TECHNICAL FIELD
The present invention pertains to a coal deactivation processing device
performing deactivation processing of coal with a processing gas that contains
oxygen.
5
BACKGROUND ART
Low-grade coal (low rank coal) such as lignite or sub-bituminous coal having
high moisture content has low calorific power per unit weight . Therefore, modification
to decrease oxygen reactivity is performed by heating in a low-oxygen atmosphere,
10 along with drying and dry distillation. As such, modified coal having high calorific
power per unit weight is produced while preventing spontaneous combustion.
CITATION LIST
Patent Literatures
15 Patent Document 1: Japanese Unexamined Patent Application Publication No.
2007-237011A
Patent Document 2: WO/95/13868
SUMMARY OF THE INVENTION
20 Technical Problem
A device has been developed as a coal deactivation processing device for
performing deactivation processing of dry distilled coal obtained by drying and dry
distillation of the above-described low-grade coal. The device is provided with a
rotary kiln and feed pipes. Dry distilled coal and a processing gas are supplied into the
25 rotary kiln. The feed pipes are arranged within the rotary kiln neighboring each other
in the circumferential direction. A coolant flows in each deed pipe.
The above-described coal deactivation processing device causes the rotary kiln
and the plurality of feed pipes to rotate. As such, the dry distilled coal is agitated by
the rotation of the rotary kiln body while the coolant flowing within the feed pipes
30 cools the dry distilled coal. In addition, the plurality of feed pipes pass through an
accumulated coal layer of the dry distilled coal within the rotary kiln and lift the dry
distilled coal higher than a coal layer surface, then drop the dry distilled coal onto the
3
coal layer surface from above, thereby further agitating the dry distilled coal . Then the
deactivation processing of the dry distilled coal is performed by the processing gas .
The above-described agitation is performed repeatedly while the dry disti lled coal is
displaced from a base end side to a tip end side of the rotary kiln, such that the dry
distilled coal is gradually pulverized5 .
In the above-described coal deactivation processing device, having a large pipe
diameter for the feed pipes leads to a large volume of the dry distilled coal being
loaded onto the feed pipes in correspondence with the size of the feed pipes . This
causes overly advanced pulverization of the dry distilled coal . There has been a
10 possibility that this pulverized dry distil led coal may accompany the processing gas
supplied within the rotary kiln and be ejected to outside the system along with the
processing gas, thereby decreasing the yield of deactivation processed coal .
Conversely, having a small pipe diameter for the feed pipes leads to a small volume of
the dry distilled coal being loaded onto the feed pipes in correspondence with the size .
15 This causes a decrease in the contact efficacy between the dry distilled coal and the
processing gas. There has been a possibility that the deactivation processing of the dry
distilled coal may not be performed in an efficient manner.
In consideration of this background, the present invention has been made in
order to solve the above-described problem, and an object thereof is to provide a coal
20 deactivation processing device enabling oxygen to be adsorbed to the surface of the
coal in an efficient manner while preventing spontaneous combustion of the coal.
Solution to Problem
A coal deactivation processing device according to a first aspect of the
25 invention and solving the above-described problem performs deactivation of coal with
a processing gas that includes oxygen. The coal deactivation processing device
includes a kiln body provided rotatably into which the coal and the processing gas are
supplied, with a feed pipe provided so as to be able to rotate along with the kiln body,
extending along a lengthwise direction of the kiln body, and having a coolant flowing
30 therein, and with a protruding portion provided on an outer circumferenti al section of
the feed pipe, protruding in a direction of rotation of the feed pipe, and having a hat
shape in a radial cross-section of the feed pipe. The feed pipe and the protruding
portion are arranged so as to pass through an accumulated coal layer of the coal within
the kiln body upon rotation of the kiln body.
4
A coal deactivation processing device according to a second aspect of the
invention and solving the above-described problem is the coal deactivation processing
device according to the first aspect described above, where the protruding portion has
a V shape in the radial cross-section of the feed pipe. Also, a vertex of the protruding
portion matches a path of a central axis of the feed pipe5 .
