CN113563176B - A Cu(II)/nitric acid binary catalytic system catalyzes O2 oxidation of cyclohexene to synthesize adipic acid in one step - Google Patents
A Cu(II)/nitric acid binary catalytic system catalyzes O2 oxidation of cyclohexene to synthesize adipic acid in one step Download PDFInfo
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- WNLRTRBMVRJNCN-UHFFFAOYSA-N adipic acid Chemical compound OC(=O)CCCCC(O)=O WNLRTRBMVRJNCN-UHFFFAOYSA-N 0.000 title claims abstract description 177
- HGCIXCUEYOPUTN-UHFFFAOYSA-N cyclohexene Chemical compound C1CCC=CC1 HGCIXCUEYOPUTN-UHFFFAOYSA-N 0.000 title claims abstract description 164
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 title claims abstract description 88
- 239000001361 adipic acid Substances 0.000 title claims abstract description 88
- 235000011037 adipic acid Nutrition 0.000 title claims abstract description 88
- 229910017604 nitric acid Inorganic materials 0.000 title claims abstract description 88
- 230000003197 catalytic effect Effects 0.000 title claims abstract description 33
- 238000007254 oxidation reaction Methods 0.000 title abstract description 21
- 230000003647 oxidation Effects 0.000 title abstract description 20
- JPVYNHNXODAKFH-UHFFFAOYSA-N Cu2+ Chemical compound [Cu+2] JPVYNHNXODAKFH-UHFFFAOYSA-N 0.000 title description 21
- 238000006243 chemical reaction Methods 0.000 claims abstract description 283
- 238000003756 stirring Methods 0.000 claims abstract description 59
- 238000000034 method Methods 0.000 claims abstract description 34
- 230000002194 synthesizing effect Effects 0.000 claims abstract description 18
- 230000001590 oxidative effect Effects 0.000 claims abstract description 13
- 238000003786 synthesis reaction Methods 0.000 claims abstract description 10
- 230000015572 biosynthetic process Effects 0.000 claims abstract description 9
- 239000007800 oxidant agent Substances 0.000 claims abstract description 7
- 150000003839 salts Chemical class 0.000 claims abstract 4
- 239000010949 copper Substances 0.000 claims description 58
- 239000000126 substance Substances 0.000 claims description 8
- ZWAJLVLEBYIOTI-UHFFFAOYSA-N cyclohexene oxide Chemical compound C1CCCC2OC21 ZWAJLVLEBYIOTI-UHFFFAOYSA-N 0.000 claims description 5
- FWFSEYBSWVRWGL-UHFFFAOYSA-N cyclohexene oxide Natural products O=C1CCCC=C1 FWFSEYBSWVRWGL-UHFFFAOYSA-N 0.000 claims description 5
- 229910021591 Copper(I) chloride Inorganic materials 0.000 claims description 3
- OXBLHERUFWYNTN-UHFFFAOYSA-M copper(I) chloride Chemical compound [Cu]Cl OXBLHERUFWYNTN-UHFFFAOYSA-M 0.000 claims description 3
- 150000004677 hydrates Chemical class 0.000 claims description 3
- 230000035484 reaction time Effects 0.000 claims description 3
- JXSRRBVHLUJJFC-UHFFFAOYSA-N 7-amino-2-methylsulfanyl-[1,2,4]triazolo[1,5-a]pyrimidine-6-carbonitrile Chemical compound N1=CC(C#N)=C(N)N2N=C(SC)N=C21 JXSRRBVHLUJJFC-UHFFFAOYSA-N 0.000 claims description 2
- ZKXWKVVCCTZOLD-UHFFFAOYSA-N copper;4-hydroxypent-3-en-2-one Chemical compound [Cu].CC(O)=CC(C)=O.CC(O)=CC(C)=O ZKXWKVVCCTZOLD-UHFFFAOYSA-N 0.000 claims description 2
- QYCVHILLJSYYBD-UHFFFAOYSA-L copper;oxalate Chemical compound [Cu+2].[O-]C(=O)C([O-])=O QYCVHILLJSYYBD-UHFFFAOYSA-L 0.000 claims description 2
- 239000000203 mixture Substances 0.000 claims description 2
- 238000001308 synthesis method Methods 0.000 claims 1
- 230000008569 process Effects 0.000 abstract description 5
- 238000010438 heat treatment Methods 0.000 abstract 1
- 238000007789 sealing Methods 0.000 abstract 1
- KDYFGRWQOYBRFD-UHFFFAOYSA-N succinic acid Chemical compound OC(=O)CCC(O)=O KDYFGRWQOYBRFD-UHFFFAOYSA-N 0.000 description 90
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 87
- 239000001301 oxygen Substances 0.000 description 87
- 229910052760 oxygen Inorganic materials 0.000 description 87
- RTBFRGCFXZNCOE-UHFFFAOYSA-N 1-methylsulfonylpiperidin-4-one Chemical compound CS(=O)(=O)N1CCC(=O)CC1 RTBFRGCFXZNCOE-UHFFFAOYSA-N 0.000 description 45
- JFCQEDHGNNZCLN-UHFFFAOYSA-N anhydrous glutaric acid Natural products OC(=O)CCCC(O)=O JFCQEDHGNNZCLN-UHFFFAOYSA-N 0.000 description 45
- 239000001384 succinic acid Substances 0.000 description 45
- 239000007795 chemical reaction product Substances 0.000 description 44
- -1 polytetrafluoroethylene Polymers 0.000 description 44
- 229920001343 polytetrafluoroethylene Polymers 0.000 description 44
- 239000004810 polytetrafluoroethylene Substances 0.000 description 44
- 229910001220 stainless steel Inorganic materials 0.000 description 44
- 239000010935 stainless steel Substances 0.000 description 44
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 15
- MWUXSHHQAYIFBG-UHFFFAOYSA-N nitrogen oxide Inorganic materials O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 description 15
- 238000002474 experimental method Methods 0.000 description 5
- 238000005984 hydrogenation reaction Methods 0.000 description 5
- 238000009776 industrial production Methods 0.000 description 5
- 238000004519 manufacturing process Methods 0.000 description 5
- 239000003054 catalyst Substances 0.000 description 4
- 230000000052 comparative effect Effects 0.000 description 4
- HPXRVTGHNJAIIH-UHFFFAOYSA-N cyclohexanol Chemical compound OC1CCCCC1 HPXRVTGHNJAIIH-UHFFFAOYSA-N 0.000 description 4
- 239000002253 acid Substances 0.000 description 3
- 229910002089 NOx Inorganic materials 0.000 description 2
- 125000001931 aliphatic group Chemical group 0.000 description 2
- 239000006227 byproduct Substances 0.000 description 2
- 238000006555 catalytic reaction Methods 0.000 description 2
- JHIVVAPYMSGYDF-UHFFFAOYSA-N cyclohexanone Chemical compound O=C1CCCCC1 JHIVVAPYMSGYDF-UHFFFAOYSA-N 0.000 description 2
- 238000005265 energy consumption Methods 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 230000006872 improvement Effects 0.000 description 2
- 239000000047 product Substances 0.000 description 2
- 238000013341 scale-up Methods 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- MGWGWNFMUOTEHG-UHFFFAOYSA-N 4-(3,5-dimethylphenyl)-1,3-thiazol-2-amine Chemical compound CC1=CC(C)=CC(C=2N=C(N)SC=2)=C1 MGWGWNFMUOTEHG-UHFFFAOYSA-N 0.000 description 1
- 229920002302 Nylon 6,6 Polymers 0.000 description 1
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 description 1
- 150000007513 acids Chemical class 0.000 description 1
- 150000001336 alkenes Chemical class 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000003889 chemical engineering Methods 0.000 description 1
- 239000003153 chemical reaction reagent Substances 0.000 description 1
- 150000001925 cycloalkenes Chemical class 0.000 description 1
- 235000014113 dietary fatty acids Nutrition 0.000 description 1
- 239000000975 dye Substances 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 229930195729 fatty acid Natural products 0.000 description 1
- 239000000194 fatty acid Substances 0.000 description 1
- 150000004665 fatty acids Chemical class 0.000 description 1
- 239000000796 flavoring agent Substances 0.000 description 1
- 235000019634 flavors Nutrition 0.000 description 1
- 235000013373 food additive Nutrition 0.000 description 1
- 239000002778 food additive Substances 0.000 description 1
- 239000003205 fragrance Substances 0.000 description 1
- 239000013067 intermediate product Substances 0.000 description 1
- 230000002427 irreversible effect Effects 0.000 description 1
- 239000010687 lubricating oil Substances 0.000 description 1
- JCXJVPUVTGWSNB-UHFFFAOYSA-N nitrogen dioxide Inorganic materials O=[N]=O JCXJVPUVTGWSNB-UHFFFAOYSA-N 0.000 description 1
- 239000012450 pharmaceutical intermediate Substances 0.000 description 1
- 239000004014 plasticizer Substances 0.000 description 1
- 229920002635 polyurethane Polymers 0.000 description 1
- 239000004814 polyurethane Substances 0.000 description 1
- 239000002243 precursor Substances 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 238000004904 shortening Methods 0.000 description 1
- 229910052723 transition metal Inorganic materials 0.000 description 1
- 150000003624 transition metals Chemical class 0.000 description 1
Classifications
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- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C51/00—Preparation of carboxylic acids or their salts, halides or anhydrides
- C07C51/16—Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation
- C07C51/31—Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation of cyclic compounds with ring-splitting
- C07C51/313—Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation of cyclic compounds with ring-splitting with molecular oxygen
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Abstract
Description
技术领域technical field
本发明属于工业催化和精细有机合成领域,具体涉及一种Cu(II)/硝酸二元催化体系催化O2氧化环己烯一步合成己二酸的方法。The invention belongs to the field of industrial catalysis and fine organic synthesis, and specifically relates to a method for synthesizing adipic acid in one step by catalyzing O2 oxidation of cyclohexene by a Cu(II)/nitric acid binary catalytic system.
