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Synthesis of Carbon Molecular Sieve from Palm Shell Using Deposition of Polyfurfuryl Alcohol
Synthesis of Carbon Molecular Sieve from Palm Shell Using Deposition of Polyfurfuryl Alcohol
Journal of the Korean Chemical Society. 2010. Jun, 54(3): 323-328
Copyright © 2010, The Korean Chemical Society
  • Received : December 02, 2009
  • Accepted : March 30, 2010
  • Published : June 20, 2010
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About the Authors
V. M. Sivakumar
Kok-Keong Lam
Abdul Rahman Mohamed
chrahman@eng.usm.my

Abstract
In this work, an intention to synthesize the carbon molecular sieve (CMS) with ideal sieving properties from palm shell has been attempted. The process includes three main stages: carbonization, carbon dioxide activation and polymer deposition using polyfurfuryl alcohols. Palm shell based activated carbon (AC) produced by carbon dioxide activation was used as raw material in synthesis of CMS. After preparing palm shell based AC, optimum concentration ratio of furfuryl alcohols and formaldehyde to AC for CMS synthesis was obtained in this study. Deposition of polyfurfuryl alcohols on the palm shell based AC was then carried out prior to carbonization. These polymer deposited AC was subjected to carbonization at 700-900℃ under inert condition. All the microporous materials were analyzed using micromeritics ASAP/2020. The results show that optimum concentration ratio of furfuryl alcohol and formaldehyde to AC is 1:2.5. The micropore with pore width less than 7 Å was formed on the polymer deposited AC at 700℃, 800℃ and 900℃ for 1.5 hours. Carbonization temperature at 900℃ for 1.5 hours was found to be optimum for CMS synthesis. The CMS produced under this condition has pore width of 5.884 Å.
Keywords
INTRODUCTION
Over the last four decades, Malaysia has become the world largest palm oil producer and currently the industry is considered as backbone of agriculture in Malaysia occupying about 60% of the total cultivated land in the country. 1 These oil palm mills produce a lot of by-products, such as palm shell. Palm shell has high carbon content, especially after carbonization process. It is a good precursor for production of AC with high porosity. These activated carbons can possibly be converted into CMS through deposition method. 2 - 5
CMS can be defined as substances with discrete pore structures that can differentiate between molecules on the basis of size. CMS have most of the pores in the molecular size range allowing separation and purification of gas mixture by adsorption. 6 - 9 CMS are a special class of AC which may exhibit advantages over zeolite molecular sieves such as higher hydrophobicity, higher resistance to both alkaline and acid media, and thermal stability at high temperatures under non-oxidizing atmosphere. 10 It does not adsorb in appreciable amounts molecules larger than a particular size. This carbon may be referred to as a form of AC, distinct from peat, coconut-based, and other conventional activated carbon.
Several methods have been proposed for producing CMS since Emmett reported the molecular sieving property of a carbonized Saran in 1948. These can be done by several methods that are pyrolyzation method, 11 , 12 covering method 13 and carbon deposition method. 14 The majority of methods are intended to slightly modify the pores created by carbonization of carbonaceous materials. All these methods have been investigated on different activated carbons. Polymer deposition method, 15 which is one of the carbon deposition methods, on palm shell based AC is still a novel research yet to be done.
To carry out polymer deposition method, which is one of the carbon deposition methods, only polymers that do not undergo transformation to the thermodynamically preferred graphite phase at high temperatures can be used for CMS synthesis. This non-graphitizing character has been attributed to the presence of heteroatoms of cross-links between the polymer chains when pyrolyzed. This character is present in materials like polyfurfuryl alcohol (PFA) and polyacrylonitrile (PAN). Polyfurfuryl alcohol (PFA) 16 is chosen as the polymer to be used. This study aims to synthesize CMS from palm shell by a means of polyfurfuryl alcohol deposition method.
EXPERIMENT
- Material and Chemicals
The primary raw material employed in this research is palm shell, which was obtained from a local oil palm mill (United Palm Oil Mill Sdn. Bhd.). The palm shell was then cleaned, sieved and dried in the oven. It was further grinded and sieved to size of 2.0 mm. Besides that, the gases employed in carbonization and activation processes were nitrogen gas and carbon dioxide. Chemicals required for polymer deposition method were supplied by Sigma-Aldrich (M) Sdn. Bhd. They were furfuryl alcohol 99 wt %, phosphoric acid 85 wt % solution in water and formaldehyde 37 wt % solution in water.
