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Thermodynamic evaluation of processe...

Kaini, Bhanu.

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Thermodynamic evaluation of processes for hydrogen production from carbonaceous fuel.

Record Type:	Language materials, printed : Monograph/item
Title/Author:	Thermodynamic evaluation of processes for hydrogen production from carbonaceous fuel./
Author:	Kaini, Bhanu.
Description:	143 p.
Notes:	Source: Masters Abstracts International, Volume: 49-02, page: 1212.
Contained By:	Masters Abstracts International49-02.
Subject:	Alternative Energy. -
Online resource:	http://pqdd.sinica.edu.tw/twdaoapp/servlet/advanced?query=1482635
ISBN:	9781124287058

Thermodynamic evaluation of processes for hydrogen production from carbonaceous fuel.
Kaini, Bhanu.

Thermodynamic evaluation of processes for hydrogen production from carbonaceous fuel. - 143 p.

Source: Masters Abstracts International, Volume: 49-02, page: 1212.

Thesis (M.S.)--Southern Illinois University at Carbondale, 2010.

This research work presents the thermodynamic analysis of hydrogen production using steam methane reforming process at different conditions. The model is developed using HSC 4.1 software and spreadsheet. Methane is chosen to represent the carbonaceous fuel and steam methane reforming process (once through and cyclic) for hydrogen production is analyzed based on 1st law and 2nd law of thermodynamics i.e., energetic and exergetic efficiencies. The mass, energy and exergy analysis of each step is done. The optimal condition for production of maximum hydrogen is found using CO 2 removal agent and O2 transfer compound. The efficiency is calculated as a function of steam content, temperature and amount of CO 2 removal agent and O2 transfer compound. The pressure is kept constant at one atmosphere. Operating temperature, CaO loading, Fe 2O3 loading and H2O content is determined from the once through process. It is found that the maximum H2 production is with the cyclic process. Maximum H2 produced in cyclic process with CaO & Fe2O3 loadings is 99.2%. Also CO2 content is comparatively lower in cyclic process. Theoretical efficiencies can be used to compare with the available data which will help to minimize the losses in the process. The results can be used as a baseline for the design of H2 production technology. The main aim of this research is to develop a thermodynamic protocol for evaluating hydrogen production processes.

ISBN: 9781124287058Subjects--Topical Terms:

1035473
Alternative Energy.

Thermodynamic evaluation of processes for hydrogen production from carbonaceous fuel.
LDR:02504nam 2200325 4500 001 1396364
005 20110603090813.5
008 130515s2010 ||||||||||||||||| ||eng d
020 $a 9781124287058
035 $a (UMI)AAI1482635
035 $a AAI1482635
040 $a UMI $c UMI
100 1 $a Kaini, Bhanu. $3 1675146
245 1 0 $a Thermodynamic evaluation of processes for hydrogen production from carbonaceous fuel.
300 $a 143 p.
500 $a Source: Masters Abstracts International, Volume: 49-02, page: 1212.
500 $a Adviser: Kanchan Mondal.
502 $a Thesis (M.S.)--Southern Illinois University at Carbondale, 2010.
520 $a This research work presents the thermodynamic analysis of hydrogen production using steam methane reforming process at different conditions. The model is developed using HSC 4.1 software and spreadsheet. Methane is chosen to represent the carbonaceous fuel and steam methane reforming process (once through and cyclic) for hydrogen production is analyzed based on 1st law and 2nd law of thermodynamics i.e., energetic and exergetic efficiencies. The mass, energy and exergy analysis of each step is done. The optimal condition for production of maximum hydrogen is found using CO 2 removal agent and O2 transfer compound. The efficiency is calculated as a function of steam content, temperature and amount of CO 2 removal agent and O2 transfer compound. The pressure is kept constant at one atmosphere. Operating temperature, CaO loading, Fe 2O3 loading and H2O content is determined from the once through process. It is found that the maximum H2 production is with the cyclic process. Maximum H2 produced in cyclic process with CaO & Fe2O3 loadings is 99.2%. Also CO2 content is comparatively lower in cyclic process. Theoretical efficiencies can be used to compare with the available data which will help to minimize the losses in the process. The results can be used as a baseline for the design of H2 production technology. The main aim of this research is to develop a thermodynamic protocol for evaluating hydrogen production processes.
590 $a School code: 0209.
650 4 $a Alternative Energy. $3 1035473
650 4 $a Chemistry, Inorganic. $3 517253
650 4 $a Engineering, Chemical. $3 1018531
690 $a 0363
690 $a 0488
690 $a 0542
710 2 $a Southern Illinois University at Carbondale. $b Mechanical Engineering. $3 1035345
773 0 $t Masters Abstracts International $g 49-02.
790 1 0 $a Mondal, Kanchan, $e advisor
790 1 0 $a Mondal, Kanchan $e committee member
790 1 0 $a Wiltowski, Tomasz $e committee member
790 1 0 $a Mathias, James $e committee member
790 $a 0209
791 $a M.S.
792 $a 2010
856 4 0 $u http://pqdd.sinica.edu.tw/twdaoapp/servlet/advanced?query=1482635