the study of lpg adsorption ability using carbon adsorbent test bed for carbon adsorbent prepared...
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The Study of LPG Adsorption Ability Using Carbon Adsorbent
Test Bed for Carbon Adsorbent
Prepared from Waste Materials
The Study of LPG Adsorption Ability Using Carbon Adsorbent
Test Bed for Carbon Adsorbent
Prepared from Waste Materials
Imran Syakir Mohamad
Safarudin Gazali Herawan, Mohd Haizal Mohd Husin,
Ahmad Anas Yusof, Ernie Mat Tokit, Imanurezeki Mohamad
Kolej Universiti Teknikal Kebangsaan Malaysia
Farid Nasir Hj AniUniversiti Teknologi Malaysia
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Carbon Adsorbent?
Type of carbon produced through exposing a source material such as wood or bone to very high temperatures in the presence of steam, air, or carbon dioxide.
Also known as Activated Carbon.
Able to attract and hold certain substances on the carbon surface.
This ability is called "adsorption".
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Why Carbon Adsorbent?
Can store gas by adsorption
Supply & availability - easy to get/find/buy
Low cost - economical
High capacity of storage
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LPG?
Generic name for
commercial propane, C3H8
commercial butane, C4H10
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Why LPG?
Alternative vehicle fuel
environmentally friendly
quieter, cleaner and economical
Compared to petrol, LPG are 63% less of CO, 40% less of HC, 82% less of NOx
Compared to diesel, LPG are 70% less of HC, 99% less of NOx
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Research Objective
To produce carbon adsorbent from coconut shell and oil palm shell (waste materials) for application in LPG storage technologies.
To develop a carbon adsorbent test bed that can be use to determine the LPG adsorptions capacity/ability.
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Experimental rig
First, design and develop the experimental rig to prepare the carbon adsorbent. Consist of
a reactor,
tube furnace,
suction blower and some accessories
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Experimental rig
Suction Blower - to remove volatile
matter
CO2 Gas - to activate the sample
N2 Gas - to obtain an inert
atmosphere
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Experimental rig
Reactor Tube Furnace
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Methodology
Collection of Raw Material
Oil palm shell and coconut shell
Preparation of Raw MaterialGrind and sieve to a size of 250μm - 425μm
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Methodology
Heat at 10oC/min of heating rate, heated up to peak temperature of 6000C and maintain for 60 minutes in 1.5 L/min of N2 flow.
50 grams of each formed particles feed into reactor, then install in the tube furnace.
Collection of Raw Material
Oil palm shell and coconut shell
Preparation of Raw MaterialGrind and sieve to a size of 250μm - 425μm
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Methodology
Repeat for 700°C and 800°C
For activation process, CO2 was then introduced into the reactor at 162 mL/min for 30 minutes.
Collection of Raw Material
Oil palm shell and coconut shell
Preparation of Raw MaterialGrind and sieve to a size of 250μm - 425μm
Heat at 10oC/min of heating rate, heated up to peak temperature of 6000C and maintain for 60 minutes in 1.5 L/min of N2 flow during pyrolysis
50 grams of each formed particles feed into reactor, then install in the tube furnace.
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Carbon Adsorbent Test Bed
Gas adsorption is regarded to be the primary methods of characterization for activated carbon.
Therefore, carbon adsorbent test bed has been developed.
To study the LPG adsorption ability.
Consists of :
two column, temperature controller, timer and gas detector.
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Carbon Adsorbent Test Bed
Gas Detector
FlowmeterColumn
Timer
Temp. Controller
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Carbon Adsorbent Test Bed
Timer for calculating the adsorption time up to saturated condition.
Gas detector to detect the flue gas after exposes to the sample.
The test will stop when the curves show the breakthrough (inlet = outlet concentration) for LPG at 5 mL/min of feeding.
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Results and Discussion
The results obtained from carbon adsorbent test bed are summarized in the graph.
More time to reach inlet concentration (Co) mean that more LPG is adsorbed in carbon adsorbent.
The more LPG adsorbed means this carbon adsorbent has a better adsorption capacity.
0
150
300
450
600Commercial
Oil Palm Shell
Coconut Shell
Peak temperature (°C)
600 700 800T
ime
to r
each
Co (
s)
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Results and Discussion
Adsorption of LPG for both prepared oil palm shell and coconut shell carbon adsorbent decreases due to the increment of peak temperature.
Temperature >, particle size >, due to agglomeration process, surface area <
Also might shrink or enlarge the pore size
0
150
300
450
600Commercial
Oil Palm Shell
Coconut Shell
Peak temperature (°C)
600 700 800T
ime
to r
each
Co (
s)
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Results and Discussion
Molecules of gases tend to adsorb most strongly in area where the pore diameter of the adsorbent is in similar size (Shepherd, 2001).
Therefore, this phenomenon may decrease the adsorption efficiency and most likely not suitable for adsorbing LPG.
0
150
300
450
600Commercial
Oil Palm Shell
Coconut Shell
Peak temperature (°C)
600 700 800T
ime
to r
each
Co (
s)
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Results and Discussion
The carbon adsorbent test bed experiment has proved that the commercial carbon adsorbent has better adsorption ability.
The result showed that it can adsorb LPG almost three times longer compared to the prepared samples.
0
150
300
450
600Commercial
Oil Palm Shell
Coconut Shell
Peak temperature (°C)
600 700 800T
ime
to r
each
Co (
s)
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Conclusion
The prepared carbons adsorbent have a capability to adsorb LPG even though it is not as good as the commercial product.
Even though the results is not so promising, this research have introduces an alternative technique to examine the adsorption ability of LPG by using the carbon adsorbent test bed.
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Conclusion
Work is still in progress to increase the LPG storage capacity in the carbon adsorbent by improving the preparation techniques and testing device.
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Acknowledgements
Short-term research grant from Ministry of Education.
Faculty of Mechanical Engineering, KUTKM
Academic Service Centre, KUTKM
Faculty of Mechanical Engineering, UTM
University-Industry Centre, KUTKM