CN107903146B - A kind of method for preparing 1,2-hexanediol by catalytic oxidation of 1-hexene - Google Patents
A kind of method for preparing 1,2-hexanediol by catalytic oxidation of 1-hexene Download PDFInfo
- Publication number
- CN107903146B CN107903146B CN201711181264.1A CN201711181264A CN107903146B CN 107903146 B CN107903146 B CN 107903146B CN 201711181264 A CN201711181264 A CN 201711181264A CN 107903146 B CN107903146 B CN 107903146B
- Authority
- CN
- China
- Prior art keywords
- hexene
- hydrogen peroxide
- hexanediol
- catalyst
- formic acid
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Active
Links
- LIKMAJRDDDTEIG-UHFFFAOYSA-N 1-hexene Chemical compound CCCCC=C LIKMAJRDDDTEIG-UHFFFAOYSA-N 0.000 title claims abstract description 120
- 229940015975 1,2-hexanediol Drugs 0.000 title claims abstract description 44
- FHKSXSQHXQEMOK-UHFFFAOYSA-N hexane-1,2-diol Chemical compound CCCCC(O)CO FHKSXSQHXQEMOK-UHFFFAOYSA-N 0.000 title claims abstract description 44
- 238000000034 method Methods 0.000 title claims abstract description 20
- 238000007254 oxidation reaction Methods 0.000 title claims abstract description 14
- 230000003647 oxidation Effects 0.000 title claims abstract description 13
- 230000003197 catalytic effect Effects 0.000 title claims abstract description 12
- MHAJPDPJQMAIIY-UHFFFAOYSA-N Hydrogen peroxide Chemical compound OO MHAJPDPJQMAIIY-UHFFFAOYSA-N 0.000 claims abstract description 110
- BDAGIHXWWSANSR-UHFFFAOYSA-N methanoic acid Natural products OC=O BDAGIHXWWSANSR-UHFFFAOYSA-N 0.000 claims abstract description 79
- 239000003054 catalyst Substances 0.000 claims abstract description 43
- 235000019253 formic acid Nutrition 0.000 claims abstract description 40
- OSWFIVFLDKOXQC-UHFFFAOYSA-N 4-(3-methoxyphenyl)aniline Chemical compound COC1=CC=CC(C=2C=CC(N)=CC=2)=C1 OSWFIVFLDKOXQC-UHFFFAOYSA-N 0.000 claims abstract description 38
- 238000006243 chemical reaction Methods 0.000 claims abstract description 26
- 238000003756 stirring Methods 0.000 claims description 20
- WJJMNDUMQPNECX-UHFFFAOYSA-N Dipicolinic acid Natural products OC(=O)C1=CC=CC(C(O)=O)=N1 WJJMNDUMQPNECX-UHFFFAOYSA-N 0.000 claims description 9
- 230000007062 hydrolysis Effects 0.000 claims description 5
- 238000006460 hydrolysis reaction Methods 0.000 claims description 5
- 239000000203 mixture Substances 0.000 claims description 5
- CABMTIJINOIHOD-UHFFFAOYSA-N 2-[4-methyl-5-oxo-4-(propan-2-yl)-4,5-dihydro-1H-imidazol-2-yl]quinoline-3-carboxylic acid Chemical compound N1C(=O)C(C(C)C)(C)N=C1C1=NC2=CC=CC=C2C=C1C(O)=O CABMTIJINOIHOD-UHFFFAOYSA-N 0.000 claims description 3
- 239000003446 ligand Substances 0.000 claims description 3
- 150000001450 anions Chemical class 0.000 claims description 2
- 150000001768 cations Chemical class 0.000 claims description 2
- 238000000926 separation method Methods 0.000 claims description 2
- 239000007800 oxidant agent Substances 0.000 abstract description 7
- 230000001590 oxidative effect Effects 0.000 abstract description 7
- 239000004593 Epoxy Substances 0.000 abstract 1
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 abstract 1
- 150000001875 compounds Chemical class 0.000 abstract 1
- -1 formic acid peroxide Chemical class 0.000 abstract 1
- XIAJQOBRHVKGSP-UHFFFAOYSA-N hexa-1,2-diene Chemical compound CCCC=C=C XIAJQOBRHVKGSP-UHFFFAOYSA-N 0.000 abstract 1
- 230000003301 hydrolyzing effect Effects 0.000 abstract 1
- 238000011065 in-situ storage Methods 0.000 abstract 1
- 239000012429 reaction media Substances 0.000 abstract 1
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 30
- 239000000243 solution Substances 0.000 description 13
- 238000010813 internal standard method Methods 0.000 description 9
- 239000011541 reaction mixture Substances 0.000 description 9
- 238000002474 experimental method Methods 0.000 description 7
- 238000010438 heat treatment Methods 0.000 description 7
- XEKOWRVHYACXOJ-UHFFFAOYSA-N Ethyl acetate Chemical compound CCOC(C)=O XEKOWRVHYACXOJ-UHFFFAOYSA-N 0.000 description 6
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 6
- 239000002994 raw material Substances 0.000 description 5
- YMWUJEATGCHHMB-UHFFFAOYSA-N Dichloromethane Chemical compound ClCCl YMWUJEATGCHHMB-UHFFFAOYSA-N 0.000 description 3
- 239000002253 acid Substances 0.000 description 3
- 239000000047 product Substances 0.000 description 3
- 239000012266 salt solution Substances 0.000 description 3
- 229920006395 saturated elastomer Polymers 0.000 description 3
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 2
