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This document details the calibration process of calorimeters and combustors using microcrystalline cellulose as a test substance for determining the calorific values of cellulose-based solid waste products. the enthalpy of combustion of microcrystalline cellulose, the heat of wetting correction, and the bomb calorimetric measurements.
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JOURNAL OF RESEARCH of the National Bureau of Standards Vol. 86, No.6, November-December 1981
National Bureau of Standards, Washington, DC 20234
August 14. 1981
A test substance with characteristics and properties similar to those of cellulose· based solid waste products is needed to calibrate calorimeters and combustors which will be routinely burning these materials to determine their calorific values precisely for use in commerce. Microcrystalline cellulose was found to be a good calibrant for this purpose. The enthalpy of combustion of microcrystalline cellulose ~H~ at (25 0q, and its estimated uncertainty, was determined to be -2B12.401±1.725 kllmol based upon the sample mass. A calculated heat of wetting correction of 1.514 kl Imol was applied to the combustion data.
Keywords: alternative fue~ bomb calorimetry, cellulose, enthalpy of combustion, refuse·derived·fue~ test substance.
The enthalpies of combustion of heterogeneous feedstocks such as refuse-derived-fuel (RDF) and wood wastes, are important thermochemical data because of the potential application of these materials in commerce as sup- plemental or alternative fuels. When determining the en- thalpy of combustion of RDF in a conventional bomb calorimeter or a newly designed multi-kilogram flow calorimeter, it is desirable to have a "test substance"[I] which can be used for their calibration which is as close to RDF in character as possible. This test substance will per- mit the intercomparison of the thermochemical results of different investigators in the new field of fuels from cellulose-based solid wastes and will essentially serve to con- trol the chemical part of the investigation. Since there is a large fraction of cellulosic materials (i.e., paper products) in municipal solid waste (MSW), we decided to investigate the possibility of using a pure cellulose as a test substance. Cellulose not only has a close compositional relationship to the major components of MSW, but also possesses a similar kinship to wood species, wood wastes from the manufacture of paper, bagasse from the sugar refining industry, agricultural wastes, and some forms of peat. These materials have a potential as supplemental or alternative fuels just like RDF.
tGuesl worker from July 1980-February 1981, Chemistry Laboratory, National Institute of Metrology, P.O. Box 2112, Peking, People's Republic of China. ·Center for Chemical Physics, Chemical Thermodynamics Division 'Numbers in brackets indicate literature references at the end of this paper.
A search was carried out to find a suitable cellulosic test substance. We needed a cellulose which was high in purity, homogeneous, inexpensive, easy to pelletize, and one which could be obtained in large quantities. Avicef,2 a readily available commercial cellulose, was chosen because it pos- sesses most of the requirements for use as a calibrant in a bomb calorimeter. This cellulose is very homogeneous, 99.81 percent pure, and presses into a pellet very easily. Calibration of the oxygen bomb calorimeter was per- formed using SRM benzoic acid, standard sample, 39i, which is the accepted primary standard substance for calibrating bomb calorimeters. Comparative calorimetric measurements were conducted on the cellulose sample. These measurements for benzoic acid and cellulose, along with the heat of wetting correction for cellulose, are presented in this paper.
2.1 Sample Characterization
Avicel, pH-lOI, lot 1018-152, is a microcrystalline cellulose, which is an acid hydrolyzed derivative of a dissolv· ing grade of wood pulp. It has an average particle size of 50 micrometers and a pH of 5.5 to 7. The sample was not subjected to any further purification but these additional analyses were made to further
'The commercial sources cited in this paper are included to adequately de~cribe the experimental procedure. Such identification does not impl~· recommendation or endorsement by the National Bureau of Standards.
characterize the cellulose. The percent moisture of seven cellulose samples was 4.910 ± 0.060 (sd.) at a relative humidity of 36 percent, as determined by drying in a 105 °C oven until a constant weight was reached. The water soluble impurities of fluoride, chloride, nitrate, and sulfate were analyzed for by the method of ion- chromatography.3 Two cellulose samples of different masses,0.51 g and 1.62 g were diluted in a solution contain- ing the buffer: 0.003M NaHC0 3 /0.0018M Na 2 C0 (^) 3. The diluted sample was mixed, allowed to settle, and filtered through a 0.2 micrometer syringe filter. The average con- centration of water soluble impurities for the two samples was 62.46 ppm. This level of anions is negligible when look- ing at the overall sample purity. The amount of ash was found to be negligible when deter- mined according to the American Society for Testing and Materials (ASTM) Standard Test Method D-3174-73 for Coal and Coke. The samples were fired for two hours in a furnace Qperating at 575-600 °C. The purity of the Avicel was determined in duplicate CO (^2) analyses of the bomb combustion products. The gaseous products of combustion were released from the bomb and passed through absorption tubes containing Ascarite and magenesium perchlorate for removal of CO 2 and H 2 0, respectively, and phosphorus pentoxide [2] to prevent the back-flow of moist room air into the absorption system. The amount of CO 2 was then determined gravimetrically. The purity of the cellulose was found to be 99.809 ± 0.103 (sd.) percent.
