2000
DOI: 10.1021/ja0013071
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Dendrimer Membranes:  A CO2-Selective Molecular Gate

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Cited by 147 publications
(106 citation statements)
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“…Some liquid membranes using porous membranes containing dendrimers in the pores were reported. [34][35][36] A dendrimer membrane was prepared by the immersion of porous a hydrophilized polyvinylidene fluoride flat membrane (porosity 0.7; pore size 0.1 mm; thickness 100 mm; tortuosity 2.58; Millipore) into pure G0 PAMAM dendrimer or glycerol solution of G0 PAMAM dendrimer. 34,35 The CO 2 /N 2 permeation performance through the liquid membranes was measured under various humidity.…”
Section: Dendrimers Supported By Membranesmentioning
confidence: 99%
See 1 more Smart Citation
“…Some liquid membranes using porous membranes containing dendrimers in the pores were reported. [34][35][36] A dendrimer membrane was prepared by the immersion of porous a hydrophilized polyvinylidene fluoride flat membrane (porosity 0.7; pore size 0.1 mm; thickness 100 mm; tortuosity 2.58; Millipore) into pure G0 PAMAM dendrimer or glycerol solution of G0 PAMAM dendrimer. 34,35 The CO 2 /N 2 permeation performance through the liquid membranes was measured under various humidity.…”
Section: Dendrimers Supported By Membranesmentioning
confidence: 99%
“…[34][35][36] A dendrimer membrane was prepared by the immersion of porous a hydrophilized polyvinylidene fluoride flat membrane (porosity 0.7; pore size 0.1 mm; thickness 100 mm; tortuosity 2.58; Millipore) into pure G0 PAMAM dendrimer or glycerol solution of G0 PAMAM dendrimer. 34,35 The CO 2 /N 2 permeation performance through the liquid membranes was measured under various humidity. The separation factor CO 2 /N 2 was almost 19000 at a low CO 2 partial pres-sure (Áp CO 2 ¼ 0:36 cmHg) under the completely humidified condition, while it was around 700 at the higher Áp CO 2 (> 30 cmHg).…”
Section: Dendrimers Supported By Membranesmentioning
confidence: 99%
“…It was suggested that the permeance of CO 2 could be increased by increasing CO 2 carrier solubility in the ILM liquid and by preparing ILMs with thinner hydrophilic supports. In another study by the same authors [202,203], they used polyamidoamine (PAMAM) generation 0 dendrimers having ethylenediamine as the CO 2 carrier in porous hydrophilic polyvinyldine fluoride supported ILM. Dendrimer immobilized liquid membranes containing a high concentration of primary and tertiary amine provided a facilitated CO 2 transport and also nearly eliminated the other gases.…”
Section: Facilitated Transport Membranesmentioning
confidence: 99%
“…Works on gas separation applications using membranes composite with PAMAM dendrimer are limited. However, PAMAM dendrimer immobilized liquid membranes are reported by distinguished researchers [8,9]. In this research paper, we have been emphasized on gas separation behaviour of PAMAM dendrimer (G-0,G-1,G-2,G-3,G-4) composite solid membranes due to its stability and regeneration.The dendrimer composite membranes selectively permeated CO 2 because of the reaction between -NH 2 and CO 2 producing a carbamate ion and a protonated base [8].…”
Section: Introductionmentioning
confidence: 96%
“…In this research paper, we have been emphasized on gas separation behaviour of PAMAM dendrimer (G-0,G-1,G-2,G-3,G-4) composite solid membranes due to its stability and regeneration.The dendrimer composite membranes selectively permeated CO 2 because of the reaction between -NH 2 and CO 2 producing a carbamate ion and a protonated base [8]. Sarma et al [9] reported the performance of Poly (amidoamine) (PAMAM G-0 ) dendrimer and ionic liquid composite membranes which provide a challenging way for CO 2 separation performances. Belmabkhout et al [10] reported that amine bearing pore expanded MCM-41 (Mobil Composition of Matter, No 41) Silica can be used for gas separation applications for CO 2 /CH 4 .…”
Section: Introductionmentioning
confidence: 99%