CN102908797B - Combined column plate with coupling of composite flow-through column plate and fiber bundle fillers - Google Patents

Combined column plate with coupling of composite flow-through column plate and fiber bundle fillers Download PDF

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CN102908797B
CN102908797B CN201210404804.9A CN201210404804A CN102908797B CN 102908797 B CN102908797 B CN 102908797B CN 201210404804 A CN201210404804 A CN 201210404804A CN 102908797 B CN102908797 B CN 102908797B
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dual
flow tray
column plate
vertical edge
flow
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CN102908797A (en
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乔英云
田原宇
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China University of Petroleum East China
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China University of Petroleum East China
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Abstract

The invention provides a combined column plate with coupling of a composite flow-through column plate and fiber bundle fillers. According to the combined column plate, flow-through sieve plates, which have the same aperture ratio and arranged in a staggering way, are fixed at the upper part of the flow-through column plate with high aperture ratio; the whole combined column plate is arranged as individual blocks based on the H-shaped vertical side; the H-shaped vertical side serves as a supporting beam of the composite flow-through column plate; a vertical separating plate is added in an upper groove; the whole column plate is divided into a plurality of mixing tanks by the H-shaped vertical side and separating plates; the fiber bundle fillers which are 300 to 2500mm in height are positioned in a lower groove. With the adoption of the combined column plate, the space in the column is fully utilized, the vapor-liquid mass transfer condition of the flow-through column plate is improved, the pressure release of the column plate is reduced, the entrainment is reduced, the processing capacity of the flow-through column plate is improved, the operation flexibly and the separating efficiency are improved, a super-large supporting ring for the column plate is removed, the extreme demand on levelness in installation and the amplifying effect are also removed, the problem due to the large supporting structure of the column plate is solved as well as the problem due to the column plate, and large-scale columns are easy to obtain.

