Coalbed methane (CBM) is a kind of important energy resources in the world. Liquefaction is a good option for recovery of CBM. Generally, CBM consists of a lot of nitrogen besides methane, which is usually required to be separated by adsorption before liquefaction, or by distillation after liquefaction. For the CBM adsorption-liquefaction processes, two novel processes are proposed, which integrate the two parts of adsorption and liquefaction together by utilizing the residue pressure of the waste nitrogen: the released nitrogen expanded directly to precool CBM or further compressed and then expanded to liquefy CBM. Taking the unit product liquefaction power consumption as the major index and the nitrogen content of CBM feed gas together with the residue pressure of waste nitrogen as variables, the system performance of these two integrated processes is studied and compared with that of the nitrogen expansion liquefaction process without integration. By simulation and calculation with HYSYS, it is confirmed that system power consumption can be reduced by both methods to utilize the residue pressure, and for CBM with high nitrogen content, the energy conservation effect is considerable; furthermore, it is better to use waste nitrogen to precool CBM than to liquefy it.

1.
Abraham
,
K.
, 2006, “
Coalbed Methane Activity Expands Further in North America: CBM Production and Reserves Growth Is Slower, but Drilling Remains Frenetic
,”
World Oil
0043-8790,
227
(
8
), pp.
61
62
.
2.
Yu
,
H. G.
,
Zhou
,
G. Z.
,
Fan
,
W. T.
, and
Ye
,
J. P.
, 2007, “
Predicted CO2 Enhanced Coalbed Methane Recovery and CO2 Sequestration in China
,”
Int. J. Coal Geol.
0166-5162,
71
(
2–3
), pp.
345
357
.
3.
Bibler
,
C. J.
,
Marshall
,
J. S.
, and
Pilcher
,
R. C.
, 1998, “
Status of Worldwide Coal Mine Methane Emissions and Use
,”
Int. J. Coal Geol.
0166-5162,
35
, pp.
283
310
.
4.
Lin
,
W. S.
,
Gu
,
M.
, and
Gu
,
A. Z.
, 2007, “
Analysis of Coal Bed Methane Enrichment and Liquefaction Processes in China
,”
Proceedings of the 15th International Conference and Exhibition on Liquefied Natural Gas
, Barcelona, Spain.
5.
Cavenati
,
S.
,
Grande
,
C. A.
, and
Rodrigues
,
A. E.
, 2006, “
Separation of CH4/CO2/N2 Mixtures by Layered Pressure Swing Adsorption for Upgrade of Natural Gas
,”
Chem. Eng. Sci.
0009-2509,
61
, pp.
3893
3906
.
6.
Xu
,
L. J.
,
Xian
,
X. F.
, and
Yang
,
M. L.
, 2005, “
Basic Research on CBM Concentration and Purification
,”
China Coalbed Methane
,
2
(
4
), pp.
11
15
.
7.
Haselden
,
G. G.
, 1979, “
Developments in Gas Liquefaction and Separation
,”
Int. J. Refrig.
0140-7007,
2
(
6
), pp.
207
210
.
8.
Terry
,
L.
, 1998, “
Comparison of Liquefaction Process
,”
LNG Journal
, (
3
), pp.
28
33
.
9.
Kapoor
,
A.
, and
Yang
,
R. T.
, 1988, “
Optimization of a Process Swing Adsorption Cycle
,”
Ind. Eng. Chem. Res.
0888-5885,
27
, pp.
204
206
.
10.
Liu
,
K. W.
,
Gu
,
M.
, and
Xian
,
X. F.
, 2007, “
Research Progress in Concentration of Methane from CH4/N2 by PSA
,”
Modern Chemical Industry
,
27
(
12
), pp.
15
18
.
11.
Finn
,
A. J.
, and
Johnson
,
G. L.
, 1999, “
Tomlinson T R. Development in Natural Gas Liquefaction
,”
Hydrocarbon Process.
0887-0284,
78
(
4
), pp.
47
59
.
12.
Gao
,
T.
,
Lin
,
W. S.
,
Gu
,
A. Z.
, and
Gu
,
M.
, 2008, “
Effects of Nitrogen Content in Coalbed Methane on Nitrogen Expansion Liquefaction Process
,”
Proceedings of the International Conference on Cryogenics and Refrigeration
,
Shanghai, China
.
13.
Remeljej
,
C. W.
, and
Hoadley
,
A. F. A.
, 2006, “
An Exergy Analysis of Small-Scale Liquefied Natural Gas (LNG) Liquefaction Processes
,”
Energy
0360-5442,
31
, pp.
2005
2019
.
14.
Yang
,
X.
,
Gu
,
A.
,
Xi
,
W.
,
Lu
,
X.
, and
Gao
,
T.
, 2008, “
Comparison Study on Small-Scale LNG Plants in China
,”
Proceedings of the AIChE Spring National Meeting
,
New Orleans, LA
.
You do not currently have access to this content.