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Thermal behavior and hydrogen production of methanol steam reforming and autothermal reforming with spiral preheating

The present study aims to investigate the thermal behavior and hydrogen production characteristics from methanol steam reforming (MSR) and autothermal reforming (ATR) under the effects of a Cu-Zn-based catalyst and spiral preheating. Two different reaction temperatures of 250 and 300 °C are taken in...

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Published in:International journal of hydrogen energy 2011-03, Vol.36 (5), p.3397-3408
Main Authors: Chen, Wei-Hsin, Syu, Yu-Jhih
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description The present study aims to investigate the thermal behavior and hydrogen production characteristics from methanol steam reforming (MSR) and autothermal reforming (ATR) under the effects of a Cu-Zn-based catalyst and spiral preheating. Two different reaction temperatures of 250 and 300 °C are taken into account. Meanwhile, the O/C ratio (i.e. the molar ratio between O 2 and methanol) and S/C ratio (i.e. the molar ratio between steam and methanol) are controlled in the ranges of 0–0.5 and 1–2, respectively. The condition of O/C = 0 represents the reaction of MSR. By monitoring the supplied power into the reactor with a fixed gas hourly space velocity (GHSV) of 72,000 h −1, the experimental results indicate that an exothermic reaction from ATR can be attained once the O/C ratio is as high as 0.125. Increasing O/C ratio causes more heat released from the reaction, this results in the decrease in the frequency of supplied power, especially at O/C = 0.5. It is noted that the concentration of CO in the product gas is quite low compared to that of CO 2. An increase in O/C ratio abates the concentration of H 2 from the consumption of per mol methanol; however, the H 2 yield in terms of thermodynamic analysis is increased. On account of the utilization of spiral preheating on the reactants, within the investigated operating conditions the methanol conversion and hydrogen yield were always higher than 95 and 90%, respectively. A comparison suggests that the methanol conversion from ATR of methanol with spiral preheating is superior to those of other studies. ► Thermal behavior of methanol steam reforming (MSR) and autothermal reforming (ATR) is studied. ► Hydrogen production characteristics from MSR and ATR are investigated. ► The effect of spiral preheating on MSR and ATR is explored. ► An exothermic reaction from ATR can be attained once the O/C ratio is as high as 0.125. ► The results suggest that the methanol conversion from ATR of methanol with spiral preheating is superior to those of other studies.
doi_str_mv 10.1016/j.ijhydene.2010.12.055
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Two different reaction temperatures of 250 and 300 °C are taken into account. Meanwhile, the O/C ratio (i.e. the molar ratio between O 2 and methanol) and S/C ratio (i.e. the molar ratio between steam and methanol) are controlled in the ranges of 0–0.5 and 1–2, respectively. The condition of O/C = 0 represents the reaction of MSR. By monitoring the supplied power into the reactor with a fixed gas hourly space velocity (GHSV) of 72,000 h −1, the experimental results indicate that an exothermic reaction from ATR can be attained once the O/C ratio is as high as 0.125. Increasing O/C ratio causes more heat released from the reaction, this results in the decrease in the frequency of supplied power, especially at O/C = 0.5. It is noted that the concentration of CO in the product gas is quite low compared to that of CO 2. An increase in O/C ratio abates the concentration of H 2 from the consumption of per mol methanol; however, the H 2 yield in terms of thermodynamic analysis is increased. On account of the utilization of spiral preheating on the reactants, within the investigated operating conditions the methanol conversion and hydrogen yield were always higher than 95 and 90%, respectively. A comparison suggests that the methanol conversion from ATR of methanol with spiral preheating is superior to those of other studies. ► Thermal behavior of methanol steam reforming (MSR) and autothermal reforming (ATR) is studied. ► Hydrogen production characteristics from MSR and ATR are investigated. ► The effect of spiral preheating on MSR and ATR is explored. ► An exothermic reaction from ATR can be attained once the O/C ratio is as high as 0.125. ► The results suggest that the methanol conversion from ATR of methanol with spiral preheating is superior to those of other studies.