WO1999045083A1 - Method and apparatus for handling and indirectly cooling coke - Google Patents

Method and apparatus for handling and indirectly cooling coke Download PDF

Info

Publication number
WO1999045083A1
WO1999045083A1 PCT/US1999/004623 US9904623W WO9945083A1 WO 1999045083 A1 WO1999045083 A1 WO 1999045083A1 US 9904623 W US9904623 W US 9904623W WO 9945083 A1 WO9945083 A1 WO 9945083A1
Authority
WO
WIPO (PCT)
Prior art keywords
coke
box
oven
carrier
cooling
Prior art date
Application number
PCT/US1999/004623
Other languages
French (fr)
Inventor
Edward S. Kress
Original Assignee
Kress Corporation
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Kress Corporation filed Critical Kress Corporation
Priority to AU29799/99A priority Critical patent/AU2979999A/en
Priority to EP99911066A priority patent/EP1060229A4/en
Publication of WO1999045083A1 publication Critical patent/WO1999045083A1/en

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10BDESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
    • C10B39/00Cooling or quenching coke
    • C10B39/18Coke ramps
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10BDESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
    • C10B39/00Cooling or quenching coke
    • C10B39/02Dry cooling outside the oven
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10BDESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
    • C10B39/00Cooling or quenching coke
    • C10B39/14Cars

