Method for coproducing cyclohexanol and alkanol

A cyclohexane and cyclohexanol technology, applied in the field of co-production of cyclohexanol and alkanol, can solve the problems of increased energy consumption, slow rate, low reaction efficiency, etc.

Inactive Publication Date: 2015-04-29
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0009] The first disadvantage of the cyclohexane oxidation method is that cyclohexanol (ketone) is more easily oxidized than cyclohexane, so in order to ensure a certain selectivity, the conversion rate of cyclohexane must be controlled at a very low level , a large amount of unreacted cyclohexane needs to be separated by distillation and re-oxidized, which greatly increases the energy consumption of the whole process
The second shortcoming that cyclohexane oxidation method exists is: even if the conversion ratio of cyclohexane is controlled at a low level, still produce quite a lot of low-value by-products in the reaction process, not only reduces the yield of product, but also Increased difficulty in separating products
The third disadvantage of the cyclohexane oxidation method is that the organic by-products produced during the oxidation process are very complex and can only be removed by alkaline washing. The resulting large amount of waste lye not only has a COD value of up to 10 5 ~10 6 mg / L, and not biodegradable, it is still a worldwide environmental problem
[0012] However, the method of Asahi Kasei still has the following deficiencies
[0013] (1) There are thermodynamic limitations in the direct hydration of cyclohexene, and the solubility of cyclohexene in water is very small. The hydration reaction mainly occurs at the two-phase interface, which leads to a slow rate of cyclohexene hydration reaction and a single-pass conversion rate. Very low, such as adopting high-silicon ZSM-5 catalyst, staying in two series slurry reactors for 2h, the conversion rate of cyclohexene is only 12.5%. Separation from the product stream for recycling, which significantly increases the energy consumption of the process
[0014] (2) It is necessary to use high-purity cyclohexene as a raw material, otherwise, due to the dilution of other components, it will lead to more recycled materials and lower reaction efficiency. However, cyclohexene is prepared by partial hydrogenation of benzene, In addition to cyclohexene, the product stream also contains a considerable amount of cyclohexane and benzene. The boiling points of these three are very close, making the purification of cyclohexene very difficult.

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  • Method for coproducing cyclohexanol and alkanol
  • Method for coproducing cyclohexanol and alkanol
  • Method for coproducing cyclohexanol and alkanol

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0131] This example is used to illustrate the method for producing cyclohexene source through partial hydrogenation of benzene.

[0132] Benzene and hydrogen are injected into the hydrogenation reactor filled with ruthenium particle catalyst at a molar ratio of 1:3, and the benzene hydrogenation reaction is carried out under the conditions of a reaction temperature of 135°C, a pressure of 4.5MPa, and a residence time of 15 minutes, and the reaction product is separated After hydrogen evolution, the liquid product was collected. Continuous operation 1000h. After the test, gas chromatographic analysis was performed on the collected liquid products, and the composition was 53.3% of benzene, 35.4% of cyclohexene, and 11.3% of cyclohexane in terms of mass percentage.

Embodiment 2

[0136] This example is used to illustrate the method of esterifying acetic acid with cyclohexene / cyclohexane / benzene.

[0137] The high-temperature-resistant sulfonic acid ion exchange resin (the brand name is Amberlyst 45, produced by Rhom&Hass Company) is crushed into a powder with a particle size of less than 200 mesh (0.074mm) with a multi-stage high-speed pulverizer, and pore-forming agents, lubricants, and antioxidants are added. The agent and adhesive are mixed evenly on a high-speed mixer, and then internally kneaded on an internal mixer at 180°C for 10 minutes to make the material completely plasticized, and then injected into a mold to make a Raschig ring with a diameter of 5mm, a height of 5mm, and a wall thickness of 1mm. type resin catalyst filler. Put 1950mL of this catalyst packing into the middle of the model reaction tower (filling height is 1m, equivalent to 8 theoretical trays), and put 1950mL of glass spring packing with a diameter of 3mm and a length of 6m...

Embodiment 3

[0147] This example is used to illustrate the method of esterifying acetic acid with cyclohexene / cyclohexane / benzene.

[0148] The ball type H of φ3~4 0.5 Cs 2.5 PW 12 o 40 / SiO 2 Catalyst (by H 0.5 Cs 2.5 PW 12 o 40 Powder and coarse-porous silica gel powder with a particle size of less than 200 meshes are fully mixed in a mixer, rolled into balls in a sugar coating machine with silica sol as a binder, and then dried and roasted) sandwiched into titanium wire mesh waves In the plate, a cylindrical structured packing with a diameter of 50 mm and a height of 50 mm was made. Put 1L of this packed catalyst into the middle of the model reaction tower (the packing height is 1m, equivalent to 12 theoretical trays), and put 1950mL glass spring packing with a diameter of 4mm and a height of 4mm at the top and bottom (the packing height is 1m, equivalent to at 15 theoretical plates).

[0149] The cyclohexene raw material and acetic acid were pumped into the preheater by the m...

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Abstract

The invention provides a method for coproducing cyclohexanol and alkanol. The method comprises the following steps: preparing benzene and/or cyclohexane into cyclohexene, carrying out addition-esterification on the cyclohexene in a catalytic distillation tower, obtaining carboxylic acid/ cyclohexyl carboxylate material flow at the bottom of the tower, hydrogenating the material flow to obtain the cyclohexanol and the alkanol. The esterification and hydrogenation reactions in the method have high conversion rate and selectivity, and high atom economy; the process is environment-friendly; the alkanol is coproduced when the cyclohexanol is produced, in particular, when acetic acid is used, the cheap acetic acid is converted into ethanol with high cost and large market capacity in an indirect manner, so as to increase the economical efficiency of the process.

Description

technical field [0001] The invention relates to a method for co-producing cyclohexanol and alkanol, and also relates to a method for producing cyclohexanone and a method for producing caprolactam. Background technique [0002] Both cyclohexanol and ethanol are important chemical raw materials and solvents. Cyclohexanol is mainly used for dehydrogenation of cyclohexanone, and cyclohexanone is not only the main intermediate for the further production of nylon 6 and nylon 66, but also widely used in paints, pesticides, dyes, aviation lubricants, grease, wax, Solvent for film removal, decontamination, spot removal, etc. Ethanol is not only a raw material for synthetic esters and other chemical products, but also widely used as a fuel additive for gasoline. [0003] The method of industrially synthesizing ethanol is mainly the direct hydration method of ethylene, but in some countries rich in agricultural and sideline products, the fermentation method is still the main method o...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07C35/08C07C31/02C07C31/08C07C29/149C07C45/29C07C49/303C07D223/10C07C13/20C07C5/333
CPCC07C5/3337C07C5/367C07C29/149C07C45/29C07C67/04C07C2601/14C07C2601/16C07D223/10C07C13/20C07C69/14C07C31/08C07C35/08C07C15/04C07C49/303Y02P20/10Y02P20/52
Inventor 宗保宁谭怀山马东强孙斌温朗友杨克勇吴明李楚新
Owner CHINA PETROLEUM & CHEM CORP
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