ZA99447B - Predominantly liquid filled vapor-liquid chemical reactor. - Google Patents
Predominantly liquid filled vapor-liquid chemical reactor.Info
- Publication number
- ZA99447B ZA99447B ZA9900447A ZA99447A ZA99447B ZA 99447 B ZA99447 B ZA 99447B ZA 9900447 A ZA9900447 A ZA 9900447A ZA 99447 A ZA99447 A ZA 99447A ZA 99447 B ZA99447 B ZA 99447B
- Authority
- ZA
- South Africa
- Prior art keywords
- liquid
- chemical reactor
- predominantly
- filled vapor
- vapor
- Prior art date
Links
Classifications
-
- 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
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/0053—Details of the reactor
- B01J19/006—Baffles
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/14—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by absorption
- B01D53/18—Absorbing units; Liquid distributors therefor
-
- 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
- B01J10/002—Chemical processes in general for reacting liquid with gaseous media other than in the presence of solid particles, or apparatus specially adapted therefor carried out in foam, aerosol or bubbles
-
- 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
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/00761—Details of the reactor
- B01J2219/00763—Baffles
- B01J2219/00765—Baffles attached to the reactor wall
- B01J2219/00777—Baffles attached to the reactor wall horizontal
-
- 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
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/18—Details relating to the spatial orientation of the reactor
- B01J2219/185—Details relating to the spatial orientation of the reactor vertical
-
- 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
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/19—Details relating to the geometry of the reactor
- B01J2219/194—Details relating to the geometry of the reactor round
- B01J2219/1941—Details relating to the geometry of the reactor round circular or disk-shaped
- B01J2219/1943—Details relating to the geometry of the reactor round circular or disk-shaped cylindrical
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Analytical Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Dispersion Chemistry (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Physical Or Chemical Processes And Apparatus (AREA)
- Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US09/019,890 US6029956A (en) | 1998-02-06 | 1998-02-06 | Predominantly liquid filled vapor-liquid chemical reactor |
Publications (1)
Publication Number | Publication Date |
---|---|
ZA99447B true ZA99447B (en) | 1999-07-21 |
Family
ID=21795593
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
ZA9900447A ZA99447B (en) | 1998-02-06 | 1999-01-21 | Predominantly liquid filled vapor-liquid chemical reactor. |
Country Status (9)
Country | Link |
---|---|
US (1) | US6029956A (xx) |
EP (1) | EP1051241B1 (xx) |
AU (1) | AU2585299A (xx) |
CA (1) | CA2320361C (xx) |
DE (1) | DE69924969D1 (xx) |
ES (1) | ES2245089T3 (xx) |
TW (1) | TW427927B (xx) |
WO (1) | WO1999039815A1 (xx) |
ZA (1) | ZA99447B (xx) |
Families Citing this family (17)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6906164B2 (en) | 2000-12-07 | 2005-06-14 | Eastman Chemical Company | Polyester process using a pipe reactor |
DE102005050283A1 (de) * | 2005-10-20 | 2007-04-26 | Basf Ag | Verteilervorrichtung für ein Gas-Flüssigphasengemisch für Apparate |
DE102005050284A1 (de) * | 2005-10-20 | 2007-05-10 | Basf Ag | Verteilervorrichtung für ein Gas-Flüssigphasengemisch für Apparate |
US7943094B2 (en) | 2006-12-07 | 2011-05-17 | Grupo Petrotemex, S.A. De C.V. | Polyester production system employing horizontally elongated esterification vessel |
US7649109B2 (en) | 2006-12-07 | 2010-01-19 | Eastman Chemical Company | Polyester production system employing recirculation of hot alcohol to esterification zone |
US7863477B2 (en) | 2007-03-08 | 2011-01-04 | Eastman Chemical Company | Polyester production system employing hot paste to esterification zone |
US7892498B2 (en) | 2007-03-08 | 2011-02-22 | Eastman Chemical Company | Polyester production system employing an unagitated esterification reactor |
DE102007021598B4 (de) | 2007-05-08 | 2022-10-20 | Bayerische Motoren Werke Aktiengesellschaft | Vorrichtung zum Verteilen von fließfähigen Zusatzstoffen in Abgasanlagen |
US7868129B2 (en) | 2007-07-12 | 2011-01-11 | Eastman Chemical Company | Sloped tubular reactor with spaced sequential trays |
US8070142B2 (en) * | 2008-01-24 | 2011-12-06 | Amt International, Inc. | Downcomer distributor |
FR2998190B1 (fr) * | 2012-11-20 | 2015-10-16 | Ifp Energies Now | Colonne d'extraction liquide liquide comportant deux types de plateaux distincts |
TWM463608U (zh) * | 2013-03-08 | 2013-10-21 | Biyoung Biotechnology Co Ltd | 用於溶氧水設備之擾流結構 |
ITMI20131514A1 (it) * | 2013-09-12 | 2015-03-13 | Innovation In Sciences & Technologi Es S R L | Method and system for fluid stream chemical compounds collection, deposition and separation |