A coal deactivation processing device according to a third aspect of the
invention and solving the above-described problem is the coal deactivation processing
device according to one of the first and second aspects described above, where the
protruding portion has a symmetrical shape in a plane passing through the vertex of
10 the protruding portion and the central axis of the feed pipe. Also, an angle formed by
a straight line joining respective intersections of the feed pipe with two tangent lines
tangent to the feed pipe passing through the vertex of the protruding portion, and by
one of the two tangent lines, is greater than an angle of repose.
A coal deactivation processing device according to a fourth aspect of the
15 invention and solving the above-described problem is the coal deactivation processing
device according to any one of the first to third aspects described above, where a
distance between the vertex of the protruding portion and the central axis of the feed
pipe is equal to or less than twice a radius of the feed pipe.
20 Advantageous Effects of Invention
According to the coal deactivation processing device pertaining to the present
invention, the protruding portion having the hat shape is provided on the outer
circumferential section of each of the feed pipes so as to protrude toward the direction
of rotation of the respective feed pipe. The feed pipes and the protruding portions are
25 arranged so as to pass through the accumulated coal layer of the coal in the kiln body
upon rotation of the kiln body. As such, the coal is agitated by the rotation of the kiln
body while the coal is also cooled by the coolant flowing in the feed pipes . In
addition, a predetermined volume of the coal is lifted up by the feed pipes and the
protruding portions higher than the coal layer surface within the rotary kiln body and
30 then dropped from above, thus enabling agitation of the coal and providing a suitable
form of opportunities for contact between the coal and the processing gas . As a result,
the spontaneous combustion of the coal may be prevented while causing oxygen to be
adsorbed to the surface of the coal in an efficient manner. Furthermore, in comparison
to a situation where the protruding portions are not provided on the feed pipes, the
35 overall length of the kiln body may be made shorter, thus enabling miniaturizat ion of
the device.
5
BRIEF DESCRIPTION OF DRAWINGS
FIG. 1 is an overall configuration view of an embodiment of a coal deactivation
processing device pertaining to the present invention.
FIG. 2 is a magnified view of a cross section taken along line II-II of FIG. 15 .
FIG. 3 is a magnified view of a feed pipe provided on the coal deactivation
processing device.
DESCRIPTION OF EMBODIMENTS
10 An embodiment of the coal deactivation processing device pertaining to the
present invention is described with reference to the drawings. However, the present
invention is not limited merely to the following embodiment as described with
reference to the drawings.
The embodiment of the coal deactivation processing device pertaining to the
15 present invention is described with reference to FIG. 1 to FIG. 3.
As illustrated in FIG. 1, a coal deactivation processing device 100, performing
deactivation processing of dry distilled coal 1, is equipped with a hopper 101
receiving the dry distilled coal 1 and with a screw feeder 102 provided with a base end
side being continuous with a feed aperture of the hopper 101 and serving as rotational
20 transport means of transporting the coal 1 within the hopper 101 from one end side
(the base end side) to another end side (a tip end side) via rotation.
The tip end side of the screw feeder 102 is continuous with a base end side of a
rotary kiln body (kiln body) 103 having a tubular shape. The base end side of the
rotary kiln body 103 is continuous with a base end side casing 111 via a sealing device
25 108. A gas intake aperture 111a taking in a processing gas 13 is provided on a top
portion of the base end side casing 111. The gas intake aperture 111a is connected to a
tip end side of a processing gas supply pipe 121 supplying the processing gas 13. A
blower 127 and a heating device 128 are provided in the path of the processing gas
supply pipe 121.
30 A tip end side of an air supply pipe 122 supplying air 11 and a tip end side of a
nitrogen supply pipe 123 supplying nitrogen gas 12 are respectively connected to the
base end side of the processing gas supply pipe 121. The base end side of the air
6
supply pipe 122 is open to the atmosphere. The base end side of the nitrogen supply
pipe 123 is connected to a nitrogen supply source 124, such as a nitrogen gas tank.
Flow rate regulation valves 125, 126 are respectively provided in the paths of the air
supply pipe 122 and the nitrogen supply pipe 123.