- 239000003513 alkali Substances 0.000 description 2
- 150000001336 alkenes Chemical class 0.000 description 2
- 239000000706 filtrate Substances 0.000 description 2
- 239000003921 oil Substances 0.000 description 2
- 238000002360 preparation method Methods 0.000 description 2
- 230000035484 reaction time Effects 0.000 description 2
- 239000011734 sodium Substances 0.000 description 2
- 239000002904 solvent Substances 0.000 description 2
- 238000001228 spectrum Methods 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 238000001308 synthesis method Methods 0.000 description 2
- PUPZLCDOIYMWBV-UHFFFAOYSA-N (+/-)-1,3-Butanediol Chemical compound CC(O)CCO PUPZLCDOIYMWBV-UHFFFAOYSA-N 0.000 description 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical group [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 230000000844 anti-bacterial effect Effects 0.000 description 1
- 230000002421 anti-septic effect Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000002537 cosmetic Substances 0.000 description 1
- 239000012043 crude product Substances 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 238000006735 epoxidation reaction Methods 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 239000012847 fine chemical Substances 0.000 description 1
- 125000002887 hydroxy group Chemical group [H]O* 0.000 description 1
- 239000000976 ink Substances 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- VLKZOEOYAKHREP-UHFFFAOYSA-N n-Hexane Chemical compound CCCCCC VLKZOEOYAKHREP-UHFFFAOYSA-N 0.000 description 1
- 230000009972 noncorrosive effect Effects 0.000 description 1
- JRZJOMJEPLMPRA-UHFFFAOYSA-N olefin Natural products CCCCCCCC=C JRZJOMJEPLMPRA-UHFFFAOYSA-N 0.000 description 1
- 150000007524 organic acids Chemical class 0.000 description 1
- 150000002894 organic compounds Chemical class 0.000 description 1
- 239000003960 organic solvent Substances 0.000 description 1
- 239000003973 paint Substances 0.000 description 1
- 150000002978 peroxides Chemical class 0.000 description 1
- 239000003444 phase transfer catalyst Substances 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- HPALAKNZSZLMCH-UHFFFAOYSA-M sodium;chloride;hydrate Chemical class O.[Na+].[Cl-] HPALAKNZSZLMCH-UHFFFAOYSA-M 0.000 description 1
- 238000013517 stratification Methods 0.000 description 1
- 230000002194 synthesizing effect Effects 0.000 description 1
- 231100000331 toxic Toxicity 0.000 description 1
- 230000002588 toxic effect Effects 0.000 description 1
Images
Classifications
-
- 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
- C07C29/03—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by addition of hydroxy groups to unsaturated carbon-to-carbon bonds, e.g. with the aid of H2O2
- C07C29/04—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by addition of hydroxy groups to unsaturated carbon-to-carbon bonds, e.g. with the aid of H2O2 by hydration of carbon-to-carbon double bonds
-
- 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
- B01J31/00—Catalysts comprising hydrides, coordination complexes or organic compounds
- B01J31/16—Catalysts comprising hydrides, coordination complexes or organic compounds containing coordination complexes
- B01J31/22—Organic complexes
- B01J31/2204—Organic complexes the ligands containing oxygen or sulfur as complexing atoms
- B01J31/2208—Oxygen, e.g. acetylacetonates
- B01J31/2226—Anionic ligands, i.e. the overall ligand carries at least one formal negative charge
- B01J31/2243—At least one oxygen and one nitrogen atom present as complexing atoms in an at least bidentate or bridging ligand
-
- 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
- B01J2231/00—Catalytic reactions performed with catalysts classified in B01J31/00
- B01J2231/70—Oxidation reactions, e.g. epoxidation, (di)hydroxylation, dehydrogenation and analogues
-
- 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
- B01J2531/00—Additional information regarding catalytic systems classified in B01J31/00
- B01J2531/50—Complexes comprising metals of Group V (VA or VB) as the central metal
- B01J2531/56—Vanadium
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Inorganic 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)
- Catalysts (AREA)
Abstract
Description
技术领域technical field
本发明属于烯烃氧化制备脂肪二醇的技术领域,具体涉及一种催化氧化1-己烯制备1,2-己二醇的方法。The invention belongs to the technical field of preparing aliphatic diol by olefin oxidation, and particularly relates to a method for preparing 1,2-hexanediol by catalytic oxidation of 1-hexene.
