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Fuel 82 (2003) 919–927 www.fuelfirst.com Specific heat and thermal conductivity of softwood bark and softwood char particlesq Murlidhar Guptaa,b, Jin Yanga, Christian Roya,* a Department of Chemical Engineering, Université Laval, Pavillon Pouliot, Sainte-Foy, Que., Canada G1K 7P4 b CANMET Energy Technology Center, 1 Haanel Drive, Ottawa, Ont., Canada Received 5 August 2002; revised 28 November 2002; accepted 10 December 2002; available online 6 January 2003 Abstract Very few data exist regarding the thermal properties of softwood bark and therein derived softwood chars. This work describes the measurement of specific heat and particle thermal conductivity of softwood (SW), softwood bark (SB) and therein derived softwood char (SC). Differential scanning calorimetery (DSC) was used to measure the specific heat. At 313 K, the measured specific heat was found to be 1172, 1364 and 768 J kg21 K21 for SW, SB and SC, respectively. The specific heat of SW and SB increased linearly from 1172 to 1726 and 1364 to 1777 J kg21 K21, respectively, with an increase in temperature from 313 to 413 K. With an increase in temperature from 313 to 713 K, the specific heat of SC doubled from 768 to 1506 J kg21 K21 and followed a polynomial relationship with temperature. A modified Fitch apparatus was constructed, calibrated and used for measurement of particle conductivity of SW, SB and SC. The particle thermal conductivity of SB was found to be twice that of SC, i.e. 0.2050 and 0.0946 W m21 K21, respectively, at 310 K. The particle thermal conductivity of SW, SB and SC followed a linear increase with temperature. q 2003 Elsevier Science Ltd. All rights reserved. Keywords: Bark; Particle; Softwood; Char; Specific heat; Thermal conductivity; Heat transfer; Pyrolysis; Measurement 1. Introduction Significant volumes of lignocellulosic residues are generated annually by the forest industry. A large portion of these residues is made of softwood bark. The North American forest industry alone produces more than 35 Mt of softwood bark every year [1,2]. Approximately 50% of these barks is currently burned for energy production while the rest is disposed in landfills raising serious concerns to the ground-water pollution. Alternatively bark can be converted to energy and value added chemicals such as Biophene through the vacuum pyrolysis technology for example [3]. Knowledge of thermal properties such as specific heat and thermal conductivity is necessary, however, to design a vacuum pyrolysis system and to model complex heat transfer phenomena [4]. Thermal properties of wood are also widely needed in building construction, thermal conversion of biomass, wood * Corresponding author. Tel.: þ 1-418-656-7406; fax: þ1-418-656-2091. E-mail addresses: [email protected] (C. Roy), [email protected] (M. Gupta). q Published first on the web via Fuelfirst.com—http://www.fuelfirst.com drying, etc. A substantial amount of information can be traced in the literature for specific heat and thermal conductivity of wood [5 – 9].Thermal properties of woody materials are often influenced by various factors, such as the wood species, density, moisture, and fiber orientation. Moreover, it is very difficult to find data for softwood bark (SB) or softwood char (SC) derived from bark. The properties of wood charcoal are highly dependent on the source and the process conditions during the pyrolysis process. For determination of the specific heat of lignocellulosic materials, the method of mixtures is the most common method reported in the literature [10]. Although this technique is direct, it is not accurate [11]. Chakrabarty and Johnson [12] described the methodology for the determination of specific heat of tobacco by differential scanning calorimetry (DSC). Recently the DSC method has been frequently used to measure the specific heat of food and agricultural materials, i.e. peanut kernels, cumin seeds, etc. [11,13]. The advantage of DSC method over the conventional method is the accuracy and speed with which data can be obtained and the small sample size required [14, 0016-2361/03/$ - see front matter q 2003 Elsevier Science Ltd. All rights reserved. PII: S 0 0 1 6 - 2 3 6 1 ( 0 2 ) 0 0 3 9 8 - 8 920 M. Gupta et al. / Fuel 82 (2003) 919–927 Nomenclature A a cp cp;c cp;r cp;s mc heat transfer area of copper plug (m2) coefficient of linear thermal expansion for copper (1.65 £ 1025 K21) specific heat (J kg21 K21) specific heat of perfect conductor, copper (J kg21 K21) specific heat of reference (J kg21 K21) specific heat of sample (J kg21 K21) mass of copper plug (kg) 15]. Moreover, the dynamic nature of DSC allows the determination of specific heat as a function of temperature. Most of the published thermal conductivity measurements on wood samples are conducted with standard hotplate apparatus (steady state method), in which the samples were placed and left under constant conditions for a sufficient length of time to insure an uniform temperature gradient throughout the sample. The temperature of the test surfaces are then recorded, and the rate of heat flow calculated from the electric input to the heating element [16]. Recently Suleiman et al. [9] have developed and used a transient plane source (TPS) technique to measure the thermal conductivity of cylindrical shaped Swedish hardwood (birch) samples having a diameter of 30 mm and a thickness of 10 mm. Hot wire probe apparatus for measuring the thermal conductivity of small agricultural samples have been used by many workers [13,17]. To reduce the error, however, the ratio between the length and diameter of the probe has to be over 20 [18]. More than 99% of the particles in SB and SC samples used in this work were smaller than 7 mm [19]. Thus the probe method is still difficult to use in materials like SB and SC particles because of size constraints. The Fitch method [20] has been the most common transient methods used to measure the conductivity of poor conductors, such as food particles [10,21]. Zuritz et al. [18] developed a modified Fitch apparatus to measure the thermal conductivity of small food particles that can be formed into small slabs. In the present work, the specific heat and the thermal conductivity of bark and char derived were experimentally measured as a function of temperature. While DSC method has been used to measure the specific heat, the modified Fitch apparatus [18] has been used to measure the particle thermal conductivity of softwood (SW), SB and SC from bark. 2. Materials and methodology mr ms lp T T0 T1 Yr Ys weight of the reference (mg) weight of the sample (mg) particle thermal conductivity (W m21 K21) temperature (K) initial temperature of copper plug (K) temperature of copper rod (K) difference between the DSC curves of the empty container and the reference difference between the DSC curves of empty container and the sample consists of two components: a residual SW fraction and pure bark (SB). Besides color and other physical properties, there is considerable difference in shape and size for these two components. The SW fraction consists of yellowish wood particles. Most of these wood particles are compact bundles of fibrous needles. The SB fraction consists of dark-brown and multi-layered flaky particles of highly irregular shapes. They are quite brittle in comparison to the SW part. In the present study, the softwood bark feedstock, which is basically a mixture of pure softwood particle and bark particles, was procured from Pyrovac Institute, Inc., in SteFoy, Province of Quebec. The feedstock was composed of balsam fir Abies balsamea (31 vol%), white spruce Picea glauca (55 vol%) and black spruce Picea mariana (14 vol%). The pure SW and pure SB samples were prepared by separation of the bulk softwood bark feedstock from Pyrovac. The feedstock contained around 81% (w/w) of pure bark and 19% (w/w) of softwood. The density and proximate analysis of the SW and pure SB fraction is given in Table 1. The carbon content in SW and SB vary due to the varying lignin and extractive contents. The mineral content of SW is less than 1%, but it can be over 6 times in SB as shown in Table 1. The composition of mineral matter can vary between and within each tree. This variation contributes to significant variation in thermo-physical as well as thermo-chemical properties of SB [7]. 