 239000012295 chemical reaction liquid Substances 0.000 claims description 2
- 238000001035 drying Methods 0.000 claims description 2
- 238000000605 extraction Methods 0.000 claims description 2
- 125000003944 tolyl group Chemical group 0.000 claims description 2
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical group [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 claims 1
- 239000003795 chemical substances by application Substances 0.000 claims 1
- 238000001816 cooling Methods 0.000 claims 1
- 150000003608 titanium Chemical class 0.000 abstract description 30
- 238000000926 separation method Methods 0.000 abstract description 3
- 230000007613 environmental effect Effects 0.000 abstract description 2
- 230000015572 biosynthetic process Effects 0.000 description 9
- 230000003197 catalytic effect Effects 0.000 description 9
- 238000003786 synthesis reaction Methods 0.000 description 9
- 239000000047 product Substances 0.000 description 8
- 239000000243 solution Substances 0.000 description 8
- 230000035484 reaction time Effects 0.000 description 7
- WEVYAHXRMPXWCK-UHFFFAOYSA-N Acetonitrile Chemical compound CC#N WEVYAHXRMPXWCK-UHFFFAOYSA-N 0.000 description 6
- 150000003839 salts Chemical class 0.000 description 6
- 239000011964 heteropoly acid Substances 0.000 description 5
- 238000002360 preparation method Methods 0.000 description 5
- 239000002994 raw material Substances 0.000 description 5
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 4
- DKGAVHZHDRPRBM-UHFFFAOYSA-N Tert-Butanol Chemical compound CC(C)(C)O DKGAVHZHDRPRBM-UHFFFAOYSA-N 0.000 description 4
- JBKVHLHDHHXQEQ-UHFFFAOYSA-N epsilon-caprolactam Chemical compound O=C1CCCCCN1 JBKVHLHDHHXQEQ-UHFFFAOYSA-N 0.000 description 4
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- 238000011084 recovery Methods 0.000 description 3
- 229910052708 sodium Inorganic materials 0.000 description 3
- 239000011734 sodium Substances 0.000 description 3
- BBMCTIGTTCKYKF-UHFFFAOYSA-N 1-heptanol Chemical compound CCCCCCCO BBMCTIGTTCKYKF-UHFFFAOYSA-N 0.000 description 2
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 2
- XDTMQSROBMDMFD-UHFFFAOYSA-N Cyclohexane Chemical compound C1CCCCC1 XDTMQSROBMDMFD-UHFFFAOYSA-N 0.000 description 2
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 2
- UGACIEPFGXRWCH-UHFFFAOYSA-N [Si].[Ti] Chemical compound [Si].[Ti] UGACIEPFGXRWCH-UHFFFAOYSA-N 0.000 description 2
- SFZULDYEOVSIKM-UHFFFAOYSA-N chembl321317 Chemical compound C1=CC(C(=N)NO)=CC=C1C1=CC=C(C=2C=CC(=CC=2)C(=N)NO)O1 SFZULDYEOVSIKM-UHFFFAOYSA-N 0.000 description 2
- 239000002808 molecular sieve Substances 0.000 description 2
- DCKVFVYPWDKYDN-UHFFFAOYSA-L oxygen(2-);titanium(4+);sulfate Chemical compound [O-2].[Ti+4].[O-]S([O-])(=O)=O DCKVFVYPWDKYDN-UHFFFAOYSA-L 0.000 description 2
- 239000003208 petroleum Substances 0.000 description 2
- 230000008569 process Effects 0.000 description 2
- URGAHOPLAPQHLN-UHFFFAOYSA-N sodium aluminosilicate Chemical compound [Na+].[Al+3].[O-][Si]([O-])=O.[O-][Si]([O-])=O URGAHOPLAPQHLN-UHFFFAOYSA-N 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 229920002994 synthetic fiber Polymers 0.000 description 2
- 239000012209 synthetic fiber Substances 0.000 description 2
- 229910000348 titanium sulfate Inorganic materials 0.000 description 2
- QQZOPKMRPOGIEB-UHFFFAOYSA-N 2-Oxohexane Chemical compound CCCCC(C)=O QQZOPKMRPOGIEB-UHFFFAOYSA-N 0.000 description 1
- RAXXELZNTBOGNW-UHFFFAOYSA-O Imidazolium Chemical compound C1=C[NH+]=CN1 RAXXELZNTBOGNW-UHFFFAOYSA-O 0.000 description 1
- BZUYOAAPZVNNSP-UHFFFAOYSA-N N.[Zr+4] Chemical class N.[Zr+4] BZUYOAAPZVNNSP-UHFFFAOYSA-N 0.000 description 1
- 229920002292 Nylon 6 Polymers 0.000 description 1
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 description 1
- 229910021529 ammonia Inorganic materials 0.000 description 1
- 150000003863 ammonium salts Chemical class 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000006555 catalytic reaction Methods 0.000 description 1
- 239000007795 chemical reaction product Substances 0.000 description 1
- 239000007810 chemical reaction solvent Substances 0.000 description 1
- 150000001868 cobalt Chemical class 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 150000001879 copper Chemical class 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000004817 gas chromatography Methods 0.000 description 1
