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Friday, 31 March 2017

Improved Physical and Chemical Properties of Rubber Wood (Hevea brasiliensi

Author
Mohammed Nasir, Othman Sulaiman, Rokiah Hashim, Noor Afeefah Nordin and Mohd Asim

Abstract 

Cellulose and lignin are the two most abundant polymers found in plant cells. Cellulose microfibrils provide mechanical properties to woody cell whereas, hemicelluloses and lignin act as glue in between the crystalline cellulose. Cellulose crystallinity directly affects the physico-chemical behavior of the individual fiber such as modulus, hardness, stiffness, tensile and swelling-shrinkage properties and ultimately to its product. This study aims to improve the physico-chemical properties of rubber wood fiber by laccase hydrolysis in order to improve the crystalline structure. Two different times of reactions i.e., 60 and 120 min were applied at constant temperature 25°C, enzyme concentration 7 U g‾1 and pH 5. After the pulp treatment, fibers were sieved out and transferred in to autoclave at 121°C for 15 min to stop further enzyme reaction. Treated fiber was dried in electric oven drier at 80-90°C for 24 h to dry up the fiber until zero moisture content. Crystallinity index of the fiber was measured by X-ray diffraction method and it was observed maximum up to 14% higher compared to untreated fiber. The treated fiber was further analyzed for elemental composition, FE-SEM and TGA and compared with untreated fiber in order to evaluate its properties. Fiber treated with enzyme exhibited superiority in fiber surface structure and thermal degradation over untreated fibers. A fiber with improved mechanical strength and crystalline structure can be utilized for various purposes to produce high quality product.

 How to cite this article:

Mohammed Nasir, Othman Sulaiman, Rokiah Hashim, Noor Afeefah Nordin and Mohd Asim, 2015. Improved Physical and Chemical Properties of Rubber Wood (Hevea brasiliensis) Fiber by Laccase. Asian Journal of Agricultural Research, 9: 166-172.

DOI: 10.3923/ajar.2015.166.172 

URL: http://scialert.net/abstract/?doi=ajar.2015.166.172 
 


Received: May 04, 2015; Accepted: June 13, 2015; Published: July 01, 2015

INTRODUCTION
Wood cell walls are composed of cellulose, hemicelluloses and lignin (Stefanidis et al., 2014). The mechanical property of wood fibers is mainly determined by cellulose and hemicelluloses, whereas lignin acts as an adhesive between the fibers (Winandy and Rowell, 2005Gea et al., 2011). Cellulose is a long polymer chain of linear crystalline interrupted with regular amorphous region, primarily responsible for strength in the wood fiber (Stefanidis et al., 2014Nazir et al., 2013). Hemicelluloses are amorphous, highly branched polymer compared to cellulose (Zhou et al., 2009), as a linkage between cellulose and lignin. Lignin, on the other hand, is an amorphous phenolic compound that functions as a cementing material and stiffening agent for the cellulose molecules within the fiber cell wall (El Mansouri et al., 2007). Most of the lignin is found inside the cell wall as an intra-cellular lignin (70%), the rest are found in the middle lamella as extracellular lignin (Tuor et al., 1995Kunamneni et al., 2007).
Laccase is a well-studied oxido-reductase enzyme, it takes part in polymerization as well as depolymerization of lignin compound through free radical reaction (Nasir et al., 2013). Since, laccase enzymes are too large to penetrate into fibers (55-80 kDa), it modifies the amorphous extracellular component only (Gochev and Krastanov, 2007). Hence, due to a size exclusion reasons, laccase treatment is only a surface modification and it alters extracellular lignin without affecting the cellulose fiber. Although, several researchers have studied the enzymatic hydrolysis of lingo-cellulosic fiber but the changes in physical and mechanical properties of fiber is still not fully understood (Yaropolov et al., 1994Kharazipour et al., 1997). Thus, this study deals the pretreatment reaction of laccase at two different times, on natural fiber and the result was compared with untreated fiber. Such improved fibers can be used in many industrial applications like fiber board, pulp and paper industries etc (Virk et al., 2012Nasir et al., 2013Wu et al., 2011). This work aims to improve the physico-chemical properties of rubber wood fiber by laccase hydrolysis in order to improve the crystalline structure.
MATERIALS AND METHOD
Material: A thermo-mechanically processed pulp of rubber wood fibers was supplied by Robin Resources (Malaysia) Sdn. Bhd. The pulp was then air dried to moisture content of 15-20% before applying any treatment. Laccase enzyme (Novo WA 20040) was supplied by Novozyme, Malaysia.