The tip end side of the rotary kiln body 103 is continuous with a tip end sid5 e
casing 112 via sealing devices 109a, 109b. A gas ejection aperture 112a ejecting used
processing gas 14 is provided on a top portion of the tip end side casing 112. The gas
ejection aperture 112a is connected to a base end side of a processing gas ejection pipe
131 ejecting the used processing gas 14. A temperature sensor 131a is provided in the
10 path of the processing gas ejection pipe 131. A chute 112b dropping and ejecting
deactivation processed coal (upgraded coal) 3 is provided on a bottom portion of the
tip end side casing 112.
A projecting portion 104 having a ring shape is provided on the tip end side and
the base end side of an outer circumferential section of the rotary kiln body 103. The
15 projecting portion 104 is supported by a roller 105. A gear 106 engaging with a gear
107a of a drive motor 107 is provided on the outer circumferential section of the
rotary kiln body 103. As a result, the rotary kiln body 103 is made to rotate by the
rotation of the gear 107a of the drive motor 107.
The above-described coal deactivation processing device 100 is further
20 equipped with a cooling device 140. The cooling device 140 is equipped with a
bearing 145 fixed to a side wall portion 103a of the tip end side of the rotary kiln body
103. The cooling device 140 is equipped with a coolant feed header 141 feeding a
coolant 21 from outside the system. The coolant feed header 141 is provided on the
bearing 145. The coolant feed header 141 is connected to a feed pipe 142 feeding the
25 coolant 21. The feed pipe 142 is provided in plurality (for example, as a double pipe)
with, for example, eight pipes being connected (see FIG. 2). The cooling device 140 is
equipped with a coolant ejection header 146 ejecting used coolant 22 that has passed
through the feed pipes 142 to outside the system.
The plurality of feed pipes 142 are arranged, as illustrated in FIG. 1 and FIG. 2,
30 within the rotary kiln body 103 so as to neighbor each other with equal spacing along
a circumferential direction of the rotary kiln body 103. The plurality of feed pipes 142
are arranged at respective positions so as to, upon rotation of the rotary kiln body 103,
pass through an accumulated coal layer of the coal 2 despite a fill ratio of the coal 2
within the rotary kiln body 103 being from 10 to 15%, for example. In addition, the
35 plurality of feed pipes 142 are arranged such that a distance D1 from a respective
7
central axis C2 of each of the feed pipes 142 to a central axis C1 of the rotary kiln
body 103 is consistently equal. The plurality of feed pipes 142 extend in parallel to the
central axis C1 of the rotary kiln body 103 within the rotary kiln body 103, and extend
across the rotary kiln body 103 from the tip end side to the base end side . As a result,
the temperature of a region where the coal 2 undergoes deactivation processing by th5 e
processing gas 13 supplied within the rotary kiln body 103 is adjusted by the coolant
21 flowing within the feed pipes 142 to a temperature at which spontaneous
combustion of the coal 2 does not occur.
The plurality of feed pipes 142 are arranged so as to pass through the side wall
10 portion 103a of the rotary kiln body 103. The plurality of feed pipes 142 are each
supported by support jigs (not illustrated in the drawings) arranged at a plurality of
locations in a lengthwise direction. As a result, the plurality of feed pipes 142 are
made to rotate about the central axis C1 of the rotary kiln 103 along with the rotary
kiln 103 upon rotation of the rotary kiln 103.
15 Here, the parameters of the above-described feed pipes 142 are described with
reference to FIG. 2 and FIG. 3.
