Patent US4170115A successfully refreshed from Google Patents.
US4170115A
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US
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Apparatus and process for vaporizing liquefied natural gas
Assignee: Osaka Gas Co Ltd
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Filing: 1977-07-05
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Granted: 1979-10-09
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Expires: 1997-07-05
Abstract
Abstract Apparatus for vaporizing liquefied natural gas using estuarine water comprising as arranged in series a heat exchanger of the indirectly heating, intermediate fluid type, a multitubular concurrent heat exchanger and a multitubular countercurrent heat exchanger and process for vaporizing liquefied natural gas using the same.
Inventors
- 👤 Isami Ooka
- 👤 Tomohiro Sato
- 👤 Kyohei Niwa
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-05 21:25
CPC Classifications
F; F17; F17C; F17C9/00; F17C9/02; F28; F28D; F28D15/00; F28D15/02; F17C2201/00; F17C2201/01; F17C2201/0104; F17C2201/0109; F17C2201/03; F17C2201/035; F17C2221/00; F17C2221/03; F17C2221/032; F17C2221/033; F17C2223/00; F17C2223/01; F17C2223/0146; F17C2223/0153; F17C2223/0161; F17C2223/03; F17C2223/033; F17C2225/00; F17C2225/01; F17C2225/0107; F17C2225/0123; F17C2227/00; F17C2227/03; F17C2227/0302; F17C2227/0309; F17C2227/0316; F17C2227/0318; F17C2227/0367; F17C2227/0388; F17C2227/0393; F17C2265/00; F17C2265/05
Claims Analysis
Total Claims: 12
Claim 1
Independent Claim
337 words
Apparatus for vaporizing liquefied natural gas and heating the vaporized gas close to the temperature of estuarine water used as the heat source comprising: (i) a heat exchanger of the indirect heating type having enclosed therein an intermediate heating medium divided into a lower liquid portion and an upper vapor portion for producing vaporized natural gas of a low temperature not higher than the freezing point of estuarine water from the liquefied natural gas, an inlet for introducing estuarine water into said lower liquid portion for indirect heat exchange with said intermediate heating medium, an outlet for discharging estuarine water from said lower liquid portion after said indirect heat exchange with said intermediate heating medium, said intermediate heating medium being heated to a vaporization temperature which is not higher than the freezing point of said estuarine water by said indirect heat exchange therewith in said lower liquid portion, the vaporized intermediate heating medium passing to said upper vapor portion, an inlet for introducing liquid natural gas into said upper vapor portion for indirect heat exchange with the vaporized intermediate heat exchange medium to vaporize said liquid natural gas, and an outlet for discharge of vaporized liquid natural gas, (ii) a multitubular concurrent heat exchanger for heating the vaporized gas from the first heat exchanger by heat exchange between the gas and estuarine water, the concurrent heat exchanger having an inlet and an outlet for the gas and an inlet and a discharge outlet for estuarine water, and the gas inlet being in fluid communication with the gas outlet of the first heat exchanger, and (iii) a multitubular countercurrent heat exchanger for heating the vaporized natural gas from the second heat exchanger close to the temperature of estuarine water by heat exchange between the gas and estuarine water, the countercurrent heat exchanger having an inlet and an outlet for the gas and an inlet and a discharge outlet for estuarine water, and the gas inlet being in fluid communication with the gas outlet of the second heat exchanger.
Claim 2
Dependent Claim
337 words
Apparatus for vaporizing liquefied natural gas and heating the vaporized gas close to the temperature of estuarine water used as the heat source comprising: (i) a heat exchanger of the indirect heating type having enclosed therein an intermediate heating medium divided into a lower liquid portion and an upper vapor portion for producing vaporized natural gas of a low temperature not higher than the freezing point of estuarine water from the liquefied natural gas, an inlet for introducing estuarine water into said lower liquid portion for indirect heat exchange with said intermediate heating medium, an outlet for discharging estuarine water from said lower liquid portion after said indirect heat exchange with said intermediate heating medium, said intermediate heating medium being heated to a vaporization temperature which is not higher than the freezing point of said estuarine water by said indirect heat exchange therewith in said lower liquid portion, the vaporized intermediate heating medium passing to said upper vapor portion, an inlet for introducing liquid natural gas into said upper vapor portion for indirect heat exchange with the vaporized intermediate heat exchange medium to vaporize said liquid natural gas, and an outlet for discharge of vaporized liquid natural gas, (ii) a multitubular concurrent heat exchanger for heating the vaporized gas from the first heat exchanger by heat exchange between the gas and estuarine water, the concurrent heat exchanger having an inlet and an outlet for the gas and an inlet and a discharge outlet for estuarine water, and the gas inlet being in fluid communication with the gas outlet of the first heat exchanger, and (iii) a multitubular countercurrent heat exchanger for heating the vaporized natural gas from the second heat exchanger close to the temperature of estuarine water by heat exchange between the gas and estuarine water, the countercurrent heat exchanger having an inlet and an outlet for the gas and an inlet and a discharge outlet for estuarine water, and the gas inlet being in fluid communication with the gas outlet of the second heat exchanger.
