CN107311970B - A kind of method for preparing 4-hydroxy-6-methyltetrahydro-2-pyrone - Google Patents
A kind of method for preparing 4-hydroxy-6-methyltetrahydro-2-pyrone Download PDFInfo
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- CN107311970B CN107311970B CN201710597479.5A CN201710597479A CN107311970B CN 107311970 B CN107311970 B CN 107311970B CN 201710597479 A CN201710597479 A CN 201710597479A CN 107311970 B CN107311970 B CN 107311970B
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- KKZQBMBBMJKIRQ-UHFFFAOYSA-N (4S,6S)-3,4,5,6-Tetrahydro-4-hydroxy-6-methyl-2H-pyran-2-one Chemical compound CC1CC(O)CC(=O)O1 KKZQBMBBMJKIRQ-UHFFFAOYSA-N 0.000 title claims abstract description 16
- 238000000034 method Methods 0.000 title claims abstract description 11
- 239000003054 catalyst Substances 0.000 claims abstract description 20
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims abstract description 19
- 238000006243 chemical reaction Methods 0.000 claims abstract description 19
- 239000001257 hydrogen Substances 0.000 claims abstract description 12
- 229910052739 hydrogen Inorganic materials 0.000 claims abstract description 12
- 239000000203 mixture Substances 0.000 claims abstract description 11
- 229910052757 nitrogen Inorganic materials 0.000 claims abstract description 10
- 239000000852 hydrogen donor Substances 0.000 claims abstract description 9
- 239000002082 metal nanoparticle Substances 0.000 claims abstract description 8
- -1 alcohol compound Chemical class 0.000 claims abstract description 7
- 150000002431 hydrogen Chemical class 0.000 claims abstract description 7
- 238000006276 transfer reaction Methods 0.000 claims abstract description 4
- 239000002994 raw material Substances 0.000 claims abstract description 3
- 229910000510 noble metal Inorganic materials 0.000 claims abstract 7
- 150000002596 lactones Chemical class 0.000 claims abstract 2
- 239000002105 nanoparticle Substances 0.000 claims description 14
- NSYSSMYQPLSPOD-UHFFFAOYSA-N triacetate lactone Chemical compound CC1=CC(O)=CC(=O)O1 NSYSSMYQPLSPOD-UHFFFAOYSA-N 0.000 claims description 14
- KFZMGEQAYNKOFK-UHFFFAOYSA-N Isopropanol Chemical group CC(C)O KFZMGEQAYNKOFK-UHFFFAOYSA-N 0.000 claims description 10
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 claims description 10
- 238000004519 manufacturing process Methods 0.000 claims description 6
- 229910052759 nickel Inorganic materials 0.000 claims description 5
- 239000010941 cobalt Substances 0.000 claims description 3
- 229910017052 cobalt Inorganic materials 0.000 claims description 3
- GUTLYIVDDKVIGB-UHFFFAOYSA-N cobalt atom Chemical compound [Co] GUTLYIVDDKVIGB-UHFFFAOYSA-N 0.000 claims description 3
- 238000011084 recovery Methods 0.000 claims description 3
- 238000001035 drying Methods 0.000 claims description 2
- 238000000926 separation method Methods 0.000 claims description 2
- 238000005406 washing Methods 0.000 claims description 2
- NVIVJPRCKQTWLY-UHFFFAOYSA-N cobalt nickel Chemical compound [Co][Ni][Co] NVIVJPRCKQTWLY-UHFFFAOYSA-N 0.000 claims 2
- 238000004064 recycling Methods 0.000 claims 1
- URAYPUMNDPQOKB-UHFFFAOYSA-N triacetin Chemical compound CC(=O)OCC(OC(C)=O)COC(C)=O URAYPUMNDPQOKB-UHFFFAOYSA-N 0.000 description 16
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 description 12
- 239000001087 glyceryl triacetate Substances 0.000 description 8
- 235000013773 glyceryl triacetate Nutrition 0.000 description 8
- 239000010970 precious metal Substances 0.000 description 8
- 239000000126 substance Substances 0.000 description 8
- 229960002622 triacetin Drugs 0.000 description 8
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 8
- LRHPLDYGYMQRHN-UHFFFAOYSA-N N-Butanol Chemical compound CCCCO LRHPLDYGYMQRHN-UHFFFAOYSA-N 0.000 description 6
- 150000001298 alcohols Chemical class 0.000 description 6
- 239000000047 product Substances 0.000 description 6
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 5
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 5
- 239000007864 aqueous solution Substances 0.000 description 5