In FIG. 2, a direction of rotation A is a direction of rotation of the rotary kiln
body 103. A path L1 is followed by the central axis C2 of each of the plurality of feed
pipes 142, and a tangent line L2 is tangent to the path L1. In FIG. 2 and FIG. 3, a
20 bisector line L3 indicates a protruding portion 143, described later. In FIG. 3, tangent
lines L4, L5 are tangent to the feed pipe 142 passing through a vertex 143c of the
protruding portion 143. A support line L11 passes through a point of contact P1
between the feed pipe 142 and the tangent line L5 and through a point of contact P2
between the feed pipe 142 and the tangent line L4. Support lines L12, L13
25 respectively pass through the central axis C2 of the feed pipe 142 and the points of
contact P1, P2. An angle α is an acute angle formed by the bisector line L3 and the
tangent line L5 (an inside plane portion 143a of a hat) and represents the angle (a hat
angle) of the protruding portion. Similarly, an angle β is an acute angle formed by the
bisector line L3 and the support line L12. An angle θ is an acute angle formed by the
30 tangent line L5 and the support line L11. Here, the support lines L11, L12, L13 form
an isosceles triangle with the central axis C2 at the vertex. Given that the support line
L12 and the tangent line L5 form a right angle, the angle β is thus equal to the angle θ.
As illustrated in FIG. 2 and FIG. 3, the feed pipe 142 has a circular crosssection
in the radial direction. The protruding portion 143 is provided on the outer
35 circumferential section of the feed pipe 142, and forms a hat shape protruding in the
8
direction of rotation A of the feed pipe 142. More specifically, the protruding portion
143 forms a V shape as seen in a radial cross-section of the feed pipe 142. The
protruding portion 143 is arranged at a position so as to, similarly to the feed pipe
142, upon rotation of the rotary kiln body 103, pass through the accumulated coal
layer of the coal 2 despite the fill ratio of the coal 2 within the rotary kiln body 105 3
being from 10 to 15%, for example.
The protruding portion 143 includes an inside plane portion 143a positioned on
a central axis C1 side of the rotary kiln body 103, and an outside plane portion 143b
positioned on an outer circumferential surface side of the rotary kiln body 103. The
10 inside plane portion 143a and the outside plane portion 143b are connected at a tip end
side. The vertex 143c of the protruding portion 143 is positioned at a position
matching the path of the central axis C2 of the feed pipe 142. As a result, a volume of
coal lifted up above a coal layer surface 2a by the feed pipe 142 and the protruding
portion 143 is decreased in comparison to a situation where the hat shaped protruding
15 portion is not provided, thereby enabling suitable conditions to be provided. These
conditions provide appropriate opportunities for contact between the coal 2 and the
processing gas 13 by agitation of the coal 2, thereby enabling the effect of
deactivation processing of the coal 2 to be provided in an efficient manner.
The inside plane portion 143a and the outside plane portion 143b are positioned
20 with symmetry in a plane passing through a tip portion 143c of the protruding portion
143 and the central axis C2. That is, the protruding portion 143 is shaped with plane
symmetry. In addition, the angle θ formed between the line L11 and the tangent line
L5 is greater than the angle of repose. Here, the tangent line L5 is one of the two
tangent lines L4, L5 tangent to the feed pipe 142 and passing through the peak 143c of
25 the protruding portion 143. Also, the line L11 is a straight line joining the points P2,
P1 where the tangent lines L4, L5 are tangent to the feed pipe 142. This is done
because having the angle θ be smaller than the angle of repose increases the volume of
the coal 2 on the protruding portion 143, thereby promoting pulverization of the coal 2
and leading to a decreased yield of deactivation processed coal 3.
30 A distance D2 between the tip portion 143c of the protruding portion 143 and
the central axis C2 of the feed pipe 142 is preferably equal to or less than twice the
radius of the feed pipe 142, and more preferably equal to or less than the radius of the
feed pipe 142. This is because having the distance D2 exceed the above-given upper
limit decreases a heat transfer surface area between the coal 2 and the coolant 21
35 within each of the feed pipes 142. This leads to a decrease in the rate of heat
exchange, enables multiple spaces to be formed between the feed pipes 142 and the
9
protruding portions 143 within the rotary kiln 103, and decreases the volume of
processed coal.
Here, the feed pipes 142 and the respective protruding portions 143 may be
manufactured using a material having no reactivity with the coal 2 and that is
thermally resistant, such as steel, for example5 .
