2012 ©
             EN, publication_detail
EN, publication_article
EN, publication_conference_work_name Simulation of High Temperature Air – Steam Biomass Gasification in a Downdraft Gasifier Using ASPEN PLUS 
EN, publication_conference_publish_date 27 December 2012 
EN, publication_conference_conference
     EN, publication_conference_conference_name 2012 International Conference on Energy Research and Power Engineering (ERPE’12) 
     EN, publication_conference_conference_institute taiyuan university of technology 
     EN, publication_conference_conference_place Jingang Hotel  
     EN, publication_conference_conference_province Taiyuan 
     EN, publication_conference_conference_from_date 19 October 2012 
     EN, publication_conference_conference_to_date 21 October 2012 
EN, publication_conference_proceeding
     EN, publication_conference_proceeding_volume_short 2013 
     EN, publication_conference_proceeding_issue_short 267 
     EN, publication_conference_proceeding_page_short 57 - 63 
     EN, publication_conference_proceeding_editor_short Trans Tech Publications  
     EN, publication_conference_abstract A comprehensive process model is developed for high temperature air – steam biomass gasification in a downdraft gasifier using the ASPEN PLUS simulator. The simulation results are compared with the experimental data obtained through pilot scale downdraft gasifier. In this study, the model is used to investigate the effects of gasifying agent preheating, equivalence ratio (ER), and steam/biomass (S/B) on producer gas composition, high heating value (HHV), and cold gas efficiency (CGE). Results indicate that H 2 and CO contents have increased when gasifying agent preheating is used, while gasifying agent preheating has no effect with H 2 and CO at high ER. At high level of S/B, the concentrations of H2 and CO are related with water-gas shift reaction in significant. HHV and CGE depend on the concentrations of H 2 and CO in producer gas, which can increase by preheated gasifying agent. However, gasifying agent preheating should apply with waste heat from the process because there is no additional cost of energy price.  
EN, publication_article_writer
537040008-7 Mr. WORAPOT NGAMCHOMPOO [EN, publication_article_main_writer]
Engineering Doctoral Degree

EN, publication_conference_evaluation มีผู้ประเมินอิสระ 
EN, publication_conference_level นานาชาติ 
EN, publication_conference_proceeding_style Full paper 
EN, publication_conference_presentation_style Oral 
EN, publication_conference_part_of_thesis EN, publication_conference_part_of_thesis_true 
EN, publication_conference_part_of_graduate EN, publication_conference_part_of_graduate_false 
EN, publication_conference_is_reward EN, publication_conference_is_reward_false 
EN, publication_attachment_file
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