A method for producing isoborneol

A production method and technology of isoborneol, applied in chemical instruments and methods, organic compound/hydride/coordination complex catalysts, organic chemistry, etc., can solve the problem of low selectivity, long reaction time, and difficulty in separation, etc. problems, to achieve the effect of reaction conversion rate and selectivity improvement, high selectivity and conversion rate, avoiding corrosion and pollution

Active Publication Date: 2016-03-16
NANJING ENETEKS +1
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Problems solved by technology

[0005] Chinese patent CN1408696A discloses a method for preparing isoborneol by one-step hydration of sulfuric acid as a catalyst, using a stirred tank reactor. This method simplifies the synthesis steps and reduces the amount of raw materials used, but due to the strong corrosion of sulfuric acid, the material of the equipment The requirements are high, and the subsequent separation is difficult, which is easy to cause pollution to the environment
Although this method has a higher conversion rate of camphene and the selectivity of isoborneol, the reaction time is long, the energy consumption is high, and the structure and composition of natural mordenite are greatly affected by the place of production, and the instability and fluctuation of its performance will lead to production is difficult to stabilize
In addition, the continuous separation and circulation reactor needs to add a large amount of solvent, the operation is complicated, the reaction time is long, and the actual production cost of the industry will be relatively high.
[0008] Chinese patent CN101973851A discloses a method for synthesizing isoborneol using synthetic molecular sieves as a catalyst. A fixed bed reactor is used to react at a reaction temperature of 120-180°C. The conversion rate of camphene is 80%-90%, and that of isoborneol is The selectivity is 73.3%-86.4%. This method does not use solvents, which is environmentally friendly and reduces the difficulty of separation in the downstream section. However, the reaction temperature is high, the selectivity is low, and the industry will also cause high production costs.
[0009] In addition, Chinese patent CN203112713U also discloses a reaction device for producing isoborneol by hydration of amphene. Compared with the traditional amphene hydration reaction and separation device, the device adds a membrane separation device between the fixed bed reactor and the separation system. , the device can concentrate the reaction liquid, increase the content of isoborneol, and reduce the subsequent energy consumption, but because the product mixture usually contains a small amount of fine catalyst particles, they are very easy to cause blockage to the separation membrane material and components, so the industrial practice Trouble occurs when applying

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  • A method for producing isoborneol

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Effect test

Embodiment 1

[0033] In the reaction system IRR, the volume of liquid flow enhanced submerged fixed bed reactor is 2m 3 (wherein the length-to-diameter ratio is 3:1), camphene, water and solvent enter the reactor at a mass ratio of 1:1:2 for reaction (the total mass is 1.4t). The catalyst bed is filled with a composite of two solid catalysts, Amberlyst15 and HZSM-5. The mass ratio of the two catalysts is 1:1, and the total mass is 35% (about 490kg) of the total liquid material mass of the first filler. The solvent is a compound of chloroform and methyl ethyl ketone, and the molar ratio is 1:0.5. The reaction temperature is 55° C., the pressure is 0.1 MPa, and the average residence time of the reaction materials in the reactor is 55 minutes. The self-priming interface 8 is set at 1 / 3 above the busbar on the outer wall of the reactor. The circulating volume of circulation pump P-1 per hour is 20 times of the total material (including solvent) in the reactor (about 30m 3 / h). The reacted m...

Embodiment 2

[0035] In the same reaction system IRR as in Example 1, the liquid flow enhanced submerged fixed bed reactor volume is 4m 3 (where the aspect ratio is 2.5:1), camphene, water and solvent enter the reactor at a mass ratio of 1:0.15:2 (the total mass is 2.8t) for reaction. The catalyst bed is filled with a composite of three solid catalysts, Amberlyst35, D72 and ZSM-35. The mass ratio of the three catalysts is 1:0.5:1, and the total mass is 28% (about 790kg) of the total mass of the liquid material loaded for the first time. The solvent is a compound of chloroform, nitroethane and acetonitrile, and the molar ratio is 1:0.5:0.5. The reaction temperature is 45° C., and the pressure is 0.12 MPa. The average residence time of the reaction materials in the reactor is 1 h. The self-priming interface 8 is set at 1 / 3 above the busbar on the outer wall of the reactor. The circulating volume of circulation pump P-1 per hour is 15 times of the total material (including solvent) in the r...

Embodiment 3

[0037] In the same reaction system IRR as in Example 1, the liquid flow enhanced submerged fixed bed reactor volume is 3m 3 (The aspect ratio is 4:1). Camphene, water and solvent enter the reactor at a mass ratio of 1:0.15:1 (about 2.1t) for reaction. The catalyst bed is loaded with a composite of three solid catalysts, Amberlyst36, NKC-9 and MCM-41, the mass ratio of the three catalysts is 1:1:1, and the total mass is 25% of the mass of the total liquid material loaded for the first time (about 530kg ) The solvent is a compound of dimethylformamide, chloroacetonitrile and nitromethane, and the molar ratio is 1:0.5:1. The reaction temperature is 88° C., the pressure is 0.25 MPa, and the average residence time of the reaction materials in the reactor is 65 minutes. The circulating volume of circulation pump P-1 per hour is 16 times (about 32t / h) of the total material (including solvent) in the reactor. The reacted material is discharged through the pipeline 4 and the valve V...

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Abstract

The invention provides an isoborneol production method which is carried out in a reinforced radial flow reaction system (IRR) composed of a liquid flow reinforced immersed fixed bed reactor. The isoborneol production method comprises the following steps: mixing the raw materials and a composite solvent by adopting a certain quantity of composite solid acid catalyst according to a certain ratio, wherein camphene and water are used as the raw materials; carrying out hydration reaction in an IRR reaction-separation system to obtain an isoborneol product. The reaction temperature is 40-90 DEG C, the mass of the catalyst is 15-50% of the total mass of the firstly-filled liquid material, the ratio of the camphene to the water to the composite solvent is 1:(0.15-2):(0.5-4), the reaction pressure is 0.1-0.3MPa, and the reaction standing time is 40-70min. After the reacted materials are separated and subjected to ion exchange, the solvent and the unreacted materials are returned to the reactor, and the product is stored. The isoborneol production method has the advantages that the industrial reliability is good, the per-pass conversion rate of the camphene is high, the isoborneol is good in selectivity, and the energy consumption per unit product is only about 60% of that of the traditional fixed bed process.

Description

field of invention [0001] The invention relates to a method for producing isoborneol. Background technique [0002] Isoborneol, also known as isoborneol, is a white translucent crystal with a special odor. It is an isomer of borneol, and its molecular formula is C 10 h 18 O, molecular weight 154.25, melting point 208-214°C. Isoborneol is an intermediate in the synthesis of camphor, and it is also widely used in the fields of spices and medicine. [0003] At present, the synthesis method of isoborneol in industry mainly contains two kinds of processes: indirect method and direct method: [0004] The first is the esterification reaction of amphene and acetic acid to generate isoborneol acetate, which is then saponified to generate isoborneol; the second is the direct hydration of amphene under the action of an acidic catalyst to generate isoborneol. The indirect method is relatively mature, but the process is complicated and the consumption of raw materials is high; althou...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C07C35/30C07C29/04B01J31/10
CPCC07C29/04C07C2602/38C07C35/30
Inventor 杨高东林力克周政王宝荣张志炳
Owner NANJING ENETEKS
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