Method and system for estimating fuel composition
US-9453475-B2 · Sep 27, 2016 · US
US9581296B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9581296-B2 |
| Application number | US-201314060718-A |
| Country | US |
| Kind code | B2 |
| Filing date | Oct 23, 2013 |
| Priority date | Mar 28, 2013 |
| Publication date | Feb 28, 2017 |
| Grant date | Feb 28, 2017 |
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A system for supplying LNG fuel includes a fuel supplying line connected from an LNG storage tank to an engine, a boosting pump provided on the fuel supplying line and configured to pressurize LNG outputted from the LNG storage tank and cool down in a standby mode, a high pressure pump configured to pressurize the LNG outputted from the boosting pump to high pressure, and a return line connected between the LNG storage tank and the high pressure pump, in which the LNG is returned through the return line.
Opening claim text (preview).
What is claimed is: 1. A system for supplying LNG fuel, the system comprising: a fuel supplying line connected from an LNG storage tank to an engine; a boosting pump provided on the fuel supplying line and configured to pressurize LNG outputted from the LNG storage tank, and cool down in a standby mode; a high pressure pump configured to pressurize the LNG outputted from the boosting pump to high pressure; and a return line connected between the LNG storage tank and the high pressure pump, wherein the LNG is returned to the LNG storage tank through the return line, wherein the return line is connected to an internal surface of the high pressure pump, wherein during the standby mode the LNG is not outputted from the high pressure pump to the engine and the return line connected to the high pressure pump is configured to be open, wherein the LNG is returned from the high pressure pump to the LNG storage tank through the return line when a cool-down operation of the high pressure pump is performed, and wherein the boosting pump is configured to operate during the standby mode to increase a flow of the LNG supplied to the high pressure pump. 2. The system of claim 1 , wherein the high pressure pump cools down in the standby mode, and a cool-down operation of the high pressure pump starts after a cool-down operation of the boosting pump is completed. 3. The system of claim 1 , wherein the boosting pump pressurizes the LNG to a pressure of 1 bar to 25 bar, and the high pressure pump pressurizes the LNG to a pressure of 200 bar to 400 bar. 4. The system of claim 1 , wherein the boosting pump is provided between the LNG storage tank and the high pressure pump. 5. The system of claim 1 , wherein the high pressure pump is configured to pressurize the LNG to change a state of the LNG from a liquid state to a supercritical state or a supercooled liquid state. 6. The system of claim 1 , further comprising a heat exchanger positioned between the high pressure pump and the engine and configured to heat the LNG to supply the LNG in a supercritical state at a temperature of 30° C. to 60° C. 7. The system of claim 1 , further comprising a valve provided on the return line and configured to open the return line to allow the LNG in the high pressure pump to flow to the LNG storage tank when the high pressure pump performs the cool-down operation. 8. The system of claim 1 , wherein the return line is opened to cool down the high pressure pump in the standby mode for changing a fuel of the engine from oil to the LNG. 9. The system of claim 1 , wherein the high pressure pump is configured to stop during the standby mode.
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Details of vessels or of the filling or discharging of vessels · CPC title
at least one pump being of the reciprocating positive-displacement type · CPC title
by injecting a liquid · CPC title
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