背景技术Background technique
1,2-己二醇在碳链的第1和第2位置上有两个羟基官能团,与水互溶,能以任何比例与多种有机化合物混合,无腐蚀性,且具有抗菌与防腐活性,因此广泛应用于制造高级化妆品、多用途高级清洁剂及油墨、油漆等产品,是重要的精细化工原料。1,2-Hexanediol has two hydroxyl functional groups on the 1st and 2nd positions of the carbon chain. It is miscible with water and can be mixed with various organic compounds in any ratio. It is non-corrosive, and has antibacterial and antiseptic activities. Therefore, it is widely used in the manufacture of advanced cosmetics, multi-purpose advanced cleaners, inks, paints and other products, and is an important fine chemical raw material.
以1-己烯为原料,双氧水为氧化剂,经环氧化水解是制备1,2-己二醇的重要方法之一。专利CN1465556报道了以1-己烯为原料,有机酸为溶剂,过氧化物为氧化剂,经过氧化反应,加碱水解得到粗产品,再加酸反调至中性,萃取、干燥、精馏后可得到纯度大于99%的1,2-己二醇,但是收率只有75%。专利CN106316783中提到采用气液管道式制备1,2-己二醇的方法,以1-己烯为原料,以过氧有机酸为氧化剂,在无水有机溶剂中发生环氧化反应,加碱水解得到1,2-己二醇粗品,经加酸调至中性,萃取、干燥、精馏后得到1,2-己二醇,纯度大于99%,收率可达88%,但该方法使用二氯甲烷作为溶剂,毒性较大。专利CN103570493报道了以HCOOH和H2O2反应生成的HCOOOH作为氧化剂,[(C18H37)2N(CH3)2]3[PW4O16]为相转移催化剂,催化氧化1-己烯合成1,2-己二醇,纯度大于99%,收率达到90.4%。由此可见,在以双氧水为氧化剂合成1,2-己二醇的方法中加入催化剂是改进的方向,合成方法还有待进一步发展。Using 1-hexene as raw material and hydrogen peroxide as oxidant, epoxidative hydrolysis is one of the important methods to prepare 1,2-hexanediol. Patent CN1465556 reported that 1-hexene is used as raw material, organic acid is used as solvent, and peroxide is used as oxidant. After oxidation reaction, alkali hydrolysis is added to obtain crude product, and acid is added to reverse adjustment to neutrality. 1,2-Hexanediol was obtained with a purity greater than 99%, but in a yield of only 75%. Patent CN106316783 mentions the method of preparing 1,2-hexanediol by gas-liquid pipeline, using 1-hexene as raw material, using peroxyorganic acid as oxidant, epoxidation reaction occurs in anhydrous organic solvent, adding Alkali hydrolysis obtains crude 1,2-hexanediol, which is adjusted to neutrality by adding acid. After extraction, drying and rectification, 1,2-hexanediol is obtained with a purity of more than 99% and a yield of 88%. The method uses dichloromethane as a solvent, which is highly toxic. Patent CN103570493 reported that HCOOOH generated by the reaction of HCOOH and H 2 O 2 was used as an oxidant, and [(C 18 H 37 ) 2 N(CH 3 ) 2 ] 3 [PW 4 O 16 ] was used as a phase transfer catalyst to catalyze the oxidation of 1-hexane 1,2-hexanediol was synthesized from alkene, the purity was more than 99%, and the yield was 90.4%. It can be seen that adding a catalyst to the method for synthesizing 1,2-hexanediol with hydrogen peroxide as an oxidant is a direction for improvement, and the synthesis method still needs to be further developed.
发明内容SUMMARY OF THE INVENTION
本发明的目的在于提供一种催化效率高、反应条件温和的制备1,2-己二醇的方法。The purpose of the present invention is to provide a method for preparing 1,2-hexanediol with high catalytic efficiency and mild reaction conditions.
本发明的技术方案:Technical scheme of the present invention:
一种催化氧化1-己烯制备1,2-己二醇的方法,包括如下步骤:A method for preparing 1,2-hexanediol by catalytic oxidation of 1-hexene, comprising the steps of:
步骤一,先将甲酸、双氧水、催化剂加入到反应器中,搅拌升温至30-60℃后,向反应体系中加入1-己烯并保持温度恒定,恒温反应0.5-2h,然后在室温下继续反应6-20h;其中,甲酸与1-己烯的摩尔比为1~12:1,双氧水中过氧化氢的质量百分数为10-50%,双氧水中过氧化氢与1-己烯的摩尔比为1~8:1;所述催化剂为MVO2dipic,催化剂用量为1-己烯质量的0.1%-0.5%;Step 1: First add formic acid, hydrogen peroxide and catalyst into the reactor, stir and heat up to 30-60°C, add 1-hexene to the reaction system and keep the temperature constant, react at a constant temperature for 0.5-2h, and then continue at room temperature Reaction 6-20h; wherein, the molar ratio of formic acid and 1-hexene is 1~12:1, the mass percentage of hydrogen peroxide in hydrogen peroxide is 10-50%, and the molar ratio of hydrogen peroxide and 1-hexene in hydrogen peroxide 1~8:1; the catalyst is MVO 2 dipic, and the catalyst dosage is 0.1%-0.5% of the mass of 1-hexene;
步骤二,将步骤一得到的混合物除去甲酸后经过水解、分离,得到1,2-己二醇。In step 2, the mixture obtained in step 1 is subjected to hydrolysis and separation after removing formic acid to obtain 1,2-hexanediol.