背景技术Background technique
己二酸,又名肥酸(简称AA),分子式HOOC(CH2)4COOH,是脂肪族二元酸中最有应用价值的二元酸,主要用于合成尼龙66、聚氨脂和增塑剂。另外,己二酸还可用于生产高级润滑油、食品添加剂、医药中间体、香精香料、染料等。(化学工程, 2013, 41(07): 42-44+49.)。目前,己二酸的年产量约为300万吨,说明了己二酸作为工业前体的重要性。在未来的市场中,己二酸需求量仍然会持续增长(European Journal of Inorganic Chemistry,2020(03): 248–252)。目前,工业上己二酸的生产工艺主要包括苯完全氢化氧化法和苯部分氢化氧化法。其中,苯部分氢化氧化法以苯为原料,经部分加氢得到环己烯,进一步水合得到中间产物环己醇。环己醇经硝酸催化氧化合成己二酸。该工艺存在的问题:(1)反应路径较长,转化率降低,能耗增加,生产成本提高。(2)采用硝酸催化氧化环己醇得到己二酸,会造成大量氮氧化物(0.3 t/1 t己二酸)的排放,对臭氧层和环境造成不可逆的破坏。因此,有效缩短工业生产的工艺路线,并采用合适、高效的催化剂直接催化氧化环己烯,一步合成己二酸,并减少硝酸的使用,将有利于苯部分氢化氧化法生产己二酸效率的提高,也有利于降低和减少工业生产成本和NOx气体的排放。该设计思路将是工业上己二酸工业合成领域一项十分新颖并且应用意义极大的工艺改进。Adipic acid, also known as fatty acid (AA for short), with molecular formula HOOC(CH 2 ) 4 COOH, is the most valuable dibasic acid among aliphatic dibasic acids, mainly used in the synthesis of nylon 66, polyurethane and plasticizer. In addition, adipic acid can also be used to produce high-grade lubricating oil, food additives, pharmaceutical intermediates, flavors and fragrances, dyes, etc. (Chemical Engineering, 2013, 41(07): 42-44+49.). Currently, the annual production of adipic acid is about 3 million tons, illustrating the importance of adipic acid as an industrial precursor. In the future market, the demand for adipic acid will continue to grow (European Journal of Inorganic Chemistry, 2020(03): 248–252). At present, the industrial production process of adipic acid mainly includes benzene complete hydrogenation oxidation method and benzene partial hydrogenation oxidation method. Among them, the benzene partial hydrogenation oxidation method uses benzene as a raw material, undergoes partial hydrogenation to obtain cyclohexene, and further hydrates to obtain the intermediate product cyclohexanol. Cyclohexanol is catalyzed by nitric acid to synthesize adipic acid. Problems in this process: (1) The reaction path is long, the conversion rate is reduced, the energy consumption is increased, and the production cost is increased. (2) Using nitric acid to catalyze the oxidation of cyclohexanol to obtain adipic acid will cause a large amount of nitrogen oxides (0.3 t/1 t adipic acid) to be emitted, causing irreversible damage to the ozone layer and the environment. Therefore, effectively shortening the process route of industrial production, and adopting a suitable and efficient catalyst to directly catalyze the oxidation of cyclohexene, one-step synthesis of adipic acid, and reducing the use of nitric acid will help to improve the efficiency of adipic acid production by the partial hydrogenation oxidation of benzene Improvement is also conducive to reducing and reducing industrial production costs and emissions of NOx gases. This design idea will be a very novel process improvement in the industrial adipic acid synthesis field with great application significance.
O2作为最符合绿色化学理念的氧化剂,其氧化副产物为H2O,对环境不会产生影响且价格便宜容易得到,原子经济性高,是最具发展前景的氧化剂。硝酸为工业中常用的氧化剂,能够有效将环己醇,环己酮氧化到己二酸,但是会产生氮氧化物NOx。Cu(II)作为一种常用过渡金属,具有催化氧化反应的能力,能够促使反应的进行(Catalysis Today, 2020,346: 40–45)。O 2 is the oxidizing agent most in line with the concept of green chemistry. Its oxidation by-product is H 2 O. It has no impact on the environment, is cheap and easy to obtain, and has high atom economy. It is the most promising oxidizing agent. Nitric acid is an oxidizing agent commonly used in industry, which can effectively oxidize cyclohexanol and cyclohexanone to adipic acid, but will produce nitrogen oxides NO x . As a commonly used transition metal, Cu(II) has the ability to catalyze oxidation reactions and can promote the reaction (Catalysis Today, 2020, 346: 40–45).
因此,本发明以Cu(II)/催化量的硝酸组成二元催化氧化体系,以Cu(II)为催化剂,硝酸为直接氧化剂,直接氧化环己烯一步合成己二酸。同时在水存在的环境中,O2氧化生成的氮氧化物NOx制备二氧化氮,重新得到氧化性的硝酸,进入氧化环己烯的循环。本发明Cu(II)/硝酸二元催化体系催化O2氧化环己烯合成己二酸的方法具有收率高,反应路线较短,氮氧化物NOx排放少,反应温度低,环境影响小,生产成本低等优势。另外,本发明采用的催化剂廉价易得,可以大幅降低工业生产成本。本发明提供了一种高效、可行、绿色的环己烯直接催化氧化一步合成己二酸的方法。Therefore, the present invention uses Cu(II)/catalytic amount of nitric acid to form a binary catalytic oxidation system, uses Cu(II) as a catalyst, and nitric acid as a direct oxidant to directly oxidize cyclohexene to synthesize adipic acid in one step. At the same time, in the environment where water exists, nitrogen oxides NO x produced by O2 oxidation produce nitrogen dioxide, and oxidative nitric acid is obtained again, which enters the cycle of cyclohexene oxide. The Cu(II)/nitric acid binary catalytic system of the present invention catalyzes the method for O2 oxidation of cyclohexene to synthesize adipic acid, which has high yield, short reaction route, less emission of nitrogen oxides NOx , low reaction temperature, and small environmental impact , low production cost and other advantages. In addition, the catalyst used in the invention is cheap and easy to obtain, which can greatly reduce the cost of industrial production. The invention provides an efficient, feasible and green method for synthesizing adipic acid in one step through the direct catalytic oxidation of cyclohexene.
发明内容Contents of the invention
针对现有技术存在的上述技术问题,本发明的目的在于提供一种Cu(II)/硝酸二元催化体系催化O2氧化环己烯一步合成己二酸的方法。For the above-mentioned technical problem that prior art exists, the object of the present invention is to provide a kind of Cu(II)/nitric acid binary catalytic system catalyzes O oxidative cyclohexene one - step method for the synthesis of adipic acid.
所述的一种Cu(II)/硝酸二元催化体系催化O2氧化环己烯一步合成己二酸的方法,其特征在于,将硝酸和Cu(II)盐分散于环己烯中,密封反应体系,搅拌升温至反应温度后,通入氧化剂O2至反应压力下进行搅拌反应,生成目标己二酸产物,以及少量的戊二酸和丁二酸产物。Described a kind of Cu(II)/nitric acid binary catalytic system catalyzes O The method for synthesizing adipic acid in one step from cyclohexene, it is characterized in that nitric acid and Cu(II) salt are dispersed in cyclohexene, sealed After the reaction system is heated up to the reaction temperature with stirring, the oxidant O2 is introduced to the reaction pressure to carry out the stirring reaction to generate the target adipic acid product, and a small amount of glutaric acid and succinic acid products.
所述的一种Cu(II)/硝酸二元催化体系催化O2氧化环己烯一步合成己二酸的方法,其特征在于,所述Cu(II)盐为Cu(CH3COO)2、Cu(NO3)2、CuSO4、CuCl2、硬脂酸铜、草酸铜、乙酰丙酮铜及其水合物中的至少一种或两种以上任意比例的混合物。The method for one-step synthesis of adipic acid by catalyzing O2 oxidation of cyclohexene by the Cu(II)/nitric acid binary catalytic system is characterized in that the Cu(II) salt is Cu(CH3COO )2 , At least one of Cu(NO 3 ) 2 , CuSO 4 , CuCl 2 , copper stearate, copper oxalate, copper acetylacetonate and their hydrates, or a mixture of two or more in any proportion.
所述的一种Cu(II)/硝酸二元催化体系催化O2氧化环己烯一步合成己二酸的方法,其特征在于,所述硝酸浓度为3.0~15.0 mol/L,优选为6.0~13.0mol/L;硝酸体积与环己烯的物质的量之比为1:0.2~10,优选为1:0.5~2.0,体积的单位是L,物质的量单位是mol。Described a kind of Cu(II)/nitric acid binary catalytic system catalyzes O The method for synthesizing adipic acid in one step from cyclohexene, it is characterized in that, described nitric acid concentration is 3.0~15.0 mol/L, is preferably 6.0~ 13.0mol/L; the ratio of the volume of nitric acid to the amount of substance of cyclohexene is 1:0.2~10, preferably 1:0.5~2.0, the unit of volume is L, and the unit of amount of substance is mol.
所述的一种Cu(II)/硝酸二元催化体系催化O2氧化环己烯一步合成己二酸的方法,其特征在于,所述Cu(II)盐与环己烯的物质的量之比是1:10~10000,优选为1:100~1000。Described a kind of Cu(II)/nitric acid binary catalytic system catalyzes O The method for synthesizing adipic acid in one step of oxidized cyclohexene, it is characterized in that, the amount of substance of described Cu(II) salt and cyclohexene The ratio is 1:10~10000, preferably 1:100~1000.
所述的一种Cu(II)/硝酸二元催化体系催化O2氧化环己烯一步合成己二酸的方法,其特征在于,所述反应温度为40~120℃,优选45~70℃。The method for one-step synthesis of adipic acid by catalyzing O2 oxidation of cyclohexene by the Cu(II)/nitric acid binary catalytic system is characterized in that the reaction temperature is 40-120°C, preferably 45-70°C.
所述的一种Cu(II)/硝酸二元催化体系催化O2氧化环己烯一步合成己二酸的方法,其特征在于,所述反应压力为0.10~2.0 MPa,优选为0.2~1.6MPa。Described a kind of Cu(II)/nitric acid binary catalytic system catalyzes O The method for synthesizing adipic acid in one step from cyclohexene, it is characterized in that, described reaction pressure is 0.10~2.0 MPa, is preferably 0.2~1.6MPa .
所述的一种Cu(II)/硝酸二元催化体系催化O2氧化环己烯一步合成己二酸的方法,其特征在于,所述搅拌的速率为100~1000 rpm,优选为200~700rpm。Described a kind of Cu(II)/nitric acid binary catalytic system catalyzes O The method for synthesizing adipic acid in one step from oxidized cyclohexene, it is characterized in that, the speed of described stirring is 100~1000 rpm, is preferably 200~700rpm .
所述的一种Cu(II)/硝酸二元催化体系催化O2氧化环己烯一步合成己二酸的方法,其特征在于,所述反应时间为2.0~24.0 h,优选为6.0~16.0h。Described a kind of Cu(II)/nitric acid binary catalytic system catalyzes O The method for synthesizing adipic acid in one step from cyclohexene, it is characterized in that, the reaction time is 2.0~24.0 h, preferably 6.0~16.0h .
