d4 universiti teknologi mara

Upload: najwa-mohd-nor

Post on 08-Apr-2018

224 views

Category:

Documents


0 download

TRANSCRIPT

  • 8/6/2019 D4 Universiti Teknologi MARA

    1/60

    Cost-Effective Technologies for ThermochemicalConversion of Biomass to Produce Fuels,

    Chemicals, Materials and Power

    Mohammad Asadullah

    Professor (Dr)

    Universiti Teknologi MARA

    Faculty of Chemical EngineeringUniversiti Teknologi MARA

    http://www.joomlaworks.gr/
  • 8/6/2019 D4 Universiti Teknologi MARA

    2/60

    Content Introduction to R & D Projects Based on BiomassBackgroundProblem Statement ObjectivesMalaysian Government Policy of Utilizing BiomassBiomass Potentiality in MalaysiaTechnologies for Thermochemical Conversion of Biomass

    Gasification of Biomass and Model of Commercial Plant Pyrolysis of Biomass and Model of Commercial Plant Summary and Conclusion

  • 8/6/2019 D4 Universiti Teknologi MARA

    3/60

    R&D/Commercialization Projects

    First R&DProject:BiomassGasification

    Heat

    Power

    Liquid

    Fuels

    Power

    ChemicalsSecond R&DProject: BiomassPyrolysis &Biorefinery

    Materials

  • 8/6/2019 D4 Universiti Teknologi MARA

    4/60

    What is Biomass

    Biomasses are organic materials derived fromliving organisms, i.e. from plants or animals.

    Depending on the source of biomass, it can be

    classified as primary and secondary biomasses.

