MY8600317A - Column and use thereof - Google Patents
Column and use thereofInfo
- Publication number
- MY8600317A MY8600317A MY317/86A MY8600317A MY8600317A MY 8600317 A MY8600317 A MY 8600317A MY 317/86 A MY317/86 A MY 317/86A MY 8600317 A MY8600317 A MY 8600317A MY 8600317 A MY8600317 A MY 8600317A
- Authority
- MY
- Malaysia
- Prior art keywords
- column
- pressure
- openings
- liquid column
- bubble
- Prior art date
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
- B01D3/14—Fractional distillation or use of a fractionation or rectification column
- B01D3/16—Fractionating columns in which vapour bubbles through liquid
- B01D3/18—Fractionating columns in which vapour bubbles through liquid with horizontal bubble plates
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J10/00—Chemical processes in general for reacting liquid with gaseous media other than in the presence of solid particles, or apparatus specially adapted therefor
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Chemistry (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Saccharide Compounds (AREA)
- Polyoxymethylene Polymers And Polymers With Carbon-To-Carbon Bonds (AREA)
- Steering Control In Accordance With Driving Conditions (AREA)
- Pharmaceuticals Containing Other Organic And Inorganic Compounds (AREA)
- Physical Or Chemical Processes And Apparatus (AREA)
Abstract
A low vapour load reaction column comprises one or more bubble plates 1 with immersion caps 2 of which the side edges comprise openings or perforations 3 for the passage of the gas phase, one or more immersed inlets 5, one or more outlets 7 and, optionally, inflow and outflow weirs 6, 8, characterised in that it has an internal diameter of from 500 to 3000 mm and one or more orifices (4) below each bubble cap (2) of which the openings in the plate (1) are designed in such away that the dry pressure loss occurring under the particular conditions under which the column is operated are 15 times to 60 times greater than the pressure difference between the pressure of the liquid column at the outlet and the pressure of the liquid column at the inlet. This column is particularly suitable for the continuous catalytic esterification of aliphatic carboxylic acids of 2 to 24 carbon atoms with alcohols in countercurrent, and for transesterifications. <IMAGE>
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE19813146142 DE3146142A1 (en) | 1981-11-21 | 1981-11-21 | REACTION COLUMN AND ITS USE |
Publications (1)
Publication Number | Publication Date |
---|---|
MY8600317A true MY8600317A (en) | 1986-12-31 |
Family
ID=6146862
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
MY317/86A MY8600317A (en) | 1981-11-21 | 1986-12-30 | Column and use thereof |
Country Status (7)
Country | Link |
---|---|
EP (1) | EP0082301B1 (en) |
JP (1) | JPS5895549A (en) |
AT (1) | ATE14678T1 (en) |
DE (2) | DE3146142A1 (en) |
GB (1) | GB2109265B (en) |
MY (1) | MY8600317A (en) |
PH (1) | PH18812A (en) |
Families Citing this family (15)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE3809417A1 (en) * | 1988-03-21 | 1989-10-12 | Henkel Kgaa | METHOD FOR CONTINUOUSLY Esterifying Fatty Acids |
DE69027304T2 (en) * | 1989-01-17 | 1997-01-23 | Davy Process Technology Ltd., London | Continuous process for the production of carboxylic acid esters |
GB2299521B (en) * | 1995-03-02 | 1998-09-09 | Norton Chem Process Prod | High capacity trays |
