Systems and methods for maintaining a hot car in a coke plant

Abstract

The present technology describes various embodiments of systems and methods for maintaining a flat push hot car. In some embodiments, the flat push hot car includes an at least partially enclosed hot box having an interior portion, an exterior portion, a base, and a plurality of sidewalls extending upward from the base. The hot box can be coupled to or integrated with a fluid distribution system. The fluid distribution system can include a spray manifold having one or more inlets configured to release a fluid directed toward the sidewalls of the interior portion so as to provide regional cooling to the hot box.

Description

TECHNICAL FIELD

The present technology is generally directed to systems and methods for maintaining a flat push hot car in a coke plant. More specifically, some embodiments are directed to systems and methods for cooling a hot box portion of a flat push hot car.

BACKGROUND

Coke is a solid carbon fuel and carbon source used to melt and reduce iron ore in the production of steel. To make coke, finely crushed coal is fed into a coke oven and heated in an oxygen depleted environment under closely controlled atmospheric conditions. Such an environment drives off volatile compounds in the coal, leaving behind coke. In some coking plants, once the coal is “coked out” or fully coked, an oven door is opened and the hot coke is pushed from the oven into a hot box of a flat push hot car (“hot car”). The hot car then transports the hot coke from the coke oven to a quenching area (e.g., wet or dry quenching) to cool the coke below its ignition temperature. After being quenched, the coke is screened and loaded into rail cars or trucks for shipment or later use.

Over time, the volatile coal constituents (i.e., water, coal-gas, coal-tar, etc.) released during the coking process can accumulate on the interior surfaces of the coke oven, forming gummy, solidified by-product deposits. As used herein, “deposit(s)” refers to one or more coking by-products that can accumulate within the coke oven, such as, for example, clinkers, ash, and others. Such deposits can have a variety of adverse effects on coke production, including slowing and/or complicating the hot coke pushing operation, decreasing the effective dimensions of the oven, and lowering the thermal conductivity of the oven walls and/or floor. Because of such adverse effects, deposit removal (“decarbonization”) is a mandatory aspect of routine coke oven maintenance in order to maintain coke plant efficiency and yield.

To remove deposits from the coke ovens, oven operation (and thus coke production) must be interrupted so that the deposits can be targeted and pushed out of the ovens and into the hot car hot box for disposal. Much like the hot coke, deposits are extremely hot and exert a large amount of thermal and mechanical stress on the hot box in addition to the wear and tear of routine hot coke transportation. For these reasons, the hot box and/or the hot box's individual components can have a relatively short life. Many conventional coke plants attempt to mitigate damage to the hot box by breaking up large deposits and transporting them to a quench tower for cooling in manageable, smaller portions. However, such an iterative approach takes a long time to remove the waste, thus keeping the ovens/quench tower out of operation and coke production at a halt. In addition, removing the waste in pieces increases the number of transports required of the hot cars, exposing hot cars and/or its individual components to increased amount of thermal and mechanical stress.

BRIEF DESCRIPTION OF THE DRAWINGS

FIG. 1 is a plan view of a portion of a coke plant in accordance with embodiments of the present technology.

FIG. 2 is an elevational end view of a flat push hot car in accordance with embodiments of the present technology.

FIG. 3A is an elevational end view of a hot box in accordance with embodiments of the present technology.

FIG. 3B is a side view of a hot box in accordance with embodiments of the present technology.

FIG. 4A is a perspective view of a fluid distribution system in accordance with embodiments of the present technology.

FIG. 4B is a simplified plan view of the fluid distribution system of FIG. 4A in accordance with embodiments of the present technology.

FIG. 4C is a simplified plan view of a fluid distribution system view in accordance with embodiments of the present technology.

FIG. 4D is a simplified plan view of a fluid distribution system view in accordance with embodiments of the present technology.

FIG. 4E is a simplified plan view of a fluid distribution system view in accordance with embodiments of the present technology.

FIG. 4F is a simplified plan view of a fluid distribution system view in accordance with embodiments of the present technology.

FIG. 4G is a simplified plan view of a fluid distribution system view in accordance with embodiments of the present technology.

FIG. 4H is a simplified plan view of a fluid distribution system view in accordance with embodiments of the present technology.