Description

The combined type column plate of compound dual-flow tray and the coupling of fibre bundle filler
Technical field
The present invention relates to separation equipment field, the combined type column plate of espespecially a kind of compound dual-flow tray and the coupling of fibre bundle filler.
Background technology
At industrial departments such as petrochemical industry, 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.Filler has the advantages such as separative efficiency is high, pressure drop is little, disposal ability is large, but cost is larger, and operating flexibility is little, to supporting tower internals, requires high; Large, the anti-obstruction of operating flexibility of tray, cost is low, 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.Desirable tower internals should have low pressure drop, high efficiency, large operating flexibility, anti-obstruction, low cost, large disposal ability and the high characteristic of Ta Nei space availability ratio simultaneously.By column plate and filler compound be one of the effective way of tower internals of realizing ideal.Fibre bundle filler is the high surface linked network formula flexible filler that a kind of liquid phase of exploitation is recently continuous phase, and more than liquid flooding high cycle speed reaches 8m/s, mass-transfer efficiency is high, and pressure drop is only the 1/2-1/3 of common structured packing.
Compound overflow-type column plate compounded mix and the throngh flowing type tray compounded mix of mainly containing of column plate and filler, because throngh flowing type tray is simple in structure, it is compound to be easy to filler, is ideal column plate filler complex form.But existing dual-flow tray compounded mix, because the liquid flooding of structured packing is restricted the elasticity of composite plate and load-bearing capacity.The patent CN101480537 declaring as the inventor has mentioned a kind of novel turbogrid type composite column plate and has adopted the sieve plate that increases identical percent opening on dual-flow tray, the structured packing that one deck 0-250mm is high is set below dual-flow tray, make full use of Ta Nei space, increase air-flow time of contact, air-flow mixing intensity and interface renewal rate have been strengthened, improve plate efficiency, simultaneously due to the existence of sieve plate makes percent opening can be up to 60%, the disposal ability and the operating flexibility that have greatly improved column plate, reduced plate pressure drop and entrainment; Throngh flowing type tray serves as the liquid distribution trough of structured packing effectively, makes liquid laterally mix and reach the desired perfect condition of filler; Conversely, the gas distributor of column plate has been served as again in structured packing, further improves vapour-liquid mass situation, has rationally effectively utilized the advantage of column plate and filler.But because the liquid flooding gas speed of structured packing is lower, maximum void tower kinetic energy factor is less than 3(m/s) .(kg/m3) 1/2, become turbogrid type composite column plate and further carry high-throughout bottleneck.
Summary of the invention
Object of the present invention is exactly that the combined type column plate of a kind of compound dual-flow tray and the coupling of fibre bundle filler is provided in order to overcome the deficiency of turbogrid type composite column plate technology existence.
Technical scheme of the present invention:
The object of the invention is by the dual-flow tray of fixing identical percent opening, wrong row on high opening rate dual-flow tray top; With H shape vertical edge, carry out sectional type installation, H shape vertical edge is as column plate self brace summer, and upper groove installs vertical partition plate additional, and H shape vertical edge and dividing plate are divided into groove under a plurality of mixing pits by whole column plate and arrange that fibre bundle filler that 300~2500mm is high realizes.It can make full use of Ta Nei space, improve the vapour-liquid mass situation of dual-flow tray, reduce plate pressure drop, reduce entrainment, improve disposal ability, operating flexibility and the separative efficiency of dual-flow tray, the harshness of eliminating column plate large bracing ring and installation level requires and enlarge-effect; Solve a column plate large supporting construction difficult problem and column plate strength problem, be easy to realize tower and maximize.
The combined type column plate of a kind of compound dual-flow tray of the present invention and the coupling of fibre bundle filler, comprises dual-flow tray, dual-flow tray, a plurality of H shape vertical edge, a plurality of dividing plate and fibre bundle filler; On described dual-flow tray, the percent opening of sieve aperture is 20~60%, and the distance of 3~8mm is provided with the described dual-flow tray of identical percent opening and hole shape by a plurality of fixed legs at an upper portion thereof; Described sieve aperture is diamond hole, square hole and the polygon hole that φ 15 ~ φ 30mm circular hole or perforated area are suitable; The wrong row of sieve aperture on described dual-flow tray and the sieve aperture of described dual-flow tray or half wrong row; Described compound dual-flow tray carries out sectional type installation with H shape vertical edge, and H shape vertical edge is as column plate self brace summer; Described H shape vertical edge surround with dual-flow tray each on groove install the described dividing plate of a plurality of vertical placements additional, described H shape vertical edge and dividing plate are divided into a plurality of mixing pits by compound dual-flow tray; Each time groove that described H shape vertical edge and dual-flow tray surround hangs the high fibre bundle filler of one deck 300~2500mm by the lower vertical edge of H shape vertical edge; During installation, between the two boards of described compound dual-flow tray, with the upper vertical edge of H shape vertical edge, with bolt, fix, between compound dual-flow tray and bracing ring, by connector, fix.
According to above-mentioned design, described fibre bundle filler is formed with rhombus or square pattern woollen yarn knitting by 15000-30000 root filament on fixed mount, and filament diameter is 0.001-0.01mm.
The combined type column plate of the compound dual-flow tray that the present invention proposes and the coupling of fibre bundle filler, owing to adopting on high opening rate dual-flow tray, put sieve plate, with H shape vertical edge, carry out sectional type installation, upper groove installs vertical partition plate and lower groove suspended fiber bundles filler additional, take full advantage of Ta Nei space, increase at double air-flow time of contact, air-flow mixing intensity and contact interface renewal rate have been strengthened, liquid flooding gas speed and plate efficiency have been improved, reduced plate pressure drop, reduce entrainment, beat the flux that has improved dual-flow tray, disposal ability, operating flexibility and separative efficiency, the harshness of eliminating column plate large bracing ring and installation level requires and enlarge-effect, compound dual-flow tray serves as the liquid distribution trough of fibre bundle filler effectively, makes liquid laterally mix and reach the desired perfect condition of filler, conversely, fibre bundle filler has served as again the gas distributor of column plate, further improves vapour-liquid mass situation, has realized the coupling of dual-flow tray and fibre bundle filler, solves a column plate large supporting construction difficult problem and column plate strength problem.
Accompanying drawing explanation
Fig. 1 is the structural representation of facing of combined column plate of the present invention;
Fig. 2 is the plan structure schematic diagram of combined column plate of the present invention;