- 229910010272 inorganic material Inorganic materials 0.000 description 1
- 239000007791 liquid phase Substances 0.000 description 1
- 238000011068 loading method Methods 0.000 description 1
- 230000007246 mechanism Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 150000002815 nickel Chemical class 0.000 description 1
- 231100000252 nontoxic Toxicity 0.000 description 1
- 230000003000 nontoxic effect Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 150000002923 oximes Chemical class 0.000 description 1
- IYDGMDWEHDFVQI-UHFFFAOYSA-N phosphoric acid;trioxotungsten Chemical compound O=[W](=O)=O.O=[W](=O)=O.O=[W](=O)=O.O=[W](=O)=O.O=[W](=O)=O.O=[W](=O)=O.O=[W](=O)=O.O=[W](=O)=O.O=[W](=O)=O.O=[W](=O)=O.O=[W](=O)=O.O=[W](=O)=O.OP(O)(O)=O IYDGMDWEHDFVQI-UHFFFAOYSA-N 0.000 description 1
- 239000004033 plastic Substances 0.000 description 1
- 229920003023 plastic Polymers 0.000 description 1
- 229910052700 potassium Inorganic materials 0.000 description 1
- 239000011591 potassium Substances 0.000 description 1
- JUJWROOIHBZHMG-UHFFFAOYSA-O pyridinium Chemical compound C1=CC=[NH+]C=C1 JUJWROOIHBZHMG-UHFFFAOYSA-O 0.000 description 1
- 125000001453 quaternary ammonium group Chemical group 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- 229910021332 silicide Inorganic materials 0.000 description 1
- 239000006228 supernatant Substances 0.000 description 1
- 229910052723 transition metal Inorganic materials 0.000 description 1
- 150000003624 transition metals Chemical group 0.000 description 1
- 238000005292 vacuum distillation Methods 0.000 description 1
Classifications
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- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C249/00—Preparation of compounds containing nitrogen atoms doubly-bound to a carbon skeleton
- C07C249/04—Preparation of compounds containing nitrogen atoms doubly-bound to a carbon skeleton of oximes
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J27/00—Catalysts comprising the elements or compounds of halogens, sulfur, selenium, tellurium, phosphorus or nitrogen; Catalysts comprising carbon compounds
- B01J27/14—Phosphorus; Compounds thereof
- B01J27/186—Phosphorus; Compounds thereof with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
- B01J27/188—Phosphorus; Compounds thereof with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium with chromium, molybdenum, tungsten or polonium
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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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- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
Abstract
本发明为一种由磷钨酸铵钛盐催化环己酮合成环己酮肟的方法。该方法包括以下步骤:将环己酮、氨水、过氧化氢和磷钨酸铵钛盐加入反应器中,在溶剂存在条件下或无溶剂条件下,在常压20~60℃、搅拌下反应3~7h,反应结束后待温度降至室温,得产物环己酮肟;其中,物料摩尔比为环己酮:氨水:过氧化氢:磷钨酸铵钛盐=1:0.5‑2.5:0.5‑2.5:0.1‑1;当有溶剂存在条件下时,体积比为:环己酮:溶剂=1:3~8。本发明具有高效、环保、反应条件温和和催化剂易分离等优势。The invention relates to a method for synthesizing cyclohexanone oxime from cyclohexanone catalyzed by ammonium phosphotungstate titanium salt. The method comprises the following steps: adding cyclohexanone, ammonia water, hydrogen peroxide and ammonium phosphotungstate titanium salt into the reactor, and reacting under normal pressure at 20-60°C under stirring in the presence of a solvent or without a solvent 3-7 hours, after the reaction is completed, wait until the temperature drops to room temperature to obtain the product cyclohexanone oxime; wherein, the molar ratio of the materials is cyclohexanone: ammonia water: hydrogen peroxide: ammonium phosphotungstate titanium salt = 1:0.5-2.5:0.5 ‑2.5: 0.1‑1; when there is a solvent, the volume ratio is: cyclohexanone: solvent = 1: 3 ~ 8. The invention has the advantages of high efficiency, environmental protection, mild reaction conditions, easy catalyst separation and the like.
Description
技术领域technical field
本发明涉及有机化工产品的合成,具体来说是采用一种磷钨酸铵钛盐为催化剂催化环己酮液相氨肟化合成环己酮肟的工艺方法。The invention relates to the synthesis of organic chemical products, in particular to a process for synthesizing cyclohexanone oxime by using an ammonium phosphotungstate titanium salt as a catalyst to catalyze cyclohexanone liquid-phase ammoximation.
