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PRODUCTS

Hydrogen & Helium Extraction & Purification from LNG BOG (Boiled-off Gas)

Process Inlet Parameters

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Process Outlet Parameters

Helium Gas Specification

  • He Purity: ≥99.999%mol

  • He Pressure: ≥200barg (Pressurized)

  • He Yield: ≥97%


Hydrogen Gas Specification

  • H2 Purity: ≥99.999%mol

  • H2 Pressure: ≥200barg (Pressurized)

  • H2 Yield: ≥95%

 
Process Description

Using LNG BOG (Boil Off Gas) as feed gas, CH4, N2 and Ne in He/H2 mixture are removed after multiple pretreatment and pre-purification (including but not limited to oil removal, water removal, low-temperature separation and purification, rewarming, pressurization, drying, decarburization, etc.), and the impurities are a large number of CH4 and N2, and the CH4, N2 and Ne in the He/H2 mixture are removed by membrane separation, PSA refining, He/H2 separation by alloy, TSA purification, etc., respectively, and high-purity He and high-purity H2 products are extracted.

The scope of this scheme is from the first shut-off valve of the feed gas inlet, the first shut-off valve of each purge gas, to the filling system outlet, the returned natural gas outlet, the last shut-off valve of each sampling port, including membrane purification unit, PSA purification unit, He/H2 separator unit, He liquefaction unit, filling unit, controlling unit, analysis unit, etc.


Natural Gas/Coalbed Methane/Shale Gas Separation System

Process Outlet Parameters

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Process Outlet Parameters

Helium Gas Specification

  • He Purity: ≥99.999%mol

  • He Pressure: ≥200barg (Pressurized)

  • He Yield: ≥97%


Hydrogen Gas Specification

  • H2 Purity: ≥99.999%mol

  • H2 Pressure: ≥200barg (Pressurized)

  • H2 Yield: ≥95%


Liquefied C
2H6 Specification

  • C2H6 Purity: ≥99.999%mol

  • C2H6 Pressure:≥1barg

  • C2H6 Yield:≥98%


LPG Specification

  • LPG Purity: ≥99%mol

  • LPG Pressure: ≥1barg

  • LPG Yield: ≥98%


LNG Specification (If Needed)

  • LNG Purity: ≥99%mol

  • LNG Pressure: ≥1barg

  • LNG Yield: ≥98%


Process Description

Using Natural Gas/Coalbed Methane/Shale Gas as feed gas, CH4, N2 and Ne in He/H2 mixture are removed after multiple pretreatment and pre-purification (including but not limited to oil removal, water removal, low-temperature separation and purification, rewarming, pressurization, drying, decarburization, etc.), and the impurities are a large number of CH4 and N2, and the CH4, N2 and Ne in the He/H2 mixture are removed by membrane separation, PSA refining, He/H2 separation by alloy, TSA purification, etc., respectively, and high-purity He and high-purity H2 products are extracted.

The scope of this scheme is from the first shut-off valve of the feed gas inlet, the first shut-off valve of each purge gas, to the filling system outlet, the returned natural gas outlet, the last shut-off valve of each sampling port, including membrane purification unit, PSA purification unit, He/H2 separator unit, He liquefaction unit, filling unit, controlling unit, analysis unit, etc.



CO2 Removal System for Natural Gas/Coalbed Methane/Shale Gas

Process Outlet Parameter

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Process Outlet Parameters

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Among them, the yield of natural gas >85%, and the CO2 content in natural gas product gas decreased from 7.357%mol to 3%mol


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