    Background

  • 8/6/2019 D4 Universiti Teknologi MARA

    5/60

    Formation of Biomass

    C6 H12 O6 6H 2 O + 6CO 2

    + 6 O 2

    Cellulose +Hemicellulose +Lignin

    PrimaryBiom ass

    Secondary Biomass

    http://www.google.com/imgres?imgurl=http://www.vitabiogroup.com/imagens/biomass/biomass1.jpg&imgrefurl=http://www.vitabiogroup.com/interna.php?pg=biomass&usg=__uZsJgVO69sMbbTc3eBIS8jkrqa4=&h=240&w=335&sz=25&hl=en&start=103&sig2=9B5wUxnJX8mL3XlyXf9gjA&zoom=1&tbnid=5HWkNKGcb4-PUM:&tbnh=85&tbnw=119&ei=sKyQTd3nFIvfccGBjYQK&prev=/images?q=Picture+of+agricultural+biomass&um=1&hl=en&safe=off&sa=X&rls=com.microsoft:en-us&biw=1259&bih=588&tbs=isch:1&um=1&itbs=1http://www.google.com/imgres?imgurl=http://newsimg.bbc.co.uk/media/images/42472000/jpg/_42472473_cowdung_patties203.jpg&imgrefurl=http://news.bbc.co.uk/2/hi/programmes/from_our_own_correspondent/6279929.stm&usg=__MSkmt5GX3yu40dfGXiGQIxwV8e8=&h=152&w=203&sz=18&hl=en&start=3&sig2=R_oP2zZhfaSQbZ_93OJotw&zoom=1&tbnid=qf-2aavYOAiNRM:&tbnh=79&tbnw=105&ei=m6uQTZesOdS8cdD98a0I&prev=/images?q=Cow+dung&um=1&hl=en&safe=off&sa=X&rls=com.microsoft:en-us&biw=1259&bih=588&tbs=isch:1&um=1&itbs=1http://www.google.com/imgres?imgurl=http://www.arunaelectricalworks.com/biomass/img/BiomassIntro/biomass_fuel.jpg&imgrefurl=http://www.arunaelectricalworks.com/biomass/BiomassIntro.aspx&usg=__sYvLdrOJ3TJaTm2cD1qWM1ikI08=&h=191&w=219&sz=16&hl=en&start=99&sig2=AhJe5L6fPv8DCOpuWCPglw&zoom=1&tbnid=p63kjLHMAfHyHM:&tbnh=93&tbnw=107&ei=sKyQTd3nFIvfccGBjYQK&prev=/images?q=Picture+of+agricultural+biomass&um=1&hl=en&safe=off&sa=X&rls=com.microsoft:en-us&biw=1259&bih=588&tbs=isch:1&um=1&itbs=1http://www.google.com/imgres?imgurl=http://www.vitabiogroup.com/imagens/biomass/biomass1.jpg&imgrefurl=http://www.vitabiogroup.com/interna.php?pg=biomass&usg=__uZsJgVO69sMbbTc3eBIS8jkrqa4=&h=240&w=335&sz=25&hl=en&start=103&sig2=9B5wUxnJX8mL3XlyXf9gjA&zoom=1&tbnid=5HWkNKGcb4-PUM:&tbnh=85&tbnw=119&ei=sKyQTd3nFIvfccGBjYQK&prev=/images?q=Picture+of+agricultural+biomass&um=1&hl=en&safe=off&sa=X&rls=com.microsoft:en-us&biw=1259&bih=588&tbs=isch:1&um=1&itbs=1http://www.google.com/imgres?imgurl=http://cache2.asset-cache.net/xc/81551738.jpg?v=1&c=IWSAsset&k=2&d=77BFBA49EF8789215ABF3343C02EA548AC5671C2A1AA514DC4B88A942F0BE7F2379A24E075764100E30A760B0D811297&imgrefurl=http://www.life.com/image/81551738&usg=__oKvYOIcoHzYCmPL4hXeXyMa0aQ4=&h=371&w=594&sz=51&hl=en&start=106&sig2=bfMXUhk3f1jo3XxchjR2pg&zoom=1&tbnid=G26CSkNOyO4ThM:&tbnh=84&tbnw=135&ei=sKyQTd3nFIvfccGBjYQK&prev=/images?q=Picture+of+agricultural+biomass&um=1&hl=en&safe=off&sa=X&rls=com.microsoft:en-us&biw=1259&bih=588&tbs=isch:1&um=1&itbs=1http://www.google.com/imgres?imgurl=http://c1.cleantechnica.com/files/2008/03/wood1.jpg&imgrefurl=http://cleantechnica.com/2008/03/09/interview-biomass-gas-and-electric-produces-energy-from-waste-products/&usg=__Dl7gAJADOg-zjHF3CBABOyDK_6g=&h=331&w=461&sz=57&hl=en&start=110&sig2=Vqn1uslOh8hZV7EyrDT1tQ&zoom=1&tbnid=seWgRfzE6PoEnM:&tbnh=92&tbnw=128&ei=sKyQTd3nFIvfccGBjYQK&prev=/images?q=Picture+of+agricultural+biomass&um=1&hl=en&safe=off&sa=X&rls=com.microsoft:en-us&biw=1259&bih=588&tbs=isch:1&um=1&itbs=1http://www.google.com/imgres?imgurl=http://www.instablogsimages.com/images/2009/05/01/brick_dUxFh_23302.jpg&imgrefurl=http://www.greendiary.com/entry/cow-dung-ecofaebrick-bags-first-prize/&usg=__dzuIM0jCi4097kDC5m-stkz021c=&h=991&w=550&sz=578&hl=en&start=24&sig2=0idnwrPMxXS7QCq9MFvfJg&zoom=1&tbnid=rjQy6LFr3ezxWM:&tbnh=149&tbnw=83&ei=mquQTc6JFseGcaLQ_fcJ&prev=/images?q=Cow+dung&um=1&hl=en&safe=off&sa=X&rls=com.microsoft:en-us&biw=1259&bih=588&tbs=isch:1&um=1&itbs=1http://www.google.com/imgres?imgurl=http://www.autoblog.com/media/2006/03/Cow-Dung-resized.jpg&imgrefurl=http://www.autoblog.com/2006/03/06/m/&usg=__RroO7P2HpPBR6fEhiPDSnIQuV4Q=&h=298&w=450&sz=28&hl=en&start=14&sig2=5CT4Tbtzvfl7NjVYv20gog&zoom=1&tbnid=E4JNZ1vp_5z7kM:&tbnh=84&tbnw=127&ei=m6uQTZesOdS8cdD98a0I&prev=/images?q=Cow+dung&um=1&hl=en&safe=off&sa=X&rls=com.microsoft:en-us&biw=1259&bih=588&tbs=isch:1&um=1&itbs=1http://www.google.com/imgres?imgurl=http://tyler.blogware.com/cowdung.jpg&imgrefurl=http://tyler.blogware.com/2006/4/11/&usg=__RgHACWxBEkhelPQz4zNCVhRqv-M=&h=220&w=220&sz=16&hl=en&start=6&sig2=b2ycePBel3xhCTCPhzy62w&zoom=1&tbnid=Ckdb2BJWMytx4M:&tbnh=107&tbnw=107&ei=m6uQTZesOdS8cdD98a0I&prev=/images?q=Cow+dung&um=1&hl=en&safe=off&sa=X&rls=com.microsoft:en-us&biw=1259&bih=588&tbs=isch:1&um=1&itbs=1http://www.google.com/imgres?imgurl=http://newsimg.bbc.co.uk/media/images/42472000/jpg/_42472473_cowdung_patties203.jpg&imgrefurl=http://news.bbc.co.uk/2/hi/programmes/from_our_own_correspondent/6279929.stm&usg=__MSkmt5GX3yu40dfGXiGQIxwV8e8=&h=152&w=203&sz=18&hl=en&start=3&sig2=R_oP2zZhfaSQbZ_93OJotw&zoom=1&tbnid=qf-2aavYOAiNRM:&tbnh=79&tbnw=105&ei=m6uQTZesOdS8cdD98a0I&prev=/images?q=Cow+dung&um=1&hl=en&safe=off&sa=X&rls=com.microsoft:en-us&biw=1259&bih=588&tbs=isch:1&um=1&itbs=1http://www.google.com/imgres?imgurl=http://en.delaval.ca/NR/rdonlyres/8334143D-7458-45B0-B2A0-19F059FC716A/0/Cows.jpg&imgrefurl=http://en.delaval.ca/About_DeLaval/PressCentre/Image_gallery_genaral.htm&usg=__32XNkJ7yd0Owj59aSVQKCg9Qa40=&h=1312&w=2000&sz=2843&hl=en&start=154&sig2=HnCuTLTFFqhLPAsjqzS0tA&zoom=1&tbnid=RxHxAdV7pI_G5M:&tbnh=98&tbnw=150&ei=OqqQTdb0HYiucLe4tYQK&prev=/images?q=Cows+picture&um=1&hl=en&safe=off&sa=X&rls=com.microsoft:en-us&biw=1259&bih=588&tbs=isch:1&um=1&itbs=1
  • 8/6/2019 D4 Universiti Teknologi MARA

