Information
-
Patent Grant
-
6187148
-
Patent Number
6,187,148
-
Date Filed
Monday, March 1, 199925 years ago
-
Date Issued
Tuesday, February 13, 200123 years ago
-
Inventors
-
Original Assignees
-
Examiners
- Beck; Shrive
- Ohorodnik; Susan
Agents
- Armstrong, Westerman, Hattori, McLeland & Naughton
-
CPC
-
US Classifications
Field of Search
US
- 202 256
- 202 258
- 202 270
- 202 239
- 202 151
- 202 135
- 251 205
- 251 207
- 251 209
- 251 122
- 251 310
- 110 163
- 137 62541
- 137 62547
-
International Classifications
-
Abstract
The present invention is a valve for a non-recovery coke oven which permits improved control of the gas pressure in the interior cavity of the oven. The valve has a rotating plug with a beveled end which progressively connects and disconnects the interior cavity of an oven with a downcomer valve disposed in an oven wall to change the gas pressure in the interior of the oven. By controlling the gas pressure the amount of combustion air entering the oven can be controlled giving an operator control over the thermal gradients established by combustion. The combustion of a majority of the coal gas in the flues below the oven floor creates a thermal gradient that rises through the oven floor, a gradient which is ideal for the production of an improved coke product.
Description
FIELD OF THE INVENTION
The present invention relates to a valve in a non-recovery coke oven between the downcomer passage and the oven interior for the purpose of regulating pressure inside the oven.
BACKGROUND OF THE INVENTION
A non-recovery coke oven is used to convert coal into blast furnace grade coke by heating the coal in a reducing atmosphere and operating under negative pressure. The oven is heated by external means to 2500° F. The external heat is shut off and a bed of coal is charged to the floor of the oven. The surface of the coal bed immediately generates combustible gas, herein referred to as “coal gas,” by the radiant energy absorbed by the oven roof from the external heat source. Approximately one-third (⅓) of the gas given off by the coal is selectively burned in a “primary” combustion by allowing “primary air” to be drawn into the oven interior through dampers in the doors of the oven. Next the combustion products and the remaining two-thirds (⅔) of the combustible gas are drawn through downcomers in the side walls of the oven into the sole flues, which are cavities below the oven floor for the combustion of gas. “Secondary air” is drawn into the sole flues to burn the remaining gases in a “secondary” combustion.
The heat generated by the primary combustion in the oven interior and the secondary combustion in the sole flues, provides the total heat to convert the coal into coke. Two independent thermal gradients occur, one beginning at the top of the coal bed and progressing downward and one beginning at the oven floor progressing upward. The proportion of primary and secondary air also controls the rate at which the thermal energy proceeds through the coal bed.
In the production of coke it is desirable to have a predominant secondary or “sole flue” coke thermal gradient beginning at the floor and progressing upward. The coke produced under this condition tends to be stronger and of high quality. The coke at the top of the bed resulting from the primary thermal gradient (called “bee-hive” coke) contains more air pockets and is somewhat spongy.
Controlling the amount of primary air in the oven interior is important. This is accomplished by manipulating air dampers in the oven doors. However, the volume of air that passes through a damper is not only a function of damper position, but also the negative pressure behind the damper which draws the air into the interior cavity of the oven. Oven interior pressure can be so different from outside pressure that even a damper position creating a small opening can overwhelm the cavity with primary air.
To solve the problem of pressure control, a valve in the downcomer passage or a “downcomer valve” acts as a variable restrictor which increases the pressure drop across the face of the downcomer. This permits a precise reduction of pressure in the interior of the oven which allows greater control of the inlet of primary combustion air.
OBJECTS OF THE INVENTION
It is the principal object of the invention to provide a valve in a non-recovery coke oven for the control and regulation of gas pressure in the interior of the oven.
It is an object of the present invention to provide a valve in a non-recovery coke oven that permits the precise reduction of gas pressure in the oven for improved control over inlet air.
It is another object of the present invention to provide a valve in a non-recovery coke oven downcomer between the oven and the sole flues which acts as a variable restrictor which increases the pressure drop across the face of the downcomer.
It is still another object of the present invention to provide a valve which improves the control over the operation of a non-recovery coke oven.
It is a yet another object of the present invention to provide an improved non-recovery coke oven which produces high quality coke.
