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Method for offshore liquefaction

  • US 8,646,289 B1
  • Filed: 09/24/2013
  • Issued: 02/11/2014
  • Est. Priority Date: 03/20/2013
  • Status: Expired due to Fees
First Claim
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1. A method for processing natural gas from an offshore well that improves fuel efficiency of a dual nitrogen expansion process for liquefying natural gas offshore, the method comprising:

  • a. connecting a subsea well to a moored floating production storage and offloading vessel using a riser;

    b. receiving well gas from one or more subsea wells and combining the well gas in a primary processing unit mounted on the moored floating production storage and offloading vessel;

    c. separating condensate from the combined gas to produce a high pressure flash gas stream, a wet low pressure natural gas stream, and a wet intermediate pressure natural gas stream, then dehydrating the separated wet condensate and transferring removed water for treatment and disposal;

    d. fractionating and stabilizing the dry condensate and transferring stabilized condensate to storage on the floating production storage and offloading vessel;

    e. compressing the wet low pressure and wet intermediate pressure natural gas streams which are then combined with the high pressure flash gas;

    f. transferring the high pressure flash gas to a gas treatment unit to create a feed gas by removing acid gases (CO2 &

    H2S), water, and heavy hydrocarbon components (C5+);

    g. compressing the feed gas with a natural gas export compressor and transfer a high pressure feed gas to a carbon dioxide refrigeration unit to reduce its temperature, forming pre-cooled high pressure feed gas;

    h. transferring the pre-cooled high pressure feed gas to a disconnectable turret which transfers the pre-cooled high pressure feed gas to a liquefaction unit on a liquefied natural gas transport vessel;

    i. using a heat exchanger to liquefy and condense the pre-cooled high pressure feed gas forming a liquefied high pressure gas stream;

    j. expanding the liquefied high pressure gas stream through a liquid expander forming a low pressure liquefied natural gas stream;

    k. using a warm loop nitrogen expander to receive cooled warm loop gas from the heat exchanger and form warm loop nitrogen refrigerant which is flowed to the heat exchanger and warmed in the heat exchanger forming warm loop nitrogen gas;

    l. using a cold loop nitrogen expander to receive cooled cold loop nitrogen from the heat exchanger and form cold loop nitrogen stream refrigerant which is flowed to the heat exchanger and warmed in the heat exchanger forming cold loop low pressure nitrogen gas which is then combined with warm loop low pressure nitrogen gas to make combined low pressure nitrogen gas;

    m. using a warm loop nitrogen compressor connected to the warm loop nitrogen expander to receive most of the combined low pressure nitrogen gas as a first stream which flows into the warm loop nitrogen compressor forming a warm loop intermediate pressure nitrogen gas;

    n. using a cold loop nitrogen compressor connected to the cold loop nitrogen expander to receive the balance of the combined low pressure nitrogen gas as a second stream, and form a cold loop intermediate pressure nitrogen gas;

    o. combining a warm loop intermediate pressure nitrogen gas with cold loop intermediate pressure nitrogen gas forming a combined intermediate pressure nitrogen gas;

    p. using a nitrogen compressor to compress a combined intermediate pressure nitrogen gas forming high pressure nitrogen gas wherein the nitrogen compressor is powered by an electric motor;

    q. connecting the electric motor to the dual fuel diesel electric main power plant;

    r. splitting the high pressure nitrogen gas into warm loop high pressure nitrogen gas and cold loop high pressure nitrogen gas, where both the warm loop high pressure nitrogen gas and the cold loop high pressure nitrogen gas are simultaneously flowed to the heat exchanger; and

    s. disconnecting the liquefaction vessel from the disconnectable turret when it is sufficiently loaded and moving the liquefaction vessel to a transfer terminal for offloading.

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