the coking properties of coal at elevated pressures. - Argonne ...
the coking properties of coal at elevated pressures. - Argonne ... the coking properties of coal at elevated pressures. - Argonne ...
The DTA/TGA studies o so im and potassium benzoate decompo . ition show that these model molecules initially decompose to form condensed ring organic molecules, alkali carbonate, and carbon dioxide. This initial decomposition process occurs over the temperature range of 400 to 600'C and is independent of the gas stream composition. Over this temperature range, there is no loss of alkali into the gas phase. Rather, all of the alkali is converted into the corresponding alkali carbonate. At higher temperature, the alkali carbonate decomposes and the course of this decomposition is determined primarily by the composition of the ambient gas. In an inert gas stream, the alkali carbonate decomposes over the temperature range of 700 to 900°C with release of carbon monoxide and atomic alkali. This decomposition has been confirmed by transporation mass spectrometer studies. l7 However, in a stream containing 20% Cop between 700 and 9OO"C, only carbon monoxide is released and the alkali is converted to alkali carbonate. This rection sequence occurs as long as residual carbon and carbon dioxide are present. Once the excess carbon has been converted to carbon monoxide, the alkali carbonate will decompose at temperatures in excess of 1200°C. Experiments were also performed with a combination of SOp, Cop, and O2 in the gas stream. Here, it was found that the alkali carbonate is converted to the alkali sulfate with no indication of alkali loss over the temperature range studied (< 1300°K). CONCLUSIONS Thus, the results of the measurements and experiments discussed above do provide a plausible way to begin an explanation for the distribution of alkali in che ash particulates. To summarize: 1. Under typical coal combustion conditions in an atmosphere rich in Cop and/or SOp, the alkalis in the organic fraction do not vaporize but remain bound in the ash as stable carbonates or sulfates. 2. The alkalis in the inorganic fraction diffuse to the surface producing enrichment by a factor of about 13 to a depth of about 100A. The results, however, do not provide conclusive evidence about the fate of the alkalis. The effect of water vapor in the combustion stream has not yet been studied. Clearly, water could have an important effect on the vaporization process. Furthermore, the reasoning we have followed to explain the absence of alkali enrichment in the submicron particles requires that the volatilization of the alkalis in both the organic and inorganic fraction not be significant (say less than 20%). 140
1, It is possible to make a reasonably clear statement about the alkalis in the organic fraction under various combustion conditions. Here, the volatilization of the alkalis is primarily determined by the heterogeneous chemical reaction of the alkalis with the gas stream. Such detailed information, however, is not available for the alkalis in the inorganic fraction. Here, experimental data were not obtained under appropriate conditions. Thus, the combustion experiments of Hims et al., which do show significant alkali vaporization, were performed in an O2 atmosphere without CO2 or SO2 enrichment. The experiments of Stinespring and Stewart, with the inorganically bound alkalis, measured only enrichment and did not study vaporization. The results of recent vaporization studies of Hastie et a1.18 were also not performed under conditions directly applicable to coal combustion. Clearly, a wider range of experimental data will have to be obtained. Specifically, the effects of surface chemistry on the alkali in the inorganic fraction will have to be studied before a more conclusive statement can be made about the fate of the alkali in coal combustion. ACKNOWLEDGMENTS This work was supported by the U.S. Department of Energy/Morgantown Energy Technology Center under Contract No. DE-AC21-81NC16244. REFERENCES 1. 