    6/60

    Biomass is the Source of Fuels,Chemicals, Materials & Power

    Every singlecarbon usedfrom fossilresources wouldbe excess into

    the atmosphere. Millionsof years

    Chemicals Materials PowerFuels

    http://www2.wwnorton.com/college/geo/animations/oil_formation_trapping.htmhttp://www.google.com/imgres?imgurl=http://www.arunaelectricalworks.com/biomass/img/BiomassIntro/biomass_fuel.jpg&imgrefurl=http://www.arunaelectricalworks.com/biomass/BiomassIntro.aspx&usg=__sYvLdrOJ3TJaTm2cD1qWM1ikI08=&h=191&w=219&sz=16&hl=en&start=99&sig2=AhJe5L6fPv8DCOpuWCPglw&zoom=1&tbnid=p63kjLHMAfHyHM:&tbnh=93&tbnw=107&ei=sKyQTd3nFIvfccGBjYQK&prev=/images?q=Picture+of+agricultural+biomass&um=1&hl=en&safe=off&sa=X&rls=com.microsoft:en-us&biw=1259&bih=588&tbs=isch:1&um=1&itbs=1http://www.google.com/imgres?imgurl=http://cache2.asset-cache.net/xc/81551738.jpg?v=1&c=IWSAsset&k=2&d=77BFBA49EF8789215ABF3343C02EA548AC5671C2A1AA514DC4B88A942F0BE7F2379A24E075764100E30A760B0D811297&imgrefurl=http://www.life.com/image/81551738&usg=__oKvYOIcoHzYCmPL4hXeXyMa0aQ4=&h=371&w=594&sz=51&hl=en&start=106&sig2=bfMXUhk3f1jo3XxchjR2pg&zoom=1&tbnid=G26CSkNOyO4ThM:&tbnh=84&tbnw=135&ei=sKyQTd3nFIvfccGBjYQK&prev=/images?q=Picture+of+agricultural+biomass&um=1&hl=en&safe=off&sa=X&rls=com.microsoft:en-us&biw=1259&bih=588&tbs=isch:1&um=1&itbs=1http://www.google.com/imgres?imgurl=http://www.autoblog.com/media/2006/03/Cow-Dung-resized.jpg&imgrefurl=http://www.autoblog.com/2006/03/06/m/&usg=__RroO7P2HpPBR6fEhiPDSnIQuV4Q=&h=298&w=450&sz=28&hl=en&start=14&sig2=5CT4Tbtzvfl7NjVYv20gog&zoom=1&tbnid=E4JNZ1vp_5z7kM:&tbnh=84&tbnw=127&ei=m6uQTZesOdS8cdD98a0I&prev=/images?q=Cow+dung&um=1&hl=en&safe=off&sa=X&rls=com.microsoft:en-us&biw=1259&bih=588&tbs=isch:1&um=1&itbs=1http://www.google.com/imgres?imgurl=http://newsimg.bbc.co.uk/media/images/42472000/jpg/_42472473_cowdung_patties203.jpg&imgrefurl=http://news.bbc.co.uk/2/hi/programmes/from_our_own_correspondent/6279929.stm&usg=__MSkmt5GX3yu40dfGXiGQIxwV8e8=&h=152&w=203&sz=18&hl=en&start=3&sig2=R_oP2zZhfaSQbZ_93OJotw&zoom=1&tbnid=qf-2aavYOAiNRM:&tbnh=79&tbnw=105&ei=m6uQTZesOdS8cdD98a0I&prev=/images?q=Cow+dung&um=1&hl=en&safe=off&sa=X&rls=com.microsoft:en-us&biw=1259&bih=588&tbs=isch:1&um=1&itbs=1
  • 8/6/2019 D4 Universiti Teknologi MARA

    7/60

    Global Carbon Cycle

    Burning of fossil fuel

    Burning of biomass

    4.5

    1.5

    1

    95

    103

    101

    50

    53

    53

    48

    2

    100

    5

  • 8/6/2019 D4 Universiti Teknologi MARA

    8/60

    Mass Balance of the GlobalCarbon Cycle

    Mass Balance

    NET EMISSION = OUTPUT - INPUT= (100 + 4.5 + 1.5 + 1.0) - (100.0 +2.0)= 5.0 Bt/y

    CO 2 Consumption

    CO 2 Release Plant and soil respiration = 100.0 Bt/yLand use = 1.0 Bt/y

    Fossil fuels burning = 4.5 Bt/yBiomass burning = 1.5 Bt/y

    Ocean uptake (Sedimentation)

    = 2.0 Bt/yPhotosynthesis = 100.0 Bt/y

  • 8/6/2019 D4 Universiti Teknologi MARA

    9/60

    Global Mean Temperature Profile

    The global temperature is supposed toincrease by 5 oC within 2050.

    These are theoverall problemsrelated to the fossilresources.

  • 8/6/2019 D4 Universiti Teknologi MARA

    10/60

    Overall Objective of this Technology

    Fuels

    Millionsof years

    ChemicalsMaterialsPower

    Fuels

    Moderntechnology

    Chemicals

    Materials

    Power

    0 yearOverall objective

    is to reducemillions of years

    to zero year.