- 238000002360 preparation method Methods 0.000 description 5
- BDERNNFJNOPAEC-UHFFFAOYSA-N propan-1-ol Chemical compound CCCO BDERNNFJNOPAEC-UHFFFAOYSA-N 0.000 description 5
- 239000000243 solution Substances 0.000 description 5
- AMQJEAYHLZJPGS-UHFFFAOYSA-N N-Pentanol Chemical compound CCCCCO AMQJEAYHLZJPGS-UHFFFAOYSA-N 0.000 description 4
- BTANRVKWQNVYAZ-UHFFFAOYSA-N butan-2-ol Chemical compound CCC(C)O BTANRVKWQNVYAZ-UHFFFAOYSA-N 0.000 description 4
- 230000003197 catalytic effect Effects 0.000 description 4
- 238000002474 experimental method Methods 0.000 description 4
- 238000004128 high performance liquid chromatography Methods 0.000 description 4
- 229910000033 sodium borohydride Inorganic materials 0.000 description 4
- 239000012279 sodium borohydride Substances 0.000 description 4
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 3
- 239000002028 Biomass Substances 0.000 description 3
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 3
- 238000006555 catalytic reaction Methods 0.000 description 3
- 239000007810 chemical reaction solvent Substances 0.000 description 3
- 238000005984 hydrogenation reaction Methods 0.000 description 3
- 238000007789 sealing Methods 0.000 description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 2
- 229910052799 carbon Inorganic materials 0.000 description 2
- 239000007795 chemical reaction product Substances 0.000 description 2
- UFMZWBIQTDUYBN-UHFFFAOYSA-N cobalt dinitrate Chemical compound [Co+2].[O-][N+]([O-])=O.[O-][N+]([O-])=O UFMZWBIQTDUYBN-UHFFFAOYSA-N 0.000 description 2
- 229910001981 cobalt nitrate Inorganic materials 0.000 description 2
- 229910052802 copper Inorganic materials 0.000 description 2
- 239000010949 copper Substances 0.000 description 2
- HPXRVTGHNJAIIH-UHFFFAOYSA-N cyclohexanol Chemical compound OC1CCCCC1 HPXRVTGHNJAIIH-UHFFFAOYSA-N 0.000 description 2
- 239000000446 fuel Substances 0.000 description 2
- ZXEKIIBDNHEJCQ-UHFFFAOYSA-N isobutanol Chemical compound CC(C)CO ZXEKIIBDNHEJCQ-UHFFFAOYSA-N 0.000 description 2
- 230000000813 microbial effect Effects 0.000 description 2
- 244000005700 microbiome Species 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- KBJMLQFLOWQJNF-UHFFFAOYSA-N nickel(ii) nitrate Chemical compound [Ni+2].[O-][N+]([O-])=O.[O-][N+]([O-])=O KBJMLQFLOWQJNF-UHFFFAOYSA-N 0.000 description 2
- 150000003138 primary alcohols Chemical class 0.000 description 2
- 238000011160 research Methods 0.000 description 2
- 150000003333 secondary alcohols Chemical class 0.000 description 2
- 239000002904 solvent Substances 0.000 description 2
- 238000012546 transfer Methods 0.000 description 2
- QXZUUHYBWMWJHK-UHFFFAOYSA-N [Co].[Ni] Chemical compound [Co].[Ni] QXZUUHYBWMWJHK-UHFFFAOYSA-N 0.000 description 1
- 238000010170 biological method Methods 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 150000001720 carbohydrates Chemical class 0.000 description 1
- 235000014633 carbohydrates Nutrition 0.000 description 1
- 238000009903 catalytic hydrogenation reaction Methods 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- XTVVROIMIGLXTD-UHFFFAOYSA-N copper(II) nitrate Chemical compound [Cu+2].[O-][N+]([O-])=O.[O-][N+]([O-])=O XTVVROIMIGLXTD-UHFFFAOYSA-N 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000001514 detection method Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 125000000524 functional group Chemical group 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 239000000543 intermediate Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 230000037353 metabolic pathway Effects 0.000 description 1
- QJGQUHMNIGDVPM-UHFFFAOYSA-N nitrogen group Chemical group [N] QJGQUHMNIGDVPM-UHFFFAOYSA-N 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 239000006228 supernatant Substances 0.000 description 1
- 238000003786 synthesis reaction Methods 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
Classifications
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- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07D—HETEROCYCLIC COMPOUNDS