Enzymatic pulp treatment: About 25 g of oven dried wood fibers of was suspended in 475 g of deionized water to make a solution of 5.0% consistency (mass pulp/mass suspension) in a 2 L Erlenmeyer flasks. A buffer solution of sodium acetate and acetic acid was used to maintain the pH. Two different reaction time (60 and 120 min) were applied at constant temperature of 25°C, enzyme concentration of 7 U g–1 and pH 5 (Nasir et al., 2014). The two treatment were named as FT1 (Fiber treated) and FT2 when treated at 60 and 120 min, respectively, whereas untreated was named as UT in later part of result and discussion. After each pulp treatment, fibers were sieved out immediately from the solution and transferred in to autoclave at 121°C for 15 min to stop further enzyme reaction. Treated fiber was dried in electric oven drier at 80-90°C for 24 h to dye up the fiber until zero moisture content.
Elemental analysis: Elemental analysis of treated and untreated fiber was performed in Central Laboratory, University Malaysia Pahang. Samples were analyzed on Varo Macro Cube, S/N-2012/1005, by simple combustion process.
Crystallinity: X-ray measurements were conducted on a Rigaku MiniFlex II, bench top X-ray Diffractometer (XRD) analyzers. The fiber specimens were pressed at 10 t hydraulic pressure into a circular shape of a tablet with 14 mm diameter and 0.5 mm of thickness. The X-ray diffractometer was operated at a voltage of 30 kV with a current density of 15 mA. The scanning range was from 2q = 10-50° at a scan speed of 0.015° sec–1. The data was collected using a fixed time mode with angular intervals of 0.015°. The method adopted was based on Kim and Holtzapple (2005). Crystallinity Index (Crl) was calculated from Eq. 1:
(1)
where, I002 is the intensity of the diffraction from the 002 plane 2θ = 22.0-23.0 and Iam is the intensity of the background scatter measured at 2θ = 16.0–18.0.
RESULTS AND DISCUSSION
Fiber crystallinity index: An initial experiment was cried out to understand the real effect of laccase treatment on rubber wood fiber. Figure 1 exhibited, the untreated fibers having the least crystallinity index of 65.5% whereas, it was improved in treated fibers to 76.4 and 72.87% in FT1 and FT2, respectively. The X-ray-based measurement of Crystallinity Index (CrI) indicates that laccase treatment increased the crystallinity of rubber wood and maximum was observed at 1 h of treatment time. However, the CrI started to reduce when the reaction was prolonged for 2 h. The change in crystallinity index was due to the removal of extracellular lignin from the fiber surface that ultimately improves the crystallinity (Lionetto et al., 2012Wu et al., 2011) but in the next 3 h fiber showed a decreasing trend. It was expected that a prolong treatment, lignin started to precipitate back on the fiber surface that results in the fall of crystallinity which is supported by the FE-SEM result (Kumar et al., 2009).

Elemental composition of treated fiber: Elemental composition (CHNS) of untreated fiber and treated fibers were analyzed. Table 1showed the mean of element percent of two tests’ result. The treated and untreated fibers exhibit a little difference. An untreated fiber displayed the lowest carbon percentage (C%) and highest hydrogen (H%) whereas, it was reverse in treated fibers. Since two processes, lignin breakdown and deposition taking place together, its elemental composition does not give a clear difference thus it was assume to be insignificant.
Microstructure analysis: Figure 2 depicted the FE-SEM picture of treated and untreated fiber at 5000x magnification. From the close view of micrograph, it was obvious that an enzyme treatment brought a distinguish change in the fiber surface. An Untreated Fiber (UT) had uneven furrowed surface whereas, a treated fibers have a very smooth surface. The uneven surface of wood fiber could be due to extra-cellular lignin found naturally on fiber surface which was either removed in lignification process or become even surface due to deposition. Furthermore, FT2 fiber exhibits slightly thicker layer of deposition as compared to the FT1 treated fiber.
Table 1:Elemental composition of treated and untreated fiber
UT: Untreated fiber, FT: Fiber treated, C: Carbon, H: Hydrogen, N: Nitrogen

Fig. 1:Fiber crystallinity index of treated at enzyme concentration of 7 U g–1 and pH 5

