U.S. patent number 3,896,557 [Application Number 05/468,315] was granted by the patent office on 1975-07-29 for process for drying and stabilizing coal.
This patent grant is currently assigned to Sun Oil Company (Delaware). Invention is credited to William S. Bradley, Walter H. Seitzer.
United States Patent |
3,896,557 |
Seitzer , et al. |
July 29, 1975 |
Process for drying and stabilizing coal
Abstract
A process for drying lignitic and subbituminous coal containing
from about 25 to about 40% by weight water which comprises heating
said coal with a fluidizing combustion gas stream containing from
about 7 to about 9% by volume of oxygen to reduce the moisture
content to a level of from about 8 to about 12% whereby said coal
is also stabilized against spontaneous combustion.
Inventors: |
Seitzer; Walter H. (West
Chester, PA), Bradley; William S. (Richardson, TX) |
Assignee: |
Sun Oil Company (Delaware)
(Southland Center, TX)
|
Family
ID: |
23859311 |
Appl.
No.: |
05/468,315 |
Filed: |
May 9, 1974 |
Current U.S.
Class: |
34/371 |
Current CPC
Class: |
C10L
9/00 (20130101); F26B 3/08 (20130101); C10F
5/00 (20130101); C10L 9/06 (20130101) |
Current International
Class: |
C10L
9/00 (20060101); C10L 9/06 (20060101); C10F
5/00 (20060101); F26B 3/02 (20060101); F26B
3/08 (20060101); F26b 003/08 (); F26b 007/00 () |
Field of
Search: |
;34/10,12
;432/14,15 |
References Cited
[Referenced By]
U.S. Patent Documents
|
|
|
3755912 |
September 1973 |
Hamada et al. |
|
Primary Examiner: Camby; John J.
Attorney, Agent or Firm: Church; George L. Johnson; Donald
R. Lipsitz; Paul
Claims
The invention claimed is:
1. A process for drying lignitic and subbituminous coal containing
from about 25 percent to about 40% by weight water which comprises
heating said coal with a fluidizing combustion gas stream
containing from about 7 percent to about 9% by volume of oxygen to
reduce the moisture content to a level of from about 8 to about 12%
whereby said coal is also stabilized against spontaneous
combustion.
2. The process of claim 1 where the coal is dried to a moisture
level of from about 9 to about 10%.
3. The process of claim 1 where the coal is a subbituminous
coal.
4. The process of claim 3 where the coal is Wyodak coal.
5. The process of claim 1 where the coal is lignite.
Description
Lignitic and subbituminous coals are received from the mine
containing from about 25 to about 40% internal moisture and such
coals are usually subjected to a drying procedure before shipment
and use. Numerous types of equipment and techniques for such coal
drying are available and have been used for some time. In general,
a hot combustion gas is used to drive moisture from the coal and
this is done either by passing such gases through a bed of the
coal, often a fluidized bed, or by passing the coal through a kiln
or other rotary device while the gases are passed through. A
particularly useful commercial device for such coal drying is the
Parry Dryer (see U.S. Pat. No. 2,666,269) which employs the hot
combustion drying gases to fluidize the coal. In commercial use the
combustion gases are usually obtained from coal or fuel oil and the
fuel-air ratio is maintained so that the combustion gases contain
about 5 percent by volume of oxygen. The dried coal emerging from
the dryer generally contains from 0.5 to about 10% by weight, and
might even be somewhat higher.
One of the characteristics of dried coal is its tendency toward
spontaneous combustion and this becomes a serious problem during
the shipment and storage of such coal. Coal subjected to the above
described drying process is somewhat improved in its spontaneous
combustion character, but additional stability is still desired in
order to further mitigate or eliminate the fire hazard present in
shipping and storing dried coal.
It has now been found that a significant improvement in increasing
the stability of coal dried by the above described process can be
obtained by carefully controlling the oxygen content of the drying
gases and by controlling the moisture content of the dried coal. In
accord with the invention, lignitic or subbituminous coal
containing from about 25 to about 40% by weight of water is dired
and increased stabilization to spontaneous combustion is obtained
by heating said coal in a fluidized bed dryer with fluidizing
combustion gases containing from about 7 to about 9% by volume of
oxygen until the moisture content of said coal is from about 8 to
about 12% by weight. It is quite unexpected that by exercising
initial control of the oxygen content of the drying gases and the
moisture content of the dried coal as defined above that a coal of
superior stability is obtained.
The coals used in the process of the invention will be, as
indicated, lignitic and subbituminous coals and will include North
Dakota lignite, Powder River subbituminous coal, Wyodak coal, and
the like. Such coals usually contain from about 20 to 40 percent
water as they come from the mine.
