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Device and process for preparing methanol and butyl acetate

A technology of butyl acetate and methyl acetate, which is applied in the field of reactive distillation-pervaporation integrated methanol and butyl acetate preparation equipment, can solve the problems of high technical energy consumption and complicated equipment, and achieve simple technical route, low equipment investment and low cost. The effect of reduced production cost and easy source

Pending Publication Date: 2020-02-04
JIANGSU JIUMO HIGH TECH CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

In addition, although the industrial application value of the reactant methyl acetate is not high, as a by-product of PVA production, it generally exists in the form of a mixture with methanol, and extraction and distillation methods are required to separate and purify methyl acetate, so the energy consumption of the whole set of technology is relatively high , the equipment is more complex

Method used

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  • Device and process for preparing methanol and butyl acetate

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0054] Using the above-mentioned device to prepare methanol and butyl acetate, the working temperature of the membrane module is 40°C, as follows:

[0055] The polyvinyl alcohol (PVA) industry by-produces a large number of methyl acetate-methanol compounds, a typical composition of which is MM20 (70 wt% methanol, 30 wt% methyl acetate). As a typical by-product in the polyvinyl alcohol production industry, methyl acetate-methanol mixture A (70 wt% methanol and 30 wt% methyl acetate) first enters the second pervaporation membrane system 1 for the separation of methyl acetate and methanol. Complete separation, methanol C (99.2mol%) is obtained on the permeate side, and the retentate side is mixed with the return stream and enters the tower from the inlet of methyl acetate, and carries out transesterification reaction with the raw material n-butanol B in the presence of AMBERLYST™ 15 solid acid catalyst, The amount of catalyst used is 10% of the mass of the feed methyl acetate. T...

Embodiment 2

[0057] Using the above-mentioned device to prepare methanol and butyl acetate, the working temperature of the membrane module is 60°C, the details are as follows:

[0058] Polyvinyl alcohol (PVA) industry produces a large number of methyl acetate-methanol compounds, a typical composition of which is MM80 (35 mol% methanol, 65 mol% methyl acetate, approximately azeotropic composition). A typical azeotrope methyl acetate-methanol mixture A (53.5°C, 35 mol% methanol and 65 mol% methyl acetate) in the polyvinyl alcohol production industry first enters the second pervaporation membrane system 1 for methyl acetate and methanol The complete separation of methanol C (99.0mol%) is obtained on the permeate side, and the retentate side is mixed with the return stream and enters the tower from the inlet of methyl acetate, and the raw material n-butanol B is in the ionic liquid [HSO 3 -bHim]HSO 4 The transesterification reaction is carried out in the presence of a catalyst, and the amount...

Embodiment 3

[0060] Using the above device to prepare methanol and butyl acetate, the working temperature of the membrane module is 30°C, the details are as follows:

[0061] Polyvinyl alcohol (PVA) industry produces a large number of methyl acetate-methanol compounds, a typical composition of which is MM80 (35 mol% methanol, 65 mol% methyl acetate, approximately azeotropic composition). A typical azeotrope methyl acetate-methanol mixture A (53.5°C, 35 mol% methanol and 65 mol% methyl acetate) in the polyvinyl alcohol production industry first enters the second pervaporation membrane system 1 for methyl acetate and methanol The complete separation of methanol C (99.0mol%) is obtained on the permeate side, and the retentate side is mixed with the return stream and enters the tower from the inlet of methyl acetate, and carries out transesterification reaction with the raw material n-butanol B in the presence of AMBERLYST™ 15 solid acid catalyst , The amount of catalyst used is 20% of the qua...

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Abstract

The invention relates to a device and a process for preparing methanol and butyl acetate. The device comprises a reaction distillation column and a first pervaporation membrane separation system, wherein the n-butyl alcohol inlet of the reaction distillation column is formed above a methyl acetate inlet; a reboiler is connected with the bottom of the reaction distillation column; a total condenseris connected with a recovery hole in the top of the reaction distillation column; the outlet of the total condenser is connected with the reaction distillation column and the first pervaporation membrane separation system respectively; the penetrating fluid outlet of the first pervaporation membrane separation system is connected with a methanol outlet; and a penetration residual liquid outlet isconnected with the methyl acetate inlet. By adopting the device and the process, a reaction distillation-pervaporation integration process is adopted to prepare methanol and butyl acetate with high purity, the reflux ratio is greatly reduced, the volume of the reaction distillation column can be reduced, the reactant, namely the methyl acetate, is easy to obtain, large-size refining equipment canbe avoided, the technical route is simple, the energy consumption is low, environment pollution is avoided, equipment investment and production cost can be remarkably reduced, and requirements of energy conservation and emission reduction can be met.

Description

technical field [0001] The invention relates to methanol and butyl acetate preparation technology, in particular to a reactive distillation-pervaporation integrated methanol and butyl acetate preparation device and process. Background technique [0002] N-butyl acetate, also known as butyl acetate, is a colorless, transparent, fruity, flammable, volatile, and insoluble liquid. It has excellent solubility and can be miscible with organic solvents such as alcohols, ethers, and ketones. It is an important organic solvent, extraction agent, and dehydrating agent. It can also be used as a component of fragrance compounding agent and fragrance agent, and has wide industrial uses. In recent years, with the increasingly stringent environmental protection regulations worldwide and the continuous enhancement of people's environmental awareness, people tend to use n-butyl acetate as a good substitute for toxic and harmful solvents such as toluene and xylene, so its market prospect is b...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01D61/36C07C29/128C07C67/03C07C69/14C07C31/04B01D3/00B01D67/00B01D69/12B01D71/76B01J4/00B01J19/00B01J19/24
CPCB01D61/362B01D71/76B01D69/125B01D67/0079C07C67/03C07C29/1285B01J19/24B01J19/0006B01J4/001B01D3/009C07C69/14C07C31/04Y02P20/10
Inventor 丁晓斌王成涂睿赵祥强
Owner JIANGSU JIUMO HIGH TECH CO LTD
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