Methanol-water steam reforming and hydrogen separation integrated ultrahigh-pressure hydrogen production system and method thereof
A technology for steam reforming and hydrogen production system, which is applied in the fields of hydrogen separation, diffusive hydrogen separation, chemical instruments and methods, etc., can solve the problems of inability to realize cyclic hydrogen production, complex hydrogen production system, complicated hydrogen production process, etc. Cost saving, high hydrogen production efficiency, stable and reliable operation
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Image
Examples
Embodiment 1
[0055] Such as figure 1 As shown, a methanol steam reforming and hydrogen separation integrated ultra-high pressure hydrogen system includes a reforming separation device 3, a three-phase heat exchange device 2, a steam trap 7, a water-cooled heat exchanger 6, a carbon dioxide separation device 4 and The water gas reforming device 5, the reforming and separating device 3 includes a methanol water vapor inlet pipe, a hydrogen outlet pipe and a carbon dioxide mixed residual gas outlet pipe, and the carbon dioxide mixed residual gas outlet pipe is successively connected to the three-phase heat exchange device 2, the steam trap 7, A water-cooled heat exchanger 6, a carbon dioxide separation device 4, and a water-gas reformer 5, the water-cooled heat exchanger 6 is connected to a water cooling tower, and the operating temperature of the water-cooled heat exchanger 6 is 18-30.8°C; the water-gas reformer 5 The outlet is connected to the reformed mixed gas outlet pipe, and the reforme...
Embodiment 2
[0080] A methanol-water ultra-high pressure hydrogen system, using the above-mentioned ultra-high pressure hydrogen system, comprising the following steps:
[0081] S1. The liquid pump 1 sends the methanol water into the methanol water vapor pipe, and the pump pressure is 40-100 MPa. The methanol water is heated and vaporized by the three-phase heat exchange device 2 to become methanol water vapor and enters the reaction chamber of the reforming separation device 3. Methanol steam is decomposed into a mixed gas of hydrogen, carbon dioxide and carbon monoxide;
[0082] The gas phase components of the mixed gas of hydrogen, carbon dioxide and carbon monoxide are 65-75% hydrogen, 20-26% carbon dioxide, and 0.3-3% carbon monoxide;
[0083] S2, the hydrogen suction pipe 32 separates the mixed gas of hydrogen, carbon dioxide and carbon monoxide, and the separated pure hydrogen is collected from the output of the hydrogen suction pipe 32, and the pure hydrogen is sent into the hydrog...
PUM
Login to View More Abstract
Description
Claims
Application Information
Login to View More 