FIG. 4I is a simplified plan view of a fluid distribution system view in accordance with embodiments of the present technology.

FIG. 4J is a simplified plan view of a fluid distribution system view in accordance with embodiments of the present technology.

FIG. 5A is an elevational side view of a hot box and a fluid distribution system in accordance with embodiments of the present technology.

FIG. 5B is an elevational side view of a hot box and a fluid distribution system in accordance with embodiments of the present technology.

FIG. 5C is an elevational side view of a hot box and a fluid distribution system in accordance with embodiments of the present technology.

FIG. 5D is an elevational side view of a hot box and a fluid distribution system in accordance with embodiments of the present technology.

FIG. 5E is a schematic illustration of a hot box and a fluid distribution system in accordance with embodiments of the present technology.

FIG. 5F is a schematic sectional view of the hot box of FIG. 5E taken along lines 1, 2, and 3.

FIG. 6A is an elevational side view of a hot box and a fluid distribution system having a fluid source in accordance with embodiments of the present technology.

FIG. 6B is an elevational side view of a hot box and fluid source carried by a flat push hot car in accordance with embodiments of the present technology.

FIG. 6C is an elevational side view of the hot box and fluid source of FIG. 6B in accordance with embodiments of the present technology.

DETAILED DESCRIPTION

The present technology describes various embodiments of systems and methods for maintaining a flat push hot car. In some embodiments, the flat push hot car includes an at least partially enclosed hot box having an interior portion, an exterior portion, a base, and a plurality of sidewalls extending upward from the base. The hot box can be coupled to or integrated with a fluid distribution system. The fluid distribution system can include a spray manifold having one or more inlets configured to release a fluid directed toward the sidewalls of the interior portion so as to provide regional cooling to the hot box.

Specific details of several embodiments of the technology are described below with reference to FIGS. 1-6C. Other details describing well-known structures and systems often associated with coal processing and/or cooling systems have not been set forth in the following disclosure to avoid unnecessarily obscuring the description of the various embodiments of the technology. Many of the details, dimensions, angles and other features shown in the Figures are merely illustrative of particular embodiments of the technology. Accordingly, other embodiments can have other details, dimensions, angles, and features without departing from the spirit or scope of the present technology. A person of ordinary skill in the art, therefore, will accordingly understand that the technology may have other embodiments with additional elements, or the technology may have other embodiments without several of the features shown and described below with reference to FIGS. 1-6C.

FIG. 1 is a plan schematic view of a coke oven battery 10 and associated equipment, including a hot car 24, according to embodiments of the technology. As used herein, “hot car” may comprise a flat push hot car, train, and/or a combined flat push hot car/quench car. The typical coke oven battery 10 contains a plurality of side-by-side coke ovens 12. Each of the coke ovens 12 has a coal inlet end 14 and a coke outlet end 16 opposite the inlet end 14. Once the coal is fully coked (typically 24-120 hours), an exit door removing device 20 is positioned adjacent the outlet end 16 of the oven 12 and removes an exit door of the oven 12. After removing the exit door, the door removing device 20 is moved away from the outlet end 16 of the oven 12 along door removal rails 22. A discharge ram 18 positioned adjacent to the inlet end 14 of the oven 12 pushes the hot coke and/or deposits out of the oven 12. The discharge ram 18 may include a device for removing an inlet end 14 oven door prior to pushing the coke out of the oven 12. A hot car 24 (described in greater detail below) is positioned adjacent to the outlet end 16 of the oven 12 for collection of hot coke and/or deposits 26 pushed from the oven by the discharge ram 18. Once the hot coke or deposits 26 is loaded onto the hot car 24, the car 24 is transported on rails 28 to a quench car area 30. In the quench car area 30, the hot coke slab or deposits 26 on the hot car 24 is pushed by a stationary pusher 32 onto a quench car 34. Once the quench car 34 receives the hot coke or deposits 26, the quench car 34 is positioned in a quench station 36 wherein the hot coke or deposits 26 is quenched with sufficient water to cool the coke or deposits 26 to below a coking temperature. The quenched coke is then dumped onto a receiving dock 38 for further cooling and transport to a coke storage area.