Definitions

  • the present invention relates generally to a system for handling coke in an environmentally friendly manner by substantially eliminating pushing and quenching emissions, and more particularly concerns a coke box and carrier which receives the hot coke from the oven, transports it to an indirect cooling station and, when cooled, transports the coke cake to and discharges it at an environmentally sound receiving station in a cost effective manner.
  • the hot coke is pushed out of the oven and dropped into a railcar or other suitable carrier which transports the hot coke to a wet quenching station. It will be understood that dropping the coke, especially when hot, generates large amounts of particulate matter and further burning of the coke takes place until the coke is quenched.
  • Wet quenching uses thousands of gallons of water, a substantial portion of which is turned into steam and immediately released to the atmosphere. The steam picks up many chemicals detrimental to the environment and releases them into the atmosphere.
  • dry quenching An alternative to wet quenching is dry quenching and has recently been adopted and or required in some countries.
  • dry quenching a railcar carries a 2 box which captures the falling coke from the oven.
  • the box containing the hot and still burning coke is then taken to a tall silo, lifted up to the top of the silo and the coke is again dropped, this time into the silo.
  • the coke is then cooled by inert gases passing up through the coke in the silo.
  • the heat from the inert gas in some cases, is recovered and used for other purposes. However, the value of the recovered heat seldom pays for the extremely high capital cost and operating cost of such dry quenching systems.
  • the improved method and apparatus for handling and indirectly cooling coke in accordance with the present invention substantially eliminates all the problems experienced by other systems, simply by not creating them in the first 3 place. Rather, the hot coke is never exposed to the atmosphere, never physically disturbed, and always kept in its original "cake” form as it was in the oven, even after it is dry cooled and then placed, still in its original "cake” form, on the coke wharf. It is anticipated that the coke handling and indirect cooling system of the present invention will have a substantial return on investment, where other systems are very capital intensive, have no payback, have very high operating expenses, and less than desirable reliability. In addition, although revenue with conventional systems will continue to be diminished because of their tendency to reduce yield, the system of the present invention is expected to show very positive economic results.
  • the improved, environmentally sound and cost effective coke handling and indirect cooling system of the present invention uses a coke box having an interior approximately the size and shape of the coke oven.
  • the box which is effectively sealed against the coke oven during the push is preferably covered by flowing water during the push and during the cooling cycle.
  • a carrier moves the box to a cooling rack and places the box into the rack.
  • the carrier then moves to an adjacent cooled box, removes it from the cooling rack, transports the box to an environmentally sound receiving station and discharges the coke from the box into the receiving station .
  • the method and apparatus of the invention are environmentally friendly, improve the quality of the coke, improve the yield of each push, and increase the size of the coke, which is also an advantage.
  • the invention also has the potential to reduce the time the coke needs to spend in the oven thereby increasing the productivity of the coke ovens.
  • the present invention is a vast improvement over existing pushing emission systems which may require large bag houses, large suction fans, large exhaust ducts and special valves for each oven. All these systems are very costly to construct and maintain and generate pollutants in themselves. Furthermore, they are not as effective environmentally as the system of the present invention when pushing is taking place.
  • the preferred system disclosed herein is more reliable.
  • the system of the present invention is not a fixed system. It provides for extra carriers and coke boxes for off-line repair and maintenance which fixed systems do not have, 4 causing them to be inoperative when repair and maintenance is required.
  • the system of the present invention also produces higher yields, because the hot coke is not dropped. Rather, it will be slid, largely intact, onto a receiving surface and thus greatly reduces particulate matter emissions. To further reduce these emissions, a receiving chute can be added. Moreover, coke losses from burning, even when wet quenching is required, will be a small fraction of the losses experienced with conventional pushing emission systems.
  • wet quenching in a traditional quench tower must be accomplished in only one or two minutes because the quench car that contains the hot coke must continue the cycle and quickly return to the coke oven. As a consequence, it is nearly impossible to contain the vast amount of steam and associated pollutants that are generated by the thousands of gallons of water used to quickly quench the hot coke.
  • FIGURE 1 is a schematic perspective view showing the general arrangement of a coke oven battery, cooling rack, and receiving station with which the coke box and carrier of the present invention are associated;
  • FIG. 2 is a small perspective view of the entry end of the coke box carrier shown in FIG. 1 ;
  • FIG. 2a is an enlarged, fragmentary perspective view, of the portion substantially within circle A of Fig. 2, showing the mechanism that drives the coke box into and out of the cooling rack and how the box is moved fore and aft in the carrier of FIGS. 1 and 2; 5
  • FIG. 3 is a small perspective view of the opposite end of the coke box and carrier shown in FIG. 1 ;
  • FIG. 3a is an enlarged, fragmentary perspective view of the portion substantially within circle A of FIG. 3 showing the mechanism used to push the coke from the coke box into the receiving station;
  • FIG. 4 is a schematic perspective view somewhat larger than FIG. 1, showing the carrier at the receiving station with the pushing mechanism in the operative position and the coke being pushed into the receiving box;
  • FIG. 5 is a view similar to FIG. 4 showing the carrier leaving the receiving station with the pushing mechanism rotated to the transport position as well as the receiving box in a tipped position with a coke cake sliding out of the receiving box onto the coke wharf;
  • FIG. 6 is a schematic perspective view of the coke box and carrier with an alternative pushing mechanism supported on its own carrier;
  • FIG. 7 is a side elevation of the coke box, carrier and pushing mechanism of FIG. 6 showing the coke being pushed from the coke box onto a receiving wharf;
  • FIG. 8 is a view similar to FIG. 4 showing a plurality of water jets on the receiving surface of the coke wharf
  • FIG. 9 is a view similar to FIG. 5 showing the addition of a plurality of water spray nozzles directed downwardly onto the coke cake on the receiving surface of the coke wharf;
  • FIG. 10 is a schematic perspective view of the coke box and carrier, somewhat larger than FIG. 4 but from the opposite end, showing the coke being pushed onto an alternative receiving chute disposed below a plurality of water spray nozzles to wet quench the coke, if necessary; and
  • FIG. 1 1 is another schematic perspective of the coke box and carrier, similar to FIG. 6 but from the opposite end, showing the coke being pushed from the opposite end of the coke box into an alternative receiving station located on the opposite side of the carrier rail tracks from the coke ovens.
  • the present invention is comprised of a carrier 100 containing a main frame structure 1 supported on rail wheels 2 rolling on ground rails 3 precisely located in front of a battery of coke ovens 103.
  • the rails 3 are also used in moving and positioning a coke box 8 on the carrier 100 in front of one of the coke ovens 103, a cooling rack 104, and a receiving station 105.
  • the ground rails 3 maintain the proper height and distance of the carrier 100 from the ovens 103.
  • the lateral position of the carrier 100 is controlled by other suitable means for selectively moving the carrier along the rails 3. It will be understood by those skilled in the art that a door machine, schematically illustrated at 18 in FIG.
  • the main frame structure 1 carries a large water tank 5 with a pump and a vertical pipe 6 running to the top of the frame structure 1 above the box 8.
  • the pipe 6 is connected to a horizontal pipe 7 which distributes water over the top of the hot coke box 8, allowing the water to flow down over the box 8, cooling the box and the hot coke inside. The water then drains back into the tank 5 and is recirculated.
  • the coke box 8 has two doors. On the front of the box 8 is a guillotine door 10 and on the back is a swinging door 11. When closed, both doors 10 and 1 1 are tightly sealed to the respective front and rear ends of the box 8.
  • the door 11 on the rear of the box 8, preferably has a one way vent 12 that allows volatile gasses, that can still be given off by the coke for a period of time after the push, to escape and be ignited. It will be understood that the ignited gas is substantially completely burned and is not environmentally detrimental. Furthermore, since no emission can escape during pushing, and some coking can continue to take place in the box, a reduction in the time the coke is in the oven can be utilized to increase the production of the ovens.
  • the guillotine door 10 at the front of the box 8 is opened and closed by actuating arms 38 connected to the main frame 1 and controlled by cylinders 39.
  • the guillotine door 10 preferably contains locating slots 49 and as the box 8 moves into position against the oven door jamb 22, or the receiving box jamb 36, the door actuating arms 38 will index the guillotine door slots 49 with appropriate locating lugs on the respective door jambs.
  • the door 10 can then be opened and 7 closed as required.
  • the actuating arms 38 are rotated back far enough to clear the door machine 18 as the carrier travels on the rails 3 in front of the ovens 103.
  • the coke box 8 preferably has four sets of rail wheels.
  • the outer set 13 and the inner set 14 both allow the box 8 to be freely moved fore and aft on a pair of rails 4 within the carrier frame 1 by an advancing cylinder 15 disposed under the box 8. (See FIG. 2A).
  • the front outer set of wheels 13 on the box 8 are disposed beyond the support of the main frame box rail 4 when a "dragon tongue" 20 made up of items 16, 17, 24, 25, 26, 40 and 41 selectively advances toward any one of the ovens 103, cooling rack 104, or the receiving station 105 shown in FIG. 1, or an alternative receiving chute 58 as shown in FIG. 10.
  • the "dragon tongue” 20 is not designed to carry a vertical load traveling in and out from the envelope of the carrier 100.
  • the inside set of wheels 14 are, therefore, required to support the box 8.
  • the advancing cylinder 15 is preferably connected to an advancing structure 17 which contains a lock cylinder 40 and a box lock 16 that locks onto the box 8.
  • the actuator 15 controls the fore and aft movement of the box 8 relative to the main frame 1 as long as the box lock 16 is in place.
  • the "dragon tongue" 20 is also used to transmit horizontal forces to the advancing cylinder 15, when the box lock 16 is in place. It will be understood that there are three basic box 8 positions when the box lock 16 is in place. First, when the advancing cylinder 15 is fully retracted, the box 8 is drawn into the carrier 100. This position is used when the carrier 100 is moving and allows the box 8 and carrier 100 to pass freely by the door machine 18..
  • the second position places the box 8 and its associated box seal tightly against the oven door jamb 22 in position to receive the coke push from the oven 103. This position is also used when the box 8 is against the receiving station jamb 36.
  • the third position occurs when the advancing cylinder 15 is fully extended. This positions the box 8 at the cooling rack 104 where a lift cylinder 25 is extended against a cooling rack reaction pad 55 thereby forcing a drive roller 24 against the box 8.
  • the lock 16 is then disengaged and a drive motor 26 and the roller 24 drive the box 8 forward into the rack 104.
  • the process is reversed when 8 the cooled box 8 is pulled back into the carrier 100 from the rack 104.
  • two sets of rollers 35 are positioned on the end of the main frame 1 and engage opposite sides of a supporting rail 41 on the "dragon tongue” 20.
  • Support rails 37 are provided at the cooling rack 104.
  • both doors 10 and 1 1 When at the receiving station, both doors 10 and 1 1 will be opened and the cooled coke can be pushed out in either direction by a ram 28.
  • the ram 28 can be either part of the carrier 100 as shown in FIGS. 1, 3-5 and 8-10 or separate from and located at either end of the carrier as shown in FIGS. 6, 7 and 11.
  • the ram 28 is connected to the rear of the carrier 100 and the coke can be conveniently pushed out of the box 8 at any location. It will be understood that if the ram 28 is rigidly fixed to the carrier 100, it will almost double the length of the carrier 100 and the area required for the carrier to operate.
  • the ram drive structure 29 pivots, it will preferably open the sealed door 1 1 on back of the box.
  • the push arms 30, in turn, contact and push two spring loaded arms 31 mounted on the box that carry the rear door 11.
  • the springs 33 which hold the door tightly shut are overcome when the ram drive structure 29 is rotated.
  • the two spring loaded arms 31 hold the door 1 1 on two door center mount bearings 32, one on the top and one on the bottom, which evenly apply force to the door 1 1 and the seal 21 when the door is shut against the rear of the box 8.
  • the door 1 1 can also be opened by independent means, which would be provided when the ram 28 is independently mounted as shown in FIGS. 6. 7 and 11.
  • the front door 10 is opened as described above in connection with taking a push of coke from the oven 103. Then the ram 28, when in the position shown in FIG. 4, can push the hot or cooled coke cake 27 into the receiving box 34. The ram 28 is then retracted and rotated away as shown in FIG. 5 and the springs 33 close the door 1 1.
  • the front door 10 can stay open as 9 the carrier 100 travels to the next oven 103 to receive a fresh charge of hot coke pushed from the oven.
  • the wharf receiving box 34 after receiving the cooled coke, is then rotated and the cool coke 27, still in its "cake” form, slides out onto the coke wharf 43 and will effectively stay in its cake form. There is an additional advantage to this procedure.
  • the cool coke 27 can then be analyzed with appropriate optical or other sensing equipment which will be able to show just how each area of the respective oven 103 and cooling rack 104 is performing.
  • the receiving box 34 can be rotated to the opposite side for additional wharf capacity and the ability to analyze the coke which was in contact with the opposite side of the associated oven 103 and cooling rack 104.
  • the wharf receiving box 34 is mounted in the front by rollers 45 which are supported by a roller frame structure 46.
  • the wharf receiving box 34 can be rotated 120 degrees or more in each direction by two tipping cylinders 44 mounted on the wharf 43, or may be rotated by other power driven rotating means.
  • FIGS. 6 and 7 Such an alternative arrangement is shown in FIGS. 6 and 7 where the pushing ram 28 is mounted on a separate transport mechanism or carrier 107 supported by rail-engaging wheels 110 riding on a pair of rails 106 disposed parallel to the rails 3 which support the coke box carrier 100. Also, there are times that coke must be discharged onto a wharf 109 that will allow the coke to be picked up by a loader and placed into trucks for transport rather than by the belt off of the wharf. This can be done by either a ram 28 mounted on the carrier 100 or separately mounted on a transport mechanism 107 traveling on separate rails 106.
  • FIG. 6 shows the position of the ram 28 prior to pushing the coke from the box and
  • FIG. 7 shows the ram 28 extended substantially into the coke box to push the coke out onto the wharf 109.
  • a plurality of high pressure water jets 50 may be recessed in the surface of the wharf as shown in FIG. 8 so as to spray cooling water up through the coke "cake" 27 as shown in FIG. 9.
  • cake may be sprayed with cooling water from a plurality of spray nozzles 52 supplied by a pipe or manifold 51 mounted above the wharf 43.
  • the present invention accomplishes this type of discharge by means of a transition chute 58 secured to the coke box 8 so as to receive the coke "cake” 57 pushed by the ram 28 and turn the "cake” 57 through approximately 90° so that it exits substantially horizontally from the discharge end 56 of the chute 58.
  • this type of discharge chute 58 may be used to reorient the coke "cake” after it is cooled in the cooling rack 104 or, alternatively, the coke can be wet quenched by suitable spray nozzles 54 mounted on a supply manifold above the coke "cake” 57 on the open slide portion 56 of the discharge chute 58.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Organic Chemistry (AREA)
  • Coke Industry (AREA)

Abstract

An improved, environmentally sound method and cost effective handling and indirect cooling system is provided for coke as it is pushed out of the coke oven (103), indirectly cooled in a coke box (8) and discharged at a receiving station (105). The system uses a coke box (8) having approximately the same internal size and shape of the coke oven (103). The box (8) which is effectively sealed at the coke oven (103) during the push is covered by flowing water during the push and during the cooling cycle. A carrier (100) moves the box (8) to a cooling rack (104) and places the box (8) into the rack. The carrier (100) then moves to an adjacent cooled box (8), removes it from the cooling rack (104), transports the box (8) to an environmentally sound receiving station (105) and discharges the coke from the box (8) in substantially its original 'cake' form into the receiving station. When space is not available near existing ovens for cooling racks (104), the hot coke can be pushed from the box into the receiving station and dumped or the hot coke may be pushed into a receiving chute (58) or directly onto a wharf (109) or pit and wet quenched with water. The method and apparatus of the invention are environmentally friendly, improve the quality of the coke, improve the yield of each push, and increase the size of the coke which is also an advantage. The coke cooling and handling method and apparatus also have the potential to reduce the time the coke needs to spend in the oven thereby increasing the productivity of the ovens. There is also a potential of treating the coke as it is cooled in the box (8) to further improve the quality of the coke.

