Liquefaction co-processing of coal shale oil at - Argonne National ...
Liquefaction co-processing of coal shale oil at - Argonne National ...
Liquefaction co-processing of coal shale oil at - Argonne National ...
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EXPERIMENTAL<br />
Wyodak <strong>co</strong>al was pretre<strong>at</strong>ed and tre<strong>at</strong>ed with steam in a semi-Row micro reactor <strong>at</strong> <strong>co</strong>ntrolled <strong>co</strong>ndi-<br />
tions to exclude oxygen. The appar<strong>at</strong>us is depicted in Figure 1. The main <strong>co</strong>mponents are a Milton Roy<br />
metering pump (29 to 290cm3/hr) which provides a <strong>co</strong>ntinuous and <strong>co</strong>nstant Row <strong>of</strong> distilled deoxy-<br />
gen<strong>at</strong>ed w<strong>at</strong>er to the re<strong>at</strong>or, a Tecam fluidized sand b<strong>at</strong>h (model SBS-4) <strong>co</strong>ntrolled with a Leeds and<br />
Northrup <strong>co</strong>ntroller (Electromax Ill), a Heli<strong>co</strong>id pressure gauge (0 to 3000 PSIG), an autoclave micro<br />
metering valve and a Picro reactor equipped with a she<strong>at</strong>hed thermo<strong>co</strong>uple (see Figure 2).<br />
The feed m<strong>at</strong>erial was an unwe<strong>at</strong>hered subbituminous Wyodak <strong>co</strong>al provided by EPRI in a w<strong>at</strong>er<br />
slurry kept in a sealed air-tight barrel (#4171). Table 1 shows the elemental analysis <strong>of</strong> samples taken<br />
from this barrel. Samples A and B were taken from the top and middle <strong>of</strong> the barrel and were suction<br />
dried for use. These were the main feed m<strong>at</strong>erial. About a 50 gm sampled <strong>of</strong> this m<strong>at</strong>erial was removed<br />
from the barrel and vacuum dried; a sample <strong>of</strong> this m<strong>at</strong>erial is repoted as sample C. A tew reactions<br />
were carried out with this m<strong>at</strong>erial.<br />
The suction dried <strong>co</strong>al was prepared in a Buchner filter, by applying suction to it tor about one hour.<br />
The top portion <strong>of</strong> the m<strong>at</strong>erial was removed from the filter and thoroughly mixed to insure a homogeneous<br />
sample for reaction. The moisture <strong>co</strong>ntent <strong>of</strong> this m<strong>at</strong>erial (z 30 wt %) was determined by weighing<br />
a sample before and after further drying in a vacuum oven <strong>at</strong> 45 O c for 6 hours. Duplic<strong>at</strong>e samples<br />
were used for moisture determin<strong>at</strong>ions.<br />
Suction dried Wyodak <strong>co</strong>al is paste-like, and is messy to bandle. A free-Rowing <strong>co</strong>al powder was<br />
obtained for reaction experiments by drying the <strong>co</strong>al in vacuum under mild he<strong>at</strong>ing. The vacuum dried<br />
<strong>co</strong>al wan prepared by suction drying in a Buchner funnel over nitrogen; the m<strong>at</strong>erial was then transferred<br />
in a jar 611ed with nitrogen, to a vacuum oven and dried for 72 hours <strong>at</strong> 45 O c. The experimental reac-<br />
tion procedure for vacuum dried <strong>co</strong>al was similar to suction dried <strong>co</strong>al except th<strong>at</strong> the separ<strong>at</strong>e moisture<br />
determin<strong>at</strong>ion <strong>of</strong> the dried <strong>co</strong>al was no longer necessary.<br />
To prepare for reaction the oven dried micro reactor (see Figure 2) was weighed and then filled with<br />
about 4 gm ot wet suction dried <strong>co</strong>al or 3 gm <strong>of</strong> vacuum dried <strong>co</strong>al and reweighed for an accur<strong>at</strong>e deter-<br />
min<strong>at</strong>ion <strong>of</strong> the quantity <strong>of</strong> m<strong>at</strong>erial charged to the reactor. The charged reactor was fitted into the<br />
appar<strong>at</strong>ns upon <strong>co</strong>nnecting tubings and fittings. The system was purged <strong>of</strong> air by Rushing with nitrogen.<br />
Enough w<strong>at</strong>er was pumped from the buret into the reactor to raise the pressure to SO pia, about 10 to<br />
nCm3 being required. The reactor was lowered into the sand b<strong>at</strong>h, the pressure adjusted to 750 psia<br />
with the aid <strong>of</strong> the micro metering valve, as w<strong>at</strong>er was pumped into the system <strong>at</strong> 0.4cm3/min. The<br />
steam gener<strong>at</strong>ed in the he<strong>at</strong>ing <strong>co</strong>il passed through the reactor, was <strong>co</strong>ndensed, and <strong>co</strong>llected in an Erlen-<br />
meyer Bask.<br />
At the termin<strong>at</strong>ion <strong>of</strong> an experiment the reactor WBB removed trom the aand b<strong>at</strong>h, and placed in a<br />
vacuum oven over night <strong>at</strong> 45 O c to remove any w<strong>at</strong>er. The reactor was then wekhed, the <strong>co</strong>ntents<br />
were removed and placed in a predried and weighed thimble. The reactor was then reweighed, the<br />
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