CN108821941A - Method for preparing cyclopentanol or cyclopentanone by catalytic conversion of biomass - Google Patents
Method for preparing cyclopentanol or cyclopentanone by catalytic conversion of biomass Download PDFInfo
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- CN108821941A CN108821941A CN201810794182.2A CN201810794182A CN108821941A CN 108821941 A CN108821941 A CN 108821941A CN 201810794182 A CN201810794182 A CN 201810794182A CN 108821941 A CN108821941 A CN 108821941A
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- 238000006243 chemical reaction Methods 0.000 title claims abstract description 251
- BGTOWKSIORTVQH-UHFFFAOYSA-N cyclopentanone Chemical compound O=C1CCCC1 BGTOWKSIORTVQH-UHFFFAOYSA-N 0.000 title claims abstract description 112
- XCIXKGXIYUWCLL-UHFFFAOYSA-N cyclopentanol Chemical compound OC1CCCC1 XCIXKGXIYUWCLL-UHFFFAOYSA-N 0.000 title claims abstract description 60
- 238000000034 method Methods 0.000 title claims abstract description 17
- 239000002028 Biomass Substances 0.000 title claims abstract description 7
- 230000003197 catalytic effect Effects 0.000 title claims abstract description 4
- HYBBIBNJHNGZAN-UHFFFAOYSA-N furfural Chemical compound O=CC1=CC=CO1 HYBBIBNJHNGZAN-UHFFFAOYSA-N 0.000 claims abstract description 278
- XPFVYQJUAUNWIW-UHFFFAOYSA-N furfuryl alcohol Chemical compound OCC1=CC=CO1 XPFVYQJUAUNWIW-UHFFFAOYSA-N 0.000 claims abstract description 162
- 239000003054 catalyst Substances 0.000 claims abstract description 95
- 239000001257 hydrogen Substances 0.000 claims abstract description 87
- 229910052739 hydrogen Inorganic materials 0.000 claims abstract description 87
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 55
- 239000008367 deionised water Substances 0.000 claims abstract description 51
- 229910021641 deionized water Inorganic materials 0.000 claims abstract description 51
- 239000002904 solvent Substances 0.000 claims abstract description 12
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims description 45
- 150000002431 hydrogen Chemical class 0.000 claims description 41
- 150000001875 compounds Chemical class 0.000 claims description 2
- 230000035484 reaction time Effects 0.000 claims description 2
- 238000005984 hydrogenation reaction Methods 0.000 abstract description 5
- 238000002360 preparation method Methods 0.000 abstract description 3
- 125000004435 hydrogen atom Chemical class [H]* 0.000 abstract 1
- XEKOWRVHYACXOJ-UHFFFAOYSA-N Ethyl acetate Chemical compound CCOC(C)=O XEKOWRVHYACXOJ-UHFFFAOYSA-N 0.000 description 117
- 238000010438 heat treatment Methods 0.000 description 91
- 239000010949 copper Substances 0.000 description 46
- 239000011777 magnesium Substances 0.000 description 43
- 238000009903 catalytic hydrogenation reaction Methods 0.000 description 40
- 238000004817 gas chromatography Methods 0.000 description 39
- 239000000243 solution Substances 0.000 description 12
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 9
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 6
- MFUVDXOKPBAHMC-UHFFFAOYSA-N magnesium;dinitrate;hexahydrate Chemical compound O.O.O.O.O.O.[Mg+2].[O-][N+]([O-])=O.[O-][N+]([O-])=O MFUVDXOKPBAHMC-UHFFFAOYSA-N 0.000 description 6
- 238000004519 manufacturing process Methods 0.000 description 6
- 239000012298 atmosphere Substances 0.000 description 5
- 239000002994 raw material Substances 0.000 description 5
- 239000000126 substance Substances 0.000 description 5
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 description 4
- XNDZQQSKSQTQQD-UHFFFAOYSA-N 3-methylcyclohex-2-en-1-ol Chemical compound CC1=CC(O)CCC1 XNDZQQSKSQTQQD-UHFFFAOYSA-N 0.000 description 3
- 239000007864 aqueous solution Substances 0.000 description 3
- 238000001816 cooling Methods 0.000 description 3
- SXTLQDJHRPXDSB-UHFFFAOYSA-N copper;dinitrate;trihydrate Chemical compound O.O.O.[Cu+2].[O-][N+]([O-])=O.[O-][N+]([O-])=O SXTLQDJHRPXDSB-UHFFFAOYSA-N 0.000 description 3
- 239000012153 distilled water Substances 0.000 description 3
- 239000003814 drug Substances 0.000 description 3
- 239000003205 fragrance Substances 0.000 description 3
- 239000011259 mixed solution Substances 0.000 description 3
- 239000012299 nitrogen atmosphere Substances 0.000 description 3
- 239000012041 precatalyst Substances 0.000 description 3
- 229910000029 sodium carbonate Inorganic materials 0.000 description 3
- 238000003756 stirring Methods 0.000 description 3
- VQKFNUFAXTZWDK-UHFFFAOYSA-N 2-Methylfuran Chemical compound CC1=CC=CO1 VQKFNUFAXTZWDK-UHFFFAOYSA-N 0.000 description 2
- SRBFZHDQGSBBOR-IOVATXLUSA-N D-xylopyranose Chemical compound O[C@@H]1COC(O)[C@H](O)[C@H]1O SRBFZHDQGSBBOR-IOVATXLUSA-N 0.000 description 2
- WNLRTRBMVRJNCN-UHFFFAOYSA-N adipic acid Chemical compound OC(=O)CCCCC(O)=O WNLRTRBMVRJNCN-UHFFFAOYSA-N 0.000 description 2
- LPIQUOYDBNQMRZ-UHFFFAOYSA-N cyclopentene Chemical compound C1CC=CC1 LPIQUOYDBNQMRZ-UHFFFAOYSA-N 0.000 description 2
- 230000018044 dehydration Effects 0.000 description 2
- 238000006297 dehydration reaction Methods 0.000 description 2
- 229940079593 drug Drugs 0.000 description 2
- 239000012847 fine chemical Substances 0.000 description 2
- 239000000446 fuel Substances 0.000 description 2
- 238000011084 recovery Methods 0.000 description 2
- 238000004064 recycling Methods 0.000 description 2
- PMJHHCWVYXUKFD-SNAWJCMRSA-N (E)-1,3-pentadiene Chemical compound C\C=C\C=C PMJHHCWVYXUKFD-SNAWJCMRSA-N 0.000 description 1
- 229940043375 1,5-pentanediol Drugs 0.000 description 1
- JWUJQDFVADABEY-UHFFFAOYSA-N 2-methyltetrahydrofuran Chemical compound CC1CCCO1 JWUJQDFVADABEY-UHFFFAOYSA-N 0.000 description 1
- 241000609240 Ambelania acida Species 0.000 description 1
- 229920002488 Hemicellulose Polymers 0.000 description 1
- 239000001361 adipic acid Substances 0.000 description 1
- 235000011037 adipic acid Nutrition 0.000 description 1
- PYMYPHUHKUWMLA-UHFFFAOYSA-N arabinose Natural products OCC(O)C(O)C(O)C=O PYMYPHUHKUWMLA-UHFFFAOYSA-N 0.000 description 1
- 239000010905 bagasse Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- SRBFZHDQGSBBOR-UHFFFAOYSA-N beta-D-Pyranose-Lyxose Natural products OC1COC(O)C(O)C1O SRBFZHDQGSBBOR-UHFFFAOYSA-N 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 238000000975 co-precipitation Methods 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 239000000975 dye Substances 0.000 description 1
- 239000002803 fossil fuel Substances 0.000 description 1
- 239000004009 herbicide Substances 0.000 description 1
- 239000010903 husk Substances 0.000 description 1
- 239000011261 inert gas Substances 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- RGSFGYAAUTVSQA-UHFFFAOYSA-N pentamethylene Natural products C1CCCC1 RGSFGYAAUTVSQA-UHFFFAOYSA-N 0.000 description 1
- WCVRQHFDJLLWFE-UHFFFAOYSA-N pentane-1,2-diol Chemical compound CCCC(O)CO WCVRQHFDJLLWFE-UHFFFAOYSA-N 0.000 description 1
- -1 pentose sugars Chemical class 0.000 description 1
- 239000000575 pesticide Substances 0.000 description 1
- 238000000197 pyrolysis Methods 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- 239000005060 rubber Substances 0.000 description 1
- 239000010902 straw Substances 0.000 description 1
- 235000000346 sugar Nutrition 0.000 description 1
- 238000001308 synthesis method Methods 0.000 description 1
- 238000003786 synthesis reaction Methods 0.000 description 1
- BSYVTEYKTMYBMK-UHFFFAOYSA-N tetrahydrofurfuryl alcohol Chemical compound OCC1CCCO1 BSYVTEYKTMYBMK-UHFFFAOYSA-N 0.000 description 1
Classifications
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- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C29/00—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring
- C07C29/132—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of an oxygen containing functional group
- C07C29/136—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of an oxygen containing functional group of >C=O containing groups, e.g. —COOH
- C07C29/14—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of an oxygen containing functional group of >C=O containing groups, e.g. —COOH of a —CHO group
- C07C29/141—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of an oxygen containing functional group of >C=O containing groups, e.g. —COOH of a —CHO group with hydrogen or hydrogen-containing gases
-
- 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
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
- B01J23/72—Copper
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- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C29/00—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring
- C07C29/132—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of an oxygen containing functional group
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C45/00—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds
- C07C45/56—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds from heterocyclic compounds
- C07C45/57—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds from heterocyclic compounds with oxygen as the only heteroatom
- C07C45/59—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds from heterocyclic compounds with oxygen as the only heteroatom in five-membered rings
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- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C2601/00—Systems containing only non-condensed rings
- C07C2601/06—Systems containing only non-condensed rings with a five-membered ring
- C07C2601/08—Systems containing only non-condensed rings with a five-membered ring the ring being saturated
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- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
- Catalysts (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
Description
技术领域technical field
本发明涉及一种催化转化生物质制备环戊醇或环戊酮的方法。The invention relates to a method for catalytically converting biomass to prepare cyclopentanol or cyclopentanone.