    http://www.google.com/imgres?imgurl=http://www.arunaelectricalworks.com/biomass/img/BiomassIntro/biomass_fuel.jpg&imgrefurl=http://www.arunaelectricalworks.com/biomass/BiomassIntro.aspx&usg=__sYvLdrOJ3TJaTm2cD1qWM1ikI08=&h=191&w=219&sz=16&hl=en&start=99&sig2=AhJe5L6fPv8DCOpuWCPglw&zoom=1&tbnid=p63kjLHMAfHyHM:&tbnh=93&tbnw=107&ei=sKyQTd3nFIvfccGBjYQK&prev=/images?q=Picture+of+agricultural+biomass&um=1&hl=en&safe=off&sa=X&rls=com.microsoft:en-us&biw=1259&bih=588&tbs=isch:1&um=1&itbs=1http://www.google.com/imgres?imgurl=http://cache2.asset-cache.net/xc/81551738.jpg?v=1&c=IWSAsset&k=2&d=77BFBA49EF8789215ABF3343C02EA548AC5671C2A1AA514DC4B88A942F0BE7F2379A24E075764100E30A760B0D811297&imgrefurl=http://www.life.com/image/81551738&usg=__oKvYOIcoHzYCmPL4hXeXyMa0aQ4=&h=371&w=594&sz=51&hl=en&start=106&sig2=bfMXUhk3f1jo3XxchjR2pg&zoom=1&tbnid=G26CSkNOyO4ThM:&tbnh=84&tbnw=135&ei=sKyQTd3nFIvfccGBjYQK&prev=/images?q=Picture+of+agricultural+biomass&um=1&hl=en&safe=off&sa=X&rls=com.microsoft:en-us&biw=1259&bih=588&tbs=isch:1&um=1&itbs=1http://www.google.com/imgres?imgurl=http://www.autoblog.com/media/2006/03/Cow-Dung-resized.jpg&imgrefurl=http://www.autoblog.com/2006/03/06/m/&usg=__RroO7P2HpPBR6fEhiPDSnIQuV4Q=&h=298&w=450&sz=28&hl=en&start=14&sig2=5CT4Tbtzvfl7NjVYv20gog&zoom=1&tbnid=E4JNZ1vp_5z7kM:&tbnh=84&tbnw=127&ei=m6uQTZesOdS8cdD98a0I&prev=/images?q=Cow+dung&um=1&hl=en&safe=off&sa=X&rls=com.microsoft:en-us&biw=1259&bih=588&tbs=isch:1&um=1&itbs=1http://www.google.com/imgres?imgurl=http://newsimg.bbc.co.uk/media/images/42472000/jpg/_42472473_cowdung_patties203.jpg&imgrefurl=http://news.bbc.co.uk/2/hi/programmes/from_our_own_correspondent/6279929.stm&usg=__MSkmt5GX3yu40dfGXiGQIxwV8e8=&h=152&w=203&sz=18&hl=en&start=3&sig2=R_oP2zZhfaSQbZ_93OJotw&zoom=1&tbnid=qf-2aavYOAiNRM:&tbnh=79&tbnw=105&ei=m6uQTZesOdS8cdD98a0I&prev=/images?q=Cow+dung&um=1&hl=en&safe=off&sa=X&rls=com.microsoft:en-us&biw=1259&bih=588&tbs=isch:1&um=1&itbs=1http://www2.wwnorton.com/college/geo/animations/oil_formation_trapping.htmhttp://www.google.com/imgres?imgurl=http://www.arunaelectricalworks.com/biomass/img/BiomassIntro/biomass_fuel.jpg&imgrefurl=http://www.arunaelectricalworks.com/biomass/BiomassIntro.aspx&usg=__sYvLdrOJ3TJaTm2cD1qWM1ikI08=&h=191&w=219&sz=16&hl=en&start=99&sig2=AhJe5L6fPv8DCOpuWCPglw&zoom=1&tbnid=p63kjLHMAfHyHM:&tbnh=93&tbnw=107&ei=sKyQTd3nFIvfccGBjYQK&prev=/images?q=Picture+of+agricultural+biomass&um=1&hl=en&safe=off&sa=X&rls=com.microsoft:en-us&biw=1259&bih=588&tbs=isch:1&um=1&itbs=1http://www.google.com/imgres?imgurl=http://cache2.asset-cache.net/xc/81551738.jpg?v=1&c=IWSAsset&k=2&d=77BFBA49EF8789215ABF3343C02EA548AC5671C2A1AA514DC4B88A942F0BE7F2379A24E075764100E30A760B0D811297&imgrefurl=http://www.life.com/image/81551738&usg=__oKvYOIcoHzYCmPL4hXeXyMa0aQ4=&h=371&w=594&sz=51&hl=en&start=106&sig2=bfMXUhk3f1jo3XxchjR2pg&zoom=1&tbnid=G26CSkNOyO4ThM:&tbnh=84&tbnw=135&ei=sKyQTd3nFIvfccGBjYQK&prev=/images?q=Picture+of+agricultural+biomass&um=1&hl=en&safe=off&sa=X&rls=com.microsoft:en-us&biw=1259&bih=588&tbs=isch:1&um=1&itbs=1http://www.google.com/imgres?imgurl=http://www.autoblog.com/media/2006/03/Cow-Dung-resized.jpg&imgrefurl=http://www.autoblog.com/2006/03/06/m/&usg=__RroO7P2HpPBR6fEhiPDSnIQuV4Q=&h=298&w=450&sz=28&hl=en&start=14&sig2=5CT4Tbtzvfl7NjVYv20gog&zoom=1&tbnid=E4JNZ1vp_5z7kM:&tbnh=84&tbnw=127&ei=m6uQTZesOdS8cdD98a0I&prev=/images?q=Cow+dung&um=1&hl=en&safe=off&sa=X&rls=com.microsoft:en-us&biw=1259&bih=588&tbs=isch:1&um=1&itbs=1http://www.google.com/imgres?imgurl=http://newsimg.bbc.co.uk/media/images/42472000/jpg/_42472473_cowdung_patties203.jpg&imgrefurl=http://news.bbc.co.uk/2/hi/programmes/from_our_own_correspondent/6279929.stm&usg=__MSkmt5GX3yu40dfGXiGQIxwV8e8=&h=152&w=203&sz=18&hl=en&start=3&sig2=R_oP2zZhfaSQbZ_93OJotw&zoom=1&tbnid=qf-2aavYOAiNRM:&tbnh=79&tbnw=105&ei=m6uQTZesOdS8cdD98a0I&prev=/images?q=Cow+dung&um=1&hl=en&safe=off&sa=X&rls=com.microsoft:en-us&biw=1259&bih=588&tbs=isch:1&um=1&itbs=1
  • 8/6/2019 D4 Universiti Teknologi MARA

    11/60

    Why Biomass is a CarbonNeutral Fuel

    Heat or

    6CO 2 + 6H 2O

    Bacterialaction

    NaturalCycleC6H12 O6

    XGasificationGas orLiquid

    6H 2O + 6CO 2

    Pyrolysis

    Artificial Cycle

    Energy

    Biomass

    http://www.google.com/imgres?imgurl=http://www.arunaelectricalworks.com/biomass/img/BiomassIntro/biomass_fuel.jpg&imgrefurl=http://www.arunaelectricalworks.com/biomass/BiomassIntro.aspx&usg=__sYvLdrOJ3TJaTm2cD1qWM1ikI08=&h=191&w=219&sz=16&hl=en&start=99&sig2=AhJe5L6fPv8DCOpuWCPglw&zoom=1&tbnid=p63kjLHMAfHyHM:&tbnh=93&tbnw=107&ei=sKyQTd3nFIvfccGBjYQK&prev=/images?q=Picture+of+agricultural+biomass&um=1&hl=en&safe=off&sa=X&rls=com.microsoft:en-us&biw=1259&bih=588&tbs=isch:1&um=1&itbs=1http://www.google.com/imgres?imgurl=http://www.arunaelectricalworks.com/biomass/img/BiomassIntro/biomass_fuel.jpg&imgrefurl=http://www.arunaelectricalworks.com/biomass/BiomassIntro.aspx&usg=__sYvLdrOJ3TJaTm2cD1qWM1ikI08=&h=191&w=219&sz=16&hl=en&start=99&sig2=AhJe5L6fPv8DCOpuWCPglw&zoom=1&tbnid=p63kjLHMAfHyHM:&tbnh=93&tbnw=107&ei=sKyQTd3nFIvfccGBjYQK&prev=/images?q=Picture+of+agricultural+biomass&um=1&hl=en&safe=off&sa=X&rls=com.microsoft:en-us&biw=1259&bih=588&tbs=isch:1&um=1&itbs=1
  • 8/6/2019 D4 Universiti Teknologi MARA

    12/60

    Malaysian Governmental Policy of Utilizing Renewable Resources, 2011

    On June 10, 2010, the government announced the NationalRenewable Energy Policy and Action Plan with a goal of increasing renewable energy from 1% to 5.5% of electricity

    supply by 2015.The program is going to be launched by the secondquarter of 2011.

