Development and efficient energy utilization of biomass energy based system for renewable hydrogen production and storage

2021 ◽  
pp. 1-27
Author(s):  
Haris Ishaq ◽  
Ibrahim Dincer

Abstract The increasing environmental limits and carbon emissions taxes are making is substantial to develop the efficient systems offering the effective energy utilization. This study proposed a new biomass gasification assisted configuration for renewable hydrogen production system offering efficient energy utilization. A multi-effect desalination system is employed for water desalination which is converted to the steam and fed to the entrained flow gasifier. The integrated heat recovery steam generator recovers the additional heat from the syngas to generate steam using fresh water from the desalination unit. The produced hydrogen is supplied to the multistage compression unit that stores hydrogen at high pressure. Industrial Aspen Plus software V9 version is employed for the simulation under the RK-SOAVE property method. The production of hydrogen before water gas shift reactor is 129.5 mol/s and after the water gas shift reactor is found to be 171 mol/s. The thermodynamic performance of the biomass energy-assisted system is determined through overall energetic and exergetic efficiencies that are revealed to be 40.86% and 38.63%. Numerous sensitivity studies are performance to explore the performance of the designed system and presented and discussed.

2013 ◽  
Vol 15 (29) ◽  
pp. 12004 ◽  
Author(s):  
José A. Rodriguez ◽  
Jonathan C. Hanson ◽  
Dario Stacchiola ◽  
Sanjaya D. Senanayake

Author(s):  
Giovanni Pisani ◽  
Alberto Zerbinato ◽  
Carlo Tregambe ◽  
Ernesto Benini

This paper describes technological of a fuel processor for hydrogen production able to convert 10 cubic meters of methane per hour. This device has been developed to feed hydrogen CHP suitable for the most common residential applications. The measured conversion efficiencies are extremely high: after the steam reformer the results are 76%H2; 18%CO2; 0,5%CH4; 5%CO; but the carbon monoxide is totally reduced throughout the water gas shift and the partial oxidation which contemporarily increase the hydrogen to over 77%. According to these results, this fuel processor is one of the first middle sized reformer to achieve, at comparable costs per cubic meter, conversion performance that were normally obtained only by industrial reforming plants.


2008 ◽  
Vol 20 (6) ◽  
pp. 064237 ◽  
Author(s):  
S M Opalka ◽  
T H Vanderspurt ◽  
R Radhakrishnan ◽  
Y She ◽  
R R Willigan

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