BIOHYDROGEN GAS STRIPPING FORMED IN ANAEROBIC PROCESS OF HIGH-CONCENTRATION ARTIFICIAL WASTEWATER USING NITROGEN GAS FLUSHING
The use of biomass as a renewable energy source has become a primary focus to decrease reliance on fossil fuels and tackle environmental issues. Due to its high organic content, palm oil mill effluent (POME) holds significant potential as a feedstock for renewable energy generation, offering an a...
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id-itb.:870252025-01-10T08:22:24ZBIOHYDROGEN GAS STRIPPING FORMED IN ANAEROBIC PROCESS OF HIGH-CONCENTRATION ARTIFICIAL WASTEWATER USING NITROGEN GAS FLUSHING Rizqi Meutia, Raihannisa Teknik saniter dan perkotaan; teknik perlindungan lingkungan Indonesia Theses anaerobic, gas transfer, hydrogen, nitrogen flushing, palm oil mill effluent INSTITUT TEKNOLOGI BANDUNG https://digilib.itb.ac.id/gdl/view/87025 The use of biomass as a renewable energy source has become a primary focus to decrease reliance on fossil fuels and tackle environmental issues. Due to its high organic content, palm oil mill effluent (POME) holds significant potential as a feedstock for renewable energy generation, offering an alternative to food crops in bioenergy production. Renewable energy production from POME can be achieved through anaerobic bioconversion via fermentation. During the acidogenesis phase, bioenergy products such as bioethanol, biohydrogen, and volatile fatty acids can be produced. Several previous studies have investigated the conversion of POME waste into hydrogen, but the biohydrogen concentration remains relatively low. This is likely due to the majority of the hydrogen being dissolved in the liquid phase, making it difficult to measure directly. The addition of nitrogen flushing into the reactor aims to promote the release of dissolved biohydrogen into the gas phase. The effectiveness of hydrogen gas release is evaluated using mass transfer coefficients (kLa and kL) by varying the superficial gas velocity. The hydrodynamic properties of the gas bubbles formed are analyzed to understand the gas transfer process. An increase in the volumetric flow rate and superficial gas velocity positively affects the gas transfer process, with the optimum mass transfer coefficient achieved at a superficial velocity of 0.0079 m/s, yielding a mass transfer coefficient (kLa) and gas transfer coefficient (kL) of 0.00032 s-1 and 2.69×10-5 m/s, respectively. The application of nitrogen gas flushing with a gas superficial velocity of 0.0079 m/s in the processing of high organic artificial waste can increase hydrogen gas concentration, with a maximum concentration increase of 41.7% and the maximum biohydrogen concentration produced being 17.3%, achieved at a reaction time of 72 hours. text |
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Teknik saniter dan perkotaan; teknik perlindungan lingkungan Rizqi Meutia, Raihannisa BIOHYDROGEN GAS STRIPPING FORMED IN ANAEROBIC PROCESS OF HIGH-CONCENTRATION ARTIFICIAL WASTEWATER USING NITROGEN GAS FLUSHING |
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The use of biomass as a renewable energy source has become a primary focus to
decrease reliance on fossil fuels and tackle environmental issues. Due to its high
organic content, palm oil mill effluent (POME) holds significant potential as a
feedstock for renewable energy generation, offering an alternative to food crops in
bioenergy production. Renewable energy production from POME can be achieved
through anaerobic bioconversion via fermentation. During the acidogenesis phase,
bioenergy products such as bioethanol, biohydrogen, and volatile fatty acids can
be produced. Several previous studies have investigated the conversion of POME
waste into hydrogen, but the biohydrogen concentration remains relatively low.
This is likely due to the majority of the hydrogen being dissolved in the liquid phase,
making it difficult to measure directly. The addition of nitrogen flushing into the
reactor aims to promote the release of dissolved biohydrogen into the gas phase.
The effectiveness of hydrogen gas release is evaluated using mass transfer
coefficients (kLa and kL) by varying the superficial gas velocity. The hydrodynamic
properties of the gas bubbles formed are analyzed to understand the gas transfer
process. An increase in the volumetric flow rate and superficial gas velocity
positively affects the gas transfer process, with the optimum mass transfer
coefficient achieved at a superficial velocity of 0.0079 m/s, yielding a mass transfer
coefficient (kLa) and gas transfer coefficient (kL) of 0.00032 s-1 and 2.69×10-5 m/s,
respectively. The application of nitrogen gas flushing with a gas superficial velocity
of 0.0079 m/s in the processing of high organic artificial waste can increase
hydrogen gas concentration, with a maximum concentration increase of 41.7% and
the maximum biohydrogen concentration produced being 17.3%, achieved at a
reaction time of 72 hours. |
format |
Theses |
author |
Rizqi Meutia, Raihannisa |
author_facet |
Rizqi Meutia, Raihannisa |
author_sort |
Rizqi Meutia, Raihannisa |
title |
BIOHYDROGEN GAS STRIPPING FORMED IN ANAEROBIC PROCESS OF HIGH-CONCENTRATION ARTIFICIAL WASTEWATER USING NITROGEN GAS FLUSHING |
title_short |
BIOHYDROGEN GAS STRIPPING FORMED IN ANAEROBIC PROCESS OF HIGH-CONCENTRATION ARTIFICIAL WASTEWATER USING NITROGEN GAS FLUSHING |
title_full |
BIOHYDROGEN GAS STRIPPING FORMED IN ANAEROBIC PROCESS OF HIGH-CONCENTRATION ARTIFICIAL WASTEWATER USING NITROGEN GAS FLUSHING |
title_fullStr |
BIOHYDROGEN GAS STRIPPING FORMED IN ANAEROBIC PROCESS OF HIGH-CONCENTRATION ARTIFICIAL WASTEWATER USING NITROGEN GAS FLUSHING |
title_full_unstemmed |
BIOHYDROGEN GAS STRIPPING FORMED IN ANAEROBIC PROCESS OF HIGH-CONCENTRATION ARTIFICIAL WASTEWATER USING NITROGEN GAS FLUSHING |
title_sort |
biohydrogen gas stripping formed in anaerobic process of high-concentration artificial wastewater using nitrogen gas flushing |
url |
https://digilib.itb.ac.id/gdl/view/87025 |
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