优选地,上述步骤一中甲酸与1-己烯的摩尔比为2~10:1。Preferably, in the above step 1, the molar ratio of formic acid to 1-hexene is 2-10:1.
优选地,上述双氧水中过氧化氢的质量百分数为20-40%。Preferably, the mass percentage of hydrogen peroxide in the above-mentioned hydrogen peroxide is 20-40%.
优选地,上述双氧水中过氧化氢与1-己烯的摩尔比为2~6:1。Preferably, the molar ratio of hydrogen peroxide to 1-hexene in the above hydrogen peroxide is 2-6:1.
优选地,上述催化剂用量为1-己烯质量的0.2%-0.4%。Preferably, the above-mentioned catalyst dosage is 0.2%-0.4% of the mass of 1-hexene.
进一步地,上述催化剂MVO2dipic的阳离子M+为NH4 +、Na+、K+、Cs+中的一种或者多种的混合;dipic为2,6-吡啶二羧酸配体;阴离子[VO2dipic]-的结构如下:Further, the cation M + of the above-mentioned catalyst MVO 2 dipic is a mixture of one or more of NH 4 + , Na + , K + , and Cs + ; dipic is a 2,6-pyridinedicarboxylic acid ligand; anion [ VO 2 dipic] - has the following structure:
进一步地,上述步骤一中搅拌的速度为300r/min-500r/min。Further, the stirring speed in the above step 1 is 300r/min-500r/min.
进一步地,上述催化剂MVO2dipic的制备方法为:称取V2O5、吡啶二羧酸在水中溶解,搅拌升温至70℃,保温4h,降温至室温,过滤,向滤液中加入质量分数为30%的双氧水,再加入饱和盐溶液至沉淀产生,其中,V2O5和吡啶二羧酸质量比为1:1~2,V2O5和水的质量比为1:10~50,V2O5和双氧水的质量比2~4:1,V2O5和相应饱和盐溶液质量比为1:1~3。然后,将溶液降至0℃,保温24h,过滤,洗涤,干燥,得到催化剂。Further, the preparation method of the above catalyst MVO 2 dipic is as follows: Weigh V 2 O 5 and dipicolinic acid and dissolve them in water, stir and heat up to 70° C., keep the temperature for 4 hours, cool down to room temperature, filter, and add to the filtrate the mass fraction of 30% hydrogen peroxide, then add saturated salt solution to precipitate, wherein, the mass ratio of V 2 O 5 and dipicolinic acid is 1:1~2, and the mass ratio of V 2 O 5 and water is 1:10~50, The mass ratio of V 2 O 5 and hydrogen peroxide is 2-4:1, and the mass ratio of V 2 O 5 and the corresponding saturated salt solution is 1: 1-3. Then, the solution was lowered to 0° C., incubated for 24 h, filtered, washed, and dried to obtain the catalyst.
进一步地,上述步骤二具体为,首先减压蒸出步骤一得到的混合物中甲酸,得到透明油状物,然后向油状物中边搅拌边加入20%-30%的氢氧化钠溶液,调pH=10~12;冷却至室温,保温2h后,加入盐酸调pH=7;再加入饱和食盐水静置分层,上层油相(产品),下层水相,水相用乙酸乙酯萃取,合并油相;开启搅拌、开启冷凝器。升温,常压蒸出乙酸乙酯,而后减压蒸馏出产品。Further, the above-mentioned step 2 is specifically as follows: first, the formic acid in the mixture obtained in the step 1 is evaporated under reduced pressure to obtain a transparent oily substance, and then a 20%-30% sodium hydroxide solution is added to the oily substance while stirring, and the pH= 10~12; Cool to room temperature, keep the temperature for 2 hours, add hydrochloric acid to adjust pH=7; then add saturated brine and let stand for stratification, the upper oil phase (product), the lower water phase, and the water phase are extracted with ethyl acetate, and the oils are combined. phase; turn on stirring, turn on condenser. The temperature was raised, the ethyl acetate was distilled off at atmospheric pressure, and then the product was distilled off under reduced pressure.
本发明的有益效果为:以MVO2dipic(M+=NH4 +、Na+、K+、Cs+)为催化剂,其中dipic为2,6-吡啶二羧酸配体,双氧水为氧化剂,催化氧化1-己烯制备合成1,2-己二醇,工艺合成方法中加入催化剂使反应时间缩短;甲酸与1-己烯的比例减小;双氧水的用量减少;工艺简单;反应条件温和,提高了反应效率。The beneficial effects of the invention are as follows: MVO 2 dipic (M + =NH 4 + , Na + , K + , Cs + ) is used as a catalyst, wherein dipic is a 2,6-pyridinedicarboxylic acid ligand, hydrogen peroxide is an oxidant, and the catalyst Oxidation of 1-hexene to prepare and synthesize 1,2-hexanediol, the addition of a catalyst in the process synthesis method shortens the reaction time; the ratio of formic acid to 1-hexene is reduced; the amount of hydrogen peroxide is reduced; the process is simple; the reaction conditions are mild, improve the reaction efficiency.