2.2. Softwood char SC is the solid residue obtained after pyrolysis reactions. During the pyrolysis process, complex chemical reactions and mechanical wear and tear produce highly porous and Table 1 Density and proximate analysis of SW, SB and SC particles Sample Density (kg m23) [19] Proximate analysis (wt%, anhydrous) Volatile matter Ash Fixed carbon 78.8 70.2 13.0 0.6 3.7 6.4 20.6 26.1 80.6 2.1. Softwood bark SB is the outer shell of the softwood stem. It is produced in large quantities when softwood logs are debarked. It SW SB SC 360 482 299 M. Gupta et al. / Fuel 82 (2003) 919–927 921 brittle char particles. Like mother bark particles, the char particles are also irregular in shape and size. In the present investigation, the SC sample (CH000413/12:50 –0.2)) was produced by Pyrovac Institute, Inc., Jonquière, Province of Québec, in a 3000 kg h21 Pyrocyclinge demonstration plant which has been described elsewhere [3]. The total pressure in the reactor was kept below 20 kPa while the char outlet temperature was maintained at approximately 475 8C (< 750 K). SC is rich in carbon. The density and proximate analysis of char used in this study are given in Table 1. 2.3. Measurement of specific heat by DSC The specific heat in this study was measured by using the DSC technique by means of a SII DSC6100 (Seiko Instruments, Inc., Japan). Three types of measurement were carried out: (i) baseline measurement; (ii) reference measurement and (iii) sample measurement. In the baseline measurement, empty crucibles were placed in both the sample and the reference holders. For a reference measurement, an empty crucible was put on the reference side holder, while another crucible with a reference material (i.e. sapphire) in the sample side holder. In the sample run, an empty crucible and a crucible with sample were loaded at the reference and the sample side holders, respectively. Aluminum crucibles were used. The empty crucible was always covered by a lid which was in contact with the bottom of the crucible; thus no air was enclosed in the crucible. When the reference or the sample material were enclosed, the crucible was covered with a lid which touched the top surface of the sample material. A three step heating program was applied for the measurements: (i) an isothermal heating at 308 K for 10 min; (ii) a dynamic heating from 308 K to the final temperature Tf ; at a heating rate of 5 K min21 and (iii) an isothermal heating at Tf for 10 min. The value of Tf was set to be 413 K for SW and SB samples, and 700 K for the char sample. To ensure good reproducibility, each test was repeated at least twice until satisfactory reproducibility was observed in the DSC curves. Since the SW and SW bark samples contained about 5% moisture, a preheating run from 308 to 413 K was always carried out for each sample to remove any residual moisture. Similarly the cp measurement of the SC samples was performed after preheating from 308 to 873 K to remove the residual volatile matter condensed during char cooling process at the reactor outlet. Before DSC tests, the SW, SB and SC samples were crushed into fine particles, to ensure homogeneity and get rid of air inside the samples in the crucible. To calculate specific heat from DSC measurement, the SEIKO EXSTAR 6000 is equipped with softwares such as DSC SUB, DSC ANALYSIS and DSC CP (Fig. 1). The Fig. 1. The flowchart used by SEIKO apparatus to calculate the cp : principle of cp calculation is expressed as cps ¼ Ys mr c Yr ms pr ð1Þ where cps and cpr are the specific heat of sample and reference material, respectively. Ys and Yr represent the difference in heat flow between the DSC curves of the baseline and sample runs. ms and mr are the mass of sample and the reference material, respectively. As shown in Fig. 1, the value of Y is determined by using the DSC SUB program. Then by using the DSC ANALYSIS and DSC CP programs which are developed based on Eq. (1), the final values of specific heat are calculated over the programmed temperature range. 2.4. Measurement of particle thermal conductivity The thermal conductivity of SW, SB and SC particles was determined using the modified Fitch apparatus, designed and constructed according to guidelines described elsewhere [18]. The device consists of a constant temperature vacuum flask (thermos bottle) with a specially designed cork stopper. A solid cylindrical copper rod is pierced through the cork stopper to seal the vacuum flask. The copper rod has two co-axial solid cylinders in series with diameters of 19 and 10 mm, respectively, as shown in Fig. 2. The lower diameter section is emerged outside the cork stopper, while the larger diameter is pierced though and beyond the stop cork into the flask water. A polystyrene disc is glued on top of the cork stopper. Thermocouple wires are installed in the copper rod about 2 mm from the exposed end for measurement of source temperature T1 : The exposed end of the copper is machined to 6.35 mm diameter and 922 M. Gupta et