Installation method of equipment, inspection method of equipment, inspection method of connection of equipment, supporting structure
US-2019314939-A1 · Oct 17, 2019 · US
US10161675B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10161675-B2 |
| Application number | US-201415532764-A |
| Country | US |
| Kind code | B2 |
| Filing date | Dec 9, 2014 |
| Priority date | Dec 9, 2014 |
| Publication date | Dec 25, 2018 |
| Grant date | Dec 25, 2018 |
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A natural gas liquefaction system includes a piping rack for supporting a raw material gas transporting pipe for transporting the raw material gas; a pre-cooling heat exchanger for pre-cooling the raw material gas with a first refrigerant; a first refrigerant compressor for compressing the first refrigerant; a plurality of first air-cooled heat exchangers disposed on a top of the piping; a liquefier for liquefying the raw material gas which has been cooled by the pre-cooling heat exchanger, wherein the piping rack has a widened section along a part of a length of the piping rack, wherein the pre-cooling heat exchanger and the first refrigerant compressor are disposed on either side of the widened section of the piping rack, and are connected to each other via a first refrigerant transporting pipe extending in a direction intersecting a lengthwise direction of the piping rack for transporting the first refrigerant.
Opening claim text (preview).
The invention claimed is: 1. A natural gas liquefaction system for cooling a natural gas supplied as a raw material gas to produce a liquefied natural gas, comprising: a piping rack for supporting a raw material gas transporting pipe for transporting the raw material gas; a pre-cooling heat exchanger for pre-cooling the raw material gas with a first refrigerant; a first refrigerant compressor for compressing the first refrigerant; a plurality of first air-cooled heat exchangers disposed on a top of the piping rack for cooling the first refrigerant compressed by the first refrigerant compressor; a liquefier for liquefying the raw material gas by further cooling the raw material gas which has been cooled by the pre-cooling heat exchanger; a second refrigerant compressor for compressing a second refrigerant used for cooling the raw material gas in the liquefier; a plurality of second air-cooled heat exchangers disposed on the top of the piping rack for cooling the second refrigerant compressed by the second refrigerant compressor; and a refrigerant heat exchanger for cooling the second refrigerant with the first refrigerant; wherein the piping rack defines a length measured in a lengthwise direction and has a widened section along a part of the length of the piping rack, the widened section having a first width measured in a crosswise direction perpendicular to the lengthwise direction in a plan view between a first side of the piping rack and a second side of the piping rack, the first width being greater than a second width of another part of the length of the piping rack, wherein the pre-cooling heat exchanger and the first refrigerant compressor are disposed opposite to each other in the crosswise direction across the widened section of the piping rack, and are connected to each other via a first refrigerant transporting pipe extending across the widened section for transporting the first refrigerant, wherein the second refrigerant compressor and the refrigerant heat exchanger are disposed opposite to each other in the crosswise direction across the widened section of the piping rack, and are connected to each other via a second refrigerant transporting pipe extending across the widened section for transporting the second refrigerant, and wherein the second refrigerant compressor is disposed adjacent to the first refrigerant compressor along the first side of the piping rack, and the refrigerant heat exchanger is disposed adjacent to the pre-cooling heat exchanger along the second side of the piping rack. 2. The natural gas liquefaction system according to claim 1 , wherein the piping rack comprises: a first rack extending in the lengthwise direction, the first rack having a first rack width; and a second rack extending adjacent to said first rack with a length shorter than the first rack to form the widened section, the second rack having a second rack width. 3. The natural gas liquefaction system according to claim 1 , wherein an upstream end portion of the raw material gas transporting pipe is disposed on a first side in the lengthwise direction of the piping rack, and wherein the liquefier is disposed on a second side opposite to the first side in the lengthwise direction of the piping rack. 4. The natural gas liquefaction system according to claim 3 , wherein the widened section is located on the second side in the lengthwise direction of the piping rack. 5. The natural gas liquefaction system according to claim 1 , further comprising: a first gas-liquid separator for the first refrigerant; and a second gas-liquid separator for the second refrigerant, wherein at least one of the first gas-liquid separator and the second gas-liquid separator are disposed in the widened section.
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Separating acid gases, e.g. CO2, SO2, H2S or RSH · CPC title
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