Article ID Journal Published Year Pages File Type
642276 Separation and Purification Technology 2012 11 Pages PDF
Abstract

Landfill and digester gas purification processes usually incorporate the removal of volatile methylsiloxanes (VMS). State-of-the-art technology is adsorption on activated carbon. This paper investigates a potential alternative: membranes. The permeabilities of common VMS in a commercially available polydimethylsiloxane (PDMS) membrane are determined as a function of temperature. A synthetic biogas mixture containing silicon in landfill gas-typical concentrations is purified in 3-end and 4-end operation. The results are presented using dimensionless numbers to facilitate upscaling. In general, PDMS can be used for siloxane removal, especially in 4-end operation using ambient air as sweep gas, where energy demand is significantly lower than in 3-end. However, depending on the desired degree of purification, methane losses of approximately 7% must be accepted. Only alternative membrane materials with higher carbon dioxide–methane selectivities have the potential for lower methane losses.

► Siloxane permeabilities in PDMS are between 9000 (L2) and 50,000 Barrer (D5) at 20 °C. ► Siloxane–methane selectivity in PDMS is between 13 (L2) and 76 (D5). ► Permeabilities were found to be slightly lower in 4-end than in 3-end operation. ► 4-End is significantly more energy-efficient than 3-end operation. ► Air can be used as sweep gas without reaching explosive limits.

Related Topics
Physical Sciences and Engineering Chemical Engineering Filtration and Separation
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