In some embodiments described herein, a single hot car 24 may be used for multiple coke batteries 10 since the coke is quenched in a separate quench car 34. As soon as the hot coke or deposits 26 is pushed from the hot car 24 onto the quench car 34, the hot car 24 may be repositioned adjacent to the outlet end 16 of another oven 12 for collection of coke or deposits 26 from that oven 12. In further embodiments, the hot car 24 can be a combined hot car/quench car.

With reference now to FIGS. 2-6C, various aspects of the hot car 24 will be illustrated and described. As shown in the elevated cross-sectional end view of FIG. 2, the hot car 24 can include a hot box 44 configured to receive hot coke and/or deposits 26. The hot car 24 can further include a hot box fluid distribution system 100 coupled to the hot box 44. As explained below, the fluid distribution system 100 provides efficient cooling processes to the hot box 44 to extend its useful life and/or the useful life of the individual components of the hot box 44. The hot car 24 is mounted on a frame 70 that contains wheels 72 for movement of the hot car 24 on the rails 28 to and from the ovens 12 to the quench station 36 (the ovens 12 and quench station 36 are shown in FIG. 1).

FIGS. 3A and 3B show the hot box 44 configured in accordance with embodiments of the present technology. The hot box 44 is a substantially rectangular housing having a floor 60, two sidewalls 61, 62 and a ceiling 64, together defining an interior portion 43 therein. The hot box 44 can have a width W defined between the first sidewall 61 and the second sidewall 62 and a hot box length L defined between a first end 44a and a second end 44b. Each end 44a, 44b of the hot box can open to facilitate the hot box 44 in receiving or removing hot coke and/or deposits 26. Each of the floor 60, sidewalls 61, 62 and ceiling 64 can have an exterior surface (60a, 61a, 62a, and 64a, respectively) and an interior surface (60b, 61b, 62b, and 64b, respectively) as shown in FIG. 3A. In various embodiments, the sidewalls 61, 62 and/or floor 60 can be solid or fully or partially permeable and/or have apertures and/or cooling pipes therein.

As described above, the hot box 44 can include a fluid distribution system 100 configured to contain, deliver, and/or distribute cooling fluid 108 to one or more interior and/or exterior surfaces of the hot box 44. The fluid distribution system 100 can include a fluid source 106, a supply pipe 104 and a spray manifold 102 in fluid communication with one another. The spray manifold 102 can include one or more inlet pipes 114. As used herein, the term “pipe(s)” may comprise one or more ducts, channels, conduits, tunnels, and/or any other structure and/or material capable of moving and/or guiding a fluid, gas or semi-solid. At its downstream end, the inlet pipe 114 can have an inlet 110. The inlet 110 can protrude into the interior portion 43, be flush with the ceiling 64, or be positioned above the ceiling 64 wherein the ceiling 64 has apertures to allow fluid flow therethrough. The inlet 110 can release fluid 108 into the interior portion 43 of the hot box 44, and, as will be described in further detail below, can comprise a single inlet 110 or an array of inlets. The inlet 110 can include a nozzle 116, including a flat fan nozzle, flood nozzle, raindrop nozzle, hollow-cone nozzle, full-cone nozzle, directional or bi-directional nozzle, and others. In yet other embodiments, the inlet 110 may be an opening in the inlet pipe 114 that routes fluid 108 from the spray manifold 102 to an interior portion 43 of the hot box 44 (as explained in greater detail below with reference to FIG. 5C).

Although the embodiments shown in FIGS. 2-6C illustrate a hot box having two sidewalls and a ceiling, in some embodiments, the hot box may have more or less than two sidewalls. In yet other embodiments, the hot box may not have a ceiling or have a ceiling that covers only a portion of the hot box floor. In some embodiments, the hot box may have no sidewalls and simply comprise a fluid distribution system mounted over a hotbox floor.