Description

1
METHOD AND APPARATUS FOR HANDLING AND INDIRECTLY COOLING COKE
FIELD OF THE INVENTION The present invention relates generally to a system for handling coke in an environmentally friendly manner by substantially eliminating pushing and quenching emissions, and more particularly concerns a coke box and carrier which receives the hot coke from the oven, transports it to an indirect cooling station and, when cooled, transports the coke cake to and discharges it at an environmentally sound receiving station in a cost effective manner.
BACKGROUND OF THE INVENTION
In conventional coke ovens, coal is heated to approximately 2000°F. for approximately 20 to 40 hours to drive off all volatile gases and other materials which account for approximately 30% of the weight of the coal. The still hot and burning coke is then pushed out of the oven, cooled by quenching, and placed on a wharf to be carried away by appropriate transport equipment. During both pushing and quenching, uncontrolled emissions are highly noxious and very detrimental to the environment and should be eliminated to the extent possible. It should also be realized that pushing emission control and quenching emission control conventionally are totally separate systems and it is possible to have one without the other. In fact, in North America there are no commercial dry quenching systems with effective environmental controls because of the age of the coke ovens and the tremendous cost of such installations. In Europe, most coke ovens are required to have dry quenching systems and all new ovens that are being considered worldwide must utilize dry quenching of the coke.
In typical coking systems of the type in use in North America as mentioned above, the hot coke is pushed out of the oven and dropped into a railcar or other suitable carrier which transports the hot coke to a wet quenching station. It will be understood that dropping the coke, especially when hot, generates large amounts of particulate matter and further burning of the coke takes place until the coke is quenched. Wet quenching uses thousands of gallons of water, a substantial portion of which is turned into steam and immediately released to the atmosphere. The steam picks up many chemicals detrimental to the environment and releases them into the atmosphere.
An alternative to wet quenching is dry quenching and has recently been adopted and or required in some countries. In dry quenching, a railcar carries a 2 box which captures the falling coke from the oven. The box containing the hot and still burning coke is then taken to a tall silo, lifted up to the top of the silo and the coke is again dropped, this time into the silo. The coke is then cooled by inert gases passing up through the coke in the silo. The heat from the inert gas, in some cases, is recovered and used for other purposes. However, the value of the recovered heat seldom pays for the extremely high capital cost and operating cost of such dry quenching systems.
Another serious disadvantage of such dry quenching systems is the abrasion the coke is subjected to as it works itself down from the top of the silo to the bottom of the silo. This reduces the yield of the usable coke. Coke to be of value to the steelmaking and foundry industries must be in large chunks. Small particles or coke "breeze" which is generated by the physical manipulation and degradation of the coke in the cooling process is of much less value.
In all of the above cases, the cost of containing the pollution generated as the coke falls and is moved from place to place is very high. In the past, many types of pushing emission control systems have been proposed to contain this pollution. However, a substantial number of these systems still have to be replaced because they do not meet the increasingly stringent environmental requirements. Indeed, many systems now in operation do not meet environmental standards, but are allowed to operate because closing them would have a potentially serious negative commercial impact. Moreover, due to the limited technology presently available, environmental standards in place are unnecessarily low, and need to be replaced with more environmentally sound and reliable standards. In addition, virtually all present systems are extremely expensive to install and operate.
It will also be appreciated that commercially operating coke ovens must have backup equipment for transporting the coke from place to place, even when their environmental control systems are inoperative, or being repaired. This is because the ovens themselves must continue to operate even without appropriately functioning environmental controls for handling and cooling the coke. This, of course, also negatively impacts the environment.
SUMMARY AND OBJECTS OF THE INVENTION
The improved method and apparatus for handling and indirectly cooling coke in accordance with the present invention substantially eliminates all the problems experienced by other systems, simply by not creating them in the first 3 place. Rather, the hot coke is never exposed to the atmosphere, never physically disturbed, and always kept in its original "cake" form as it was in the oven, even after it is dry cooled and then placed, still in its original "cake" form, on the coke wharf. It is anticipated that the coke handling and indirect cooling system of the present invention will have a substantial return on investment, where other systems are very capital intensive, have no payback, have very high operating expenses, and less than desirable reliability. In addition, although revenue with conventional systems will continue to be diminished because of their tendency to reduce yield, the system of the present invention is expected to show very positive economic results.
The improved, environmentally sound and cost effective coke handling and indirect cooling system of the present invention uses a coke box having an interior approximately the size and shape of the coke oven. The box which is effectively sealed against the coke oven during the push is preferably covered by flowing water during the push and during the cooling cycle. A carrier moves the box to a cooling rack and places the box into the rack. The carrier then moves to an adjacent cooled box, removes it from the cooling rack, transports the box to an environmentally sound receiving station and discharges the coke from the box into the receiving station . The method and apparatus of the invention are environmentally friendly, improve the quality of the coke, improve the yield of each push, and increase the size of the coke, which is also an advantage. The invention also has the potential to reduce the time the coke needs to spend in the oven thereby increasing the productivity of the coke ovens. In addition, there is also a potential of treating the coke as it is cooled in the box to further improve the quality of the coke.
It should be realized that many existing ovens are in very confined areas and do not have space for a cooling rack of the preferred type and in these instances wet quenching must be used. The present invention is a vast improvement over existing pushing emission systems which may require large bag houses, large suction fans, large exhaust ducts and special valves for each oven. All these systems are very costly to construct and maintain and generate pollutants in themselves. Furthermore, they are not as effective environmentally as the system of the present invention when pushing is taking place. In addition, the preferred system disclosed herein is more reliable. For example, the system of the present invention is not a fixed system. It provides for extra carriers and coke boxes for off-line repair and maintenance which fixed systems do not have, 4 causing them to be inoperative when repair and maintenance is required. The system of the present invention also produces higher yields, because the hot coke is not dropped. Rather, it will be slid, largely intact, onto a receiving surface and thus greatly reduces particulate matter emissions. To further reduce these emissions, a receiving chute can be added. Moreover, coke losses from burning, even when wet quenching is required, will be a small fraction of the losses experienced with conventional pushing emission systems.
Even in those situations where slow dry indirect cooling is not possible, and wet quenching is the only option, it will now be possible to "slow" wet quench the hot coke. By contrast, wet quenching in a traditional quench tower must be accomplished in only one or two minutes because the quench car that contains the hot coke must continue the cycle and quickly return to the coke oven. As a consequence, it is nearly impossible to contain the vast amount of steam and associated pollutants that are generated by the thousands of gallons of water used to quickly quench the hot coke. However, by using the coke box and carrier of the present invention to transport the hot coke to a receiving station with two wharves, one on each side of the receiving box, it is possible to achieve "slow" wet quenching of the hot coke of up to 20 minutes and still accommodate a 10 minute push cycle from the ovens. Thus, providing up to 10 minutes to "slow" wet quench the hot coke should enable containment of a very high percentage of the traditional quenching pollutants even when slow dry indirect cooling with all of the additional benefits of the present invention is not an option.
These and other features and advantages of the invention will be more readily apparent upon reading the following description of a preferred exemplified embodiment of the invention and upon reference to the accompanying drawings.
BRIEF DESCRIPTION OF THE DRAWINGS
FIGURE 1 is a schematic perspective view showing the general arrangement of a coke oven battery, cooling rack, and receiving station with which the coke box and carrier of the present invention are associated;
FIG. 2 is a small perspective view of the entry end of the coke box carrier shown in FIG. 1 ;
FIG. 2a is an enlarged, fragmentary perspective view, of the portion substantially within circle A of Fig. 2, showing the mechanism that drives the coke box into and out of the cooling rack and how the box is moved fore and aft in the carrier of FIGS. 1 and 2; 5
FIG. 3 is a small perspective view of the opposite end of the coke box and carrier shown in FIG. 1 ;
FIG. 3a is an enlarged, fragmentary perspective view of the portion substantially within circle A of FIG. 3 showing the mechanism used to push the coke from the coke box into the receiving station;
FIG. 4 is a schematic perspective view somewhat larger than FIG. 1, showing the carrier at the receiving station with the pushing mechanism in the operative position and the coke being pushed into the receiving box;
FIG. 5 is a view similar to FIG. 4 showing the carrier leaving the receiving station with the pushing mechanism rotated to the transport position as well as the receiving box in a tipped position with a coke cake sliding out of the receiving box onto the coke wharf;
FIG. 6 is a schematic perspective view of the coke box and carrier with an alternative pushing mechanism supported on its own carrier; FIG. 7 is a side elevation of the coke box, carrier and pushing mechanism of FIG. 6 showing the coke being pushed from the coke box onto a receiving wharf;
FIG. 8 is a view similar to FIG. 4 showing a plurality of water jets on the receiving surface of the coke wharf; FIG. 9 is a view similar to FIG. 5 showing the addition of a plurality of water spray nozzles directed downwardly onto the coke cake on the receiving surface of the coke wharf;
FIG. 10 is a schematic perspective view of the coke box and carrier, somewhat larger than FIG. 4 but from the opposite end, showing the coke being pushed onto an alternative receiving chute disposed below a plurality of water spray nozzles to wet quench the coke, if necessary; and
FIG. 1 1 is another schematic perspective of the coke box and carrier, similar to FIG. 6 but from the opposite end, showing the coke being pushed from the opposite end of the coke box into an alternative receiving station located on the opposite side of the carrier rail tracks from the coke ovens.
While the invention will be described and disclosed in connection with certain preferred embodiments and procedures, it is not intended to limit the invention to those specific embodiments. Rather it is intended to cover all such alternative embodiments and modifications as fall within the spirit and scope of the invention as disclosed herein. 6
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENT
