If it is necessary to compress hydrogen to a higher pressure than is possible with the single-compression

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If it is necessary to compress hydrogen to a higher pressure than is possible with the single-compression step above, an alternative is to use two compressors (or a two-stage compressor) with intercooling. In such a process the hydrogen is compressed in the first stage of the compressor, then cooled at constant pressure to a lower temperature, and then compressed further in a second compressor or stage. Although it may not be economical to do so, more than two stages can be used. 

a. Compute the maximum pressure that can be obtained in a two-stage compression with intercooling to 300 K between the stages, assuming hydrogen to be an ideal gas with the heat capacity given in Appendix A.II.

b. Repeat the calculation above for a three-stage compression with intercooling to 300 K. 

 Appendix A.II

Paraffinic Hydrocarbons Methane Ethane Propane n-Butane i-Butane n-Pentane n-Hexane Monoolefinic Hydrocarbons

Acetylenes and Diolefins Acetylene Methylacetylene Dimethylacetylene Propadiene 1,3-Butadiene Isoprene

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