    Source: Renewable energy world.com, August 16, 2010

    The current proposal limits the program to 219 MW in

    2011, increasing to nearly 1,000 MW in 2015. The bulk of the new generating capacity to be installed under theprogram is set aside for biomass and minihydro.

  • 8/6/2019 D4 Universiti Teknologi MARA

    13/60

    Quota of Biomass Energy out of TotalRenewable Energy Generation

  • 8/6/2019 D4 Universiti Teknologi MARA

    14/60

    Comparison of Tariffs for PV andBiomass Energy

  • 8/6/2019 D4 Universiti Teknologi MARA

    15/60

  • 8/6/2019 D4 Universiti Teknologi MARA

    16/60

    Problems with Existing GasificationTechnology

    High temperature method > 1000 oC

    Tar yield > 5%Tar deposits in the down stream applicationof syngas and makes problems

    Tar separation by physical filtration isnot technically viable

  • 8/6/2019 D4 Universiti Teknologi MARA

    17/60

    Fundamental Concept of Gasification ina Down Draft Gasifier

    Biomass

    Zone I

    Zone IIOxidation

    ReductionZone III

    Pyrolysis

    Char Volatiles (Liquid vapour + CO, H 2 ,H2O, CO 2 , CH 4 , C 2 H2 )

    C + CO 2 2COC + H 2O CO + H 2CO + H 2O CO2 + H 2

    CO, H 2 , H 2O, CO 2 , CH 4 , C 2H2 , N 2, tar Char + Ash

    Char + Ash Volatiles

    AirO2H2 OCO2

    C + O 2 COC + O 2 CO2H2+ O2 H2O

    (CO, H 2 , H 2 O, CO 2 ,CH4 , C 2 H2 , N 2 )

  • 8/6/2019 D4 Universiti Teknologi MARA

    18/60

    Asadullah et al ., Catalysis Communication , 2, 2001, 63-68.

    Catalytic Gasification of Cellulose

    Asadullah et al., Industrial and Engineering Chemistry Research , 40, 2001 , 5894 .

  • 8/6/2019 D4 Universiti Teknologi MARA

    19/60

    Result of Catalyst Screaming

  • 8/6/2019 D4 Universiti Teknologi MARA

    20/60

    Feeder

    Air

    Vibrator

    Productgas

    Furnace

    Thermocouple Distributor

    Catalyst particles

    Asadullah et al., Applied Catalysis A: General, Volume 255,Issue 2, 8 December 2003, Pages 169-180

    Asadullah et al. , Industrial and Engineering Chemistry Research ,41, 2002, 4567-4575

    Catalytic Gasification of Cellulose

  • 8/6/2019 D4 Universiti Teknologi MARA

    21/60

    TEM Images of Rh/CeO 2 Catalyst

    30 nm 30 nm

    Asadullah et al. , Industrial and Engineering Chemistry Research ,41, 2002, 4567-4575

    Rh/CeO 2sintered anddeactivated

  • 8/6/2019 D4 Universiti Teknologi MARA

    22/60

    TEM Images of Rh/CeO 2/SiO 2 Catalyst

    TEM images of Rh/CeO 2/SiO 2; (a) fresh catalyst, (b) after reaction

    Asadullah et al., Journal of Catalysis, 208, 2002 , 255-259

    Rh/CeO 2 /SiO 2No sintering

    at all afterreaction

  • 8/6/2019 D4 Universiti Teknologi MARA

    23/60

    Asadullah et al., Applied Catalysis A: General 255 (2003) 169 180.

    Rh/CeO 2/SiO 2 Catalyst for RealBiomass Gasification

    No problemsat all even at650 oC

    Ashproblems

  • 8/6/2019 D4 Universiti Teknologi MARA

    24/60

    T (oC) Formation rate

    (mmol/min) H2/CO C-

    conv Charyield

    Cokeyield

    Taryield

    CO H2 CO 2 CH4 (%-C) (%-C) (%-C) (%-C)

    Cedar 550 2152 2686 1841 517 1.3 78 20.8 1.2 0

    600 2599 3232 1752 269 1.2 80 19.1 0.8 0

    650 2902 3541 1605 148 1.2 81 18.5 0.5 0

    Jute stick 550 2032 2634 1729 323 1.3 71 24.0 3.0 2.0

    600 2362 3036 1818 306 1.3 78 17.0 1.0 0.0

    650 3057 3255 1577 218 1.1 84 14.5 0.5 0.0

    Bagasse 550 1850 2057 1645 416 1.1 68 21.0 4.0 7.0

    600 2050 2357 1739 516 1.2 75 21.0 2.0 2.0

    650 2965 3264 1587 205 1.1 82 17.0 1.0 0.0

    Ricestraw 550 1797 2057 1569 366 1.2 65 21.0 4.0 10.0

    600 2102 2162 1677 452 1 74 19.0 4.0 3.0

    650 2878 3167 1524 172 1.1 80 16.0 2.0 2.0 Conditions: Catalyst 3 g, ER = 0.24, feeding rate 150 mg/min (moisture: 5 10%), N 2 flow 100 ml/min, O 2 flow 35 ml/min through the catalyst bed.