背景技术Background technique
环戊醇是一种重要的精细化学中间体,被广泛用于医药、染料和香料的生产,同时也是药物和香料的溶剂。工业上通常用环戊酮加氢来制备环戊醇。Cyclopentanol is an important fine chemical intermediate, which is widely used in the production of medicine, dyes and fragrances, and is also a solvent for drugs and fragrances. In industry, cyclopentanol is usually prepared by hydrogenation of cyclopentanone.
环戊酮是一种多功能的精细化工原料。它可以用于合成药物,杀虫剂,橡胶化学品,除草剂和香料。环戊酮可以很容易地溶解各种树脂,因此被广泛用作电子行业的溶剂。传统的环戊酮合成方法是己二酸及其衍生物的热解和环戊烯的氧化。反应条件苛刻,过程繁琐。目前,环戊酮需求量很大,但仍然依赖化石基原料制备。Cyclopentanone is a multifunctional fine chemical raw material. It can be used in the synthesis of drugs, pesticides, rubber chemicals, herbicides and fragrances. Cyclopentanone can easily dissolve various resins, so it is widely used as a solvent in the electronics industry. The traditional synthesis methods of cyclopentanone are pyrolysis of adipic acid and its derivatives and oxidation of cyclopentene. The reaction conditions are harsh and the process is cumbersome. Currently, cyclopentanone is in great demand, but still relies on fossil-based raw materials for its production.
随着全球化石燃料的减少,对替代能源的需求迅速增长。利用可再生生物质生产化学品对于未来化学工业的可持续发展具有重要意义。糠醛是木糖的酸催化脱水产物,木糖是半纤维素的主要组分。在工业中,糠醛由富含戊聚糖的农业原料生产,如秸秆,玉米芯,燕麦壳,甘蔗渣等。糠醛的催化氢化反应是一个重要的反应,它可以获得糠醇,四氢呋喃甲醇,2-甲基呋喃,2-甲基四氢呋喃,戊二烯,戊二醇等。As the world's fossil fuels decline, the need for alternative energy sources is growing rapidly. The production of chemicals from renewable biomass is of great significance for the sustainable development of the chemical industry in the future. Furfural is the acid-catalyzed dehydration product of xylose, a major component of hemicellulose. In industry, furfural is produced from pentosan-rich agricultural raw materials, such as straw, corncobs, oat husks, bagasse, etc. The catalytic hydrogenation of furfural is an important reaction, which can obtain furfuryl alcohol, tetrahydrofuran methanol, 2-methylfuran, 2-methyltetrahydrofuran, pentadiene, pentylene glycol, etc.
糠醛是在水中进行戊糖的酸催化脱水的产物。从形成的水溶液中分离糠醛的过程增加了其生产成本。使用糠醛水溶液作为制备化学品和燃料的原料将显着降低糠醛生产成本。因此,用去离子水作为溶剂,催化糠醛或糠醇高度选择性加氢制备环戊醇或环戊酮的工艺方法,有很好的工业应用前景。Furfural is the product of the acid-catalyzed dehydration of pentose sugars in water. The process of separating furfural from the aqueous solution formed increases the cost of its production. The use of furfural aqueous solution as a raw material for the preparation of chemicals and fuels will significantly reduce furfural production costs. Therefore, using deionized water as a solvent to catalyze the highly selective hydrogenation of furfural or furfuryl alcohol to prepare cyclopentanol or cyclopentanone has a good industrial application prospect.
发明内容Contents of the invention
本发明提供一种催化转化生物质制备环戊醇或环戊酮的方法。通过控制反应条件催化糠醛或糠醇高度选择性加氢制备环戊醇或环戊酮。催化效果好,易于回收重复使用,有很好的工业应用前景。The invention provides a method for catalytically converting biomass to prepare cyclopentanol or cyclopentanone. Catalyzing highly selective hydrogenation of furfural or furfuryl alcohol to prepare cyclopentanol or cyclopentanone by controlling reaction conditions. The catalytic effect is good, it is easy to recycle and reuse, and has a good industrial application prospect.
本发明的技术方案为:一种催化转化生物质制备环戊醇或环戊酮的方法,其特征在于,使用含Cu催化剂,用去离子水作溶剂,在高压釜中加入糠醛或糠醇,充入氢气,在一定的反应温度下反应得到产物环戊醇或环戊酮。停止加热后冷却至室温,检测糠醛或糠醇的转化率和环戊醇或环戊酮的选择性。The technical scheme of the present invention is: a method for catalytically converting biomass to prepare cyclopentanol or cyclopentanone, which is characterized in that, using a Cu-containing catalyst, using deionized water as a solvent, adding furfural or furfuryl alcohol in an autoclave, fully Into hydrogen, react at a certain reaction temperature to obtain product cyclopentanol or cyclopentanone. Cool to room temperature after stopping heating, and detect the conversion rate of furfural or furfuryl alcohol and the selectivity of cyclopentanol or cyclopentanone.
优选上述的含Cu催化剂是CuxMgyAl2不同摩尔比的化合物,其中x/y=0.07-0.25,(x+y)/2=3。含Cu催化剂用常规方法制备,即先通过共沉淀法制备,然后通过在惰性气体氛围下煅烧,最后在氢气氛围下还原制得。Preferably, the above-mentioned Cu-containing catalyst is a compound of different molar ratios of Cu x Mg y Al 2 , wherein x/y=0.07-0.25, (x+y)/2=3. The Cu-containing catalyst is prepared by a conventional method, that is, it is firstly prepared by co-precipitation, then calcined in an inert gas atmosphere, and finally reduced in a hydrogen atmosphere.
优选催化剂的用量为糠醛或糠醇质量的10%-30%。优选去离子水的质量为糠醛或糠醇质量的1.6-20倍。Preferably, the catalyst is used in an amount of 10%-30% of the mass of furfural or furfuryl alcohol. Preferably, the quality of deionized water is 1.6-20 times that of furfural or furfuryl alcohol.
优选氢气的用量为0.2MPa-4.0MPa。优选反应温度为160-200℃;反应时间为3-21h。Preferably, the amount of hydrogen used is 0.2MPa-4.0MPa. The preferred reaction temperature is 160-200°C; the reaction time is 3-21h.
有益效果:Beneficial effect:
本发明提供的催化剂所用的制备方法简单,通过控制反应条件催化糠醛或糠醇高度选择性加氢制备环戊醇或环戊酮。使用糠醛水溶液作为制备化学品和燃料的原料,能显着降低糠醛生产成本。有很好的工业应用前景。The preparation method of the catalyst provided by the invention is simple, and the highly selective hydrogenation of furfural or furfuryl alcohol is catalyzed to prepare cyclopentanol or cyclopentanone by controlling the reaction conditions. Using furfural aqueous solution as a raw material for preparing chemicals and fuels can significantly reduce furfural production costs. It has a good industrial application prospect.
具体实施方式Detailed ways
实施案例1:Implementation case 1:
称取0.9664g三水合硝酸铜,14.3590g六水合硝酸镁,7.503g九水合硝酸铝于圆底烧瓶中,400ml去离子水作为溶剂将其溶解,记为溶液A。称取10.5990g碳酸钠,13.3333g氢氧化钠于圆底烧瓶中,400ml去离子水作为溶剂将其溶解,记为溶液B。在室温搅拌下将溶液A缓慢加入到溶液B中,2小时滴完。将混合溶液在110℃下环流处理12小时。过滤并用蒸馏水洗涤至PH为7。然后在真空干燥箱中80℃真空干燥12小时,得到的预催化剂于氮气氛围下在管式炉中煅烧到温度为300℃,升温速率为5℃/min,在该温度下保持4h。然后在氢气氛围下在管式炉中煅烧到温度为300℃,升温速率为5℃/min,在该温度下保持2h。自然降温到室温后得到催化剂Cu0.4Mg5.6Al2。Weigh 0.9664g of copper nitrate trihydrate, 14.3590g of magnesium nitrate hexahydrate, and 7.503g of aluminum nitrate nonahydrate into a round bottom flask, and dissolve them in 400ml of deionized water as a solvent, which is designated as solution A. Weigh 10.5990g of sodium carbonate, 13.3333g of sodium hydroxide in a round bottom flask, and dissolve it in 400ml of deionized water as a solvent, which is designated as solution B. The solution A was slowly added to the solution B under stirring at room temperature, and the drop was completed in 2 hours. The mixed solution was circulated at 110° C. for 12 hours. Filter and wash to pH 7 with distilled water. Then vacuum-dried at 80°C in a vacuum oven for 12 hours, and the obtained precatalyst was calcined in a tube furnace under a nitrogen atmosphere to a temperature of 300°C with a heating rate of 5°C/min, and kept at this temperature for 4h. Then it was calcined in a tube furnace under a hydrogen atmosphere to a temperature of 300 °C with a heating rate of 5 °C/min and kept at this temperature for 2 h. The catalyst Cu 0.4 Mg 5.6 Al 2 was obtained after natural cooling to room temperature.
