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 ...
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problems for many <strong>coal</strong> gas cleaning systems. The d<strong>at</strong>a show th<strong>at</strong><br />
refriger<strong>at</strong>ed methanol is effective in removing COS and no unusual<br />
solubility characteristics were evident <strong>at</strong> moder<strong>at</strong>e <strong>pressures</strong> and low<br />
liquid temper<strong>at</strong>ures.<br />
Trace Sulfur Compounds<br />
There are several sulfur compounds besides H2S and COS present in<br />
<strong>the</strong> gas fed to <strong>the</strong> AGRS which must be removed. Table 2 shows <strong>the</strong><br />
distribution <strong>of</strong> several <strong>of</strong> <strong>the</strong>se compounds in <strong>the</strong> AGRS. While <strong>the</strong>re is<br />
some sc<strong>at</strong>ter in <strong>the</strong> analyses for methyl mercaptan, thiophene, CS2, and<br />
ethyl mercaptan/dimethyl sulfide, it appears th<strong>at</strong> in most runs <strong>the</strong>y are<br />
removed to very low levels in <strong>the</strong> absorber.<br />
A point <strong>of</strong> potential enviromnental significance is th<strong>at</strong> while <strong>the</strong>se<br />
compounds are removed to low levels, <strong>the</strong>y are not completely accounted<br />
for in <strong>the</strong> flash and acid gas streams. This can be seen for methyl<br />
mercaptan and thiophene, which are present in rel<strong>at</strong>ively high levels in<br />
<strong>the</strong> feed gas. These compounds will accumul<strong>at</strong>e in <strong>the</strong> recircul<strong>at</strong>ory<br />
solvent and most likely eventually leave <strong>the</strong> system in one <strong>of</strong> three exit<br />
streams: sweet gas, flash gas, or acid gas. Because most sulfur<br />
recovery systems cannot tre<strong>at</strong> mercaptans and thiophene, <strong>the</strong>y will present<br />
emission problems if some additional method <strong>of</strong> tre<strong>at</strong>ing <strong>the</strong>se gases is<br />
not used. This can be a significant problem because <strong>the</strong> total sulfur<br />
from mercaptans, organic sulfides, CS2! and thiophene is approxim<strong>at</strong>ely<br />
half <strong>of</strong> <strong>the</strong> total sulfur associ<strong>at</strong>ed with COS. If <strong>the</strong>se compounds appear<br />
with <strong>the</strong> sweet gas, <strong>the</strong>y are likely to affect adversely downstream<br />
methan<strong>at</strong>ion c<strong>at</strong>alysts. The presence <strong>of</strong> <strong>the</strong>se compounds io <strong>the</strong> sweet gas<br />
stream is also a problem if <strong>the</strong> gas is to be burned for immedi<strong>at</strong>e use<br />
because <strong>the</strong> sulfur in <strong>the</strong>se compounds will be converted to SO2.<br />
In examining <strong>the</strong> results from all runs, <strong>the</strong>re appears to be some<br />
p<strong>at</strong>tern <strong>of</strong> trace sulfur species distribution. An increase in stripper<br />
temper<strong>at</strong>ure from -5.6'F to 48'F resulted in substantially gre<strong>at</strong>er amounts<br />
<strong>of</strong> mercaptan and thiophene in <strong>the</strong> acid<br />
distribute to all exit streams in most<br />
differences in process conditions.<br />
gas stream. CS seems to<br />
2<br />
<strong>of</strong> <strong>the</strong> runs despite <strong>the</strong><br />
Perhaps <strong>the</strong> most significant finding here is th<strong>at</strong> over a wide range<br />
<strong>of</strong> processing conditions, <strong>the</strong> presence <strong>of</strong> <strong>at</strong> least small amounts <strong>of</strong><br />
several different sulfur species is to be expected in all AGRS exit<br />
streams, and provision must be made for handling <strong>the</strong> associ<strong>at</strong>ed problems.<br />
Aliph<strong>at</strong>ic Hydrocarbons<br />
As <strong>the</strong> amount <strong>of</strong> vol<strong>at</strong>ile m<strong>at</strong>ter present in a particular <strong>coal</strong><br />
increases, <strong>the</strong> production <strong>of</strong> aliph<strong>at</strong>ic, arom<strong>at</strong>ic, and polynuclear<br />
arom<strong>at</strong>ic compounds produced during gasificztion also increases. Over <strong>the</strong><br />
range <strong>of</strong> conditions studied here, <strong>the</strong> most significant point to be made<br />
about <strong>the</strong> distribution <strong>of</strong> aliph<strong>at</strong>ic hydrocarbons is <strong>the</strong>ir presence in<br />
significant quantities in <strong>the</strong> flash and acid gases. Although flashing <strong>of</strong><br />
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