logo

LIMITS OF SMALL SCALE PRESSURE SWING ADSORPTION

PDF Publication Title:

LIMITS OF SMALL SCALE PRESSURE SWING ADSORPTION ( limits-small-scale-pressure-swing-adsorption )

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

Text from PDF Page: 176

(A13) The external heat transfer coefficient (hext) was found by using natural convection from the surface of the column. A.5. Momentum balance Column pressure drop was modeled using the Ergun equation.4 A.6. Boundary conditions The mass balance boundary condition for steps with an inlet gas flow is described in equation A15: where z = 0 is the end of the column where gas is entering and the velocity is set by equation A16 depending on the step. For steps with an outlet gas flow, the boundary condition described by equation A17: where z=L is the end of the column where the gas is exiting. For constant pressure steps, the total gas concentration at the inlet of the column is fixed. For varying pressure steps, the gas velocity is fixed at the outlet of the column. 157

PDF Image | LIMITS OF SMALL SCALE PRESSURE SWING ADSORPTION

limits-small-scale-pressure-swing-adsorption-176

PDF Search Title:

LIMITS OF SMALL SCALE PRESSURE SWING ADSORPTION

Original File Name Searched:

Limits of Small Scale PSA_Aaron Moran.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 | RSS | AMP