2009
DOI: 10.1016/j.ces.2009.05.024
|View full text |Cite
|
Sign up to set email alerts
|

Adsorption of carbon dioxide, ethane, and methane on titanosilicate type molecular sieves

Help me understand this report

Search citation statements

Order By: Relevance

Paper Sections

Select...
3
1
1

Citation Types

3
29
0
1

Year Published

2011
2011
2024
2024

Publication Types

Select...
8

Relationship

0
8

Authors

Journals

citations
Cited by 70 publications
(37 citation statements)
references
References 11 publications
3
29
0
1
Order By: Relevance
“…The CO 2 adsorption capacity of UZAR-S2 is about five times higher than that of original AM-4, because the delaminated product has a higher specific surface area available than the layered precursor. Although the maximum capacity of UZAR-S2 is lower than the value of 2 mmol CO 2 / g obtained for the microporous titanosilicate ETS-10, [33] which possesses an important internal surface area as well as a larger pore volume, the maximum capacity is in the same range as that of Ti-umbite (about 0.2 mmol CO 2 /g). [34] Figure 10.…”
Section: Samplementioning
confidence: 89%
“…The CO 2 adsorption capacity of UZAR-S2 is about five times higher than that of original AM-4, because the delaminated product has a higher specific surface area available than the layered precursor. Although the maximum capacity of UZAR-S2 is lower than the value of 2 mmol CO 2 / g obtained for the microporous titanosilicate ETS-10, [33] which possesses an important internal surface area as well as a larger pore volume, the maximum capacity is in the same range as that of Ti-umbite (about 0.2 mmol CO 2 /g). [34] Figure 10.…”
Section: Samplementioning
confidence: 89%
“…Previous experimental adsorption [13,15,19] and vibrational [42,43] studies disclosed that the Na2 cations, which are less coordinated than cations of the type Na1, Na3, and Na4, would be the primary sites for interaction with guest molecules in the 12-MR channels of ETS-10, with concomitant formation of sorbate-Na adducts [21] or -complexes [22], depending on the adsorbate. The experimental isosteric heats for methane adsorption in ETS-10 reported in the literature are included in the interval from -20.8 to -23.3 kJ·mol -1 , and were deduced from the fit of Toth, unilan or virial three constants models to the adsorption data obtained with volumetric systems in temperature ranges around T=298.15 K [18,41].…”
Section: Resultsmentioning
confidence: 99%
“…In fact, AlBaghli et al [15] and Anson et al [16]suggested ETS-10 as an adsorbent for hydrocarbon separation processes. Furthermore, Al-Baghli et al [18]reported adsorption isotherms and isosteric heats of adsorption for methane, ethane and ethene in ETS-10, Anson et al [19]used ETS-10 for ethene separation from ethane by an adsorptive separation technique, while Avila et al [20] evidenced the better capability of ETS-10 to separate ethane from a methane/ethane mixture.…”
Section: Introductionmentioning
confidence: 99%
“…These target different applications, such as ion exchange [20][21][22][23][24], adsorption [25][26][27][28], membrane separation [29][30][31][32], pillaring templating [33,34] and oxidation catalysis [35][36][37][38].…”
Section: Introductionmentioning
confidence: 99%