Furthermore, the above-described coal deactivation processing device 100
preferably satisfies the relationship of formula (1) given below, where a given feed
pipe 142 has a radius r2 and a distance D1 is defined from the central axis C1 of the
rotary kiln body 103 to the central axis C2 of the given feed pipe 142.
10 1/50 D1 < r2 < 1/10 D1 ...(1)
In a situation where the radius r2 of the feed pipe 142 is equal to or greater
than 1/10 D1 (one-tenth of D1), the pipe diameter of the feed pipe 142 is overly large
in comparison to the thickness of the coal layer within the rotary kiln body 103.
Given that the flow of the coal 2 is increased, this leads to the promotion of
15 pulverization of the coal 2. Conversely, in a situation where the radius r2 of the feed
pipe 142 is equal to or less than 1/50 D1 (one-fiftieth of D1), the feed pipe 142 is
narrow and heat exchange is not possible unless many of the feed pipes 142 are
arranged in the layer of the coal 2. This not only increases equipment costs, but also
increases the supply pressure of the coolant 21 supplied to the feed pipes 142, and
20 consumes a greater amount of power. As a result, satisfying formula (1), given above,
enables pulverization of the coal 2 to be constrained, and also enables equipment cost
increases and power consumption increases to be constrained.
In addition, the above-described coal deactivation processing device 100
preferably satisfies the relationship of formula (2), given below, where a distance D3
25 is defined between neighboring feed pipes 142, 142.
2r2 < D3 < 6r2 ...(2)
In a situation where the distance D3 between the neighboring feed pipes 142,
142 is equal to or less than 2r2 (twice the radius r2 of each of the feed pipes 142), then
the neighboring feed pipes 142, 142 are too close to each other and the coal 2 may
30 bridge the space between the neighboring feed pipes 142, 142. Conversely, in a
situation where the distance D3 between the neighboring feed pipes 142, 142 is equal
to or greater than 6r2 (six times the radius r2 of each of the feed pipes 142), then a
heat transfer surface area between the coolant 21 within the feed pipes 142 and the
10
coal 2 is reduced and as such, the cooling heat transfer surface area may not be
secured for the coal 2. Thus, satisfying formula (2), given above, enables the
occurrence of bridging of the space between the neighboring feed pipes 142, 142 to be
constrained and enables the cooling heat transfer surface area of the coolant 21 within
the feed pipes 142 to be secured for the coal 25 .
In the present embodiment, the processing gas supply pipe 121, the heating
device 128, the blower 127, the air supply pipe 122, the flow rate regulation valve
125, the nitrogen supply pipe 123, the flow rate regulation valve 126, the nitrogen
supply source 124, the base end side casing 111, the gas intake aperture 111a, and the
10 like constitute processing gas supply means. The coolant feed header 141, the feed
pipes 142, the protruding portion 143, the bearing 145, the coolant ejection header
146, and the like constitute the cooling device 140, which serves as cooling means.
The projecting portion 104, the roller 105, the gear 106, the drive motor 107, the gear
107a, and the like constitute rotation means. The hopper 101, the screw feeder 102,
15 and the like constitute coal supply means. The chute 112b of the tip end side casing
112 and the like constitute coal ejection means. The tip end side casing 112, the gas
ejection aperture 112a, the processing gas ejection pipe 131, and the like constitute
processing gas ejection means. Each of these means and the rotary kiln body 103, the
sealing devices 108, 109a, 109b, and the like constitute the coal deactivation
20 processing device 100.
Operations centered on the coal deactivation processing device 100 are
described next.
Upon being supplied to the hopper 101, the coal 1 is transported by the screw
feeder 102 within the rotary kiln body 103. At the other end, the air 11 and the
25 nitrogen gas 12 are supplied to the processing gas supply pipe 121 via the air supply
pipe 122 and the nitrogen supply pipe 123 by controlling a degree of aperture of the
flow rate regulation valves 125, 126 while controlling the operation of the blower 127 .
As a result, the processing gas 13 is obtained by combining the air 11 and the nitrogen
gas 12 (for example, with an oxygen concentration on the order of from 5 to 10%) .