2.2. Description of Colorimeter
The combustion measurements were made in an iso- peribol oxygen bomb calorimeter. This is an isothermal- jacket calorimeter with the calorimeter reaction vessel submerged in a water bath at 301 K and controlled to ±0.OO3K. This prevents any thermal leakage between the laboratory environment and calorimeter. The heat gen- erated when a measured amount of sample is burned is compared to the heat evolved when a measured amount of standard substance is burned in the same calorimetric sys- tem. Benzoic acid, the primary calibrant, is burned and produces a three degree temperature rise in the calorimeter. The energy equivalent of the calorimeter is determined from the amount of energy produced by the benzoic acid and divided by the temperature rise. The temperature rise is corrected for the stirring energy produced in the stirred water of the calorimeter vessel and any thermal leakage between the environment and calorimeter. In a cellulose experiment, the corrected temperature rise
'The analyses were performed by the Inorganic Analytical Research Division of the National Bureau of Standards.
is multiplied by the energy equivalent of the calorimeter. This calulation gives the total energy produced in a cellu- lose combustion experiment. This total energy is finally cor- rected for any side reactions, or thermal corrections, and is divided by the mass of the cellulose sample to produce the internal energy of combustion at constant volume, l::..CJ;. Conversion to the enthalpy of combustion at constant pres- sure, l::..H;, carried out by applying a correction term for pressure-volume expansion (l::..nRT). The l::..nRT term for
All of the cellulose samples for combustion are pressed into pellets under an approximate force of 44.4 kN. A sam- ple weight of 2.3 g was pre-determined in a trail experiment as the necessary amount of sample required to produce a three degree temperature rise.
A dried sample weight is necessary for the combustion experiments. Since cellulose is very hygroscopic, this was very difficult. The samples were placed into pre-weighed ground glass neck weighing bottles, dried at 105°C until a constant weight of ± 0.3 mg was obtained, and stored in a
2.4 Example of Colorimetric Procedure
A dried pellet was transferred from the weighing bottle to a preweighed platinum crucible. The empty weighing bottle was again weighed to account for any cellulose remaining in the bottle. The platinum crucible with pellet was placed on the crucible support of the bomb head. The fuse leads had been previously connected with a 2 cm length of 0.075 mm platinum wire which is placed in contact with the top of the pellet. Normally, 1 ml of wa ter is added to the bottom of the bomb to provide a saturated atmosphere and ensure that water formed as a combustion product is present in the liquid state. For this series of cellulose combustions, 0.2 ml of water was added directly to the pellet in the crucible and 0.8 ml added to the bottom of the bomb. The sample was wetted before burning because it was found in the previous study by Jessup and Prosen [3]4 that a more complete com- bustion results with a wetted sample rather than a dry one. The sealed bomb is charged with 3.10 MPa (30.62 atm) of high purity oxygen and placed on the bench for approxi- mately 1 hour for the sample to equilibrate with the moist environment inside the bomb. The calorimeter vessel is fined with a known amount of water, the bomb is lowered into the vessel, and the covered calorimeter is submerged in the constant temperature water bath. The rate of tempera-
TABLE II. Benzoic Acid Calibration Results.
Expt. No. .1U~(28^ 0c)^ m·BA(yac)^ q-BA^ q-ign^ q-HN0^3 JIg g^ J J J 1000 -26410.68 1.636294^ -43215.64^ 1.16^ 6. 1001 -26410.68 1.629256 -43029_76 1.16 5. 1002 -26410.68 1.632134 -43105.76^ 1.21^ 5. 1004 -26410.68 1.630985 -43075.41 0.94 3. 1008 -26410.68 1.629405 -43033.69^ 1.16 5. 1010 -26410.68^ 1.630515^ -43063.02^ 0.94^ 4. 1011 -26410.68 1.630601 -43065.29 0.94 2. 1012 -26410.68^ 1.630203^ -43054.76^ 1.06^ 6. 1013 -26410.68 1.630414 -43060.33 1.16 5.