附图说明Description of drawings
图1为1,2-己二醇的1HNMR谱图。FIG. 1 is a 1 HNMR spectrum of 1,2-hexanediol.
图2为1,2-己二醇的GC谱图。Figure 2 is a GC spectrum of 1,2-hexanediol.
具体实施方式Detailed ways
下面通过实施例详述本发明的技术方案,但本发明的保护范围不限于此。The technical solutions of the present invention will be described in detail below through examples, but the protection scope of the present invention is not limited thereto.
本发明选择催化剂种类、原料的摩尔比、催化剂用量、反应温度、搅拌速度、双氧水浓度等作为1,2-己二醇的收率影响因素。In the present invention, catalyst types, molar ratio of raw materials, catalyst dosage, reaction temperature, stirring speed, hydrogen peroxide concentration, etc. are selected as factors influencing the yield of 1,2-hexanediol.
实施例1-6:不同催化剂的制备方法:称取V2O5、吡啶二羧酸在水中溶解,搅拌升温至70℃,保温4h,降温至室温,过滤,向滤液中加入质量分数为30%的双氧水,再加入饱和盐溶液至沉淀产生,然后,将溶液降至0℃,保温24h,过滤,洗涤,干燥,得到催化剂。具体用量见下表。Example 1-6: Preparation methods of different catalysts: Weigh V 2 O 5 and dipicolinic acid and dissolve them in water, stir and heat up to 70°C, keep the temperature for 4h, cool down to room temperature, filter, and add to the filtrate with a mass fraction of 30 % hydrogen peroxide, and then add saturated salt solution until precipitation occurs, then the solution is lowered to 0° C., incubated for 24 hours, filtered, washed, and dried to obtain the catalyst. The specific dosage is shown in the table below.
采用甲酸与1-己烯摩尔比为5:1,双氧水中过氧化氢与1-己烯的摩尔比为4:1进行实验,催化剂用量为0.25%,其中,混合催化剂的各组分比例为1:1,以400r/min速度搅拌升温至45℃后,以一定的速度向体系中加入1-己烯并保持温度恒定,恒温反应1h,然后在室温下继续反应10h。反应混合物除去甲酸后经过30%氢氧化钠溶液水解、分离后得到1,2-己二醇纯品。通过内标法计算1,2-己二醇的收率,如表所示The molar ratio of formic acid and 1-hexene was 5:1, and the molar ratio of hydrogen peroxide to 1-hexene in hydrogen peroxide was 4:1. The catalyst dosage was 0.25%, and the proportion of each component of the mixed catalyst was 1:1, stir at 400 r/min and heat up to 45 °C, add 1-hexene to the system at a certain speed and keep the temperature constant, react at constant temperature for 1 h, and then continue to react at room temperature for 10 h. After removing formic acid, the reaction mixture was hydrolyzed with 30% sodium hydroxide solution and separated to obtain pure 1,2-hexanediol. The yield of 1,2-hexanediol was calculated by the internal standard method, as shown in the table
表1催化剂种类对收率的影响Table 1 Influence of catalyst types on yield
实施例7-12:采用双氧水中过氧化氢与1-己烯的摩尔比为4:1,不同摩尔比的甲酸与1-己烯,进行实验,先将甲酸、浓度为30%的双氧水、催化剂②加入到反应器中,以400r/min速度搅拌升温至45℃后,以一定的速度向体系中加入1-己烯并保持温度恒定,恒温反应1h,然后在室温下继续反应10h。反应混合物除去甲酸后经过20%氢氧化钠溶液水解、分离后得到1,2-己二醇纯品。通过内标法计算1,2-己二醇的收率,如表2所示。Embodiment 7-12: adopt the molar ratio of hydrogen peroxide and 1-hexene in hydrogen peroxide to be 4:1, different molar ratios of formic acid and 1-hexene, carry out experiments, first mix formic acid, hydrogen peroxide with a concentration of 30%, Catalyst ② was added to the reactor, stirred at a speed of 400 r/min and heated to 45 °C, then added 1-hexene to the system at a certain speed and kept the temperature constant, reacted at a constant temperature for 1 h, and then continued the reaction at room temperature for 10 h. After removing formic acid, the reaction mixture was hydrolyzed and separated with 20% sodium hydroxide solution to obtain pure 1,2-hexanediol. The yield of 1,2-hexanediol was calculated by the internal standard method, as shown in Table 2.