US5844111A (en) * | 1995-06-07 | 1998-12-01 | The Procter & Gamble Company | Method for purifying an inert gas while preparing lower alkyl esters |
US5648483A (en) * | 1995-06-07 | 1997-07-15 | The Procter & Gamble Company | Continuous transesterification method for preparing polyol polyesters |
DE19623508C2 (en) * | 1996-06-13 | 1998-08-20 | Henkel Kgaa | Process for the preparation of dialkyl carbonates |
US5945529A (en) * | 1996-07-19 | 1999-08-31 | The Procter & Gamble Company | Synthesis of polyol fatty acid polyesters using column with inert gas stripping |
DE10257525A1 (en) | 2002-12-10 | 2004-07-01 | Cognis Deutschland Gmbh & Co. Kg | Process for the production of linear or branched fatty acid esters by heterogeneously catalyzed reactive rectification with a pre-reactor |
EP1953132B1 (en) * | 2005-11-25 | 2015-08-26 | Asahi Kasei Chemicals Corporation | Process for industrial production of dialkyl carbonates and diols |
EA200801493A1 (en) * | 2005-11-30 | 2009-02-27 | Асахи Касеи Кемикалз Корпорейшн | INDUSTRIAL METHOD FOR OBTAINING HIGH QUALITY AROMATIC POLYCARBONATE |
EA200801325A1 (en) * | 2005-12-12 | 2009-02-27 | Асахи Касеи Кемикалз Корпорейшн | METHOD OF INDUSTRIAL PRODUCTION OF HIGH-QUALITY AROMATIC POLYCARBONATE |
TWI314549B (en) | 2005-12-26 | 2009-09-11 | Asahi Kasei Chemicals Corp | Industrial process for separating out dialkyl carbonate |
TW200738601A (en) * | 2005-12-27 | 2007-10-16 | Asahi Kasei Chemicals Corp | Industrial process for production of dialkyl carbonate and diol |
KR101554607B1 (en) * | 2008-11-07 | 2015-09-22 | 에스케이케미칼주식회사 | Method and apparatus for preparing fatty acid alkyl ester using fatty acid |
JP7493042B2 (en) * | 2020-01-31 | 2024-05-30 | エスケー エコ プライム カンパニー リミテッド | Method for producing bio-oil from high acid value oils and fats |
Family Cites Families (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2778621A (en) * | 1953-12-08 | 1957-01-22 | Standard Oil Co | Entrainment-obviating bubble cap |
FR1327227A (en) * | 1962-04-05 | 1963-05-17 | Air Liquide | Tray guarded for contacting liquids and gases |
JPS4631321B1 (en) * | 1968-10-08 | 1971-09-11 | ||
US3712595A (en) * | 1971-07-12 | 1973-01-23 | A Hirsch | Upflow distributive trays for fractionating columns and absorption towers |
CA1063777A (en) * | 1974-04-24 | 1979-10-09 | Allen W. Hancock (Ii) | Distillation column reactor and process |
DE2503195C3 (en) * | 1975-01-27 | 1984-10-18 | Henkel KGaA, 4000 Düsseldorf | Process and device for the continuous catalytic esterification of fatty acids with alcohols |
-
1981
- 1981-11-21 DE DE19813146142 patent/DE3146142A1/en not_active Withdrawn
-
1982
- 1982-11-13 AT AT82110505T patent/ATE14678T1/en active
- 1982-11-13 DE DE8282110505T patent/DE3265279D1/en not_active Expired
- 1982-11-13 EP EP82110505A patent/EP0082301B1/en not_active Expired
- 1982-11-19 GB GB08233066A patent/GB2109265B/en not_active Expired
- 1982-11-19 PH PH28165A patent/PH18812A/en unknown
- 1982-11-20 JP JP57204440A patent/JPS5895549A/en active Pending
-
1986
- 1986-12-30 MY MY317/86A patent/MY8600317A/en unknown
Also Published As
Publication number | Publication date |
---|---|
EP0082301A1 (en) | 1983-06-29 |
PH18812A (en) | 1985-09-27 |
DE3146142A1 (en) | 1983-06-01 |
DE3265279D1 (en) | 1985-09-12 |
EP0082301B1 (en) | 1985-08-07 |
JPS5895549A (en) | 1983-06-07 |
ATE14678T1 (en) | 1985-08-15 |
GB2109265A (en) | 1983-06-02 |
GB2109265B (en) | 1985-09-04 |
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