本发明以Cu(II)/硝酸二元催化体系催化O2氧化环己烯一步合成己二酸,不仅有效地缩短了工艺路线,降低了能耗,减少了成本,而且实现了硝酸氧化环己烯产生的NO与氧气进一步反应生成NO2,而NO2又溶于水形成硝酸溶液,实现了硝酸的循环使用,减少了副产物的生成,减少了环境污染物NOx气体的排放,符合目前化学工业对“节能减排”的现实需求。本发明不仅提供了一种环己烯高效、绿色氧化合成环己二酸的方法,对其它环烯烃类C=C键催化氧化,高效制备脂肪族二酸也具有一定的参考价值。The present invention uses the Cu(II)/nitric acid binary catalytic system to catalyze O2 to oxidize cyclohexene to synthesize adipic acid in one step, which not only effectively shortens the process route, reduces energy consumption, and reduces costs, but also realizes the nitric acid oxidation of cyclohexene The NO produced by alkenes further reacts with oxygen to form NO 2 , and NO 2 is dissolved in water to form a nitric acid solution, which realizes the recycling of nitric acid, reduces the generation of by-products, and reduces the emission of environmental pollutant NO x gas, which is in line with the current The realistic demand of the chemical industry for "energy saving and emission reduction". The invention not only provides a method for efficiently and greenly oxidizing cyclohexene to synthesize cycloadipic acid, but also has certain reference value for the efficient preparation of aliphatic diacids by catalytic oxidation of C=C bonds of other cycloalkenes.
本发明的有益效果主要体现在:本发明Cu(II)/硝酸二元催化体系催化O2氧化环己烯一步合成己二酸的方法,具有收率高,反应路线较短,氮氧化物NOx排放少,反应温度低,环境影响小,生产成本低等优势。另外,本发明采用的催化剂(即Cu(II)/硝酸二元催化体系)廉价易得,可以大幅降低工业生产成本。本发明提供了一种高效、可行、绿色的环己烯催化氧化一步合成己二酸的方法。The beneficial effects of the present invention are mainly reflected in: the Cu(II)/nitric acid binary catalytic system of the present invention catalyzes O The method for the one-step synthesis of adipic acid by oxidizing cyclohexene has high yield, short reaction route, and nitrogen oxide NO X emission is less, the reaction temperature is low, the environmental impact is small, and the production cost is low. In addition, the catalyst used in the present invention (namely the Cu(II)/nitric acid binary catalytic system) is cheap and easy to obtain, which can greatly reduce the cost of industrial production. The invention provides an efficient, feasible and green method for synthesizing adipic acid in one step through catalytic oxidation of cyclohexene.
具体实施方式detailed description
下面结合具体实施例对本发明作进一步说明,但本发明的保护范围并不限于此。The present invention will be further described below in conjunction with specific examples, but the protection scope of the present invention is not limited thereto.
本发明的实施例中所用试剂均为市售分析纯。All reagents used in the examples of the present invention are commercially available analytically pure.
实施例1~实施例40为环己烯的催化氧化案例;Embodiment 1~embodiment 40 is the catalytic oxidation case of cyclohexene;
实施例41~实施例43为对比实验案例;Embodiment 41 ~ embodiment 43 are comparative experimental cases;
实施例44为放大实验。Embodiment 44 is a scale-up experiment.
实施例1Example 1
在100 mL具有聚四氟乙烯内胆的不锈钢高压反应釜中,将8.2140 g (100 mmol)环己烯和0.1997 g无水Cu(CH3COO)2 (0.01equive)分散于50 mL摩尔浓度为11 mol/L硝酸溶液中,密封反应釜,搅拌升温到60℃反应温度、通入氧气至压力为1.0 MPa。于60℃反应温度、1.0 MPa 氧气压力,500 rpm搅拌反应12.0 h。反应完毕,冷却至室温,对反应产物进行分析检测,反应结果为:己二酸收率81%,戊二酸收率5%,丁二酸收率4%。In a 100 mL stainless steel autoclave with a polytetrafluoroethylene liner, 8.2140 g (100 mmol) cyclohexene and 0.1997 g anhydrous Cu(CH 3 COO) 2 (0.01 equive) were dispersed in 50 mL with a molar concentration of 11 mol/L nitric acid solution, seal the reaction vessel, stir and raise the temperature to 60°C reaction temperature, and feed oxygen until the pressure is 1.0 MPa. The reaction temperature was 60°C, the oxygen pressure was 1.0 MPa, and the reaction was stirred at 500 rpm for 12.0 h. After the reaction was completed, it was cooled to room temperature, and the reaction product was analyzed and detected. The reaction results were as follows: the yield of adipic acid was 81%, the yield of glutaric acid was 5%, and the yield of succinic acid was 4%.
实施例2Example 2
在100 mL具有聚四氟乙烯内胆的不锈钢高压反应釜中,将8.2140 g (100 mmol)环己烯和0.1876 g无水Cu(NO3)2 (0.01equive)分散于50 mL摩尔浓度为11 mol/L硝酸溶液中,密封反应釜,搅拌升温到60℃反应温度、通入氧气至压力为1.0 MPa。于60℃反应温度、1.0 MPa 氧气压力,500 rpm搅拌反应12.0 h。反应完毕,冷却至室温,对反应产物进行分析检测,反应结果为:己二酸收率71%,戊二酸收率10%,丁二酸收率3%。In a 100 mL stainless steel autoclave with a polytetrafluoroethylene liner, 8.2140 g (100 mmol) cyclohexene and 0.1876 g anhydrous Cu(NO 3 ) 2 (0.01 equive) were dispersed in 50 mL with a molar concentration of 11 mol/L nitric acid solution, seal the reaction vessel, heat up to 60°C reaction temperature with stirring, and feed oxygen until the pressure is 1.0 MPa. The reaction temperature was 60°C, the oxygen pressure was 1.0 MPa, and the reaction was stirred at 500 rpm for 12.0 h. After the reaction was completed, it was cooled to room temperature, and the reaction product was analyzed and detected. The reaction results were as follows: the yield of adipic acid was 71%, the yield of glutaric acid was 10%, and the yield of succinic acid was 3%.
实施例3Example 3
在100 mL具有聚四氟乙烯内胆的不锈钢高压反应釜中,将8.2140 g (100 mmol)环己烯和0.1345 g无水CuCl2 (0.01equive)分散于50 mL摩尔浓度为11 mol/L硝酸溶液中,密封反应釜,搅拌升温到60℃反应温度、通入氧气至压力为1.0 MPa。于60℃反应温度、1.0 MPa 氧气压力,500 rpm搅拌反应12.0 h。反应完毕,冷却至室温,对反应产物进行分析检测,反应结果为:己二酸收率68%,戊二酸收率11%,丁二酸收率3%。In a 100 mL stainless steel autoclave with polytetrafluoroethylene liner, 8.2140 g (100 mmol) cyclohexene and 0.1345 g anhydrous CuCl 2 (0.01 equive) were dispersed in 50 mL of nitric acid with a molar concentration of 11 mol/L solution, seal the reaction kettle, stir and heat up to 60°C reaction temperature, and feed oxygen to a pressure of 1.0 MPa. The reaction temperature was 60°C, the oxygen pressure was 1.0 MPa, and the reaction was stirred at 500 rpm for 12.0 h. After the reaction was completed, it was cooled to room temperature, and the reaction product was analyzed and detected. The reaction results were as follows: the yield of adipic acid was 68%, the yield of glutaric acid was 11%, and the yield of succinic acid was 3%.
实施例4Example 4
在100 mL具有聚四氟乙烯内胆的不锈钢高压反应釜中,将8.2140 g (100 mmol)环己烯和0.1596 g无水CuSO4 (0.01equive)分散于50 mL摩尔浓度为11 mol/L硝酸溶液中,密封反应釜,搅拌升温到60℃反应温度、通入氧气至压力为1.0 MPa。于60℃反应温度、1.0 MPa 氧气压力,500 rpm搅拌反应12.0 h。反应完毕,冷却至室温,对反应产物进行分析检测,反应结果为:己二酸收率67%,戊二酸收率10%,丁二酸收率2%。In a 100 mL stainless steel autoclave with a polytetrafluoroethylene liner, 8.2140 g (100 mmol) cyclohexene and 0.1596 g anhydrous CuSO 4 (0.01 equive) were dispersed in 50 mL of nitric acid with a molar concentration of 11 mol/L solution, seal the reaction kettle, stir and heat up to 60°C reaction temperature, and feed oxygen to a pressure of 1.0 MPa. The reaction temperature was 60°C, the oxygen pressure was 1.0 MPa, and the reaction was stirred at 500 rpm for 12.0 h. After the reaction was completed, it was cooled to room temperature, and the reaction product was analyzed and detected. The reaction results were as follows: the yield of adipic acid was 67%, the yield of glutaric acid was 10%, and the yield of succinic acid was 2%.
实施例5Example 5
在100 mL具有聚四氟乙烯内胆的不锈钢高压反应釜中,将8.2140 g (100 mmol)环己烯和0.1997 g无水Cu(CH3COO)2 (0.01equive)分散于50 mL摩尔浓度为6 mol/L硝酸溶液中,密封反应釜,搅拌升温到60℃反应温度、通入氧气至压力为1.0 MPa。于60℃反应温度、1.0 MPa 氧气压力,500 rpm搅拌反应12.0 h。反应完毕,冷却至室温,对反应产物进行分析检测,反应结果为:己二酸收率59%,戊二酸收率5%,丁二酸收率1%。In a 100 mL stainless steel autoclave with a polytetrafluoroethylene liner, 8.2140 g (100 mmol) cyclohexene and 0.1997 g anhydrous Cu(CH 3 COO) 2 (0.01 equive) were dispersed in 50 mL with a molar concentration of 6 mol/L nitric acid solution, seal the reaction vessel, heat up to 60°C reaction temperature with stirring, and feed oxygen until the pressure is 1.0 MPa. The reaction temperature was 60°C, the oxygen pressure was 1.0 MPa, and the reaction was stirred at 500 rpm for 12.0 h. After the reaction was completed, it was cooled to room temperature, and the reaction product was analyzed and detected. The reaction results were as follows: the yield of adipic acid was 59%, the yield of glutaric acid was 5%, and the yield of succinic acid was 1%.