背景技术Background technique
环己酮肟(缩写为CHO)是合成ε-己内酰胺的重要有机中间体,而己内酰胺又是重要的有机原料之一,已广泛用于合成纤维、尼龙-6、塑料和树脂等轻重工业的各个领域(李大为,合成纤维工业,2016(4):61-64)。近年来,随着环己酮肟需求的增加,研究者开始尝试采用不同的催化剂来合成环己酮肟,以期降低催化剂制备成本,优化生产工艺。Cyclohexanone oxime (abbreviated as CHO) is an important organic intermediate for the synthesis of ε-caprolactam, and caprolactam is one of the important organic raw materials. It has been widely used in various industries such as synthetic fibers, nylon-6, plastics and resins. field (Li Dawei, Synthetic Fiber Industry, 2016(4):61-64). In recent years, with the increasing demand for cyclohexanone oxime, researchers have begun to try to use different catalysts to synthesize cyclohexanone oxime in order to reduce the cost of catalyst preparation and optimize the production process.
国内外开发了一系列用于催化环己酮合成环己酮肟的催化剂,如硅化物、杂多酸、杂多化合物等。研究发现,杂多酸在催化氧化反应中显示出较高的催化活性。杂多酸具有绿色无毒、活性和选择性高等特点,但也存在活性组分易流失、反应后催化剂难以从反应体系中分离等问题。为解决上述问题采取了将杂多酸负载在多孔载体上或转变为不溶性的杂多酸盐类催化剂等方法。与负载型杂多酸相比较,杂多酸盐类催化剂易于制备,在氨肟化反应中也有广泛的应用。如磷钨酸钠盐、磷钨酸钾盐和磷钨酸铵盐(曾湘等,石油学报(石油加工),2010(5):779-784)、单过渡金属取代的磷钨酸铵锆盐、磷钨酸铵钴盐、磷钨酸铵镍盐和磷钨酸铵铜盐(刘碧玉等,分子催化,2018,28(2):140-147),以及磷钨酸季铵盐、磷钨酸吡啶盐、磷钨酸咪唑盐等一系列新型的有机无机复合杂多酸盐(曾远辉,硕士论文,湘潭大学,2010)等催化剂均能催化环己酮氨肟化合成环己酮肟。然而,上述单一型杂多酸盐类催化剂仍存在催化活性低、活性组分易流失或催化剂回收困难等缺陷。A series of catalysts for catalyzing the synthesis of cyclohexanone oxime from cyclohexanone have been developed at home and abroad, such as silicides, heteropolyacids, heteropoly compounds, etc. The study found that heteropolyacids showed high catalytic activity in catalytic oxidation reactions. Heteropolyacids have the characteristics of green, non-toxic, high activity and selectivity, but there are also problems such as easy loss of active components and difficulty in separating the catalyst from the reaction system after the reaction. In order to solve the above problems, methods such as loading the heteropolyacid on a porous carrier or converting it into an insoluble heteropolyacid salt catalyst have been adopted. Compared with supported heteropolyacids, heteropolyacid salt catalysts are easy to prepare and widely used in ammoximation reactions. Such as sodium phosphotungstate, potassium phosphotungstate and ammonium phosphotungstate (Zeng Xiang et al., Journal of Petroleum (Petroleum Processing), 2010 (5): 779-784), single transition metal substituted ammonium zirconium phosphotungstate Salt, ammonium phosphotungstate cobalt salt, ammonium phosphotungstate nickel salt and ammonium phosphotungstate copper salt (Liu Biyu et al., Molecular Catalysis, 2018, 28(2):140-147), and quaternary ammonium phosphotungstate, Pyridinium phosphotungstate, imidazolium phosphotungstate and a series of new organic-inorganic compound heteropolyacid salts (Zeng Yuanhui, master thesis, Xiangtan University, 2010) and other catalysts can catalyze the synthesis of cyclohexanone oxime from cyclohexanone ammoximide . However, the above-mentioned single-type heteropolyacid salt catalysts still have defects such as low catalytic activity, easy loss of active components, or difficulty in catalyst recovery.
因此,开发绿色、高效、稳定且易于与反应体系分离的催化剂,并将其用于环己酮氨肟化反应以及优化生产工艺,仍是本领域的研究者亟待解决的问题。Therefore, it is still an urgent problem to be solved by researchers in this field to develop a green, efficient, stable and easy-to-separate catalyst from the reaction system, and to use it in the ammoximation reaction of cyclohexanone and to optimize the production process.
发明内容Contents of the invention
本发明针对目前环己酮肟生产工艺复杂、以及使用单一型杂多酸盐类催化剂仍存在催化活性低、活性组分易流失或催化剂回收困难等问题,提供一种由磷钨酸铵钛盐催化环己酮合成环己酮肟的方法。该方法通过以环己酮为原料,首次以磷钨酸铵钛盐为催化剂,实现了温和条件下的环己酮肟的合成。本发明具有高效、环保、反应条件温和和催化剂易分离等优势。The present invention aims at the current complex production process of cyclohexanone oxime and the problems of low catalytic activity, easy loss of active components or difficulty in catalyst recovery when using a single heteropoly salt catalyst, and provides a titanium ammonium phosphotungstate The invention discloses a method for synthesizing cyclohexanone oxime from cyclohexanone. The method realizes the synthesis of cyclohexanone oxime under mild conditions by using cyclohexanone as a raw material and using ammonium phosphotungstate titanium salt as a catalyst for the first time. The invention has the advantages of high efficiency, environmental protection, mild reaction conditions, easy catalyst separation and the like.