In operation, the fluid source 106 provides fluid 108 to the supply pipe 104 which in turn transfers the fluid 108 to the spray manifold 102 for release and/or distribute through the inlet(s) 110 onto at least a portion of the interior and/or exterior surfaces of the hot box 44. For example, the inlets 110 can release and/or distribute fluid 108 onto at least a portion of the interior surface of the sidewalls 61b, 62b, floor 60b and/or ceiling 64b of the hot box 44, providing regional zones of cooling to the hot box 44. Such regional cooling almost immediately reduces the average temperature of the hot box 44 and decreases thermal stresses. In some embodiments, the sidewalls 61, 62 and/or floor 60 can be solid or fully or partially permeable and/or have apertures and/or cooling pipes therein to release the cooling fluid 108 after it has interfaced with the interior surfaces of the hot box 44 or to provide fluid flow within the hot box 44. A “fluid” 108 may refer to any gas, liquid and/or semi-solid capable of lowering the average temperature of the hot box 44 or portion of the hot box 44 when applied to any portion of the hot box 44 and/or its contents. For example, in several embodiments, the fluid 108 can be water. In other embodiments, the fluid may include one or more chemicals able to extinguish or at least partially control a fire.

FIGS. 4A and 4B illustrate a perspective view and plan view, respectively, of the spray manifold 102. The spray manifold 102 may include an inlet array having one or more inlets 110 configured about one or more rows 112 and/or crosspieces 113 (the crosspieces are shown and discussed below with reference to FIGS. 4F-4I). The rows 112 and/or crosspieces 113 can be coupled to the supply pipe 104 in order to direct the cooling fluid from the supply pipe 104 to the inlets 110 via the inlet pipes 114.

As used herein, an “inlet array” refers to the various configurations and/or placement of the inlets 110 with respect to the rest of the hot box structure. For example, FIG. 4B shows the inlets 110 may be spaced along one or more parallel rows 112. In other embodiments, as shown in the schematic plan views of FIGS. 4C-4J, the spray manifold 102 may comprise one or more of a variety of inlet arrays based on the desired fluid distribution pattern and/or targeted cooling regions. For example, in the embodiment shown in FIG. 4F, the inlets 110 and/or inlet pipes 114 may be arranged on the spray manifold 102 along a perimeter of the hot box 44 so as to direct a cooling fluid towards the interior surfaces of the sidewalls 61b, 62b and/or ends 44a, 44b of the hot box 44. During decarbonization, it is important to adequately cool the hot box sidewalls so as to preserve the integrity of the hot box 44 structure and/or materials.

The inlet pipes 114 and/or inlets 110 may have approximately the same or varied placement along one or more rows 112 and/or crosspieces 113. For example, in some embodiments the inlet pipes 114 and/or inlets 110 may be evenly spaced along the row 112 and/or crosspiece 113 (i.e., FIG. 4B), while in other embodiments the inlet pipes 114 and/or inlets 110 may be unevenly spaced. In some embodiments, the inlet pipes 114 and/or inlets 110 may have approximately the same placement along adjacent rows 112 and/or crosspieces 113 relative to a length L of the hot box 44 (FIG. 4B), and/or in other embodiments the inlet pipes 114 and/or inlets may be offset (FIG. 4E).

The rows 112 and crosspieces 113 (and inlet array) can have a variety of sizes and/or configurations. In some embodiments, the inlet array may span the length L of the hot box 44 or may be shorter (i.e., FIG. 4J) or longer than the hot box (i.e., FIG. 4C). In some embodiments, some or all of the inlet pipes and/or inlets may be positioned outside of the width and/or length of the hot box so as to direct a cooling fluid onto an exterior surface of the hot box sidewalls 61, 62, ceiling 64, and/or floor 60 (i.e., FIG. 4F). In some embodiments, adjacent rows 112 may have approximately the same (i.e., FIG. 4E) or different lengths (i.e., FIG. 4J) to provide symmetric or asymmetric cooling in the hot box 44. The crosspieces 113 may run transverse to the rows 112 (i.e., FIGS. 4G and 4H) or may extend at any angle from the rows 112 (i.e., FIG. 4I). The crosspieces 113 may span the width W of the hot box 44 or may be shorter (i.e., FIG. 4G) or longer than (for example, see FIG. 4H) the hot box 44.