2. 3. 4. 5. 6. 7. 8. 9. D.F.S. Natusch and J.R. Wallace, Science 186, 695 (1974). R.L. Davison, D.F.S. Natusch, J.R. Wallace, and C.A. Evans, Jr., Environ. Sci. & Technol. 8, 1107 (1974). J.M. Ondov, R.C. Ragaini, and A.H. Biermann, Environ. Sci. & Technol. 2, 947 (1979). D.G. Coles, R.C. Ragaini, J.M. Ondov, G.L. Fisher, D. Silberman, and B.A. Prentice, Environ. Sci. & Technol. 13, 455 (1979). L.E. Wangen, Environ. Sci. & Technol. 15, 1081 (1981). R.D. Smith, Prog. In Energy & Comb. Sci. 6, 53 (1980). R.W. Linton, A. Loh, and D.S.F. Natusch, Science 191, 852 (1976). J.A. Campbell, R.D. Smith, and L.E. Davis, Appl. Spectrosc. 32, 316 (1978). S.J. Rothenberg, P. Denee, and P. Holloway, Appl. Spectrosc. 2, 549 (1980). 141 - -
- Page 89 and 90: t 5360-096pj There is an interactio
- Page 91 and 92: 1 I > \ i I 5360-096bw bed data. Be
- Page 93 and 94: I 1. I 5360-096bw ranging from atmo
- Page 95 and 96: uY.ku ICHlMAlIC OF MINI-FLUID BE0 R
- Page 97 and 98: 800-12-1133 -9 FIGURE IO CALCULATED
- Page 99 and 100: Mexico coal. Table 1 shows an analy
- Page 101 and 102: ', Complete results from all runs c
- Page 103 and 104: I the methanol down to atmospheric
- Page 105 and 106: TABLE 3 -----______________________
- Page 107 and 108: \ "I N z 107 c. . 0 0
- Page 109 and 110: I. INTRODUCTION DIRECT METHANATION
- Page 111 and 112: The catalyst development program fo
- Page 113 and 114: Preparing process flow diagrams and
- Page 115 and 116: \ \ i 1. 2,000 4,000 6,000 8,000 10
- Page 117 and 118: (JMS-OlBM-2). The mass spectra were
- Page 119 and 120: I I Fairbridge, R.W. (ed.) 1972, En
- Page 121 and 122: v- W V z d 3 z m 4 ? P m W c3 W m N
- Page 123 and 124: e. \ I , W 2 m 4 t- CI 99-79 noooo
- Page 125 and 126: L Table I: Compositions of High Tem
- Page 127 and 128: \ " \ I For all three coals, the pr
- Page 129 and 130: 4 , 1024 1024 3a 3b J Mineral Parti
- Page 131 and 132: The Determination of Mineral Distri
- Page 133 and 134: pyrite crystals in framboids locate
- Page 135 and 136: FIG. 1. TEM MICROGRAPH OF A HIGH VO
- Page 137 and 138: \ \ FIG. 5. SEM MICROGRAPH SHOWING
- Page 139: \ , species. In fact, combustion ex
- Page 143 and 144: \ i SURFACE AND BULK ENRICHMENT OF
- Page 145 and 146: I Coal Ash Sintering Model and the
- Page 147 and 148: 5 carried out such sintering measur
- Page 149 and 150: I this ash and other bituminous coa
- Page 151 and 152: forming propensity. However, none o
- Page 153 and 154: t I 153
- Page 155 and 156: CENTRAL ELECTRICIN RESEARCH LABORAT
- Page 157 and 158: 157 18 I I a I
- Page 159 and 160: temperature, sulfur species concent
- Page 161 and 162: The facility is fired with coal usi
- Page 163 and 164: Tests have been carried out to dete
- Page 165 and 166: under which conditions sulfur speci
- Page 167 and 168: I TITANIUM L Corn AS A TRACER FOR D
- Page 169 and 170: E 6 i i h \ 1 1 \ on the XRF is cau
- Page 171 and 172: \ ? CONCLUSIONS Titanium can accura
- Page 173 and 174: NY) m * oa
- Page 175 and 176: GFETC constructed a 0.2 square mete
- Page 177 and 178: \: Stage 3. Sulfated ash-cemented a
- Page 179 and 180: I FIG. 1. Initial ash coating on qu
- Page 181 and 182: FIG 9. Limestone bed material alter
- Page 183 and 184: (4) Since the operating temperature
- Page 185 and 186: I I maximum particle diameter leavi
- Page 187 and 188: ! suspension chambers and cyclone f
- Page 189 and 190: Pilot Plant of a Coal Fired Fluidiz
The DTA/TGA studies o so im and potassium benzo<strong>at</strong>e decompo . ition show<br />
th<strong>at</strong> <strong>the</strong>se model molecules initially decompose to form condensed ring organic<br />
molecules, alkali carbon<strong>at</strong>e, and carbon dioxide. This initial decomposition<br />
process occurs over <strong>the</strong> temper<strong>at</strong>ure range <strong>of</strong> 400 to 600'C and is independent<br />
