Internal pressure vacuum membrane distillation concentration method of ethylene glycol solution

A vacuum membrane distillation and ethylene glycol technology, which is applied to the internal pressure vacuum membrane distillation technology to concentrate and process ethylene glycol solution, and the use of membrane distillation technology to concentrate and process the ethylene glycol solution field can solve problems such as membrane hydrophilicity and achieve treatment High efficiency, reduced hydrophilization problems, low operating pressure effects

Active Publication Date: 2017-07-28
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Although the patent and literature use membrane distillation technology to process polyol aqueous solution, the patent and literature use internal pressure membrane distillation, and the membrane material is polypropylene (PP). membrane hydrophilicity

Method used

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  • Internal pressure vacuum membrane distillation concentration method of ethylene glycol solution

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0038] process flow advice figure 1 .

[0039] The main water quality characteristics of the ethylene glycol solution in the ethylene glycol hydration process of ethylene oxide are: monoethylene glycol (MEG) 14% (wt), diethylene glycol (DEG) 0.5% (wt), triethylene glycol Alcohol (TEG) 0.5% (wt), the rest is ethylene glycol aqueous solution of water.

[0040] The membrane module used is a polytetrafluoroethylene (PTFE) hollow fiber hydrophobic membrane module with a membrane pore size of 0.2 μm. There are two groups of hollow fiber hydrophobic membrane modules, which are used alternately. The process is as follows:

[0041] First, pump the ethylene glycol aqueous solution at a temperature of 90°C into the raw water tank; secondly, pump the ethylene glycol aqueous solution in the raw water tank into the tube side of the hollow fiber membrane module at a specific membrane surface flow rate through the feed pump; finally, pump the The permeation side of the hollow fiber membra...

Embodiment 2

[0046] process flow advice figure 1 . The main water quality characteristics of the ethylene glycol solution in the ethylene glycol hydration process are the same as in Example 1.

[0047] The membrane module used is a polytetrafluoroethylene (PTFE) hollow fiber hydrophobic membrane module with a membrane pore size of 0.2 μm. There are two groups of hollow fiber hydrophobic membrane modules, which are used alternately. The process is as follows:

[0048] First, pump the ethylene glycol aqueous solution with a temperature of about 85°C into the raw water tank; secondly, pump the ethylene glycol aqueous solution in the raw water tank into the tube side of the hollow fiber membrane module at a specific membrane surface flow rate through the feed pump; finally, Vacuumize the permeate side of the hollow fiber membrane module, that is, the shell side. Under the action of vacuuming, the water vapor in the ethylene glycol aqueous solution passes through the membrane pores and conde...

Embodiment 3

[0053] process flow advice figure 1 . The main water quality characteristics of the ethylene glycol solution in the ethylene glycol hydration process are the same as in Example 1.

[0054] The membrane module used is a polytetrafluoroethylene (PTFE) hollow fiber hydrophobic membrane module with a membrane pore size of 0.2 μm. There are two groups of hollow fiber hydrophobic membrane modules, which are used alternately. The process is as follows:

[0055] First, pump the ethylene glycol aqueous solution at a temperature of about 95°C into the raw water tank; secondly, pump the ethylene glycol aqueous solution in the raw water tank into the tube side of the hollow fiber membrane module at a specific membrane surface flow rate through the feed pump; finally, Vacuumize the permeate side of the hollow fiber membrane module, that is, the shell side. Under the action of vacuuming, the water vapor in the ethylene glycol aqueous solution passes through the membrane pores and condens...

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Abstract

The invention discloses an internal pressure vacuum membrane distillation concentration method for ethylene glycol solution, which adopts the internal pressure vacuum membrane distillation technology coupled with rectification technology to carry out the ethylene glycol solution in the ethylene glycol hydration process. Concentration and purification treatment. First, pump the ethylene glycol aqueous solution with a temperature of about 85°C to 100°C into the raw water tank; secondly, pump the ethylene glycol aqueous solution in the raw water tank into the tube side of the hollow fiber membrane module at a specific membrane surface flow rate through the feed pump ;Finally, vacuumize the permeate side of the hollow fiber membrane module, that is, the shell side, and the condensable gas will be condensed on the permeate side through the condenser to form produced water, and the relatively concentrated ethylene glycol solution in the tube side of the membrane module will return to the raw water tank for circulation concentrate. Compared with multi-effect evaporation, the method of the invention has the advantages of less equipment investment, high treatment efficiency, low operating temperature, low operating pressure, low energy consumption and the like.

Description

technical field [0001] The invention relates to a method for concentrating ethylene glycol solution in the ethylene glycol hydration process of ethylene oxide, in particular to a method for concentrating and treating ethylene glycol solution using membrane distillation technology, and more specifically, to an internal A method for concentrating and treating ethylene glycol solution by pressure-type vacuum membrane distillation technology. Background technique [0002] At present, ethylene glycol is mostly produced by hydrolysis of ethylene oxide, and the prepared dilute ethylene glycol solution (mass concentration 15%) is evaporated and concentrated by a downstream multi-effect evaporation tower, and the solution concentration reaches approximately equal to 85% (mass). , sent to the crude ethylene glycol storage tank. The crude ethylene glycol containing 15% (mass) water is dehydrated and aldehyde discharged in the dehydration tower, and the bottom liquid of the tower is se...

Claims

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Application Information

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Patent Type & AuthorityPatents(China)
IPC IPC(8): B01D61/36C07C31/20C07C29/78
Inventor张新妙杨永强彭海珠
OwnerCHINA PETROLEUM & CHEM CORP