JPS57113804A - Tray type gas-liquid contact device - Google Patents
Tray type gas-liquid contact deviceInfo
- Publication number
- JPS57113804A JPS57113804A JP55188075A JP18807580A JPS57113804A JP S57113804 A JPS57113804 A JP S57113804A JP 55188075 A JP55188075 A JP 55188075A JP 18807580 A JP18807580 A JP 18807580A JP S57113804 A JPS57113804 A JP S57113804A
- Authority
- JP
- Japan
- Prior art keywords
- gas
- liquid contact
- liquid
- froth
- foams
- 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.)
- Pending
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D3/00—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
- B01D3/009—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping in combination with chemical reactions
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Gas Separation By Absorption (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
- Physical Or Chemical Processes And Apparatus (AREA)
Abstract
PURPOSE:To improve tray efficiency and to increase treatment capacity by dis posing mesh-like structural members in the froth layers of the gas-liquid mixed phases on each tray in order to fine the foam in the froth layers while maintaining the superficial velocity in a gas-liquid contact column relatively high. CONSTITUTION:A gas-liquid contact column body 1 is divided to a plurality of contact reaction chambers by means of gas-liquid contact trays 2, and these are connected vertically by means of downcomers 3. Vapor ascends by passing through the opening parts 4 of the trays 2, and enters the liquid phase retained between inlet and outlet weirs 5, 6, where it undergoes gas-liquid contact. On the other hand, liquid passes through the clearance at the bottom of the downcomer 3, overflows from the weir 5, flows onto the tray 2, and overflows from the weir 6 while contacting the steam. In this case, the gas-liquid contact state is in the form of froth of gas-liquid mixed phases, and forms a froth layer A between the weirs 5, 6. The small foams (b) produced in the opening parts 4 grow to large foams B as they ascend, and the leyer A arrives at the top surface. However, there are the mesh-like structural members 7 approximately parallel with the trays 2 in the layer A and therefore the foams B are again divided into small foams (c), whereby the gas-liquid contact areas are increased.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP55188075A JPS57113804A (en) | 1980-12-29 | 1980-12-29 | Tray type gas-liquid contact device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP55188075A JPS57113804A (en) | 1980-12-29 | 1980-12-29 | Tray type gas-liquid contact device |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS57113804A true JPS57113804A (en) | 1982-07-15 |
Family
ID=16217260
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP55188075A Pending JPS57113804A (en) | 1980-12-29 | 1980-12-29 | Tray type gas-liquid contact device |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS57113804A (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS6058234U (en) * | 1983-09-26 | 1985-04-23 | 株式会社日立製作所 | Gas-liquid contact device |
JPH0456490U (en) * | 1990-09-25 | 1992-05-14 | ||
WO1999050235A1 (en) * | 1998-04-01 | 1999-10-07 | Siirtec-Nigi S.P.A. | Apparatus and process for the preparation of urea from carbon dioxide and ammonia |
JP2010005604A (en) * | 2007-08-16 | 2010-01-14 | Jgc Corp | Contact column |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS53113267A (en) * | 1977-03-15 | 1978-10-03 | Chiyoda Chem Eng & Constr Co Ltd | Gas-liquid contacting apparatus |
-
1980
- 1980-12-29 JP JP55188075A patent/JPS57113804A/en active Pending
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS53113267A (en) * | 1977-03-15 | 1978-10-03 | Chiyoda Chem Eng & Constr Co Ltd | Gas-liquid contacting apparatus |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS6058234U (en) * | 1983-09-26 | 1985-04-23 | 株式会社日立製作所 | Gas-liquid contact device |
JPS6337081Y2 (en) * | 1983-09-26 | 1988-09-30 | ||
JPH0456490U (en) * | 1990-09-25 | 1992-05-14 | ||
WO1999050235A1 (en) * | 1998-04-01 | 1999-10-07 | Siirtec-Nigi S.P.A. | Apparatus and process for the preparation of urea from carbon dioxide and ammonia |
JP2010005604A (en) * | 2007-08-16 | 2010-01-14 | Jgc Corp | Contact column |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US3217469A (en) | Feed device for gas-and-liquid contact tower | |
US2973189A (en) | Fractionating columns | |
US2787453A (en) | Fractionating tower utilizing directional upflow means in conjunction with slanted trays | |
US2767966A (en) | Perforated bubble tray | |
KR940003585A (en) | Down-commercial tray device for chemical process tower and mixing method of liquid and vapor from it | |
ATE112694T1 (en) | DEVICE FOR FLOW SEPARATION OF OIL FROM WATER WITH MEANDER FLOW. | |
CA2284584A1 (en) | De-entrainment tray and method of operation | |
WO1980000418A1 (en) | Apparatus for bringing vapor into contact with liquid | |
GB2307424A (en) | Vapor-liquid contact apparatus | |
US4118285A (en) | Separation of liquid mixtures | |
US5047179A (en) | Distillation tray | |
US2639973A (en) | Method of and apparatus for improving gas distribution in bubble-cap tower operating on fluidized solids | |
US3151042A (en) | Bubble-plate chamber stepped still and the process for using such a still for alcohol or petroleum purification | |
US5049319A (en) | Distillation tray | |
KR970006990B1 (en) | Active liquid distributor containing packed column | |
US3632315A (en) | Liquid-liquid contacting tray system | |
CA1129332A (en) | Multi-stage hydrogen water isotopic exchange column | |
JPS57113804A (en) | Tray type gas-liquid contact device | |
US2757915A (en) | Gas-liquid contact apparatus | |
US2965548A (en) | Fractionation method and apparatus for conducting same | |
US3979281A (en) | Continuous liquid extraction process with periodic flow of the denser stream | |
GB687987A (en) | Improvements in or relating to a gas-liquid contacting apparatus | |
EP0234876A3 (en) | Process and apparatus to establish contact between liquid and vapour or gas, particularly in distillation and or absoorption columns | |
US2507325A (en) | Bubble tower construction and method of fractionating vapors | |
US3199962A (en) | Method of countercurrent contacting of immiscible fluids |