Claim 3
Dependent Claim
17 words
Apparatus as defined in claim 1 wherein the intermediate heat exchange medium comprises propane, Freon-12 or ammonia.
Claim 4
Dependent Claim
38 words
Apparatus as defined in claim 2 wherein the intermediate heat exchange medium comprises propane which is maintained at a temperature not lower than -10° C. (2 Kg/cm 2 ) within the heat exchanger of the intermediate fluid type.
Claim 5
Dependent Claim
38 words
Apparatus as defined in claim 2 wherein the intermediate heat exchange medium comprises Freon-12 which is maintained at a temperature not lower than -15° C. (0.9 Kg/cm 2 ) within the heat exchanger of the intermediate fluid type.
Claim 6
Dependent Claim
35 words
Apparatus as defined in claim 1 wherein the vaporized natural gas produced in the heat exchanger of the intermediate fluid type has a temperature of -30° to -50° C. (10 to 70 Kg/cm 2 ).
Claim 7
Dependent Claim
159 words
A process for vaporizing liquefied natural gas and heating the vaporized gas close to the temperature of estuarine water used as the heat source comprising the steps of: (i) heating a liquefied refrigerant in indirect heat exchange with estuarine water to a temperature not higher than the freezing point of the estuarine water to produce vaporized refrigerant, the flow velocity of estuarine water being at a value preventing its freezing, (ii) heating liquefied natural gas in indirect heat exchange with the vaporized refrigerant to produce vaporized natural gas having a temperature not higher than the freezing point of estuarine water and to liquefy the refrigerant, the liquefied refrigerant being returned to step (i), (iii) heating the low-temperature vaporized natural gas from step (i) in concurrent indirect heat exchange with estuarine water, and (iv) heating the vaporized natural gas from step (iii) in countercurrent indirect heat exchange with estuarine water to a temperature close to that of the estuarine water.
Claim 8
Dependent Claim
159 words
A process for vaporizing liquefied natural gas and heating the vaporized gas close to the temperature of estuarine water used as the heat source comprising the steps of: (i) heating a liquefied refrigerant in indirect heat exchange with estuarine water to a temperature not higher than the freezing point of the estuarine water to produce vaporized refrigerant, the flow velocity of estuarine water being at a value preventing its freezing, (ii) heating liquefied natural gas in indirect heat exchange with the vaporized refrigerant to produce vaporized natural gas having a temperature not higher than the freezing point of estuarine water and to liquefy the refrigerant, the liquefied refrigerant being returned to step (i), (iii) heating the low-temperature vaporized natural gas from step (i) in concurrent indirect heat exchange with estuarine water, and (iv) heating the vaporized natural gas from step (iii) in countercurrent indirect heat exchange with estuarine water to a temperature close to that of the estuarine water.
Claim 9
Dependent Claim
15 words
A process as defined in claim 6 wherein the refrigerant comprises propane, Freon-12 or ammonia.
Claim 10
Dependent Claim
36 words
A process as defined in claim 7 wherein the refrigerant comprises propane which is maintained at a temperature not lower than -10° C. (2 Kg/cm 2 ) within the heat exchanger of the intermediate fluid type.
Claim 11
Dependent Claim
36 words
A process as defined in claim 7 wherein the refrigerant comprises Freon-12 which is maintained at a temperature not lower than -15° C. (0.9 Kg/cm 2 ) within the heat exchanger of the intermediate fluid type.
Claim 12
Dependent Claim
36 words
A process as defined claim 6 wherein the liquefied natural gas is heated with the refrigerant to produce vaporized natural gas having a low temperature of -30° to -50° C. (10 to 70 Kg/cm 2 ).
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USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1982-10-08 | 1983-04-09 | 1983-10-09 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1986-10-08 | 1987-04-09 | 1987-10-09 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1990-10-08 | 1991-04-09 | 1991-10-09 | $7700.00 | Window Closed / Lapsed |