Novel method for concentration-improving alcohol removing of alcohol-containing thin formaldehyde solution

A formaldehyde solution and a new method of technology, applied in the separation/purification of carbonyl compounds, organic chemistry and other directions, can solve the problems of long process flow, difficult processing, increased cost investment, etc., and achieve high rectification efficiency, simple equipment, and energy efficiency. consumption reduction effect

Inactive Publication Date: 2008-03-12
ZHEJIANG SANPO POLYMER
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0002] At present, the treatment of dilute formaldehyde is firstly used to produce urotropine, but urotropine is far from being able to consume the dilute formaldehyde by-produced in the production of formaldehyde downstream products; the other is to carry out secondary vacuum concentration, but still have to produce concentration Lower dilute formaldehyde; the third is direct emission, which seriously pollutes the environment
In the production of high-concentration formaldehyde required by some formaldehyde downstream products (such as paraformaldehyde), the methods used are all vacuum concentration, which will inevitably produce a large amount of dilute formaldehyde solution. The treatment of these dilute formaldehyde is more difficult and will cause Leading to too long process and increased cost investment

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0018] Send the dilute formaldehyde solution containing 15% alcohol and 1% aldehyde into the pressurized rectification tower, and carry out rectification under the conditions of pressure 2.0Mpa, temperature 200°C, and reflux ratio 3, and formaldehyde is obtained from the top of the pressurized rectification tower The concentration is 10% product, and the bottom product is organic waste water. The product obtained at the top of the pressurized rectification tower is sent to the second pressurized rectification tower, and rectification is continued under the conditions of pressure 1.5Mpa, temperature 150°C, and reflux ratio 10, and a 30% formaldehyde solution is obtained at the top of the tower. Send the product obtained from the top of the second pressurized rectification tower into a heat exchanger to cool to 120°C and then send it to the dealcoholization tower, continue rectification under the conditions of pressure 1.0Mpa, temperature 180°C, and reflux ratio 100, dealcoholiza...

Embodiment 2

[0020] Send the dilute formaldehyde solution containing 0.5% alcohol and 30% aldehyde into the pressurized rectification tower, and carry out rectification under the conditions of pressure 0Mpa, temperature 150°C, and reflux ratio 0.05, and formaldehyde concentration is obtained at the top of the pressurized rectification tower. The product is 65%, and the bottom product is organic waste water. The product obtained from the top of the pressurized rectification tower is sent to the heat exchanger to cool to 120°C and then sent to the dealcoholization tower, and the rectification is continued under the conditions of pressure 0Mpa, temperature 130°C, and reflux ratio 0.001, and the bottom of the dealcoholization tower A formaldehyde solution with a concentration of 67% is obtained, and a methanol solution with a concentration of 40% is obtained at the top of the tower.

Embodiment 3

[0022] Send the dilute formaldehyde solution containing 10% alcohol and 15% aldehyde into the pressurized rectification tower, and carry out rectification under the conditions of pressure 0.8Mpa, temperature 180°C, and reflux ratio 100, and formaldehyde is obtained from the top of the pressurized rectification tower The concentration is 55% of the product, and the bottom product is organic waste water. The product obtained from the top of the pressurized rectification tower is sent to the heat exchanger to cool to 120°C and then sent to the dealcoholization tower, and the rectification is continued under the conditions of pressure 0.5Mpa, temperature 140°C, and reflux ratio 50, and the dealcoholization tower A 60% formaldehyde solution is obtained at the bottom, and a 98% methanol solution is obtained at the top of the tower.

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Abstract

The present invention discloses a novel method by concentrating the diluted formaldehyde solution containing alcohol and eliminating the alcohol, belonging to the technological field of the concentration and elimination of the alcohol of the diluted formaldehyde solution containing alcohol; the diluted formaldehyde solution containing alcohol with the alcohol of 0.5 to 15 percent and the aldehyde of 1 to 30 percent is sent into the pressurization and rectification tower for rectification; the product with the formaldehyde concentration of 1.5 to 65 percent can be got on the top of the pressurization and rectification tower; the product on the bottom of the tower is the organic wastewater; the products on the top of the pressurization and rectification tower are sent to the heat exchanger and are cooled to be at the temperature between 80 and 120 DEG C; then the products are sent to the alcohol-doffing tower for the continuous rectification; the methanol solution with the concentration of 40 to 80 percent can be got on the top of the alcohol-doffing tower; the formaldehyde solution with the concentration of 2 to 67 percent can be got on the bottom. The present invention is of the large output and the high rectification efficiency; the formaldehyde can be diluted to have the concentration of the conventional formaldehyde product; at the same time, the separated methanol can be recycled used for the formaldehyde production and so on.

Description

technical field [0001] The invention discloses a new method for concentrating and removing alcohol from an alcohol-containing dilute formaldehyde solution, and belongs to the technical field of concentrating and removing alcohol from an alcohol-containing dilute formaldehyde solution. Background technique [0002] At present, the treatment of dilute formaldehyde is firstly used to produce urotropine, but urotropine is far from being able to consume the dilute formaldehyde by-produced in the production of formaldehyde downstream products; the other is to carry out secondary vacuum concentration, but still have to produce concentration Lower dilute formaldehyde; the third is direct emission, which seriously pollutes the environment. In the production of high-concentration formaldehyde required by some formaldehyde downstream products (such as paraformaldehyde), the methods used are all vacuum concentration, which will inevitably produce a large amount of dilute formaldehyde so...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07C47/058C07C45/82C07C31/08
Inventor 周赞斌傅大放程晔华
Owner ZHEJIANG SANPO POLYMER
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