实施案例2:Implementation case 2:
称取1.9328g三水合硝酸铜,13.3333六水合硝酸镁,7.503g九水合硝酸铝于圆底烧瓶中,400ml去离子水作为溶剂将其溶解,记为溶液A。称取10.5990g碳酸钠,13.3333g氢氧化钠于圆底烧瓶中,400ml去离子水作为溶剂将其溶解,记为溶液B。在室温搅拌下将溶液A缓慢加入到溶液B中,2小时滴完。将混合溶液在110℃下环流处理12小时。过滤并用蒸馏水洗涤至PH为7。然后在真空干燥箱中80℃真空干燥12小时,得到的预催化剂于氮气氛围下在管式炉中煅烧到温度为300℃,升温速率为5℃/min,在该温度下保持4h。然后在氢气氛围下在管式炉中煅烧到温度为300℃,升温速率为5℃/min,在该温度下保持2h。自然降温到室温后得到催化剂Cu0.8Mg5.2Al2。Weigh 1.9328g of copper nitrate trihydrate, 13.3333g of magnesium nitrate hexahydrate, and 7.503g of aluminum nitrate nonahydrate in a round bottom flask, and dissolve them in 400ml of deionized water as a solvent, which is recorded as solution A. Weigh 10.5990g of sodium carbonate, 13.3333g of sodium hydroxide in a round bottom flask, and dissolve it in 400ml of deionized water as a solvent, which is designated as solution B. The solution A was slowly added to the solution B under stirring at room temperature, and the drop was completed in 2 hours. The mixed solution was circulated at 110° C. for 12 hours. Filter and wash to pH 7 with distilled water. Then vacuum-dried at 80°C in a vacuum oven for 12 hours, and the obtained precatalyst was calcined in a tube furnace under a nitrogen atmosphere to a temperature of 300°C with a heating rate of 5°C/min, and kept at this temperature for 4h. Then it was calcined in a tube furnace under a hydrogen atmosphere to a temperature of 300 °C with a heating rate of 5 °C/min and kept at this temperature for 2 h. The catalyst Cu 0.8 Mg 5.2 Al 2 was obtained after natural cooling to room temperature.
实施案例3:Implementation case 3:
称取2.8992g三水合硝酸铜,12.3077g六水合硝酸镁,7.503g九水合硝酸铝于圆底烧瓶中,400ml去离子水作为溶剂将其溶解,记为溶液A。称取10.5990g碳酸钠,13.3333g氢氧化钠于圆底烧瓶中,400ml去离子水作为溶剂将其溶解,记为溶液B。在室温搅拌下将溶液A缓慢加入到溶液B中,2小时滴完。将混合溶液在110℃下环流处理12小时。过滤并用蒸馏水洗涤至PH为7。然后在真空干燥箱中80℃真空干燥12小时,得到的预催化剂于氮气氛围下在管式炉中煅烧到温度为300℃,升温速率为5℃/min,在该温度下保持4h。然后在氢气氛围下在管式炉中煅烧到温度为300℃,升温速率为5℃/min,在该温度下保持2h。自然降温到室温后得到催化剂Cu1.2Mg4.8Al2。Weigh 2.8992g of copper nitrate trihydrate, 12.3077g of magnesium nitrate hexahydrate, and 7.503g of aluminum nitrate nonahydrate in a round bottom flask, and dissolve them in 400ml of deionized water as a solvent, which is recorded as solution A. Weigh 10.5990g of sodium carbonate, 13.3333g of sodium hydroxide in a round bottom flask, and dissolve it in 400ml of deionized water as a solvent, which is designated as solution B. The solution A was slowly added to the solution B under stirring at room temperature, and the drop was completed in 2 hours. The mixed solution was circulated at 110° C. for 12 hours. Filter and wash to pH 7 with distilled water. Then vacuum-dried at 80°C in a vacuum oven for 12 hours, and the obtained precatalyst was calcined in a tube furnace under a nitrogen atmosphere to a temperature of 300°C with a heating rate of 5°C/min, and kept at this temperature for 4h. Then it was calcined in a tube furnace under a hydrogen atmosphere to a temperature of 300 °C with a heating rate of 5 °C/min and kept at this temperature for 2 h. The catalyst Cu 1.2 Mg 4.8 Al 2 was obtained after natural cooling to room temperature.
实施案例4:催化糠醛或糠醇加氢制备环戊醇Example 4: Catalytic hydrogenation of furfural or furfuryl alcohol to prepare cyclopentanol
在反应釜中,加入0.1000g糠醛,2.0000g去离子水和催化剂Cu0.4Mg5.6Al2,且催化剂的量为20.0mg,密封反应釜。用氢气置换反应釜内的空气,置换3次后,充入2.0MPa氢气。置于190℃的加热套中加热反应12h,待反应结束后,从加热套中取出反应釜置于室温下降温到室温,用乙酸乙酯萃取,气相色谱检测糠醛的转化率和环戊醇的选择性。反应结果见表1中的实施案例4所示。In the reaction kettle, add 0.1000g furfural, 2.0000g deionized water and catalyst Cu 0.4 Mg 5.6 Al 2 , and the amount of the catalyst is 20.0mg, and seal the reaction kettle. Replace the air in the reactor with hydrogen, and after replacing it 3 times, fill it with 2.0MPa hydrogen. Place it in a heating mantle at 190°C and heat it for 12 hours. After the reaction is over, take out the reaction kettle from the heating mantle and let it cool down to room temperature, extract with ethyl acetate, and detect the conversion rate of furfural and cyclopentanol by gas chromatography. selective. The reaction results are shown in Example 4 in Table 1.
实施案例5:催化糠醛或糠醇加氢制备环戊醇Example 5: Catalytic hydrogenation of furfural or furfuryl alcohol to prepare cyclopentanol
在反应釜中,加入0.1000g糠醛,2.0000g去离子水和催化剂Cu0.8Mg5.2Al2,且催化剂的量为20.0mg,密封反应釜。用氢气置换反应釜内的空气,置换3次后,充入2.0MPa氢气。置于190℃的加热套中加热反应12h,待反应结束后,从加热套中取出反应釜置于室温下降温到室温,用乙酸乙酯萃取,气相色谱检测糠醛的转化率和环戊醇的选择性。反应结果见表1中的实施案例5所示。In the reaction kettle, add 0.1000g furfural, 2.0000g deionized water and catalyst Cu 0.8 Mg 5.2 Al 2 , and the amount of catalyst is 20.0mg, and seal the reaction kettle. Replace the air in the reactor with hydrogen, and after replacing it 3 times, fill it with 2.0MPa hydrogen. Place it in a heating mantle at 190°C and heat it for 12 hours. After the reaction is over, take out the reaction kettle from the heating mantle and let it cool down to room temperature, extract with ethyl acetate, and detect the conversion rate of furfural and cyclopentanol by gas chromatography. selective. The reaction results are shown in Example 5 in Table 1.
实施案例6:催化糠醛或糠醇加氢制备环戊醇Example 6: Catalytic hydrogenation of furfural or furfuryl alcohol to prepare cyclopentanol
在反应釜中,加入0.1000g糠醛,2.0000g去离子水和催化剂Cu1.2Mg4.8Al2,且催化剂的量为20.0mg,密封反应釜。用氢气置换反应釜内的空气,置换3次后,充入2.0MPa氢气。置于190℃的加热套中加热反应12h,待反应结束后,从加热套中取出反应釜置于室温下降温到室温,用乙酸乙酯萃取,气相色谱检测糠醛的转化率和环戊醇的选择性。反应结果见表1中的实施案例6所示。In the reaction kettle, add 0.1000g furfural, 2.0000g deionized water and catalyst Cu 1.2 Mg 4.8 Al 2 , and the amount of the catalyst is 20.0mg, and seal the reaction kettle. Replace the air in the reactor with hydrogen, and after replacing it 3 times, fill it with 2.0MPa hydrogen. Place it in a heating mantle at 190°C and heat it for 12 hours. After the reaction is over, take out the reaction kettle from the heating mantle and let it cool down to room temperature, extract with ethyl acetate, and detect the conversion rate of furfural and cyclopentanol by gas chromatography. selective. The reaction results are shown in Example 6 in Table 1.
实施案例7:催化糠醛或糠醇加氢制备环戊醇Example 7: Catalytic hydrogenation of furfural or furfuryl alcohol to prepare cyclopentanol
在反应釜中,加入0.1000g糠醇,2.0000g去离子水和催化剂Cu0.4Mg5.6Al2,且催化剂的量为20.0mg,密封反应釜。用氢气置换反应釜内的空气,置换3次后,充入2.0MPa氢气。置于190℃的加热套中加热反应12h,待反应结束后,从加热套中取出反应釜置于室温下降温到室温,用乙酸乙酯萃取,气相色谱检测糠醛的转化率和环戊醇的选择性。反应结果见表1中的实施案例7所示。In the reactor, add 0.1000g furfuryl alcohol, 2.0000g deionized water and catalyst Cu 0.4 Mg 5.6 Al 2 , and the amount of catalyst is 20.0mg, and seal the reactor. Replace the air in the reactor with hydrogen, and after replacing it 3 times, fill it with 2.0MPa hydrogen. Place it in a heating mantle at 190°C and heat it for 12 hours. After the reaction is over, take out the reaction kettle from the heating mantle and let it cool down to room temperature, extract with ethyl acetate, and detect the conversion rate of furfural and cyclopentanol by gas chromatography. selective. The reaction results are shown in Example 7 in Table 1.