表2不同比例的甲酸与1-己烯对收率的影响Table 2 Influence of different ratios of formic acid and 1-hexene on yield
实施例13-17:采用甲酸与1-己烯摩尔比为5:1,不同摩尔比的双氧水中过氧化氢与1-己烯进行实验,先将甲酸、浓度为30%的双氧水、催化剂③加入到反应器中,催化剂用量为0.25%,以400r/min速度搅拌升温至45℃后,以一定的速度向体系中加入1-己烯并保持温度恒定,恒温反应1h,然后在室温下继续反应10h。反应混合物除去甲酸后经过30%氢氧化钠溶液水解、分离后得到1,2-己二醇纯品。通过内标法计算1,2-己二醇的收率,如表3所示。Example 13-17: The mol ratio of formic acid and 1-hexene was 5:1, and the hydrogen peroxide and 1-hexene in different mol ratios were tested. It was added to the reactor with a catalyst dosage of 0.25%. After stirring at a speed of 400 r/min and heating up to 45 °C, 1-hexene was added to the system at a certain speed and the temperature was kept constant. The reaction was performed at a constant temperature for 1 h, and then continued at room temperature. Reaction for 10h. After removing formic acid, the reaction mixture was hydrolyzed with 30% sodium hydroxide solution and separated to obtain pure 1,2-hexanediol. The yield of 1,2-hexanediol was calculated by the internal standard method, as shown in Table 3.
表3不同比例的过氧化氢与1-己烯对收率的影响The influence of hydrogen peroxide and 1-hexene in different proportions of table 3 on yield
实施例18-23:采用甲酸与1-己烯摩尔比为5:1,双氧水中过氧化氢与1-己烯的摩尔比为4:1进行实验,先将甲酸、浓度为30%的双氧水、催化剂①加入到反应器中,催化剂用量为0.1%-0.5%,以400r/min速度搅拌升温至45℃后,以一定的速度向体系中加入1-己烯并保持温度恒定,恒温反应1h,然后在室温下继续反应10h。反应混合物除去甲酸后经过30%氢氧化钠溶液水解、分离后得到1,2-己二醇纯品。通过内标法计算1,2-己二醇的收率,如表4所示。虽然催化剂用量增加,但收率没有明显增加,因此催化剂较佳用量定为0.25%。Embodiment 18-23: adopt formic acid and 1-hexene molar ratio of 5: 1, hydrogen peroxide and 1-hexene molar ratio in hydrogen peroxide to be 4: 1 to carry out experiments, first formic acid, concentration of 30% hydrogen peroxide , Catalyst ① is added to the reactor, the amount of catalyst is 0.1%-0.5%, after stirring at a speed of 400r/min and heating up to 45 ℃, add 1-hexene to the system at a certain speed and keep the temperature constant, the constant temperature reaction is 1h , and then continued the reaction for 10 h at room temperature. After removing formic acid, the reaction mixture was hydrolyzed with 30% sodium hydroxide solution and separated to obtain pure 1,2-hexanediol. The yield of 1,2-hexanediol was calculated by the internal standard method, as shown in Table 4. Although the amount of catalyst increased, the yield did not increase significantly, so the preferred amount of catalyst was set at 0.25%.
表4不同催化剂用量对收率的影响Table 4 Influence of different catalyst dosage on yield
实施例24-26:采用甲酸与1-己烯摩尔比为5:1,双氧水中过氧化氢与1-己烯的摩尔比为4:1进行实验,先将甲酸、浓度为30%的双氧水、催化剂②加入到反应器中,催化剂用量为0.25%,以300r/min-500r/min的速度搅拌升温至45℃后,以一定的速度向体系中加入1-己烯并保持温度恒定,恒温反应1h,然后在室温下继续反应10h。反应混合物除去甲酸后经过30%氢氧化钠溶液水解、分离后得到1,2-己二醇纯品。通过内标法计算1,2-己二醇的收率,如表5所示。Embodiment 24-26: adopt formic acid and 1-hexene molar ratio of 5:1, hydrogen peroxide and 1-hexene molar ratio in hydrogen peroxide to be 4:1 to carry out experiments, first formic acid, concentration of 30% hydrogen peroxide , catalyst ② is added to the reactor, the catalyst dosage is 0.25%, after stirring at a speed of 300r/min-500r/min and heating up to 45 ℃, add 1-hexene to the system at a certain speed and keep the temperature constant, constant temperature The reaction was continued for 1 h and then continued at room temperature for 10 h. After removing formic acid, the reaction mixture was hydrolyzed with 30% sodium hydroxide solution and separated to obtain pure 1,2-hexanediol. The yield of 1,2-hexanediol was calculated by the internal standard method, as shown in Table 5.
表5不同搅拌速度对收率的影响Table 5 Influence of different stirring speeds on yield
实施例27-30:采用甲酸与1-己烯摩尔比为5:1,双氧水中过氧化氢与1-己烯的摩尔比为4:1进行实验,先将甲酸、浓度为30%的双氧水、催化剂④加入到反应器中,催化剂用量为0.25%,以400r/min的速度搅拌升温至30-60℃后,以一定的速度向体系中加入1-己烯并保持温度恒定,恒温反应1h,然后在室温下继续反应10h。反应混合物除去甲酸后经过30%氢氧化钠溶液水解、分离后得到1,2-己二醇纯品。通过内标法计算1,2-己二醇的收率,如表6所示。Example 27-30: The mol ratio of formic acid and 1-hexene was 5:1, and the molar ratio of hydrogen peroxide to 1-hexene in hydrogen peroxide was 4:1. First, formic acid and hydrogen peroxide with a concentration of 30% were used for the experiment. , catalyst ④ was added to the reactor, the amount of catalyst was 0.25%, after stirring at a speed of 400r/min and heating up to 30-60 ℃, 1-hexene was added to the system at a certain speed and the temperature was kept constant, and the reaction was held at a constant temperature for 1h , and then continued the reaction for 10 h at room temperature. After removing formic acid, the reaction mixture was hydrolyzed with 30% sodium hydroxide solution and separated to obtain pure 1,2-hexanediol. The yield of 1,2-hexanediol was calculated by the internal standard method, as shown in Table 6.
