GB1199554A - Improved Method and Apparatus for Varying Physical Condition of a Gas. - Google Patents
Improved Method and Apparatus for Varying Physical Condition of a Gas.Info
- Publication number
- GB1199554A GB1199554A GB4837/69A GB483769A GB1199554A GB 1199554 A GB1199554 A GB 1199554A GB 4837/69 A GB4837/69 A GB 4837/69A GB 483769 A GB483769 A GB 483769A GB 1199554 A GB1199554 A GB 1199554A
- Authority
- GB
- United Kingdom
- Prior art keywords
- air
- compartment
- valve
- piston
- vessel
- 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
- B01D5/00—Condensation of vapours; Recovering volatile solvents by condensation
- B01D5/0003—Condensation of vapours; Recovering volatile solvents by condensation by using heat-exchange surfaces for indirect contact between gases or vapours and the cooling medium
- B01D5/0012—Vertical tubes
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D1/00—Evaporating
- B01D1/28—Evaporating with vapour compression
- B01D1/2887—The compressor is integrated in the evaporation apparatus
-
- 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
- B01D3/06—Flash distillation
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D5/00—Condensation of vapours; Recovering volatile solvents by condensation
- B01D5/0033—Other features
- B01D5/0039—Recuperation of heat, e.g. use of heat pump(s), compression
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/02—Treatment of water, waste water, or sewage by heating
- C02F1/04—Treatment of water, waste water, or sewage by heating by distillation or evaporation
- C02F1/043—Details
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A20/00—Water conservation; Efficient water supply; Efficient water use
- Y02A20/124—Water desalination
Abstract
1,199,554. Moving gases hydraulically. ANGLO AMERICAN CORP. OF SOUTH AFRICA Ltd. Jan.29, 1969 [Feb. 2, 1968], No.4837/69. Heading F1N. [Also in Divisions B1-2] Apparatus for changing the temperature and moisture content of a gas comprises expansion and compression compartments 4, 5, each having an inlet valve 7 or 11 and an outlet valve 8 or 10 and each variable in volume by a reciprocating liquid piston 1. The reciprocation of the pistons may be effected by mechanically rocking the compartments or simply as a result of the sequentially occurring pressures in the compartments. The apparatus may perform either a heating or cooling cycle. To operate as an air heater and dehumidifier, the air for treatment is admitted to the expansion compartment 4 through the inlet valve 7. The valve 7 is closed by a spring 15 before the liquid piston 1 completes its downward stroke in the compartment 4. Hence the air is expanded and moisture is condensed before pressure responsive outlet valve 10 opens to admit the air to a vessel 9, possibly containing a heater. The condensate is removed through a flexible tube 29 leading through a float 3 situated above the liquid 1. From the vessel 9 the air enters the compression compartment 5, this transfer occurring during the downward stroke of its piston. Dryer and hotter air, but at substantially the original pressure, is then discharged from the compartment during the piston's upward stroke. To cool air a reverse operation is effected, and this mode of operation may additionally be used to evaporate a liquid for example in desalination of brine. Thus air enters through the valve 11 and is compressed in the compartment 5 in the presence of the brine injected into the compartment through a spray 26. The compressed air is transferred via a vessel 6 to the expansion compartment where the evaporated water is condensed. The concentrated brine is removed through a valve 27.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
ZA686058 | 1968-02-02 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB1199554A true GB1199554A (en) | 1970-07-22 |
Family
ID=25561242
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB4837/69A Expired GB1199554A (en) | 1968-02-02 | 1969-01-29 | Improved Method and Apparatus for Varying Physical Condition of a Gas. |
Country Status (6)
Country | Link |
---|---|
US (1) | US3577880A (en) |
AT (1) | AT319904B (en) |
BE (1) | BE727730A (en) |
DE (1) | DE1905191A1 (en) |
FR (1) | FR2001243A1 (en) |
GB (1) | GB1199554A (en) |
Families Citing this family (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4418547A (en) * | 1980-12-08 | 1983-12-06 | The Saint E. Company, Inc. | Thermally powered heat transfer systems |
US4403478A (en) * | 1982-03-26 | 1983-09-13 | The United States Of America As Represented By The Secretary Of The Navy | Expander stroke delay mechanism for split stirling cryogenic cooler |
US4450690A (en) * | 1983-01-10 | 1984-05-29 | Clark Jr Robert W | Thermally powered, gravitationally assisted heat transfer systems |
JPS60500424A (en) * | 1983-02-14 | 1985-03-28 | ゼネラル ニユ−メテイツクス コ−ポレ−シヨン | Closed cycle cryogenic cooling equipment |
US4566291A (en) * | 1983-02-14 | 1986-01-28 | General Pneumatics Corporation | Closed cycle cryogenic cooling apparatus |
DE102009020925A1 (en) * | 2009-05-12 | 2010-11-18 | Linde Aktiengesellschaft | Compressor with piston dummy |
FR3107127B1 (en) | 2020-02-07 | 2023-03-24 | Commissariat Energie Atomique | Method and device for designing a computational memory circuit |
FR3113332B1 (en) | 2020-08-04 | 2022-08-26 | Commissariat Energie Atomique | Reconfigurable memory module adapted to implement calculation operations |
Family Cites Families (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US1469729A (en) * | 1923-10-02 | myers | ||
US1257607A (en) * | 1908-07-17 | 1918-02-26 | Humphrey Gas Pump Company | Method of compressing air or gases. |
US1152394A (en) * | 1912-01-31 | 1915-09-07 | Humphrey Gas Pump Company | Utilizing heat energy. |
US1258407A (en) * | 1916-09-16 | 1918-03-05 | Stirling B Hill | Air-compressor. |
US1254693A (en) * | 1917-06-19 | 1918-01-29 | Humphrey Gas Pump Company | Method of compressing an elastic fluid. |
-
1969
- 1969-01-24 US US793673*A patent/US3577880A/en not_active Expired - Lifetime
- 1969-01-29 GB GB4837/69A patent/GB1199554A/en not_active Expired
- 1969-01-31 BE BE727730D patent/BE727730A/xx unknown
- 1969-01-31 FR FR6902210A patent/FR2001243A1/fr not_active Withdrawn
- 1969-02-03 AT AT01086/69A patent/AT319904B/en not_active IP Right Cessation
- 1969-02-03 DE DE19691905191 patent/DE1905191A1/en active Pending
Also Published As
Publication number | Publication date |
---|---|
BE727730A (en) | 1969-07-01 |
DE1905191A1 (en) | 1969-08-28 |
AT319904B (en) | 1975-01-10 |
FR2001243A1 (en) | 1969-09-26 |
US3577880A (en) | 1971-05-11 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
PS | Patent sealed [section 19, patents act 1949] | ||
PCNP | Patent ceased through non-payment of renewal fee |