实施例6Example 6
在100 mL具有聚四氟乙烯内胆的不锈钢高压反应釜中,将8.2140 g (100 mmol)环己烯和0.1997 g无水Cu(CH3COO)2分散于50 mL摩尔浓度为7 mol/L硝酸溶液中,密封反应釜,搅拌升温到60℃反应温度、通入氧气至压力为1.0 MPa。于60℃反应温度、1.0 MPa 氧气压力,500 rpm搅拌反应12.0 h。反应完毕,冷却至室温,对反应产物进行分析检测,反应结果为:己二酸收率61%,戊二酸收率6%,丁二酸收率1%。In a 100 mL stainless steel autoclave with polytetrafluoroethylene liner, 8.2140 g (100 mmol) cyclohexene and 0.1997 g anhydrous Cu(CH3COO) 2 were dispersed in 50 mL with a molar concentration of 7 mol/L In the nitric acid solution, seal the reaction kettle, stir and heat up to the reaction temperature of 60°C, and feed oxygen until the pressure is 1.0 MPa. The reaction temperature was 60°C, the oxygen pressure was 1.0 MPa, and the reaction was stirred at 500 rpm for 12.0 h. After the reaction was completed, it was cooled to room temperature, and the reaction product was analyzed and detected. The reaction results were as follows: the yield of adipic acid was 61%, the yield of glutaric acid was 6%, and the yield of succinic acid was 1%.
实施例7Example 7
在100 mL具有聚四氟乙烯内胆的不锈钢高压反应釜中,将8.2140 g (100 mmol)环己烯和0.1997 g无水Cu(CH3COO)2分散于50 mL摩尔浓度为8 mol/L硝酸溶液中,密封反应釜,搅拌升温到60℃反应温度、通入氧气至压力为1.0 MPa。于60℃反应温度、1.0 MPa 氧气压力,500 rpm搅拌反应12.0 h。反应完毕,冷却至室温,对反应产物进行分析检测,反应结果为:己二酸收率65%,戊二酸收率6%,丁二酸收率2%。In a 100 mL stainless steel autoclave with polytetrafluoroethylene liner, 8.2140 g (100 mmol) cyclohexene and 0.1997 g anhydrous Cu(CH3COO) 2 were dispersed in 50 mL with a molar concentration of 8 mol/L In the nitric acid solution, seal the reaction kettle, stir and heat up to the reaction temperature of 60°C, and feed oxygen until the pressure is 1.0 MPa. The reaction temperature was 60°C, the oxygen pressure was 1.0 MPa, and the reaction was stirred at 500 rpm for 12.0 h. After the reaction was completed, it was cooled to room temperature, and the reaction product was analyzed and detected. The reaction results were as follows: the yield of adipic acid was 65%, the yield of glutaric acid was 6%, and the yield of succinic acid was 2%.
实施例8Example 8
在100 mL具有聚四氟乙烯内胆的不锈钢高压反应釜中,将8.2140 g (100 mmol)环己烯和0.1997 g无水Cu(CH3COO)2分散于50 mL摩尔浓度为9 mol/L硝酸溶液中,密封反应釜,搅拌升温到60℃反应温度、通入氧气至压力为1.0 MPa。于60℃反应温度、1.0 MPa 氧气压力,500 rpm搅拌反应12.0 h。反应完毕,冷却至室温,对反应产物进行分析检测,反应结果为:己二酸收率70%,戊二酸收率6%,丁二酸收率2%。In a 100 mL stainless steel autoclave with a polytetrafluoroethylene liner, 8.2140 g (100 mmol) cyclohexene and 0.1997 g anhydrous Cu(CH3COO) 2 were dispersed in 50 mL with a molar concentration of 9 mol/L In the nitric acid solution, seal the reaction kettle, stir and heat up to the reaction temperature of 60°C, and feed oxygen until the pressure is 1.0 MPa. The reaction temperature was 60°C, the oxygen pressure was 1.0 MPa, and the reaction was stirred at 500 rpm for 12.0 h. After the reaction was completed, it was cooled to room temperature, and the reaction product was analyzed and detected. The reaction results were as follows: the yield of adipic acid was 70%, the yield of glutaric acid was 6%, and the yield of succinic acid was 2%.
实施例9Example 9
在100 mL具有聚四氟乙烯内胆的不锈钢高压反应釜中,将8.2140 g (100 mmol)环己烯和0.1997 g无水Cu(CH3COO)2分散于50 mL摩尔浓度为10 mol/L硝酸溶液中,密封反应釜,搅拌升温到60℃反应温度、通入氧气至压力为1.0 MPa。于60℃反应温度、1.0 MPa 氧气压力,500 rpm搅拌反应12.0 h。反应完毕,冷却至室温,对反应产物进行分析检测,反应结果为:己二酸收率72%,戊二酸收率6%,丁二酸收率3%。In a 100 mL stainless steel autoclave with polytetrafluoroethylene liner, 8.2140 g (100 mmol) cyclohexene and 0.1997 g anhydrous Cu(CH3COO) 2 were dispersed in 50 mL with a molar concentration of 10 mol/L In the nitric acid solution, seal the reaction kettle, stir and heat up to the reaction temperature of 60°C, and feed oxygen until the pressure is 1.0 MPa. The reaction temperature was 60°C, the oxygen pressure was 1.0 MPa, and the reaction was stirred at 500 rpm for 12.0 h. After the reaction was completed, it was cooled to room temperature, and the reaction product was analyzed and detected. The reaction results were as follows: the yield of adipic acid was 72%, the yield of glutaric acid was 6%, and the yield of succinic acid was 3%.
实施例10Example 10
在100 mL具有聚四氟乙烯内胆的不锈钢高压反应釜中,将8.2140 g (100 mmol)环己烯和0.1997 g无水Cu(CH3COO)2分散于50 mL摩尔浓度为12 mol/L硝酸溶液中,密封反应釜,搅拌升温到60℃反应温度、通入氧气至压力为1.0 MPa。于60℃反应温度、1.0 MPa 氧气压力,500 rpm搅拌反应12.0 h。反应完毕,冷却至室温,对反应产物进行分析检测,反应结果为:己二酸收率68%,戊二酸收率4%,丁二酸收率3%。In a 100 mL stainless steel autoclave with a polytetrafluoroethylene liner, 8.2140 g (100 mmol) cyclohexene and 0.1997 g anhydrous Cu(CH3COO) 2 were dispersed in 50 mL with a molar concentration of 12 mol/L In the nitric acid solution, seal the reaction kettle, stir and heat up to the reaction temperature of 60°C, and feed oxygen until the pressure is 1.0 MPa. The reaction temperature was 60°C, the oxygen pressure was 1.0 MPa, and the reaction was stirred at 500 rpm for 12.0 h. After the reaction was completed, it was cooled to room temperature, and the reaction product was analyzed and detected. The reaction results were as follows: the yield of adipic acid was 68%, the yield of glutaric acid was 4%, and the yield of succinic acid was 3%.
实施例11Example 11
在100 mL具有聚四氟乙烯内胆的不锈钢高压反应釜中,将8.2140 g (100 mmol)环己烯和0.1997 g无水Cu(CH3COO)2分散于50 mL摩尔浓度为13 mol/L硝酸溶液中,密封反应釜,搅拌升温到60℃反应温度、通入氧气至压力为1.0 MPa。于60℃反应温度、1.0 MPa 氧气压力,500 rpm搅拌反应12.0 h。反应完毕,冷却至室温,对反应产物进行分析检测,反应结果为:己二酸收率65%,戊二酸收率3%,丁二酸收率3%。In a 100 mL stainless steel autoclave with a polytetrafluoroethylene liner, 8.2140 g (100 mmol) cyclohexene and 0.1997 g anhydrous Cu(CH3COO) 2 were dispersed in 50 mL with a molar concentration of 13 mol/L In the nitric acid solution, seal the reaction kettle, stir and heat up to the reaction temperature of 60°C, and feed oxygen until the pressure is 1.0 MPa. The reaction temperature was 60°C, the oxygen pressure was 1.0 MPa, and the reaction was stirred at 500 rpm for 12.0 h. After the reaction was completed, it was cooled to room temperature, and the reaction product was analyzed and detected. The reaction results were as follows: the yield of adipic acid was 65%, the yield of glutaric acid was 3%, and the yield of succinic acid was 3%.
实施例12Example 12
在100 mL具有聚四氟乙烯内胆的不锈钢高压反应釜中,将8.2140 g (100 mmol)环己烯和0.1997 g无水Cu(CH3COO)2分散于50 mL摩尔浓度为11 mol/L硝酸溶液中,密封反应釜,搅拌升温到40℃反应温度、通入氧气至压力为1.0 MPa。于40℃反应温度、1.0 MPa 氧气压力,500 rpm搅拌反应12.0 h。反应完毕,冷却至室温,对反应产物进行分析检测,反应结果为:己二酸收率65%,戊二酸收率2%,丁二酸收率1%。In a 100 mL stainless steel autoclave with a polytetrafluoroethylene liner, 8.2140 g (100 mmol) cyclohexene and 0.1997 g anhydrous Cu(CH3COO) 2 were dispersed in 50 mL with a molar concentration of 11 mol/L In the nitric acid solution, seal the reaction kettle, stir and heat up to the reaction temperature of 40°C, and feed oxygen until the pressure is 1.0 MPa. The reaction temperature was 40°C, the oxygen pressure was 1.0 MPa, and the reaction was stirred at 500 rpm for 12.0 h. After the reaction was completed, it was cooled to room temperature, and the reaction product was analyzed and detected. The reaction results were as follows: the yield of adipic acid was 65%, the yield of glutaric acid was 2%, and the yield of succinic acid was 1%.
实施例13Example 13
在100 mL具有聚四氟乙烯内胆的不锈钢高压反应釜中,将8.2140 g (100 mmol)环己烯和0.1997 g无水Cu(CH3COO)2分散于50 mL摩尔浓度为11 mol/L硝酸溶液中,密封反应釜,搅拌升温到60℃反应温度、通入氧气至压力为1.0 MPa。于45℃反应温度、1.0 MPa 氧气压力,500 rpm搅拌反应12.0 h。反应完毕,冷却至室温,对反应产物进行分析检测,反应结果为:己二酸收率70%,戊二酸收率2%,丁二酸收率1%。In a 100 mL stainless steel autoclave with a polytetrafluoroethylene liner, 8.2140 g (100 mmol) cyclohexene and 0.1997 g anhydrous Cu(CH3COO) 2 were dispersed in 50 mL with a molar concentration of 11 mol/L In the nitric acid solution, seal the reaction kettle, stir and heat up to the reaction temperature of 60°C, and feed oxygen until the pressure is 1.0 MPa. The reaction temperature was 45°C, the oxygen pressure was 1.0 MPa, and the reaction was stirred at 500 rpm for 12.0 h. After the reaction was completed, it was cooled to room temperature, and the reaction product was analyzed and detected. The reaction results were as follows: the yield of adipic acid was 70%, the yield of glutaric acid was 2%, and the yield of succinic acid was 1%.