本发明的具体技术方案如下:Concrete technical scheme of the present invention is as follows:
一种由磷钨酸铵钛盐催化环己酮合成环己酮肟的方法,该方法包括以下步骤:A method for catalyzing cyclohexanone to synthesize cyclohexanone oxime by ammonium phosphotungstate titanium salt, the method comprises the following steps:
将环己酮、氨水、过氧化氢和磷钨酸铵钛盐加入反应器中,在溶剂存在条件下或无溶剂条件下,在常压20~60℃、搅拌下反应3~7h,反应结束后待温度降至室温,得产物环己酮肟;Add cyclohexanone, ammonia water, hydrogen peroxide and ammonium phosphotungstate titanium salt into the reactor, and react under normal pressure 20-60°C under stirring for 3-7 hours in the presence of solvent or without solvent, and the reaction is completed After the temperature drops to room temperature, the product cyclohexanone oxime is obtained;
其中,物料摩尔比为环己酮:氨水:过氧化氢:磷钨酸铵钛盐=1:0.5-2.5:0.5-2.5:0.1-1;当有溶剂存在条件下时,体积比为,环己酮:溶剂=1:3~8;Among them, the material molar ratio is cyclohexanone: ammonia water: hydrogen peroxide: ammonium phosphotungstate titanium salt = 1: 0.5-2.5: 0.5-2.5: 0.1-1; when there is a solvent, the volume ratio is, ring Hexanone: solvent = 1: 3 ~ 8;
所述的溶剂具体为乙醇、乙腈、叔丁醇、环己烷或水;Described solvent is specifically ethanol, acetonitrile, tert-butanol, cyclohexane or water;
所述的方法还包括磷钨酸铵钛盐催化剂的回收,包括以下步骤:反应结束后,加入萃取剂萃取,反应液分为两层,上层为含产物环己酮肟的有机相,下层为含有磷钨酸铵钛盐相;将下层液体减压蒸馏除水、干燥后,用于下一轮反应;The method also includes the recovery of the ammonium phosphotungstate titanium salt catalyst, including the following steps: after the reaction is completed, adding an extractant for extraction, the reaction solution is divided into two layers, the upper layer is an organic phase containing the product cyclohexanone oxime, and the lower layer is an organic phase containing cyclohexanone oxime. Contains ammonium phosphotungstate titanium salt phase; the lower liquid is distilled under reduced pressure to remove water and dried for the next round of reaction;
其中,体积比为,环己酮:萃取剂=1:1~3。Wherein, the volume ratio is cyclohexanone:extractant=1:1-3.
所述的萃取剂为甲苯。The extractant is toluene.
本发明的有益效果:Beneficial effects of the present invention:
(1)该方法首次实现了将磷钨酸铵钛盐作为催化剂用于环己酮氨肟化合成环己酮肟。本发明涉及的磷钨酸铵钛盐催化剂具有较好的keggin型结构,催化性能优异,能有效催化环己酮氨肟化反应,产物环己酮肟的选择性高。(1) This method realizes for the first time that ammonium phosphotungstate titanium salt is used as a catalyst for the synthesis of cyclohexanone oxime from cyclohexanone amidoxime. The ammonium phosphotungstate titanium salt catalyst involved in the invention has a better keggin structure, excellent catalytic performance, can effectively catalyze the ammoximation reaction of cyclohexanone, and has high selectivity of the product cyclohexanone oxime.
(2)催化剂所需原料易得,价格便宜,制备过程简单,催化效率高,反应结束后,反应液分为两层,催化剂与产物易于分离,并且可以回收利用,有很好的应用前景。(2) The raw materials required for the catalyst are easy to obtain, cheap, simple in the preparation process, and high in catalytic efficiency. After the reaction, the reaction solution is divided into two layers, the catalyst and the product are easy to separate, and can be recycled, so it has a good application prospect.
(3)与现有的以环己酮为原料,以钛硅分子筛作为催化剂制备环己酮肟相比,该反应以磷钨酸铵钛盐为催化剂,反应在常压、低温20-60℃下反应3-7h即可得到目标产物环己酮肟,反应条件温和(相比将采用钛硅分子筛做催化剂的反应,温度可由80℃降至20℃),能有效避免过氧化氢的分解,进而提高过氧化氢的利用率。该方法首次实现了将磷钨酸铵钛盐作为催化剂用于环己酮氨肟化合成环己酮肟。本发明涉及的磷钨酸铵钛盐催化剂具有较好的keggin型结构,催化性能优异,能有效催化环己酮氨肟化反应,产物环己酮肟的选择性高。环己酮转化率为92.5%,环己酮肟选择性为91.0%。(3) Compared with the existing preparation of cyclohexanone oxime with cyclohexanone as raw material and titanium silicon molecular sieve as catalyst, the reaction uses ammonium phosphotungstate titanium salt as catalyst, and the reaction is carried out at normal pressure and low temperature of 20-60°C The target product cyclohexanone oxime can be obtained after 3-7 hours of reaction. The reaction conditions are mild (compared with the reaction using titanium silicon molecular sieve as catalyst, the temperature can be reduced from 80 ° C to 20 ° C), which can effectively avoid the decomposition of hydrogen peroxide. And then improve the utilization rate of hydrogen peroxide. This method realizes for the first time that ammonium phosphotungstate titanium salt is used as a catalyst for the synthesis of cyclohexanone oxime from cyclohexanone amidoxime. The ammonium phosphotungstate titanium salt catalyst involved in the invention has a better keggin structure, excellent catalytic performance, can effectively catalyze the ammoximation reaction of cyclohexanone, and has high selectivity of the product cyclohexanone oxime. The conversion rate of cyclohexanone was 92.5%, and the selectivity of cyclohexanone oxime was 91.0%.