Turning now more specifically to the accompanying drawings, the present invention is comprised of a carrier 100 containing a main frame structure 1 supported on rail wheels 2 rolling on ground rails 3 precisely located in front of a battery of coke ovens 103. The rails 3 are also used in moving and positioning a coke box 8 on the carrier 100 in front of one of the coke ovens 103, a cooling rack 104, and a receiving station 105. The ground rails 3 maintain the proper height and distance of the carrier 100 from the ovens 103. The lateral position of the carrier 100 is controlled by other suitable means for selectively moving the carrier along the rails 3. It will be understood by those skilled in the art that a door machine, schematically illustrated at 18 in FIG. 1 , is used to remove the door from the coke oven 103 before the coke is pushed from the oven into the box 8 and to replace the door after the push. The present invention can work with or without the door machine 18 as an integral part of the carrier 100. As best seen in FIGS. 4 and 5, the main frame structure 1 carries a large water tank 5 with a pump and a vertical pipe 6 running to the top of the frame structure 1 above the box 8. The pipe 6 is connected to a horizontal pipe 7 which distributes water over the top of the hot coke box 8, allowing the water to flow down over the box 8, cooling the box and the hot coke inside. The water then drains back into the tank 5 and is recirculated.
The coke box 8 has two doors. On the front of the box 8 is a guillotine door 10 and on the back is a swinging door 11. When closed, both doors 10 and 1 1 are tightly sealed to the respective front and rear ends of the box 8. The door 11 on the rear of the box 8, preferably has a one way vent 12 that allows volatile gasses, that can still be given off by the coke for a period of time after the push, to escape and be ignited. It will be understood that the ignited gas is substantially completely burned and is not environmentally detrimental. Furthermore, since no emission can escape during pushing, and some coking can continue to take place in the box, a reduction in the time the coke is in the oven can be utilized to increase the production of the ovens.
The guillotine door 10 at the front of the box 8 is opened and closed by actuating arms 38 connected to the main frame 1 and controlled by cylinders 39. The guillotine door 10 preferably contains locating slots 49 and as the box 8 moves into position against the oven door jamb 22, or the receiving box jamb 36, the door actuating arms 38 will index the guillotine door slots 49 with appropriate locating lugs on the respective door jambs. The door 10 can then be opened and 7 closed as required. When the coke box 8 is retracted back into the main frame 1 , the actuating arms 38 are rotated back far enough to clear the door machine 18 as the carrier travels on the rails 3 in front of the ovens 103.
As shown in FIG. 3 A, the coke box 8 preferably has four sets of rail wheels. The outer set 13 and the inner set 14 both allow the box 8 to be freely moved fore and aft on a pair of rails 4 within the carrier frame 1 by an advancing cylinder 15 disposed under the box 8. (See FIG. 2A). As mentioned above, it is desirable for the carrier 100 to be able to pass the door machine 18, located on a bench 19 in front of the ovens 103. Therefore, the box 8 must be pulled back at least six feet from the face of the ovens 103.
The front outer set of wheels 13 on the box 8 are disposed beyond the support of the main frame box rail 4 when a "dragon tongue" 20 made up of items 16, 17, 24, 25, 26, 40 and 41 selectively advances toward any one of the ovens 103, cooling rack 104, or the receiving station 105 shown in FIG. 1, or an alternative receiving chute 58 as shown in FIG. 10. The "dragon tongue" 20, however, is not designed to carry a vertical load traveling in and out from the envelope of the carrier 100. The inside set of wheels 14 are, therefore, required to support the box 8.
The advancing cylinder 15 is preferably connected to an advancing structure 17 which contains a lock cylinder 40 and a box lock 16 that locks onto the box 8. The actuator 15 controls the fore and aft movement of the box 8 relative to the main frame 1 as long as the box lock 16 is in place. During receiving and discharging coke, the "dragon tongue" 20 is also used to transmit horizontal forces to the advancing cylinder 15, when the box lock 16 is in place. It will be understood that there are three basic box 8 positions when the box lock 16 is in place. First, when the advancing cylinder 15 is fully retracted, the box 8 is drawn into the carrier 100. This position is used when the carrier 100 is moving and allows the box 8 and carrier 100 to pass freely by the door machine 18.. The second position places the box 8 and its associated box seal tightly against the oven door jamb 22 in position to receive the coke push from the oven 103. This position is also used when the box 8 is against the receiving station jamb 36. The third position occurs when the advancing cylinder 15 is fully extended. This positions the box 8 at the cooling rack 104 where a lift cylinder 25 is extended against a cooling rack reaction pad 55 thereby forcing a drive roller 24 against the box 8. The lock 16 is then disengaged and a drive motor 26 and the roller 24 drive the box 8 forward into the rack 104. The process is reversed when 8 the cooled box 8 is pulled back into the carrier 100 from the rack 104. To support the "dragon tongue" 20, which is not intended to support the weight of the box 8, two sets of rollers 35 are positioned on the end of the main frame 1 and engage opposite sides of a supporting rail 41 on the "dragon tongue" 20. Support rails 37 are provided at the cooling rack 104.
When at the receiving station, both doors 10 and 1 1 will be opened and the cooled coke can be pushed out in either direction by a ram 28. The ram 28 can be either part of the carrier 100 as shown in FIGS. 1, 3-5 and 8-10 or separate from and located at either end of the carrier as shown in FIGS. 6, 7 and 11. In the preferred embodiment, the ram 28 is connected to the rear of the carrier 100 and the coke can be conveniently pushed out of the box 8 at any location. It will be understood that if the ram 28 is rigidly fixed to the carrier 100, it will almost double the length of the carrier 100 and the area required for the carrier to operate. Pursuant to the present invention, by pivoting the ram 28 and ram drive structure 29, which includes ram support rollers 48, a ram drive motor 51, rack gear 52, pinion gear 53, and 90 degree drive for pinion gear 54, by 90 degrees or more relative to the mainframe 1 of the carrier 100, with a ram drive structure rotating cylinder 42, this extra working space can be eliminated.
In further accordance with the invention, as the ram drive structure 29 pivots, it will preferably open the sealed door 1 1 on back of the box. This is accomplished by two push arms 30 pivotally mounted on the ram drive structure 29. The push arms 30, in turn, contact and push two spring loaded arms 31 mounted on the box that carry the rear door 11. The springs 33, which hold the door tightly shut are overcome when the ram drive structure 29 is rotated. The two spring loaded arms 31 hold the door 1 1 on two door center mount bearings 32, one on the top and one on the bottom, which evenly apply force to the door 1 1 and the seal 21 when the door is shut against the rear of the box 8. It will be understood, of course, that alternatively, the door 1 1 can also be opened by independent means, which would be provided when the ram 28 is independently mounted as shown in FIGS. 6. 7 and 11.
At the receiving station 105, the front door 10 is opened as described above in connection with taking a push of coke from the oven 103. Then the ram 28, when in the position shown in FIG. 4, can push the hot or cooled coke cake 27 into the receiving box 34. The ram 28 is then retracted and rotated away as shown in FIG. 5 and the springs 33 close the door 1 1. The front door 10 can stay open as 9 the carrier 100 travels to the next oven 103 to receive a fresh charge of hot coke pushed from the oven.
The wharf receiving box 34, after receiving the cooled coke, is then rotated and the cool coke 27, still in its "cake" form, slides out onto the coke wharf 43 and will effectively stay in its cake form. There is an additional advantage to this procedure. The cool coke 27 can then be analyzed with appropriate optical or other sensing equipment which will be able to show just how each area of the respective oven 103 and cooling rack 104 is performing. On the next push, the receiving box 34 can be rotated to the opposite side for additional wharf capacity and the ability to analyze the coke which was in contact with the opposite side of the associated oven 103 and cooling rack 104. In the illustrated embodiment, the wharf receiving box 34 is mounted in the front by rollers 45 which are supported by a roller frame structure 46. On the back, it is supported by a center-mounted bearing 47 which takes both vertical and horizontal forces. Preferably, the wharf receiving box 34 can be rotated 120 degrees or more in each direction by two tipping cylinders 44 mounted on the wharf 43, or may be rotated by other power driven rotating means.
It is also the intent of this invention to provide for a pushing ram 28 mounted separately from the coke box carrier 100 in case there are special circumstances that would benefit from this arrangement. Such an alternative arrangement is shown in FIGS. 6 and 7 where the pushing ram 28 is mounted on a separate transport mechanism or carrier 107 supported by rail-engaging wheels 110 riding on a pair of rails 106 disposed parallel to the rails 3 which support the coke box carrier 100. Also, there are times that coke must be discharged onto a wharf 109 that will allow the coke to be picked up by a loader and placed into trucks for transport rather than by the belt off of the wharf. This can be done by either a ram 28 mounted on the carrier 100 or separately mounted on a transport mechanism 107 traveling on separate rails 106. FIG. 6 shows the position of the ram 28 prior to pushing the coke from the box and FIG. 7 shows the ram 28 extended substantially into the coke box to push the coke out onto the wharf 109. In certain instances it may also be necessary or desirable to supplement or even replace the indirect cooling of the coke in the cooling rack 104 with wet quenching of the coke on the surface of the coke wharf 43. For this purpose, a plurality of high pressure water jets 50 may be recessed in the surface of the wharf as shown in FIG. 8 so as to spray cooling water up through the coke "cake" 27 as shown in FIG. 9. Additionally, as also shown here, the upper surface of the coke 10
"cake" may be sprayed with cooling water from a plurality of spray nozzles 52 supplied by a pipe or manifold 51 mounted above the wharf 43.
Due to the physical layout and other space limitations of the coking facility, it may be desirable to discharge the coke 'cake" 57 from the coke box 8 and turn the coke "cake" 57 from its substantially vertical position to a generally horizontal orientation. As shown in FIG. 10, the present invention accomplishes this type of discharge by means of a transition chute 58 secured to the coke box 8 so as to receive the coke "cake" 57 pushed by the ram 28 and turn the "cake" 57 through approximately 90° so that it exits substantially horizontally from the discharge end 56 of the chute 58. It will be understood that this type of discharge chute 58 may be used to reorient the coke "cake" after it is cooled in the cooling rack 104 or, alternatively, the coke can be wet quenched by suitable spray nozzles 54 mounted on a supply manifold above the coke "cake" 57 on the open slide portion 56 of the discharge chute 58. From the foregoing, it will be seen that a novel method and apparatus for handling and indirectly cooling coke has been provided which attains the aforementioned objects. When necessary due to space considerations, wet quenching may be used to supplement or replace the indirect cooling racks. Various other modifications of the embodiments in addition to those specifically illustrated and described herein will be apparent to those skilled in the art, particularly in light of the teachings of this invention. The present invention should not be construed as limited to the specific embodiments shown and described herein, but instead is intended to encompass such alternatives, as well.