It is a further object of the present invention to provide an improved method for operating a non-recovery coke oven.
Other objects, features and advantages of the present invention will become apparent from the following detailed description taken in conjunction with the accompanying drawings.
SUMMARY OF THE INVENTION
The present invention is a valve for connecting and disconnecting an interior of a non-recovery coke oven with an oven downcomer passage and oven sole flues. The valve has a housing having two passages, a first passage opening into the oven interior and a second passage opening into the downcomer passage. The second passage intersects the first passage at one end of the first passage which is opposite the oven interior. A rotatable cylindrical plug is disposed within the second passage and rotatable therein and has two ends, a first beveled end extending into an area of intersection between the first and second passages and a second end extending opposite the downcomer passage. Thus the non-recovery coke oven valve has a housing with two passages and a rotatable cylindrical plug disposable and rotatable within one of the passages of the housing.
Upon the rotation of the plug, the beveled end increases or decreases the intersecting area between the first and second passages creating an opening of variable size between the oven interior and the downcomer passage thereby controlling the pressure drop across the downcomer. This enables the change or reduction of pressure in the oven interior to permit enhanced control and regulation of the entrance of primary combustion air into the oven interior. The valve and method of operation allow for the control of the gas pressure within the interior of a non-recovery coke oven.
BRIEF DESCRIPTION OF THE DRAWINGS
FIG. 1
is a schematic view of a non-recovery coke oven with a downcomer valve in each downcomer;
FIG. 2
is a perspective view of a downcomer valve of a first embodiment suitable for the oven of
FIG. 1
;
FIG. 3
is a schematic view of a non-recovery coke oven having a downcomer valve of a second embodiment in each downcomer;
FIG. 4
is a perspective view of a downcomer valve of the second embodiment;
FIG. 5
is a cross-section view of the downcomer valve of
FIG. 4
;
FIG. 6
is a perspective view of a downcomer valve of the second embodiment showing the plug rotated in the closed position; and
FIG. 7
is a schematic view of a non-recovery coke oven with a downcomer valve of a third embodiment in each downcomer.
DETAILED DESCRIPTION OF THE INVENTION
The present invention is a valve and a method of operating a valve for a non-recovery coke oven which permits improved control and regulation of the gas pressure in the interior of the oven. By controlling the gas pressure the amount of combustion air entering the oven can be controlled giving an operator control over the thermal gradients established by combustion of gases in the oven. The combustion of a majority of coal gas in the sole flues below the oven floor creates a thermal gradient that rises through the oven floor, a gradient which is ideal for the production of an improved coke product.
Referring to
FIG. 1
, a non-recovery coke oven
1
is a large refractory structure constructed typically of silica brick
3
. The non-recovery coke oven
1
is used to convert a bed of coal
5
into blast furnace grade coke by heating the coal
5
in a reducing atmosphere and operating under negative pressure. The non-recovery coke oven
1
has a main interior cavity
7
which is formed by an arched roof
9
, a first side wall
11
, a second side wall
13
, an oven floor
15
, upon which lies coal
5
to be converted into coke, a front door
17
and a rear door
19
. Coal
5
is charged through front door
17
at the front end of non-recovery coke oven
1
and the finished coke product is removed through the rear door
19
at the rear end.
Below oven floor
15
is a plurality of sole flues
21
which typically run the length of non-recovery coke oven
1
and are separated by brick walls
23
typically made of silica brick. Each sole flue
21
has an interior cavity
25
, for the combustion of coal gas and air, which is formed by oven floor
15
at the top, a front wall and a rear wall (not shown) at the front and rear ends of non-recovery coke oven
1
, a bottom wall, which is part of a larger sub-structure
27
and either two brick walls
23
or one brick wall
23
and one first side wall
11
or one second side wall
13
. Sub-structure
27
forms the base of non-recovery coke oven
1
. Sub-structure
27
is typically made of steel strong enough for supporting the entire non-recovery coke oven
1
. Located within sub-structure
27
are a plurality of secondary air inlets
29
which communicate with sole flues
21
. Each sole flue
21
may have a plurality of secondary air inlets
29
which are located along the length of each sole flue
21
. Secondary air inlets
29
communicate with conduits
31
further associated with an air source (not shown) so that air can be injected directly into sole flues
21
. Additionally, air inlets
29
provide the means by which the sole flues
21
which are closest to the center of non-recovery coke oven
1
communicate with the respective sole flues
21
which closest to the side walls of non-recovery coke oven
1
.