实施例14Example 14
在100 mL具有聚四氟乙烯内胆的不锈钢高压反应釜中,将8.2140 g (100 mmol)环己烯和0.1997 g无水Cu(CH3COO)2分散于50 mL摩尔浓度为11 mol/L硝酸溶液中,密封反应釜,搅拌升温到50℃反应温度、通入氧气至压力为1.0 MPa。于50℃反应温度、1.0 MPa 氧气压力,500 rpm搅拌反应12.0 h。反应完毕,冷却至室温,对反应产物进行分析检测,反应结果为:己二酸收率75%,戊二酸收率3%,丁二酸收率1%。In a 100 mL stainless steel autoclave with a polytetrafluoroethylene liner, 8.2140 g (100 mmol) cyclohexene and 0.1997 g anhydrous Cu(CH3COO) 2 were dispersed in 50 mL with a molar concentration of 11 mol/L In the nitric acid solution, seal the reaction kettle, stir and heat up to the reaction temperature of 50°C, and feed oxygen until the pressure is 1.0 MPa. Stir the reaction at 50°C, 1.0 MPa oxygen pressure, and 500 rpm for 12.0 h. After the reaction was completed, it was cooled to room temperature, and the reaction product was analyzed and detected. The reaction results were as follows: the yield of adipic acid was 75%, the yield of glutaric acid was 3%, and the yield of succinic acid was 1%.
实施例15Example 15
在100 mL具有聚四氟乙烯内胆的不锈钢高压反应釜中,将8.2140 g (100 mmol)环己烯和0.1997 g无水Cu(CH3COO)2分散于50 mL摩尔浓度为11 mol/L硝酸溶液中,密封反应釜,搅拌升温到55℃反应温度、通入氧气至压力为1.0 MPa。于55℃反应温度、1.0 MPa 氧气压力,500 rpm搅拌反应12.0 h。反应完毕,冷却至室温,对反应产物进行分析检测,反应结果为:己二酸收率78%,戊二酸收率3%,丁二酸收率2%。In a 100 mL stainless steel autoclave with a polytetrafluoroethylene liner, 8.2140 g (100 mmol) cyclohexene and 0.1997 g anhydrous Cu(CH3COO) 2 were dispersed in 50 mL with a molar concentration of 11 mol/L In the nitric acid solution, seal the reaction kettle, stir and raise the temperature to a reaction temperature of 55°C, and feed oxygen to a pressure of 1.0 MPa. The reaction temperature was 55°C, the oxygen pressure was 1.0 MPa, and the reaction was stirred at 500 rpm for 12.0 h. After the reaction was completed, it was cooled to room temperature, and the reaction product was analyzed and detected. The reaction results were as follows: the yield of adipic acid was 78%, the yield of glutaric acid was 3%, and the yield of succinic acid was 2%.
实施例16Example 16
在100 mL具有聚四氟乙烯内胆的不锈钢高压反应釜中,将8.2140 g (100 mmol)环己烯和0.1997 g无水Cu(CH3COO)2分散于50 mL摩尔浓度为11 mol/L硝酸溶液中,密封反应釜,搅拌升温到65℃反应温度、通入氧气至压力为1.0 MPa。于65℃反应温度、1.0 MPa 氧气压力,500 rpm搅拌反应12.0 h。反应完毕,冷却至室温,对反应产物进行分析检测,反应结果为:己二酸收率74%,戊二酸收率3%,丁二酸收率3%。In a 100 mL stainless steel autoclave with a polytetrafluoroethylene liner, 8.2140 g (100 mmol) cyclohexene and 0.1997 g anhydrous Cu(CH3COO) 2 were dispersed in 50 mL with a molar concentration of 11 mol/L In the nitric acid solution, seal the reaction kettle, stir and heat up to the reaction temperature of 65°C, and feed in oxygen until the pressure is 1.0 MPa. The reaction temperature was 65°C, the oxygen pressure was 1.0 MPa, and the reaction was stirred at 500 rpm for 12.0 h. After the reaction was completed, it was cooled to room temperature, and the reaction product was analyzed and detected. The reaction results were as follows: the yield of adipic acid was 74%, the yield of glutaric acid was 3%, and the yield of succinic acid was 3%.
实施例17Example 17
在100 mL具有聚四氟乙烯内胆的不锈钢高压反应釜中,将8.2140 g (100 mmol)环己烯和0.1997 g无水Cu(CH3COO)2分散于50 mL摩尔浓度为11 mol/L硝酸溶液中,密封反应釜,搅拌升温到70℃反应温度、通入氧气至压力为1.0 MPa。于70℃反应温度、1.0 MPa 氧气压力,500 rpm搅拌反应12.0 h。反应完毕,冷却至室温,对反应产物进行分析检测,反应结果为:己二酸收率71%,戊二酸收率4%,丁二酸收率2%。In a 100 mL stainless steel autoclave with a polytetrafluoroethylene liner, 8.2140 g (100 mmol) cyclohexene and 0.1997 g anhydrous Cu(CH3COO) 2 were dispersed in 50 mL with a molar concentration of 11 mol/L In the nitric acid solution, seal the reaction kettle, stir and heat up to the reaction temperature of 70°C, and feed in oxygen until the pressure is 1.0 MPa. The reaction temperature was 70°C, the oxygen pressure was 1.0 MPa, and the reaction was stirred at 500 rpm for 12.0 h. After the reaction was completed, it was cooled to room temperature, and the reaction product was analyzed and detected. The reaction results were as follows: the yield of adipic acid was 71%, the yield of glutaric acid was 4%, and the yield of succinic acid was 2%.
实施例18Example 18
在100 mL具有聚四氟乙烯内胆的不锈钢高压反应釜中,将8.2140 g (100 mmol)环己烯和0.1997 g无水Cu(CH3COO)2分散于50 mL摩尔浓度为11 mol/L硝酸溶液中,密封反应釜,搅拌升温到75℃反应温度、通入氧气至压力为1.0 MPa。于75℃反应温度、1.0 MPa 氧气压力,500 rpm搅拌反应12.0 h。反应完毕,冷却至室温,对反应产物进行分析检测,反应结果为:己二酸收率60%,戊二酸收率4%,丁二酸收率1%。In a 100 mL stainless steel autoclave with a polytetrafluoroethylene liner, 8.2140 g (100 mmol) cyclohexene and 0.1997 g anhydrous Cu(CH3COO) 2 were dispersed in 50 mL with a molar concentration of 11 mol/L In the nitric acid solution, seal the reaction kettle, stir and heat up to the reaction temperature of 75°C, and feed in oxygen until the pressure is 1.0 MPa. The reaction temperature was 75°C, the oxygen pressure was 1.0 MPa, and the reaction was stirred at 500 rpm for 12.0 h. After the reaction was completed, it was cooled to room temperature, and the reaction product was analyzed and detected. The reaction results were as follows: the yield of adipic acid was 60%, the yield of glutaric acid was 4%, and the yield of succinic acid was 1%.
实施例19Example 19
在100 mL具有聚四氟乙烯内胆的不锈钢高压反应釜中,将8.2140 g (100 mmol)环己烯和0.1997 g无水Cu(CH3COO)2分散于50 mL摩尔浓度为11 mol/L硝酸溶液中,密封反应釜,搅拌升温到60℃反应温度、通入氧气至压力为0.2 MPa。于60℃反应温度、0.2 MPa 氧气压力,500 rpm搅拌反应12.0 h。反应完毕,冷却至室温,对反应产物进行分析检测,反应结果为:己二酸收率55%,戊二酸收率1%,丁二酸收率1%。In a 100 mL stainless steel autoclave with a polytetrafluoroethylene liner, 8.2140 g (100 mmol) cyclohexene and 0.1997 g anhydrous Cu(CH3COO) 2 were dispersed in 50 mL with a molar concentration of 11 mol/L In the nitric acid solution, seal the reaction kettle, stir and heat up to the reaction temperature of 60°C, and feed in oxygen until the pressure is 0.2 MPa. The reaction temperature was 60°C, the oxygen pressure was 0.2 MPa, and the reaction was stirred at 500 rpm for 12.0 h. After the reaction was completed, it was cooled to room temperature, and the reaction product was analyzed and detected. The reaction results were as follows: the yield of adipic acid was 55%, the yield of glutaric acid was 1%, and the yield of succinic acid was 1%.
实施例20Example 20
在100 mL具有聚四氟乙烯内胆的不锈钢高压反应釜中,将8.2140 g (100 mmol)环己烯和0.1997 g无水Cu(CH3COO)2分散于50 mL摩尔浓度为11 mol/L硝酸溶液中,密封反应釜,搅拌升温到60℃反应温度、通入氧气至压力为0.4 MPa。于60℃反应温度、0.4 MPa 氧气压力,500 rpm搅拌反应12.0 h。反应完毕,冷却至室温,对反应产物进行分析检测,反应结果为:己二酸收率68%,戊二酸收率3%,丁二酸收率1%。In a 100 mL stainless steel autoclave with a polytetrafluoroethylene liner, 8.2140 g (100 mmol) cyclohexene and 0.1997 g anhydrous Cu(CH3COO) 2 were dispersed in 50 mL with a molar concentration of 11 mol/L In the nitric acid solution, seal the reaction kettle, stir and heat up to the reaction temperature of 60°C, and feed in oxygen until the pressure is 0.4 MPa. Stir the reaction at 500 rpm for 12.0 h at a reaction temperature of 60 °C, an oxygen pressure of 0.4 MPa, and 500 rpm. After the reaction was completed, it was cooled to room temperature, and the reaction product was analyzed and detected. The reaction results were as follows: the yield of adipic acid was 68%, the yield of glutaric acid was 3%, and the yield of succinic acid was 1%.
实施例21Example 21
在100 mL具有聚四氟乙烯内胆的不锈钢高压反应釜中,将8.2140 g (100 mmol)环己烯和0.1997 g无水Cu(CH3COO)2分散于50 mL摩尔浓度为11 mol/L硝酸溶液中,密封反应釜,搅拌升温到60℃反应温度、通入氧气至压力为0.6 MPa。于60℃反应温度、0.6 MPa 氧气压力,500 rpm搅拌反应12.0 h。反应完毕,冷却至室温,对反应产物进行分析检测,反应结果为:己二酸收率69%,戊二酸收率2%,丁二酸收率1%。In a 100 mL stainless steel autoclave with a polytetrafluoroethylene liner, 8.2140 g (100 mmol) cyclohexene and 0.1997 g anhydrous Cu(CH3COO) 2 were dispersed in 50 mL with a molar concentration of 11 mol/L In the nitric acid solution, seal the reaction kettle, stir and raise the temperature to 60°C reaction temperature, and feed oxygen until the pressure is 0.6 MPa. The reaction temperature was 60°C, the oxygen pressure was 0.6 MPa, and the reaction was stirred at 500 rpm for 12.0 h. After the reaction was completed, it was cooled to room temperature, and the reaction product was analyzed and detected. The reaction results were as follows: the yield of adipic acid was 69%, the yield of glutaric acid was 2%, and the yield of succinic acid was 1%.