表6保温反应温度对收率的影响Table 6 Influence of holding reaction temperature on yield
实施例31-34:采用甲酸与1-己烯摩尔比为5:1,双氧水中过氧化氢与1-己烯的摩尔比为4:1进行实验,先将甲酸、浓度为30%的双氧水、催化剂③加入到反应器中,催化剂用量为0.25%,以400r/min的速度搅拌升温至45℃后,以一定的速度向体系中加入1-己烯并保持温度恒定,恒温反应1h,然后在室温下继续反应6-20h。反应混合物除去甲酸后经过30%氢氧化钠溶液水解、分离后得到1,2-己二醇纯品。通过内标法计算1,2-己二醇的收率,如表7所示。Embodiment 31-34: adopt formic acid and 1-hexene molar ratio to be 5:1, the molar ratio of hydrogen peroxide and 1-hexene in hydrogen peroxide to be 4:1 to carry out experiments, first formic acid, concentration of 30% hydrogen peroxide , catalyst ③ was added to the reactor, the amount of catalyst was 0.25%, after stirring at a speed of 400r/min and heating up to 45 ℃, 1-hexene was added to the system at a certain speed and the temperature was kept constant, and the reaction was performed at a constant temperature for 1h, and then The reaction was continued for 6-20 h at room temperature. After removing formic acid, the reaction mixture was hydrolyzed with 30% sodium hydroxide solution and separated to obtain pure 1,2-hexanediol. The yield of 1,2-hexanediol was calculated by the internal standard method, as shown in Table 7.
表7室温下搅拌时间对收率的影响Table 7 Influence of stirring time on yield at room temperature
实施例35-39:采用甲酸与1-己烯摩尔比为5:1,双氧水中过氧化氢与1-己烯的摩尔比为4:1进行实验,先将甲酸、浓度为10%-50%的双氧水、催化剂④加入到反应器中,催化剂用量为0.25%,以400r/min的速度搅拌升温至45℃后,以一定的速度向体系中加入1-己烯并保持温度恒定,恒温反应1h,然后在室温下继续反应10h。反应混合物除去甲酸后经过30%氢氧化钠溶液水解、分离后得到1,2-己二醇纯品。通过内标法计算1,2-己二醇的收率,如表8所示。Embodiment 35-39: adopt formic acid and 1-hexene molar ratio to be 5:1, the molar ratio of hydrogen peroxide and 1-hexene in hydrogen peroxide to be 4:1 to carry out experiments, first formic acid, concentration of 10%-50 % hydrogen peroxide and catalyst ④ were added to the reactor, and the amount of catalyst was 0.25%. After stirring at a speed of 400r/min and heating up to 45°C, 1-hexene was added to the system at a certain speed and the temperature was kept constant, and the reaction was carried out at a constant temperature. 1 h, and then continued the reaction for 10 h at room temperature. After removing formic acid, the reaction mixture was hydrolyzed with 30% sodium hydroxide solution and separated to obtain pure 1,2-hexanediol. The yield of 1,2-hexanediol was calculated by the internal standard method, as shown in Table 8.
表8双氧水浓度对收率的影响Table 8 Influence of hydrogen peroxide concentration on yield
实施例40-43:采用甲酸与1-己烯摩尔比为5:1,双氧水中过氧化氢与1-己烯的摩尔比为4:1进行实验,先将甲酸、浓度为30%的双氧水、催化剂②加入到反应器中,催化剂用量为0.25%,以400r/min的速度搅拌升温至45℃后,以一定的速度向体系中加入1-己烯并保持温度恒定,恒温反应0.5-2h,然后在室温下继续反应10h。反应混合物除去甲酸后经过30%氢氧化钠溶液水解、分离后得到1,2-己二醇纯品。通过内标法计算1,2-己二醇的收率,如表9所示。Example 40-43: The mol ratio of formic acid and 1-hexene was 5:1, and the molar ratio of hydrogen peroxide and 1-hexene in hydrogen peroxide was 4:1. First, formic acid and hydrogen peroxide with a concentration of 30% were used for experiments. , catalyst ② was added to the reactor, the catalyst dosage was 0.25%, after stirring at a speed of 400r/min and heating up to 45 ℃, 1-hexene was added to the system at a certain speed and the temperature was kept constant, and the constant temperature reaction was performed for 0.5-2h , and then continued the reaction for 10 h at room temperature. After removing formic acid, the reaction mixture was hydrolyzed with 30% sodium hydroxide solution and separated to obtain pure 1,2-hexanediol. The yield of 1,2-hexanediol was calculated by the internal standard method, as shown in Table 9.