Within first side wall
11
is located a downcomer
33
which is a passage for transporting gases from the interior cavity
7
of non-recovery coke oven
1
to sole flues
21
. Downcomer
33
, vertically disposed in side wall
11
, extends from an opening
30
at the top of side wall
11
to a point proximate sub-structure
27
, the point being adjacent to sole flue
21
. Horizontally disposed in side wall
11
is passage
32
, located proximate arched roof
9
, connecting downcomer
33
with interior cavity
7
and passage
34
connecting downcomer
33
with sole flue
21
. Opening
30
at the top of side wall
11
is suitable for receiving and mounting a downcomer valve
39
which extends vertically from opening
30
to passage
32
. Downcomer valve
39
can be rotated to obstruct passage
32
to completely close or disconnect interior cavity
7
from downcomer
33
.
A similar downcomer
35
is located in second side wall
13
and also communicates with interior cavity
7
and sole flues
21
of non-recovery coke oven
1
for transporting gases from the interior cavity
7
to sole flues
21
. Downcomer
35
, vertically disposed in side wall
13
, extends from an opening
36
at the top of side wall
13
to a point proximate sub-structure
27
, the point being adjacent to sole flue
21
. Horizontally disposed in side wall
13
is passage
38
, located proximate arched roof
9
, connecting downcomer
35
with interior cavity
7
and passage
40
connecting downcomer
35
with sole flue
21
. Opening
36
at the top of side wall
13
is suitable for receiving and mounting another downcomer valve
39
which extends vertically from opening
36
to passage
38
. Non-recovery coke oven
1
has two downcomer valves
39
which are the same and operate in the same way.
The formation of high quality coke from coal in non-recovery coke oven
1
is as follows: Non-recovery coke oven
1
is heated by an external means (not shown) to approximately 2,500° F. The external heat is removed and a bed of coal
5
is charged to oven floor
15
through front door
17
of non-recovery coke oven
1
. The surface of coal
5
immediately generates combustible gas, or coal gas, by the radiant energy absorbed from the external heat source by arched roof
9
. Approximately one third (⅓) of the gas generated is selectively burned in the interior cavity
7
by allowing air to be drawn in through dampers
37
in front door
17
and dampers (not shown) in the rear door
19
. Air that is drawn in through dampers
37
directly into the interior cavity
7
is called primary air.
The combustion products produced from the burning of the coal gas and the primary air and the remaining two thirds (⅔) of the coal gas are drawn through downcomers
33
and
35
into the plurality of sole flues
21
, by opening downcomer valves
39
so that downcomers
33
and
35
communicate with interior cavity
7
. Air is drawn into the plurality of sole flues
21
through the plurality of secondary air inlets
29
to burn the remaining combustible gases drawn down into sole flues
21
through downcomers
33
and
35
. The air which is drawn directly into the plurality of sole flues
21
through secondary air inlets
29
is called secondary air.
The heat generated by the combustion of primary air and coal gas in the interior cavity
7
of non-recovery coke oven
1
and the heat generated by the combustion of coal gas and secondary air in the plurality of sole flues
21
provides the total heat necessary to convert the bed of coal
5
into coke. Two independent thermal gradients occur, one beginning at the top of bed of coal
5
progressing downward to oven floor
15
and the other beginning at oven floor
15
and progressing upward. The proportion of primary and secondary air, which affects the thermal gradients established, controls the rate at which thermal energy proceeds through the bed of coal
5
on oven floor
15
.
It is desirable to have a predominant secondary or “sole flue” coke thermal gradient beginning at the oven floor
15
and progressing upward toward the arched roof
9
of non-recovery coke oven
1
. Coal converted to coke under conditions with a strong secondary thermal gradient tends to be stronger and of higher quality. The coke at the top of the bed which is subject mainly to the primary thermal gradient (called the “bee-hive” coke) contains more air pockets and is spongy.
Controlling the amount of primary air in the interior cavity
7
of non-recovery coke oven
1
is important because it affects the quality and properties of the coke produced. Control of the primary air is accomplished by manipulating air dampers
37
on front door
17
and the air dampers (not shown) on the rear door
19
. The problem that exists is that the volume of air that passes through the dampers
37
is not only a function of the position of individual damper
37
, but also the negative pressure behind each damper
37
which draws air into the interior cavity
7
. The pressure difference between the interior cavity
7
and the exterior of the oven can be so great that even a small opening of damper
37
can draw in more primary air than desired.