Claims

1 1 I claim as my invention:
1. A method for receiving a charge of hot coke pushed from a horizontal discharge coke oven containing other emissions, cooling the coke and placing the cooled coke on a receiving surface, comprising:
(a) aligning the open end of a coke box substantially completely closed on five sides at the time of the push and open on one end and having a cross section, volume and surface area substantially equal to that of the charge of coke;
(b) creating an effective seal between the coke oven face and the coke box to minimize the escape of coke, particulate matter and gas during the coke oven discharging operation;
(c) pushing the charge of coke horizontally from within the coke oven directly into the coke box through the open end while maintaining the coke in a form with substantially the same cross section and surface area as it had within the coke oven;
(d) enclosing the coke within the coke box while the coke box is in position at the discharge end of the coke oven by closing the open end of the box to substantially isolate the coke and trapped gases from atmospheric oxygen and external cooling media; (e) indirectly cooling the coke within the coke box to below its kindling temperature by passing an external cooling media over the exterior surfaces of the coke box;
(f) moving the coke box and cooled coke to a coke discharging area;
(g) opening the coke box; and pushing the coke out of the box.
2. The method of claim 1 wherein the coke is pushed from the coke box into a receiving box, similar in size to the coke box while substantially maintaining the coke in its original coke "cake" shape, rotating the receiving box in either direction to an angle sufficient for the coke still in its original "cake" form to slip out from the open top of the receiving box onto a receiving surface.
3. The method of claim 1 wherein a ram is provided for pushing the coke out of the coke box and rotating the ram to a position so it will take no additional space as the coke box travels laterally in front of the coke ovens, a cooling rack and a receiving and discharge station. 12
4. The method of claim 3 wherein rotating the ram to an in-line position to push the coke from the box will open the rear door of the coke box by overcoming the spring force holding the door shut.
5. The method of claim 1 including positioning the box, when traveling, back far enough from the oven door jamb to clear all objects in front of the oven and, when positioned in front of the oven, advancing the box up to the face of the oven to effectively seal the box against the oven.
6. The method of claim 3 wherein the ram is rotated horizontally to one side, the ram being permanently fixed to a carrier on which the coke box is mounted.
7. The method of claim 1 including the step of opening the rear door and front door of the coke box and pushing the coke onto the ground or into a pit with a ram longitudinally aligned with the coke box.
8. The method of claim 1 wherein the coke box is supported on multiple sets of wheels or a low friction surface on a carrier and moving the coke box beyond the envelope of the carrier and back onto the carrier with provision for disengaging the box from the carrier and leaving the box in a cooling rack.
9. The method of claim 8 including a linear actuator which moves an extendable structure, supported by rollers, beyond the envelope of the carrier, the extendable structure including a lock that secures the structure to the box and including a drive roller on the outer end of the structure for moving the coke box out of and back onto the carrier when the lock is disengaged.
10. The method of claim 9 arranged so that when the linear actuator is extended, a vertical cylinder extends contacting the surface of the cooling rack lifting the extendable structure which forces the drive roller against the box and disengaging the lock so that as the drive roller turns in one direction, the box is moved out of the carrier and into a cooling rack.
1 1. The method of claim 10 wherein the procedure is reversed to move the box out of the cooling rack and back onto the carrier. 13
12. A method for receiving a charge of hot coke pushed from a horizontal discharge coke oven containing other emissions, and placing the hot coke on a receiving surface, comprising: (a) aligning the open end of a coke box substantially completely closed on five sides at the time of the push and open on one end and having a cross section, volume and surface area substantially equal to that of the charge of coke;
(b) creating an effective seal between the coke oven face and the coke box to minimize the escape of coke, particulate matter, and gas during the coke discharging operation;
(c) pushing the charge of coke horizontally from within the coke oven directly into the coke box through the open end while maintaining the coke in a form with substantially the same cross section and surface area as it had within the coke oven; (d) enclosing the coke within the coke box while the coke box is in position at the discharge end of the coke oven by closing the open end of the box to substantially isolate the coke and trapped gases from atmospheric oxygen;
(e) moving the coke box and hot coke to a coke discharging area;
(f) opening the coke box; and pushing the coke out of the box.
13. The method of claim 12 wherein the coke is pushed from the coke box into a receiving box, similar in size to the coke box while substantially maintaining the coke in its original coke "cake" shape, rotating the receiving box in either direction to an angle sufficient for the coke still in its original "cake" form to slip out from the open top of the receiving box onto a receiving surface where it can be wet quenched.
14. The method of claim 13 including the step of forcing water up from the receiving surface through the coke which is generally in the original "cake" form to cool the hot coke to below its kindling temperature.
15. The method of claim 13 including the step of supplying water to the upper surface of the hot coke.
16. The method of claim 14 including the step of supplying water to the upper surface of the hot coke. 14
17. The method of claim 12 including the step of directing quench water onto the hot coke for a period of about 10 minutes to about 20 minutes to reduce the temperature of the hot coke to below its kindling temperature and thereby slowly wet quench the hot coke.
18. The method of claim 12 including the step of pushing the coke "cake" from the coke box and through a transition chute to reorient the coke "cake" from a substantially vertical position to a generally horizontal position.
19. The method of claim 18 including the step of indirectly cooling the coke in the coke box by directing cooling water over the outer surface of the coke box before the coke is pushed from the coke box.
20. The method of claim 18 including the step of directing quench water onto the coke "cake" after it is pushed from the coke box.
PCT/US1999/004623 1998-03-04 1999-03-03 Method and apparatus for handling and indirectly cooling coke WO1999045083A1 (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
AU29799/99A AU2979999A (en) 1998-03-04 1999-03-03 Method and apparatus for handling and indirectly cooling coke
EP99911066A EP1060229A4 (en) 1998-03-04 1999-03-03 Method and apparatus for handling and indirectly cooling coke