- Preparation of Palm Shell Based AC
Approximately 100 g of the grinded and sieved palm shells was accurately weighed using a top-pan digital balance and charged into reactor of the carbonization rig. The reactor was then inserted into furnace gradually using electrical controller. The reactor with the sample was purged with pure nitrogen gas at pressure of 2 psi and flow rate of 500 mL/min for 15 minutes to remove air. Then the furnace was switched on and the samples were heated in a stream of nitrogen gas flow at 500 mL/min. Carbonization time begins when temperature reached 1100 ℃. Temperature was kept constant for 1 hour by the temperature controller of the furnace.
After this period, the supply of nitrogen was closed and valve of carbon dioxide was open instead. The pressure of carbon dioxide was set at 20 psi. The samples were then heated in a stream of carbon dioxide flowing constantly at 500 mL/min for 1 hour 30 minutes. After that, the furnace was switched off and the reactor was allowed to cool to room temperature under nitrogen gas flow. The product formed was then discharged from the reactor and characterization was carried out on it prior to subsequent processes.
- Polymerization of furfuryl alcohols
25 wt % furfuryl alcohol and 20 wt % formaldehyde were mixed in a flask containing AC and were then heated up to 80 ℃. 5 wt % H 3 PO 4 was added to the flask and the temperature was increased up to 100 ℃ for 2 hours.
- Preparation of CMS
PFA coated AC produced was charged into the reactor of carbonization rig. It was purged with pure nitrogen gas at pressure of 2psi and flow rate of 200 mL/min for 15 minutes to remove air. Then, the furnace was switched on. The samples were heated constantly at 200 mL/min. The reactor bed temperature was varied at 700 - 900 ℃ for 1.5 hours. After deposition process, the reactor was cooled to room temperature under constant flow of nitrogen. The product was removed from the reactor.
- Characterization
An ASAP/2020 Micromeritics was used to determine the surface area, micropore volume and the pore size distribution. The instrument is fully computerized high vacuum system, which allows the adsorption isotherms for each pressure step monitored in real time using computer algorithm. The reproducibility of the results was checked by preparing several samples under the same conditions and characterizing these samples by gas adsorption unit.
RESULTS AND DISCUSSION
- Preparation of palm shell based AC
AC synthesized by our group from palm shell in two different batches using identical preparation method was labelled as sample 1 and sample 2. 1 shows the comparisons between samples 1 and 2. It indicates that the AC synthesized can be employed for subsequent CMS synthesis and method used can produce an appropriate precursor for CMS synthesis.
Comparisons between samples 1 and 2 according to the summary report.
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Comparisons between samples 1 and 2 according to the summary report.
1 shows the adsorption isotherm of sample 1 and 2. Both curves were plateau when relative pressures approached 0.99. This implies that the adsorption has virtually achieved equilibrium and apparently stopped. It is because multilayer of adsorbates cannot be established due to close proximity of the pore wall.
These curves are categorized as type 1 adsorption isotherm. Sample 1 and 2 have type 1 adsorption isotherm and it shows that both samples 1 and 2 have microporosity development. Both samples are ideal raw material to synthesize CMS using PFA deposition method due to their identity as microporous materials. Besides that, it shows that the carbonization and activation process employed in producing AC is appropriate to achieve this objective. According to the 1 , sample 2 has higher equilibrium quantity adsorption capacity compared to sample 1. Sample 2 has higher micropore volume and exhibits the larger microporosity. It is also preferred as a base material for CMS synthesis.
T-plot. In the t-plot method, amounts adsorbed on the porous adsorbent are plotted against‘t’, the corresponding multilayer thickness of the standard non-porous solid. A straight t-plot curve starts from the origin corresponds to non-porous material whereas a linear curve intercepts at y-axis above origin corresponds to a microporous solid.
From 2 , it indicates that both samples are microporous solids. The slope passing through the origin provides a measure of total surface area of the solid. Sample 2 apparently has higher surface area than sample 1, according to the intercepts of both curves. Sample 2 has more pores and is a better base material for CMS synthesis.