al. / Fuel 82 (2003) 919–927 In the second boundary condition, m and cp;c represent the mass/unit heat transfer area and the specific heat, respectively, of the perfect conductor (copper here). The analytical solution for the above equation is given by Carslaw and Jaeger [22]. However, assumption of quasisteady conduction heat transfer through the sample, i.e. the rate of heat gain by the heat sink (copper plug) equals the rate of heat transfer through the specimen, yields the following simplified equation [10,20] Alp ðT 2 T1 Þ dT ¼ mc cp;c L dt ð6Þ subject to the following initial condition: T ¼ T0 at t ¼ 0 The solution to Eq. (6) is: Alp t T0 2 T1 ln ¼ Lmc cp;c T 2 T1 Fig. 2. The Fitch apparatus: (1) copper rod, (2) vacuum flask, (3) copper plug, (4) polystyrene disc, (5) thermocouple for copper rod temperature T1, (6) thermocouple for copper plug temperature T, (7) the sample slab, (8) the stopper cork. (all dimensions in mm). thermocouple was installed at the axis, 2 mm above the exposed surface. The copper plug is also insulated with polystyrene. Two screws in the copper plug insulation pass through two matching holes in the polystyrene discs to maintain the alignment and avoid the movement during the experiments. In the modified Fitch apparatus, the sample is sandwiched between the copper rod and the copper plug. The copper rod acts as the heat source while the copper plug is the heat sink. The mathematical formulation of the sample Fitch apparatus system is that of the case of a slab with one face being in contact with a layer of perfect conductor (copper plug) while the opposite face is kept at a constant temperature (T1). The governing differential equations for the temperature field within the sample are expressed as ›T ›2 T ¼a 2 ›t ›z ð3Þ And boundary conditions T ¼ T0 at t . 0 for z ¼ 0 2lp ›T ›2 T ¼ mcp;c 2 at t . 0 for z ¼ L ›t ›z where thermal diffusivity a ¼ lp =rcp;c : The values of T, T0 and T1 are obtained by measurements. A plot of temperature ratio ðT0 2 T1 Þ=ðT 2 T1 Þ vs time on a semi-log scale gives a straight line. The thermal conductivity of the specimen sample is calculated from the slope ðAlp =Lmc cp;c Þ of the temperature history. 2.4.1. Sample preparation To prepare the slabs for the test, few large particles (oversize US mesh #4) were chosen. The large particles were then carefully sanded into thin slabs required for the tests. The samples were made such that their surfaces were smooth, parallel and large enough to accommodate a circle with a diameter of at least 6.5 mm. Samples were then oven dried and kept in air tight bottles for overnight to come in equilibrium with the room temperature. The average thickness of the samples was measured. For this study, two slabs of SW with the mean thickness of 1.42 (SD ¼ 0.02) and 1.05 mm (SD ¼ 0.02) were used. For SB, the sample thickness used were 1.49 (SD ¼ 0.03) and 0.96 mm (SD ¼ 0.07), respectively. For SC samples, the thickness used were 0.71 (SD ¼ 0.01) and 1.17 mm (SD ¼ 0.06), respectively. To avoid the moisture absorption, the samples were kept inside the air tight bottles except for the experimental duration. ð2Þ with the initial condition T ¼ Ti at t ¼ 0 for 0 , z , L ð7Þ ð4Þ ð5Þ 2.4.2. Procedure The Fitch apparatus used in this study, was calibrated with a standard reference material (SRM 1453, Expanded Polystyrene Board) supplied by Building and Research Laboratory, NIST, Maryland, USA. SRM is a low thermal conductivity material (lp ¼ 0.03511 W m21 K21 at 313 K). For calibration, two samples of SRM were prepared with mean thickness, of 1.73 (SD ¼ 0.01) and 2.25 mm (SD ¼ 0.01), respectively. Four tests on each sample were conducted and the mean thermal conductivity at 309 K was compared with the standard value. The mean values M. Gupta et al. / Fuel 82 (2003) 919–927 obtained were found to be low and hence a calibration factor of 0.9233 was introduced [10]. To measure the thermal conductivity of SW, SB and SC, tests were performed on each specimen at an average temperature of 310 K. Four replications were used for each specimen. To study the influence of temperature, the water temperature T1 was changed and the same procedure was adapted for the thicker SW, SB and SC samples. Two replicates for each set were used. The temperature histories of each replicate were recorded for 300 s using a 10 s interval and values of thermal conductivity were calculated on EXCEL spreadsheets using Eq. (7). 