CN101480537B - Novel turbogrid type composite column plate - Google Patents

Novel turbogrid type composite column plate Download PDF

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Publication number
CN101480537B
CN101480537B CN 200810000614 CN200810000614A CN101480537B CN 101480537 B CN101480537 B CN 101480537B CN 200810000614 CN200810000614 CN 200810000614 CN 200810000614 A CN200810000614 A CN 200810000614A CN 101480537 B CN101480537 B CN 101480537B
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plate
draining
column
sieve
plates
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CN 200810000614
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CN101480537A (en
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田原宇
乔英云
盖希坤
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Shandong University of Science and Technology
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Shandong University of Science and Technology
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  • Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)

Abstract

The invention provides a draining composite column plate which is mainly used for fully utilizing the space in a column, improving the vapor-liquid mass transfer status of draining column plates, reducing the pressure drop of the column plate, reducing the entrainment, and improving the processing capacity, the operating elasticity and the separating efficiency of the draining column plates through arranging draining sieve plates with identical opening ratio on the draining column plates in a staggered manner and a layer of high regular filling material of 100-250 mm under the draining column plates. The novel draining composite column plate adopts the structure that 20-60 percent of sieve pores are arranged on the draining column plates; sieve plates with identical opening ratio are arranged in the position 3-6 mm away from the upper parts of the draining column plates; each sieve opening can be a circular hole with the diameter of 3-20 arranged on a plate of 2-10 mm, a diamond hole with equivalent opening area, and a strip-shaped bulge with a slot on the lateral surface; the circular hole, the diamond hole or the strip-shaped bulge on each sieve plate and the circular hole, the diamond hole or the strip-shaped bulge on each draining column plate are arranged in a staggered manner or a half staggered manner; the high regular filling material with the height of 100-250 mm is fixed under the draining composite column plate through a self bearing beam; upper bearing beams of the sieve plates are fixed among the plates of the composite column plate when the composite column plate is mounted; and the plate and a supporting ring are fixed by a connecting piece.

