Published at : 25 Nov 2019
Volume : IJtech
Vol 10, No 6 (2019)
DOI : https://doi.org/10.14716/ijtech.v10i6.3695
Eny Kusrini | Department of Chemical Engineering, Faculty of Engineering, Universitas Indonesia, Kampus UI-Depok, Depok 16424, Indonesia |
Shella Wu | Department of Chemical Engineering, Faculty of Engineering, Universitas Indonesia, Kampus UI-Depok, Depok 16424, Indonesia |
Bambang Heru Susanto | Department of Chemical Engineering, Faculty of Engineering, Universitas Indonesia, Kampus UI-Depok, Depok 16424, Indonesia |
Maya Lukita | Department of Chemical Engineering, Faculty of Engineering, Universitas Indonesia, Kampus UI-Depok, Depok 16424, Indonesia |
Misri Gozan | Department of Chemical Engineering, Faculty of Engineering, Universitas Indonesia, Kampus UI-Depok, Depok 16424, Indonesia |
Muhammad Dicky hans | Department of Chemical Engineering, Faculty of Engineering, Universitas Indonesia, Kampus UI-Depok, Depok 16424, Indonesia |
Arif Rahman | Department of Chemistry, Faculty of Mathematics & Natural Sciences, Universitas Negeri Jakarta, Rawamangun 13220, Indonesia |
Volkan Degirmenci | School of Engineering, The University of Warwick, Coventry CV4 7AL, UK |
Anwar Usman | Department of Chemistry, Faculty of Science, Universiti Brunei Darussalam, Jalan Tungku Link, Gadong BE1410, Negara Brunei Darussalam |
This study examined
the effects of acid/base activation and chitosan coating on clinoptilolite zeolite
as an adsorbent for biogas purification from palm oil mill effluent (POME)
using simultaneous absorption–adsorption methods. The effects of chitosan
concentration in the clinoptilolite zeolite/chitosan (ZAC) composites were
studied to determine the best type of adsorbent for purifying biogas to obtain
the highest methane (CH4) concentration: the biogas produced from
POME via an anaerobic digestion process had a CH4 concentration of
87% and a carbon dioxide (CO2) concentration of 13%. In this study, the
Ca(OH)2 solution was used for the absorption process, and the ZAC
composite was used as the adsorbent in the adsorption process. To enhance the
adsorption efficiency of the adsorbent when purifying biogas, clinoptilolite
zeolite (ZA) was activated using strong acid (HCl) and base (NaOH) in various
concentrations (ranging from 1–3 M), calcination at 450°C for 2 h, and coating
with chitosan concentrations (ranging from 0.25–1 v/v%). The ZA was coated with
chitosan to increase its adsorption efficiency, as chitosan contains high
levels of amine and hydroxyl groups that interact with CO2
impurities and form carbamic acid, ultimately producing carbamate salt. The
composition of biogas before and after treatment was analyzed using gas
chromatography. Overall, the final content of
the biogas after the purification process with absorption using the Ca(OH)2
solution and adsorption in a fixed-bed column using the ZAC2-0.5 composite was
0.42% CO2 and 99.58% CH4. The purified biogas
had a very high methane gas content; thus, this study’s findings suggest that
purified biogas can be used as a clean energy source for wider industrial
applications.
Biogas purification; Chitosan; Clinoptilolite zeolite; Composite; Methane content; Simultaneous absorption–adsorption
The production and utilization
of biogas for green energy in wider industrial applications and cleaner fuels
has attracted a great deal of attention for many countries. It is necessary to
purify raw
biogas to enhance its energy content; this is done by removing impurities such
as CO2, H2S, and water vapor. This increases the methane
purity of the biogas, making it possible
to inhibit corrosion when used in pipelines and other instruments such as column
reactor and machine. This also has implications for new green energy, reducing
the economic losses from maintenance and operational costs for this devices and
also pipelines (Bak et al., 2019).
In
contrast, enriching biogas has the potential to replace natural gas in future
altogether, as biogas can be used in electricity production in co-generation
with heat and power (Kadam & Panwar, 2017). The amount of CH4
is increased and concentrated in enriched biogas to achieve a similar
composition and the same standards as a natural gas, allowing it to be used as
transportation fuel and in pipeline systems for household use. Biogas can also
be converted into a liquid form using cryogenic freezing, chilling the gas to
-80°C and then
further chilling it to -162°C (Kadam & Panwar, 2017). This method makes it more economical to compress and
transport the biogas over longer distances for further applications.
Huge increases in the price of fossil fuels since 2008 due to the economic crisis have prompted researchers to study methods of upgrading biogas since 19th century (Osman et al., 2019). Enriching biogas involves removing unwanted gases such as CO2, H2S, and water vapor to increase its calorific value and specific heat and minimize its corrosive nature caused by the acidic gases it contains (Leonzio, 2016; Kusrini et al., 2017). Its high CO2 content results in low calorific value, and further purification of the resultant gas to remove CO2 is required. Some methods for purification include pressure swing adsorption, adsorption, and chemical absorption (Ackley et al., 2003; Alonso-Vicario et al., 2010; Leonzio, 2016). Masyhuri et al. (2013) purified biogas using a Ca(OH)2 solution. Kusrini et al. (2018) captured CO2 using graphite waste composites and ceria. In terms of the adsorptive purification of biogas, researchers have used adsorbents containing physisorption, such as activated carbon and zeolite. Chemisorption efforts have utilized iron oxide and iron oxide hydroxide (Bak et al., 2019). The most-used substances for biogas purification are activated carbon and zeolite (Alonso-Vicario et al., 2010; Peluso et al., 2019).
This study
successfully modified clinoptilolite zeolites via acid/base activation,
calcination, and coating with chitosan and applied them as an adsorbent to purify
biogas from POME using simultaneous absorption and adsorption methods. The
modification changed the structure of the clinoptilolite zeolites, making them
highly effective as an adsorbent to remove CO2 from biogas. The final content of the biogas after the purification process with
absorption with the Ca(CO)2 solution and adsorption in a fixed-bed
column using the ZAC2-0.5 composite was the most effective, with a composition
of CH4 (99.58%) and CO2 (0.42%). The resultant
purified biogas had a very high methane gas content (99.58%) and very low concentration of impurities. This study
recommends that biogas produced via purification using a Ca(OH)2
solution and a ZAC-0.5 composite be used as a clean energy source for wider
industrial applications.
We thank the Ministry of
Agriculture, Republic of Indonesia through Grant of Kerjasama Kemitraan
Penelitian dan Pengembangan Pertanian Nasional (KKP3N) No.
54.30/HM.240/I.1/3/2016.
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