    Effect of Temperature on the Gasification ofVarious Biomass on Rh/CeO 2 /SiO 2 Catalyst

  • 8/6/2019 D4 Universiti Teknologi MARA

    25/60

    0

    20

    40

    60

    80

    100

    450 550 650 750 850 950 1050

    W e i g

    h t r a t

    i o / %

    Temperature/K

    Rice straw

    Bagasse

    Cedar

    Jute stick

    Properties of Various Biomasses

  • 8/6/2019 D4 Universiti Teknologi MARA

    26/60

    Mechanism of Rh/CeO 2/SiO 2 Catalytic Reaction

    CO 2 + H 2OCH 4

    H2O O2

    CharCO + H 2

    H2O

    Tar

    Oxidizedcatalyst

    Reducedcatalyst

    CeO 2

    SiO 2

    O2 Mobility

    high

    Highsurface

    area

    Very

    active

    RhCeO 2SiO2

  • 8/6/2019 D4 Universiti Teknologi MARA

    27/60

    Problem Statement and Objectivesfor Further Development of Catalysts

    Problem:

    Rh catalyst is expensive

    Objectives:

    To develop cheap catalysts with high activity

    To produce highly dispersed catalyst on highsurface area cheap materials

  • 8/6/2019 D4 Universiti Teknologi MARA

    28/60

    Asadullah, et al., Fuel, doi:10.1016/j.fuel.2010.12.039.

    Asadullah et al. , Fuel (In Press, 2011)

    Cheap Catalyst for Tar Reforming

    Charsupportedcatalyst

    P f f Ch S d

  • 8/6/2019 D4 Universiti Teknologi MARA

    29/60

    0

    5

    10

    15

    20

    25

    30

    35

    400 500 600 700 800 900Temperature ( oC)

    T a r y i e l

    d ( w t %

    o f b i o m a s s ,

    d b ) Pyrolysis

    Reforming no catalystReforming with H-charReforming with Fe-charReforming with Ni-char

    0

    5

    10

    15

    20

    25

    30

    35

    400 500 600 700 800 900Temperature ( oC)

    T a r y i e l

    d ( w t %

    o f b i o m a s s ,

    d b )

    Pyrolysis

    Reforming no catalyst

    Reforming with ilmenite

    Performance of Char SupportedCatalyst

    Ilmenite CatalystChar supportedcatalyst

    P f f Ch S t d

  • 8/6/2019 D4 Universiti Teknologi MARA

    30/60

    0

    500

    1000

    1500

    2000

    2500

    260 300 340 380 420 460 500Wavelength (nm)

    (a)

    I n t e n s i t y ( a

    . u . ,

    p e r g o f b i o m a s s ( d b )

    PyrolysisReforming no catalystReforming with H-charReforming with Fe-charReforming with Ni-char

    0

    500

    1000

    1500

    2000

    2500

    260 300 340 380 420 460 500Wavelength (nm)

    (b)

    I n t e n s

    i t y ( a

    . u . ,

    p e r g o

    f b i o m a s s

    ( d b )

    PyrolysisReforming no catalys tReforming with H-charReforming with Fe-charReforming with Ni-char

    0

    500

    1000

    1500

    2000

    2500

    260 300 340 380 420 460 500Wavelength (nm)

    (c)

    I n t e n s

    i t y ( a

    . u . ,

    p e r g o

    f b i o m a s s

    ( d b ) )

    PyrolysisReforming no catalystReforming with H-charReforming with Fe-charReforming with Ni-char

    0

    500

    1000

    1500

    2000

    2500

    260 300 340 380 420 460 500

    Wavelength (nm)(d)

    I n t e n s i

    t y ( a

    . u . ,

    p e r g o

    f b i o m a s s

    ( d b )

    PyrolysisReforming no catalystReforming with H-charReforming with Fe-charReforming with Ni-char

    0

    500

    1000

    1500

    2000

    2500

    260 300 340 380 420 460 500Wavelength (nm)

    (e)

    I n t e n s i

    t y ( a

    . u . ,

    p e r g o f

    b i o m a s s

    ( d b )

    PyrolysisReforming no catalystReforming with H-charReforming with Fe-charReforming with Ni-char

    Constant energy ( = -2800 cm -1) synchronous spectra of mallee wood tar solution (4ppm) after the steam reforming of its volatiles with/without the char-supported

    catalysts at the temperatures of (a), 500 C; (b), 600 C; (c), 700 C; (d), 800 C and(e), 850 C.

    Performance of Char SupportedCatalyst

  • 8/6/2019 D4 Universiti Teknologi MARA

    31/60

    Asadullah et al., Bioresource Technology ,doi:10.1016/j.biortech.2010.05.048

    Asadullah et al ., Industrial and Engineering Chemistry Research, 48, 2 009, 9858-9863.

    Asadullah et al., Fuel ProcessingTechnology In Press, Corrected Proof , Available online 3 September 2009.

    A schematic diagram of the fluidised-bedreactor used for the fast heating pyrolysis.