- C07D309/00—Heterocyclic compounds containing six-membered rings having one oxygen atom as the only ring hetero atom, not condensed with other rings
- C07D309/16—Heterocyclic compounds containing six-membered rings having one oxygen atom as the only ring hetero atom, not condensed with other rings having one double bond between ring members or between a ring member and a non-ring member
- C07D309/28—Heterocyclic compounds containing six-membered rings having one oxygen atom as the only ring hetero atom, not condensed with other rings having one double bond between ring members or between a ring member and a non-ring member with hetero atoms or with carbon atoms having three bonds to hetero atoms with at the most one bond to halogen, e.g. ester or nitrile radicals, directly attached to ring carbon atoms
- C07D309/30—Oxygen atoms, e.g. delta-lactones
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- 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
-
- 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
- B01J23/74—Iron group metals
- B01J23/75—Cobalt
-
- 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
- B01J23/74—Iron group metals
- B01J23/755—Nickel
-
- 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
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/40—Catalysts, in general, characterised by their form or physical properties characterised by dimensions, e.g. grain size
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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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- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Catalysts (AREA)
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
Description
技术领域technical field
本发明具体涉及一种制备4-羟基-6-甲基四氢吡喃酮的方法。The invention specifically relates to a method for preparing 4-hydroxy-6-methyltetrahydropyranone.
背景技术Background technique
生物质是唯一可再生的有机碳资源,是替代石油生产燃料和化学品的理想候选。因此,充分利用生物质中的有机碳资源,发展生物质转化制燃料和化学品的新路线和新方法,已成为新能源和新材料领域研究热点。微生物合成的平台分子为碳水化合物转化为商业化学品提供了新的机遇,这类微生物来源的平台分子是微生物单一代谢途径的产物,并具有灵活可控的官能团,化学催化升级可将这些平台分子转化为多样的终端产品,用以替代现有的石化产品。三乙酸内酯(4-羟基-6-甲基-2-吡喃酮,Triacetic acid lactone)就是这样一种微生物来源的新一代平台分子,其既可来源于自然(植物和微生物),也可由乙酸合成,被认为是“联系生物催化和化学催化的桥梁化合物”,研究其高效转化利用有助于克服单一化学法或单一生物法制备生物基高值化学品的缺点。三乙酸内酯经过催化升级可转化为多种有商业价值的化学中间体和终端产品。三乙酸内酯转化的第一步是催化加氢,目前存在的问题是三乙酸内酯在水溶液中易降解,加氢步骤需使用正丁醇为溶剂,氢气为氢源,贵金属为催化剂。Biomass is the only renewable organic carbon resource and an ideal candidate to replace petroleum in the production of fuels and chemicals. Therefore, it has become a research hotspot in the field of new energy and new materials to make full use of the organic carbon resources in biomass and develop new routes and methods for converting biomass into fuels and chemicals. Microbially synthesized platform molecules provide new opportunities for the conversion of carbohydrates into commercial chemicals. Such microbial-derived platform molecules are the products of a single metabolic pathway of microorganisms and have flexible and controllable functional groups. Chemical catalysis upgrades can convert these platform molecules. Converted into a variety of end products to replace existing petrochemical products. Triacetic acid lactone (4-hydroxy-6-methyl-2-pyrone, Triacetic acid lactone) is such a new generation platform molecule of microbial origin, which can be derived either from nature (plants and microorganisms) or from Acetic acid synthesis, considered as a "bridge compound linking biocatalysis and chemical catalysis", research on its efficient conversion and utilization helps to overcome the shortcomings of single chemical method or single biological method to prepare bio-based high-value chemicals. Triacetin can be converted into a variety of commercially valuable chemical intermediates and end products through catalytic upgrading. The first step of triacetin conversion is catalytic hydrogenation. The existing problem is that triacetin is easily degraded in an aqueous solution. The hydrogenation step requires n-butanol as a solvent, hydrogen as a hydrogen source, and precious metal as a catalyst.