Ei-cont, the heat capacity of the initial bomb contents,
E,si-empty, the energy equivalent of the empty calorime- ter at 28°C, in J/K. E,si-mean, the mean value of the measured energy equiv- alent, in J/K. Std. Dev,_ the standard deviation of a measurement, (sd),
Std. Dev. Mean, the standard deviation of the mean,
mean, % sdm). The combustion data for Avicel are presented in table III. These are additional headings used in the table that were not described previously and are identified as follows: q-wetting, a correction to the overall energy due to the combustion of the wetted sample, in J. When the sample is wetted, heat is evolved. During the burning process, that amount of water used in pre-wetting the sample is dried during the combustion. Therefore, the amount of heat gen- erated in the combustion reaction is less than would be expected due to the amount of heat required to dry the sam- ple. The number of joules due to the combustion of the com- pound initially is smaller and the amount of heat due to the wetting must be put back in to produce the correct enthalpy of combustion. q-corr to tf , A correction applied for the deviation of the actual final temperature from the selected standard final temperature (ussually 28 0c), in J. Q-cellulose, total energy delivered to the calorimeter after corrections for ignition energy, formation of nitric acid, sulfuric acid, heat of wetting and the like, in J. m-cellulose, mass of the Avicel (cellulose) sample, in g, reduced to mass in vacuum. l:1U: (28 ° C), the internal energy of combustion of the cel- lulose sample at constant volume in JI g.
q-WC Q-total J J 34.646 -43257. 34.415 -43070. 34.461 -43146. 34.463 -43114. 34.503 -43074. 34.580 -43103. 34.500 -43103. 34.625 -43096. 34.567 -43101.
E,si-mean J/K Std. Dey. J/K Std. Dey. Mean J/K
.1T-corr E-cal K J/K 3.010633 14368. 2.997890 14367. 3.002835 14368. 3.001051 14366. 2.998000 14367. 3.001390 14361. 3.000125 14367. 2.999317 14368. 3.000575 14364.
2.47(0.017%) 0.82(0.006%)
Ei-cont E,si-empty J/K J/K 18.92 14349. 18.89 14348. 18.88 14349. 18.89 (^) 14347. 18.93 14348. 18.95 14342. 18.91 14348. 18.97 14349. 18.95 14345.
l:1nRT, the correction term needed to change l:1U: to t:JI: at a given temperature. ~28 ° C), the enthalpy of combustion of the sample in pure oxygen at the final temperature, in kJ/mole. l:1Cp l:1T, a correction which includes the calculated change of heat capacity of the calorimeter system with tem- perature (25-28 CC), in kJ/mole. The following values for CplJmol- 1 at 298 K were used: a-cellulose C 6 H100S(c), 188.554 [16]: 02(g), 29.355: CO2(g), 37.112: H20(liq), 75.29l. 1ll/J.25 °C), the enthalpy of combustion of the sample at the standard temperature, in kJ/mole.
obtained for the internal energy of combustion, l:1U:, of the Avicel sample at 28°C, according to eq. (1).
The formula weight of cellulose used in this study is 162.1439 g/mole. The results of this study and the values derived from the results are summarized in table IV. The uncertainties assigned to l:1U: and t:JI: were obtained by combining (square root of the sum of the squares) 2 sdm (in %) for the calib.ration experiments, 2 sdm (in %) for the combustion experiments, 0.01 percent for the possible effect of organic impuri ties in the sample, 0.01 percent for the uncertainty in the certified value for benzoic acid and reasonable esti- mates of all other sources of error, 0.01 percent Our values are calculated at 30°C for purposes of com- parison with work that was carried out by Jessup and Prosen
J/g(sdm) which is a mean of three experiments. Our results
these values are calculated based upon the mass of sample burned. A 0.276 percent difference exists between the two
TABLE III. Combustion Data on Cellulose
Expt. No. 1014 1015 1016 E.si·empty JIK 14347.75 14347.75 14347. Ei·cont JIK 28.04^ 28.62^ 28. E-cal JIK 14375.79 14376.37 14376. .1T -corr K 2.755973 2.894679 2. Q-total (^) J -39619.30 -41614.99 -42295. q·ign J 1.16 1.16 1. q·HNO. J -44.5308^ -45.3003^ -23. q.wetting (^) J -21.2809 -22.3577 -22. q·WC J 34.6815^ 36.8266^ 37. q-corr to t, (^) J -2.0237 -1.4655 -1. Qcellulose J -39562.23 -41555.25^ -42256. m-cellulose g 2.281250, 2.396698 2. .1U:'(28 "C) Jig -17352.35 -17338.66^ -17355. °.1nRTa kJ/mol 0 0 0 .1 H:'(28 0c) kJ/mol -2811.956 -2811.358 -2810. .1C,I,.1n kJ/mol^ -0.703^ -0.703^ -0. .1 H:'(25 OC) kJ/mol -2812.659 -2812.061 -2811. aThe values of atomic weights used in this work are:
Mean, Ml:'(28 0c) Std. Dev. Std. Dev. Mean
kJ/mol kJ/mol kJ/mol
-2811. 0.84 (.030%) 0.28 (.010%)
1018
-41095.