3. Results and discussion 3.1. Specific heat The output of the DSC measurement is a thermogram, in which the ordinate depicts the heat flow rate as a function of temperature. In line with the procedure described in Section 2.3, a typical DSC thermogram output for cp determination is given in Fig. 3. The curve A shows the baseline, while curve B and curve C represent the DSC curves of reference and sample, respectively. The curve D shows the heating program during the experiment. The difference between the baseline and the sample DSC curves represents the sensible heat of sample consumed during the heating. Fig. 3 shows that as the temperature increases the base-reference and base-sample difference increase. The specific heat of SW 923 increases with temperature. Similar thermograms were obtained for SB and SC. The samples of SW and SB could be tested up to a temperature of about 413 K only, as at higher temperatures, the devolatization of the samples starts. However, char samples could be tested to temperatures up to those seen during pyrolysis (up to 700 K). The reproducibility of DSC measurements was found to be within 2, 4 and 5% for SW, SB and SC, respectively. The specific heat cp of the samples was calculated using the SEIKO software version 5.5 and using the flow chart shown in Fig. 1 and Eq. (1). The calculated results of cp of SW, SB and SC are illustrated in Fig. 4. The values of SB are found to be higher than SC over the same temperature range. In both cases, however, the value of specific heat increases with the increase in the temperature. The specific heat of wood is reported to vary between 670 and 2500 J kg21 K21 [23]. Fig. 4 shows that with an increase of 100 K, the specific heat of SW increases by 47% and basically follows a linear pattern in line with the reported values of wood by other workers [6,7,24 –26]. The linear regression equation for SW (313 , T , 413) is cp ¼ 5:46T 2 524:77 ð8Þ with a correlation coefficient of 0:995 On an average, the specific heat of SB is observed to increase from 1364 J kg 21 K 21 at 313 K to 1777 J kg21 K21 at 413 K, accounting for a 30% increase compared to 47% for SW. However, the values obtained for SB are greater than SW for the corresponding temperatures. A peak is observed between 313 and 341 K for SB. Fig. 3. Typical thermogram for specific heat determination of softwood sample. (A) Base run, (B) reference run, (C) sample run, (D) temperature. 924 M. Gupta et al. / Fuel 82 (2003) 919–927 Fig. 4. Specific heat cp vs temperature, (A) SW, (B) SB, (C) SC. Repeated experiments gave the same pattern. To avoid the influence of residual moisture, the samples were preheated till 423 K before DSC analysis. Thus the effect of latent heat of water evaporation was ruled out. To the authors’ knowledge, this phenomenon has not been reported before. However, the mechanism of this unusual peak was not further investigated as it was falling well beyond the objectives of this study. The linear regression equation fitted to the overall data (313 , T , 413) is cp ¼ 3:69T þ 231:06 with a correlation coefficient of 0:924 ð9Þ The values obtained for SC are shown in Fig. 4. Compared to SW and SB, the specific heat of char is lower for the corresponding temperatures and does not follow a linear pattern. The values for char rather follow a second order polynomial, in line with the work of Gronli and Melaaen [25]. Following regression equation (313 , T , 686) is obtained cp ¼ 20:0038T 2 þ 5:98T 2 795:28 ð10Þ and the correlation coefficient is 0.991. With the increase in temperature, the specific heat of the SC almost doubles from 768 J kg21 K21 at 313 K to 1506 J kg21 K21 at 413 K. This shows that the variation Fig. 5. A typical temperature history data for samples. K SW ðL ¼ 1:42 mmÞ; V SB ðL ¼ 1:49 mmÞ; X SC ðL ¼ 1:17 mmÞ: M. Gupta et al. / Fuel 82 (2003) 919–927 Table 2 Design parameters used in the modified Fitch apparatus Parameter Value Heat transfer area of copper plug, A Mass of copper plug, mc Specific heat of copper, cp;c 3.16 £ 1025 m2 5.24 £ 1023 kg 376 J kg21 K21 of the specific heat with temperature should not be neglected, as it is often done in modeling studies [7,27,28]. 