BJH adsorption cumulative pore volume curve. The BJH adsorption cumulative pore volume curve can be used to characterize the AC. The pore size distributions of the AC for the sample 1 and 2 are shown in the 3 . The gradual increase in pore size distribution towards the smallest pore diameters as shown in the above plot implies the formation of micropores.
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Adsorption isotherm of AC (samples 1 and 2); Sample 1 (♦), sample 2(■).
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t-Plot of samples 1 and 2 using Harkins and Jura equation; Sample 1 (♦), sample 2(■).
The increase in the pore size distribution indicates that more micropores are exhibited by the sample. From 3 , it was observed that increase in micropore volume was more significant for the sample 2. Where as Sample 1 exhibited more mesopores than sample 2. As a matter of fact, AC with higher micropores is the ideal base material for CMS synthesis. In the nutshell, from the pore size distribution curves for both samples, it clearly shows that sample 2 is more ideal to be employed for CMS synthesis. This proves that the AC produced can be used for subsequent PFA deposition processes.
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BJH Adsorption cumulative pore volume of sample 1 and 2; Sample 1 (♦), sample 2(■).
- Polymerization and polymer coating on AC
Polymerization of furfuryl alcohol was effected by the concentration ratio of polymer to AC. We have considered three different concentration ratio of polymer i.e., 1:1, 1:2.5 and 1:5 to AC. For the concentration ratio of 1:5, there was 1 mole of both furfuryl alcohol and formaldehyde mixed with 5 mole of AC.
There was no apparent reaction of the mixture during heating and before and after adding phosphoric acid. During heating of the mixture, the liquid chemical evaporated and dried rapidly before it reached 80 ℃ (as shown in 4 ). Apparently, the amount of furfuryl alcohol and formaldehyde added was not enough and the amount of polymers formed were not enough to coat the surface and pores of the AC.
For the concentration ratio of 1:2.5, it was then turned into dark orange slowly as the heating proceeded (as shown in 5 ). Sticky polymers were formed in the end of the process. After 2 hours of drying, the product formed was attached to each other. It had to be made discreet as AC. There was an apparent shinny layer coating the AC. This product was referred to as polymer coated AC.
For concentration ratio of 1:1, the mixture turned colour from pale orange into milky orange as shown in 6 . The colour became darker and viscous. After drying for two hours, the product obtained was seemed to be shinny on the surface and clogged to each other. It was concluded that the polymer coating on the AC was too excessive in quantity. It might lead to fully closing of the pores, leaving no pore on the product at the end of subsequent heating. From these observations on different concentration ratios, it was concluded that the concentration ratio 1:2.5 was more suitable and optimum to be used for subsequent heating process.
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Final product for 1:5 ratio
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Final product for 1:2.5 ratio
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Final product for 1:1 ratio
- Synthesis of CMS
2 showed the conditions that had been used in synthesis of carbon molecular sieves under three different reaction temperatures. The reaction time was maintained constant at 1.5 hours for all the three cases.
3 shows the summary report of CMS-1, CMS-2 and CMS-3. According to 3 , all the samples have smaller surface area than AC. Surface area of AC produced is approximately 706 m 2 /g whereas surface area of the CMS samples produced was less than 240 m 2 /g. Approximately 465 m 2 /g surface area of AC eliminated due to the closure of pores by PFA. This is a typical phenomenon of CMS synthesis. The change in surface area before and after the carbonization indicates that the samples can be the desired product which was considered to be CMS. Besides that, by using Horvath-Kawazoe equation, the pore widths of these three samples were calculated to be less than 6.5 Å. It was within the range of pore width of CMS. Therefore, it implies that these three samples are certified as CMS.
Conditions used in producing samples 1, 2 and 3
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Conditions used in producing samples 1, 2 and 3
Adsorption isotherm. 7 shows the adsorption isotherm of sample CMS-1, CMS-2 and CMS-3. The data of quantity adsorbed at relative pressure (after P/P O = 0.0003) could not be obtained by the equipment. Therefore, the adsorption isotherm obtained is shown in 7 but yet it still can be used to compare the capacity and properties of respective samples. Based on 7 , CMS-3 that was produced under carbonization temperature of 900 ℃ for 1.5 hours has the highest equilibrium quantity adsorption capacity. This argument can be made based on the gradient of the curve. The steeper the curve is, the higher the equilibrium value it can achieve. That means that CMS-3 has the highest micropore volume and exhibits the largest microporous property. CMS-3 is the best CMS among all the synthesized CMS under different conditions. It also indicates that the optimum carbonization temperature was 900 ℃.