具体实施方式Detailed ways
本发明的实质特点和显著效果可以从下述的实施例得以体现,但他们并不对本发明作任何限制,该领域的技术人员可以根据本发明的内容做出一些非本质的改进和调整。下面通过具体实施方式对本发明作进一步的说明。The essential features and remarkable effects of the present invention can be manifested from the following examples, but they do not limit the present invention in any way, and those skilled in the art can make some non-essential improvements and adjustments according to the contents of the present invention. The present invention will be further described below through specific embodiments.
本发明的反应机理为:Reaction mechanism of the present invention is:
该方法通过以环己酮为原料,以磷钨酸铵钛盐为催化剂,实现了环己酮肟的一步清洁合成。The method realizes the one-step clean synthesis of cyclohexanone oxime by using cyclohexanone as a raw material and ammonium phosphotungstate titanium salt as a catalyst.
本发明所述磷钨酸铵钛盐为公知物质,其结构简式为:(NH4)5PW11TiO39。其制备过程包括如下步骤:The ammonium phosphotungstate titanium salt described in the present invention is a known substance, and its simplified structure is: (NH 4 ) 5 PW 11 TiO 39 . Its preparation process comprises the following steps:
(1)将硫酸钛、铵盐与磷钨酸钠溶于水中形成溶液;(1) dissolving titanium sulfate, ammonium salt and sodium phosphotungstate in water to form a solution;
(2)反应后过滤、重结晶得到所述磷钨酸铵钛盐。(2) After the reaction, filter and recrystallize to obtain the ammonium phosphotungstate titanium salt.
实施例1Example 1
本发明涉及的磷钨酸铵钛盐催化剂的制备过程如下:The preparation process of the ammonium phosphotungstate titanium salt catalyst involved in the present invention is as follows:
将硫酸钛溶液(6mmol)溶解在1mL硫酸(2M)中,加入到装有6mmol的磷钨酸钠的水溶液中,并使用1mol·L-1NaHCO3溶液将pH值调至4.0–5.0。60℃下搅拌30分钟,加入0.01mol的NH4Cl继续搅拌2h后停止反应,将所得反应产物过滤,用水重结晶3次,即可得到分子式为(NH4)5PW11TiO39的磷钨酸铵钛盐。Dissolve titanium sulfate solution (6mmol) in 1mL sulfuric acid (2M), add it to the aqueous solution containing 6mmol sodium phosphotungstate, and use 1mol L -1 NaHCO 3 solution to adjust the pH value to 4.0–5.0.60 Stir at ℃ for 30 minutes, add 0.01mol of NH 4 Cl and continue stirring for 2 hours to stop the reaction, filter the obtained reaction product, and recrystallize with water for 3 times to obtain phosphotungstic acid with the molecular formula (NH 4 ) 5 PW 11 TiO 39 ammonium titanium salt.
实施例2Example 2
将环己酮(0.05mol)、磷钨酸铵钛盐(0.0125mol)、氨水(0.075mol-氨水浓度为25%)和过氧化氢(0.025mol-过氧化氢浓度为30%)加入烧瓶中,磁力搅拌、在常压、30℃下反应3小时后停止反应。反应液冷却至室温,用甲苯(5ml-15ml)萃取反应液;反应液分为两层,上层为含产物环己酮肟的有机相,下层为含有磷钨酸铵钛盐相;将下层液体减压蒸馏除水、干燥后,用于下一轮反应;取上清液以正庚醇做内标,在气相色谱上进行分析,反应结果是环己酮转化率为72.49%,环己酮肟的选择性为60.58%。Add cyclohexanone (0.05mol), ammonium phosphotungstate titanium salt (0.0125mol), ammonia water (0.075mol-the concentration of ammonia water is 25%) and hydrogen peroxide (0.025mol-the concentration of hydrogen peroxide is 30%) into the flask , magnetically stirred, reacted at normal pressure and 30° C. for 3 hours, then stopped the reaction. The reaction solution was cooled to room temperature, and the reaction solution was extracted with toluene (5ml-15ml); the reaction solution was divided into two layers, the upper layer was an organic phase containing the product cyclohexanone oxime, and the lower layer was a phase containing ammonium phosphotungstate titanium salt; the lower layer liquid After vacuum distillation to remove water and drying, it was used for the next round of reaction; the supernatant was taken as an internal standard with n-heptanol, and analyzed on gas chromatography. The reaction result was that the conversion rate of cyclohexanone was 72.49%, and the The selectivity of oxime is 60.58%.