Downcomer valves
39
, as shown in
FIG. 1
, are variable restrictors between interior cavity
7
and downcomers
33
and
35
and can be operated to reduce the pressure difference between interior cavity
7
and the exterior of the oven. More particularly, downcomer valves
39
can be operated to obtain a particular pressure inside interior cavity
7
. They can be operated to reduce the negative pressure within interior cavity
7
so that any desired amount of primary air can be drawn in through dampers
37
.
In the preferred embodiment shown in
FIG. 1
, downcomer valves
39
are disposed in the existing brick work of side walls
11
and
13
. The brick work creates the vertical interior passages which are downcomers
33
and
35
as well as the horizontal passages connecting the downcomers
33
and
35
to interior cavity
7
and sole flues
21
. Alternatively, downcomer valves
39
can be built as units or structures having a housing which has similar passages as those created in the brick work of side walls
11
and
13
. A downcomer valve built with a housing, like that illustrated in
FIGS. 4-6
, can be installed into the side wall of a non-recovery coke oven so it functions like downcomer valve
39
in FIG.
1
.
FIG. 2
illustrates a close up view of the preferred embodiment of downcomer valve
39
suitable for use in non-recovery coke oven
1
of FIG.
1
. Because downcomer valve
39
is shown in
FIG. 2
independent of non-recovery coke oven
1
, a partial view of the brick work
41
of side wall
11
is also shown for purposes of illustration.
Downcomer valve
39
of
FIG. 2
, is associated with two passages: first passage
32
having an opening
43
at a first end
45
communicating with the interior cavity
7
of non-recovery coke oven
1
, and second passage
47
, which is the top portion of downcomer
33
, from first passage
32
to opening
30
, as shown in FIG.
1
. In
FIG. 2
, second passage
47
is only partially illustrated. The top of second passage
47
opens at the top of side wall
11
at opening
30
(
FIG. 1
) which is not shown in FIG.
2
. Second passage
47
intersects first passage
32
proximate a second end
49
of the first passage
32
. Again second passage
47
has opening
30
shown in
FIG. 1
for disposing and mounting downcomer valve
39
.
Downcomer valve
39
includes a cylindrical plug
53
with a beveled end
57
and a flanged portion
59
, of a larger diameter than cylindrical plug
53
, attached to the end opposite the beveled end
57
of cylindrical plug
53
. Associated with the intersection of the first passage
32
and the second passage
47
is the cylindrical plug
53
of downcomer valve
39
which is rotatable and disposable within the second passage
47
. In this embodiment, the second passage
47
of downcomer
33
is the same cross-sectional area as downcomer
33
of FIG.
1
. Although, in another embodiment, the cross-sectional area of passage
47
may be larger or smaller than that of downcomer
33
.
The cylindrical plug
53
has a first, beveled end
57
extending into the second end
49
of the first passage
32
. Upon the rotation of downcomer valve
39
the beveled end
57
cylindrical plug
53
increases or decreases the intersecting area between the first passage
32
and second passage
47
creating an opening of variable size between the oven interior cavity
7
and the downcomer
33
(and sole flues
21
) thereby controlling the pressure drop across the downcomer
33
. Downcomer valve
39
can be made of any castable material having good thermal shock resistance.
The beveled end
57
is preferably beveled at a 45° angle, but may be beveled in the range of about 30° to 60° and more preferably in the range of about 40° to 50°. Cylindrical plug
53
has flanged portion
59
opposite beveled end
57
. Flanged portion
59
is suitable for receiving a means for rotating cylindrical plug
53
. Flanged portion
59
, as illustrated in
FIG. 2
, has a groove
61
for the insertion of a tool
63
for rotating downcomer valve
39
.