30 The processing gas 13 is heated by the heating device 128 in accordance with
temperature data of the used processing gas 14 obtained by the temperature sensor
131a so that the temperature inside the rotary kiln body 103 is adjusted to within a
range of from 40 to 200°C. The processing gas 13 is then supplied within the rotary
kiln body 103 by the processing gas supply pipe 121 via the gas intake aperture 111a.
11
The rotary kiln body 103 is driven to rotate by the rotation of the gear 107a of
the drive motor 107 being transmitted via the gear 106. The coal 2 transported within
the rotary kiln body 103 along with the rotation of the rotary kiln body 103 is
displaced from the base end side to the tip end side of the rotary kiln body 103 while
being agitated. At this time, the coal 2 within the rotary kiln body 103 adsorbs th5 e
oxygen in the processing gas 13 supplied within the rotary kiln body 103. The coal 2
thus becomes the deactivation processed coal (upgraded coal) 3 as a result of this
oxygen adsorption, and is then transported to outside the system via the chute 112b .
The coal 2 in the rotary kiln body 103 produces heat by adsorbing the oxygen in the
10 processing gas 13. The temperature is therefore adjusted by the flow of the coolant 21
within the feed pipes 142 to a temperature at which spontaneous combustion of the
coal 2 does not occur.
The used processing gas (approximately from 50 to 70°C) 14 that has been used
in the deactivation processing of the coal 2 within the rotary kiln body 103 flows in
15 the same direction as the direction of transport of the coal 2. The used processing gas
14 flows from the gas ejection aperture 112a of the tip end side casing 112 provided
on the tip end side of the rotary kiln body 103 to the processing gas ejection pipe 131,
and is ejected outside the system via the processing gas ejection pipe 131.
Here, in the above-described coal deactivation processing device 100, the
20 plurality of feed pipes 142 are provided within the rotary kiln body 103 so as to rotate
about the central axis C1 of the rotary kiln body 103 along with the rotary kiln body
103 upon rotation of the rotary kiln body 103 so as to pass through the accumulated
coal layer of the coal 2 supplied to the rotary kiln body 103, and the respective
protruding portions 143 are provided on each of the feed pipes 142. Given the various
25 factors described above, the following operations are further obtained.
That is, in the present embodiment, the plurality of feed pipes 142 are driven to
rotate about the central axis C1 of the rotary kiln body 103 along with the rotation of
the rotary kiln body 103. Also, upon passing through the coal layer, the coal 2 is
lifted by the feed pipes 142 and the respective protruding portions 143 higher than the
30 coal layer surface 2a. Here, providing the protruding portion 143 on each of the feed
pipes 142 leads to a smaller volume of the coal 2 being lifted higher than the coal
layer surface 2a than is lifted at the angle of repose of the feed pipes 142. As a result,
providing the protruding portion 143 enables constraint of the pulverization of the
coal 2 due to excessive agitation of the coal 2.
12
As a result, according to the coal deactivation processing device 100 pertaining
to the present embodiment, the protruding portion 143 is provided on the outer
circumferential section of each of the feed pipes 142 so as to protrude toward the
direction of rotation A of the respective feed pipe 142. The feed pipes 142 and the
protruding portions 143 are arranged so as to pass through the accumulated coal laye5 r
of the coal 2 within the rotary kiln body 103 upon rotation of the rotary kiln body 103 .
As such, the coal 2 is agitated by the rotation of the rotary kiln body 103 while the
coal 2 is also cooled by the coolant 21 flowing in the feed pipes 142. In addition, a
predetermined volume of the coal 2 is lifted up by the feed pipes 142 and the
10 protruding portions 143 higher than the coal layer surface 2a within the rotary kiln
body 103 and dropped from above, thus enabling agitation of the coal 2 and providing
a suitable form of opportunities for contact between the coal 2 and the processing gas
13. As a result, the spontaneous combustion of the coal 2 may be prevented while
causing oxygen to be adsorbed to the surface of the coal 2 in an efficient manner.