Fig. 2(a-c):FE-SEM of (a) UT, (b) FT1 and (c) FT2 treated fibers at different reaction condition at 5000x magnification
Although, laccase act specifically on lignin, the deposition composition should be studied thoroughly. Thus, it was concluded that the smoothness of the fiber surface could be due to the removal of loosely bonded lignin and then precipitation of the hydrolyzed lignin, as a smooth layer on the fiber surface which is similar to the finding of Kumar et al. (2009).
Thermogravimetric analysis (TGA) analysis of treated fiber: Thermal stability of treated and untreated fibers was analyzed on TGA. Thermal degradation of wood fibers occurs in two stages, it initiates from the amorphous cellulose at around 300°C followed by the crystalline cellulose degradation at a higher temperature around 350°C (Quintana et al., 2015). From the Table 2, it was observed that initial degradation of untreated fiber (UT) was started at temperature 331°C whereas, this temperature was found higher for treated fibers (FT1 and FT2). Final degradation temperature of treated fiber was also increased from 449°C of untreated fiber to 491°C of treated fiber. Among the treated fibers, FT1 exhibits higher degradation temperature as compared to FT2 due to its higher Crystallinity Index (CrI). Transition temperature (Tg) was calculated as a mid-point of onset and end point from TGA curve and summarized in Table 2. It was observed that Tg value of treated fiber was higher and increases with the increase in crystallinity of the fiber.
Figure 3 shows the DTA curves were all wood fibers (either treated or untreated fibers) exhibited two exothermic peaks overlapping with regions of weight loss (Jawaid and Khalil, 2011).
Fig. 3:Thermogravimetric analysis showing a two-step decomposition of fiber

Table 2:Transition temperature value and weight loss obtained from thermogravimetric analysis graph
Tg: Transition temperature, FT, Fiber treated, UT: Untreated fiber
The untreated rubber wood fiber started to degrade at 331°C were as this temperature was increased to 340 and 344°C for FT2 and FT1 samples, respectively. Therefore, it was concluded that a treated fiber were having a higher decomposition temperature as compared to untreated fiber (Li and Pickering, 2008).
CONCLUSION
Crystallinity index was observed maximum up to 76%, at 1 h enzyme reaction condition then after it decreased considerably and remained constant for a wide range of around 71-72%. Fiber treated with enzyme exhibited superiority in fiber surface structure and thermal degradation over other treated and untreated fibers. Thus, to obtain a highly crystalline and mechanically strong fiber, a thorough study of various reaction parameters such as time, concentration and temperature of the reaction is recommended. A fiber with improved mechanical strength and crystalline structure can be utilized for various purposes to produce high quality product.
ACKNOWLEDGMENTS
The authors acknowledged Universiti Sains Malaysia for Post-doctoral fellowship to Dr. Mohammad Nasir.
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Nasir, M., A. Gupta, M.D.H. Beg, G.K. Chua and M. Asim, 2014. Laccase application in medium density fibreboard to prepare a bio-composite. RSC Adv., 4: 11520-11527.
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Nasir, M., A. Gupta, M.D.H. Beg, G.K. Chua, M. Jawaid, A. Kumar and T.A. Khan, 2013. Fabricating eco-friendly binderless fiberboard from laccase-treated rubber wood fiber. BioResources, 8: 3599-3608.
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Economics of marketing wood fuel in south western Nigeria

Author
Olugbire O.O.Opute O.H.Aremu F.J.Ojedokun C.A. and Adisa A.
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Russian Journal of Agricultural and Socio-Economic Sciences, 2016, vol. 53, issue 5, pages 165-171

Abstract: Marketing of fuel wood is an important source of livelihood for most parts of Nigeria. The study examined the economics of marketing of wood fuel in south western Nigeria with a view to determine the socio-economic characteristics of the marketers, the profitability of marketing wood fuel, the market structure and constraints to profitability. Data for the study were obtained from a total sample of 100 randomly selected wood fuel marketers through interviews schedules and application of structured questionnaires. Descriptive statistics was used to analyze the socio-economic characteristics of the marketers. Cash analysis was used to determine the profitability of the enterprise while Gini-coefficient was used to examine the markets’ concentration. The result showed that majority of the marketers was in their active years as 51% were between 21-40 years of age. 71% were female while 56% of them were married. Most of the marketers (76%) had formal education and were well experienced in the business. Cash analysis revealed that marketing of wood fuel is profitable with an average Gross margin of 21,190.65 naira per month. The marketing efficiency was found to be 128% and the rate of return on investment was 28% which indicates that for every 100 naira investment in the business, the marketers will enjoy a return of 28 naira. The value of Gini-Coefficient (0.393) indicates high level of market concentration and inefficiency in the market structure. Transportation was the greatest constraint to the business profitability followed by season of the year and government policy.
Keywords: WOOD FUELMARKETPROFITABILITYNAIRAGINI-COEFFICIENT (search for similar items in EconPapers)
Date: 2016
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Effects of innovation on the European wood industry market structure

