Process for producing neopentyl glycol by continuous catalytic hydrogenation

A neopentyl glycol, catalytic hydrogenation technology, applied in the field of fine chemicals, can solve the problems of high equipment investment and operating costs, affecting product yield and quality, complex catalyst system, etc., to achieve good anchoring and stabilizing effects, Reduce subsequent separation costs, low equipment investment and low operating costs

Active Publication Date: 2021-03-23
上海翼湍科技有限责任公司 +1
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Problems solved by technology

According to the catalytic process used to convert hydroxypivalaldehyde into neopentyl glycol, it can be divided into two types: formaldehyde disproportionation method and catalytic hydrogenation method. Among them, the formaldehyde disproportionation method uses a strong alkali catalyst, which is characterized by mild process conditions and simple operation. Large consumption will form a large amount of by-product formate, which is difficult to separate, resulting in poor product quality, more waste water discharge, and great pressure on environmental protection
At present, the production technology of neopentyl glycol at home and abroad has been gradually replaced by the catalytic hydrogenation method. This process has low raw material consumption, outstanding environmental protection advantages, high product quality, and is suitable for deep processing of downstream products. The disadvantage is that the operation is relatively complicated and uses medium and high pressure. Hydrogenation equipment, equipment investment is relatively high
[0004] In the process of synthesizing

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  • Process for producing neopentyl glycol by continuous catalytic hydrogenation
  • Process for producing neopentyl glycol by continuous catalytic hydrogenation
  • Process for producing neopentyl glycol by continuous catalytic hydrogenation

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Embodiment Construction

[0026] process such as figure 1 As shown, the hydrogenation raw material of hydroxypivalaldehyde raw material produced by organic amine catalyzed isobutyraldehyde and formaldehyde, after simple separation of unreacted light components such as isobutyraldehyde and formaldehyde, the corresponding composition is shown in Table 1. The above-mentioned hydrogen and the raw material (the molar ratio of hydrogen to aldehyde is 1.1-3:1) directly enter the transfer heat hydrogenation reactor R301 (with steam drum V301) from the upper opening of the reactor to undergo hydrogenation reaction, and the hydrogenated product is firstly hydrogenated. Hydrogen outlet separator S301 gas-liquid separation, the separated gas phase components mainly contain hydrogen, part of which is returned to the inlet of transfer heat hydrogenation reactor R301 for recycling, and the rest is discharged as relaxation gas; the separated liquid phase product is then delightened The neopentyl glycol product with a ...

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Abstract

The invention discloses a process for producing neopentyl glycol by continuous catalytic hydrogenation, which solves the problems of complex operation, long flow and high investment and cost in the traditional neopentyl glycol production process, and adopts the technical scheme that a hydroxypivalaldehyde hydrogenation raw material and hydrogen are directly fed into a heat transfer hydrogenation reactor filled with a hydrogenation catalyst for reaction; a reaction product is led out from the bottom of the reactor and sent into a hydrogenation outlet separator for gas-liquid separation, one part of the separated gas returns to an inlet of the heat transfer hydrogenation reactor for cyclic utilization, and the other part of the separated gas is exhausted as purge gas; the separated liquid istreated through a light component removal tower and a heavy component removal tower to obtain a refined neopentyl glycol product; and the hydrogen-aldehyde molar ratio of the hydrogen to the hydroxypivalaldehyde hydrogenation raw material is (1.1-3): 1. The method has the advantages of simple process, short flow, mild reaction conditions, no need of additional addition of an organic solvent or separation and refining, energy saving, consumption reduction, low production cost and investment cost, and high yield.

Description

technical field [0001] The invention relates to the field of fine chemical industry, in particular to a process for continuously catalytic hydrogenation to produce neopentyl glycol. Background technique [0002] As an important diol product, neopentyl glycol (NPG) is currently mainly used in the production of polyester resins for powder coatings and saturated polyester resins for coil steel (accounting for about 70% of the consumption of neopentyl glycol ), unsaturated polyester resin and alkyd resin chemical products. [0003] The production method of neopentyl glycol in industry usually uses isobutyraldehyde and formaldehyde as raw materials, and prepares neopentyl glycol through hydroxypivalaldehyde (2,2-dimethyl 3-hydroxypropanal) intermediate. According to the catalytic process used to convert hydroxypivalaldehyde into neopentyl glycol, it can be divided into two types: formaldehyde disproportionation method and catalytic hydrogenation method. Among them, the formaldeh...

Claims

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Application Information

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IPC IPC(8): C07C29/141C07C31/20
CPCC07C29/141C07C31/20
Inventor 张大洲卢文新刘佳肖敦峰吴殊斌张威夏吴
Owner 上海翼湍科技有限责任公司
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