Downcomer valve
39
is mounted in second passage
47
by inserting downcomer valve
39
into second passage
47
until flanged portion
59
contacts and rests on top of side wall
11
. Because the diameter of flanged portion
59
is larger the diameter of opening
30
of second passage
47
, downcomer valve
39
extends into downcomer
33
until the flanged portion
59
contacts the top of side wall
11
. Cylindrical plug
53
extends down into second passage
47
until beveled end
57
is located in the intersection of passage
32
and
47
. Downcomer valve
39
is of physical dimensions such that a good fit between the surface of cylindrical plug
53
and the surface of second passage
47
of downcomer
33
is created forming a seal that is relatively gas-tight and physically tight. Downcomer valve
39
is secured in downcomer
33
by gravity.
Downcomer valve
39
operates as follows: Upon the rotation downcomer valve
39
by tool
63
, the beveled end
57
of cylindrical plug
53
increases or decreases an intersecting area between first passage
32
and second passage
47
. The intersecting area can be increased or decreased progressively in an infinite number of increments. The increase or decrease of the intersecting area creates an opening of variable size between downcomer
33
and interior cavity
7
which enables the accurate control and regulation of gas pressure in the interior cavity
7
of non-recovery coke oven
1
, illustrated in FIG.
1
. The control of the pressure allows the control of the inlet of primary combustion air through dampers
37
of non-recovery coke oven
1
.
For example, after coal
5
is charged to oven floor
15
the surface of the coal
5
generates coal gas. Even with the production of coal gas, the pressure in the interior cavity
7
is still negative because the operating temperature of approximately 2,500° F. and the initial operating pressure. The pressure is such that even a small opening of dampers
37
in the front door
17
would draw in too much primary air which would flood the interior cavity
7
. In order to reduce the pressure difference between the interior cavity
7
and the outside of the non-recovery coke oven
1
, downcomer valve
39
, for example, is rotated from a shut or closed position, the position where the interior cavity
7
and downcomer
33
are not connected, to a position where a connection or opening exists between the interior cavity
7
and downcomer
33
. This causes the flow of gas residing in downcomer
33
and sole flues
21
to enter into the interior cavity
7
which results in a reduction of the pressure difference or an increase in positive pressure in interior cavity
7
. Downcomer valve
39
may be rotated back to the closed position when a desired reduction in pressure difference has occurred.
After the pressure difference as been reduced, dampers
37
are opened which allows the entrance of a controlled amount of primary air into interior cavity
7
. The dampers
37
are regulated as primary air enters the interior cavity
7
and the coal gas is burned by the primary air. Downcomer valve
39
is then fully opened so that the intersecting area between the first passage
32
and the second passage
47
is optimum. Next the combustion products and the remaining two-thirds (⅔) of the combustible gas are drawn through downcomer
33
into the sole flues
21
where the remaining coal gas is burned. Since non-recovery coke oven
1
can have one downcomer valve
39
located in each downcomer
33
and
35
, a first downcomer valve
39
in downcomer
33
may be rotated either simultaneously or independently of a second downcomer valve
39
in downcomer
35
to increase the rate of pressure change.
The tool
63
may be used to rotate downcomer valve
39
to connect and disconnect the interior cavity
7
with downcomer
33
, as shown in FIG.
2
. Again, the rotation of cylindrical plug
53
of downcomer valve
39
increases or decreases an intersecting area between the first passage
32
and the second passage
47
to control the pressure drop across the downcomer passage thereby enabling accurate reduction of a pressure difference in the interior cavity of a non-recovery coke oven so the inlet of primary air may be better controlled.
Furthermore, downcomer valve
39
can be optionally operated by a PLC (process logic controller) device
65
as represented by the dashed lines. A pressure sensor (not shown) also connected to the PLC device
65
may be added to the interior cavity
7
of non-recovery coke oven
1
so the downcomer valve
39
may be controlled based on information about gas pressure obtained from the pressure sensor in the interior cavity
7
. Often, however, downcomer valve
39
is controlled manually at the top of side wall
11
, in
FIG. 1
, by the use of a tool for rotating downcomer valve
39
.
FIG. 3
illustrates a non-recovery coke oven
67
similar to non-recovery coke oven
1
of FIG.
1
. An interior cavity
71
formed by an arched roof
73
, a first side wall
75
, a second side wall
77
, an oven floor
79
, upon which is charged a bed of coal
81
, and front and rear doors (not shown). Underneath oven floor
79
are a plurality of sole flues
69
connected by internal passages
70
.