FIGS. 5A-5F illustrate several embodiments of fluid distributions systems providing regions of cooling in accordance with embodiments of the technology. In FIG. 5A, more than one inlet pipe 214 can branch from approximately the same portion of a spray manifold 202 to form a nozzle cluster 115. Likewise, the inlet pipes 214 and/or nozzles 216 associated with a nozzle cluster 115 may have varying directionality. For example, in FIG. 5A, inlet pipe 214a is angled towards sidewall 61, inlet pipe 214b extends substantially straight down, and inlet pipe 214c is angled towards sidewall 62.

In some embodiments, as shown in FIG. 5A, the spray manifold 202 can be positioned along the hot box ceiling 64, or can be spaced apart from the hot box ceiling 64. In further embodiments, as shown in FIG. 5B, the spray manifold 302 can be positioned along one or more hot box sidewalls 61, 62. The spray manifold 302 may comprise rows 312 positioned proximate the sides 61, 62 of the hot box 344 with inlet pipes 314 coming through or positioned along the sidewalls 61, 62. In other embodiments, the rows can be proximate to the bottom 49 of the hot box (not shown). In still further embodiments, the inlet pipes can be positioned all or partially external to the hot box (e.g., to distribute fluid to an exterior surface of the hot box).

As shown in FIG. 5C, the inlets 410 can comprise an opening in the inlet pipe 414 and/or spray manifold 402 such that gravity pulls the fluid onto the hot box 444. In these embodiments, at least a portion of the fluid source (not shown) can be positioned vertically above the inlets 410 so as to create sufficient head pressure (as discussed below with reference to FIGS. 6A-6B). In some embodiments, as shown in FIG. 5D, the inlet pipes 514 may be angled as they extend downward from the intersection 515. In yet other embodiments, the inlet pipes 514 may extend substantially perpendicular to the hot box floor 60 (for example, see FIG. 3A, described above).

FIGS. 5E and 5F show an embodiment in accordance with the present technology where a hot box 744 has a fluid distribution system 700 comprising pipes 702 within its sidewalls 761, 762, ceiling 764, and/or floor 760 (collectively represented in FIG. 5F by element 763). The pipes 702 carry a cooling fluid 704 and may comprise a serpentine configuration (as shown in the cross-sectional view of FIG. 5F) or may comprise any appropriate configuration to achieve one or more desired regions of cooling.

The fluid distribution system may have one or more valves located at any point within the system. For example, a valve may be located at the juncture between the fluid supply and the supply pipes. In other embodiments, valves may be located at each inlet. Control of the valves and/or release of the fluid may be triggered manually, on a pre-set schedule, automatically by a controller, or manually with an automatic override. Likewise, the fluid may be released from all inlets simultaneously and/or programmed preferentially to form a localized group of targeted cooling regions.

The controller can be a discrete controller associated with a single inlet or multiple automatic inlets, a centralized controller (e.g., a distributed control system or a programmable logic control system), or a combination of the two. Accordingly, individual inlets and/or valves can be operated individually or in conjunction with other inlets or valves.

In some embodiments, the coke plant, hot car, hot box, and/or fluid distribution system may include a fluid collection system to redirect and/or retain fluid overflow from the hot box. In some embodiments, the fluid collection system may filter then recycle the overflow. In other embodiments, the fluid collection system may include a pump to facilitate reuse of the overflow. In yet other embodiments, at least a portion of the fluid collection system may be positioned below the base of the hot box such that fluid overthrow is forced through the fluid collection system, which filters the overflow before it hits the ground. In further embodiments, fluid overflow may be allowed to flow substantially unfiltered to the ground.

As shown in FIG. 6A, the fluid source 106 may comprise a local fluid reservoir 106 having a hose 120 in fluid connection with the supply pipe 104 which transfers the fluid 108 from the fluid source 106 to the spray manifold 102. The length of the hose 120 can be sufficient to remain coupled to the fluid distribution system 100 of the hot car 44 as the hot car 24 moves along the rails 28, or can be separable from the hot car 44.