实施例22Example 22
在100 mL具有聚四氟乙烯内胆的不锈钢高压反应釜中,将8.2140 g (100 mmol)环己烯和0.1997 g无水Cu(CH3COO)2分散于50 mL摩尔浓度为11 mol/L硝酸溶液中,密封反应釜,搅拌升温到60℃反应温度、通入氧气至压力为0.8 MPa。于60℃反应温度、0.8 MPa 氧气压力,500 rpm搅拌反应12.0 h。反应完毕,冷却至室温,对反应产物进行分析检测,反应结果为:己二酸收率72%,戊二酸收率3%,丁二酸收率2%。In a 100 mL stainless steel autoclave with a polytetrafluoroethylene liner, 8.2140 g (100 mmol) cyclohexene and 0.1997 g anhydrous Cu(CH3COO) 2 were dispersed in 50 mL with a molar concentration of 11 mol/L In the nitric acid solution, seal the reaction kettle, stir and heat up to the reaction temperature of 60°C, and feed in oxygen until the pressure is 0.8 MPa. The reaction temperature was 60°C, the oxygen pressure was 0.8 MPa, and the reaction was stirred at 500 rpm for 12.0 h. After the reaction was completed, it was cooled to room temperature, and the reaction product was analyzed and detected. The reaction results were as follows: the yield of adipic acid was 72%, the yield of glutaric acid was 3%, and the yield of succinic acid was 2%.
实施例23Example 23
在100 mL具有聚四氟乙烯内胆的不锈钢高压反应釜中,将8.2140 g (100 mmol)环己烯和0.1997 g无水Cu(CH3COO)2分散于50 mL摩尔浓度为11 mol/L硝酸溶液中,密封反应釜,搅拌升温到60℃反应温度、通入氧气至压力为1.2 MPa。于60℃反应温度、1.2 MPa 氧气压力,500 rpm搅拌反应12.0 h。反应完毕,冷却至室温,对反应产物进行分析检测,反应结果为:己二酸收率70%,戊二酸收率4%,丁二酸收率3%。In a 100 mL stainless steel autoclave with a polytetrafluoroethylene liner, 8.2140 g (100 mmol) cyclohexene and 0.1997 g anhydrous Cu(CH3COO) 2 were dispersed in 50 mL with a molar concentration of 11 mol/L In the nitric acid solution, seal the reaction kettle, stir and heat up to the reaction temperature of 60°C, and feed in oxygen until the pressure is 1.2 MPa. At 60°C reaction temperature, 1.2 MPa oxygen pressure, and 500 rpm stirring reaction for 12.0 h. After the reaction was completed, it was cooled to room temperature, and the reaction product was analyzed and detected. The reaction results were as follows: the yield of adipic acid was 70%, the yield of glutaric acid was 4%, and the yield of succinic acid was 3%.
实施例24Example 24
在100 mL具有聚四氟乙烯内胆的不锈钢高压反应釜中,将8.2140 g (100 mmol)环己烯和0.1997 g无水Cu(CH3COO)2分散于50 mL摩尔浓度为11 mol/L硝酸溶液中,密封反应釜,搅拌升温到60℃反应温度、通入氧气至压力为1.4 MPa。于60℃反应温度、1.4 MPa 氧气压力,500 rpm搅拌反应12.0 h。反应完毕,冷却至室温,对反应产物进行分析检测,反应结果为:己二酸收率61%,戊二酸收率3%,丁二酸收率2%。In a 100 mL stainless steel autoclave with a polytetrafluoroethylene liner, 8.2140 g (100 mmol) cyclohexene and 0.1997 g anhydrous Cu(CH3COO) 2 were dispersed in 50 mL with a molar concentration of 11 mol/L In the nitric acid solution, seal the reaction kettle, stir and heat up to the reaction temperature of 60°C, and feed in oxygen until the pressure is 1.4 MPa. At 60°C reaction temperature, 1.4 MPa oxygen pressure, and 500 rpm, the reaction was stirred for 12.0 h. After the reaction was completed, it was cooled to room temperature, and the reaction product was analyzed and detected. The reaction results were as follows: the yield of adipic acid was 61%, the yield of glutaric acid was 3%, and the yield of succinic acid was 2%.
实施例25Example 25
在100 mL具有聚四氟乙烯内胆的不锈钢高压反应釜中,将8.2140 g (100 mmol)环己烯和0.1997 g无水Cu(CH3COO)2分散于50 mL摩尔浓度为11 mol/L硝酸溶液中,密封反应釜,搅拌升温到60℃反应温度、通入氧气至压力为(1.6 MPa)。于60℃反应温度、1.6 MPa氧气压力,500 rpm搅拌反应12.0 h。反应完毕,冷却至室温,对反应产物进行分析检测,反应结果为:己二酸收率50%,戊二酸收率3%,丁二酸收率1%。In a 100 mL stainless steel autoclave with a polytetrafluoroethylene liner, 8.2140 g (100 mmol) cyclohexene and 0.1997 g anhydrous Cu(CH3COO) 2 were dispersed in 50 mL with a molar concentration of 11 mol/L In the nitric acid solution, seal the reaction kettle, stir and raise the temperature to 60°C reaction temperature, and feed oxygen until the pressure is (1.6 MPa). The reaction temperature was 60°C, the oxygen pressure was 1.6 MPa, and the reaction was stirred at 500 rpm for 12.0 h. After the reaction was completed, it was cooled to room temperature, and the reaction product was analyzed and detected. The reaction results were as follows: the yield of adipic acid was 50%, the yield of glutaric acid was 3%, and the yield of succinic acid was 1%.
实施例26Example 26
在100 mL具有聚四氟乙烯内胆的不锈钢高压反应釜中,将8.2140 g (100 mmol)环己烯和0.1997 g无水Cu(CH3COO)2分散于50 mL摩尔浓度为11 mol/L硝酸溶液中,密封反应釜,搅拌升温到60℃反应温度、通入氧气至压力为(1.0 MPa)。于60℃反应温度、1.0 MPa氧气压力,500 rpm搅拌反应4.0 h。反应完毕,冷却至室温,对反应产物进行分析检测,反应结果为:己二酸收率41%,戊二酸收率1%,丁二酸收率1%。In a 100 mL stainless steel autoclave with a polytetrafluoroethylene liner, 8.2140 g (100 mmol) cyclohexene and 0.1997 g anhydrous Cu(CH3COO) 2 were dispersed in 50 mL with a molar concentration of 11 mol/L In the nitric acid solution, seal the reaction vessel, heat up to 60°C reaction temperature with stirring, and feed oxygen until the pressure is (1.0 MPa). The reaction temperature was 60°C, the oxygen pressure was 1.0 MPa, and the reaction was stirred at 500 rpm for 4.0 h. After the reaction was completed, it was cooled to room temperature, and the reaction product was analyzed and detected. The reaction results were as follows: the yield of adipic acid was 41%, the yield of glutaric acid was 1%, and the yield of succinic acid was 1%.
实施例27Example 27
在100 mL具有聚四氟乙烯内胆的不锈钢高压反应釜中,将8.2140 g (100 mmol)环己烯和0.1997 g无水Cu(CH3COO)2分散于50 mL摩尔浓度为11 mol/L硝酸溶液中,密封反应釜,搅拌升温到60℃反应温度、通入氧气至压力为(1.0 MPa)。于60℃反应温度、1.0 MPa氧气压力,500 rpm搅拌反应6.0 h。反应完毕,冷却至室温,对反应产物进行分析检测,反应结果为:己二酸收率52%,戊二酸收率1%,丁二酸收率1%。In a 100 mL stainless steel autoclave with a polytetrafluoroethylene liner, 8.2140 g (100 mmol) cyclohexene and 0.1997 g anhydrous Cu(CH3COO) 2 were dispersed in 50 mL with a molar concentration of 11 mol/L In the nitric acid solution, seal the reaction vessel, heat up to 60°C reaction temperature with stirring, and feed oxygen until the pressure is (1.0 MPa). The reaction temperature was 60°C, the oxygen pressure was 1.0 MPa, and the reaction was stirred at 500 rpm for 6.0 h. After the reaction was completed, it was cooled to room temperature, and the reaction product was analyzed and detected. The reaction results were as follows: the yield of adipic acid was 52%, the yield of glutaric acid was 1%, and the yield of succinic acid was 1%.
实施例28Example 28
在100 mL具有聚四氟乙烯内胆的不锈钢高压反应釜中,将8.2140 g (100 mmol)环己烯和0.1997 g无水Cu(CH3COO)2分散于50 mL摩尔浓度为11 mol/L硝酸溶液中,密封反应釜,搅拌升温到60℃反应温度、通入氧气至压力为(1.0 MPa)。于60℃反应温度、1.0 MPa氧气压力,500 rpm搅拌反应8.0 h。反应完毕,冷却至室温,对反应产物进行分析检测,反应结果为:己二酸收率65%,戊二酸收率3%,丁二酸收率1%。In a 100 mL stainless steel autoclave with a polytetrafluoroethylene liner, 8.2140 g (100 mmol) cyclohexene and 0.1997 g anhydrous Cu(CH3COO) 2 were dispersed in 50 mL with a molar concentration of 11 mol/L In the nitric acid solution, seal the reaction vessel, heat up to 60°C reaction temperature with stirring, and feed oxygen until the pressure is (1.0 MPa). The reaction temperature was 60°C, the oxygen pressure was 1.0 MPa, and the reaction was stirred at 500 rpm for 8.0 h. After the reaction was completed, it was cooled to room temperature, and the reaction product was analyzed and detected. The reaction results were as follows: the yield of adipic acid was 65%, the yield of glutaric acid was 3%, and the yield of succinic acid was 1%.
实施例29Example 29
在100 mL具有聚四氟乙烯内胆的不锈钢高压反应釜中,将8.2140 g (100 mmol)环己烯和0.1997 g无水Cu(CH3COO)2分散于50 mL摩尔浓度为11 mol/L硝酸溶液中,密封反应釜,搅拌升温到60℃反应温度、通入氧气至压力为(1.0 MPa)。于60℃反应温度、1.0 MPa氧气压力,500 rpm搅拌反应10.0 h。反应完毕,冷却至室温,对反应产物进行分析检测,反应结果为:己二酸收率71%,戊二酸收率3%,丁二酸收率2%。In a 100 mL stainless steel autoclave with a polytetrafluoroethylene liner, 8.2140 g (100 mmol) cyclohexene and 0.1997 g anhydrous Cu(CH3COO) 2 were dispersed in 50 mL with a molar concentration of 11 mol/L In the nitric acid solution, seal the reaction vessel, heat up to 60°C reaction temperature with stirring, and feed oxygen until the pressure is (1.0 MPa). At 60°C reaction temperature, 1.0 MPa oxygen pressure, and 500 rpm stirring reaction for 10.0 h. After the reaction was completed, it was cooled to room temperature, and the reaction product was analyzed and detected. The reaction results were as follows: the yield of adipic acid was 71%, the yield of glutaric acid was 3%, and the yield of succinic acid was 2%.