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US7672198P 1998-03-04 1998-03-04
US60/076,721 1998-03-04

Publications (1)

Publication Number Publication Date
WO1999045083A1 true WO1999045083A1 (en) 1999-09-10

Family

ID=22133798

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/US1999/004623 WO1999045083A1 (en) 1998-03-04 1999-03-03 Method and apparatus for handling and indirectly cooling coke

Country Status (4)

Country Link
EP (1) EP1060229A4 (en)
CN (1) CN1298437A (en)
AU (1) AU2979999A (en)
WO (1) WO1999045083A1 (en)

Cited By (43)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1994121A2 (en) * 2006-03-03 2008-11-26 Suncoke Energy, Inc. Improved method and apparatus for producing coke
WO2011063898A1 (en) * 2009-11-25 2011-06-03 Uhde Gmbh Device and method for emptying quenched or unquenched coke from a coke quenching car into a receiving device
CN104449771A (en) * 2014-03-10 2015-03-25 晏子俊 Charcoal production system with continuous externally-heating dry distillation mechanism
US9169439B2 (en) 2012-08-29 2015-10-27 Suncoke Technology And Development Llc Method and apparatus for testing coal coking properties
US9193915B2 (en) 2013-03-14 2015-11-24 Suncoke Technology And Development Llc. Horizontal heat recovery coke ovens having monolith crowns
US9193913B2 (en) 2012-09-21 2015-11-24 Suncoke Technology And Development Llc Reduced output rate coke oven operation with gas sharing providing extended process cycle
US9200225B2 (en) 2010-08-03 2015-12-01 Suncoke Technology And Development Llc. Method and apparatus for compacting coal for a coal coking process
US9238778B2 (en) 2012-12-28 2016-01-19 Suncoke Technology And Development Llc. Systems and methods for improving quenched coke recovery
US9243186B2 (en) 2012-08-17 2016-01-26 Suncoke Technology And Development Llc. Coke plant including exhaust gas sharing
US9249357B2 (en) 2012-08-17 2016-02-02 Suncoke Technology And Development Llc. Method and apparatus for volatile matter sharing in stamp-charged coke ovens
US9273249B2 (en) 2012-12-28 2016-03-01 Suncoke Technology And Development Llc. Systems and methods for controlling air distribution in a coke oven
US9273250B2 (en) 2013-03-15 2016-03-01 Suncoke Technology And Development Llc. Methods and systems for improved quench tower design
US9321965B2 (en) 2009-03-17 2016-04-26 Suncoke Technology And Development Llc. Flat push coke wet quenching apparatus and process
US9359554B2 (en) 2012-08-17 2016-06-07 Suncoke Technology And Development Llc Automatic draft control system for coke plants
US9476547B2 (en) 2012-12-28 2016-10-25 Suncoke Technology And Development Llc Exhaust flow modifier, duct intersection incorporating the same, and methods therefor
US9580656B2 (en) 2014-08-28 2017-02-28 Suncoke Technology And Development Llc Coke oven charging system
US9683740B2 (en) 2012-07-31 2017-06-20 Suncoke Technology And Development Llc Methods for handling coal processing emissions and associated systems and devices
US10016714B2 (en) 2012-12-28 2018-07-10 Suncoke Technology And Development Llc Systems and methods for removing mercury from emissions
US10047295B2 (en) 2012-12-28 2018-08-14 Suncoke Technology And Development Llc Non-perpendicular connections between coke oven uptakes and a hot common tunnel, and associated systems and methods
US10526542B2 (en) 2015-12-28 2020-01-07 Suncoke Technology And Development Llc Method and system for dynamically charging a coke oven
US10526541B2 (en) 2014-06-30 2020-01-07 Suncoke Technology And Development Llc Horizontal heat recovery coke ovens having monolith crowns
US10619101B2 (en) 2013-12-31 2020-04-14 Suncoke Technology And Development Llc Methods for decarbonizing coking ovens, and associated systems and devices
US10760002B2 (en) 2012-12-28 2020-09-01 Suncoke Technology And Development Llc Systems and methods for maintaining a hot car in a coke plant
US10851306B2 (en) 2017-05-23 2020-12-01 Suncoke Technology And Development Llc System and method for repairing a coke oven
US10883051B2 (en) 2012-12-28 2021-01-05 Suncoke Technology And Development Llc Methods and systems for improved coke quenching
US10968395B2 (en) 2014-12-31 2021-04-06 Suncoke Technology And Development Llc Multi-modal beds of coking material
US10968393B2 (en) 2014-09-15 2021-04-06 Suncoke Technology And Development Llc Coke ovens having monolith component construction
US11008518B2 (en) 2018-12-28 2021-05-18 Suncoke Technology And Development Llc Coke plant tunnel repair and flexible joints
US11021655B2 (en) 2018-12-28 2021-06-01 Suncoke Technology And Development Llc Decarbonization of coke ovens and associated systems and methods
US11060032B2 (en) 2015-01-02 2021-07-13 Suncoke Technology And Development Llc Integrated coke plant automation and optimization using advanced control and optimization techniques
US11071935B2 (en) 2018-12-28 2021-07-27 Suncoke Technology And Development Llc Particulate detection for industrial facilities, and associated systems and methods
US11098252B2 (en) 2018-12-28 2021-08-24 Suncoke Technology And Development Llc Spring-loaded heat recovery oven system and method
US11142699B2 (en) 2012-12-28 2021-10-12 Suncoke Technology And Development Llc Vent stack lids and associated systems and methods
US11261381B2 (en) 2018-12-28 2022-03-01 Suncoke Technology And Development Llc Heat recovery oven foundation
US11395989B2 (en) 2018-12-31 2022-07-26 Suncoke Technology And Development Llc Methods and systems for providing corrosion resistant surfaces in contaminant treatment systems
US11486572B2 (en) 2018-12-31 2022-11-01 Suncoke Technology And Development Llc Systems and methods for Utilizing flue gas
US11508230B2 (en) 2016-06-03 2022-11-22 Suncoke Technology And Development Llc Methods and systems for automatically generating a remedial action in an industrial facility
US11760937B2 (en) 2018-12-28 2023-09-19 Suncoke Technology And Development Llc Oven uptakes
US11767482B2 (en) 2020-05-03 2023-09-26 Suncoke Technology And Development Llc High-quality coke products
US11788012B2 (en) 2015-01-02 2023-10-17 Suncoke Technology And Development Llc Integrated coke plant automation and optimization using advanced control and optimization techniques
US11851724B2 (en) 2021-11-04 2023-12-26 Suncoke Technology And Development Llc. Foundry coke products, and associated systems, devices, and methods
US11946108B2 (en) 2021-11-04 2024-04-02 Suncoke Technology And Development Llc Foundry coke products and associated processing methods via cupolas
US12110458B2 (en) 2022-11-04 2024-10-08 Suncoke Technology And Development Llc Coal blends, foundry coke products, and associated systems, devices, and methods