发明内容SUMMARY OF THE INVENTION
本发明的主要目的在于提供一种制备4-羟基-6-甲基四氢-2-吡喃酮的方法,以克服现有技术中的不足。The main purpose of the present invention is to provide a method for preparing 4-hydroxy-6-methyltetrahydro-2-pyrone so as to overcome the deficiencies in the prior art.
为实现前述发明目的,本发明采用的技术方案包括:In order to realize the foregoing invention purpose, the technical scheme adopted in the present invention includes:
将三乙酸内酯原料与具有氢供体的醇类化合物混合加入到密闭高压反应釜内,在氮气压力为1-12MPa、反应温度为室温-150℃,催化剂存在的条件下,进行氢转移反应0.5-48h,得到4-羟基-6甲基四氢-2-吡喃酮,所述的催化剂为非贵金属纳米颗粒。The triacetate lactone raw material and the alcohol compound with hydrogen donor are mixed and added into the closed autoclave, and the hydrogen transfer reaction is carried out under the condition that the nitrogen pressure is 1-12MPa, the reaction temperature is room temperature-150℃, and the catalyst exists. 0.5-48h, 4-hydroxy-6-methyltetrahydro-2-pyranone is obtained, and the catalyst is non-precious metal nanoparticles.
进一步的,所述的醇类化合物包括一级醇和二级醇,所述一级醇为甲醇、乙醇、正丙醇、正丁醇、正戊醇或环己醇,所述二级醇为异丙醇、异丁醇、或仲丁醇。Further, the alcohol compounds include primary alcohol and secondary alcohol, the primary alcohol is methanol, ethanol, n-propanol, n-butanol, n-pentanol or cyclohexanol, and the secondary alcohol is isopropyl alcohol Propanol, isobutanol, or sec-butanol.
进一步的,所述的醇类化合物与三乙酸内酯的比例为5-50mL∶1g。Further, the ratio of the alcohol compound to the triacetin is 5-50 mL:1 g.
进一步的,所述的非贵金属包括镍、钴、铜中的一种或两种以上。Further, the non-precious metal includes one or more of nickel, cobalt and copper.
进一步的,所述的非贵金属纳米颗粒催化剂与三乙酸内酯的用量比为0.03-2.0g∶1g。Further, the dosage ratio of the non-precious metal nanoparticle catalyst to triacetin is 0.03-2.0g:1g.
进一步的,还包括对非贵金属纳米颗粒催化剂的回收及重复利用的步骤;所述催化剂的回收方法包括离心分离、洗涤、干燥。Further, it also includes the steps of recovering and reusing the non-precious metal nanoparticle catalyst; the method for recovering the catalyst includes centrifugal separation, washing and drying.
与现有技术相比,本发明的优点包括:氢转移反应中醇类化合物既作为溶剂又提供氢源,不需要额外氢源,所使用的催化剂为常见易得的非贵金属,成本低廉,可回收利用。与现有技术相比,本发明的工艺不需要额外氢气,操作简单安全。Compared with the prior art, the advantages of the present invention include: in the hydrogen transfer reaction, the alcohol compound both serves as a solvent and provides a hydrogen source, no additional hydrogen source is needed, the catalyst used is a common and readily available non-precious metal, the cost is low, and the cost is low. recycle and re-use. Compared with the prior art, the process of the present invention does not require additional hydrogen, and the operation is simple and safe.
附图说明Description of drawings
图1是实施例1产物的高效液相色谱检测结果图。Fig. 1 is the high-performance liquid chromatography detection result diagram of the product of Example 1.
具体实施方式Detailed ways
下面将结合本发明的若干实施例,对本发明的技术方案进行详细的描述,显然,所描述的实施例仅仅是本发明一部分实施例,而不是全部的实施例。基于本发明中的实施例,本领域普通技术人员在没有做出创造性劳动的前提下所获得的所有其他实施例,都属于本发明保护的范围。The technical solutions of the present invention will be described in detail below with reference to several embodiments of the present invention. Obviously, the described embodiments are only a part of the embodiments of the present invention, rather than all the embodiments. Based on the embodiments of the present invention, all other embodiments obtained by those of ordinary skill in the art without creative work fall within the protection scope of the present invention.