实施例3Example 3
其它步骤同实施例2,不同之处在于反应前在体系中还加入环己酮4倍体积的溶剂乙醇,反应结果是环己酮转化率为56.39%,环己酮肟的选择性为39.53%。Other steps are the same as in Example 2, except that before the reaction, 4 times the volume of solvent ethanol of cyclohexanone is added to the system. The reaction result is that the conversion rate of cyclohexanone is 56.39%, and the selectivity of cyclohexanone oxime is 39.53%. .
实施例4Example 4
其它步骤同实施例3,不同之处在于加入的溶剂改为乙腈,反应结果是环己酮转化率为48.86%,环己酮肟的选择性为36.23%。Other steps are the same as in Example 3, except that the added solvent is changed to acetonitrile, the reaction result is that the conversion rate of cyclohexanone is 48.86%, and the selectivity of cyclohexanone oxime is 36.23%.
实施例5Example 5
其它步骤同实施例3,不同之处在于加入的溶剂改为环己烷,反应结果是环己酮转化率为43.56%,环己酮肟的选择性为34.78%。Other steps are the same as in Example 3, except that the added solvent is changed to cyclohexane, and the reaction result is that the conversion rate of cyclohexanone is 43.56%, and the selectivity of cyclohexanone oxime is 34.78%.
实施例6Example 6
其它步骤同实施例3,不同之处在于加入的溶剂改为叔丁醇,反应结果是环己酮转化率为60.35%,环己酮肟的选择性为40.26%。Other steps are the same as in Example 3, except that the added solvent is changed to tert-butanol, the reaction result is that the conversion rate of cyclohexanone is 60.35%, and the selectivity of cyclohexanone oxime is 40.26%.
实施例7Example 7
其它步骤同实施例3,不同之处在于加入的溶剂改为水,反应结果是环己酮转化率为69.29%,环己酮肟的选择性为54.86%。Other steps are the same as in Example 3, except that the added solvent is changed to water, and the reaction result is that the conversion rate of cyclohexanone is 69.29%, and the selectivity of cyclohexanone oxime is 54.86%.
实施例8Example 8
其它步骤同实施例2,不同之处在于加入的磷钨酸铵钛盐为0.005mol,反应结果是环己酮转化率为68.34%,环己酮肟的选择性为56.23%。Other steps are the same as in Example 2, except that the added ammonium phosphotungstate titanium salt is 0.005 mol, and the reaction result is that the conversion rate of cyclohexanone is 68.34%, and the selectivity of cyclohexanone oxime is 56.23%.
实施例9Example 9
其它步骤同实施例2,不同之处在于加入的磷钨酸铵钛盐为0.025mol,反应结果是环己酮转化率为78.61%,环己酮肟的选择性为72.78%。Other steps are the same as in Example 2, except that the added ammonium phosphotungstate titanium salt is 0.025 mol, and the reaction result is that the conversion rate of cyclohexanone is 78.61%, and the selectivity of cyclohexanone oxime is 72.78%.
实施例10Example 10
其它步骤同实施例2,不同之处在于加入的磷钨酸铵钛盐为0.0375mol,反应结果是环己酮转化率为78.82%,环己酮肟的选择性为73.12%。The other steps are the same as in Example 2, except that the added ammonium phosphotungstate titanium salt is 0.0375 mol, the reaction result is that the conversion rate of cyclohexanone is 78.82%, and the selectivity of cyclohexanone oxime is 73.12%.
实施例11Example 11
其它步骤同实施例2,不同之处在于加入的磷钨酸铵钛盐为0.05mol,反应结果是环己酮转化率为79.03%,环己酮肟的选择性为73.83%。The other steps are the same as in Example 2, except that the added ammonium phosphotungstate titanium salt is 0.05 mol, the reaction result is that the conversion rate of cyclohexanone is 79.03%, and the selectivity of cyclohexanone oxime is 73.83%.
实施例12Example 12
其它步骤同实施例9,不同之处在于加入的氨水为0.025mol,反应结果是环己酮转化率为62.26%,环己酮肟的选择性为46.38%。Other steps are the same as in Example 9, except that the added ammonia water is 0.025 mol, the reaction result is that the conversion rate of cyclohexanone is 62.26%, and the selectivity of cyclohexanone oxime is 46.38%.
实施例13Example 13
其它步骤同实施例9,不同之处在于加入的氨水为0.05mol,反应结果是环己酮转化率为69.31%,环己酮肟的选择性为54.23%。The other steps were the same as in Example 9, except that the amount of ammonia water added was 0.05 mol. The reaction result showed that the conversion rate of cyclohexanone was 69.31%, and the selectivity of cyclohexanone oxime was 54.23%.