</description><identifier>ISSN: 0360-3199</identifier><identifier>EISSN: 1879-3487</identifier><identifier>DOI: 10.1016/j.ijhydene.2010.12.055</identifier><identifier>CODEN: IJHEDX</identifier><language>eng</language><publisher>Kidlington: Elsevier Ltd</publisher><subject>Alternative fuels. 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Two different reaction temperatures of 250 and 300 °C are taken into account. Meanwhile, the O/C ratio (i.e. the molar ratio between O 2 and methanol) and S/C ratio (i.e. the molar ratio between steam and methanol) are controlled in the ranges of 0–0.5 and 1–2, respectively. The condition of O/C = 0 represents the reaction of MSR. By monitoring the supplied power into the reactor with a fixed gas hourly space velocity (GHSV) of 72,000 h −1, the experimental results indicate that an exothermic reaction from ATR can be attained once the O/C ratio is as high as 0.125. Increasing O/C ratio causes more heat released from the reaction, this results in the decrease in the frequency of supplied power, especially at O/C = 0.5. It is noted that the concentration of CO in the product gas is quite low compared to that of CO 2. An increase in O/C ratio abates the concentration of H 2 from the consumption of per mol methanol; however, the H 2 yield in terms of thermodynamic analysis is increased. 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Production and utilization</subject><subject>Applied sciences</subject><subject>Catalysts</subject><subject>Conversion</subject><subject>Energy</subject><subject>Exact sciences and technology</subject><subject>Fuels</subject><subject>H 2 yield</subject><subject>Heating</subject><subject>Hydrogen</subject><subject>Hydrogen production</subject><subject>Hydrogen production and generation</subject><subject>Methanol steam reforming (MSR) and autothermal reforming (ATR)</subject><subject>Methyl alcohol</subject><subject>Preheating</subject><subject>Reforming</subject><subject>Spiral preheating</subject><subject>Spirals</subject><subject>Steam electric power generation</subject><subject>Thermal characteristics</subject><issn>0360-3199</issn><issn>1879-3487</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2011</creationdate><recordtype>article</recordtype><recordid>eNqFkE9P3DAQxa0KJBbKV0C-VJyy2LGdTW6tUP8gIXGhZ2tiT4hXib21HRDfHm93S4-cLD3_3puZR8gVZ2vOeHOzXbvt-GrR47pme7FeM6U-kRVvN10lZLs5ISsmGlYJ3nVn5DylLWN8w2S3IsvjiHGGifY4wrMLkYK3tMTF8ISe7mKwi8kueBoGOmMewYeJpoww04hDiLPzT389sOSQj2H_f15cHmnauVjUXcQRIRf5MzkdYEp4eXwvyO8f3x9vf1X3Dz_vbr_dV0ZylSvOxQDWtEZY0SnTGaVED2AVl6Zte2FqwWwjlOxbVBuOA8he9bVopGxsbztxQa4PueWOPwumrGeXDE4TeAxL0m0hBW-YKmRzIE0MKZX99S66GeKr5kzva9Zb_a9mva9Z81qXmovxy3EEJAPTEMEbl97dteikqBtZuK8HDsu9zw6jTsahN2hdRJO1De6jUW-Kz5oE</recordid><startdate>20110301</startdate><enddate>20110301</enddate><creator>Chen, Wei-Hsin</creator><creator>Syu, Yu-Jhih</creator><general>Elsevier Ltd</general><general>Elsevier</general><scope>IQODW</scope><scope>AAYXX</scope><scope>CITATION</scope><scope>7SP</scope><scope>8FD</scope><scope>L7M</scope></search><sort><creationdate>20110301</creationdate><title>Thermal behavior and hydrogen production of methanol steam reforming and autothermal reforming with spiral preheating</title><author>Chen, Wei-Hsin ; Syu, Yu-Jhih</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c415t-113fadc8c3d395c9c553baad514c88b3c230d6354b8e571efa4b5b236446dbd93</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2011</creationdate><topic>Alternative fuels. Production and utilization</topic><topic>Applied sciences</topic><topic>Catalysts</topic><topic>Conversion</topic><topic>Energy</topic><topic>Exact sciences and technology</topic><topic>Fuels</topic><topic>H 2 