实施例1-4:Examples 1-4:
本实施例提供不同金属纳米颗粒的制备,以及催化氢转移三乙酸内酯制备4-羟基-6-甲基四氢-2-吡喃酮的实验:This embodiment provides the preparation of different metal nanoparticles, and the experiment of catalyzing hydrogen transfer of triacetin to prepare 4-hydroxy-6-methyltetrahydro-2-pyranone:
镍纳米颗粒的制备:将0.1g硝酸镍溶解于4mL水中,滴加到40mL乙二醇和40mL水的混合液中,超声分散30min,将16mL硼氢化钠水溶液(0.01g/mL)滴加至上述溶液,室温搅拌8h,过滤,80℃真空干燥24h。Preparation of nickel nanoparticles: 0.1 g of nickel nitrate was dissolved in 4 mL of water, added dropwise to a mixture of 40 mL of ethylene glycol and 40 mL of water, ultrasonically dispersed for 30 min, and 16 mL of sodium borohydride aqueous solution (0.01 g/mL) was added dropwise to the above. The solution was stirred at room temperature for 8h, filtered, and dried under vacuum at 80°C for 24h.
钴纳米颗粒的制备:将0.1g硝酸钴溶解于4mL水中,滴加到40mL乙二醇和40mL水的混合液中,超声分散30min,将16mL硼氢化钠水溶液(0.01g/mL)滴加至上述溶液,室温搅拌8h,过滤,80℃真空干燥24h。Preparation of cobalt nanoparticles: 0.1 g of cobalt nitrate was dissolved in 4 mL of water, added dropwise to a mixture of 40 mL of ethylene glycol and 40 mL of water, ultrasonically dispersed for 30 min, and 16 mL of sodium borohydride aqueous solution (0.01 g/mL) was added dropwise to the above. The solution was stirred at room temperature for 8h, filtered, and dried under vacuum at 80°C for 24h.
铜纳米颗粒的制备:将0.1g硝酸铜溶解于4mL水中,滴加到40mL乙二醇和40mL水的混合液中,超声分散30min,将16mL硼氢化钠水溶液(0.01g/mL)滴加至上述溶液,室温搅拌8h,过滤,80℃真空干燥24h。Preparation of copper nanoparticles: 0.1 g of copper nitrate was dissolved in 4 mL of water, added dropwise to a mixture of 40 mL of ethylene glycol and 40 mL of water, ultrasonically dispersed for 30 min, and 16 mL of sodium borohydride aqueous solution (0.01 g/mL) was added dropwise to the above. The solution was stirred at room temperature for 8h, filtered, and dried under vacuum at 80°C for 24h.
镍钴双金属纳米颗粒的制备:将0.05g硝酸镍和0.05g硝酸钴溶解于4mL水中,滴加到40mL乙二醇和40mL水的混合液中,超声分散30min,将16mL硼氢化钠水溶液(0.01g/mL)滴加至上述溶液,室温搅拌8h,过滤,80℃真空干燥24h。Preparation of nickel-cobalt bimetallic nanoparticles: 0.05g of nickel nitrate and 0.05g of cobalt nitrate were dissolved in 4mL of water, added dropwise to a mixture of 40mL of ethylene glycol and 40mL of water, ultrasonically dispersed for 30min, and 16mL of sodium borohydride aqueous solution (0.01 g/mL) was added dropwise to the above solution, stirred at room temperature for 8 h, filtered, and dried under vacuum at 80 °C for 24 h.
