System and method for liquefying natural gas
US-2015338161-A1 · Nov 26, 2015 · US
US10215486B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10215486-B2 |
| Application number | US-201314655405-A |
| Country | US |
| Kind code | B2 |
| Filing date | Dec 27, 2013 |
| Priority date | Dec 28, 2012 |
| Publication date | Feb 26, 2019 |
| Grant date | Feb 26, 2019 |
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A liquefied gas production facility includes a plurality of liquefied gas producers which produce liquefied gas by removing an unnecessary substance and liquefying feed gas containing methane as a main component.
Opening claim text (preview).
The invention claimed is: 1. A liquefied gas production facility comprising: a plurality of liquefied gas producers which produce liquefied gas by removing an unnecessary substance and liquefying feed gas containing methane as a main component, wherein the plurality of liquefied gas producers comprise a first liquefied gas producer, a second liquefied gas producer, and a third liquefied gas producer, wherein the first and second liquefied gas producers are adjacent to each other, the second and third liquefied gas producers are adjacent to each other, and the second gas producer is arranged between the first and third gas producers, wherein each of the liquefied gas producers is rectangular and comprises: a heat exchanger that cools the feed gas by causing the feed gas to exchange heat with a refrigerant; a compressor that compresses the refrigerant that is evaporated as a result of the heat exchange with the feed gas, an air fin cooler unit that cools the compressed refrigerant, the air fin cooler unit being rectangular and comprising a plurality of air fin coolers that are arranged along at least one straight line; and an expander that cools the cooled refrigerant through adiabatic expansion, wherein, in the each of the liquefied gas producers, each of the heat exchanger, the compressor, and the expander is arranged at a side of the air fin cooler unit in a longitudinal direction of the air fin cooler unit, wherein the first and second liquefied gas producers are shifted from each other in a longitudinal direction of the first liquefied gas producer, wherein a first ratio X/L of a distance (X) to a length (L) is equal to or greater than 0.2, the distance (X) being a longitudinally shifted distance of the second liquefied gas producer and the length (L) being a longitudinal length of the first liquefied gas producer, wherein the plurality of air fin coolers in the second liquefied gas producer comprise a propane subcooler that is disposed at the opposite side of the direction in which the second liquefied gas producer is shifted, wherein the second and third liquefied gas producers are shifted from each other in the longitudinal direction of the first liquefied gas producer, wherein a second ratio X/L of a distance (X) to a length (L) is equal to or greater than 0.2, the distance (X) being a longitudinally shifted distance of the third liquefied gas producer and the length (L) being a longitudinal length of the second liquefied gas producer, and wherein the second and third liquefied gas producers are arranged in a lateral direction of the first liquefied gas producer. 2. The liquefied gas production facility according to claim 1 , wherein hot air discharged from the air fin cooler unit of the first liquefied gas producer does not accumulate in a space between the air fin cooler unit of the first liquefied gas producer and the air fin cooler unit of the second liquefied gas producer. 3. The liquefied gas production facility according to claim 1 , wherein the first ratio X/L is equal to or greater than 0.5. 4. The liquefied gas production facility according to claim 1 , wherein the first ratio X/L is equal to or greater than 0.6. 5. The liquefied gas production facility according to claim 1 , wherein each of the liquefied gas producers is provided with a utility facility that is arranged at a side of each of the liquefied gas producers in a direction opposite to the direction in which the second liquefied gas producers is shifted. 6. The liquefied gas production facility according to claim 1 , wherein a plurality of weather information sets are selected from a plurality of items of weather information which are related to areas and times and which include at least temperature data, the plurality of weather information sets being related to a plurality of times over a fixed period concerning a first area containing a location at which the liquefied gas producers are placed, wherein a plurality of first narrow-area weather information sets related to a plurality of second areas which are disposed within the first area and which are smaller than the first area are generated by solving, with the use of the selected plurality of weather information sets as input data, differential equations expressing the weather information based on analysis models used for conducting weather simulations, wherein a second narrow-area weather information set concerning a second area containing the location of the liquefied gas producers is selected from among the generated plurality of first narrow-area weather information sets, and wherein, by using wind direction data included in the second narrow-area weather information set, the first and second liquefied gas producers are arranged so as to be shifted from each other in the longitudinal direction of the first liquefied gas producer so that gas discharged from the first liquefied gas producer, which is at an upwind side according to the wind direction data included in the second narrow-area weather information set, is not sucked in by the second liquefied gas producer, which is at a downwind side according to the wind direction data included in the second narrow-area weather information.
using air or other gas as the cooling medium · CPC title
Removal of the heat of compression, e.g. within an inter- or afterstage-cooler against an ambient heat sink · CPC title
Modularity and arrangement of parts of the liquefaction unit and in particular of the cold box, e.g. pre-fabrication, assembling and erection, dimensions, horizontal layout "plot" · CPC title
Natural gas; Synthetic natural gas obtained by processes not covered by C10G, C10K3/02 or C10K3/04 {(liquefying by pressure and cold treatment F25J)} · CPC title
Hydrocarbons, e.g. natural gas · CPC title
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