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103857769A (en) * 2011-08-16 2014-06-11 北京华泰焦化工程技术有限公司 Dry coke-quenching device for heat-recovery-type coke oven
CN110791299B (en) * 2019-12-05 2024-07-23 大连重矿设备制造有限公司 Dry quenching rotary coke tank adjusting and positioning device

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4886580A (en) * 1987-04-22 1989-12-12 Kress Corporation Dry quenching coke box
US4997527A (en) * 1988-04-22 1991-03-05 Kress Corporation Coke handling and dry quenching method
US5190617A (en) * 1987-04-22 1993-03-02 Kress Corporation Coke handling apparatus including coke box and carrier vehicle
US5192398A (en) * 1987-04-22 1993-03-09 Kress Corporation Coke box with indirectly cooled receiving chamber and exhaust gas burner

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US755154A (en) * 1902-09-18 1904-03-22 Edwin A Moore Coke quenching and bleaching apparatus.
US4285772A (en) * 1979-02-06 1981-08-25 Kress Edward S Method and apparatus for handlng and dry quenching coke

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4886580A (en) * 1987-04-22 1989-12-12 Kress Corporation Dry quenching coke box
US5190617A (en) * 1987-04-22 1993-03-02 Kress Corporation Coke handling apparatus including coke box and carrier vehicle
US5192398A (en) * 1987-04-22 1993-03-09 Kress Corporation Coke box with indirectly cooled receiving chamber and exhaust gas burner
US4997527A (en) * 1988-04-22 1991-03-05 Kress Corporation Coke handling and dry quenching method

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
See also references of EP1060229A4 *

Cited By (83)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1994121A2 (en) * 2006-03-03 2008-11-26 Suncoke Energy, Inc. Improved method and apparatus for producing coke
EP1994121A4 (en) * 2006-03-03 2014-04-16 Suncoke Technology & Dev Llc Improved method and apparatus for producing coke
US9321965B2 (en) 2009-03-17 2016-04-26 Suncoke Technology And Development Llc. Flat push coke wet quenching apparatus and process
WO2011063898A1 (en) * 2009-11-25 2011-06-03 Uhde Gmbh Device and method for emptying quenched or unquenched coke from a coke quenching car into a receiving device
US9303210B2 (en) 2009-11-25 2016-04-05 Thyssenkrupp Uhde Gmbh Apparatus and process for the discharge of quenched or unquenched coke from a coke quenching car into a receiving device
RU2577367C2 (en) * 2009-11-25 2016-03-20 ТюссенКрупп Уде ГмбХ Method and device for discharge of quenched or unquenched coke from coke-quenching car onto receiving facility
US9200225B2 (en) 2010-08-03 2015-12-01 Suncoke Technology And Development Llc. Method and apparatus for compacting coal for a coal coking process
US9683740B2 (en) 2012-07-31 2017-06-20 Suncoke Technology And Development Llc Methods for handling coal processing emissions and associated systems and devices
US9359554B2 (en) 2012-08-17 2016-06-07 Suncoke Technology And Development Llc Automatic draft control system for coke plants
US9243186B2 (en) 2012-08-17 2016-01-26 Suncoke Technology And Development Llc. Coke plant including exhaust gas sharing
US9249357B2 (en) 2012-08-17 2016-02-02 Suncoke Technology And Development Llc. Method and apparatus for volatile matter sharing in stamp-charged coke ovens
US10611965B2 (en) 2012-08-17 2020-04-07 Suncoke Technology And Development Llc Coke plant including exhaust gas sharing
US10041002B2 (en) 2012-08-17 2018-08-07 Suncoke Technology And Development Llc Coke plant including exhaust gas sharing
US11692138B2 (en) 2012-08-17 2023-07-04 Suncoke Technology And Development Llc Automatic draft control system for coke plants
US11441077B2 (en) 2012-08-17 2022-09-13 Suncoke Technology And Development Llc Coke plant including exhaust gas sharing
US9169439B2 (en) 2012-08-29 2015-10-27 Suncoke Technology And Development Llc Method and apparatus for testing coal coking properties
US10053627B2 (en) 2012-08-29 2018-08-21 Suncoke Technology And Development Llc Method and apparatus for testing coal coking properties
US9193913B2 (en) 2012-09-21 2015-11-24 Suncoke Technology And Development Llc Reduced output rate coke oven operation with gas sharing providing extended process cycle
US10016714B2 (en) 2012-12-28 2018-07-10 Suncoke Technology And Development Llc Systems and methods for removing mercury from emissions
US9273249B2 (en) 2012-12-28 2016-03-01 Suncoke Technology And Development Llc. Systems and methods for controlling air distribution in a coke oven
US9476547B2 (en) 2012-12-28 2016-10-25 Suncoke Technology And Development Llc Exhaust flow modifier, duct intersection incorporating the same, and methods therefor
US11142699B2 (en) 2012-12-28 2021-10-12 Suncoke Technology And Development Llc Vent stack lids and associated systems and methods
US9862888B2 (en) 2012-12-28 2018-01-09 Suncoke Technology And Development Llc Systems and methods for improving quenched coke recovery
US11359145B2 (en) 2012-12-28 2022-06-14 Suncoke Technology And Development Llc Systems and methods for maintaining a hot car in a coke plant
US11117087B2 (en) 2012-12-28 2021-09-14 Suncoke Technology And Development Llc Systems and methods for removing mercury from emissions
US11008517B2 (en) 2012-12-28 2021-05-18 Suncoke Technology And Development Llc Non-perpendicular connections between coke oven uptakes and a hot common tunnel, and associated systems and methods
US10047295B2 (en) 2012-12-28 2018-08-14 Suncoke Technology And Development Llc Non-perpendicular connections between coke oven uptakes and a hot common tunnel, and associated systems and methods
US10975309B2 (en) 2012-12-28 2021-04-13 Suncoke Technology And Development Llc Exhaust flow modifier, duct intersection incorporating the same, and methods therefor
US9238778B2 (en) 2012-12-28 2016-01-19 Suncoke Technology And Development Llc. Systems and methods for improving quenched coke recovery
US10883051B2 (en) 2012-12-28 2021-01-05 Suncoke Technology And Development Llc Methods and systems for improved coke quenching
US10323192B2 (en) 2012-12-28 2019-06-18 Suncoke Technology And Development Llc Systems and methods for improving quenched coke recovery
US11939526B2 (en) 2012-12-28 2024-03-26 Suncoke Technology And Development Llc Vent stack lids and associated systems and methods
US11845037B2 (en) 2012-12-28 2023-12-19 Suncoke Technology And Development Llc Systems and methods for removing mercury from emissions
US10760002B2 (en) 2012-12-28 2020-09-01 Suncoke Technology And Development Llc Systems and methods for maintaining a hot car in a coke plant
US9193915B2 (en) 2013-03-14 2015-11-24 Suncoke Technology And Development Llc. Horizontal heat recovery coke ovens having monolith crowns
US9273250B2 (en) 2013-03-15 2016-03-01 Suncoke Technology And Development Llc. Methods and systems for improved quench tower design
US10927303B2 (en) 2013-03-15 2021-02-23 Suncoke Technology And Development Llc Methods for improved quench tower design
US11746296B2 (en) 2013-03-15 2023-09-05 Suncoke Technology And Development Llc Methods and systems for improved quench tower design
US11359146B2 (en) 2013-12-31 2022-06-14 Suncoke Technology And Development Llc Methods for decarbonizing coking ovens, and associated systems and devices
US10619101B2 (en) 2013-12-31 2020-04-14 Suncoke Technology And Development Llc Methods for decarbonizing coking ovens, and associated systems and devices
CN104449771B (en) * 2014-03-10 2016-06-01 晏子俊 Retorting machine charcoal production system is heated outside a kind of continous way
CN104449771A (en) * 2014-03-10 2015-03-25 晏子俊 Charcoal production system with continuous externally-heating dry distillation mechanism
US10526541B2 (en) 2014-06-30 2020-01-07 Suncoke Technology And Development Llc Horizontal heat recovery coke ovens having monolith crowns
US10920148B2 (en) 2014-08-28 2021-02-16 Suncoke Technology And Development Llc Burn profiles for coke operations
US10233392B2 (en) 2014-08-28 2019-03-19 Suncoke Technology And Development Llc Method for optimizing coke plant operation and output
US10308876B2 (en) 2014-08-28 2019-06-04 Suncoke Technology And Development Llc Burn profiles for coke operations
US9976089B2 (en) 2014-08-28 2018-05-22 Suncoke Technology And Development Llc Coke oven charging system
US9580656B2 (en) 2014-08-28 2017-02-28 Suncoke Technology And Development Llc Coke oven charging system
US11053444B2 (en) 2014-08-28 2021-07-06 Suncoke Technology And Development Llc Method and system for optimizing coke plant operation and output
US9708542B2 (en) 2014-08-28 2017-07-18 Suncoke Technology And Development Llc Method and system for optimizing coke plant operation and output
US10968393B2 (en) 2014-09-15 2021-04-06 Suncoke Technology And Development Llc Coke ovens having monolith component construction
US11795400B2 (en) 2014-09-15 2023-10-24 Suncoke Technology And Development Llc Coke ovens having monolith component construction
US10968395B2 (en) 2014-12-31 2021-04-06 Suncoke Technology And Development Llc Multi-modal beds of coking material
US10975311B2 (en) 2014-12-31 2021-04-13 Suncoke Technology And Development Llc Multi-modal beds of coking material
US10975310B2 (en) 2014-12-31 2021-04-13 Suncoke Technology And Development Llc Multi-modal beds of coking material
US11060032B2 (en) 2015-01-02 2021-07-13 Suncoke Technology And Development Llc Integrated coke plant automation and optimization using advanced control and optimization techniques
US11788012B2 (en) 2015-01-02 2023-10-17 Suncoke Technology And Development Llc Integrated coke plant automation and optimization using advanced control and optimization techniques
US10526542B2 (en) 2015-12-28 2020-01-07 Suncoke Technology And Development Llc Method and system for dynamically charging a coke oven
US11214739B2 (en) 2015-12-28 2022-01-04 Suncoke Technology And Development Llc Method and system for dynamically charging a coke oven
US11508230B2 (en) 2016-06-03 2022-11-22 Suncoke Technology And Development Llc Methods and systems for automatically generating a remedial action in an industrial facility
US11845898B2 (en) 2017-05-23 2023-12-19 Suncoke Technology And Development Llc System and method for repairing a coke oven
US10851306B2 (en) 2017-05-23 2020-12-01 Suncoke Technology And Development Llc System and method for repairing a coke oven
US11680208B2 (en) 2018-12-28 2023-06-20 Suncoke Technology And Development Llc Spring-loaded heat recovery oven system and method
US11365355B2 (en) 2018-12-28 2022-06-21 Suncoke Technology And Development Llc Systems and methods for treating a surface of a coke plant
US11505747B2 (en) 2018-12-28 2022-11-22 Suncoke Technology And Development Llc Coke plant tunnel repair and anchor distribution
US11597881B2 (en) 2018-12-28 2023-03-07 Suncoke Technology And Development Llc Coke plant tunnel repair and flexible joints
US11643602B2 (en) 2018-12-28 2023-05-09 Suncoke Technology And Development Llc Decarbonization of coke ovens, and associated systems and methods
US11098252B2 (en) 2018-12-28 2021-08-24 Suncoke Technology And Development Llc Spring-loaded heat recovery oven system and method
US12060525B2 (en) 2018-12-28 2024-08-13 Suncoke Technology And Development Llc Systems for treating a surface of a coke plant sole flue
US11261381B2 (en) 2018-12-28 2022-03-01 Suncoke Technology And Development Llc Heat recovery oven foundation
US11760937B2 (en) 2018-12-28 2023-09-19 Suncoke Technology And Development Llc Oven uptakes
US11071935B2 (en) 2018-12-28 2021-07-27 Suncoke Technology And Development Llc Particulate detection for industrial facilities, and associated systems and methods
US11008518B2 (en) 2018-12-28 2021-05-18 Suncoke Technology And Development Llc Coke plant tunnel repair and flexible joints
US11021655B2 (en) 2018-12-28 2021-06-01 Suncoke Technology And Development Llc Decarbonization of coke ovens and associated systems and methods
US11193069B2 (en) 2018-12-28 2021-12-07 Suncoke Technology And Development Llc Coke plant tunnel repair and anchor distribution
US11845897B2 (en) 2018-12-28 2023-12-19 Suncoke Technology And Development Llc Heat recovery oven foundation
US11395989B2 (en) 2018-12-31 2022-07-26 Suncoke Technology And Development Llc Methods and systems for providing corrosion resistant surfaces in contaminant treatment systems
US11819802B2 (en) 2018-12-31 2023-11-21 Suncoke Technology And Development Llc Methods and systems for providing corrosion resistant surfaces in contaminant treatment systems
US11486572B2 (en) 2018-12-31 2022-11-01 Suncoke Technology And Development Llc Systems and methods for Utilizing flue gas
US11767482B2 (en) 2020-05-03 2023-09-26 Suncoke Technology And Development Llc High-quality coke products
US11851724B2 (en) 2021-11-04 2023-12-26 Suncoke Technology And Development Llc. Foundry coke products, and associated systems, devices, and methods
US11946108B2 (en) 2021-11-04 2024-04-02 Suncoke Technology And Development Llc Foundry coke products and associated processing methods via cupolas
US12110458B2 (en) 2022-11-04 2024-10-08 Suncoke Technology And Development Llc Coal blends, foundry coke products, and associated systems, devices, and methods