Non-recovery coke oven
67
has a first downcomer valve
83
in a first downcomer passage
85
and a second downcomer valve
87
in a second downcomer passage
89
. Downcomer valves
83
and
87
are variable restrictors and can be operated to increase or decrease the pressure drop across the face of downcomers
85
and
89
. Downcomer valves
85
and
89
permit a precise control and regulation of the pressure inside the interior cavity
71
of non-recovery coke oven
67
shown in FIG.
3
. This allows for greater control of the inlet of primary combustion air which allows for greater control over the thermal gradients created inside non-recovery coke oven
67
.
First downcomer valve
83
, for example, connects and disconnects the interior cavity
71
of non-recovery coke oven
67
with downcomer
85
. First downcomer valve
83
is built into first side wall
75
. First downcomer valve
83
of
FIGS. 4 and 5
has a housing
91
having a plurality of openings, a first opening
93
communicating with the interior cavity
71
of non-recovery coke oven
67
; a second opening
95
, communicating with the first opening
93
by an intersecting area and communicating with the downcomer
85
; and a third opening
97
for the insertion of a cylindrical plug
99
disposable and rotatable within the housing
91
located in downcomer
85
. First downcomer valve
83
has housing
91
which is a single housing with a plurality of openings. The cylindrical plug
99
has a first, beveled end
101
extending into the intersecting area
103
of first opening
93
and second opening
95
.
First downcomer valve
83
of
FIGS. 4 and 5
is shown with an orifice
105
in cylindrical plug
99
. Housing
91
is in a contacting relationship with first downcomer passage
85
of first side wall
75
. Housing
91
is secured into first downcomer passage
85
so first downcomer valve
83
will have a secure fit in first downcomer passage
85
.
Orifice
105
is for the purpose of letting air into first downcomer passage
85
to burn coal gas in either the interior cavity
71
or sole flues
69
. When cylindrical plug
99
is positioned in the shut or closed position, the position disconnecting the interior cavity
71
from first downcomer passage
85
(
FIG. 6
) air enters into downcomer valve
85
and travels to sole flues
69
. In this embodiment, secondary combustion air is drawn into sole flues
69
through the orifice
105
in cylindrical plug
99
of first downcomer valve
83
. First, downcomer valve
83
with an orifice
105
in the cylindrical plug
99
may also be used in conjunction with secondary air inlets in the plurality of sole flues. It is a design option for flexibility in air flow.
FIG. 6
is a perspective view of downcomer valve
83
of the second embodiment showing cylindrical plug
99
rotated in the closed or shut position, indicated by the diagonal lines at the base of cylindrical plug
99
viewed through first opening
93
. In the closed position, orifice
105
and second opening
95
are blocked by cylindrical plug
99
from communicating with first opening
93
and interior cavity
71
of non-recovery coke oven
67
.
The above description for first downcomer valve
83
is applicable to second downcomer valve
87
. Further first downcomer valve
83
functions in the same was as downcomer valve
39
of
FIG. 2
, except for the operational feature of allowing the inlet of secondary combustion air through orifice
105
. The first downcomer valve
83
of
FIGS. 4 and 5
may also be controlled by a PLC device (not shown).
FIG. 7
illustrates a non-recovery coke oven
107
similar to the non-recovery coke oven
1
of FIG.
1
. The reference numbers of
FIG. 7
that are the same as the reference numbers of
FIG. 1
correspond to like parts. The main difference of non-recovery coke oven
107
is the location and shape of the downcomer valves
109
disposed in downcomers
33
and
35
.
Downcomer valve
109
includes a rectangular plug
111
attached to an extension arm
113
for actuating the rectangular plug
111
. Downcomer valve
109
, located at the bottom of downcomer
33
, is disposed and mounted in sub-structure
27
at the bottom of non-recover coke oven
107
. Downcomer valve
109
extends from an opening
115
in the base of sub-structure
27
into downcomer
33
. A protective housing
117
is constructed around opening
115
where rectangular plug
115
extends through sub-structure
27
.
Downcomer valves
109
, as shown in
FIG. 7
, are variable restrictors between interior cavity
7
and downcomers
33
and
35
and can be operated to obtain a particular pressure with in interior cavity
7
. They can be operated to reduce the negative pressure within interior cavity
7
so that any desired amount of primary air can be drawn in through dampers
37
.
