Performance of the IGCC with distributed feeding of H2 in the gas turbine burner

被引:4
作者
Jordal, Kristin [1 ]
Anantharaman, Rahul [1 ]
Gruber, Andrea [1 ]
Peters, Thijs [2 ]
Henriksen, Partow P. [2 ]
Berstad, David [1 ]
Bredesen, Rune [2 ]
机构
[1] SINTEF Energy Res, NO-7465 Trondheim, Norway
[2] SINTEF Mat & Chem, NO-0314 Oslo, Norway
来源
12TH INTERNATIONAL CONFERENCE ON GREENHOUSE GAS CONTROL TECHNOLOGIES, GHGT-12 | 2014年 / 63卷
关键词
IGCC; distributed fuel injection; porous wall; H-2; membrane; DIRECT NUMERICAL-SIMULATION; FLAME STABILIZATION; CROSS-FLOW; JET; CONFIGURATION; PRESSURE;
D O I
10.1016/j.egypro.2014.11.219
中图分类号
O69 [应用化学];
学科分类号
081704 ;
摘要
A main hurdle for realizing the IGCC with CO2 capture is the lack of gas turbines capable of burning hydrogen in an environmental-friendly, yet energy-efficient manner. With currently proposed combustion schemes an efficiency penalty is caused by the preparation (separation and compression) of the inert diluent, i.e. nitrogen. Distributed Fuel Injection (DFI), where hydrogen is provided to the combustion air through a H-2-separating membrane or a porous wall, could be a means of avoiding both concentrated fuel point sources and N-2 dilution of the fuel. The paper presents two potential schemes for DFI: Scheme 1 with upstream H-2 separation and scheme 2 with integrated H-2 separation from the shifted syngas. First process simulation results for an IGCC with a reheat gas turbine yielded an IGCC efficiency increase of 0.7%-points with Scheme 1 and of 1.3%-points with scheme 2, compared to a reference case with nitrogen fuel dilution. This is mainly due to savings in N2 compression work but for scheme 2 also because the partial pressure difference of H-2 over the Pd membrane can be employed as driving force. The results should however be regarded as indicative only one of the reasons being that fuel injection pressure drop for DFI is yet unknown, and is presumably a trade-off between membrane/porous wall size. (C) 2014 The Authors. Published by Elsevier Ltd.
引用
收藏
页码:2037 / 2044
页数:8
相关论文
共 10 条
[1]  
[Anonymous], 2014, ENERGY TECHNOLOGY PE
[2]   Low-temperature CO2 capture technologies - Applications and potential [J].
Berstad, David ;
Anantharaman, Rahul ;
Neksa, Petter .
INTERNATIONAL JOURNAL OF REFRIGERATION-REVUE INTERNATIONALE DU FROID, 2013, 36 (05) :1403-1416
[3]  
Franco F., 2011, TEST CASES PRELIMINA
[4]   A direct numerical simulation study of turbulence and flame structure in transverse jets analysed in jet-trajectory based coordinates [J].
Grout, R. W. ;
Gruber, A. ;
Kolla, H. ;
Bremer, P. -T. ;
Bennett, J. C. ;
Gyulassy, A. ;
Chen, J. H. .
JOURNAL OF FLUID MECHANICS, 2012, 706 :351-383
[5]   Direct numerical simulation of flame stabilization downstream of a transverse fuel jet in cross-flow [J].
Grout, R. W. ;
Gruber, A. ;
Yoo, C. S. ;
Chen, J. H. .
PROCEEDINGS OF THE COMBUSTION INSTITUTE, 2011, 33 :1629-1637
[6]   Direct numerical simulation of laminar flame-wall interaction for a novel H2-selective membrane/injector configuration [J].
Gruber, Andrea ;
Salimath, Prashant S. ;
Chen, Jacqueline H. .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2014, 39 (11) :5906-5918
[7]   Mechanisms of flame stabilization and blowout in a reacting turbulent hydrogen jet in cross-flow [J].
Kolla, Hemanth ;
Grout, Ray W. ;
Gruber, Andrea ;
Chen, Jacqueline H. .
COMBUSTION AND FLAME, 2012, 159 (08) :2755-2766
[8]   Experimental investigation of a microchannel membrane configuration with a 1.4 μm Pd/Ag23 wt.% membrane-Effects of flow and pressure [J].
Mejdell, A. L. ;
Jondahl, M. ;
Peters, T. A. ;
Bredesen, R. ;
Venvik, H. J. .
JOURNAL OF MEMBRANE SCIENCE, 2009, 327 (1-2) :6-10
[9]   High pressure performance of thin Pd-23%Ag/stainless steel composite membranes in water gas shift gas mixtures; influence of dilution, mass transfer and surface effects on the hydrogen flux [J].
Peters, T. A. ;
Stange, M. ;
Klette, H. ;
Bredesen, R. .
JOURNAL OF MEMBRANE SCIENCE, 2008, 316 (1-2) :119-127
[10]   On the high pressure performance of thin supported Pd-23%Ag membranes-Evidence of ultrahigh hydrogen flux after air treatment [J].
Peters, T. A. ;
Stange, M. ;
Bredesen, R. .
JOURNAL OF MEMBRANE SCIENCE, 2011, 378 (1-2) :28-34