CN204709846U - Vertical sieve tray tower tray in a kind of methanol stripper tower - Google Patents

Vertical sieve tray tower tray in a kind of methanol stripper tower Download PDF

Info

Publication number
CN204709846U
CN204709846U CN201520284268.2U CN201520284268U CN204709846U CN 204709846 U CN204709846 U CN 204709846U CN 201520284268 U CN201520284268 U CN 201520284268U CN 204709846 U CN204709846 U CN 204709846U
Authority
CN
China
Prior art keywords
column plate
downspout
tower
tray
methanol stripper
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
CN201520284268.2U
Other languages
Chinese (zh)
Inventor
费昱恺
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.)
Tianjin You Hua Science And Technology Ltd
Original Assignee
Tianjin You Hua Science And Technology Ltd
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 Tianjin You Hua Science And Technology Ltd filed Critical Tianjin You Hua Science And Technology Ltd
Priority to CN201520284268.2U priority Critical patent/CN204709846U/en
Application granted granted Critical
Publication of CN204709846U publication Critical patent/CN204709846U/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Landscapes

  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)

Abstract

Vertical sieve tray tower tray in a kind of methanol stripper tower, comprising: column plate, liquid barrier, sieve aperture, downspout; The upper surface of column plate arranges liquid barrier, and sieve aperture is evenly distributed on column plate; Downspout has two kinds of distribution modes on column plate: a kind of center being downspout and being positioned at column plate, and another kind is that downspout is circumferentially arranged near column plate edge; On column plate, two kinds of downspout are distributed in methanol stripper tower and are alternately arranged.In this methanol stripper tower, vertical sieve tray tower tray increases the radial distance of adjacent two layers column plate downspout by two kinds of distributions of downspout, namely adds liquid radial cross-flow time in tower, improves gas-liquid mass transfer efficiency, have higher stability.

Description

Vertical sieve tray tower tray in a kind of methanol stripper tower
Technical field
The utility model relates to technical field of chemical, particularly vertical sieve tray tower tray in a kind of methanol stripper tower.
Background technology
The processing method of methanol process waste water common both at home and abroad at present has: physical treatment process, method of chemical treatment, biological treatment etc.Because methyl alcohol is the strong polar substances of Small molecular, be easy to miscible with water, therefore the physical method such as ion-exchange and charcoal absorption all can not well be removed.Press through the steam stripped method process of vapours during prior art often adopts containing alcohol waste water, so the application of sieve tray is just very extensive.Existing sieve tray, absorbing fluid from overhead stream through each sieve tray time, cannot ensure that absorbing fluid can flow through the various piece of sieve tray fully completely, thus cannot ensure that gas-liquid fully exchanges, productivity ratio is declined.
Utility model content
The purpose of this utility model is, provide a kind of flexible for installation for the deficiencies in the prior art, structure is simple, improves mass-transfer efficiency, vertical sieve tray tower tray in the methanol stripper tower with higher stability.
To achieve these goals, the technical scheme that the utility model adopts is as follows: vertical sieve tray tower tray in a kind of methanol stripper tower, comprising: column plate, liquid barrier, sieve aperture, downspout; The upper surface of column plate arranges liquid barrier, and sieve aperture is evenly distributed on column plate; Downspout has two kinds of distribution modes on column plate: a kind of center being downspout and being positioned at column plate, and another kind is that downspout is circumferentially arranged near column plate edge; On column plate, two kinds of downspout are distributed in methanol stripper tower and are alternately arranged.
Described sieve aperture spacing is equidistantly, and sieve aperture adopts tubaeform.
Described column plate thickness is 2mm.
The beneficial effects of the utility model are, in this methanol stripper tower, vertical sieve tray tower tray increases the radial distance of adjacent two layers column plate downspout by two kinds of distributions of downspout, namely add liquid radial cross-flow time in tower, improve gas-liquid mass transfer efficiency, there is higher stability.
Accompanying drawing explanation
Fig. 1 is vertical sieve tray tower tray scheme of installation in methanol stripper tower.
Fig. 2 is a kind of structural representation of vertical sieve tray tower tray in methanol stripper tower.
Fig. 3 is the another kind of structural representation of vertical sieve tray tower tray in methanol stripper tower.
Above-mentioned number in the figure is described as follows:
1---tower body; 2---column plate; 3---liquid barrier; 4---sieve aperture; 5---downspout; 6---support.
Detailed description of the invention
The technical solution of the utility model is described further by specific embodiment below in conjunction with accompanying drawing.
Vertical sieve tray tower tray in a kind of methanol stripper tower, comprising: column plate 2, liquid barrier 3, sieve aperture 4, downspout 5; The upper surface of column plate 2 arranges liquid barrier 3, and sieve aperture 4 is evenly distributed on column plate 2; Downspout 5 has two kinds of distribution modes on column plate 2: a kind of center being downspout 5 and being positioned at column plate 2, and another kind is that downspout 5 is circumferentially arranged near column plate 2 edge; On column plate 2, two kinds of downspout 5 are distributed in methanol stripper tower and are alternately arranged.Support 6 is welded on the side of tower body 1, and column plate 2 is positioned on support 6.
Carrying out practically process is as follows: gas is arrive above column plate 2 by tubaeform sieve aperture 4 below the column plate 2 of 2mm from thickness, time gas passes through column plate 2, fully carries out gas-liquid exchange with the absorbing fluid being positioned at column plate 2 upper surface.When column plate 2 upper surface absorbing fluid liquid level higher than downspout 5 height time, absorbing fluid is flow on the column plate 2 of lower one deck by downspout 5.Column plate 2 is also provided with liquid barrier 3, the runner that absorbing fluid can be formed by liquid barrier 3 flows through the various piece of column plate 2 simultaneously.Because the downspout 5 between each layer is not on same longitudinal direction, so absorbing fluid fully can both flow through tower tray at every layer, make production efficiency higher.