In downcomer
33
in the embodiment of
FIG. 7
, downcomer valve
109
is actuated up and down (in the direction of the arrow below extension arm
113
), either manually or automatically by an actuating means connected to extension arm
113
, to open and close passage
34
between downcomer
33
and sole flue
21
. By connecting and disconnecting downcomer
33
and interior cavity
7
to the sole flues
21
the pressure in interior cavity
7
can be regulated.
In
FIG. 7
, downcomer valve
109
slides up and down in downcomer
33
as opposed to downcomer valve
39
in
FIG. 1
which is rotated in downcomer
33
.
While there has been illustrated and described several embodiments of the present invention, it will be apparent that various changes and modifications thereof will occur to those skilled in the art. It is intended in the appended claims to cover all such changes and modifications that fall within the true spirit and scope of the present invention.
Claims
- 1. A valve disposed in a downcomer connecting an interior cavity of a non-recovery coke oven with sole flues below the interior cavity comprising:a housing with a plurality of openings; at least one first opening in said housing communicating with said interior cavity of a non-recovery coke oven; at least one second opening in said housing communicating with said first opening and said downcomer; at least one third opening in said housing for accepting a valve plug; and said hollow valve plug having a first end and a second end and an orifice extending there between, said hollow valve plug disposed in said at least one third opening and the first end extending into an intersecting area between said at least one first opening and said at least one second opening whereby moving said valve plug increases or decreases an intersecting volume thereby connecting or disconnecting said interior cavity and said downcomer to control and regulate the gas pressure in the interior cavity of said non-recovery coke oven, and whereby secondary combustion air can be drawn through the orifice to the sole flues wherein said valve plug is cylindrical and has the first end which is beveled and said first end is associated with said intersecting area of said at least one first opening and said at least one second opening and said valve plug has the second end for accepting a means for rotating said valve plug, whereby said valve plug can be rotated thereby increasing or decreasing an intersecting volume thus controlling the pressure drop across said downcomer.
- 2. The valve according to claim 1, wherein said first, beveled end of said cylindrical plug is beveled at an angle in a range of 30° to 60°.
- 3. The valve according to claim 1, wherein said first, beveled end of said cylindrical plug is beveled at a 45° angle.
- 4. The valve according to claim 1, wherein said valve plug is controlled by a PLC device.
- 5. The valve according to claim 1, wherein said valve is built into a side wall of said non-recovery coke oven, such that it is part of the brick work.
- 6. The valve according to claim 1, wherein said valve is independent from and disposed in a side wall of said non-recovery coke oven.
- 7. In combination, a valve disposed in a downcomer and a non-recovery coke oven with the downcomer, the combination comprising:a non-recovery coke oven having an interior cavity, sole flues below the interior cavity and the downcomer connecting the interior cavity and the sole flues, the downcomer having the valve disposed therein; a housing for the valve with a plurality of openings; at least one first opening in said housing communicating with said interior cavity of a non-recovery coke oven; at least one second opening in said housing communicating with said first opening and said downcomer; at least one third opening in said housing for accepting a valve plug; and said hollow valve plug having a first end and a second end and an orifice extending there between, said hollow valve plug disposed in said at least one third opening and the first end extending into an intersecting area between said at least one first opening and said at least one second opening whereby moving said valve plug increases or decreases an intersecting volume thereby connecting or disconnecting said interior cavity and said downcomer to control and regulate the gas pressure in the interior cavity of said non-recovery coke oven, and whereby secondary combustion air can be drawn through the orifice to the sole flues wherein said valve plug is cylindrical and has the first end which is beveled and said first end is associated with said intersecting area of said at least one first opening and said at least one second opening and said valve plug has the second end for accepting a means for rotating said valve plug, whereby said valve plug can be rotated thereby increasing or decreasing an intersecting volume thus controlling the pressure drop across said downcomer.
- 8. The combination according to claim 7, wherein said first, beveled end of said cylindrical plug is beveled at an angle in a range of 30° to 60°.
- 9. The combination according to claim 7, wherein said first, beveled end of said cylindrical plug is beveled at a 45° angle.
- 10. The combination according to claim 7, wherein said valve plug is controlled by a PLC device.
- 11. The combination according to claim 7, wherein said valve is built into a side wall of said non-recovery coke oven, such that it is part of the brick work.
- 12. The combination according to claim 7, wherein said valve is independent from and disposed in a side wall of said non-recovery coke oven.
US Referenced Citations (14)