3.2. Particle thermal conductivity A typical plot of temperature history of SW, SB and SC samples is shown as Fig. 5. The semi-log temperature history of the samples almost follows a linear profile. The thermal conductivity of the samples was determined by calculating the slope of the temperature histories of each run in EXCEL spreadsheets and using Eq. (7). Four replicates of each sample were used for calculation of the mean thermal conductivity. The values of design parameters used in calculations are given in Table 2. The calculated mean thermal conductivity of SW, SB and SC is given in Table 3. The mean thermal conductivity of SW was calculated to be 0.0986 W m21 K21 at 310 K. The mean thermal conductivity of SB and SC were determined to be 0.2050 W m21 K21 at 310 K and 0.0946 W m21 K21 at 308 K, respectively. The values measured here for SW were basically the thermal conductivity values measured along the transverse directions (perpendicular to direction of fibers). Because of the size limitations of the softwood feedstock, it was not possible to prepare a sample for the measurement along the longitudinal direction. Fig. 6 gives the variation of thermal conductivity lp of SW, SB and SW particles as a function of temperature. With an increase in temperature from 310 to 341 K, the values of lp for SW, SB and SC increased by 13, 13 and 22%, respectively. The values almost follow a linear pattern. Due to practical limitations of the Fitch apparatus, the thermal 925 conductivity was measured only up to the mean temperature of 348 K; within this range, bark values are always higher than wood and char. After 325 K, however, the lp for char increased at a higher rate compared to wood and bark. The thermal emissivity of bark and char is reported to be 0.80 and 0.95, respectively [7,28]. Also the absolute porosity of bark and char is calculated to be 0.68 and 0.80, respectively [19]. The effective scattering factor in porous materials depends upon the material emissivity and the porosity [29]. Thus, the effective scattering factor of char is almost twice that of bark at 2.0 and 1.1, respectively. However, considering the relative standard deviation of thermal conductivity measurements in the range of 6% (Table 3), no conclusion can be drawn. One might be concerned that a possible thermal expansion of the copper plug and copper rod results in a compression of the sample density. Copper has a very low coefficient of linear expansion ða ¼ 1:65 £ 1025 K21 Þ [30]. In the modified Fitch apparatus (Fig. 2), when the sample is sandwiched between the copper rod and copper plug, the maximum temperature variation is around 32 K. The copper plug thickness being less than 21 mm (Fig. 2), the maximum possible linear expansion of the copper plug is 0.0107 mm. This is just 1.5% of the thinnest sample tested (0.71 mm). However, it must be noted that the top end of the cover is not bolted. Rather it is free end and lies on the sample. Therefore, despite any vertical expansion in copper plug and rod, there will be no additional pressure or compression in the sample. Consequently, we do not believe that the reported measurements are affected by the temperature variation in the copper. Table 4 gives a comparative review of the thermal conductivity of wood, bark and char. While significant literature has been reported on thermal conductivity of SW, little has been reported on SB and SC. The values for SW are in good agreement with the reported values for Norway spruce and Douglas fir [6,26]. Gronli et al. [25] have reported thermal conductivity of birch/pine/spruce at 0.35 W m21 K21 which is about three times higher than the values reported in the literature and in the present work (Table 4). In general, the thermal conductivity of softwood Table 3 Particle thermal conductivity of SW, SW and SC Sample Mean temperature, Tmean (K) Thickness L (mm) Particle thermal conductivity SD (%) lp (W m 21 21 K ) Mean particle thermal conductivity SD (%) lp (W m21 K21) SW 309 310 1.42 1.05 1.4 1.9 0.0975 0.0997 6.2 6.0 0.0986 SB 310 310 1.49 0.96 2.0 7.3 0.1993 0.2107 1.2 2.5 0.2050 SC 309 307 0.71 1.17 11.3 5.1 0.0934 0.0958 5.9 3.6 0.0946 SD here is basically relative standard deviation in %. 