Claims (3)

1. a vertical sieve tray tower tray in methanol stripper tower, is characterized in that, comprising: column plate (2), liquid barrier (3), sieve aperture (4), downspout (5); The upper surface of column plate (2) arranges liquid barrier (3), and sieve aperture (4) is evenly distributed on column plate (2); Downspout (5) has two kinds of distribution modes on column plate (2): one is the center that downspout (5) is positioned at column plate (2), and another kind is that downspout (5) is circumferentially arranged near column plate (2) edge; Two kinds of the upper downspout (5) of column plate (2) are distributed in methanol stripper tower and are alternately arranged.
2. vertical sieve tray tower tray in methanol stripper tower according to claim 1, is characterized in that, described sieve aperture (4) spacing is equidistantly, and sieve aperture (4) adopts tubaeform.
3. vertical sieve tray tower tray in methanol stripper tower according to claim 1, is characterized in that, described column plate (2) thickness is 2mm.
CN201520284268.2U 2015-05-05 2015-05-05 Vertical sieve tray tower tray in a kind of methanol stripper tower Expired - Fee Related CN204709846U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201520284268.2U CN204709846U (en) 2015-05-05 2015-05-05 Vertical sieve tray tower tray in a kind of methanol stripper tower

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201520284268.2U CN204709846U (en) 2015-05-05 2015-05-05 Vertical sieve tray tower tray in a kind of methanol stripper tower

Publications (1)

Publication Number Publication Date
CN204709846U true CN204709846U (en) 2015-10-21

Family

ID=54308879

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201520284268.2U Expired - Fee Related CN204709846U (en) 2015-05-05 2015-05-05 Vertical sieve tray tower tray in a kind of methanol stripper tower

Country Status (1)

Country Link
CN (1) CN204709846U (en)

Similar Documents

Publication Publication Date Title
CN101817586A (en) Spiral-flow water-distribution hydrocyclone internal-circulation anaerobic reactor
CN203346151U (en) Double-layer aeration curtain membrane module
CN204709846U (en) Vertical sieve tray tower tray in a kind of methanol stripper tower
CN202506160U (en) Slurry stripping tower with overflow weirs
CN201362615Y (en) Cyclone water distributor for anaerobic reactor
CN201362614Y (en) Internal circulation anaerobic reactor for cyclone water distribution cyclone separation
CN202961927U (en) Continuous type modularized distiller
CN203803141U (en) Liquid collection and redistribution device applied to crylic acid refining process
CN205020090U (en) High -efficient angle -steel tower board
CN203648126U (en) Novel rectifying tower
CN202289517U (en) Distillation tower distributor
CN205019758U (en) Tray structure of float valve tower and float valve tower with same
CN103657348A (en) Plate-type absorption tower
CN2676997Y (en) Inclined hole tower tray used for ammonia evaporation tower
CN208865235U (en) A kind of smooth plate various dimensions extraction stuffing piece and filler
CN104117267A (en) Ammonia gas film-falling absorption device
CN205040453U (en) Ecological pond push away water oxygenation device
CN104258590B (en) A kind of percolation tower
CN216093088U (en) Electrodialysis membrane piece jumbo size baffle structure
CN203577349U (en) Water distribution system for falling film evaporator
CN214105848U (en) Bubbling anti-blocking distributor for tower
CN211226469U (en) Ion exchange equipment for sewage treatment
CN203458824U (en) Novel chemical distillation liquid distributor
CN204644245U (en) A kind of reactive system for unsaturated polyester resin
CN2477247Y (en) Sieve-plate tower for pulse extraction

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

Granted publication date: 20151021

Termination date: 20170505