Design and Operation of Pressure Swing Adsorption Processes

PDF Publication Title:

Design and Operation of Pressure Swing Adsorption Processes ( design-and-operation-pressure-swing-adsorption-processes )

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

Text from PDF Page: 016

Separation of gases accounts for a major fraction of the production cost in chemical, petro- chemical, and related industries. There has been a growing demand for economical and energy efficient gas separation processes. The new generation of more selective adsorbents developed in recent years has enabled adsorption-based technologies to compete successfully with tra- ditional gas separation techniques, such as cryogenic distillation and absorption. The last few decades have seen a considerable increase in the applications of adsorptive gas separation technologies, such as pressure swing adsorption (PSA). Pressure swing adsorption is a versa- tile technology for separation and purification of gas mixtures. While initial applications of PSA included gas drying and purification of dilute mixtures, current industrial applications include solvent vapor recovery, air fractionation, production of hydrogen from steam-methane reformer (SMR) and petroleum refinery offgases, separation of hydrocarbons such as carbon monoxide-hydrogen, carbon dioxide-methane, and n-paraffins separation, and alcohol dehy- dration. Advent of commercial PSA operations started with the early patents on this subject granted to Skarstrom [176] and Guerin de Montgareuil and Domine [60]. Since then, PSA has become the state-of-the-art separation technology for applications like air fractionation and hydrogen production. Many of these processes are described in published books and review articles on this subject [31, 92, 106, 154, 156, 166, 169, 181, 206]. Moreover, Sircar [167] has given an extensive list of publications on PSA which highlights growth in the research and development of PSA technology. PSA processes involve selectively adsorbing certain components of a gas mixture on a microporous-mesoporous solid adsorbent at a relatively high pressure, via gas-solid contact in a packed column, in order to produce a gas stream enriched in less strongly adsorbed components of the feed gas. The adsorbed components are then desorbed from the solid by lowering their gas-phase partial pressures inside the column to enable adsorbent re-usability. Desorbed gases, as a result, are enriched in the more strongly adsorbed components of the feed gas. No external heat is generally used for desorption. The selectivity in a PSA process comes 1.1 PSA Overview 1.1 PSA Overview Chapter 1. Introduction 2

PDF Image | Design and Operation of Pressure Swing Adsorption Processes

PDF Search Title:

Design and Operation of Pressure Swing Adsorption Processes

Original File Name Searched:

anshul_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)