yield</topic><topic>Heating</topic><topic>Hydrogen</topic><topic>Hydrogen production</topic><topic>Hydrogen production and generation</topic><topic>Methanol steam reforming (MSR) and autothermal reforming (ATR)</topic><topic>Methyl alcohol</topic><topic>Preheating</topic><topic>Reforming</topic><topic>Spiral preheating</topic><topic>Spirals</topic><topic>Steam electric power generation</topic><topic>Thermal characteristics</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Chen, Wei-Hsin</creatorcontrib><creatorcontrib>Syu, Yu-Jhih</creatorcontrib><collection>Pascal-Francis</collection><collection>CrossRef</collection><collection>Electronics &amp; Communications Abstracts</collection><collection>Technology Research Database</collection><collection>Advanced Technologies Database with Aerospace</collection><jtitle>International journal of hydrogen energy</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Chen, Wei-Hsin</au><au>Syu, Yu-Jhih</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Thermal behavior and hydrogen production of methanol steam reforming and autothermal reforming with spiral preheating</atitle><jtitle>International journal of hydrogen energy</jtitle><date>2011-03-01</date><risdate>2011</risdate><volume>36</volume><issue>5</issue><spage>3397</spage><epage>3408</epage><pages>3397-3408</pages><issn>0360-3199</issn><eissn>1879-3487</eissn><coden>IJHEDX</coden><abstract>The present study aims to investigate the thermal behavior and hydrogen production characteristics from methanol steam reforming (MSR) and autothermal reforming (ATR) under the effects of a Cu-Zn-based catalyst and spiral preheating. Two different reaction temperatures of 250 and 300 °C are taken into account. Meanwhile, the O/C ratio (i.e. the molar ratio between O 2 and methanol) and S/C ratio (i.e. the molar ratio between steam and methanol) are controlled in the ranges of 0–0.5 and 1–2, respectively. The condition of O/C = 0 represents the reaction of MSR. By monitoring the supplied power into the reactor with a fixed gas hourly space velocity (GHSV) of 72,000 h −1, the experimental results indicate that an exothermic reaction from ATR can be attained once the O/C ratio is as high as 0.125. Increasing O/C ratio causes more heat released from the reaction, this results in the decrease in the frequency of supplied power, especially at O/C = 0.5. It is noted that the concentration of CO in the product gas is quite low compared to that of CO 2. An increase in O/C ratio abates the concentration of H 2 from the consumption of per mol methanol; however, the H 2 yield in terms of thermodynamic analysis is increased. On account of the utilization of spiral preheating on the reactants, within the investigated operating conditions the methanol conversion and hydrogen yield were always higher than 95 and 90%, respectively. A comparison suggests that the methanol conversion from ATR of methanol with spiral preheating is superior to those of other studies. ► Thermal behavior of methanol steam reforming (MSR) and autothermal reforming (ATR) is studied. ► Hydrogen production characteristics from MSR and ATR are investigated. ► The effect of spiral preheating on MSR and ATR is explored. ► An exothermic reaction from ATR can be attained once the O/C ratio is as high as 0.125. ► The results suggest that the methanol conversion from ATR of methanol with spiral preheating is superior to those of other studies.</abstract><cop>Kidlington</cop><pub>Elsevier Ltd</pub><doi>10.1016/j.ijhydene.2010.12.055</doi><tpages>12</tpages></addata></record>
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subjects Alternative fuels. Production and utilization
Applied sciences
Catalysts
Conversion
Energy
Exact sciences and technology
Fuels
H 2 yield
Heating
Hydrogen
Hydrogen production
Hydrogen production and generation
Methanol steam reforming (MSR) and autothermal reforming (ATR)
Methyl alcohol
Preheating
Reforming
Spiral preheating
Spirals
Steam electric power generation
Thermal characteristics
title Thermal behavior and hydrogen production of methanol steam reforming and autothermal reforming with spiral preheating
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