TY - JOUR
T1 - A micro-fuel processor with trench-refilled thick silicon dioxide for thermal isolation fabricated by water-immersion contact photolithography
AU - Chang, Kuei Sung
AU - Tanaka, Shuji
AU - Esashi, Masayoshi
PY - 2005/9/1
Y1 - 2005/9/1
N2 - This paper presents a micro-fuel processor to produce hydrogen for micro-fuel cells. The micro-fuel processor has an original design for a heat source and a reforming chamber to improve thermal efficiency. To improve the mechanical strength as well as to maintain the effectiveness of thermal isolation, the reaction area is suspended by trench-refilled thick SiO 2. When the reaction area was heated at 200°C, the outer silicon frame was at 100°C, confirming the effectiveness of thermal isolation. To fabricate the trench-refilled thick SiO2 using a contact aligner, water-immersion contact photolithography was used and successfully demonstrated to produce fine patterns with line/space of 2 νm/1 νm (a pitch of 3 νm). The highest temperature could be controlled by tuning the equivalent ratio of H2-air mixture fed into the catalytic micro-combustor. The conversion rate of methanol to hydrogen by steam reforming was lower than 1% due to uneven temperature distribution and channeling effect.
AB - This paper presents a micro-fuel processor to produce hydrogen for micro-fuel cells. The micro-fuel processor has an original design for a heat source and a reforming chamber to improve thermal efficiency. To improve the mechanical strength as well as to maintain the effectiveness of thermal isolation, the reaction area is suspended by trench-refilled thick SiO 2. When the reaction area was heated at 200°C, the outer silicon frame was at 100°C, confirming the effectiveness of thermal isolation. To fabricate the trench-refilled thick SiO2 using a contact aligner, water-immersion contact photolithography was used and successfully demonstrated to produce fine patterns with line/space of 2 νm/1 νm (a pitch of 3 νm). The highest temperature could be controlled by tuning the equivalent ratio of H2-air mixture fed into the catalytic micro-combustor. The conversion rate of methanol to hydrogen by steam reforming was lower than 1% due to uneven temperature distribution and channeling effect.
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U2 - 10.1088/0960-1317/15/9/S01
DO - 10.1088/0960-1317/15/9/S01
M3 - Article
AN - SCOPUS:23944515375
SN - 0960-1317
VL - 15
SP - S171-S178
JO - Journal of Micromechanics and Microengineering
JF - Journal of Micromechanics and Microengineering
IS - 9
ER -