Abstract:Emission of sulfur dioxide (SO2) from coal power plants has to be controlled and minimized to reduce environmental risk. This study aimed to investigate the hollow fiber composite membrane was used for the removal of SO2 from a SO2/CO2/N2 mixed gas. Moreover, for the improvement of SO2 removal efficiency, the polyetherimide (PEI) membrane was coated with poly(vinyl chloride)‐graft‐poly(oxyethylene methacrylate) (PVC‐g‐POEM). The PVC‐g‐POEM/PEI composite hollow fiber membrane was extensively characterized by va… Show more
“…Pristine polyetherimide (PEI Ultem 1000P) was supplied in powder form by Sabic Innovative Plastics (Pittsfield, USA). Polyetherimide has a high chemical and thermal resistance ( T g = 215 °C), good mechanical properties and is frequently used in membrane applications …”
A chemical‐free option to reduce membrane fouling is the use of electrical fields for membranes. To maximize the strength of the electric field in compact membrane module constructions, electrically conductive membranes are preferred to only conductive supports. Conductive, porous membranes are sintered from polyetherimide powder particles that are surface‐covered with multi‐walled carbon nanotubes (MWCNT). The fusion of the surface‐covered particles forms a conductive MWCNT network in the composite, with a large number of inter‐MWCNT contacts. Membranes with a high specific electrical conductivity of up to 2.28 Sm−1 at a concentration of 3.0 wt% MWCNT are produced in an adapted sintering process. The sintering behavior of decorated particles depends on the coverage of the polymer particles with MWCNT.
“…Pristine polyetherimide (PEI Ultem 1000P) was supplied in powder form by Sabic Innovative Plastics (Pittsfield, USA). Polyetherimide has a high chemical and thermal resistance ( T g = 215 °C), good mechanical properties and is frequently used in membrane applications …”
A chemical‐free option to reduce membrane fouling is the use of electrical fields for membranes. To maximize the strength of the electric field in compact membrane module constructions, electrically conductive membranes are preferred to only conductive supports. Conductive, porous membranes are sintered from polyetherimide powder particles that are surface‐covered with multi‐walled carbon nanotubes (MWCNT). The fusion of the surface‐covered particles forms a conductive MWCNT network in the composite, with a large number of inter‐MWCNT contacts. Membranes with a high specific electrical conductivity of up to 2.28 Sm−1 at a concentration of 3.0 wt% MWCNT are produced in an adapted sintering process. The sintering behavior of decorated particles depends on the coverage of the polymer particles with MWCNT.
“…The membrane process requires low energy consumption and has characteristics of low-cost, compact space, and flexible design compared with other processes (Park et al, 2008). Compared to disk and tubular membranes, hollow fiber membranes possess much larger membrane area per unit volume allowing good gas permeation, and are easy to handle for large scale application and process operation (Sukitpaneenit and Chung, 2014;Kim et al, 2014). Previous literature clearly showed the benefits of using hollow fiber membrane contactors for gas separations (Albo et al, 2010;Albo et al, 2011; M A N U S C R I P T A C C E P T E D ACCEPTED MANUSCRIPT 3 the lower the selectivity; further, the upper bound is the goal in order to improve existing membranes (Robeson, 2008).…”
“…One vital issue in recent years has been the development of effective approaches for the capture and separation of SO2, which is an origin of air pollution and global warming [1,2]. As an alternative to solvent absorption, membrane separation has been considered an attractive method in systems including sour gas purification and concentration of SO2 [3]. Thus far, polymer membranes have been extensively investigated to remove SO2 and purify exhaust gases, and these have shown remarkable SO2 solubility and selectivity, which favors SO2 permeation [3].…”
Section: Introductionmentioning
confidence: 99%
“…As an alternative to solvent absorption, membrane separation has been considered an attractive method in systems including sour gas purification and concentration of SO2 [3]. Thus far, polymer membranes have been extensively investigated to remove SO2 and purify exhaust gases, and these have shown remarkable SO2 solubility and selectivity, which favors SO2 permeation [3]. A novel application is the O2/SO2 separation in the Iodine-Sulfur thermochemical water-splitting cycle (IS process) for hydrogen production [4].…”
In the present study, a BTESE-TEOS mixed precursor was proposed for control of the pore sizes of organosilica networks in organic-inorganic hybrid silica membranes. FT-IR spectrometry confirmed the formation of a partially cross-linked polysiloxane structure with hydrocarbon units in a BTESE-TEOS-derived silica network produced by the co-hydrolysis and condensation of BTESE with TEOS, which also showed an improved thermal stability. Single gas permeation measurements and normalized Knudsen-based permeance (NKP) established the order of the average membrane pore sizes as follows: BTESE > BTESE-TEOS > TEOS. The organosilica membranes derived from BTESE-TEOS exhibited a superior O2 permeance that was higher than 10 −8 mol m −2 s −1 Pa −1 with an O2/SO2 selectivity of 7.3, which indicated that the pore size control in organosilica networks using BTESE-TEOS as a precursor was effective for selective O2/SO2 separation. Moreover, the effective molecular size of SO2 permeates through organosilica membranes was discussed.
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