实施例14Example 14
其它步骤同实施例9,不同之处在于加入的氨水为0.1mol,反应结果是环己酮转化率为73.47%,环己酮肟的选择性为64.22%。The other steps were the same as in Example 9, except that the amount of ammonia water added was 0.1 mol. The reaction result showed that the conversion rate of cyclohexanone was 73.47%, and the selectivity of cyclohexanone oxime was 64.22%.
实施例15Example 15
其它步骤同实施例9,不同之处在于加入的氨水为0.125mol,反应结果是环己酮转化率为69.92%,环己酮肟的选择性为62.24%。The other steps are the same as in Example 9, except that the amount of ammonia water added is 0.125 mol, the reaction result is that the conversion rate of cyclohexanone is 69.92%, and the selectivity of cyclohexanone oxime is 62.24%.
实施例16Example 16
其它步骤同实施例9,不同之处在于加入的过氧化氢为0.025mol,反应结果是环己酮转化率为80.35%,环己酮肟的选择性为76.28%。Other steps are the same as in Example 9, except that the added hydrogen peroxide is 0.025 mol, the reaction result is that the conversion rate of cyclohexanone is 80.35%, and the selectivity of cyclohexanone oxime is 76.28%.
实施例17Example 17
其它步骤同实施例9,不同之处在于加入的过氧化氢为0.075mol,反应结果是环己酮转化率为85.39%,环己酮肟的选择性为80.34%。Other steps are the same as in Example 9, except that the added hydrogen peroxide is 0.075 mol, the reaction result is that the conversion rate of cyclohexanone is 85.39%, and the selectivity of cyclohexanone oxime is 80.34%.
实施例18Example 18
其它步骤同实施例9,不同之处在于加入的过氧化氢为0.1mol,反应结果是环己酮转化率为80.02%,环己酮肟的选择性为78.36%。The other steps were the same as in Example 9, except that the added hydrogen peroxide was 0.1 mol, and the reaction result was that the conversion rate of cyclohexanone was 80.02%, and the selectivity of cyclohexanone oxime was 78.36%.
实施例19Example 19
其它步骤同实施例9,不同之处在于加入的过氧化氢为0.125mol,反应结果是环己酮转化率为72.03%,环己酮肟的选择性为73.32%。Other steps are the same as in Example 9, except that the added hydrogen peroxide is 0.125 mol, the reaction result is that the conversion rate of cyclohexanone is 72.03%, and the selectivity of cyclohexanone oxime is 73.32%.
实施例20Example 20
其它步骤同实施例17,不同之处在于反应温度为20℃,反应结果是环己酮转化率为75.32%,环己酮肟的选择性为63.25%。Other steps were the same as in Example 17, except that the reaction temperature was 20° C., and the reaction result was that the conversion rate of cyclohexanone was 75.32%, and the selectivity of cyclohexanone oxime was 63.25%.
实施例21Example 21
其它步骤同实施例17,不同之处在于反应温度为40℃,反应结果是环己酮转化率为83.25%,环己酮肟的选择性为79.96%。Other steps were the same as in Example 17, except that the reaction temperature was 40° C., and the reaction result was that the conversion rate of cyclohexanone was 83.25%, and the selectivity of cyclohexanone oxime was 79.96%.
实施例22Example 22
其它步骤同实施例17,不同之处在于反应温度为50℃,反应结果是环己酮转化率为73.01%,环己酮肟的选择性为68.20%。Other steps were the same as in Example 17, except that the reaction temperature was 50° C., the reaction result was that the conversion rate of cyclohexanone was 73.01%, and the selectivity of cyclohexanone oxime was 68.20%.
实施例23Example 23
其它步骤同实施例17,不同之处在于反应温度为60℃,反应结果是环己酮转化率为60.13%,环己酮肟的选择性为53.68%。Other steps are the same as in Example 17, except that the reaction temperature is 60° C., the reaction result is that the conversion rate of cyclohexanone is 60.13%, and the selectivity of cyclohexanone oxime is 53.68%.
实施例24Example 24
其它步骤同实施例17,不同之处在于反应时间为4h,反应结果是环己酮转化率为86.35%,环己酮肟的选择性为83.28%。The other steps were the same as in Example 17, except that the reaction time was 4 hours. The reaction result showed that the conversion rate of cyclohexanone was 86.35%, and the selectivity of cyclohexanone oxime was 83.28%.
实施例25Example 25
其它步骤同实施例17,不同之处在于反应时间为5h,反应结果是环己酮转化率为90.36%,环己酮肟的选择性为89.44%。The other steps were the same as in Example 17, except that the reaction time was 5 hours. The reaction result showed that the conversion rate of cyclohexanone was 90.36%, and the selectivity of cyclohexanone oxime was 89.44%.
实施例26Example 26
其它步骤同实施例17,不同之处在于反应时间为6h,反应结果是环己酮转化率为91.17%,环己酮肟的选择性为89.13%。The other steps are the same as in Example 17, except that the reaction time is 6 hours. The reaction result is that the conversion rate of cyclohexanone is 91.17%, and the selectivity of cyclohexanone oxime is 89.13%.
