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72篇 您的检索式:作者名="ASSABUMRUNGRAT"
    题名 作者 年代 出处 被引量
1Hybrid Process of Reactive Distillation and Pervaporation for the Production of Tert-amyl Ethyl Ether显示文摘在这研究,化学反应和分离同时在发生的反应蒸馏柱被申请从乙醇(EtOH ) 和 tert 戊基酒精(TAA ) 的 tert 戊基乙醇醚(TAEE ) 的合成。Pervaporation,一种有效的膜分离技术,随为提高 TAEE 的效率的反应蒸馏是综合的生产。一个 pervaporation 单位的一个自定义 Fortran 子程序被开发,允许在白杨正模拟器的反应蒸馏和 pervaporation 的混杂流程的设计和模拟。如此的混杂流程的表演被分析,结果显示 pervaporation 增加的反应蒸馏 witfi 的集成 TAA 和 TAEE 产品的纯净的变换,与常规反应蒸馏相比。Amornchai Arpornwichanop Ukrit Sahapatsombud Yaneeporn Patcharavorachot Suttichai Assabumrungrat 2008Chinese Journal of Chemical Engineering2008,16,1:3
2Effect of membrane module arrangement of gas-liquid membrane contacting process on CO2 absorption performance: A modeling study显示文摘Boributh S Assabumrungrat S Laosiripojana N 2011Journal of Membrane Science2011,372,12:1
3Cleaner gasoline production by using glycerol as fuel extender显示文摘Worapon Kiatkittipong Sirima Suwanmanee Navadol Laosiripojana Piyasan Praserthdam Suttichai Assabumrungrat 2009Fuel Processing Technology2009,,5:1
4Catalytic steam reforming of ethanol over high surface area CeO2: The role of CeO2 as an intemal pre-refoming catalyst显示文摘Laosiripojana N Assabumrungrat S 2006Applied Catalysis B: Environmental2006,66,12:1
5Surface segregation of siloxane containing component in polysiloxane-block-polyimide and s-BPDA/ODA polyimide blends 显示文摘Sarawut Rimdusit Wanpen Benjapan Suttichai Assabumrungrat 2007Polym Eng Sci2007,47,4:1
6Synthesis gas production from dry reforming of methane over CeO2 doped Ni/Al2O3:Influence of the doping ceria on the resistance toward carbon formation 显示文摘Laosiripojana N Sutthisripok W Assabumrungrat S 2005Chemical Engineering Journal2005,112,13:1
7显示文摘Laosiripojana N Assabumrungrat S 2006Applied Catalysis B:Environmental2006,66,12:1
8Role of Sn and K on hydrogen spillover on Pt/γ-Al2O3 catalyst显示文摘 Choungchaisukasam P Assabumrungrat S 2001Journal of the Chinese Institute of Chemical Engineers2001,32,2:1
9Catalytic dry refor- ming of methane over high surface area ceria显示文摘Laosiripojana N Assabumrungrat S 2005Applied Catalysis B : Environmental2005,60,1:1
10Multiphase parallel flow stabilization in curved microchannel 显示文摘Kositanont C Putivisutisak S Tagawa T Yamada H Assabumrungrat S 2014Chemical Engineering Journal2014,253,:1
11Hydrogen production from steam and autothermal reforming of LPG over high surface area ceria显示文摘Laosiripojana N Assabumrungrat S 2006Journal of Power Sources2006,158,2:1
12Self-Etherification Process for Cleaner Fuel Production显示文摘Worapon Kiatkittipong Khamron Yoothongkham Choowong Chaisuk Piyasan Praserthdam Shigeo Goto Suttichai Assabumrungrat 2009Catalysis Letters (-)2009,,1:1
13Comparison of carbon formation boundary in different modes of solid oxide fuel cells fueled by methane 显示文摘Sangtongkitcharoen W Assabumrungrat S Pavarajarn V 2005Journal of Power sources2005,142,1:1
14Modeling of IT-SOFC with indirect internal reforming operation fueled by methane: Effect of oxygen adding as autothermal reforming显示文摘P. Dokmaingam J.T.S. Irvine S. Assabumrungrat S. Charojrochkul N. Laosiripojana 2010International Journal of Hydrogen Energy2010,,24:1
15Simulations of sorbent regeneration in a circulating fluidized bed system for sorption enhanced steam reforming with dolomite显示文摘In this work,the sorption enhanced steam reforming (SESR) method was developed for improved hydrogen (H2) production,and the drawbacks of conventional steam reforming processes on H2 yield and purity were overcome.However,the SESR process is discontinuous and requires regeneration after sorbent saturation with CO2.The circulating fluidized bed reactor (CFBR) system has previously been proposed for continuous H2 production,with both reforming and sorbent regeneration occurring simultaneously.The main aim of this work was to determine the feasibility and performance of SESR with a proper design and conditions in conjunction with the CFBR system.The reforming riser and bubbling bed regenerator are studied separately but related to each other.Two-dimensional transient models using the Euler-Euler approach and kinetic theory of granular flow were used for fluid dynamic simulations combined with the decarbonation kinetics of dolomite,to investigate a conceptual regenerator system and determine its key conditions.A mixture of the Ni-based catalyst and dolomite from the risers was injected with a flux of 200 kg/(m2 s) and a catalyst to sorbent ratio of 2.54 kg/kg.A double-stage bubbling bed regenerator system was designed with 1.2 m width,0.8 m bed height,a gas inlet velocity of 0.2 m/s and solid preheating at 950 ℃.The used dolomite was regenerated with an assumed CaO conversion of 3%;the almost fresh dolomite was then released with good mixing of the catalyst and sorbent.Kiattikhoon Phuakpunk Benjapon Chalermsinsuwan Sompong Putivisutisak Suttichai Assabumrungrat 2020Particuology2020,18,3:1
16Effect of membrane module arrangement of gas-liquid membrane contacting process on CO2 absorption performance:A modeling study显示文摘BORIBUTH S ASSABUMRUNGRAT S LAOSIRIPOJANA N 0,,1:1
17Hydrogen production from steam and autothermal reforming of LPG over high surface area ceria显示文摘Laosiripojana N Assabumrungrat S 0,,:1
18Modeling of SOFC with indirect internal reforming operation: Comparison of conventional packed-bed and catalytic coated-wall internal reformer显示文摘P. Dokamaingam S. Assabumrungrat A. Soottitantawat I. Sramala N. Laosiripojana 2008International Journal of Hydrogen Energy2008,,1:1
19Catalytic steam reforming of ethane and propane over CeO2-doped Ni/A1203 at SOFC temperature: Improvement of resistance toward carbon formation by the redox property of doping CeO2 显示文摘LAOSIRIPOJANA N SANGTONGKITCHAROEN W ASSABUMRUNGRAT S 2006Fuel2006,85,3:1
20Catalytic steam reforming of ethanol over high surface area CeO2:The role of CeO2 as an internal pre-reforming catalyst显示文摘Laosiripojana N Assabumrungrat S 2006Applied Catalysis B:Environmental2006,66,12:1
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