ABSTRACT
Over the years fossil fuel has been the major source of
energy, this fuel after passing through the process of fraction distillation
produces different products used for power generation for the industrial sector
likewise for domestic consumption therefore increasing its demand as well as
price. Fossil fuel as a non-renewable source of energy tends to exhibit some
flaws. Due to its non-renewable nature it emits pollutants during processing
and consumption. This necessitated the need for an alternative source of energy
called bio-energy. Bio-energy is produced from the fermentation of biomaterials
in an anaerobic environment. It can be used as a fuel or as starting material
for the production of chemicals, hydrogen and/or synthesis gas etc. The main
constituents of biogas are carbon dioxide (CU2), hydrogen suiphide (H2S), water
vapour with negligible quantities of contaminants, such as ammonia (NH3),
methyl siloxanes, nitrogen (N2), oxygen (02), halogenated volatile organic
compounds (VOCs), carbon monoxide (CU) and hydrocarbons. These contaminants
presence and quantities depend largely on the biogas source. Howeyer, its
hydrogen sulphide and carbondioxide content must be eliminated to avoid
possible damages to equipment and hazards to users and the environment. To do
this three stage purification methods was used, the first stage involve removal
of H2S using iron chips followed by the removal of CO2using sodium hydroxide
then silica gel was used to get rid of moisture in the gas. Afterwards analysis
was carried out in other to ascertain the percentage constituents of both the
raw and purified biogas using Pascal's Manometric glass tube technique. Also to
determine the level of purity of the biogas. The result gotten after the
purification showed biogas, CO2, and H2S content of 97.54-95.13%, 2.54-1.87%,
and 2-0.5 ppm respectively in the biogas produced against the initial raw
biogas content of 74.8-70.6 % o, 29.1-25.2 of CO2and 50-35 ppm of H2S. With a
lower heat valve (LHV) of 9.8± 0.2 for purified gas and 7.1± 0.2 for raw
biogas. from the result of the analysis it can be concluded that the removal of
these contaminants especially H2S and CO2significantly improved the quality of
the biogas for its further uses.
ONYEANUSI, B (2021). Construction And Modification Of An Organic Biodigester As Heating Source For Biogas Production. Repository.mouau.edu.ng: Retrieved Nov 22, 2024, from https://repository.mouau.edu.ng/work/view/construction-and-modification-of-an-organic-biodigester-as-heating-source-for-biogas-production-7-2
BRIGHT, ONYEANUSI. "Construction And Modification Of An Organic Biodigester As Heating Source For Biogas Production" Repository.mouau.edu.ng. Repository.mouau.edu.ng, 17 Nov. 2021, https://repository.mouau.edu.ng/work/view/construction-and-modification-of-an-organic-biodigester-as-heating-source-for-biogas-production-7-2. Accessed 22 Nov. 2024.
BRIGHT, ONYEANUSI. "Construction And Modification Of An Organic Biodigester As Heating Source For Biogas Production". Repository.mouau.edu.ng, Repository.mouau.edu.ng, 17 Nov. 2021. Web. 22 Nov. 2024. < https://repository.mouau.edu.ng/work/view/construction-and-modification-of-an-organic-biodigester-as-heating-source-for-biogas-production-7-2 >.
BRIGHT, ONYEANUSI. "Construction And Modification Of An Organic Biodigester As Heating Source For Biogas Production" Repository.mouau.edu.ng (2021). Accessed 22 Nov. 2024. https://repository.mouau.edu.ng/work/view/construction-and-modification-of-an-organic-biodigester-as-heating-source-for-biogas-production-7-2