926 M. Gupta et al. / Fuel 82 (2003) 919–927 Fig. 6. Particle thermal conductivity lp as a function of temperature: K SW; V SB; X SC. is reported to increase linearly with the temperature. Temperature dependency of thermal conductivity of SW in this work, is in close agreement with values reported by Ragland et al. [7]. For an increase in temperature from 420 to 575 K, Suuberg et al. [23] have reported thermal conductivity values for virgin cellulose pellets to increase from 0.05 to 0.07 W m21 K21. For the corresponding temperature range, our values (through extrapolation) are observed to be higher (Table 4). The thermal conductivity of SB is almost twice the thermal conductivity of SW. Reported literature on softwood bark thermal conductivity is rare [5,27] The values range from 0.055 to 0.48 W m21 K21 (Table 4). In absence of precise sample specifications and measurement conditions, it is difficult to compare the results from the present work with reported values. The thermal conductivity values obtained for the char and for the softwood are close to each other in this study. Table 4 A comparative review of thermal conductivity values of wood, bark and char Material Sample form Density (kg m23) Temperature (K) Thermal conductivity (W m21 K21) Reference Wood Fir Spruce Norwegian birch/pine/spruce Hardwood birch Norway spruce Douglas fir Wood1 Virgin cellulose Present work Particle Particle Particle Particle Particle Particle – Pellets Particle 540 410 – 680 350 512 350 458 360 – – – 294– 373 – – T 420– 575 310– 341 0.138 0.109 0.350 0.214–0.250 0.100 0.110 0.035 þ 1.73 £ 1024T 0.05–0.07 0.0986–0.1114 [26] [26] [25] [9] [6] [6] [7] [23] Bark Paper bark Bark1 Present work Bed – Particle 118 400 –600 482 – – 310– 348 0.48 0.055–0.074 0.2050–0.2313 [31] [5] Particle bed Particle pellets Particle – 120 999 199 425 299 – 819 320 – 420– 520 310– 341 0.1 0.620 0.370 0.062 0.05–0.06 0.0946–0.1156 [25] [26] [32] [5] [23] Char Norwegian (birch/pine/spruce) char Graphite char Coal char Char1 Cellulose char Present work 1 Source not specified. M. Gupta et al. / Fuel 82 (2003) 919–927 The thermal properties of char highly depend upon the source of raw material, the pyrolysis conditions and the composition of the char. Although many workers have reported values of char particles (Table 4), a direct comparison is not possible as char precise specifications are lacking in these studies. Nevertheless, the values obtained in this work are close to values reported by Gronli et al. [25] for Norwegian (birch/pine/spruce) char. The thermal conductivity values of char in the present work are much lower than the values reported for graphite char [26] or char obtained from coal [32], in which cases the source and processing conditions are very different in comparison with the present work. For low temperature conduction in the lignocellulosic materials, the density plays an important role [9]. As shown in Table 1, the density of the char is the lowest and the density of bark is the highest among the three species. Perhaps this is the reason why SB which has the highest density among SW, SB and SC, exhibited the highest conductivity while SC which has the lowest density, exhibited the lowest conductivity. 4. Conclusion The specific heat of SW, SB and SC particles was measured by DSC apparatus. A modified Fitch apparatus was constructed, calibrated and used to measure the particle thermal conductivity of SW, SB and SC. 1. The specific heat of SW and SB increased linearly from 1172 to 1726 and 1364 to 1777 J kg21 K21 with an increase in temperature from 313 to 413 K. With an increase in temperature from 313 to 713 K, the specific heat of SC doubled from 768 to 1506 J kg21 K21 and followed a polynomial relationship with temperature. 2. The thermal conductivity of SW, SB and SC was determined to be 0.0986, 0.2050 and 0.0946 W m21 K21, respectively, at 310 K (for bark, the thermal conductivity has been measured in the transverse direction only). The thermal conductivity of SW, SB and SC linearly increased with temperature. The measured thermal properties of SW, in this work, are in good agreement with the reported values in the literature for similar wood species. The measurements in this work provide new contribution for the thermal characterization of softwood bark and softwood char in terms of thermal conductivity and specific heat. Acknowledgements We are grateful to the Fonds pour la Formation de Chercheurs et l’Aide à la Recherche (FCAR, Gouvernement 927 du Québec), for partial financial support of the first author of this article. References [1] David McKeever. Biocyle 1998;39(1):65. [2] Troughton Gary E. Recycling 1996;(September):10. [3] Roy C, Blanchette D, Caumia BD, Dubé F, Pinault J, Bélanger É, Laprise P. In: Kyritsis S, Beenackers AACM, Helm P, Grassi A, Chiaramonti D, editors. Industrial scale demonstration of the pyrocyclinge process for the conversion of biomass to biofuel and chemicals. 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