-45. -22.
-1. -41036.
-17337. 0 -2811. -0. -2811.
T ABLE IV. Data Summary with Estimated Uncertainty.
AU~(28 QC) AH:'(28 QC)
-17 340.76 ± 10.64 Jig
values, but considering that Jessup and Prosen's sample was not well characterized and its purity uncertain, the values are in very good agreement Our precision indicates that the Avicel can be burned very reproducibly.
A test substance with characteristics and properties simi· lar to those of cellulose·based solid waste products is needed to calibrate calorimeters and combustors which will be rou- tinely burning these materials to determine their calorific values precisely for use in commerce. Microcrystalline cellulose is a good calibrant for this pur- pose because it is ashless, of high purity, homongeneous, inexpensive, and easy to pelletize. For hygroscopic cellu- lose materials a heat of wetting correction is neccessary. Extremely dry ceIlut'ose does not produce a complete burn in a combustion calorimeter. Our heat of wetting correction of 1.514 kJ/mol was calculated based upon previous data in the literature. The enthalpy of combustion of microcrystal- line cellulose, !:::..Jt: at (25°C), and its estimated uncertainty, was determined to be -2812.401 ± 1.725 k.l/mol based upon the sample mass. Microcrystalline cellulose appears to
1020 1021 1023 1024 1032 14347.75 14347.75 14347.75 14347.75 14347. 28.24 28.28 28.15 28.46 28. 14375.99 14376.03 14375.90 14376.22 14376.04- 2.801024 2.8Il611 2.779214 2.851034 2. -40267.49 -40419.82 -39953.71 -40987.08 -40487. 1.49 l.l8 1.24 0.92 0. -45.9112 -44.7364 -45.6938 -43.9845 -29. -21.6333 -21.7140 -21.4625 -22.0711 -21. 35.3811 35.5512 35.0807 36.2219 35. -1.7402 -1.8014 -1.9352 -1.6774 -1. -40208.08 -40361.86 -39895.09 -40929.65 -40445. 2.319141 2.327693 2.300729 2.360262 2. -17337.49 -17339.86 -17340.20 -17341.15 -17353. 0 0 0 0 0 -2811.168 -2811.553 -2811.608 -2811.762 -2813. -0.703 -0.703 -0.703 I -0.703 -0. -2811.871 I -2812.256 -2812.311 I -2812.465 -2814.
have good potential for serving as a test substance in the combustion calorimetry of cellulose-based solid waste pro- ducts.
[1] Waddington, Guy. Physicochemical Standards for Thermochemistry, chap. 13 in Experimental Thermochemistry. Vol. 1. F.D. Rossini, ed. NY: Interscience Publishers, Inc.; 1956.287-295. [2] Prosen. Edward J.; Rossini, Frederick D. "Heats of Izomerization of the Five Hexanes." J. Res. Nat Bur. Stand. (U.S.) 27: 289-310; September 1941. [3] Jessup, Ralph 5.; Prosen, Edward J.; "Heats of Combustion and For- mation of Cellulose and Nitrocellulose." J. Res. Nat Bur. Stand. (U.S.)44: 387-393; April 1950. [4] Coops, J.; Jessup, R.S.; van Nes, K. Calibration of Calorimeters for Reactions in a Bomb at Constant Volume, chapter 3 in Experimen- tal Thermochemistry, Vol. 1. F.D. Rossini, ed. NY: Interscience Publishers, Inc.; 1956. 27-58. [5] Wahba, M.; Nashed, S. The effect of hysteresis on the heat of wetting of partially saturated cellulose in water and its bearing on the physical structure of cellulose. Proceedings of the Egyptain Academy of Sciences. 8: 128-139; December 1952. [6] Wahba, M.; Moisture relationships of cellulose. I. J. Physical & Col- loidal Chem. 52: Il97-1208: 1948. [7] Wahba, M.; Moisture relationships of cellulose. II. J. Physical & Col- loidal Chem.54: 1148-1160; 1950. [8] Wahba, M.; Aziz, K.; Moisture relations of cellulose, J. Textile Insti· tute 50: T558-T568; 1959. [9] Wahba, M.; Aziz, K.; Hysteresis and the heats of sorption of water on cotton cellulose below and above its second-order transition of about 25 QG. Chemica. Scripta. 7: 233-238; 1975. [10] Argue, G.H.; Maas, 0.; Measurement of the heats of wetting of cellu- lose and wood pulp. Can. J. Chem.12: 564-574; 1935.