Description

A kind of turbogrid type composite column plate
1. technical field
The invention provides a kind of turbogrid type composite column plate, belong to the separation equipment field.
2. background technology
In petrochemical industry, the industrial departments such as petroleum refining, chemical industry, light industry, environmental protection, medicine and atomic energy, column plate and filler are widely used in distillation, absorption, extraction, absorption, washing, the unit processes in chemical synthesis such as cooling.The advantages such as it is high that filler has separative efficiency, and pressure drop is little, and disposal ability is large, but cost is larger, and operating flexibility is little, requires high to supporting tower internals; Operating flexibility of tray is large, anti-obstruction, and cost is low, and separative efficiency is relatively large, but pressure drop will be larger, and disposal ability is lower.Column plate is by having or not downspout can be divided into overflow-type column plate and throngh flowing type tray, and by contrast, existing throngh flowing type tray is simple in structure, and in tower, space availability ratio is high, and cost is low, and disposal ability is large, but vapour-liquid is short time of contact, and mass-transfer efficiency is low, and operating flexibility is little.The ideal column internals should have advantages of column plate and filler simultaneously, and namely low pressure drop, high efficiency, large operating flexibility, anti-obstruction, low cost, large disposal ability and Ta Nei space availability ratio are high.With column plate and filler compound be one of the effective way of tower internals of realizing ideal.
Compound overflow-type column plate compounded mix and the throngh flowing type tray compounded mix of mainly containing of column plate and filler, simple in structure due to throngh flowing type tray, to be easy to filler compound, is ideal column plate filler complex form.But existing dual-flow tray compounded mix is because the not high elasticity of composite plate and the load-bearing capacity of making of liquid flux of dual-flow tray is restricted.
3. summary of the invention
Purpose of the present invention is exactly a kind of turbogrid type composite column plate for the deficiency that overcomes the prior art existence.
Technical scheme of the present invention:
The objective of the invention is by increase the sieve plate of identical percent opening on dual-flow tray, arrange below dual-flow tray that one deck structured packing realizes, it can take full advantage of space in tower, improve the vapour-liquid mass situation of dual-flow tray, reduce plate pressure drop, reduced entrainment, improved the disposal ability of dual-flow tray, operating flexibility and separative efficiency.It is mainly by dual-flow tray, the formation such as sieve plate and structured packing, it is characterized in that having 20~60% sieve aperture on dual-flow tray, the distance of 3~6mm is provided with the sieve plate of identical percent opening at an upper portion thereof, sieve aperture can be the suitable diamond hole of φ 3~φ 20mm circular hole of opening on the thick plate of 2~10mm or perforated area, the strip bulge that cracks in the side, the wrong row of the circular hole of the circular hole on sieve plate, diamond hole or strip bulge and dual-flow tray, diamond hole or bar hole or half wrong row; Pass through self fixedly high structured packing of one deck 100~250mm of brace summer below dual-flow tray; During installation between composite plate plate and plate the upper support beam by sieve plate fix, fix by connector between plate and bracing ring.
The turbogrid type composite column plate that the present invention proposes, due to put on adopting sieve plate and under add structured packing, take full advantage of space in tower, increase at double air-flow time of contact, strengthened air-flow mixing intensity and contact interface renewal rate, improved plate efficiency, simultaneously due to the existence of sieve plate makes percent opening can be up to 60%, greatly improve disposal ability and the operating flexibility of column plate, reduced plate pressure drop and entrainment; Throngh flowing type tray serves as the liquid distribution trough of structured packing effectively, liquid is laterally mixed reach the desired perfect condition of filler; Conversely, the gas distributor of column plate has been served as again in structured packing, further improves the vapour-liquid mass situation, rationally effectively utilizes the advantage of column plate and filler, has reached both perfect adaptations.
4, description of drawings
Accompanying drawing Fig. 1 is structural representation of the present invention, and Fig. 2 is the column plate connection diagram.
The drawing of accompanying drawing is established bright as follows:
1. dual-flow tray 2. sieve plate 3. structured filling material layer 4. fixed mount 5. bolt 6. connectors
5. the specific embodiment
The present invention will be described in detail below in conjunction with accompanying drawing:
embodiment 1, the present invention is by dual-flow tray 1, sieve plate 2 and structured packing 3 form, column plate is that thickness of slab is to have 20~60% diameter or sieve aperture or the diamond hole of equivalent diameter 3~20mm on the flat board of 2~10mm, sieve plate 2 is the flat board of thickness of slab 2~10mm, have equally corresponding sieve aperture or diamond hole with the identical percent opening of dual-flow tray, the wrong row of sieve aperture on sieve plate and dual-flow tray or diamond hole or the wrong row of part, link together by fixed mount 4 and dual-flow tray 1, structured packing 3 is the thick plate ripple arranged packing of 100mm, be fixed on the below of dual-flow tray by dual-flow tray self brace summer, between column plate and filler the space high be 5~100mm, utilize the upper support beam of sieve plate to be bolted during installation between composite plate plate and plate fixing, fix by connector between plate and bracing ring.
embodiment 2, the present invention is by dual-flow tray 1, sieve plate 2 and structured packing 3 form, dual-flow tray 1 has wide 6~20mm of 20~60% on thickness of slab 2~10mm flat board, the bar hole of long 30~200mm, sieve plate 2 is the flat board of thickness of slab 2~10mm, same punching has 20~60% wide 6~20mm, the strip bulge that cracks in the side of long 30~200mm, strip bulge and the institute's column plate cylindrical void that covers mistake are arranged, half wrong row, sieve plate is connected fixed mount 4 and forms connection with dual-flow tray, structured packing 3 is the thick mellapak packing of 150mm, be fixed under dual-flow tray by column plate self-supporting beam, between filler and column plate hole high be 20~100mm, utilize the upper support beam of sieve plate to be bolted during installation between composite plate plate and plate fixing, fix by connector between plate and bracing ring.
Turbogrid type composite column plate provided by the present invention has the following advantages: (1) takes full advantage of space in tower, and the vapour-liquid contact of every layer of column plate has liquid bubbling mass transfer simultaneously, and liquid drenches and falls mass transfer and liquid film turbulent mass transfer.(2) vapour-liquid contact mixing intensity improves greatly, and the interface is upgraded probability and greatly strengthened, and increase time of contact, and the contact of falling the ship shape when especially vapour-liquid passed column plate has improved the mass transfer separative efficiency of composite plate significantly, compares with the F1 float valve, has improved 50%.(3) the vapour-liquid two-phase is all without back-mixing, and the mass transfer way of contact is simple, is conducive to carry out column plate mass transfer separation simulation.Pass column plate final level ejection and pass upward due to gas phase, bubble is little simultaneously, without poly-also, entrainment is few.(4) the veneer percent opening is high, and compound percent opening adjustable extent is large; Quite under gas speed, plate pressure drop is little, and is suitable with the filler pressure drop of the height equivalent to one theoretical plate (HETP), and energy-saving efficiency is high.(5) operating flexibility is large, and optimum operation elasticity is 4, and maximum operating flexibility is 8, can satisfy various industrial production needs.(6) simple in structure, intensity is high, and cost is low, and installation and decoration is convenient, is particularly suitable for tower and maximizes.