Fig. 3 is the fixed rack structure figure of fibre bundle filler square pattern;
Fig. 4 is the fixed rack structure figure of fibre bundle filler diamond pattern.
Description of reference numerals
1. 32 times grooves of groove on dual-flow tray 2. dual-flow tray 3.H shape vertical edge 4. dividing plate 5. fixed leg 6. bolt 7. connector 8. fibre bundle filler 9. filament 10. fixed mounts 31.
The specific embodiment
Below in conjunction with the drawings and specific embodiments, the present invention is described in further details.
Embodiment 1, and as shown in Figure 1 and Figure 2, the present invention is assembled into column plate by the compound dual-flow tray of several strips.Compound dual-flow tray is by dual-flow tray 1, and dual-flow tray 2, H shape vertical edge 3 and dividing plate 4 form, and dual-flow tray 1 is the flat board that 2~10mm is thick, has the diameter of percent opening 20~60% or circular hole or the diamond hole of equivalent diameter 20mm on it; The distance high at dual-flow tray 1 top 3~8mm is fixed with the dual-flow tray 2 of identical percent opening and hole shape by a plurality of fixed legs 5, fixed leg 5 and dual-flow tray 1 and dual-flow tray 2 can be welding and also can be bolt and be connected.Dual-flow tray 2 thicknesss of slab are 2~10mm; The wrong row of sieve aperture on dual-flow tray 2 and dual-flow tray 1 or diamond hole or the wrong row of part.H shape vertical edge 3 is vertically fixed on dual-flow tray 1 and dual-flow tray 2 two ends, H shape vertical edge Shang Xia 3 two ends all above dual-flow tray 1 and dual-flow tray 2, compound dual-flow tray is welded into by H shape vertical edge 3 and middle dual-flow tray 1 and dual-flow tray 2 structure that cross section is H shape, H shape vertical edge 3 is on top and dual-flow tray 2 surrounds Cao31, bottom and dual-flow tray 1 surrounds lower groove 32.Compound dual-flow tray can carry out sectional type installation, and H shape vertical edge 3 is as piecemeal column plate self brace summer.In the upper groove 31 of compound dual-flow tray H shape, vertical partition plate 4 is installed in welding additional, and H shape vertical edge 3 and dividing plate 4 are divided into a plurality of mixing pits by whole column plate; At the lower groove 32 of compound dual-flow tray H shape, pass through the high fibre bundle filler 8 of lower vertical edge suspension one deck 2500mm of H shape, between compound dual-flow tray and fibre bundle filler 8, space height is 100mm, and every bundle fiber filler beam 8 is formed with diamond pattern woollen yarn knitting by 20000 filaments 9 on fixed mount 10.As shown in Figure 3, the grid beam that fixed mount 10 is diamond-mesh, by the metal tube of both sides and intermediate mesh iron wire or iron plate, be welded, the metal tube of both sides and H shape vertical edge 3(outermost are be connected in connector 7 following) weld below or be spirally connected by screw, intermediate mesh iron wire or iron plate intersection are node, and each grid node is provided with for the support of anchoring fiber filler beam 8 or hole.Fixed mount 10 is fixed on the downside of H shape vertical edge 3, and filament 9 diameters are 0.001-0.01mm; During installation, between the two boards of compound dual-flow tray, the upper vertical edge by H shape vertical edge 3 is fixing with bolt 6.
As mentioned above, middle compound dual-flow tray piecemeal is that cross section is the structure (these dual-flow tray 1 two ends are fixed by the bracing ring of whole circle on connector 7 and outer wall) of H shape, and the compound dual-flow tray piecemeal that both sides outermost is connected with outer wall, H shape vertical edge 3 is no longer established in outside, only by inner side H shape vertical edge 3 and fixed leg 5, complete fixing, the structure that the compound dual-flow tray cross section in outside is T shape, dual-flow tray 1 is wherein fixed by the bracing ring of whole circle on connector 7 and outer wall, fastener in the standard tower that connector 7 is existing column plate, just in this case, it is smaller that the outer rim of the dual-flow tray 2 on top is compared dual-flow tray 1, so that assembly and connection part 7.Certainly also can be made as by dual-flow tray 2 and connect bracing ring and connector 7.
Embodiment 2, can be with reference to Fig. 1, Fig. 2, the compound dual-flow tray of the present invention is comprised of dual-flow tray 1, dual-flow tray 2, H shape vertical edge 3 and dividing plate 4, and dual-flow tray 1 is the flat board that 2~10mm is thick, on it, have percent opening and be wide 6~20mm of 20~60%, the bar hole of long 30~200mm; In the high distance of dual-flow tray 1 top 3~8mm, by the dual-flow tray 2 of the fixing identical percent opening of a plurality of fixed legs 5 and hole shape, fixed leg 5 and dual-flow tray 1 and dual-flow tray 2 can be welding and also can be bolt and be connected.Dual-flow tray 2 thicknesss of slab are 2~10mm; The wrong row of bar hole on dual-flow tray 2 and dual-flow tray 1 or the wrong row of part.H shape vertical edge 3 is vertically fixed on dual-flow tray 1 and dual-flow tray 2 two ends, H shape vertical edge Shang Xia 3 two ends all above dual-flow tray 1 and dual-flow tray 2, compound dual-flow tray is welded into by H shape vertical edge 3 and middle dual-flow tray 1 and dual-flow tray 2 structure that cross section is H shape, H shape vertical edge 3 is on top and dual-flow tray 2 surrounds Cao31, bottom and dual-flow tray 1 surrounds lower groove 32.Compound dual-flow tray can carry out sectional type installation, and H shape vertical edge 3 is as compound dual-flow tray self brace summer, and in the upper groove 31 of compound dual-flow tray H shape, vertical partition plate 4 is installed in welding additional, and H shape vertical edge 3 and dividing plate 4 are divided into a plurality of mixing pits by whole column plate; At the lower groove 32 of compound dual-flow tray H shape, pass through the high fibre bundle filler 8 of lower vertical edge suspension one deck 500mm of H shape vertical edge 3, between compound dual-flow tray and fibre bundle filler 8, space height is 50mm, and every filler beam is formed with square pattern woollen yarn knitting by 25000 filaments 9 on fixed mount 10.As shown in Figure 4, the grid beam that fixed mount 10 is square mesh, by the metal tube of both sides and intermediate mesh iron wire or iron plate, be welded, the metal tube of both sides and H shape vertical edge 3(outermost are be connected in connector 7 following) weld below or be spirally connected by screw, intermediate mesh iron wire or iron plate intersection are node, and each grid node is provided with for the support of anchoring fiber filler beam 8 or hole.Fixed mount 10 is fixed on the downside of H shape vertical edge 3, and filament 9 diameters are 0.001-0.01mm; During installation, between the two boards of compound dual-flow tray, the upper vertical edge by H shape vertical edge 3 is fixing with bolt 6, fixing by connector 7 between compound dual-flow tray and bracing ring.
Combined type column plate cold mould measuring through laboratory of compound dual-flow tray proposed by the invention and fibre bundle coupling, void tower kinetic energy factor 0.3-6(m/s) .(kg/m3) 1/2in scope, column plate point efficiency surpasses 98%, and higher than common dual-flow tray, more than 43%, pressure drop is less than 300Pa, suitable with the filler pressure drop of the height equivalent to one theoretical plate (HETP); Maximum void tower kinetic energy factor is up to 7(m/s) .(kg/m3) 1/2above, operating flexibility is 6, and disposal ability improves more than 4 times.
As known by the technical knowledge, the present invention can realize by other the embodiment that does not depart from its Spirit Essence or essential feature.Therefore, above-mentioned disclosed embodiment, with regard to each side, all just illustrates, and is not only.Change within the scope of the present invention all or within being equal to scope of the present invention is all included in the invention.

