DKT Energy Technology

National High-Tech Enterprise; Sichuan Provincial Enterprise Technology Center; Class B Qualification For Chemical Engineering Design; Class A Qualification For Environmental Pollution Prevention And Control; Pressure Pipeline GC1 Design Qualification

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Hydrogen Recovery via Pressure Swing Adsorption at a Chemical Plant in Shaanxi



Detailed Introduction


  Project Content

  Pressure Swing Adsorption Hydrogen Production Unit (PSA-H2)

  Scale

  24,000 Nm³/h Methanol Flash Gas Pressure Swing Adsorption Hydrogen Recovery Unit

  Technical Indicators

  Methanol purge gas flow rate: 24,000 Nm³/h;

  Methanol purge gas composition: 77.8% H2, 4.2% CO, 6.8% CH4, 8.2% N2, 2.9% CO2.

  Pressure: 5.0 MPa

  Ammonia synthesis purge gas flow rate: 850 Nm³/h;

  Composition of the ammonia synthesis purge gas: 69% H2, 2% CH4, 22.5% N2, 6.5% NH3.

  Pressure: 10.0 MPa

  Hydrogen content of the product: ≥99.7%

  Hydrogen recovery rate: ≥91.0%

  Technical Features

  The comprehensive utilization of methanol purge gas and ammonia synthesis purge gas is achieved through the application of highly efficient high-pressure ammonia scrubbing technology, enabling single-stage PSA separation to meet specification requirements. This approach features low energy consumption, reduced operating costs, high purity of the recovered valuable components, and reliable recovery rates.


Keyword: Hydrogen Recovery via Pressure Swing Adsorption at a Chemical Plant in Shaanxi

Sichuan DKT Energy Technology Co., Ltd.( A subsidiary of Hydrexia (China))