FIGS. 6B-6C illustrate embodiments wherein the fluid source comprises a pump or pressurized tank and/or reservoir 606 coupled to the hot car 24. In some embodiments, at least a portion of the fluid source can be positioned vertically above the inlets 610 so as to create sufficient head pressure. The hot box 644 includes a hot box connection 124 in fluid connection with the spray manifold 602. The connection 124 is configured to mate with a hot car connection 126. In operation, when an elevation and translation system 46 moves the hot box 44 back onto the flat push hot car 24 after being positioned adjacent to the oven 12, the hot box connection 124 mates with the flat push hot car connection 126 to effectively seal the system. Furthermore, in some embodiments, the reservoir 606 could be carried by the hot box 44. For example, the reservoir 606 may be located on top of a hot box ceiling or be coupled to a sidewall.

In some embodiments, the hot car may include several other features for interfacing with the coke oven, quench car, and/or other coke plant equipment. For example, the hot car may include an elevation and translation mechanism 46 (shown in FIG. 6B) configured to elevate and translate the hot box 44 so as to position the hot box 44 adjacent the outlet end 16 of the oven 12. The elevation and translation mechanism provides for a relatively smooth transition for the hot coke and/or deposits 26 to move from the oven floor to the hot box 44. The flat push hot car 24 may also include a dust collection system in flow communication with the hot box 44 via a collection duct to collect any dust or fumes that may be evolved from the coke during the coke pushing operations. In some embodiments, the flat push hot car 24 may further include a lintel sealing device that provides sealing between the hot box 44 and the oven 12 in order to reduce an amount of dust that may escape from the open end 16 of the oven 12. In yet other embodiments, an oven skirt sweeping mechanism may be provided on the transition section in order to prevent accumulation of coke dust on an oven sill attached to each oven 12 after removing the oven exit door 40 or after pushing the hot coke and/or deposits 26 onto the hot car 24.

In operation, the fluid distribution system 100 may be utilized during an emergency situation where the hot car 24 breaks down and is unable to complete transport of the hot coke and/or deposits to a quenching area. Not only does this stall coke production, but it also significantly delays cooling of the hot car, likely resulting in irreparable damage to the hot car 24 and/or hot box 44. If such a failure occurs, the fluid distribution system may be manually or automatically triggered and immediately begin cooling the hot box and/or its contents.

The fluid distribution system 100 may also be used during the decarbonization process. As explained above, decarbonization is a mandatory aspect of routine coke oven maintenance in order to maintain coke plant efficiency and yield. Because the fluid distribution system provides regional cooling of the hot box (thus lowering the average temperature of the hot box), the hot box is able to handle and thus transport larger deposits piles than it could without a cooling system. By transporting larger deposits piles, the flat push hot car can dispose of deposits in fewer transports than conventional coke oven systems. Fewer transports free the flat push hot cars and ovens sooner so that coke production may continue, giving a coke plant a higher coke yield. Moreover, fewer transports also means less thermal and mechanical stress on the flat push hot cars, thus increasing their useful life.

EXAMPLES

1. A hot car for use in a coke plant, the hot car comprising:

• • an at least partially enclosed hot box having an interior portion, an exterior portion, a base, and a sidewall extending upward from the base; and
  • a fluid distribution system coupled to the hot box, the fluid distribution system comprising a plurality of fluid inlets configured to release a fluid directed toward the sidewall of the interior portion.

2. The hot car of example 1, further comprising a reservoir in fluid communication with the fluid distribution system and configured to contain fluid.

3. The hot car of example 1 wherein at least a portion of the fluid distribution system is positioned within at least one of the sidewalls.

4. The hot car of example 1 wherein at least a portion of the fluid distribution system is positioned within the base.

5. The hot car of example 1 wherein the interior portion comprises a peripheral portion proximate to the sidewalls and a central portion spaced apart from the sidewalls, and wherein the fluid inlets are positioned in the peripheral portion.

6. The hot car of example 1 wherein individual fluid inlets comprise a nozzle configured to direct fluid toward the sidewalls.

7. The hot car of example 1 wherein the hot box comprises a top portion at least partially covering the interior portion of the hot box, wherein the plurality of fluid inlets are spaced apart from the top portion.

8. The hot car of example 1 wherein at least one fluid inlet is coupled to a sidewall.

9. The hot car of example 1, further comprising an elevation and translation mechanism.

10. The hot car of example 1 wherein the fluid comprises water.

11. The hot car of example 1 wherein the fluid inlets are evenly spaced along two substantially parallel rows along a longitudinal axis of the hot box.