    Char Characteristics Studies

    L b S l D t ti Pl t f

  • 8/6/2019 D4 Universiti Teknologi MARA

    32/60

    Product gasoutlet

    Air inlet

    Water

    Steam Thermocouple

    Thermocouple

    Lab Scale Demonstration Plant forBiomass Gasification

    Lab Scale Demonstration Plant for

  • 8/6/2019 D4 Universiti Teknologi MARA

    33/60

    Solidsamplingport

    399mm

    340mm

    1-100 rpm

    400mm

    Solid samplingport

    Solid samplingport

    Solid samplingport

    Lookingglass

    Lookingglass

    Lookingglass

    1500mm

    150mm

    Gas samplingport

    Gas samplingport

    Gas samplingport

    Gas samplingport

    Thermocouple

    Thermoco

    uple

    Lab Scale Demonstration Plant forBiomass Gasification

    Looking

    glass

    Solidsampling

    port

    Rotatingshaft

  • 8/6/2019 D4 Universiti Teknologi MARA

    34/60

  • 8/6/2019 D4 Universiti Teknologi MARA

    35/60

    Water in

    Water out

    300 mm

    120mm

    Moving

    Moving

    Moving

    Moving

    Hot gas

    out

    1350 mm

    150 mm

    350 mm

    350 mm

    350 mm

    80 mm

    360mm

    20 o

    20 o

    20 o

    Inner Design

    RotatingArms

  • 8/6/2019 D4 Universiti Teknologi MARA

    36/60

    1500mm

    120

    mm

    150mm

    Air

    Water

    Out View of the Gasifier Main Body

    BiomassHopper

    CatalystHopper

    Gas outlet

  • 8/6/2019 D4 Universiti Teknologi MARA

    37/60

    1500mm

    120mm

    150mm

    Air Water

    Volatiles inletinto thecatalystchamber

    Inner Design

  • 8/6/2019 D4 Universiti Teknologi MARA

    38/60

    Picture of Complete Gasifier

  • 8/6/2019 D4 Universiti Teknologi MARA

    39/60

    Picture of Complete Gasifier

    f l f

  • 8/6/2019 D4 Universiti Teknologi MARA

    40/60

    Picture of Complete Gasifier

    Picture of Complete Gasifier

  • 8/6/2019 D4 Universiti Teknologi MARA

    41/60

    Picture of Complete Gasifier

    Pi f C l G ifi

  • 8/6/2019 D4 Universiti Teknologi MARA

    42/60

    Picture of Complete Gasifier

    Product Gas Quality from Non-

  • 8/6/2019 D4 Universiti Teknologi MARA

    43/60

    Gasification temperature, oC 850 50 850 50 850 50 850 50 850 50

    Biomass feeding rate, kg/h 4 4 4 4 4

    Air fuel ratio 0.09 0.18 0.27 0.36 0.53 Steam flow rate, kg/h 0.6 0.6 0.6 0.6 0.6

    Gas composition

    H2 26.62 17.54 19.77 15.11 16.11

    CO 30.42 33.59 27.27 31.34 24.76

    CH4 11.55 12.50 10.55 10.55 9.73 C2H6 0.32 0.43 0.38 0.39 0.39

    C2H4 1.74 2.42 2.17 2.59 2.45

    CO 2 12.87 11.12 12.94 13.55 13.36

    N2 10.38 14.73 21.73 24.94 30.67

    O2 0.24 0.85 1.29 0.08 1.00

    LHV, MJ/kg 13.43 12.60 10.75 10.14 9.21

    LHV, MJ/Nm 3 11.76 12.10 10.36 10.35 9.34

    Tar yield, mg/Nm 3 5100 9900 8600 8400 10900

    Tar yield, mg/MJ 929 725 866 1027 589

    Product Gas Quality from Non-Catalytic Experiment

    Product Gas Quality from

  • 8/6/2019 D4 Universiti Teknologi MARA

    44/60

    Gasification temperature, oC 850 50 850 50 850 50

    Biomass feeding rate, kg/h 4 4 4 Air fuel ratio 0.09 0.27 0.53

    Steam flow rate, kg/h 0.6 0.6 0.6

    Gas composition

    H2 50.50 35.98 31.37

    CO 32.15 35.89 33.30 CH4 4.14 6.14 7.22

    C2H6 0.08 0.07 0.05

    C2H4 0.24 0.36 0.37

    CO 2 5.05 6.72 9.54

    N2 6.58 10.01 13.97 O2 0.02 0.03 0.01

    LHV, MJ/kg 13.74 12.03 9.18

    LHV, MJ/Nm 3 10.44 9.95 8.31

    Tar yield, mg/Nm 3 2400 4900 2200

    Tar yield, mg/MJ 929 866 589

    Product Gas Quality fromCatalytic Experiment

  • 8/6/2019 D4 Universiti Teknologi MARA

    45/60

    Empty Fruit Bunches 19.00 million tones/y

    Mesocarp Fiber 13.00 million tones/yShell 5.20 million tones/y

    Palm Kernel Expeller 2.11 million tones/y

    Total 47.61 million tones/y

    Approximate energycontent

    8.09 x 10 11 MJ2.24 x 10 5 GWh

    Total price 6.27 x 10 4 BRM

    Biomass Potentiality in Malaysia

  • 8/6/2019 D4 Universiti Teknologi MARA

    46/60

    Input and Output of a 20 MWPower Plant

    Raw Materials Wood chips 176 t/day 64,689 t/y

    Power

    Generation

    Gasification New type

    Efficiency >50%

    Electricity tobe sold

    636 x 10 6 kWh 231 x 10 9 kWh

    Total sell

    price- RM

    177 MRM/day 64 BRM/y

    EnvironmentalEffects

    CO2 reduction 91,000 t/y

    Energy saving 60,944 t heavyoil/y

    Model of Commercial Power Generation

  • 8/6/2019 D4 Universiti Teknologi MARA

    47/60

    Gasifier

    Gas Scrubbing

    Water

    Fly Ash

    Catalytic

    Reformer

    GasEngine

    Steampowergeneration

    To Stack

    Ashcollector

    Conveyer

    Gas Cooler

    Gas BufferTank

    Steam +Air

    Gas Filter

    Model of Commercial Power Generationfrom Biomass (Wood Log)

  • 8/6/2019 D4 Universiti Teknologi MARA

    48/60

    N l f h P

  • 8/6/2019 D4 Universiti Teknologi MARA

    49/60

    Novelty of the Process

    Moisture content 0-50% in biomass can be used

    Biomass particle size 3-5 cm 3, real size from the large scalechipper, can be used

    Almost all kinds of cellulosic biomass can be used

    Pyrolyser is a compact and high throughput design

    Catalyst is char supported and thus very cheap

    Biorefinery Concept to Produce Fuels,

  • 8/6/2019 D4 Universiti Teknologi MARA

    50/60

    Dryer

    Pyrolyzer

    H2O

    Char

    Bi-oil

    W e t B i o

    m a s s

    W e t B i o

    m a s s

    Resin

    Electricity

    Gas (H 2)

