CN1023593C - Spiral tower - Google Patents

Spiral tower Download PDF

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Publication number
CN1023593C
CN1023593C CN 90103754 CN90103754A CN1023593C CN 1023593 C CN1023593 C CN 1023593C CN 90103754 CN90103754 CN 90103754 CN 90103754 A CN90103754 A CN 90103754A CN 1023593 C CN1023593 C CN 1023593C
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CN
China
Prior art keywords
tower
height
spiral
helicoid
present
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
CN 90103754
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Chinese (zh)
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CN1056823A (en
Inventor
邢林
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.)
Individual
Original Assignee
Individual
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Individual filed Critical Individual
Priority to CN 90103754 priority Critical patent/CN1023593C/en
Publication of CN1056823A publication Critical patent/CN1056823A/en
Application granted granted Critical
Publication of CN1023593C publication Critical patent/CN1023593C/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)

Abstract

The present invention relates to a spiral tower which belongs to gas liquid mass transfer equipment. The spiral tower with high separation efficiency is suitable for rectification and absorption. The height equivalent to one theoretical plate is less than 25mm, so that the height of the tower is greatly reduced.

Description

Spiral tower
The invention belongs to gas-liquid mass transfer (contact) equipment.
At present, widely used valve tower in distillation process, its distance between plates is 300-500mm.The wire netting ripple packed tower that separative efficiency is higher, its height equivalent to one theoretical plate (HETP) is also up to about 100mm.If design needs the rectifying column of 100 column plate separation requirement, select valve tower for use, then tower height reaches about 50m, selects wire netting ripple packed tower for use, and tower height also needs about 10m.Therefore, develop high efficiency knockout tower,, be convenient to operate positive effect for reducing tower height.
Reduce the height equivalent to one theoretical plate (HETP) of tower effectively, reducing tower height significantly is purpose of the present invention.
The present invention adopts helical structure, has helicoid 1 and spiral space 2 in the tower, and helicoid 1 is made up of the dictyosome material.During operation, gas rises along spiral space 2, and liquid descends along helicoid 1, forms gas phase and liquid phase contact interface thus, carries out gas-liquid mass transfer.
The present invention carries out the column efficiency test with ethanol-water solution under the infinite reflux condition,, in scope, in certain pitch scope, reach in certain gas speed scope at certain tower, record the height equivalent to one theoretical plate (HETP) of the present invention below 25mm, promptly the separating effect of every meter tower height reaches about 40 theoretical plates.In unit height, its separative efficiency is about 20 times of valve tower.Be about 4 times of wire netting ripple packed tower.In addition, void tower pressure drop of the present invention is little, has operating flexibility preferably.
The present invention is applicable to rectifying, absorbs.
In conjunction with the description of the drawings, narrate enforcement of the present invention: 1-helicoid, 2-spiral space, 3-outer cylinder body, 4-inner barrel.The helicoid of being made up of the dictyosome material 1 is connected on the cylindrical shell 3,4 that two diameters of coaxial line do not wait, and constitutes the spiral tower with helicoid 1 and spiral space 2.

Claims (1)

1, a kind of rectifying column is characterized in that the helicoid of being made up of wind body material (1) is connected on the outer cylinder body (3) and inner barrel (4) that two diameters of coaxial line do not wait, and constitutes the spiral tower with helicoid (1) and spiral space (2).
CN 90103754 1990-05-20 1990-05-20 Spiral tower Expired - Fee Related CN1023593C (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 90103754 CN1023593C (en) 1990-05-20 1990-05-20 Spiral tower

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN 90103754 CN1023593C (en) 1990-05-20 1990-05-20 Spiral tower

Publications (2)

Publication Number Publication Date
CN1056823A CN1056823A (en) 1991-12-11
CN1023593C true CN1023593C (en) 1994-01-26

Family

ID=4878232

Family Applications (1)

Application Number Title Priority Date Filing Date
CN 90103754 Expired - Fee Related CN1023593C (en) 1990-05-20 1990-05-20 Spiral tower

Country Status (1)

Country Link
CN (1) CN1023593C (en)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN100355475C (en) * 2005-09-22 2007-12-19 上海天之冠可再生能源有限公司 Highly efficient distilling filled tower
CN109499086B (en) * 2018-12-18 2023-08-22 北矿检测技术股份有限公司 Vacuum sleeve type multilayer rectifying tower
CN110420473B (en) * 2019-08-29 2021-08-24 四川华南无机盐有限公司 Self-lifting film evaporator and method for preparing high-concentration electronic-grade manganese nitrate
CN112093701B (en) * 2020-09-22 2021-10-01 中国空气动力研究与发展中心超高速空气动力研究所 Jacking structure and jacking device

Also Published As

Publication number Publication date
CN1056823A (en) 1991-12-11

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