实施案例8:催化糠醛或糠醇加氢制备环戊醇Example 8: Catalytic hydrogenation of furfural or furfuryl alcohol to prepare cyclopentanol
在反应釜中,加入0.1000g糠醛,2.0000g去离子水和催化剂Cu0.4Mg5.6Al2,且催化剂的量为10.0mg,密封反应釜。用氢气置换反应釜内的空气,置换3次后,充入2.0MPa氢气。置于190℃的加热套中加热反应12h,待反应结束后,从加热套中取出反应釜置于室温下降温到室温,用乙酸乙酯萃取,气相色谱检测糠醛的转化率和环戊醇的选择性。反应结果见表1中的实施案例8所示。In the reaction kettle, add 0.1000g furfural, 2.0000g deionized water and catalyst Cu 0.4 Mg 5.6 Al 2 , and the amount of the catalyst is 10.0mg, and seal the reaction kettle. Replace the air in the reactor with hydrogen, and after replacing it 3 times, fill it with 2.0MPa hydrogen. Place it in a heating mantle at 190°C and heat it for 12 hours. After the reaction is over, take out the reaction kettle from the heating mantle and let it cool down to room temperature, extract with ethyl acetate, and detect the conversion rate of furfural and cyclopentanol by gas chromatography. selective. The reaction results are shown in Example 8 in Table 1.
实施案例9:催化糠醛或糠醇加氢制备环戊醇Example 9: Catalytic hydrogenation of furfural or furfuryl alcohol to prepare cyclopentanol
在反应釜中,加入0.1000g糠醛,2.0000g去离子水和催化剂Cu0.4Mg5.6Al2,且催化剂的量为15.0mg,密封反应釜。用氢气置换反应釜内的空气,置换3次后,充入2.0MPa氢气。置于190℃的加热套中加热反应12h,待反应结束后,从加热套中取出反应釜置于室温下降温到室温,用乙酸乙酯萃取,气相色谱检测糠醛的转化率和环戊醇的选择性。反应结果见表1中的实施案例9所示。In the reaction kettle, add 0.1000g furfural, 2.0000g deionized water and catalyst Cu 0.4 Mg 5.6 Al 2 , and the amount of the catalyst is 15.0mg, and seal the reaction kettle. Replace the air in the reactor with hydrogen, and after replacing it 3 times, fill it with 2.0MPa hydrogen. Place it in a heating mantle at 190°C and heat it for 12 hours. After the reaction is over, take out the reaction kettle from the heating mantle and let it cool down to room temperature, extract with ethyl acetate, and detect the conversion rate of furfural and cyclopentanol by gas chromatography. selective. The reaction results are shown in Example 9 in Table 1.
实施案例10:催化糠醛或糠醇加氢制备环戊醇Example 10: Catalytic hydrogenation of furfural or furfuryl alcohol to prepare cyclopentanol
在反应釜中,加入0.1000g糠醛,2.0000g去离子水和催化剂Cu0.4Mg5.6Al2,且催化剂的量为25.0mg,密封反应釜。用氢气置换反应釜内的空气,置换3次后,充入2.0MPa氢气。置于190℃的加热套中加热反应12h,待反应结束后,从加热套中取出反应釜置于室温下降温到室温,用乙酸乙酯萃取,气相色谱检测糠醛的转化率和环戊醇的选择性。反应结果见表1中的实施案例10所示。In the reaction kettle, add 0.1000g furfural, 2.0000g deionized water and catalyst Cu 0.4 Mg 5.6 Al 2 , and the amount of the catalyst is 25.0mg, and seal the reaction kettle. Replace the air in the reactor with hydrogen, and after replacing it 3 times, fill it with 2.0MPa hydrogen. Place it in a heating mantle at 190°C and heat it for 12 hours. After the reaction is over, take out the reaction kettle from the heating mantle and let it cool down to room temperature, extract with ethyl acetate, and detect the conversion rate of furfural and cyclopentanol by gas chromatography. selective. The reaction results are shown in Example 10 in Table 1.
实施案例11:催化糠醛或糠醇加氢制备环戊醇Example 11: Catalytic hydrogenation of furfural or furfuryl alcohol to prepare cyclopentanol
在反应釜中,加入0.1000g糠醛,2.0000g去离子水和催化剂Cu0.4Mg5.6Al2,且催化剂的量为30.0mg,密封反应釜。用氢气置换反应釜内的空气,置换3次后,充入2.0MPa氢气。置于190℃的加热套中加热反应12h,待反应结束后,从加热套中取出反应釜置于室温下降温到室温,用乙酸乙酯萃取,气相色谱检测糠醛的转化率和环戊醇的选择性。反应结果见表1中的实施案例11所示。In the reaction kettle, add 0.1000g furfural, 2.0000g deionized water and catalyst Cu 0.4 Mg 5.6 Al 2 , and the amount of the catalyst is 30.0mg, and seal the reaction kettle. Replace the air in the reactor with hydrogen, and after replacing it 3 times, fill it with 2.0MPa hydrogen. Place it in a heating mantle at 190°C and heat it for 12 hours. After the reaction is over, take out the reaction kettle from the heating mantle and let it cool down to room temperature, extract with ethyl acetate, and detect the conversion rate of furfural and cyclopentanol by gas chromatography. selective. The reaction results are shown in Example 11 in Table 1.
实施案例12:催化糠醛或糠醇加氢制备环戊醇Example 12: Catalytic hydrogenation of furfural or furfuryl alcohol to prepare cyclopentanol
在反应釜中,加入0.1000g糠醛,2.0000g去离子水和催化剂Cu0.4Mg5.6Al2,且催化剂的量为20.0mg,密封反应釜。用氢气置换反应釜内的空气,置换3次后,充入2.0MPa氢气。置于170℃的加热套中加热反应12h,待反应结束后,从加热套中取出反应釜置于室温下降温到室温,用乙酸乙酯萃取,气相色谱检测糠醛的转化率和环戊醇的选择性。反应结果见表1中的实施案例12所示。In the reaction kettle, add 0.1000g furfural, 2.0000g deionized water and catalyst Cu 0.4 Mg 5.6 Al 2 , and the amount of the catalyst is 20.0mg, and seal the reaction kettle. Replace the air in the reactor with hydrogen, and after replacing it 3 times, fill it with 2.0MPa hydrogen. Place it in a heating mantle at 170°C and heat it for 12 hours. After the reaction is over, take out the reaction kettle from the heating mantle and let it cool down to room temperature, extract with ethyl acetate, and detect the conversion rate of furfural and cyclopentanol by gas chromatography. selective. The reaction results are shown in Example 12 in Table 1.
实施案例13:催化糠醛或糠醇加氢制备环戊醇Example 13: Catalytic hydrogenation of furfural or furfuryl alcohol to prepare cyclopentanol
在反应釜中,加入0.1000g糠醛,2.0000g去离子水和催化剂Cu0.4Mg5.6Al2,且催化剂的量为20.0mg,密封反应釜。用氢气置换反应釜内的空气,置换3次后,充入2.0MPa氢气。置于180℃的加热套中加热反应12h,待反应结束后,从加热套中取出反应釜置于室温下降温到室温,用乙酸乙酯萃取,气相色谱检测糠醛的转化率和环戊醇的选择性。反应结果见表1中的实施案例13所示。In the reaction kettle, add 0.1000g furfural, 2.0000g deionized water and catalyst Cu 0.4 Mg 5.6 Al 2 , and the amount of the catalyst is 20.0mg, and seal the reaction kettle. Replace the air in the reactor with hydrogen, and after replacing it 3 times, fill it with 2.0MPa hydrogen. Place it in a heating mantle at 180°C and heat it for 12 hours. After the reaction is over, take out the reaction kettle from the heating mantle and let it cool down to room temperature, extract with ethyl acetate, and detect the conversion rate of furfural and cyclopentanol by gas chromatography. selective. The reaction results are shown in Example 13 in Table 1.
实施案例14:催化糠醛或糠醇加氢制备环戊醇Example 14: Catalytic hydrogenation of furfural or furfuryl alcohol to prepare cyclopentanol
在反应釜中,加入0.1000g糠醛,2.0000g去离子水和催化剂Cu0.4Mg5.6Al2,且催化剂的量为20.0mg,密封反应釜。用氢气置换反应釜内的空气,置换3次后,充入2.0MPa氢气。置于200℃的加热套中加热反应12h,待反应结束后,从加热套中取出反应釜置于室温下降温到室温,用乙酸乙酯萃取,气相色谱检测糠醛的转化率和环戊醇的选择性。反应结果见表1中的实施案例14所示。In the reaction kettle, add 0.1000g furfural, 2.0000g deionized water and catalyst Cu 0.4 Mg 5.6 Al 2 , and the amount of the catalyst is 20.0mg, and seal the reaction kettle. Replace the air in the reactor with hydrogen, and after replacing it 3 times, fill it with 2.0MPa hydrogen. Place it in a heating mantle at 200°C and heat it for 12 hours. After the reaction is over, take out the reaction kettle from the heating mantle and let it cool down to room temperature, extract with ethyl acetate, and detect the conversion rate of furfural and cyclopentanol by gas chromatography. selective. The reaction results are shown in Example 14 in Table 1.