Author
Oscar AlfrancaRoberto VocesA. Casimiro Herruzo and Luis Diaz-Balteiro
Forest Policy and Economics, 2014, vol. 40, issue C, pages 40-47

Abstract: This study primarily aimed to contrast the potential relationships between innovation and market concentration. Thus, the relationship between innovation and the European wood industry market structure was analysed. An empirical model was assessed through panel techniques, wherein the wood industry market structure was explained through business-related variables and additional variables associated with generating innovation. The primary conclusion of this study with respect to the European wood industry is that R&D spending and R&D personnel are key factors in explaining market concentration. However, the influence of these variables may be affected by the initial degree of market concentration in the industry.
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Modelling and simulation of a wood solar dryer in a Moroccan climate

Author
F. BentayebN. Bekkioui and B. Zeghmati
Renewable Energy, 2008, vol. 33, issue 3, pages 501-506

Abstract: We present a numerical simulation of the functioning of a wood solar dryer in atmospheric conditions of Moroccan climate. A comparison of our numerical results with experimental measurements carried out on a wood solar dryer shows a good agreement. Results show that drying period is closely linked to glass partitions and timber thickness. The type of ventilation has no effect on the drying period (initial timber humidity lower than 40%). The substitution of east and west glass faces by concrete walls has practically no effect on drying period.
Keywords: SolarDryingClimateWoodSimulationVentilation (search for similar items in EconPapers)
Date: 2008
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A model of wood flash pyrolysis in fluidized bed reactor

Author
Zhongyang LuoShurong Wang and Kefa Cen
Renewable Energy, 2005, vol. 30, issue 3, pages 377-392

Abstract: With a view of exploiting renewable biomass energy as a highly efficient and clean energy, liquid fuel from biomass pyrolysis, called bio-oil, is expected to play a major role in future energy supply. At present, fluidized bed technology appears to have maximum potential in producing high-quality bio-oil. A model of wood pyrolysis in a fluidized bed reactor has been developed. The effect of main operation parameters on wood pyrolysis product distribution was well simulated. The model shows that reaction temperature plays a major important role in wood pyrolysis. And a good agreement between experimental and theoretical results was obtained. It was shown that particles less than 500 μm could achieve a high heating-up rate to meet flash pyrolysis demand.
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Depollution of atmospheric emissions of wood pyrolysis furnaces

Author
Kamel Halouani and Habib Farhat
Renewable Energy, 2003, vol. 28, issue 1, pages 129-138

Abstract: The wood carbonization in Tunisia consists essentially of traditional activity using charcoaling stacks and pits characterized by high atmospheric pollution and poor energy conversion. Indeed, 70% of the initial mass of anhydrous wood are found in the vapor as aerosols, polluting and toxic gases and complex condensable organic compounds that can cause a substantial pollution of air, ground and water. Several processes of treatment and energy valorization of such effluents were proposed, but the incineration remains at present the most promising technique of depollution. The results show that the incineration, at about 1000°C, of wood carbonization smokes allows the destruction of 99% of the mass of pollutants except CO2 and the reduction of polluting gas emission. The possible valorization of the smoke’s energy in the exit of the incinerator enhances the thermal efficiency of the process.
Keywords: Wood carbonizationPyrolysisCharcoalAtmospheric emissionsIncineration (search for similar items in EconPapers)
Date: 2003
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Future prospect and sustainability of wood fuel resources in Tanzania

Author
Mwema Felix
Renewable and Sustainable Energy Reviews, 2015, vol. 51, issue C, pages 856-862