<strong>of</strong> <strong>the</strong> gas stream composition. Over this temper<strong>at</strong>ure range, <strong>the</strong>re is no loss<br />
<strong>of</strong> alkali into <strong>the</strong> gas phase. Ra<strong>the</strong>r, all <strong>of</strong> <strong>the</strong> alkali is converted into <strong>the</strong><br />
corresponding alkali carbon<strong>at</strong>e. At higher temper<strong>at</strong>ure, <strong>the</strong> alkali carbon<strong>at</strong>e<br />
decomposes and <strong>the</strong> course <strong>of</strong> this decomposition is determined primarily by <strong>the</strong><br />
composition <strong>of</strong> <strong>the</strong> ambient gas. In an inert gas stream, <strong>the</strong> alkali carbon<strong>at</strong>e<br />
decomposes over <strong>the</strong> temper<strong>at</strong>ure range <strong>of</strong> 700 to 900°C with release <strong>of</strong> carbon<br />
monoxide and <strong>at</strong>omic alkali. This decomposition has been confirmed by<br />
transpor<strong>at</strong>ion mass spectrometer studies. l7 However, in a stream containing<br />
20% Cop between 700 and 9OO"C, only carbon monoxide is released and <strong>the</strong> alkali<br />
is converted to alkali carbon<strong>at</strong>e. This rection sequence occurs as long as<br />
residual carbon and carbon dioxide are present. Once <strong>the</strong> excess carbon has<br />
been converted to carbon monoxide, <strong>the</strong> alkali carbon<strong>at</strong>e will decompose <strong>at</strong><br />
temper<strong>at</strong>ures in excess <strong>of</strong> 1200°C. Experiments were also performed with a<br />
combin<strong>at</strong>ion <strong>of</strong> SOp, Cop, and O2 in <strong>the</strong> gas stream. Here, it was found th<strong>at</strong><br />
<strong>the</strong> alkali carbon<strong>at</strong>e is converted to <strong>the</strong> alkali sulf<strong>at</strong>e with no indic<strong>at</strong>ion <strong>of</strong><br />
alkali loss over <strong>the</strong> temper<strong>at</strong>ure range studied (< 1300°K).<br />
CONCLUSIONS<br />
Thus, <strong>the</strong> results <strong>of</strong> <strong>the</strong> measurements and experiments discussed above do<br />
provide a plausible way to begin an explan<strong>at</strong>ion for <strong>the</strong> distribution <strong>of</strong> alkali<br />
in che ash particul<strong>at</strong>es. To summarize:<br />
1. Under typical <strong>coal</strong> combustion conditions in an <strong>at</strong>mosphere rich in<br />
Cop and/or SOp, <strong>the</strong> alkalis in <strong>the</strong> organic fraction do not vaporize<br />
but remain bound in <strong>the</strong> ash as stable carbon<strong>at</strong>es or sulf<strong>at</strong>es.<br />
2. The alkalis in <strong>the</strong> inorganic fraction diffuse to <strong>the</strong> surface<br />
producing enrichment by a factor <strong>of</strong> about 13 to a depth <strong>of</strong> about<br />
100A.<br />
The results, however, do not provide conclusive evidence about <strong>the</strong> f<strong>at</strong>e<br />
<strong>of</strong> <strong>the</strong> alkalis. The effect <strong>of</strong> w<strong>at</strong>er vapor in <strong>the</strong> combustion stream has not<br />
yet been studied. Clearly, w<strong>at</strong>er could have an important effect on <strong>the</strong><br />
vaporiz<strong>at</strong>ion process. Fur<strong>the</strong>rmore, <strong>the</strong> reasoning we have followed to explain<br />
<strong>the</strong> absence <strong>of</strong> alkali enrichment in <strong>the</strong> submicron particles requires th<strong>at</strong> <strong>the</strong><br />
vol<strong>at</strong>iliz<strong>at</strong>ion <strong>of</strong> <strong>the</strong> alkalis in both <strong>the</strong> organic and inorganic fraction not<br />
be significant (say less than 20%).<br />
140