实施案例15:催化糠醛或糠醇加氢制备环戊醇Example 15: Catalytic hydrogenation of furfural or furfuryl alcohol to prepare cyclopentanol
在反应釜中,加入0.1000g糠醛,2.0000g去离子水和催化剂Cu0.4Mg5.6Al2,且催化剂的量为20.0mg,密封反应釜。用氢气置换反应釜内的空气,置换3次后,充入2.0MPa氢气。置于190℃的加热套中加热反应9h,待反应结束后,从加热套中取出反应釜置于室温下降温到室温,用乙酸乙酯萃取,气相色谱检测糠醛的转化率和环戊醇的选择性。反应结果见表1中的实施案例15所示。In the reaction kettle, add 0.1000g furfural, 2.0000g deionized water and catalyst Cu 0.4 Mg 5.6 Al 2 , and the amount of the catalyst is 20.0mg, and seal the reaction kettle. Replace the air in the reactor with hydrogen, and after replacing it 3 times, fill it with 2.0MPa hydrogen. Place it in a heating mantle at 190°C and heat it for 9 hours. After the reaction is over, take out the reaction kettle from the heating mantle and let it cool down to room temperature, extract with ethyl acetate, and detect the conversion rate of furfural and cyclopentanol by gas chromatography. selective. The reaction results are shown in Example 15 in Table 1.
实施案例16:催化糠醛或糠醇加氢制备环戊醇Example 16: Catalytic hydrogenation of furfural or furfuryl alcohol to prepare cyclopentanol
在反应釜中,加入0.1000g糠醛,2.0000g去离子水和催化剂Cu0.4Mg5.6Al2,且催化剂的量为20.0mg,密封反应釜。用氢气置换反应釜内的空气,置换3次后,充入2.0MPa氢气。置于190℃的加热套中加热反应10h,待反应结束后,从加热套中取出反应釜置于室温下降温到室温,用乙酸乙酯萃取,气相色谱检测糠醛的转化率和环戊醇的选择性。反应结果见表1中的实施案例16所示。In the reaction kettle, add 0.1000g furfural, 2.0000g deionized water and catalyst Cu 0.4 Mg 5.6 Al 2 , and the amount of the catalyst is 20.0mg, and seal the reaction kettle. Replace the air in the reactor with hydrogen, and after replacing it 3 times, fill it with 2.0MPa hydrogen. Place it in a heating mantle at 190°C and heat it for 10 hours. After the reaction is over, take out the reaction kettle from the heating mantle and let it cool down to room temperature, extract with ethyl acetate, and detect the conversion rate of furfural and cyclopentanol by gas chromatography. selective. The reaction results are shown in Example 16 in Table 1.
实施案例17:催化糠醛或糠醇加氢制备环戊醇Example 17: Catalytic hydrogenation of furfural or furfuryl alcohol to prepare cyclopentanol
在反应釜中,加入0.1000g糠醛,2.0000g去离子水和催化剂Cu0.4Mg5.6Al2,且催化剂的量为20.0mg,密封反应釜。用氢气置换反应釜内的空气,置换3次后,充入2.0MPa氢气。置于190℃的加热套中加热反应11h,待反应结束后,从加热套中取出反应釜置于室温下降温到室温,用乙酸乙酯萃取,气相色谱检测糠醛的转化率和环戊醇的选择性。反应结果见表1中的实施案例17所示。In the reaction kettle, add 0.1000g furfural, 2.0000g deionized water and catalyst Cu 0.4 Mg 5.6 Al 2 , and the amount of the catalyst is 20.0mg, and seal the reaction kettle. Replace the air in the reactor with hydrogen, and after replacing it 3 times, fill it with 2.0MPa hydrogen. Place it in a heating mantle at 190°C for a heating reaction for 11 hours. After the reaction is over, take out the reaction kettle from the heating mantle and let it cool down to room temperature, extract with ethyl acetate, and detect the conversion rate of furfural and cyclopentanol by gas chromatography. selective. The reaction results are shown in Example 17 in Table 1.
实施案例18:催化糠醛或糠醇加氢制备环戊醇Example 18: Catalytic hydrogenation of furfural or furfuryl alcohol to prepare cyclopentanol
在反应釜中,加入0.1000g糠醛,2.0000g去离子水和催化剂Cu0.4Mg5.6Al2,且催化剂的量为20.0mg,密封反应釜。用氢气置换反应釜内的空气,置换3次后,充入2.0MPa氢气。置于190℃的加热套中加热反应13h,待反应结束后,从加热套中取出反应釜置于室温下降温到室温,用乙酸乙酯萃取,气相色谱检测糠醛的转化率和环戊醇的选择性。反应结果见表1中的实施案例18所示。In the reaction kettle, add 0.1000g furfural, 2.0000g deionized water and catalyst Cu 0.4 Mg 5.6 Al 2 , and the amount of the catalyst is 20.0mg, and seal the reaction kettle. Replace the air in the reactor with hydrogen, and after replacing it 3 times, fill it with 2.0MPa hydrogen. Place it in a heating mantle at 190°C and heat it for 13 hours. After the reaction is over, take out the reaction kettle from the heating mantle and let it cool down to room temperature, extract with ethyl acetate, and detect the conversion rate of furfural and cyclopentanol by gas chromatography. selective. The reaction results are shown in Example 18 in Table 1.
实施案例19:催化糠醛或糠醇加氢制备环戊醇Example 19: Catalytic hydrogenation of furfural or furfuryl alcohol to prepare cyclopentanol
在反应釜中,加入0.1000g糠醛,2.0000g去离子水和催化剂Cu0.4Mg5.6Al2,且催化剂的量为20.0mg,密封反应釜。用氢气置换反应釜内的空气,置换3次后,充入1.0MPa氢气。置于190℃的加热套中加热反应12h,待反应结束后,从加热套中取出反应釜置于室温下降温到室温,用乙酸乙酯萃取,气相色谱检测糠醛的转化率和环戊醇的选择性。反应结果见表1中的实施案例19所示。In the reaction kettle, add 0.1000g furfural, 2.0000g deionized water and catalyst Cu 0.4 Mg 5.6 Al 2 , and the amount of the catalyst is 20.0mg, and seal the reaction kettle. Replace the air in the reactor with hydrogen, and after replacing it 3 times, fill it with 1.0MPa hydrogen. Place it in a heating mantle at 190°C and heat it for 12 hours. After the reaction is over, take out the reaction kettle from the heating mantle and let it cool down to room temperature, extract with ethyl acetate, and detect the conversion rate of furfural and cyclopentanol by gas chromatography. selective. The reaction results are shown in Example 19 in Table 1.
实施案例20:催化糠醛或糠醇加氢制备环戊醇Example 20: Catalytic hydrogenation of furfural or furfuryl alcohol to prepare cyclopentanol
在反应釜中,加入0.1000g糠醛,2.0000g去离子水和催化剂Cu0.4Mg5.6Al2,且催化剂的量为20.0mg,密封反应釜。用氢气置换反应釜内的空气,置换3次后,充入1.5MPa氢气。置于190℃的加热套中加热反应12h,待反应结束后,从加热套中取出反应釜置于室温下降温到室温,用乙酸乙酯萃取,气相色谱检测糠醛的转化率和环戊醇的选择性。反应结果见表1中的实施案例20所示。In the reaction kettle, add 0.1000g furfural, 2.0000g deionized water and catalyst Cu 0.4 Mg 5.6 Al 2 , and the amount of the catalyst is 20.0mg, and seal the reaction kettle. Replace the air in the reactor with hydrogen, and after replacing it 3 times, fill it with 1.5MPa hydrogen. Place it in a heating mantle at 190°C and heat it for 12 hours. After the reaction is over, take out the reaction kettle from the heating mantle and let it cool down to room temperature, extract with ethyl acetate, and detect the conversion rate of furfural and cyclopentanol by gas chromatography. selective. The reaction results are shown in Example 20 in Table 1.
实施案例21:催化糠醛或糠醇加氢制备环戊醇Example 21: Catalytic hydrogenation of furfural or furfuryl alcohol to prepare cyclopentanol
在反应釜中,加入0.1000g糠醛,2.0000g去离子水和催化剂Cu0.4Mg5.6Al2,且催化剂的量为20.0mg,密封反应釜。用氢气置换反应釜内的空气,置换3次后,充入2.5MPa氢气。置于190℃的加热套中加热反应12h,待反应结束后,从加热套中取出反应釜置于室温下降温到室温,用乙酸乙酯萃取,气相色谱检测糠醛的转化率和环戊醇的选择性。反应结果见表1中的实施案例21所示。In the reaction kettle, add 0.1000g furfural, 2.0000g deionized water and catalyst Cu 0.4 Mg 5.6 Al 2 , and the amount of the catalyst is 20.0mg, and seal the reaction kettle. Replace the air in the reactor with hydrogen, and after replacing it 3 times, fill it with 2.5MPa hydrogen. Place it in a heating mantle at 190°C and heat it for 12 hours. After the reaction is over, take out the reaction kettle from the heating mantle and let it cool down to room temperature, extract with ethyl acetate, and detect the conversion rate of furfural and cyclopentanol by gas chromatography. selective. The reaction results are shown in Example 21 in Table 1.