实施例30Example 30
在100 mL具有聚四氟乙烯内胆的不锈钢高压反应釜中,将8.2140 g (100 mmol)环己烯和0.1997 g无水Cu(CH3COO)2分散于50 mL摩尔浓度为11 mol/L硝酸溶液中,密封反应釜,搅拌升温到60℃反应温度、通入氧气至压力为(1.0 MPa)。于60℃反应温度、1.0 MPa氧气压力,500 rpm搅拌反应14.0 h。反应完毕,冷却至室温,对反应产物进行分析检测,反应结果为:己二酸收率75%,戊二酸收率4%,丁二酸收率2%。In a 100 mL stainless steel autoclave with a polytetrafluoroethylene liner, 8.2140 g (100 mmol) cyclohexene and 0.1997 g anhydrous Cu(CH3COO) 2 were dispersed in 50 mL with a molar concentration of 11 mol/L In the nitric acid solution, seal the reaction vessel, heat up to 60°C reaction temperature with stirring, and feed oxygen until the pressure is (1.0 MPa). At 60°C reaction temperature, 1.0 MPa oxygen pressure, and 500 rpm, the reaction was stirred for 14.0 h. After the reaction was completed, it was cooled to room temperature, and the reaction product was analyzed and detected. The reaction results were as follows: the yield of adipic acid was 75%, the yield of glutaric acid was 4%, and the yield of succinic acid was 2%.
实施例31Example 31
在100 mL具有聚四氟乙烯内胆的不锈钢高压反应釜中,将8.2140 g (100 mmol)环己烯和0.1997 g无水Cu(CH3COO)2分散于50 mL摩尔浓度为11 mol/L硝酸溶液中,密封反应釜,搅拌升温到60℃反应温度、通入氧气至压力为(1.0 MPa)。于60℃反应温度、1.0 MPa氧气压力,500 rpm搅拌反应16.0 h。反应完毕,冷却至室温,对反应产物进行分析检测,反应结果为:己二酸收率63%,戊二酸收率5%,丁二酸收率1%。In a 100 mL stainless steel autoclave with a polytetrafluoroethylene liner, 8.2140 g (100 mmol) cyclohexene and 0.1997 g anhydrous Cu(CH3COO) 2 were dispersed in 50 mL with a molar concentration of 11 mol/L In the nitric acid solution, seal the reaction vessel, heat up to 60°C reaction temperature with stirring, and feed oxygen until the pressure is (1.0 MPa). The reaction temperature was 60°C, the oxygen pressure was 1.0 MPa, and the reaction was stirred at 500 rpm for 16.0 h. After the reaction was completed, it was cooled to room temperature, and the reaction product was analyzed and detected. The reaction results were as follows: the yield of adipic acid was 63%, the yield of glutaric acid was 5%, and the yield of succinic acid was 1%.
实施例32Example 32
在100 mL具有聚四氟乙烯内胆的不锈钢高压反应釜中,将8.2140 g (100 mmol)环己烯和0.0018 g无水Cu(CH3COO)2 (0.01% equive)分散于50 mL摩尔浓度为11 mol/L硝酸溶液中,密封反应釜,搅拌升温到60℃反应温度、通入氧气至压力为(1.0 MPa)。于60℃反应温度、1.0 MPa 氧气压力,500 rpm搅拌反应12.0 h。反应完毕,冷却至室温,对反应产物进行分析检测,反应结果为:己二酸收率66%,戊二酸收率1%,丁二酸收率1%。In a 100 mL stainless steel autoclave with a polytetrafluoroethylene liner, 8.2140 g (100 mmol) cyclohexene and 0.0018 g anhydrous Cu(CH3COO) 2 (0.01% equive) were dispersed in a 50 mL molar concentration 11 mol/L nitric acid solution, seal the reaction vessel, heat up to 60°C reaction temperature with stirring, and feed oxygen until the pressure is (1.0 MPa). The reaction temperature was 60°C, the oxygen pressure was 1.0 MPa, and the reaction was stirred at 500 rpm for 12.0 h. After the reaction was completed, it was cooled to room temperature, and the reaction product was analyzed and detected. The reaction results were as follows: the yield of adipic acid was 66%, the yield of glutaric acid was 1%, and the yield of succinic acid was 1%.
实施例33Example 33
在100 mL具有聚四氟乙烯内胆的不锈钢高压反应釜中,将8.2140 g (100 mmol)环己烯和0.0188 g无水Cu(CH3COO)2 (0.1% equive)分散于50 mL摩尔浓度为11 mol/L硝酸溶液中,密封反应釜,搅拌升温到60℃反应温度、通入氧气至压力为(1.0 MPa)。于60℃反应温度、1.0 MPa 氧气压力,500 rpm搅拌反应12.0 h。反应完毕,冷却至室温,对反应产物进行分析检测,反应结果为:己二酸收率69%,戊二酸收率2%,丁二酸收率1%。In a 100 mL stainless steel autoclave with a polytetrafluoroethylene liner, 8.2140 g (100 mmol) cyclohexene and 0.0188 g anhydrous Cu(CH3COO) 2 (0.1% equive) were dispersed in a 50 mL molar concentration 11 mol/L nitric acid solution, seal the reaction vessel, heat up to 60°C reaction temperature with stirring, and feed oxygen until the pressure is (1.0 MPa). The reaction temperature was 60°C, the oxygen pressure was 1.0 MPa, and the reaction was stirred at 500 rpm for 12.0 h. After the reaction was completed, it was cooled to room temperature, and the reaction product was analyzed and detected. The reaction results were as follows: the yield of adipic acid was 69%, the yield of glutaric acid was 2%, and the yield of succinic acid was 1%.
实施例34Example 34
在100 mL具有聚四氟乙烯内胆的不锈钢高压反应釜中,将8.2140 g (100 mmol)环己烯和1.8760 g无水Cu(CH3COO)2 (0.1equive)分散于50 mL摩尔浓度为11 mol/L硝酸溶液中,密封反应釜,搅拌升温到60℃反应温度、通入氧气至压力为(1.0 MPa)。于60℃反应温度、1.0 MPa 氧气压力,500 rpm搅拌反应12.0 h。反应完毕,冷却至室温,对反应产物进行分析检测,反应结果为:己二酸收率71%,戊二酸收率4%,丁二酸收率3%。In a 100 mL stainless steel autoclave with polytetrafluoroethylene liner, 8.2140 g (100 mmol) cyclohexene and 1.8760 g anhydrous Cu(CH 3 COO) 2 (0.1 equive) were dispersed in 50 mL with a molar concentration of 11 mol/L nitric acid solution, seal the reaction vessel, heat up to 60°C reaction temperature with stirring, and feed oxygen until the pressure is (1.0 MPa). The reaction temperature was 60°C, the oxygen pressure was 1.0 MPa, and the reaction was stirred at 500 rpm for 12.0 h. After the reaction was completed, it was cooled to room temperature, and the reaction product was analyzed and detected. The reaction results were as follows: the yield of adipic acid was 71%, the yield of glutaric acid was 4%, and the yield of succinic acid was 3%.
实施例35Example 35
在100 mL具有聚四氟乙烯内胆的不锈钢高压反应釜中,将8.2140 g (100 mmol)环己烯和0.1997 g无水Cu(CH3COO)2分散于50 mL摩尔浓度为11 mol/L硝酸溶液中,密封反应釜,搅拌升温到60℃反应温度、通入氧气至压力为(1.0 MPa)。于60℃反应温度、1.0 MPa氧气压力,100 rpm搅拌反应12.0 h。反应完毕,冷却至室温,对反应产物进行分析检测,反应结果为:己二酸收率42%,戊二酸收率1%,丁二酸收率2%。In a 100 mL stainless steel autoclave with a polytetrafluoroethylene liner, 8.2140 g (100 mmol) cyclohexene and 0.1997 g anhydrous Cu(CH3COO) 2 were dispersed in 50 mL with a molar concentration of 11 mol/L In the nitric acid solution, seal the reaction vessel, heat up to 60°C reaction temperature with stirring, and feed oxygen until the pressure is (1.0 MPa). The reaction temperature was 60°C, the oxygen pressure was 1.0 MPa, and the reaction was stirred at 100 rpm for 12.0 h. After the reaction was completed, it was cooled to room temperature, and the reaction product was analyzed and detected. The reaction results were as follows: the yield of adipic acid was 42%, the yield of glutaric acid was 1%, and the yield of succinic acid was 2%.
实施例36Example 36
在100 mL具有聚四氟乙烯内胆的不锈钢高压反应釜中,将8.2140 g (100 mmol)环己烯和0.1997 g无水Cu(CH3COO)2分散于50 mL摩尔浓度为11 mol/L硝酸溶液中,密封反应釜,搅拌升温到60℃反应温度、通入氧气至压力为(1.0 MPa)。于60℃反应温度、1.0 MPa氧气压力,200 rpm搅拌反应12.0 h。反应完毕,冷却至室温,对反应产物进行分析检测,反应结果为:己二酸收率52%,戊二酸收率2%,丁二酸收率2%。In a 100 mL stainless steel autoclave with a polytetrafluoroethylene liner, 8.2140 g (100 mmol) cyclohexene and 0.1997 g anhydrous Cu(CH3COO) 2 were dispersed in 50 mL with a molar concentration of 11 mol/L In the nitric acid solution, seal the reaction vessel, heat up to 60°C reaction temperature with stirring, and feed oxygen until the pressure is (1.0 MPa). The reaction temperature was 60°C, the oxygen pressure was 1.0 MPa, and the reaction was stirred at 200 rpm for 12.0 h. After the reaction was completed, it was cooled to room temperature, and the reaction product was analyzed and detected. The reaction results were as follows: the yield of adipic acid was 52%, the yield of glutaric acid was 2%, and the yield of succinic acid was 2%.