Abstract: Tanzania is among the lowest income countries with the majority of the people living below a poverty line of less than US$ 2/day. Its energy sector is dominated by wood fuel, mainly charcoal and firewood with over 75% dependency. Wood resources for charcoal and firewood production are collected from a wide variety of tree species. The country has no formal biofuel policies thus leaving biofuel producers (including charcoal and firewood producers) without a reliable framework. This poses a danger to the forest resources and the environment. Little is known about the empirical findings on future prospect and sustainability of charcoal and firewood resources. This study reviewed over 100 articles on the state of the art of wood fuel resources in Tanzania, and the extent and degree of forest resource utilization and sustainability is assessed. Forest loss is estimated at 0.4 million ha per year. Results suggest that it would take about 85 years for all forest resources to be destroyed completely. Assuming year 2005 as a reference year, generations from year 2090 would be left with no forest resources to meet their needs. The study concludes that future prospect and sustainability of charcoal production and firewood harvesting in the country is at stake. Before any irreversible changes occur, it is therefore necessary to protecting forest resources using proper management strategies such as the use of alternative fuel resources, improved conversion technologies and deployment of participatory forest management.
Keywords: CharcoalElectricityTanzaniaWood fuelSustainability (search for similar items in EconPapers)
Date: 2015
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CLUSTERS: INNOVATION, KNOWLEDGE AND COMPETITIVENESS IN THE WOOD PROCESSING INDUSTRY

Author
Margareta Rusu-Tanasa
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SEA - Practical Application of Science, 2014, issue 6, pages 81-86

Abstract: This paper proposes an overview of the evolution in the wood processing industry in the process of regional development. The concept of clusters has become more and more popular in recent years, as more and more theorists and practitioners realize its potential; nevertheless the idea of cluster research in the wood processing industry is relatively new. With the shift to knowledge based management, the difference made by creative networks and clusters that promote research, development and innovation is crucial. The purpose of this paper is to underline the benefits that can come from cluster development and outline the impact of clusters on innovation, Knowledge and competitiveness in the wood processing industry and the Romanian Economy.
Keywords: CompetitivenessClusterInnovationKnowledgeWood processing industry (search for similar items in EconPapers)
JEL-codes: D83 F63 O32 O38 (search for similar items in EconPapers)
Date: 2014
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Global patterns and trends of wood harvest and use between 1990 and 2010

Author
Anna Liza S. BaisChristian LaukThomas Kastner and Karlheinz Erb
Ecological Economics, 2015, vol. 119, issue C, pages 326-337

Abstract: Wood biomass forms the basis for a variety of products and it represents an important source of technical energy. Woodfuels and forests play an important role for climate change mitigation, by their ability to replace fossil fuel and sequester atmospheric carbon. At the same time, wood extraction is an important driver for deforestation. However, large uncertainties relate to the amount and spatio-temporal pattern of wood use. We here present a comprehensive assessment of wood biomass flows in 11 world regions from 1990 to 2010. We found that global total biomass appropriation (TBA) amounts to 1.81GtC/year in 1990 and 1.94GtC/year in 2010 (+7%). In 2010, TBA represents 4% of the global forest net primary production. Only 54% of TBA enters socioeconomic systems while 46% remain in forests or represent waste flows. About 56% of economically used wood biomass enters the energy sector. There are considerable regional variations in wood biomass flows among world regions, owing to differences in population, affluence, and area. Global demand for wood is expected to increase in the near future, putting additional pressure to forest ecosystems. We discuss the potential of cascading use of wood as a means to reduce impacts related to resource use.
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Techno-economic analysis of wood biomass boilers for the greenhouse industry

Author
J. ChauT. SowlatiS. SokhansanjF. PretoS. Melin and X. Bi
Applied Energy, 2009, vol. 86, issue 3, pages 364-371

Abstract: The objective of this study is to perform a techno-economic analysis on a typical wood pellet and wood residue boiler for generation of heat to an average-sized greenhouse in British Columbia. The variables analyzed included greenhouse size and structure, boiler efficiency, fuel types, and source of carbon dioxide (CO2) for crop fertilization. The net present value (NPV) show that installing a wood pellet or a wood residue boiler to provide 40% of the annual heat demand is more economical than using a natural gas boiler to provide all the heat at a discount rate of 10%. For an assumed lifespan of 25 years, a wood pellet boiler system could generate NPV of C$259,311 without electrostatic precipitator (ESP) and C$74,695 with ESP, respectively. While, installing a wood residue boiler with or without an ESP could provide NPV of C$919,922 or C$1,104,538, respectively. Using a wood biomass boiler could also eliminate over 3000Â tonne CO2 equivalents of greenhouse gases annually. Wood biomass combustion generates more particulate matters than natural gas combustion. However, an advanced emission control system could significantly reduce particulate matters emission from wood biomass combustion which would bring the particulate emission to a relatively similar level as for natural gas.
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Advantages and Disadvantages of Fasting for Runners

Author BY   ANDREA CESPEDES  Food is fuel, especially for serious runners who need a lot of energy. It may seem counterintuiti...