MODELING CHAR OXIDATION AS A FUNCTION OF PRESSURE ...
MODELING CHAR OXIDATION AS A FUNCTION OF PRESSURE ... MODELING CHAR OXIDATION AS A FUNCTION OF PRESSURE ...
To Air Water Bath Water Traps Flowmeters Vacuum Pumps F Soot-Leg Filter F Cooling Water Char-Leg Filter Flat- Flame Burner 144 Coal Particles from the Feeder Cyclone/ Char Collector Virtual Impactor Suction Probe Quartz Tower Cooling Water Quench Nitrogen Char Stream Soot Cloud Oxidizer Figure A.1. Schematic of the flat-flame burner and the particle collection and separation system. Fuel
To study the effects of steam, CO was used in the place of methane, while again maintaining the total flow rate and temperature profile in the first inch after the injection. Typical methane flames produce 16-25 mole-% steam in the post-flame gases. CO is an ideal alternative fuel to reduce steam in the post-flame gases, but as mentioned above, some hydrogen is necessary to stabilize the CO flame. Therefore, a total absence of steam in the post-flame gases was not possible. However, by using CO as the fuel, the steam concentration was reduced from about 17 mole-% to less than 1 mole-%. The four different char preparation conditions are described in Table A.1, and the measured temperature profiles for these conditions are given in Table A.2. Table A.1. Reactor Conditions Used Condition number #1 #2 #3* #4 Condition name CH4 fuel-rich CH4 fuel-lean CO fuel-rich CO fuel-lean CH4 (slpm) 4.84 1.52 0 0 CO (slpm) 0 0 16.9 6.41 H2 (slpm) 2.79 4.63 0.37 2 N2 (slpm) 5.41 0 6.46 0 Air (slpm) 38.6 43.7 21.0 40.7 Total flow rate (slpm) 51.6 49.9 44.8 49.1 Quench nitrogen (slpm) 65 65 65 65 Carrier nitrogen (slpm) 0.037 0.037 0.037 0.037 Equivalence ratio 1.37 0.58 1.96 0.49 Post-flame H2O (mole-%) 17.1 16.1 0.69 4.45 Post-flame O2 (mole-%) † 0 8.0 0 9.6 * Flow rates in condition #3 were measured with rotameters while those in other conditions were measured with mass flow meters. † Post-flame H 2O and O 2 mole fractions were calculated using EDWRDS code at 1600 K. 145
- Page 113 and 114: The value of the roughness factor w
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- Page 135 and 136: q = A 1p e − E 1 p / RT P os 1 +
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- Page 151 and 152: References Ahmed, S., M. H. Back an
- Page 153 and 154: Essenhigh, R. H., D. Fortsch and H.
- Page 155 and 156: Mehta, B. N. and R. Aris , “Commu
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- Page 161 and 162: Introduction Appendix A: Experiment
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To study the effects of steam, CO was used in the place of methane, while again<br />
maintaining the total flow rate and temperature profile in the first inch after the injection.<br />
Typical methane flames produce 16-25 mole-% steam in the post-flame gases. CO is an<br />
ideal alternative fuel to reduce steam in the post-flame gases, but as mentioned above,<br />
some hydrogen is necessary to stabilize the CO flame. Therefore, a total absence of<br />
steam in the post-flame gases was not possible. However, by using CO as the fuel, the<br />
steam concentration was reduced from about 17 mole-% to less than 1 mole-%.<br />
The four different char preparation conditions are described in Table A.1, and the<br />
measured temperature profiles for these conditions are given in Table A.2.<br />
Table A.1. Reactor Conditions Used<br />
Condition number #1 #2 #3* #4<br />
Condition name CH4 fuel-rich CH4 fuel-lean CO fuel-rich CO fuel-lean<br />
CH4 (slpm) 4.84 1.52 0 0<br />
CO (slpm) 0 0 16.9 6.41<br />
H2 (slpm) 2.79 4.63 0.37 2<br />
N2 (slpm) 5.41 0 6.46 0<br />
Air (slpm) 38.6 43.7 21.0 40.7<br />
Total flow rate (slpm) 51.6 49.9 44.8 49.1<br />
Quench nitrogen (slpm) 65 65 65 65<br />
Carrier nitrogen (slpm) 0.037 0.037 0.037 0.037<br />
Equivalence ratio 1.37 0.58 1.96 0.49<br />
Post-flame H2O (mole-%) 17.1 16.1 0.69 4.45<br />
Post-flame O2 (mole-%) †<br />
0 8.0 0 9.6<br />
* Flow rates in condition #3 were measured with rotameters while those in other conditions<br />
were measured with mass flow meters.<br />
† Post-flame H 2O and O 2 mole fractions were calculated using EDWRDS code at 1600 K.<br />
145