CN203960087U - High pressure alcohol wash system - Google Patents

High pressure alcohol wash system Download PDF

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Publication number
CN203960087U
CN203960087U CN201420363431.XU CN201420363431U CN203960087U CN 203960087 U CN203960087 U CN 203960087U CN 201420363431 U CN201420363431 U CN 201420363431U CN 203960087 U CN203960087 U CN 203960087U
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CN
China
Prior art keywords
alcohol
alcohol wash
thick
wash tower
desalination tank
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
CN201420363431.XU
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Chinese (zh)
Inventor
钮德根
赵勇群
刘宏伟
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
ANHUI QUANSHENG CHEMICAL CO LTD
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ANHUI QUANSHENG CHEMICAL CO LTD
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Filing date
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Application filed by ANHUI QUANSHENG CHEMICAL CO LTD filed Critical ANHUI QUANSHENG CHEMICAL CO LTD
Priority to CN201420363431.XU priority Critical patent/CN203960087U/en
Application granted granted Critical
Publication of CN203960087U publication Critical patent/CN203960087U/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Abstract

A kind of high pressure alcohol wash system, relates to chemical technology field, comprises desalination tank, described desalination tank is connected to alcohol wash tower by alcohol wash pump, de-salted water and the alcohol pneumatic transmission of assigning to is entered to alcohol wash tower, and after alcohol wash tower is processed, gas enters alkanisation operation, thick alcohol enters thick alcohol flash drum, thick alcohol outlet at described alcohol wash tower is connected to desalination tank by circulation line, sends into alcohol wash tower after desalination tank is processed again, and alcohol wash is washed the thick alcohol obtaining, through juice circulation, be disposed to thick alcohol flash drum after up to standard.The utility model is simple in structure, modern design, and after operational path transformation, product determining alcohol is effectively controlled, and has both reduced the alcohol content going in alkanisation system gas, alleviates the impact on alkanisation system; Simultaneously by-product methyl alcohol.

Description

High pressure alcohol wash system
Technical field
The utility model relates to chemical technology field, is specifically related to a kind of high pressure alcohol wash system.
Background technology
The original flow setting of high pressure alcoholization system: alcohol wash be after washing directly by wash thick alcohol discharge.But so thick determining alcohol cannot be controlled, simultaneously because our factory is without smart alcohol operation, the too low thick alcohol of concentration cannot concentrate, is unfavorable for selling etc.In production, attempt by the alcohol wash pump shortcut control water yield, to no effect; Set up frequency transformer to pump afterwards, still uncontrollable determining alcohol.
Utility model content
Technical problem to be solved in the utility model is to provide a kind of and forms simply, good in economic efficiency high pressure alcohol wash system.
Technical problem to be solved in the utility model realizes by the following technical solutions:
A kind of high pressure alcohol wash system, comprise desalination tank, described desalination tank is connected to alcohol wash tower by alcohol wash pump, and de-salted water and the alcohol pneumatic transmission of assigning to is entered to alcohol wash tower, after alcohol wash tower is processed, gas enters alkanisation operation, and thick alcohol enters thick alcohol flash drum, is connected to desalination tank in the thick alcohol outlet of described alcohol wash tower by circulation line, after processing again, desalination tank sends into alcohol wash tower, alcohol wash is washed the thick alcohol obtaining, and through juice circulation, is disposed to thick alcohol flash drum after up to standard.
The beneficial effects of the utility model are: the utility model is simple in structure, modern design, and after operational path transformation, product determining alcohol is effectively controlled, and has both reduced the alcohol content going in alkanisation system gas, alleviates the impact on alkanisation system; Simultaneously by-product methyl alcohol, through measuring and calculating and actual metered, therefore transform every day and the economic benefit that directly obtains is the thick alcohol/sky of 5t, signature coal 2500t/, and the cost increasing is only about 5m ¢ 57 pipeline material expenses, this reconstruction flow is simple, but abnormal practical and efficient.
Brief description of the drawings
Fig. 1 is the utility model systematic schematic diagram.
Embodiment
For technique means, creation characteristic that the utility model is realized, reach object and effect is easy to understand, below in conjunction with concrete diagram, further set forth the utility model.
As shown in Figure 1, a kind of high pressure alcohol wash system, comprises desalination tank, described desalination tank is connected to alcohol wash tower by alcohol wash pump, de-salted water and the alcohol pneumatic transmission of assigning to is entered to alcohol wash tower, and after alcohol wash tower is processed, gas enters alkanisation operation, thick alcohol enters thick alcohol flash drum, thick alcohol outlet at described alcohol wash tower is connected to desalination tank by circulation line, sends into alcohol wash tower after desalination tank is processed again, and alcohol wash is washed the thick alcohol obtaining, through juice circulation, be disposed to thick alcohol flash drum after up to standard.
After operational path transformation, product determining alcohol is effectively controlled, and has both reduced the alcohol content going in alkanisation system gas, alleviates the impact on alkanisation system; Simultaneously by-product methyl alcohol, through measuring and calculating and actual metered, therefore transform and the economic benefit that directly obtains is the thick alcohol/sky of 5t signature coal 2500t/, and the cost increasing is only about 5m ¢ 57 pipeline material expenses every day.This reconstruction flow is simple, but abnormal practical and efficient.
More than show and described ultimate principle of the present utility model and principal character and advantage of the present utility model.The technician of the industry should understand; the utility model is not restricted to the described embodiments; that in above-described embodiment and specification sheets, describes just illustrates principle of the present utility model; do not departing under the prerequisite of the utility model spirit and scope; the utility model also has various changes and modifications, and these changes and improvements all fall within the scope of claimed the utility model.The claimed scope of the utility model is defined by appending claims and equivalent thereof.

Claims (1)

1. a high pressure alcohol wash system, it is characterized in that: comprise desalination tank, described desalination tank is connected to alcohol wash tower by alcohol wash pump, de-salted water and the alcohol pneumatic transmission of assigning to is entered to alcohol wash tower, described alcohol wash tower connects thick alcohol flash drum, and the thick alcohol outlet of described alcohol wash tower is connected to desalination tank by circulation line.
CN201420363431.XU 2014-07-02 2014-07-02 High pressure alcohol wash system Expired - Fee Related CN203960087U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201420363431.XU CN203960087U (en) 2014-07-02 2014-07-02 High pressure alcohol wash system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201420363431.XU CN203960087U (en) 2014-07-02 2014-07-02 High pressure alcohol wash system

Publications (1)

Publication Number Publication Date
CN203960087U true CN203960087U (en) 2014-11-26

Family

ID=51920696

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201420363431.XU Expired - Fee Related CN203960087U (en) 2014-07-02 2014-07-02 High pressure alcohol wash system

Country Status (1)

Country Link
CN (1) CN203960087U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113521968A (en) * 2021-08-17 2021-10-22 安徽金禾实业股份有限公司 Device and method for purifying alcohol post-gas in ammonia synthesis system

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113521968A (en) * 2021-08-17 2021-10-22 安徽金禾实业股份有限公司 Device and method for purifying alcohol post-gas in ammonia synthesis system

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Legal Events

Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20141126

Termination date: 20210702

CF01 Termination of patent right due to non-payment of annual fee