Method and system for treating and feeding natural gas to an apparatus for generating power in order to propel a ship

Patent metadata

Field	Value
Publication number	US-10012350-B2
Application number	US-201414783724-A
Country	US
Kind code	B2
Filing date	Apr 3, 2014
Priority date	Apr 11, 2013
Publication date	Jul 3, 2018
Grant date	Jul 3, 2018

Abstract

The invention relates to a method for treating and feeding natural gas from a tank for storing liquefied gas storage to an apparatus for generating power, and to a burner of an apparatus for generating power in a ship, said method comprising the following consecutive steps:
supplying power to the apparatus for generating power, during which step natural gas is fed through a phase separator that returns a heavy fraction of the natural gas containing the hydrocarbons having the longest carbon chains to the tank as condensate and feeding a light fraction of the natural gas containing the hydrocarbons having the shortest carbon chains to the apparatus for generating power; and then recovering the heavy fraction of the natural gas, during which step natural gas is carried from the tank to the burner, bypassing said phase separator.

First claim

The invention claimed is:

1. A method for treating and feeding natural gas, in a ship, from a liquefied gas storage tank to an apparatus for generating power and to a burner of an installation for generating power, said method comprising the steps of:
supplying the apparatus for generating power with natural gas, during which step a first stream of natural gas is carried through a phase separator that separates the first stream of natural gas into a heavy fraction and a light fraction, each fraction containing hydrocarbons that have carbon chains; the carbon chains of the heavy fraction being longer than the carbon chains of the light fraction; the step of supplying the apparatus for generating power further comprising the step of returning the heavy fraction to the tank in the form of condensate and feeding the light fraction to the apparatus for generating power; then
recovering the heavy fraction during which step a second stream of natural gas is fed from the tank to the burner, bypassing the phase separator.

2. The method as claimed in claim 1 , wherein the step of supplying the apparatus for generating power further comprises the step of monitoring a variable indicative of the methane number of the first stream of natural gas.

3. The method as claimed in claim 2 , wherein the step of monitoring the variable indicative of the methane number of the first stream of natural gas comprises at least one of an automatic switchover and an alarm that signals when the variable indicative of the methane number of the first stream of natural gas reaches a threshold.

4. The method as claimed in claim 2 , wherein the variable indicative of the methane number of the first stream of natural gas is determined by measuring at least one of a flow rate of the light fraction downstream of the phase separator, a temperature of evaporated natural gas collected in the tank, a level in a condensate collecting container, and a purge frequency of the condensate collecting container.

5. A system carried onboard a ship, for treating and feeding natural gas from a liquefied gas storage tank to an apparatus for generating power, and to a burner of an installation for generating power, the system comprising:
a first supply circuit feeding the apparatus for generating power, said first circuit comprising a phase separator arranged to separate a first stream of natural gas into a heavy fraction and a light fraction, each fraction containing hydrocarbons that have carbon chains, the carbon chains of the heavy fraction being longer than the carbon chains of the light fraction; the phase separator connected, downstream to a return conduit allowing the heavy fraction to be returned to the tank in the form of condensate and, to a supply conduit feeding the light fraction to the apparatus for generating power
a second supply circuit feeding the burner arranged to feed a second stream of natural gas from the tank to the burner, the second circuit bypassing the phase separator.

6. The system as claimed in claim 5 , wherein the first circuit comprises, upstream of the phase separator, at least one portion in common with the second circuit and designed to allow at least one of forced vaporization of liquefied natural gas and collection of natural gas that has evaporated in the tank.

7. The system as claimed in claim 6 , wherein the circuit portion common to the first and to the second circuit comprises an intake pipeline opening toward a bottom of the tank, equipped with a pump and a forced vaporization apparatus allowing liquefied natural gas to be converted into the first or second stream of gas.

8. The system as claimed in claim 6 , wherein the circuit portion common to the first and to the second circuit comprises a pipeline opening into a top part of the tank to collect natural gas that has evaporated in the tank.

9. The system as claimed in claim 5 , wherein the circuit portion common to the first and to the second circuit is limited downstream by a switchable three way connection member allowing the circuit portion in common to be connected selectively to an inlet of the phase separator or to a portion of the second circuit leading to the burner.

10. The system as claimed in claim 5 , wherein the second circuit for feeding the burner is fitted with a gas heating appliance.

11. The system as claimed in claim 5 , wherein the first circuit for supplying natural gas to the apparatus for generating power comprises a compressor positioned downstream of the phase separator.

12. The system as claimed in claim 5 , further comprising a device for monitoring a variable indicative of a methane number of the first stream of natural gas.

13. The system as claimed in claim 12 , wherein the device for monitoring a variable indicative of the methane number of the first stream of natural gas comprises a sensor for measuring at least one of a flow rate in the supply conduit leading toward the apparatus for generating power, a sensor for measuring a temperature of evaporated natural gas collected in the tank, a sensor for measuring a level in a condensate collecting container, and a counter for measuring the purge frequency of a condensate collection container.

14. The system as claimed in claim 12 , wherein the device for monitoring a variable indicative of the methane number of the first stream of natural gas is designed to activate at least one of an alarm signal, and a switchable three-way connection member so as to feed the second stream of natural gas toward the burner when the variable indicative of the methane number of the first stream of natural gas crosses a threshold.

15. A ship comprising a liquefied gas storage tank, an apparatus for generating power, a burner of an installation for generating power and a system for treating and feeding the natural gas, the system comprising:
a first supply circuit feeding the apparatus for generating power, said first circuit comprising a phase separator arranged to separate a first stream of natural gas into a heavy fraction and a light fraction, each fraction containing hydrocarbons that have carbon chains, the carbon chains of the heavy fraction being longer than the carbon chains of the light fraction; the phase separator connected, downstream to a return conduit allowing the heavy fraction to be returned to the tank in the form of condensate and, to a supply conduit feeding the light fraction to the apparatus for generating power
a second supply circuit feeding the burner arranged to feed a second stream of natural gas from the tank to the burner, the second circuit bypassing the phase separator.

16. The ship as claimed in claim 15 , wherein the apparatus for generating power is intended for the propulsion of the ship.

17. The ship as claimed in claim 15 , wherein the liquefied gas storage tank is a tank with a membrane.

18. The ship as claimed in claim 15 , wherein the liquefied gas storage tank is a storage tank at atmospheric pressure.

19. A method for filling the liquefied gas storage tank of the ship as claimed in claim 15 , wherein the method comprises the step of feeding a fluid through insulated pipelines from a floating or on shore storage facility to the liquefied gas storage tank of the ship.

20. A fluid transfer system, the system comprising the ship as claimed in claim 15 , insulated pipelines arranged in such a way as to connect the liquefied gas storage tank which is installed in a hull of the ship to a floating or on shore storage facility and a pump for driving a stream of fluid through the insulated pipelines f

Assignees

• Gaztransport Et Technigaz

Inventors

• Le Bruchec Pierre
• Denier-Guenegou Anaïs
• Guernec Loïc
• Spittael Laurent
• Beauvais David
• Huchet Jérôme
• Diouf Abdoulaye

Classifications

• F17C13/082

  for large sea-borne storage vessels (load-accommodating arrangements for ships or waterborne vessels B63B25/12) · CPC title

• F17C13/004

  for large storage vessels not under pressure (F17C13/008 and F17C13/02 - F17C13/12 take precedence) · CPC title

• F17C2270/0136

  Terminals · CPC title

• F17C2260/015

  Facilitating maintenance · CPC title

• F17C9/02 Primary

  with change of state, e.g. vaporisation · CPC title