Elucidating the solid, liquid and gaseous products from batch pyrolysis of cotton-gin trash.
Cotton-gin trash (CGT) was pyrolyzed at different temperatures and reaction times using an externally-heated batch reactor. The average yields of output products (solid/char, liquid/bio-oil, and gaseous) were determined. The heating value (HV) of CGT was measured to be around 15-16 MJ kg- 1 (6500-70...
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ndltd-tamu.edu-oai-repository.tamu.edu-1969.1-ETD-TAMU-24252013-01-08T10:39:36ZElucidating the solid, liquid and gaseous products from batch pyrolysis of cotton-gin trash.Aquino, Froilan Ludanapyrolysiscotton-gin trashbio-oilcharsyn-gastarCotton-gin trash (CGT) was pyrolyzed at different temperatures and reaction times using an externally-heated batch reactor. The average yields of output products (solid/char, liquid/bio-oil, and gaseous) were determined. The heating value (HV) of CGT was measured to be around 15-16 MJ kg- 1 (6500-7000 Btu lb-1). In the first set of tests, CGT was pyrolyzed at 600, 700, and 800°C and at 30, 45, and 60 min reaction period. The maximum char yield of 40% by weight (wt.%) was determined at 600°C and 30 min settings, however, the HV of char was low and almost similar to the HV of CGT. A maximum gas yield of 40 wt.% was measured at 800°C and 60 min and the highest liquid yield of 30 wt.% was determined at 800°C and 30 min. In the modified pyrolysis test, the effects of temperature (500, 600, 700, and 800°C) on the product yield and other properties were investigated. The experiment was performed using the same reactor purged with nitrogen at a rate of 1000 cm3 min-1. Gas yield increased as temperature was increased while the effect was opposite on char yield. The maximum char yield of 38 wt.% was determined at 500°C and 30 min. The char had the largest fraction in the energy output (70-83%) followed by gas (10-20%) and bio-oil (7- 9%). Maximum gas yield of 35 wt.% was determined at 800°C. The average yield of CO, H2 and total hydrocarbons (THC) generally increased with increased temperature but CO2 production decreased. Methane, ethane, and propane dominated the THC. The bio-oil yield at 600°C was the highest at about 30 wt.% among the temperature settings. The HV of bio-oil was low (2-5 MJ kg-1) due to minimal non-HC compounds and high moisture content (MC). A simple energy balance of the process was performed. The process was considered energy intensive due to the high amount of energy input (6100 kJ) while generating a maximum energy output of only 10%. After disregarding the energy used for preparation and pyrolysis, the energy losses ranged from 30-46% while the energy of the output represent between 55-70% of the input energy from CGT.Capareda, Sergio C.2010-01-15T00:06:45Z2010-01-16T00:32:12Z2010-01-15T00:06:45Z2010-01-16T00:32:12Z2007-122009-05-15BookThesisElectronic Thesistextelectronicapplication/pdfborn digitalhttp://hdl.handle.net/1969.1/ETD-TAMU-2425http://hdl.handle.net/1969.1/ETD-TAMU-2425en_US |
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pyrolysis cotton-gin trash bio-oil char syn-gas tar |
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pyrolysis cotton-gin trash bio-oil char syn-gas tar Aquino, Froilan Ludana Elucidating the solid, liquid and gaseous products from batch pyrolysis of cotton-gin trash. |
description |
Cotton-gin trash (CGT) was pyrolyzed at different temperatures and reaction
times using an externally-heated batch reactor. The average yields of output products
(solid/char, liquid/bio-oil, and gaseous) were determined. The heating value (HV) of
CGT was measured to be around 15-16 MJ kg- 1 (6500-7000 Btu lb-1). In the first set of
tests, CGT was pyrolyzed at 600, 700, and 800°C and at 30, 45, and 60 min reaction
period. The maximum char yield of 40% by weight (wt.%) was determined at 600°C and
30 min settings, however, the HV of char was low and almost similar to the HV of CGT.
A maximum gas yield of 40 wt.% was measured at 800°C and 60 min and the highest
liquid yield of 30 wt.% was determined at 800°C and 30 min. In the modified pyrolysis
test, the effects of temperature (500, 600, 700, and 800°C) on the product yield and other
properties were investigated. The experiment was performed using the same reactor
purged with nitrogen at a rate of 1000 cm3 min-1. Gas yield increased as temperature was
increased while the effect was opposite on char yield. The maximum char yield of 38
wt.% was determined at 500°C and 30 min. The char had the largest fraction in the
energy output (70-83%) followed by gas (10-20%) and bio-oil (7- 9%). Maximum gas yield of 35 wt.% was determined at 800°C. The average yield of CO, H2 and total
hydrocarbons (THC) generally increased with increased temperature but CO2 production
decreased. Methane, ethane, and propane dominated the THC. The bio-oil yield at 600°C
was the highest at about 30 wt.% among the temperature settings. The HV of bio-oil was
low (2-5 MJ kg-1) due to minimal non-HC compounds and high moisture content (MC).
A simple energy balance of the process was performed. The process was considered
energy intensive due to the high amount of energy input (6100 kJ) while generating a
maximum energy output of only 10%. After disregarding the energy used for preparation
and pyrolysis, the energy losses ranged from 30-46% while the energy of the output
represent between 55-70% of the input energy from CGT. |
author2 |
Capareda, Sergio C. |
author_facet |
Capareda, Sergio C. Aquino, Froilan Ludana |
author |
Aquino, Froilan Ludana |
author_sort |
Aquino, Froilan Ludana |
title |
Elucidating the solid, liquid and gaseous products from batch pyrolysis of cotton-gin trash. |
title_short |
Elucidating the solid, liquid and gaseous products from batch pyrolysis of cotton-gin trash. |
title_full |
Elucidating the solid, liquid and gaseous products from batch pyrolysis of cotton-gin trash. |
title_fullStr |
Elucidating the solid, liquid and gaseous products from batch pyrolysis of cotton-gin trash. |
title_full_unstemmed |
Elucidating the solid, liquid and gaseous products from batch pyrolysis of cotton-gin trash. |
title_sort |
elucidating the solid, liquid and gaseous products from batch pyrolysis of cotton-gin trash. |
publishDate |
2010 |
url |
http://hdl.handle.net/1969.1/ETD-TAMU-2425 http://hdl.handle.net/1969.1/ETD-TAMU-2425 |
work_keys_str_mv |
AT aquinofroilanludana elucidatingthesolidliquidandgaseousproductsfrombatchpyrolysisofcottongintrash |
_version_ |
1716504004978016256 |