Claims (2)

1. a combined type column plate for compound dual-flow tray and the coupling of fibre bundle filler, is characterized in that, comprises dual-flow tray, dual-flow tray, a plurality of H shape vertical edge, a plurality of dividing plate and fibre bundle filler; On described dual-flow tray, the percent opening of sieve aperture is 20~60%, and the distance of 3~8mm is provided with the described dual-flow tray of identical percent opening and hole shape by a plurality of fixed legs at an upper portion thereof; Described sieve aperture is φ 15~φ 30mm circular hole or the suitable polygon hole of perforated area; The wrong row of sieve aperture on described dual-flow tray and the sieve aperture of described dual-flow tray or half wrong row; Described compound dual-flow tray carries out sectional type installation with H shape vertical edge, and H shape vertical edge is as column plate self brace summer; The upper and lower two ends of described H shape vertical edge are all above described dual-flow tray and dual-flow tray, and described H shape vertical edge top and dual-flow tray surround groove, and described H shape vertical edge bottom and dual-flow tray surround lower groove; Described H shape vertical edge surround with dual-flow tray each on groove install the described dividing plate of a plurality of vertical placements additional, described H shape vertical edge and dividing plate are divided into a plurality of mixing pits by compound dual-flow tray; Each time groove that described H shape vertical edge and dual-flow tray surround hangs the high fibre bundle filler of one deck 300~2500mm by the lower vertical edge of H shape vertical edge; During installation, between the two boards of described compound dual-flow tray, with the upper vertical edge of H shape vertical edge, with bolt, fix, between compound dual-flow tray and bracing ring, by connector, fix.
2. the combined type column plate that compound dual-flow tray according to claim 1 and fibre bundle filler are coupled, it is characterized in that, described fibre bundle filler is formed with rhombus or square pattern woollen yarn knitting by 15000-30000 root filament on fixed mount, and filament diameter is 0.001-0.01mm.
CN201210404804.9A 2012-10-22 2012-10-22 Combined column plate with coupling of composite flow-through column plate and fiber bundle fillers Active CN102908797B (en)

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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
CN113559817B (en) * 2020-06-16 2022-10-14 上海化工研究院有限公司 Corrugated wire mesh sheet for forming structured packing, structured packing and rectifying tower
CN111659149B (en) * 2020-06-16 2021-10-08 上海化工研究院有限公司 Rectifying tower, rectifying system and application thereof

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JPS5146747B1 (en) * 1971-06-05 1976-12-10
JPS53118274A (en) * 1977-03-25 1978-10-16 Kansai Kagaku Kikai Seisaku Kk Layer type gassliquid contact tray
CN2657758Y (en) * 2003-10-20 2004-11-24 北京欣博通创新能源技术开发有限公司 High-efficient contact fiber type filler tower
KR100682452B1 (en) * 2005-08-03 2007-02-15 (주)에이엠티퍼시픽 The flag misfortune contacting device for the dosage augmentation of Ul flow right Tray
CN101480537B (en) * 2008-01-11 2013-05-15 山东科技大学 Novel turbogrid type composite column plate

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