实施案例22:催化糠醛或糠醇加氢制备环戊醇Example 22: Catalytic hydrogenation of furfural or furfuryl alcohol to prepare cyclopentanol
在反应釜中,加入0.2000g糠醛,2.0000g去离子水和催化剂Cu0.4Mg5.6Al2,且催化剂的量为40.0mg,密封反应釜。用氢气置换反应釜内的空气,置换3次后,充入2.5MPa氢气。置于190℃的加热套中加热反应13h,待反应结束后,从加热套中取出反应釜置于室温下降温到室温,用乙酸乙酯萃取,气相色谱检测糠醛的转化率和环戊醇的选择性。反应结果见表1中的实施案例22所示。In the reaction kettle, add 0.2000g furfural, 2.0000g deionized water and catalyst Cu 0.4 Mg 5.6 Al 2 , and the amount of the catalyst is 40.0mg, and seal the reaction kettle. Replace the air in the reactor with hydrogen, and after replacing it 3 times, fill it with 2.5MPa hydrogen. Place it in a heating mantle at 190°C and heat it for 13 hours. After the reaction is over, take out the reaction kettle from the heating mantle and let it cool down to room temperature, extract with ethyl acetate, and detect the conversion rate of furfural and cyclopentanol by gas chromatography. selective. The reaction results are shown in Example 22 in Table 1.
实施案例23:催化糠醛或糠醇加氢制备环戊醇Example 23: Catalytic hydrogenation of furfural or furfuryl alcohol to prepare cyclopentanol
在反应釜中,加入0.5000g糠醛,2.0000g去离子水和催化剂Cu0.4Mg5.6Al2,且催化剂的量为100.0mg,密封反应釜。用氢气置换反应釜内的空气,置换3次后,充入3.0MPa氢气。置于190℃的加热套中加热反应18h,待反应结束后,从加热套中取出反应釜置于室温下降温到室温,用乙酸乙酯萃取,气相色谱检测糠醛的转化率和环戊醇的选择性。反应结果见表1中的实施案例23所示。In the reaction kettle, add 0.5000g furfural, 2.0000g deionized water and catalyst Cu 0.4 Mg 5.6 Al 2 , and the amount of the catalyst is 100.0mg, and seal the reaction kettle. Replace the air in the reactor with hydrogen, and after replacing it 3 times, fill it with 3.0MPa hydrogen. Place it in a heating mantle at 190°C and heat it for 18 hours. After the reaction is over, take out the reaction kettle from the heating mantle and let it cool down to room temperature, extract with ethyl acetate, and detect the conversion rate of furfural and cyclopentanol by gas chromatography. selective. The reaction results are shown in Example 23 in Table 1.
实施案例24:催化糠醛或糠醇加氢制备环戊醇Example 24: Catalytic hydrogenation of furfural or furfuryl alcohol to prepare cyclopentanol
在反应釜中,加入1.2500g糠醛,2.0000g去离子水和催化剂Cu0.4Mg5.6Al2,且催化剂的量为250.0mg,密封反应釜。用氢气置换反应釜内的空气,置换3次后,充入4.0MPa氢气。置于190℃的加热套中加热反应21h,待反应结束后,从加热套中取出反应釜置于室温下降温到室温,用乙酸乙酯萃取,气相色谱检测糠醛的转化率和环戊醇的选择性。反应结果见表1中的实施案例24所示。In the reactor, add 1.2500g furfural, 2.0000g deionized water and catalyst Cu 0.4 Mg 5.6 Al 2 , and the amount of catalyst is 250.0mg, and seal the reactor. Replace the air in the reactor with hydrogen, and after replacing it 3 times, fill it with 4.0MPa hydrogen. Place it in a heating mantle at 190°C and heat it for 21 hours. After the reaction is over, take out the reaction kettle from the heating mantle and let it cool down to room temperature, extract with ethyl acetate, and detect the conversion rate of furfural and cyclopentanol by gas chromatography. selective. The reaction results are shown in Example 24 in Table 1.
实施案例25:催化糠醛或糠醇加氢制备环戊酮Example 25: Catalytic hydrogenation of furfural or furfuryl alcohol to prepare cyclopentanone
在反应釜中,加入0.1000g糠醛,2.0000g去离子水和催化剂Cu0.4Mg5.6Al2,且催化剂的量为20.0mg,密封反应釜。用氢气置换反应釜内的空气,置换3次后,充入0.2MPa氢气。置于180℃的加热套中加热反应5h,待反应结束后,从加热套中取出反应釜置于室温下降温到室温,用乙酸乙酯萃取,气相色谱检测糠醛的转化率和环戊酮的选择性。反应结果见表2中的实施案例25所示。In the reaction kettle, add 0.1000g furfural, 2.0000g deionized water and catalyst Cu 0.4 Mg 5.6 Al 2 , and the amount of the catalyst is 20.0mg, and seal the reaction kettle. Replace the air in the reactor with hydrogen, and after replacing it 3 times, fill it with 0.2MPa hydrogen. Place it in a heating mantle at 180°C and heat it for 5 hours. After the reaction is over, take out the reaction kettle from the heating mantle and let it cool down to room temperature, extract with ethyl acetate, and detect the conversion rate of furfural and cyclopentanone by gas chromatography. selective. The reaction results are shown in Example 25 in Table 2.
实施案例26:催化糠醛或糠醇加氢制备环戊酮Example 26: Catalytic hydrogenation of furfural or furfuryl alcohol to prepare cyclopentanone
在反应釜中,加入0.1000g糠醛,2.0000g去离子水和催化剂Cu0.8Mg5.2Al2,且催化剂的量为20.0mg,密封反应釜。用氢气置换反应釜内的空气,置换3次后,充入0.2MPa氢气。置于180℃的加热套中加热反应5h,待反应结束后,从加热套中取出反应釜置于室温下降温到室温,用乙酸乙酯萃取,气相色谱检测糠醛的转化率和环戊酮的选择性。反应结果见表2中的实施案例26所示。In the reaction kettle, add 0.1000g furfural, 2.0000g deionized water and catalyst Cu 0.8 Mg 5.2 Al 2 , and the amount of catalyst is 20.0mg, and seal the reaction kettle. Replace the air in the reactor with hydrogen, and after replacing it 3 times, fill it with 0.2MPa hydrogen. Place it in a heating mantle at 180°C and heat it for 5 hours. After the reaction is over, take out the reaction kettle from the heating mantle and let it cool down to room temperature, extract with ethyl acetate, and detect the conversion rate of furfural and cyclopentanone by gas chromatography. selective. The reaction results are shown in Example 26 in Table 2.
实施案例27:催化糠醛或糠醇加氢制备环戊酮Example 27: Catalytic hydrogenation of furfural or furfuryl alcohol to prepare cyclopentanone
在反应釜中,加入0.1000g糠醛,2.0000g去离子水和催化剂Cu1.2Mg4.8Al2,且催化剂的量为20.0mg,密封反应釜。用氢气置换反应釜内的空气,置换3次后,充入0.2MPa氢气。置于180℃的加热套中加热反应5h,待反应结束后,从加热套中取出反应釜置于室温下降温到室温,用乙酸乙酯萃取,气相色谱检测糠醛的转化率和环戊酮的选择性。反应结果见表2中的实施案例27所示。In the reaction kettle, add 0.1000g furfural, 2.0000g deionized water and catalyst Cu 1.2 Mg 4.8 Al 2 , and the amount of the catalyst is 20.0mg, and seal the reaction kettle. Replace the air in the reactor with hydrogen, and after replacing it 3 times, fill it with 0.2MPa hydrogen. Place it in a heating mantle at 180°C and heat it for 5 hours. After the reaction is over, take out the reaction kettle from the heating mantle and let it cool down to room temperature, extract with ethyl acetate, and detect the conversion rate of furfural and cyclopentanone by gas chromatography. selective. The reaction results are shown in Example 27 in Table 2.
实施案例28:催化糠醛或糠醇加氢制备环戊酮Example 28: Catalytic hydrogenation of furfural or furfuryl alcohol to prepare cyclopentanone
在反应釜中,加入0.1000g糠醇,2.0000g去离子水和催化剂Cu0.4Mg5.6Al2,且催化剂的量为20.0mg,密封反应釜。用氢气置换反应釜内的空气,置换3次后,充入0.2MPa氢气。置于180℃的加热套中加热反应4h,待反应结束后,从加热套中取出反应釜置于室温下降温到室温,用乙酸乙酯萃取,气相色谱检测糠醛的转化率和环戊酮的选择性。反应结果见表2中的实施案例28所示。In the reactor, add 0.1000g furfuryl alcohol, 2.0000g deionized water and catalyst Cu 0.4 Mg 5.6 Al 2 , and the amount of catalyst is 20.0mg, and seal the reactor. Replace the air in the reactor with hydrogen, and after replacing it 3 times, fill it with 0.2MPa hydrogen. Place it in a heating mantle at 180°C for a heating reaction for 4 hours. After the reaction is over, take out the reaction kettle from the heating mantle and let it cool down to room temperature, extract with ethyl acetate, and detect the conversion rate of furfural and cyclopentanone by gas chromatography. selective. The reaction results are shown in Example 28 in Table 2.