实施例37Example 37
在100 mL具有聚四氟乙烯内胆的不锈钢高压反应釜中,将8.2140 g (100 mmol)环己烯和0.1997 g无水Cu(CH3COO)2分散于50 mL摩尔浓度为11 mol/L硝酸溶液中,密封反应釜,搅拌升温到60℃反应温度、通入氧气至压力为(1.0 MPa)。于60℃反应温度、1.0 MPa氧气压力,300 rpm搅拌反应12.0 h。反应完毕,冷却至室温,对反应产物进行分析检测,反应结果为:己二酸收率59%,戊二酸收率3%,丁二酸收率2%。In a 100 mL stainless steel autoclave with a polytetrafluoroethylene liner, 8.2140 g (100 mmol) cyclohexene and 0.1997 g anhydrous Cu(CH3COO) 2 were dispersed in 50 mL with a molar concentration of 11 mol/L In the nitric acid solution, seal the reaction vessel, heat up to 60°C reaction temperature with stirring, and feed oxygen until the pressure is (1.0 MPa). At 60°C reaction temperature, 1.0 MPa oxygen pressure, and 300 rpm, the reaction was stirred for 12.0 h. After the reaction was completed, it was cooled to room temperature, and the reaction product was analyzed and detected. The reaction results were as follows: the yield of adipic acid was 59%, the yield of glutaric acid was 3%, and the yield of succinic acid was 2%.
实施例38Example 38
在100 mL具有聚四氟乙烯内胆的不锈钢高压反应釜中,将8.2140 g (100 mmol)环己烯和0.1997 g无水Cu(CH3COO)2分散于50 mL摩尔浓度为11 mol/L硝酸溶液中,密封反应釜,搅拌升温到60℃反应温度、通入氧气至压力为(1.0 MPa)。于60℃反应温度、1.0 MPa氧气压力,400 rpm搅拌反应12.0 h。反应完毕,冷却至室温,对反应产物进行分析检测,反应结果为:己二酸收率70%,戊二酸收率4%,丁二酸收率2%。In a 100 mL stainless steel autoclave with a polytetrafluoroethylene liner, 8.2140 g (100 mmol) cyclohexene and 0.1997 g anhydrous Cu(CH3COO) 2 were dispersed in 50 mL with a molar concentration of 11 mol/L In the nitric acid solution, seal the reaction vessel, heat up to 60°C reaction temperature with stirring, and feed oxygen until the pressure is (1.0 MPa). The reaction temperature was 60°C, the oxygen pressure was 1.0 MPa, and the reaction was stirred at 400 rpm for 12.0 h. After the reaction was completed, it was cooled to room temperature, and the reaction product was analyzed and detected. The reaction results were as follows: the yield of adipic acid was 70%, the yield of glutaric acid was 4%, and the yield of succinic acid was 2%.
实施例39Example 39
在100 mL具有聚四氟乙烯内胆的不锈钢高压反应釜中,将8.2140 g (100 mmol)环己烯和0.1997 g无水Cu(CH3COO)2分散于50 mL摩尔浓度为11 mol/L硝酸溶液中,密封反应釜,搅拌升温到60℃反应温度、通入氧气至压力为(1.0 MPa)。于60℃反应温度、1.0 MPa氧气压力,600 rpm搅拌反应12.0 h。反应完毕,冷却至室温,对反应产物进行分析检测,反应结果为:己二酸收率73%,戊二酸收率4%,丁二酸收率3%。In a 100 mL stainless steel autoclave with a polytetrafluoroethylene liner, 8.2140 g (100 mmol) cyclohexene and 0.1997 g anhydrous Cu(CH3COO) 2 were dispersed in 50 mL with a molar concentration of 11 mol/L In the nitric acid solution, seal the reaction vessel, heat up to 60°C reaction temperature with stirring, and feed oxygen until the pressure is (1.0 MPa). The reaction temperature was 60°C, the oxygen pressure was 1.0 MPa, and the reaction was stirred at 600 rpm for 12.0 h. After the reaction was completed, it was cooled to room temperature, and the reaction product was analyzed and detected. The reaction results were as follows: the yield of adipic acid was 73%, the yield of glutaric acid was 4%, and the yield of succinic acid was 3%.
实施例40Example 40
在100 mL具有聚四氟乙烯内胆的不锈钢高压反应釜中,将8.2140 g (100 mmol)环己烯和0.1997 g无水Cu(CH3COO)2分散于50 mL摩尔浓度为11 mol/L硝酸溶液中,密封反应釜,搅拌升温到60℃反应温度、通入氧气至压力为(1.0 MPa)。于60℃反应温度、1.0 MPa氧气压力,700 rpm搅拌反应12.0 h。反应完毕,冷却至室温,对反应产物进行分析检测,反应结果为:己二酸收率74%,戊二酸收率4%,丁二酸收率4%。In a 100 mL stainless steel autoclave with a polytetrafluoroethylene liner, 8.2140 g (100 mmol) cyclohexene and 0.1997 g anhydrous Cu(CH3COO) 2 were dispersed in 50 mL with a molar concentration of 11 mol/L In the nitric acid solution, seal the reaction vessel, heat up to 60°C reaction temperature with stirring, and feed oxygen until the pressure is (1.0 MPa). The reaction temperature was 60°C, the oxygen pressure was 1.0 MPa, and the reaction was stirred at 700 rpm for 12.0 h. After the reaction was completed, it was cooled to room temperature, and the reaction product was analyzed and detected. The reaction results were as follows: the yield of adipic acid was 74%, the yield of glutaric acid was 4%, and the yield of succinic acid was 4%.
实施例41 (对比实验)Embodiment 41 (comparative experiment)
在100 mL具有聚四氟乙烯内胆的不锈钢高压反应釜中,将8.2140 g (100 mmol)环己烯分散于50 mL摩尔浓度为11 mol/L硝酸溶液中,密封反应釜,搅拌升温到60℃反应温度、通入氧气至压力为(1.0 MPa)。于60℃反应温度、 1.0 MPa 氧气压力,500 rpm搅拌反应12.0 h。反应完毕,冷却至室温,对反应产物进行分析检测,反应结果为:己二酸收率44%,戊二酸收率1%,未检测到丁二酸。In a 100 mL stainless steel autoclave with polytetrafluoroethylene liner, disperse 8.2140 g (100 mmol) cyclohexene in 50 mL of nitric acid solution with a molar concentration of 11 mol/L, seal the autoclave, stir and heat up to 60 °C reaction temperature, feed oxygen to a pressure of (1.0 MPa). Stir the reaction at 500 rpm at a reaction temperature of 60°C, an oxygen pressure of 1.0 MPa, and 12.0 h. After the reaction was completed, it was cooled to room temperature, and the reaction product was analyzed and detected. The reaction results were as follows: the yield of adipic acid was 44%, the yield of glutaric acid was 1%, and no succinic acid was detected.
实施例42 (对比实验)Embodiment 42 (comparative experiment)
在100 mL具有聚四氟乙烯内胆的不锈钢高压反应釜中,将0.1997 g无水Cu(CH3COO)2分散8.2140 g (100 mmol)环己烯中,密封反应釜,搅拌升温到60℃反应温度、通入氧气至压力为(1.0 MPa)。于60℃反应温度、1.0 MPa氧气压力,500 rpm搅拌反应12.0 h。反应完毕,冷却至室温,对反应产物进行分析检测,反应结果为:己二酸收率5%,未检测到戊二酸,未检测到丁二酸。In a 100 mL stainless steel autoclave with a polytetrafluoroethylene liner, disperse 0.1997 g of anhydrous Cu(CH 3 COO) 2 in 8.2140 g (100 mmol) of cyclohexene, seal the autoclave, stir and heat up to 60 °C Reaction temperature, feed oxygen to pressure (1.0 MPa). The reaction temperature was 60°C, the oxygen pressure was 1.0 MPa, and the reaction was stirred at 500 rpm for 12.0 h. After the reaction was completed, it was cooled to room temperature, and the reaction product was analyzed and detected. The reaction result was: the yield of adipic acid was 5%, no glutaric acid was detected, and no succinic acid was detected.
实施例43 (对比实验)Embodiment 43 (comparative experiment)
在100 mL具有聚四氟乙烯内胆的不锈钢高压反应釜中,将8.2140 g (100 mmol)环己烯和0.1997 g无水Cu(CH3COO)2分散于50 mL摩尔浓度为11 mol/L硝酸溶液中,密封反应釜,搅拌升温到60 ºC。于60℃反应温度、500 rpm搅拌反应12.0 h。反应完毕,冷却至室温,对反应产物进行分析检测,反应结果为:己二酸收率36%,戊二酸收率1%,未检测到丁二酸。In a 100 mL stainless steel autoclave with a polytetrafluoroethylene liner, 8.2140 g (100 mmol) cyclohexene and 0.1997 g anhydrous Cu(CH3COO) 2 were dispersed in 50 mL with a molar concentration of 11 mol/L In the nitric acid solution, seal the reaction vessel, stir and heat up to 60 ºC. Stir the reaction at 60 °C reaction temperature, 500 rpm for 12.0 h. After the reaction was completed, it was cooled to room temperature, and the reaction product was analyzed and detected. The reaction results were as follows: the yield of adipic acid was 36%, the yield of glutaric acid was 1%, and no succinic acid was detected.
实施例44 (放大实验)Embodiment 44 (scale-up experiment)
在1000 mL具有聚四氟乙烯内胆的不锈钢高压反应釜中,将82.1400 g (1 mol)环己烯和1.9970 g无水Cu(CH3COO)2分散于500 mL摩尔浓度为11 mol/L硝酸溶液中,密封反应釜,搅拌升温到60℃反应温度、通入氧气至压力为(1.0 MPa)。于60℃反应温度、1.0 MPa 氧气压力,500 rpm搅拌反应12.0 h。反应完毕,冷却至室温,对反应产物进行分析检测,反应结果为:己二酸收率80%,戊二酸收率5%,丁二酸收率5%。In a 1000 mL stainless steel autoclave with polytetrafluoroethylene liner, 82.1400 g (1 mol) cyclohexene and 1.9970 g anhydrous Cu(CH 3 COO) 2 were dispersed in 500 mL with a molar concentration of 11 mol/L In the nitric acid solution, seal the reaction vessel, heat up to 60°C reaction temperature with stirring, and feed oxygen until the pressure is (1.0 MPa). The reaction temperature was 60°C, the oxygen pressure was 1.0 MPa, and the reaction was stirred at 500 rpm for 12.0 h. After the reaction was completed, it was cooled to room temperature, and the reaction product was analyzed and detected. The reaction results were as follows: the yield of adipic acid was 80%, the yield of glutaric acid was 5%, and the yield of succinic acid was 5%.
本说明书所述的内容仅仅是对发明构思实现形式的列举,本发明的保护范围不应当被视为仅限于实施例所陈述的具体形式。The content described in this specification is only an enumeration of the implementation forms of the inventive concepts, and the protection scope of the present invention should not be regarded as limited to the specific forms stated in the embodiments.
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