US9968895B1 (en) * | 2015-09-22 | 2018-05-15 | James Dartez | Submersible aerator |
CN105727868B (zh) * | 2016-04-01 | 2017-12-15 | 无锡市翱宇特新科技发展有限公司 | 一种生物质反应釜 |
FR3093652B1 (fr) * | 2019-03-13 | 2022-09-16 | Lab Sa | Installation d’épuration par voie humide de fumées d’échappement d’un moteur d’un navire marin |
FR3105018B1 (fr) * | 2019-12-18 | 2021-12-10 | Ifp Energies Now | Reacteur gaz/liquide d’oligomerisation comprenant des internes transversaux |
Family Cites Families (26)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US1776032A (en) * | 1928-01-05 | 1930-09-16 | Julius E Kobernik | Duplex bubble cap |
US2698746A (en) * | 1950-10-11 | 1955-01-04 | David G Reynolds | Vapor-liquid contact apparatus |
US2787453A (en) * | 1953-11-30 | 1957-04-02 | Exxon Research Engineering Co | Fractionating tower utilizing directional upflow means in conjunction with slanted trays |
US3143482A (en) * | 1961-01-09 | 1964-08-04 | Phillips Petroleum Co | Separation apparatus |
BE674013A (xx) * | 1965-01-22 | |||
US3920750A (en) * | 1974-03-21 | 1975-11-18 | Int Paper Canada | Process for producing vanillin |
CA1137434A (en) * | 1978-07-11 | 1982-12-14 | Mohammed Akbar | Process for the continuous thermal cracking of hydrocarbon oils |
US4547326A (en) * | 1981-02-27 | 1985-10-15 | Union Carbide Corporation | Gas liquid contacting tray |
US4668494A (en) * | 1984-12-24 | 1987-05-26 | Foster Wheeler Energy Corporation | Method of using solar energy in a chemical synthesis process |
GB8526978D0 (en) * | 1985-11-01 | 1985-12-04 | Foster Wheeler Energy Ltd | Chemical process fired heaters &c |
US4816191A (en) * | 1988-01-19 | 1989-03-28 | Koch Engineering Company, Inc. | Distributor for liquid-gas contact column and method of preparation and use |
US4915061A (en) * | 1988-06-06 | 1990-04-10 | Foster Wheeler Energy Corporation | Fluidized bed reactor utilizing channel separators |
US5024684A (en) * | 1989-05-12 | 1991-06-18 | Pyropower Corporation | Multi-stage vortex reactor |
US5601788A (en) * | 1991-09-25 | 1997-02-11 | Foster Wheeler Energia Oy | Combined cycle power plant with circulating fluidized bed reactor |
GB9124241D0 (en) * | 1991-11-14 | 1992-01-08 | Boc Group Plc | Liquid-vapour contact columns |
US5218932A (en) * | 1992-03-02 | 1993-06-15 | Foster Wheeler Energy Corporation | Fluidized bed reactor utilizing a baffle system and method of operating same |
FI91220C (fi) * | 1992-05-21 | 1994-06-10 | Ahlstroem Oy | Menetelmä ja laite kaasulukon toteuttamiseksi palautusputkessa ja/tai kiertomateriaalin virtauksen säätämiseksi kiertoleijureaktorissa |
US5349813A (en) * | 1992-11-09 | 1994-09-27 | Foster Wheeler Energy Corporation | Vibration of systems comprised of hot and cold components |
US5500195A (en) * | 1992-11-13 | 1996-03-19 | Foster Wheeler Energy Corporation | Method for reducing gaseous emission of halogen compounds in a fluidized bed reactor |
US5325823A (en) * | 1992-12-24 | 1994-07-05 | Foster Wheeler Energy Corporation | Large scale fluidized bed reactor |
US5491967A (en) * | 1994-02-23 | 1996-02-20 | Foster Wheeler Energia Oy | Pressurized fluidized bed reactor and a method of operating the same |
CA2141886E (en) * | 1994-05-11 | 1999-10-12 | Federico Zardi | Reactor for two-phase reactions, in particular for urea synthesis at high pressure and temperature |
US5526775A (en) * | 1994-10-12 | 1996-06-18 | Foster Wheeler Energia Oy | Circulating fluidized bed reactor and method of operating the same |
US5582515A (en) * | 1995-05-04 | 1996-12-10 | Foster Wheeler Energy Corporation | Acoustically pulsating burner with integral adjustable Sondhauss thermoacoustic elements |
US5567228A (en) * | 1995-07-03 | 1996-10-22 | Foster Wheeler Energy Corporation | System for cooling and cleaning synthesized gas using ahot gravel bed |
US6025403A (en) * | 1997-07-07 | 2000-02-15 | Mobil Oil Corporation | Process for heat integration of an autothermal reformer and cogeneration power plant |
-
1998
- 1998-02-06 US US09/019,890 patent/US6029956A/en not_active Expired - Lifetime
-
1999
- 1999-01-21 TW TW088100352A patent/TW427927B/zh active
- 1999-01-21 ZA ZA9900447A patent/ZA99447B/xx unknown
- 1999-02-05 CA CA002320361A patent/CA2320361C/en not_active Expired - Lifetime
- 1999-02-05 EP EP99905763A patent/EP1051241B1/en not_active Expired - Lifetime
- 1999-02-05 AU AU25852/99A patent/AU2585299A/en not_active Abandoned
- 1999-02-05 ES ES99905763T patent/ES2245089T3/es not_active Expired - Lifetime
- 1999-02-05 WO PCT/US1999/002471 patent/WO1999039815A1/en active IP Right Grant
- 1999-02-05 DE DE69924969T patent/DE69924969D1/de not_active Expired - Lifetime
Also Published As
Publication number | Publication date |
---|---|
AU2585299A (en) | 1999-08-23 |
EP1051241A1 (en) | 2000-11-15 |
TW427927B (en) | 2001-04-01 |
CA2320361A1 (en) | 1999-08-12 |
US6029956A (en) | 2000-02-29 |
WO1999039815A1 (en) | 1999-08-12 |
DE69924969D1 (de) | 2005-06-02 |
ES2245089T3 (es) | 2005-12-16 |
EP1051241B1 (en) | 2005-04-27 |
CA2320361C (en) | 2003-08-26 |
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