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...
Gespeichert in:
Veröffentlicht in: | Adsorption : journal of the International Adsorption Society 2011-12, Vol.17 (6), p.949-954 |
---|---|
Hauptverfasser: | , |
Format: | Artikel |
Sprache: | eng |
Schlagworte: | |
Online-Zugang: | Volltext |
Tags: |
Tag hinzufügen
Keine Tags, Fügen Sie den ersten Tag hinzu!
|
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 |