实施案例29:催化糠醛或糠醇加氢制备环戊酮Example 29: Catalytic hydrogenation of furfural or furfuryl alcohol to prepare cyclopentanone
在反应釜中,加入0.1000g糠醛,2.0000g去离子水和催化剂Cu0.4Mg5.6Al2,且催化剂的量为10.0mg,密封反应釜。用氢气置换反应釜内的空气,置换3次后,充入0.2MPa氢气。置于180℃的加热套中加热反应5h,待反应结束后,从加热套中取出反应釜置于室温下降温到室温,用乙酸乙酯萃取,气相色谱检测糠醛的转化率和环戊酮的选择性。反应结果见表2中的实施案例29所示。In the reaction kettle, add 0.1000g furfural, 2.0000g deionized water and catalyst Cu 0.4 Mg 5.6 Al 2 , and the amount of the catalyst is 10.0mg, and seal the reaction kettle. Replace the air in the reactor with hydrogen, and after replacing it 3 times, fill it with 0.2MPa hydrogen. Place it in a heating mantle at 180°C and heat it for 5 hours. After the reaction is over, take out the reaction kettle from the heating mantle and let it cool down to room temperature, extract with ethyl acetate, and detect the conversion rate of furfural and cyclopentanone by gas chromatography. selective. The reaction results are shown in Example 29 in Table 2.
实施案例30:催化糠醛或糠醇加氢制备环戊酮Example 30: Catalytic hydrogenation of furfural or furfuryl alcohol to prepare cyclopentanone
在反应釜中,加入0.1000g糠醛,2.0000g去离子水和催化剂Cu0.4Mg5.6Al2,且催化剂的量为15.0mg,密封反应釜。用氢气置换反应釜内的空气,置换3次后,充入0.2MPa氢气。置于180℃的加热套中加热反应5h,待反应结束后,从加热套中取出反应釜置于室温下降温到室温,用乙酸乙酯萃取,气相色谱检测糠醛的转化率和环戊酮的选择性。反应结果见表2中的实施案例30所示。In the reaction kettle, add 0.1000g furfural, 2.0000g deionized water and catalyst Cu 0.4 Mg 5.6 Al 2 , and the amount of the catalyst is 15.0mg, and seal the reaction kettle. Replace the air in the reactor with hydrogen, and after replacing it 3 times, fill it with 0.2MPa hydrogen. Place it in a heating mantle at 180°C and heat it for 5 hours. After the reaction is over, take out the reaction kettle from the heating mantle and let it cool down to room temperature, extract with ethyl acetate, and detect the conversion rate of furfural and cyclopentanone by gas chromatography. selective. The reaction results are shown in Example 30 in Table 2.
实施案例31:催化糠醛或糠醇加氢制备环戊酮Example 31: Catalytic hydrogenation of furfural or furfuryl alcohol to prepare cyclopentanone
在反应釜中,加入0.1000g糠醛,2.0000g去离子水和催化剂Cu0.4Mg5.6Al2,且催化剂的量为25.0mg,密封反应釜。用氢气置换反应釜内的空气,置换3次后,充入0.2MPa氢气。置于180℃的加热套中加热反应5h,待反应结束后,从加热套中取出反应釜置于室温下降温到室温,用乙酸乙酯萃取,气相色谱检测糠醛的转化率和环戊酮的选择性。反应结果见表2中的实施案例31所示。In the reaction kettle, add 0.1000g furfural, 2.0000g deionized water and catalyst Cu 0.4 Mg 5.6 Al 2 , and the amount of the catalyst is 25.0mg, and seal the reaction kettle. Replace the air in the reactor with hydrogen, and after replacing it 3 times, fill it with 0.2MPa hydrogen. Place it in a heating mantle at 180°C and heat it for 5 hours. After the reaction is over, take out the reaction kettle from the heating mantle and let it cool down to room temperature, extract with ethyl acetate, and detect the conversion rate of furfural and cyclopentanone by gas chromatography. selective. The reaction results are shown in Example 31 in Table 2.
实施案例32:催化糠醛或糠醇加氢制备环戊酮Example 32: Catalytic hydrogenation of furfural or furfuryl alcohol to prepare cyclopentanone
在反应釜中,加入0.1000g糠醛,2.0000g去离子水和催化剂Cu0.4Mg5.6Al2,且催化剂的量为30.0mg,密封反应釜。用氢气置换反应釜内的空气,置换3次后,充入0.2MPa氢气。置于180℃的加热套中加热反应5h,待反应结束后,从加热套中取出反应釜置于室温下降温到室温,用乙酸乙酯萃取,气相色谱检测糠醛的转化率和环戊酮的选择性。反应结果见表2中的实施案例32所示。In the reaction kettle, add 0.1000g furfural, 2.0000g deionized water and catalyst Cu 0.4 Mg 5.6 Al 2 , and the amount of the catalyst is 30.0mg, and seal the reaction kettle. Replace the air in the reactor with hydrogen, and after replacing it 3 times, fill it with 0.2MPa hydrogen. Place it in a heating mantle at 180°C and heat it for 5 hours. After the reaction is over, take out the reaction kettle from the heating mantle and let it cool down to room temperature, extract with ethyl acetate, and detect the conversion rate of furfural and cyclopentanone by gas chromatography. selective. The reaction results are shown in Example 32 in Table 2.
实施案例33:催化糠醛或糠醇加氢制备环戊酮Example 33: Catalytic hydrogenation of furfural or furfuryl alcohol to prepare cyclopentanone
在反应釜中,加入0.1000g糠醛,2.0000g去离子水和催化剂Cu0.4Mg5.6Al2,且催化剂的量为20.0mg,密封反应釜。用氢气置换反应釜内的空气,置换3次后,充入0.2MPa氢气。置于160℃的加热套中加热反应5h,待反应结束后,从加热套中取出反应釜置于室温下降温到室温,用乙酸乙酯萃取,气相色谱检测糠醛的转化率和环戊酮的选择性。反应结果见表2中的实施案例33所示。In the reaction kettle, add 0.1000g furfural, 2.0000g deionized water and catalyst Cu 0.4 Mg 5.6 Al 2 , and the amount of the catalyst is 20.0mg, and seal the reaction kettle. Replace the air in the reactor with hydrogen, and after replacing it 3 times, fill it with 0.2MPa hydrogen. Place it in a heating mantle at 160°C for a heating reaction for 5 hours. After the reaction is over, take out the reaction kettle from the heating mantle and place it at room temperature to lower the temperature to room temperature, extract with ethyl acetate, and detect the conversion rate of furfural and cyclopentanone by gas chromatography. selective. The reaction results are shown in Example 33 in Table 2.
实施案例34:催化糠醛或糠醇加氢制备环戊酮Example 34: Catalytic hydrogenation of furfural or furfuryl alcohol to prepare cyclopentanone
在反应釜中,加入0.1000g糠醛,2.0000g去离子水和催化剂Cu0.4Mg5.6Al2,且催化剂的量为20.0mg,密封反应釜。用氢气置换反应釜内的空气,置换3次后,充入0.2MPa氢气。置于170℃的加热套中加热反应5h,待反应结束后,从加热套中取出反应釜置于室温下降温到室温,用乙酸乙酯萃取,气相色谱检测糠醛的转化率和环戊酮的选择性。反应结果见表2中的实施案例34所示。In the reaction kettle, add 0.1000g furfural, 2.0000g deionized water and catalyst Cu 0.4 Mg 5.6 Al 2 , and the amount of the catalyst is 20.0mg, and seal the reaction kettle. Replace the air in the reactor with hydrogen, and after replacing it 3 times, fill it with 0.2MPa hydrogen. Place it in a heating mantle at 170°C and heat it for 5 hours. After the reaction is over, take out the reaction kettle from the heating mantle and let it cool down to room temperature, extract with ethyl acetate, and detect the conversion rate of furfural and cyclopentanone by gas chromatography. selective. The reaction results are shown in Example 34 in Table 2.
实施案例35:催化糠醛或糠醇加氢制备环戊酮Example 35: Catalytic hydrogenation of furfural or furfuryl alcohol to prepare cyclopentanone
在反应釜中,加入0.1000g糠醛,2.0000g去离子水和催化剂Cu0.4Mg5.6Al2,且催化剂的量为20.0mg,密封反应釜。用氢气置换反应釜内的空气,置换3次后,充入0.2MPa氢气。置于190℃的加热套中加热反应5h,待反应结束后,从加热套中取出反应釜置于室温下降温到室温,用乙酸乙酯萃取,气相色谱检测糠醛的转化率和环戊酮的选择性。反应结果见表2中的实施案例35所示。In the reaction kettle, add 0.1000g furfural, 2.0000g deionized water and catalyst Cu 0.4 Mg 5.6 Al 2 , and the amount of the catalyst is 20.0mg, and seal the reaction kettle. Replace the air in the reactor with hydrogen, and after replacing it 3 times, fill it with 0.2MPa hydrogen. Place it in a heating mantle at 190°C for a heating reaction for 5 hours. After the reaction is over, take out the reaction kettle from the heating mantle and place it at room temperature to lower the temperature to room temperature, extract with ethyl acetate, and detect the conversion rate of furfural and cyclopentanone by gas chromatography. selective. The reaction results are shown in Example 35 in Table 2.