12. The hot car of example 1 wherein the fluid inlets are positioned along a crosspiece extending along a width of the hot box.

13. The hot car of example 1, further comprising a fluid source operably connected to the fluid distribution system.

14. A method of cooling a hot car in a coke production system, the method comprising:

• • introducing fluid to a fluid distribution system coupled to the hot car, wherein the hot car comprises a car base and a plurality of car sidewalls extending upward from the car base;
  • directing fluid from the fluid distribution system toward the sidewalls; and
  • cooling the sidewalls.

15. The method of example 14, further comprising releasing the fluid through one or more apertures in the hot car after the fluid has interfaced with the sidewalls.

16. The method of example 14 wherein directing fluid from the fluid distribution system toward the sidewalls comprises directing fluid through an array of nozzles.

17. The method of example 14 wherein directing fluid from the fluid distribution system toward the sidewalls comprises directing fluid through a plurality of inlet pipes proximate to the sidewalls.

18. The method of example 14 wherein introducing fluid to the fluid distribution system comprises introducing fluid from a fluid reservoir carried by the hot car.

19. The method of example 14 wherein directing fluid from the fluid distribution system toward the sidewalls comprises directing the fluid using a gravity-feed system.

20. The method of example 14 wherein directing fluid from the fluid distribution system toward the sidewalls comprises directing pressurized fluid toward the sidewalls.

21. A system for cooling a hot box, wherein the hot box has an interior surface comprising a floor and at least two sidewalls, the system comprising:

• • a fluid source;
  • a supply conduit coupled to the fluid source;
  • a spray manifold carried by the hot box and in fluid communication with the supply conduit; and
  • a dispenser coupled to the spray manifold, wherein the dispenser is configured to direct a fluid onto an interior surface of a hot box.

22. The system of example 21 wherein the dispenser comprises one or more of a flat fan nozzle, flood nozzle, raindrop nozzle, hollow-cone nozzle, full-cone nozzle, or directional or bi-directional nozzle.

23. The system of example 21, further comprising a fluid collection system configured to collect the fluid for at least one of reuse and disposal.

24. The system of example 21 wherein the hot box is coupled to at least one of a hot car and a hot train.

25. The system of example 21 wherein the hot box has an exterior surface, and wherein the dispenser is configured to direct a fluid onto at least one of an exterior surface and the interior surface.

The present technology offers several additional advantages over traditional systems. For example, the steel plates within the hot car may begin the cooling process sooner, thus extending the useful life of the steel plates and reducing the frequency of steel plate changes. Further, use of a fluid distribution system requires fewer people to start the cooling process. In several embodiments, the present system is able to cool the hot box while simultaneously decarbing the ovens.

Examples of suitable flat push hot cars are described in U.S. Pat. No. 8,152,970, filed Mar. 3, 2006, incorporated herein by reference in its entirety. Other suitable technologies are described in U.S. Pat. No. 7,998,316, filed Mar. 17, 2009 and U.S. patent application Ser. No. 13/205,960, filed Aug. 9, 2011, each of which are incorporated herein by reference in their entireties.

From the foregoing it will be appreciated that, although specific embodiments of the technology have been described herein for purposes of illustration, various modifications may be made without deviating from the spirit and scope of the technology. Further, certain aspects of the new technology described in the context of particular embodiments may be combined or eliminated in other embodiments. Moreover, while advantages associated with certain embodiments of the technology have been described in the context of those embodiments, other embodiments may also exhibit such advantages, and not all embodiments need necessarily exhibit such advantages to fall within the scope of the technology. Accordingly, the disclosure and associated technology can encompass other embodiments not expressly shown or described herein. Thus, the disclosure is not limited except as by the appended claims.

Claims

1. A system configured to cool a hot car for use in a coke plant, the system comprising: a hot box including a base configured to directly support a load of hot coke, a pair of opposing sidewalls extending vertically upward from and orthogonal to a surface of the base, the base and sidewalls defining an interior portion of the hot box, the hot box having a width dimension defining a width axis and a length dimension defining a length axis; anda fluid distribution system positioned over the hot box and configured to receive a cooling fluid from a fluid source, the fluid distribution system comprising— supply piping having (i) a first portion extending vertically adjacent each of the opposing sidewalls of the hot box and along the width axis over the hot box, and (ii) a second portion fluidically coupled to the first portion and including at least two rows of piping spaced apart from one another, each of the rows extending along the length axis over the hot box, anda plurality of fluid inlets spaced apart from one another and each extending toward the hot box from one of the rows, individual ones of the fluid inlets being configured to disperse the cooling fluid over at least a region of the interior portion and one of the sidewalls of the hot box.