The drying procedure will be carried out with a fluidized bed type
dryer where the drying gas is used to fluidize the bed. A preferred
type of dryer is the Parry Dryer referred to above and the process
of the invention will be illustrated with such equipment.
In operation, the raw coal is fed to the dryer column through a
screw feeder. The coal particles are entrained in a stream of high
velocity gases from a combustion furnace and carried through the
column to a primary separator. The drying is accomplished almost
instantaneously due to the intimate mixing of coal with the
turbulent gases in the dryer column. Coal and gases leaving the
dryer column expand into the primary separator where the velocity
is decreased to allow the main product to drop out and the gases
continue to move slowly to the entrance of cyclones, or secondary
separators. This action drops out up to 98 percent of the coal, or
all but the fine dust. The coal is discharged from a conical bottom
of the primary separator through a rotary valve to be carried away
on a dry product conveyor. The gases flow through high efficiency
cyclones to a common stack and are discharged to the
atmosphere.
The fine dust is separated from the gas stream in the cyclones,
collected in a hopper and discharged to a conveyor. The major part
of the dust collected is introduced into the primary combustion air
at controlled rates, conveyed to the furnace, and burned. The
particle size of about 80 percent minus 200 mesh makes it ideal for
use as a pulverized fuel for the combustion furnace which furnishes
the fluidizing drying gases. However, materials other than coal,
such as gas or oil may be used for fuel.
A portion of the stack gas may be recycled to the furnace for
tempering the drying gases. This eliminates the use of excess air
for tempering and allows accurate control of the oxygen content in
the drying system.
The dryer operates under a positive pressure to prevent air leakage
into the system. Before feeding coal to the dryer, the system is
preferably purged with inert gas obtained from an oil fire in the
furnace. The primary air blower is a positive displacement type and
supplies air to the oil fire at a constant rate. The fuel oil is
maintained at a controlled pressure and metered by the atomizing
nozzle in the burner. This maintains the desired fuel-air ratio, so
that the products of combustion are essentially inert. The oil fire
is continued for a predetermined interval, normally about 5
minutes, until the system is completely purged. The recycle blower,
fuel dust feeder, and forced draft blower are then started after
the system is purged. The fuel oil is no longer required and may be
turned off a few minutes after the coal dust feed is started.
The drying gases rise to operating temperatures of from about
1000.degree. to about 2200.degree.F. about 5 minutes after the dust
is started, and then the raw coal feeder is started. The moisture
in the dried product is held at the desired value of from about 8
to about 12%, preferably about 9 to about 10% by a temperature
controller that regulates the heat liberated in the furnace. This
is accomplished by controlling the forced draft damper and the fuel
dust feeder to maintain a constant temperature of from about
150.degree. to 250.degree.F. (preferably about 180.degree. to about
230 .degree.F.) at the top of the drying column. This temperature
is recorded on the controller.
The temperature control system is designed to vary the fuel dust
fed to the furnace as required to hold the drying column top
temperature constant. An oxygen recorder is used to make a
continuous record of the oxygen content of the stack gases which
will be from about 0 to about 10%. Forced draft air is varied as
necessary to hold the desired oxygen content of the input gases
from about 7 to about 9% by volume oxygen content as required by
the process of the invention.
In order to more fully exemplify the process of the invention the
following examples are given:
Wyodak coal of one-fourth inch to 0 mesh containing about 30%
moisture (inherent) was dried in a Parry Dryer. The temperature of
the input gases was from about 1900.degree. to about 2100.degree.F.
and other conditons of the various runs are shown in the following
table:
Percent Percent Moisture Example Oxygen Content Content Of No. Of
Drying Gases Dried Coal ______________________________________ A
4.5 5 B 8.6 5 C 4.2 5 D 8.4 5 E 3.5 10 F 7.5 9.4
______________________________________
Each of the above samples of dried coal was subjected to a
stability test carried out by placing the coal in a Dewar flask
fitted at the bottom with a sparging tube to pass oxygen through
the coal and equipped with a temperature measuring device. The coal
(450g.) in Dewar flask (70 mm.I.D.) is about 200 mm. in depth and
oxygen saturated with water is passed through it at 62.degree.C. at
a rate of 200 ml/min. The time for combustion of the coal to occur
is noted as shown by the sudden temperature increase and is taken
as a measure of stability. The results are shown in the following
table:
Example No. Hours To Combustion
______________________________________ A 2.5 B 2.7 C 1.6 D 2.0 E
9.2 F Did not combust ______________________________________
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