Adsorption of natural gas and its whole components on adsorbents

Adsorption of each component of natural gas on adsorbent prepared from petroleum coke was studied. At 25 °C and 3.5 MPa, adsorption capacity of the components of natural gas are as follows: C 3 H 8 , H 2 S(0.980) > CO 2 (0.691) > C 2 H 6 (0.160) > CH 4 (0.136) > N 2 (0.096) (g/g). For na...

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Veröffentlicht in:Adsorption : journal of the International Adsorption Society 2011-12, Vol.17 (6), p.949-954
Hauptverfasser: Li, Xingcun, Chen, Jinfu
Format: Artikel
Sprache:eng
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Zusammenfassung:Adsorption of each component of natural gas on adsorbent prepared from petroleum coke was studied. At 25 °C and 3.5 MPa, adsorption capacity of the components of natural gas are as follows: C 3 H 8 , H 2 S(0.980) > CO 2 (0.691) > C 2 H 6 (0.160) > CH 4 (0.136) > N 2 (0.096) (g/g). For natural gas, adsorption capacity is 145.2 (mL/mL) and delivery capacity is 105.7 (mL/mL). One equation between adsorption capacity and boiling point of adsorbed gas was firstly generalized. The adsorption capacity of different component like O 2 , N 2 , CH 4 , C 2 H 6 , CO 2 , H 2 S on adsorbents were predicted using the equation. The results fit well with the experimental data. The equation has significance in predicting the adsorption capacity for any component of natural gas. Charge-discharge tests were conducted 10 times, the result indicates that natural gas has significantly worse reversibility in adsorption and desorption in the adsorbent than that of CH 4 . The contents of the components after 10 charge-discharge show that the adsorption capacity drop of natural gas is due to the irreversible adsorption of heavy or polar components like C 3 H 8 , H 2 S.
ISSN:0929-5607
1572-8757
DOI:10.1007/s10450-011-9373-z