实施例27Example 27
其它步骤同实施例17,不同之处在于反应时间为7h,反应结果是环己酮转化率为92.5%,环己酮肟选择性为91.0%。The other steps are the same as in Example 17, except that the reaction time is 7 hours. The reaction result is that the conversion rate of cyclohexanone is 92.5%, and the selectivity of cyclohexanone oxime is 91.0%.
实施例28Example 28
其它步骤同实施例25,不同之处在于在反应液冷却至室温后,将磷钨酸铵钛盐回收,将回收的磷钨酸铵钛盐和用于催化环己酮氨肟化的新制的磷钨酸铵钛盐进行对比。环己酮的转化率和环己酮肟的选择性基本不变,说明反应结束后,磷钨酸铵钛盐仍具备keggin型结构,催化剂可以回收重复使用,从而实现了环境友好的环己酮肟合成过程。Other steps are the same as in Example 25, except that after the reaction liquid is cooled to room temperature, the ammonium phosphotungstate titanium salt is recovered, and the recovered ammonium phosphotungstate titanium salt and the newly produced Ammonium phosphotungstate titanium salt for comparison. The conversion rate of cyclohexanone and the selectivity of cyclohexanone oxime are basically unchanged, indicating that after the reaction, the ammonium phosphotungstate titanium salt still has a keggin structure, and the catalyst can be recycled and reused, thus realizing the environmentally friendly cyclohexanone Oxime synthesis process.
28个实施实例汇总表Summary table of 28 implementation examples
表1溶剂对环己酮氨肟化反应的影响The influence of table 1 solvent on cyclohexanone ammoximation reaction
Table 1 Influence ofsolvent on ammoximation ofcyclohexanoneTable 1 Influence ofsolvent on ammoximation of cyclohexanone
表2催化剂用量对环己酮氨肟化反应的影响The impact of table 2 catalyst dosage on cyclohexanone ammoximation reaction
Table2 Influence ofthe amount ofcatalyst on ammoximationofcyclohexanoneTable2 Influence of the amount of catalyst on ammoximation of cyclohexanone
表3氨水添加量对环己酮氨肟化反应的影响The influence of table 3 ammoniacal liquor addition amount on cyclohexanone ammoximation reaction
Table3 Influence ofthe addition ofammonia on ammoximationofcyclohexanoneTable 3 Influence of the addition of ammonia on ammoximation of cyclohexanone
表4过氧化氢添加量对环己酮氨肟化反应的影响The influence of table 4 hydrogen peroxide addition amount on cyclohexanone ammoximation reaction
Table4 Influence ofthe addition ofhydrogen peroxide on ammoximationofcyclohexanoneTable4 Influence of the addition of hydrogen peroxide on ammoximation of cyclohexanone
表5反应温度对环己酮氨肟化反应的影响The influence of table 5 reaction temperature on cyclohexanone ammoximation reaction
Table 5Influence ofthe reaction temperature on ammoximationofcyclohexanoneTable 5Influence of the reaction temperature on ammoximation of cyclohexanone
表6反应时间对环己酮氨肟化反应的影响The impact of table 6 reaction time on cyclohexanone ammoximation reaction
Table 6Influence ofthe reaction time on ammoximation ofcyclohexanoneTable 6Influence of the reaction time on ammoximation of cyclohexanone
从实施例可以看出,磷钨酸铵钛盐作催化剂催化环己酮氨肟化反应具有较高的催化活性,物料比例、反应温度、反应时间等反应条件对于环己酮氨肟化反应有较大的影响,适宜的反应条件能够明显提高环己酮肟的收率。此外,对于反应溶剂而言,在无溶剂条件下的催化效果更好,同时,无溶剂时避免了溶剂的使用及后续分离,节约成本。As can be seen from the examples, the ammonium phosphotungstate titanium salt has higher catalytic activity as a catalyst to catalyze the ammoximation reaction of cyclohexanone, and the reaction conditions such as material ratio, reaction temperature, and reaction time have certain effects on the ammoximation reaction of cyclohexanone. Larger impact, suitable reaction conditions can significantly improve the yield of cyclohexanone oxime. In addition, for the reaction solvent, the catalytic effect is better under the condition of no solvent, and at the same time, the use of solvent and subsequent separation are avoided when there is no solvent, which saves cost.
本发明未尽事宜为公知技术。应当理解,本发明虽然已通过以上实施例进行了清楚说明,然而在不背离本发明精神及其实质的情况下,所属技术领域的技术人员当可根据本发明作出各种相应的变化和修正,但这些相应的变化和修正都应属于本发明的权利要求的保护范围。Matters not covered in the present invention are known technologies. It should be understood that although the present invention has been clearly described through the above embodiments, those skilled in the art can make various corresponding changes and modifications according to the present invention without departing from the spirit and essence of the present invention. But these corresponding changes and amendments should all belong to the protection scope of the claims of the present invention.
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