将所制备的金属纳米颗粒加入到高压反应釜中,再加入0.25g三乙酸内酯和5mL异丙醇(既作为供氢体又作为反应溶剂),密封后,用氮气置换五次,然后充入0.1MPa的氮气,50℃反应10h,反应结束后产物组成使用高效液相色谱分析定量。具体结果见表1:The prepared metal nanoparticles were added to the autoclave, and then 0.25 g of triacetate lactone and 5 mL of isopropanol (both as a hydrogen donor and a reaction solvent) were added, and after sealing, they were replaced with nitrogen five times, and then filled with nitrogen. Introduce 0.1MPa nitrogen, react at 50°C for 10h, after the reaction, the composition of the product is analyzed and quantified by high performance liquid chromatography. The specific results are shown in Table 1:
表1.不同催化剂的催化结果Table 1. Catalytic results of different catalysts
实施例5-10:Examples 5-10:
本实施例提供不同醇类化合物作为氢供体时,三乙酸内酯加氢制备4-羟基-6-甲基四氢-2-吡喃酮的实验:This example provides an experiment for preparing 4-hydroxy-6-methyltetrahydro-2-pyranone by hydrogenation of triacetin when different alcohol compounds are used as hydrogen donors:
将0.02g镍纳米颗粒加入到高压反应釜中,再加入0.25g三乙酸内酯和5mL不同醇类化合物(既作为供氢体又作为反应溶剂),密封后,用氮气置换五次,然后充入0.1MPa的氮气,50℃反应10h,反应结束后产物组成使用高效液相色谱分析定量。具体结果见表2:Add 0.02g of nickel nanoparticles into the autoclave, then add 0.25g of triacetate lactone and 5mL of different alcohol compounds (both as a hydrogen donor and as a reaction solvent), after sealing, replace with nitrogen five times, and then fill with Introduce 0.1MPa nitrogen, react at 50°C for 10h, after the reaction, the composition of the product is analyzed and quantified by high performance liquid chromatography. The specific results are shown in Table 2:
表2.使用不同醇类化合物作为氢供体时的催化结果Table 2. Catalytic results when using different alcohols as hydrogen donors
实施例11-13:Examples 11-13:
本实施例提供不同反应温度下,三乙酸内酯加氢制备4-羟基-6-甲基四氢-2-吡喃酮的实验:This example provides the experiment of preparing 4-hydroxy-6-methyltetrahydro-2-pyranone by hydrogenation of triacetin at different reaction temperatures:
将0.02g镍纳米颗粒加入到高压反应釜中,再加入0.25g三乙酸内酯和5mL不同醇类化合物(既作为供氢体又作为反应溶剂),密封后,用氮气置换五次,然后充入0.1MPa的氮气,不同温度下反应10h,反应结束后产物组成使用高效液相色谱分析定量。具体结果见表3:Add 0.02g of nickel nanoparticles into the autoclave, then add 0.25g of triacetate lactone and 5mL of different alcohol compounds (both as a hydrogen donor and as a reaction solvent), after sealing, replace with nitrogen five times, and then fill with Enter 0.1MPa of nitrogen, and react at different temperatures for 10h. After the reaction, the composition of the product is analyzed and quantified by high performance liquid chromatography. The specific results are shown in Table 3:
表3.不同温度下的催化结果Table 3. Catalysis results at different temperatures
实施例14-17:Examples 14-17:
本实验中所使用的反应条件与实施例1的实验条件相同,不同之处在于增加了对催化剂进行回收、重复使用的步骤。The reaction conditions used in this experiment are the same as the experimental conditions in Example 1, except that the steps of recovering and reusing the catalyst are added.
回收及重复使用的操作步骤如下:反应结束后,离心分离催化剂,倒出上层清液,用乙醇将沉淀物洗涤三次,80℃真空干燥,用于下次反应,重复使用的测试结果见表4:The operation steps of recovery and reuse are as follows: after the reaction is completed, the catalyst is centrifuged, the supernatant is poured out, the precipitate is washed three times with ethanol, and vacuum-dried at 80 ° C for the next reaction. The test results of repeated use are shown in Table 4. :
表4.催化剂回收、重复使用的催化结果Table 4. Catalytic results for catalyst recovery and reuse
参阅前述内容,可以证明,本发明通过非贵金属纳米颗粒催化氢转移三乙酸内酯制备4-羟基-6-甲基四氢-2-吡喃酮,不需要额外氢气和贵金属催化剂,成本低廉,催化剂可回收利用。Referring to the foregoing content, it can be proved that the present invention prepares 4-hydroxy-6-methyltetrahydro-2-pyranone by catalyzing hydrogen transfer of triacetolactone by non-precious metal nanoparticles, does not require additional hydrogen and precious metal catalysts, and has low cost, The catalyst can be recycled.
应当理解的是,以上所述仅为本发明的优选实施例而已,并不用于限制本发明,对于本领域的技术人员来说,本发明可以有各种更改和变化。凡在本发明的精神和原则之内,所作的任何修改、等同替换、改进等,均应包含在本发明的保护范围之内。It should be understood that the above descriptions are only preferred embodiments of the present invention, and are not intended to limit the present invention. For those skilled in the art, the present invention may have various modifications and changes. Any modification, equivalent replacement, improvement, etc. made within the spirit and principle of the present invention shall be included within the protection scope of the present invention.
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