2013
DOI: 10.1016/j.memsci.2012.12.001
|View full text |Cite
|
Sign up to set email alerts
|

Post-combustion CO2 capture using super-hydrophobic, polyether ether ketone, hollow fiber membrane contactors

Help me understand this report

Search citation statements

Order By: Relevance

Paper Sections

Select...
1
1
1
1

Citation Types

0
34
0

Year Published

2013
2013
2021
2021

Publication Types

Select...
3
3
1

Relationship

1
6

Authors

Journals

citations
Cited by 59 publications
(35 citation statements)
references
References 13 publications
0
34
0
Order By: Relevance
“…For example, adding piperazine into the amine solution decreases the membrane degradation due to polyolefin membrane stabilization . Also, modification of the polymer surface by depositing a thin superhydrophobic coating may improve the hydrophobicity of the membrane and decrease the membrane wetting, leading to a stable performance over time …”
Section: Membrane Technology In Co2 Capturementioning
confidence: 99%
“…For example, adding piperazine into the amine solution decreases the membrane degradation due to polyolefin membrane stabilization . Also, modification of the polymer surface by depositing a thin superhydrophobic coating may improve the hydrophobicity of the membrane and decrease the membrane wetting, leading to a stable performance over time …”
Section: Membrane Technology In Co2 Capturementioning
confidence: 99%
“…Assuming a constant price of 50 € m -2 for all investigated membranes, the economic performance strongly correlates with the membrane area. The determination of the required membrane area for the MC process is performed in accordance to Li et al (2013). 1 and 14 in Figure 3) are illustrated in Figure 4.…”
Section: Process Evaluationmentioning
confidence: 99%
“…Current state-of-the-art for CO 2 removal is the reactive absorption using aqueous amine solutions (e.g. MC provide a constant volume-specific interfacial area which can be orders of magnitude higher than for conventional equipment (Li et al, 2013). Due to the loss in process efficiency, caused by the high energy demand for the solvent regeneration, CO 2 removal is practically not used at large scale industrial application.…”
Section: Introductionmentioning
confidence: 99%
“…Separation of CO 2 Gas Technology Institute (GTI) and PoroGen Corporation are jointly developing a novel hybrid membraneabsorption process for pre-and post-combustion CO 2 capture (Carbo-Lock TM process) [7]. The novel CarboLock TM process combines beneficial features of both absorption and membrane technologies for cost-effective separation and capture of CO 2 from various emission sources.…”
Section: Gti-porogen Carbo-lock Technology For Thementioning
confidence: 99%
“…The sour gas feed enters Water Contactor, where it is contacted with a stream of circulating water. At the pressure, temperature, and water content of the syngas, the circulating water will have a steady-state content of NH 3 and (Figure 4(a)) uses Case A (UCSRP-HP) with GTI/PoroGen's CarboLock membrane contactor [7,14] (Figure 4(b)) is the published SRI study [8] that uses LANL/SRI's PBI membrane for hydrogen/acid gas separation and purification of the CO 2 stream by a single-stage Selexol TM /Claus/Tail Gas process for sulfur recovery. The syngas from the Water-Gas Shift (WGS) is first processed for CO 2 (Figure 4(b)) uses Case C and incorporates UCSRP-HP for multi-contaminant removal downstream of LANL/SRI's PBI membrane rather than the Selexol TM /Claus/Tail Gas trains.…”
Section: Economic Potential For the Ucsrp-hp Technology In Coal Gasifmentioning
confidence: 99%