2. The system of claim 1, the ceiling being curved such that peripheral portions of the ceiling are closer to the base than an intermediate portion of the ceiling.

3. The system of claim 1, wherein at least one of the fluid inlets includes a plurality of inlet nozzles fluidly coupled thereto.

4. The system of claim 1, wherein the hot box further comprises fluid distribution piping configured to receive the cooling fluid.

5. The system of claim 4, wherein the distribution piping is at least partially within at least one of the sidewalls or the base.

6. The system of claim 1, wherein the rows are laterally inward of the sidewalls.

7. The system of claim 1, wherein the second portion further comprises a crosspieces extending between the two rows to define a perimeter of the second portion.

8. The system of claim 7, wherein the perimeter of the second portion is within a perimeter defined by the hot box.

9. A cooling system for use in an industrial facility, the system comprising: a hot box including a base configured to directly support a load of hot coke, a first sidewall extending upward from the base along a first vertical plane, and a second sidewall extending upward from the base along a second vertical plane parallel to the first vertical plane, the first and second sidewalls each being substantially orthogonal to the base, wherein the base, first sidewall, and second sidewall define an interior portion of the hot box, the hot box having a width dimension defining a width axis and a length dimension defining a length axis; anda fluid distribution system positioned over the hot box and configured to receive a cooling fluid from a fluid source, the fluid distribution system comprising— supply piping having (i) a first portion extending vertically adjacent each of the opposing sidewalls of the hot box and along the width axis over the hot box, and (ii) a second portion fluidically coupled to the first portion and including at least two rows of piping spaced apart from one another, each of the rows extending along the length axis over the hot box, anda plurality of fluid inlets spaced apart from one another and each extending toward the hot box from one of the rows, individuals ones of the fluid inlets being configured to disperse the cooling fluid over at least a region of the interior portion and one of the sidewalls of the hot box.

10. The system of claim 9, further comprising curved ceiling such that peripheral portions of the ceiling are closer to the base than an intermediate portion of the ceiling.

11. The system of claim 9, wherein at least one of the fluid inlets includes a plurality of inlet nozzles fluidly coupled thereto.

12. The system of claim 9, wherein the hot box further comprises fluid distribution piping configured to receive the cooling fluid.

13. The system of claim 12, wherein the distribution piping is at least partially within at least one of the sidewalls or the base.

14. The system of claim 9, wherein the rows are laterally inward of the sidewalls.

15. The system of claim 9, wherein the second portion further comprises a crosspieces extending between the two rows to define a perimeter of the second portion.

16. The system of claim 15, wherein the perimeter of the second portion is within a perimeter defined by the hot box.

17. A cooling system for use in an industrial facility, the system comprising: a hot box including a base configured to directly support a load of hot coke, a first sidewall extending upward from the base along a first vertical plane, and a second sidewall extending upward from the base along a second vertical plane parallel to the first vertical plane, the first and second sidewalls each being substantially orthogonal to the base, wherein the base, first sidewall, and second sidewall define an interior portion of the hot box, the hot box having a width dimension defining a width axis and a length dimension defining a length axis; anda fluid distribution system positioned over the hot box and configured to receive a cooling fluid from a fluid source, the fluid distribution system comprising— supply piping having (i) a first portion extending vertically adjacent each of the opposing sidewalls of the hot box and along the width axis over the hot box, and (ii) a second portion fluidically coupled to the first portion and including a row of piping extending along the length axis over the hot box and a crosspiece of piping extending along the width axis over the hot box, anda plurality of fluid inlets spaced apart from one another and each extending toward the hot box from one of the row or the crosspiece, individuals ones of the fluid inlets being configured to disperse the cooling fluid over at least a region of the interior portion of the hot box.