    Gas (H 2) GasEnginesor FuelCellsGasifier

    SteamReformer

    Route 1b

    R o u t e1

    R o u t e2

    Route 1a

    Route 1c

    O p t i on1

    O p t i on

    3

    Option 2

    Option 2a

    Option 2bWater

    Light Olefine, CO 2

    Oxidizer EsterifierH2O2 Ethanol

    D i s t i l l er y

    Low Temperature

    Hydrogenation

    High TemperatureHydrogenation

    H2

    H2

    H2

    ZSM-5400-500 oC

    SteamActivator

    AdsorbentActivated Carbon

    Fertilizerabsorber

    Slow ReleaseFertilizer

    O

    OH

    OH

    O

    OH

    OH

    OH

    OH

    OH

    OHOH

    OH

    OH

    CH 3

    OH

    OH

    OH

    OH

    CH 3

    OH

    OH

    OH

    OH

    OH

    OH

    OH

    OH

    O

    O

    H

    O

    O

    O

    O

    H

    O

    O

    O

    O

    O

    OH OH

    OO

    O

    OH

    O

    O

    OH

    OH

    O

    OH

    O

    OOOH

    OH

    O OH

    OH Polymerizer

    (to Steam Reformeror Furnace)

    Light Alkane

    y pChemicals, Materials and Power

    Rotating Cone Reactor for

  • 8/6/2019 D4 Universiti Teknologi MARA

    51/60

    Rotating Cone Reactor forFast Pyrolysis

    Controlpanel

    BinCombustor

    Reactor Condenser

    Pump

    Compressor

    Liquidcollector

    CoolingWater

    Screw feeder

    Flue gas

    Productgas

  • 8/6/2019 D4 Universiti Teknologi MARA

    52/60

    120mm

  • 8/6/2019 D4 Universiti Teknologi MARA

    53/60

    120mm

    Product Distribution from Jute

  • 8/6/2019 D4 Universiti Teknologi MARA

    54/60

    Product Distribution from JuteStick Pyrolysis

    Pyrolysis conditionsJute stick feeding rate, kg/h 0.50

    Temperature, oC 500

    Nitrogen gas flow rate, ml/min 300

    Pyrolysis products

    Bio-oil

    First condenser, kg/h (wt%) 0.14 (28)

    Second condenser, kg/h (wt%) 0.16 (32)Total, kg/h (wt%) 0.30 (60)

    Char, kg/h (wt%) 0.12 (24)

    Gas, kg/h (wt%) 0.08 (16)

    Effect of Temperature on Product

  • 8/6/2019 D4 Universiti Teknologi MARA

    55/60

    Effect of Temperature on Product Distribution

    0

    20

    40

    60

    80

    100

    0 200 400 600 800

    Temperature, oC

    Y i e l d o f b i o - o i l a n d c h a r , w t %

    0

    4

    8

    12

    16

    20

    Y i e l d o f g a s , w t %

    Gas

    Bio-oil

    Char

  • 8/6/2019 D4 Universiti Teknologi MARA

    56/60

    What is Bio-oil?

    Bio-oil is a dark brown liquid. It contains about 200 types of chemicals mainly phenols, aromatic hydrocarbons, carboxylicacids and other highly oxygenated materials.

    Bio-oil

    Physical Properties of

  • 8/6/2019 D4 Universiti Teknologi MARA

    57/60

    Physical Properties of Bio-oil

    PropertiesDensity, g/cc 1.07 - 1.09

    pH 3.20 - 3.35

    Water content, wt% 15 - 20Char/Solid content, wt% 0.07 - 0.10

    Pyrolytic lignin 3.83 - 4.91

    Acid Value 122.5 - 134.2 Ash content, wt% 0.03

    Viscosity, Centipoise 2.59

  • 8/6/2019 D4 Universiti Teknologi MARA

    58/60

    Next Step Pilot Plant

    Condenser

    Char Collector

    Pyrolyser10 kg/h

    Conveyer Dryer

    Pyrolyzer

    H2O

    Char

    Bi-oil

    W e t

    B i o m

    a s s

    W e t

    B i o m

    a s s

    Resin

    ElectricityGas(H2)

    Gas(H2)

    GasEngine

    s orFuelCells

    Gasifier

    SteamReformer

    Route1b

    R o u t

    e1

    R o u t

    e2

    Route1a

    Route1c

    O p t i o

    n1

    O p t i o

    n 3

    Option 2

    Option2a

    Option 2b

    Water

    LightOlefine, CO 2

    Oxidizer

    EsterifierH2O2 Ethanol

    D i s t i l l er

    y

    LowTemperatureHydrogenation

    HighTemperatureHydrogenationH

    2

    H2

    H2 ZSM-5

    400-500 oC

    SteamActivato

    rAdsorbentActivated

    CarbonFertilize

    rabsorb

    er

    Slow ReleaseFertilizer

    O

    OH

    OH

    O

    OH

    OH

    OH

    OH

    OH

    OHOH

    OH

    OH

    CH 3

    OH

    OH

    OH

    OH

    CH 3

    OH

    OH

    OH

    OH

    OH

    OH

    OH

    OH

    O

    O

    H

    O

    O

    O

    O

    H

    O

    O

    O

    O

    O

    OH OH

    OO

    O

    OH

    O

    O

    OH

    OH

    O

    OH

    O

    OO

    OH

    OHO OH

    OH Polymerizer

    (to SteamReformer

    orFurnace)

    Light Alkane

    Bio-oil Tank

    Bio-oil forRefining

    Novelty of this Process

  • 8/6/2019 D4 Universiti Teknologi MARA

    59/60

    Novelty of this Process

    Compact and high throughput pyrolyser has been designed.

    A novel catalyst has been developed for bio-oil reforming.

    Bio-oil has been separated in high volatile fraction and highmolecular organic fraction.Novolac resin has been synthesized from organic fraction.

    Big particles of biomass can be pyrolysed as a fast heatingpyrolysis.

    High surface area activated carbon has been produced fromchar.

    Summary and Conclusion

  • 8/6/2019 D4 Universiti Teknologi MARA

    60/60

    Summary and Conclusion

    Gasification technology is almost ready for large scalepilot plant testing.

    For pilot plant, approximate costing may be RM 1,000,000 to5,000,000 depending on the plant size from 50 kg to 1 ton/h.

    Pyrolysis technology is ready for lab scale pilot plant withthe capacity of 20 kg/h 50 kg/h. Approximate costing maybe RM 2,000,000 for pyrolysis and refining setup.

    From bio-oil, liquid fuels, chemicals, materials includingbioplastic and resin and power can be produced.