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 ...
components of the limestone bed of run 2481 changed as follows: CaO decreased by 1 dilution to 37% by the coal ash; SO3 increased to 28% by adsorption; and Na20 increased to 7.7% of the bed. Si02, A1203, Fez03 and MgO remained constant throughout the run after the initial eight hours. The concentrations of alumina and silica remain constant during the run indicating that the aluminosilicate clay particles leave the bed during combustion. On the other hand, the calcium oxide and sodium oxide which largely originate from the organic structure of the lignite are free to react with the SO2 and bed material increasing their concentration. OXIDE A Si02 10.76 A1203 11.70 FeO 4.82 MgO 5.71 CaO 18.11 Na20 12.70 so3 34.45 TABLE 3. CHEMICAL ANALYSIS DATA FOR FIGURE 1 TO 11. WT. % OXIDE H I B 12.45 11.20 0.55 1 .I4 32.86 3.99 37.25 Si02 15.50 19.66 A1203 10.28 0.15 FeO 0.75 0.37 MgO 3.84 0.09 CaO 40.45 53.36 Na20 1.91 1.74 so3 21.49 24.39 C D 8.22 12.16 18.94 8.94 6.94 3.02 11.86 5.73 12.63 12.83 10.14 17.97 30.80 38.27 E F G 31 .EO 47.80 48.32 19.13 10.03 10.61 13.14 9.95 9.48 10.27 4.44 6.26 19.82 20.28 20.29 2.04 6.11 3.73 3.39 0.43 0.52 J K L M 12.39 1.81 0.89 31.50 5.13 5.91 1.87 8.20 1.15 0.32 81.69 0.56 0.93 0.17 0.91 0.00 44.23 39.58 13.55 44.19 0.78 0.40 0.00 2.76 35.37 51.66 6.33 11.89 CONCLUSIONS I Agglomeration of the bed material can be manifested in many different ways depending on the chemical composition of the bed. The elements which have a ma- jor effect are sodium, calcium and sulfur which react with the bed material possibly forming possibly a molten phase. This phase causes other ash constituents to ad- here to the bed particles. As this phenomenon reoccurs many times, agglomeration becomes more severe. REFERENCE 1. Goblirsch, G.M., Vander Molen, R.H., and Hajicek, D.R., AFBC Testing of North Dakota Lignite, Sixth International Fluidized Bed Conference, Atlanta, Georgia, April, 1980. 178
I FIG. 1. Initial ash coating on quartz bed material. SEM/BEI image. Analysis A (Table 3). Run 2181, 40 hrs. FIG. 3. Quartz bed grains loosely ce- mented by sulfated aluminosilicate ash. SEM/BEI image. Analysis D given in Table 3. Run 2181, 69 hrs. 173 FIG. 2. Thickened nodular ash coating on quartz bed material. SEM/BEI image. Analysis B of fine light sulfated ash and C of darker interior of coarser ash particle (Table 3). Run 2181, 54 hrs. FIG. 4. Quartz bed agglomerate bonded by altered sulfated ash, bottom of the dot- ted boundary (analysis E); Ca-rich, S- poor glass, top of the dashed line (analy- sis F); and intermediate fringe of meli- lite or augite crystals. SEM/BEI image. Run 2181, 69 hrs.
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components <strong>of</strong> <strong>the</strong> limestone bed <strong>of</strong> run 2481 changed as follows: CaO decreased by 1<br />
dilution to 37% by <strong>the</strong> <strong>coal</strong> ash; SO3 increased to 28% by adsorption; and Na20<br />
increased to 7.7% <strong>of</strong> <strong>the</strong> bed. Si02, A1203, Fez03 and MgO remained constant<br />
throughout <strong>the</strong> run after <strong>the</strong> initial eight hours.<br />
The concentr<strong>at</strong>ions <strong>of</strong> alumina and silica remain constant during <strong>the</strong> run<br />
indic<strong>at</strong>ing th<strong>at</strong> <strong>the</strong> aluminosilic<strong>at</strong>e clay particles leave <strong>the</strong> bed during combustion.<br />
On <strong>the</strong> o<strong>the</strong>r hand, <strong>the</strong> calcium oxide and sodium oxide which largely origin<strong>at</strong>e from<br />
<strong>the</strong> organic structure <strong>of</strong> <strong>the</strong> lignite are free to react with <strong>the</strong> SO2 and bed m<strong>at</strong>erial<br />
increasing <strong>the</strong>ir concentr<strong>at</strong>ion.<br />
OXIDE A<br />
Si02 10.76<br />
A1203 11.70<br />
FeO 4.82<br />
MgO 5.71<br />
CaO 18.11<br />
Na20 12.70<br />
so3 34.45<br />
TABLE 3. CHEMICAL ANALYSIS DATA FOR FIGURE 1 TO 11.<br />
WT. %<br />
OXIDE H I<br />
B<br />
12.45<br />
11.20<br />
0.55<br />
1 .I4<br />
32.86<br />
3.99<br />
37.25<br />
Si02 15.50 19.66<br />
A1203 10.28 0.15<br />
FeO 0.75 0.37<br />
MgO 3.84 0.09<br />
CaO 40.45 53.36<br />
Na20 1.91 1.74<br />
so3 21.49 24.39<br />
C D<br />
8.22 12.16<br />
18.94 8.94<br />
6.94 3.02<br />
11.86 5.73<br />
12.63 12.83<br />
10.14 17.97<br />
30.80 38.27<br />
E F G<br />
31 .EO 47.80 48.32<br />
19.13 10.03 10.61<br />
13.14 9.95 9.48<br />
10.27 4.44 6.26<br />
19.82 20.28 20.29<br />
2.04 6.11 3.73<br />
3.39 0.43 0.52<br />
J K L M<br />
12.39 1.81 0.89 31.50<br />
5.13 5.91 1.87 8.20<br />
1.15 0.32 81.69 0.56<br />
0.93 0.17 0.91 0.00<br />
44.23 39.58 13.55 44.19<br />
0.78 0.40 0.00 2.76<br />
35.37 51.66 6.33 11.89<br />
CONCLUSIONS I<br />
Agglomer<strong>at</strong>ion <strong>of</strong> <strong>the</strong> bed m<strong>at</strong>erial can be manifested in many different ways<br />
depending on <strong>the</strong> chemical composition <strong>of</strong> <strong>the</strong> bed. The elements which have a ma-<br />
jor effect are sodium, calcium and sulfur which react with <strong>the</strong> bed m<strong>at</strong>erial possibly<br />
forming possibly a molten phase. This phase causes o<strong>the</strong>r ash constituents to ad-<br />
here to <strong>the</strong> bed particles. As this phenomenon reoccurs many times, agglomer<strong>at</strong>ion<br />
becomes more severe.<br />
REFERENCE<br />
1. Goblirsch, G.M., Vander Molen, R.H., and Hajicek, D.R., AFBC Testing <strong>of</strong><br />
North Dakota Lignite, Sixth Intern<strong>at</strong>ional Fluidized Bed Conference, Atlanta,<br />
Georgia, April, 1980.<br />
178