实施案例36:催化糠醛或糠醇加氢制备环戊酮Example 36: Catalytic hydrogenation of furfural or furfuryl alcohol to prepare cyclopentanone
在反应釜中,加入0.1000g糠醛,2.0000g去离子水和催化剂Cu0.4Mg5.6Al2,且催化剂的量为20.0mg,密封反应釜。用氢气置换反应釜内的空气,置换3次后,充入0.2MPa氢气。置于180℃的加热套中加热反应3h,待反应结束后,从加热套中取出反应釜置于室温下降温到室温,用乙酸乙酯萃取,气相色谱检测糠醛的转化率和环戊酮的选择性。反应结果见表2中的实施案例36所示。In the reaction kettle, add 0.1000g furfural, 2.0000g deionized water and catalyst Cu 0.4 Mg 5.6 Al 2 , and the amount of the catalyst is 20.0mg, and seal the reaction kettle. Replace the air in the reactor with hydrogen, and after replacing it 3 times, fill it with 0.2MPa hydrogen. Place it in a heating mantle at 180°C for a heating reaction for 3 hours. After the reaction is over, take out the reaction kettle from the heating mantle and place it at room temperature to lower the temperature to room temperature, extract with ethyl acetate, and detect the conversion rate of furfural and cyclopentanone by gas chromatography. selective. The reaction results are shown in Example 36 in Table 2.
实施案例37:催化糠醛或糠醇加氢制备环戊酮Example 37: Catalytic hydrogenation of furfural or furfuryl alcohol to prepare cyclopentanone
在反应釜中,加入0.1000g糠醛,2.0000g去离子水和催化剂Cu0.4Mg5.6Al2,且催化剂的量为20.0mg,密封反应釜。用氢气置换反应釜内的空气,置换3次后,充入0.2MPa氢气。置于180℃的加热套中加热反应4h,待反应结束后,从加热套中取出反应釜置于室温下降温到室温,用乙酸乙酯萃取,气相色谱检测糠醛的转化率和环戊酮的选择性。反应结果见表2中的实施案例37所示。In the reaction kettle, add 0.1000g furfural, 2.0000g deionized water and catalyst Cu 0.4 Mg 5.6 Al 2 , and the amount of the catalyst is 20.0mg, and seal the reaction kettle. Replace the air in the reactor with hydrogen, and after replacing it 3 times, fill it with 0.2MPa hydrogen. Place it in a heating mantle at 180°C for a heating reaction for 4 hours. After the reaction is over, take out the reaction kettle from the heating mantle and let it cool down to room temperature, extract with ethyl acetate, and detect the conversion rate of furfural and cyclopentanone by gas chromatography. selective. The reaction results are shown in Example 37 in Table 2.
实施案例38:催化糠醛或糠醇加氢制备环戊酮Example 38: Catalytic hydrogenation of furfural or furfuryl alcohol to prepare cyclopentanone
在反应釜中,加入0.1000g糠醛,2.0000g去离子水和催化剂Cu0.4Mg5.6Al2,且催化剂的量为20.0mg,密封反应釜。用氢气置换反应釜内的空气,置换3次后,充入0.2MPa氢气。置于180℃的加热套中加热反应6h,待反应结束后,从加热套中取出反应釜置于室温下降温到室温,用乙酸乙酯萃取,气相色谱检测糠醛的转化率和环戊酮的选择性。反应结果见表2中的实施案例38所示。In the reaction kettle, add 0.1000g furfural, 2.0000g deionized water and catalyst Cu 0.4 Mg 5.6 Al 2 , and the amount of the catalyst is 20.0mg, and seal the reaction kettle. Replace the air in the reactor with hydrogen, and after replacing it 3 times, fill it with 0.2MPa hydrogen. Place it in a heating mantle at 180°C and heat it for 6 hours. After the reaction is over, take out the reaction kettle from the heating mantle and let it cool down to room temperature, extract with ethyl acetate, and detect the conversion rate of furfural and cyclopentanone by gas chromatography. selective. The reaction results are shown in Example 38 in Table 2.
实施案例39:催化糠醛或糠醇加氢制备环戊酮Example 39: Catalytic hydrogenation of furfural or furfuryl alcohol to prepare cyclopentanone
在反应釜中,加入0.1000g糠醛,2.0000g去离子水和催化剂Cu0.4Mg5.6Al2,且催化剂的量为20.0mg,密封反应釜。用氢气置换反应釜内的空气,置换3次后,充入0.2MPa氢气。置于180℃的加热套中加热反应7h,待反应结束后,从加热套中取出反应釜置于室温下降温到室温,用乙酸乙酯萃取,气相色谱检测糠醛的转化率和环戊酮的选择性。反应结果见表2中的实施案例39所示。In the reaction kettle, add 0.1000g furfural, 2.0000g deionized water and catalyst Cu 0.4 Mg 5.6 Al 2 , and the amount of the catalyst is 20.0mg, and seal the reaction kettle. Replace the air in the reactor with hydrogen, and after replacing it 3 times, fill it with 0.2MPa hydrogen. Place it in a heating mantle at 180°C and heat it for 7 hours. After the reaction is over, take out the reaction kettle from the heating mantle and let it cool down to room temperature, extract with ethyl acetate, and detect the conversion rate of furfural and cyclopentanone by gas chromatography. selective. The reaction results are shown in Example 39 in Table 2.
实施案例40:催化糠醛或糠醇加氢制备环戊酮Example 40: Catalytic hydrogenation of furfural or furfuryl alcohol to prepare cyclopentanone
在反应釜中,加入0.1000g糠醛,2.0000g去离子水和催化剂Cu0.4Mg5.6Al2,且催化剂的量为20.0mg,密封反应釜。用氢气置换反应釜内的空气,置换3次后,充入0.4MPa氢气。置于180℃的加热套中加热反应5h,待反应结束后,从加热套中取出反应釜置于室温下降温到室温,用乙酸乙酯萃取,气相色谱检测糠醛的转化率和环戊酮的选择性。反应结果见表2中的实施案例40所示。In the reaction kettle, add 0.1000g furfural, 2.0000g deionized water and catalyst Cu 0.4 Mg 5.6 Al 2 , and the amount of the catalyst is 20.0mg, and seal the reaction kettle. Replace the air in the reactor with hydrogen, and after replacing it 3 times, fill it with 0.4MPa hydrogen. Place it in a heating mantle at 180°C and heat it for 5 hours. After the reaction is over, take out the reaction kettle from the heating mantle and let it cool down to room temperature, extract with ethyl acetate, and detect the conversion rate of furfural and cyclopentanone by gas chromatography. selective. The reaction results are shown in Example 40 in Table 2.
实施案例41:催化糠醛或糠醇加氢制备环戊酮Example 41: Catalytic hydrogenation of furfural or furfuryl alcohol to prepare cyclopentanone
在反应釜中,加入0.1000g糠醛,2.0000g去离子水和催化剂Cu0.4Mg5.6Al2,且催化剂的量为20.0mg,密封反应釜。用氢气置换反应釜内的空气,置换3次后,充入0.6MPa氢气。置于180℃的加热套中加热反应5h,待反应结束后,从加热套中取出反应釜置于室温下降温到室温,用乙酸乙酯萃取,气相色谱检测糠醛的转化率和环戊酮的选择性。反应结果见表2中的实施案例41所示。In the reaction kettle, add 0.1000g furfural, 2.0000g deionized water and catalyst Cu 0.4 Mg 5.6 Al 2 , and the amount of the catalyst is 20.0mg, and seal the reaction kettle. Replace the air in the reactor with hydrogen, and after replacing it 3 times, fill it with 0.6MPa hydrogen. Place it in a heating mantle at 180°C and heat it for 5 hours. After the reaction is over, take out the reaction kettle from the heating mantle and let it cool down to room temperature, extract with ethyl acetate, and detect the conversion rate of furfural and cyclopentanone by gas chromatography. selective. The reaction results are shown in Example 41 in Table 2.
实施案例42:催化糠醛或糠醇加氢制备环戊酮Example 42: Catalytic hydrogenation of furfural or furfuryl alcohol to prepare cyclopentanone
在反应釜中,加入0.1000g糠醛,2.0000g去离子水和催化剂Cu0.4Mg5.6Al2,且催化剂的量为20.0mg,密封反应釜。用氢气置换反应釜内的空气,置换3次后,充入0.8MPa氢气。置于180℃的加热套中加热反应5h,待反应结束后,从加热套中取出反应釜置于室温下降温到室温,用乙酸乙酯萃取,气相色谱检测糠醛的转化率和环戊酮的选择性。反应结果见表2中的实施案例42所示。In the reaction kettle, add 0.1000g furfural, 2.0000g deionized water and catalyst Cu 0.4 Mg 5.6 Al 2 , and the amount of the catalyst is 20.0mg, and seal the reaction kettle. Replace the air in the reactor with hydrogen, and after replacing it 3 times, fill it with 0.8MPa hydrogen. Place it in a heating mantle at 180°C and heat it for 5 hours. After the reaction is over, take out the reaction kettle from the heating mantle and let it cool down to room temperature, extract with ethyl acetate, and detect the conversion rate of furfural and cyclopentanone by gas chromatography. selective. The reaction results are shown in Example 42 in Table 2.
表1:Table 1:
表2:Table 2:
将实施案例4中催化剂过滤并用丙酮洗涤,干燥后重复使用。工艺流程与实施案例4一致,催化剂回收使用情况如下表:The catalyst in Example 4 was filtered and washed with acetone, dried and reused. The process flow is consistent with the implementation case 4, and the recovery and use of the catalyst are as follows:
将实施案例25中催化剂过滤并用丙酮洗涤,干燥后重复使用。工艺流程与实施案例25一致,催化剂回收使用情况如下表:The catalyst in Example 25 was filtered and washed with acetone, dried and reused. The process flow is consistent with the implementation case 25, and the recovery and use of the catalyst is as follows:
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