Also Published As

Publication number Publication date
AU2979999A (en) 1999-09-20
EP1060229A4 (en) 2002-10-02
EP1060229A1 (en) 2000-12-20
CN1298437A (en) 2001-06-06

Similar Documents

Publication Publication Date Title
EP1060229A1 (en) Method and apparatus for handling and indirectly cooling coke
US7998316B2 (en) Flat push coke wet quenching apparatus and process
EP1994121B1 (en) Improved method and apparatus for producing coke
US4285772A (en) Method and apparatus for handlng and dry quenching coke
US4997527A (en) Coke handling and dry quenching method
CN104312596B (en) One kind leads the moveable tamping coke furnace U-tube smoke-guiding car of smoke pipe and its application method
CN107794063B (en) Red coke transfer device and transfer method suitable for coke quenching
CN220746018U (en) Quenching lifting structure for heat treatment of caterpillar links
US5190617A (en) Coke handling apparatus including coke box and carrier vehicle
CN217026048U (en) Vacuum carburizing multipurpose furnace production line
SU1701725A1 (en) Coke receiver for coke ovens
CN114381283B (en) Multilayer tunnel type carbonization pyrolysis furnace and carbonization method
SU1765155A1 (en) Transport system for loading of scorching coke into chamber of dry extinguishing
JPH09208965A (en) Red-hot coke transporting apparatus of chamber coke oven
PL106895B1 (en) COOLING CAB FOR EXTINGUISHING DISTRIBUTED COKEY STEEL
JPS6035083A (en) Apparatus for treating recovery coke from coke pusher

Legal Events

Date Code Title Description
WWE Wipo information: entry into national phase

Ref document number: 99805446.1

Country of ref document: CN

AK Designated states

Kind code of ref document: A1

Designated state(s): AU BR CA CN HU ID IL IN JP KR PL TR UA US

AL Designated countries for regional patents

Kind code of ref document: A1

Designated state(s): AM AZ BY KG KZ MD RU TJ TM AT BE CH CY DE DK ES FI FR GB GR IE IT LU MC NL PT SE

121 Ep: the epo has been informed by wipo that ep was designated in this application
DFPE Request for preliminary examination filed prior to expiration of 19th month from priority date (pct application filed before 20040101)
WWE Wipo information: entry into national phase

Ref document number: IN/PCT/2000/337/CHE

Country of ref document: IN

WWE Wipo information: entry into national phase

Ref document number: 09623720

Country of ref document: US

NENP Non-entry into the national phase

Ref country code: KR

WWE Wipo information: entry into national phase

Ref document number: 1999911066

Country of ref document: EP

WWP Wipo information: published in national office

Ref document number: 1999911066

Country of ref document: EP

WWW Wipo information: withdrawn in national office

Ref document number: 1999911066

Country of ref document: EP