Claims (1)

1. turbogrid type composite column plate, formed by dual-flow tray, sieve plate and structured packing, it is characterized in that having 20~60% sieve aperture on dual-flow tray, the distance of 3~6mm is provided with the sieve plate of identical percent opening at an upper portion thereof, sieve aperture is the suitable diamond hole of φ 3~φ 20mm circular hole of opening on 2~10mm slab or perforated area, the strip bulge that cracks in the side, the wrong row of the circular hole of the circular hole on sieve plate, diamond hole or strip bulge and dual-flow tray, diamond hole or bar hole or half wrong row; Pass through self fixedly high structured packing of one deck 100~250mm of brace summer below dual-flow tray; Utilize the upper support beam of sieve plate to be bolted during installation between composite plate plate and plate fixing, fix by connector between plate and bracing ring.
CN 200810000614 2008-01-11 2008-01-11 Novel turbogrid type composite column plate Active CN101480537B (en)

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Application Number Priority Date Filing Date Title
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Application Number Priority Date Filing Date Title
CN 200810000614 CN101480537B (en) 2008-01-11 2008-01-11 Novel turbogrid type composite column plate

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CN101480537B true CN101480537B (en) 2013-05-15

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Families Citing this family (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101785931A (en) * 2010-03-31 2010-07-28 天津天大天久科技股份有限公司 Flow crossing-baffling composite gasoline fractionating tower of ethylene device
GB201203332D0 (en) * 2012-02-27 2012-04-11 Water Powered Technologies Ltd Static filter screen
CN102935293B (en) * 2012-10-22 2014-01-15 中国石油大学(华东) Ultra-large high-efficiency high-operation-flexibility high-throughput anti-blocking composite flow-through tray
CN102908797B (en) * 2012-10-22 2014-01-15 中国石油大学(华东) Combined column plate with coupling of composite flow-through column plate and fiber bundle fillers
CN104258590B (en) * 2014-09-28 2016-02-17 郑州大学 A kind of percolation tower
CN105482846B (en) * 2016-01-08 2017-05-17 新疆石油工程设计有限公司 SAGD produced liquid flash evaporation and dehydration device, SAGD produced liquid reversed-phase separation device and SAGD produced liquid reversed-phase separation method
CN106730970B (en) * 2017-03-22 2023-11-21 中国石油大学(华东) Vacuum tower internal part of heat-taking coupling through-flow column plate and spraying
CN111013177B (en) * 2019-12-16 2020-10-20 常州大学 Composite tower plate structure and composite tower equipment

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB1383218A (en) * 1971-06-05 1975-02-05 Kansai Kagaku Kikai Seisaku Kk Method and apparatus for contacting and or dispersing fluids and other materials
CN2381371Y (en) * 1999-07-05 2000-06-07 田原宇 Turbogrid large composite float valve tray
CN1298751A (en) * 2000-04-04 2001-06-13 中国石油化工集团公司 Tower plate for gas-liquid mass transfer
CN201171919Y (en) * 2007-11-23 2008-12-31 山东科技大学 Novel percolation type composite column plate

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB1383218A (en) * 1971-06-05 1975-02-05 Kansai Kagaku Kikai Seisaku Kk Method and apparatus for contacting and or dispersing fluids and other materials
CN2381371Y (en) * 1999-07-05 2000-06-07 田原宇 Turbogrid large composite float valve tray
CN1298751A (en) * 2000-04-04 2001-06-13 中国石油化工集团公司 Tower plate for gas-liquid mass transfer
CN201171919Y (en) * 2007-11-23 2008-12-31 山东科技大学 Novel percolation type composite column plate

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