15 Furthermore, in comparison to a situation where the hat -shaped protruding portions
are not provided on the feed pipes, the overall length of the rotary kiln body 103 may
be made shorter, thus enabling miniaturization of the device.
[Other Embodiments]
Here, the protruding portion 143 provided on each of the plurality of feed pipes
20 142 is not limited to a single shape. Two or more types of the protruding portion 143
may also be provided.
The coal deactivation processing device 100 has been described above as being
equipped with eight of the feed pipes 142. However, the quantity of the feed pipes is
not limited to eight. The coal deactivation processing device may also be equipped
25 with seven or fewer and with nine or more of the feed pipes.
13
Reference Signs List
1, 2, 3 Coal
11 Air
12 Nitrogen gas
13, 14 Processing ga5 s
21, 22 Coolant
100 Coal deactivation processing device
101 Hopper
102 Screw feeder
10 103 Rotary kiln body (Kiln body)
104 Projecting portion
105 Roller
106 Gear
107 Drive motor
15 107a Gear
108 Sealing device
109a, 109b Sealing device
111 Base end side casing
111a Gas intake aperture
20 112 Tip end side casing
112a Gas ejection aperture
112b Chute
121 Processing gas supply pipe
122 Air supply pipe
25 123 Nitrogen supply pipe
124 Nitrogen supply source
125, 126 Flow rate regulation valve
127 Blower
128 Heating device
30 131 Processing gas ejection pipe
131a Temperature sensor
140 Cooling device
141 Coolant feed header
142 Feed pipe
35 143 Protruding portion
143a Inside plane portion
143b Outside plane portion
14
143c Vertex
145 Bearing
146 Coolant ejection header
A Rotation direction of rotary kiln body
C1 Central axis of rotary kiln bod5 y
C2 Central axis of feed pipe
D1 Distance between central axis of rotary kiln body and central axis of feed pipe
D2 Distance between vertex of protruding portion and central axis of feed pipe
D3 Distance between neighboring feed pipes
10 L1 Path of central axis of feed pipe
L2 Tangent line of path of central axis of feed pipe
L3 Bisector line of protruding portion
L4, L5 Tangent line to feed pipe passing through vertex of protruding portion
L11 Support line
15 L12 Line passing through point P1 and central axis C2 of feed pipe
L13 Line passing through point P2 and central axis C2 of feed pipe
P1, P2 Point of contact
r1 Radius of rotary kiln body
r2 Radius of feed pipe
20 α Angle of protruding portion (Hat angle)
θ Angle between line L5 and line 11
β Angle between line L3 and line L12
15

CLAIMS:
1. A coal deactivation processing device performing deactivation of coal with a
processing gas that includes oxygen, comprising:
a kiln body provided rotatably into which the coal and the processin5 g
gas are supplied; and
a feed pipe provided so as to be able to rotate along with the kiln body,
extending along a lengthwise direction of the kiln body, and having a coolant
flowing therein,
10 a protruding portion provided on an outer circumferential section of the
feed pipe, protruding in a direction of rotation of the feed pipe, and having a
hat shape in a radial cross-section of the feed pipe; and
the feed pipe and the protruding portion being arranged so as to pass
through an accumulated coal layer of the coal within the kiln body upon
15 rotation of the kiln body.
2. The coal deactivation processing device according to claim 1, wherein
the protruding portion has a V shape in the radial cross-section of the
feed pipe, and
20 a vertex of the protruding portion matches a path of a central axis of the
feed pipe.
3. The coal deactivation processing device according to claim 1 or 2, wherein
the protruding portion has a symmetrical shape in a plane passing
25 through the vertex of the protruding portion and the central axis of the feed
pipe, and
an angle formed by a straight line joining respective intersections of the
feed pipe with two tangent lines tangent to the feed pipe passing through the
vertex of the protruding portion, and by one of the two tangent lines, is greater
30 than an angle of repose.
4. The coal deactivation processing device according to any one of claim 1 to
claim 3, wherein
16
a distance between the vertex of the protruding portion and the central
axis of the feed pipe is equal to or less than twice a radius of the feed pipe.