GB1265188A - - Google Patents
Info
- Publication number
- GB1265188A GB1265188A GB1265188DA GB1265188A GB 1265188 A GB1265188 A GB 1265188A GB 1265188D A GB1265188D A GB 1265188DA GB 1265188 A GB1265188 A GB 1265188A
- Authority
- GB
- United Kingdom
- Prior art keywords
- liquid
- coil
- gas
- jacket
- coils
- 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
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
- B01D3/008—Liquid distribution
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D1/00—Evaporating
- B01D1/14—Evaporating with heated gases or vapours or liquids in contact with the liquid
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
1,265,188. Heat and mass transfer apparatus. SEVERODONETSKY ORDENA LENINA KHIMICHESKY KOMBINAT. 14 Nov., 1969, No. 55777/69. Heading B1B. A heat and mass transfer process, such as evaporation wherein downflowing liquid and rising gas are contacted in a series of foam layers, is carried out in an apparatus comprising a shell 1 in which a plurality of conically-coiled tubes 3 are mounted one above another, each coil 3 having apertures for the upward flow of gas and being provided with a central tubular member 5 which projects downwardly into a liquid overflow vessel 6 thereby forming a liquid-seal for downflowing liquid which is to be distributed onto the coil 3 below. The liquid to be treated is introduced into the apparatus through inlet 10; and the gas is supplied through inlet 12. The rising gas stream is set in whirling motion by fins 7 under each coil 3. A turbulent foamlayer is produced on each coil 3. The treated liquid is discharged through outlet 15; and the gas is discharged through separator 9. Shell 1 is surrounded by a jacket 2. Additional coiled tubes 8 are disposed between the coils 3. The jacket 2 and coils 3 and 8 may be supplied with steam or with, cooling medium. The production of concentrated ammonium nitrate is referred to.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB5577769 | 1969-11-14 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB1265188A true GB1265188A (en) | 1972-03-01 |
Family
ID=10474848
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB1265188D Expired GB1265188A (en) | 1969-11-14 | 1969-11-14 |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB1265188A (en) |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2015090476A1 (en) * | 2013-12-20 | 2015-06-25 | Statoil Petroleum As | System for fluid redistribution |
CN105980025A (en) * | 2013-12-18 | 2016-09-28 | 格雷迪安特公司 | Counter-flow heat/mass exchange feedback control |
US9981860B2 (en) | 2015-05-21 | 2018-05-29 | Gradiant Corporation | Production of ultra-high-density brines using transiently-operated desalination systems |
US10143936B2 (en) | 2015-05-21 | 2018-12-04 | Gradiant Corporation | Systems including an apparatus comprising both a humidification region and a dehumidification region with heat recovery and/or intermediate injection |
US10294123B2 (en) | 2016-05-20 | 2019-05-21 | Gradiant Corporation | Humidification-dehumidification systems and methods at low top brine temperatures |
-
1969
- 1969-11-14 GB GB1265188D patent/GB1265188A/en not_active Expired
Cited By (12)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN105980025A (en) * | 2013-12-18 | 2016-09-28 | 格雷迪安特公司 | Counter-flow heat/mass exchange feedback control |
CN105980025B (en) * | 2013-12-18 | 2017-08-22 | 格雷迪安特公司 | Reverse-flow heat/mass exchange feedback control |
WO2015090476A1 (en) * | 2013-12-20 | 2015-06-25 | Statoil Petroleum As | System for fluid redistribution |
GB2536182A (en) * | 2013-12-20 | 2016-09-07 | Statoil Petroleum As | System for fluid redistribution |
RU2656503C2 (en) * | 2013-12-20 | 2018-06-05 | Статойл Петролеум Ас | Fluid media redistribution system |
US10179299B2 (en) | 2013-12-20 | 2019-01-15 | Statoil Petroleum As | System for fluid redistribution |
GB2536182B (en) * | 2013-12-20 | 2020-09-23 | Equinor Energy As | System for fluid redistribution |
US9981860B2 (en) | 2015-05-21 | 2018-05-29 | Gradiant Corporation | Production of ultra-high-density brines using transiently-operated desalination systems |
US10143936B2 (en) | 2015-05-21 | 2018-12-04 | Gradiant Corporation | Systems including an apparatus comprising both a humidification region and a dehumidification region with heat recovery and/or intermediate injection |
US10479701B2 (en) | 2015-05-21 | 2019-11-19 | Gradiant Corporation | Production of ultra-high-density brines using transiently-operated desalination systems |
US11084736B2 (en) | 2015-05-21 | 2021-08-10 | Gradiant Corporation | Production of ultra-high-density brines using transiently-operated desalination systems |
US10294123B2 (en) | 2016-05-20 | 2019-05-21 | Gradiant Corporation | Humidification-dehumidification systems and methods at low top brine temperatures |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
PS | Patent sealed | ||
PCNP | Patent ceased through non-payment of renewal fee |