表9恒温反应时间对收率的影响The influence of table 9 constant temperature reaction time on yield
Claims (6)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201711181264.1A CN107903146B (en) | 2017-11-23 | 2017-11-23 | A kind of method for preparing 1,2-hexanediol by catalytic oxidation of 1-hexene |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201711181264.1A CN107903146B (en) | 2017-11-23 | 2017-11-23 | A kind of method for preparing 1,2-hexanediol by catalytic oxidation of 1-hexene |
Publications (2)
Publication Number | Publication Date |
---|---|
CN107903146A CN107903146A (en) | 2018-04-13 |
CN107903146B true CN107903146B (en) | 2020-06-16 |
Family
ID=61847407
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201711181264.1A Active CN107903146B (en) | 2017-11-23 | 2017-11-23 | A kind of method for preparing 1,2-hexanediol by catalytic oxidation of 1-hexene |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN107903146B (en) |
Families Citing this family (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110590507A (en) * | 2018-06-12 | 2019-12-20 | 北京旭阳科技有限公司 | Method for preparing 1, 2-hexanediol by oxidizing 1-hexene |
CN110724116B (en) * | 2018-07-16 | 2023-10-24 | 东营市海科新源化工有限责任公司 | Preparation method and production system of vicinal diol compound |
CN110272329A (en) * | 2019-07-05 | 2019-09-24 | 乐平市瑞盛制药有限公司 | The preparation method of one kind 1,2- hexylene glycol |
Family Cites Families (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1228294C (en) * | 2002-06-12 | 2005-11-23 | 合肥丰乐科技有限责任公司 | Process for preparing 1,2-hexandiol |
KR101620925B1 (en) * | 2014-04-23 | 2016-05-17 | 광운대학교 산학협력단 | Process for preparing 1,2-hexanediol |
CN105646144B (en) * | 2014-12-03 | 2018-04-20 | 苏州亚培克生物科技有限公司 | A kind of preparation method of 1,2 aliphatic glycols |
-
2017
- 2017-11-23 CN CN201711181264.1A patent/CN107903146B/en active Active
Also Published As
Publication number | Publication date |
---|---|
CN107903146A (en) | 2018-04-13 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN101507917B (en) | Solid base catalyst for synthesis of alkanolamide compounds and preparation method thereof | |
CN108794400B (en) | A kind of cationic amino acid-containing ionic liquid containing amino acid and preparation method and application thereof | |
CN107903146B (en) | A kind of method for preparing 1,2-hexanediol by catalytic oxidation of 1-hexene | |
CN103447059B (en) | Preparation method of acetate hydrogenation catalyst | |
CN106045913B (en) | A kind of imidazoles perrhenate ions liquid and its preparation method and application with amino | |
CN101941958B (en) | Method for preparing 5-hydroxymethyl furfural and 2,5-furandimethanol simultaneously | |
CN108893204B (en) | Method for synthesizing refined lanolin by inert gas with water | |
CN103464157A (en) | Preparation method of acetic ester hydrogenation catalyst | |
CN107245065A (en) | A kind of method that catalytic hydrogenation ethyl levulinate prepares valerolactone | |
CN104418344B (en) | A kind of synthetic method of total silicon mesoporous material | |
CN110368987B (en) | Preparation method and application of tree-like loofah sponge supported ionic liquid catalyst | |
CN1461291A (en) | Method for isomerisation of alcohols | |
CN108752217B (en) | Synthesis method of dolutegravir key intermediate 2, 4-difluorobenzylamine | |
CN114011457B (en) | Preparation method of p-ethoxyphenol | |
CN114425438B (en) | Preparation method of titanium-containing catalyst, titanium-containing catalyst and method for preparing epoxy compound | |
CN111484415B (en) | A kind of preparation method of diisopropylethylamine | |
WO2012157578A1 (en) | Catalyst for producing alcohol compound or olefin compound, and method for producing alcohol compound or olefin compound | |
CN107216332A (en) | The synthetic method of (6H) the formic acid base ester of 7 methylol of the tert-butyl group, 7,8 dihydro 4H pyrazolos diazepine 5 | |
CN101125799B (en) | Method for synthesizing sandalwood | |
CN108546233B (en) | A method for preparing arylamines by semiconductor photocatalytic C-H activation | |
CN104926629B (en) | Domino reaction is utilized to prepare the green method of 3,3-diaryl acrylic aldehyde | |
CN112574007B (en) | A novel cycloheximide ionic liquid and method for catalyzing the synthesis of butyl citrate and bisphenol F | |
RU2290994C1 (en) | Catalyst, method for preparation thereof, and dihydroxyalkane production process | |
CN115772090B (en) | Synthesis method of chlorantraniliprole key intermediate | |
CN119528734B (en) | A CO2-based extended surfactant and its preparation method |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PB01 | Publication | ||
PB01 | Publication | ||
SE01 | Entry into force of request for substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
GR01 | Patent grant | ||
GR01 | Patent grant |