Operation and Control of Pressure Swing Adsorption Systems

PDF Publication Title:

Operation and Control of Pressure Swing Adsorption Systems ( operation-and-control-pressure-swing-adsorption-systems )

Previous Page View | Next Page View | Return to Search List

Text from PDF Page: 111

Chapter 5. Simultaneous Design and Control Optimization of PSA Systems Under Uncertainty Table 5.5: Boundary conditions for the counter-current purge, counter-current pressure equalization and co-current product repressurization steps for the six step PSA cycle z=0 z=L Counter-current Purge U = fvalve (P, Ppurge, CVbldn) ∂Ci = 0 CU = −fvalve (Pprod, P, CVpurge) Cprod Ci = P Ciprod RT Cprod ∂Z ∂T = 0 ∂Z U = 0 ∂Ci = 0 ∂Z ∂T = 0 ∂Z T = Tprod Counter-current pressure equalization CU = −fvalve (Pdep, P, CVdep) Cdep Ci = P Cidep RT Cdep T = Tdep Co-current repressurization with product U = fvalve (Pfeed, P, CVrepres) Ci=Pyifeed RT T = T feed U = 0 ∂Ci =0 ∂Z ∂T = 0 ∂Z 111

PDF Image | Operation and Control of Pressure Swing Adsorption Systems

PDF Search Title:

Operation and Control of Pressure Swing Adsorption Systems

Original File Name Searched:

Khajuria-H-2011-PhD-Thesis.pdf

DIY PDF Search: Google It | Yahoo | Bing

CO2 Organic Rankine Cycle Experimenter Platform The supercritical CO2 phase change system is both a heat pump and organic rankine cycle which can be used for those purposes and as a supercritical extractor for advanced subcritical and supercritical extraction technology. Uses include producing nanoparticles, precious metal CO2 extraction, lithium battery recycling, and other applications... More Info

Heat Pumps CO2 ORC Heat Pump System Platform More Info

CONTACT TEL: 608-238-6001 Email: greg@infinityturbine.com (Standard Web Page)