Comparisons among CMS-1, CMS-2 and CMS-3 according to the summary report.
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Comparisons among CMS-1, CMS-2 and CMS-3 according to the summary report.
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Adsorption isotherm of CMS-1, CMS-2 and CMS-3.
CONCLUSION
According to the experimental investigation, the following conclusions were drawn. AC was synthesized successfully from palm shell and applicable in PFA deposition method. The optimum concentration ratio of PFA to AC was 1:2.5. The large pores of the AC were successfully closed by PFA through carbonization of polymer coated AC under temperature of 700 ℃, 800 ℃ and 900 ℃ for 1.5 hours. The micropore with pore width less than 7Å was formed on the AC after the carbonization of polymer coated AC. It showed that all three samples prepared are proved to exhibit characteristics of CMS. Optimum carbonization temperature for CMS synthesis was at 900 ℃ for 1.5 hours. The CMS produced under this condition has pore width of 5.884 Å. It can be used for certain gas separation processes.
Acknowledgements
The authors gratefully acknowledge the financial support provided by the Ministry of Science, Technology and Innovations (MOSTI) under Science Fund (Project a/c No: 6013327) and Universiti Sains Malaysia for funding this project under RU Grant (Project a/c No: 814004)and Student Fellowship Scheme. Also, the author likes to extend his gratitude to Dr. D. Jagan Mohan for his scientific suggestions.
References
http://www.malaysiapalmoil.org/life/implanting.asp
Moreira R. F. P. M. , José H. J. , Rodrigues A. E. 2001 Carbon 39 2269 -    DOI : 10.1016/S0008-6223(01)00046-X
Zhang T. , Walawender W. P. , Fan L. T. 2005 Bioresource Technology 96 1929 -    DOI : 10.1016/j.biortech.2005.01.026
Vyas S. N. , Patwardhan S. R. , Vijayalakshmi S. , Bathula Gangadhar 1993 Fuel 72 551 -    DOI : 10.1016/0016-2361(93)90115-I
Wang L. J. , Chau-Nan Hong F. 2005 Microporous and Mesoporous Materials 77 167 -    DOI : 10.1016/j.micromeso.2004.09.001
Koresh J. E. , Soffer A. 1986 J. Chem. Soc., Faraday Trans. 1 82
Freitas M. M. A. , Figueiredo J. L. 2001 Fuel 80 1 -    DOI : 10.1016/S0016-2361(00)00066-1
LaCava A. I. , Koss V. A. , Wickens D. 1989 Gas Prep. Purif. 3 180 -    DOI : 10.1016/0950-4214(89)80003-9
Jüntgen H. , Knoblauch K. , Harder K. 1981 Fuel 60 817 -    DOI : 10.1016/0016-2361(81)90144-7
Satyendra P. , Walker P. L. 1976 Separation Science 11 441 -    DOI : 10.1080/01496397608085334
Wan Daud W. M. A. , Ahmad M. A. , Aroua M. K. 2007 Separation and Purification Technology 57 289 -    DOI : 10.1016/j.seppur.2007.04.006
Bello G. , Garcia R. , Arriagada R. , Escribano A. S. , Reinoso F. R. 2002 Microporousand Mesoporous Material 56 139 -    DOI : 10.1016/S1387-1811(02)00465-1
Freitas M. M. A. , Figueiredo J. L. 2001 Fuel 80 1 -    DOI : 10.1016/S0016-2361(00)00066-1
Kawabuchi Y. , Kishino M. , Kawano S. , Whitehurst D. D. , ochida I. 1996 Langmuir 12 4281 -    DOI : 10.1021/la960292a
Somanathan T. , Pandurangan A. , Sathiyamoorthy D. 2006 Journal of Molecular Catalysis A: Chemical 256 193 -    DOI : 10.1016/j.molcata.2006.04.052
Schmitt J. L. , Walker P. L. 1972 Carbon 10 87 -    DOI : 10.1016/0008-6223(72)90013-9