1. Field of the Invention
The present invention relates to gas and fluid cooling of equipment, and more particularly to methods and devices for eliminating eddy currents in high velocity coolant flows through serpentine passageways.
2. Description of the Prior Art
Cooling is widely used in equipment and machines of all sizes and descriptions. Three modes of cooling, or heat transfer, depend on thermal radiation, heat conduction, and heat convention. Engines and other devices can generate enough heat that will destroy themselves if cooling were not used to keep the operating temperatures within acceptable limits. Radiators in cars are a familiar way that water coolants are circulated through a gas engine to keep its operating temperatures under 200° F. The excess heat is transferred to the air blowing through the engine compartment.
Fluid and gas-cooled castings and machined coolers are widely used in the roofs, walls and hearths of metallurgical furnaces, molds for solidification of molten materials, burners, lances, electrode clamps for conducting electricity in high voltage equipment, tuyere forced-air nozzles in iron smelting blast furnaces, etc. The most common cooling medias employed are forced air, circulating water, common oils, and synthetic oils.
Cooling passages can be manufactured inside metal pieces by drilling, machining, or casting. Coolant pipes can be cast inside the bulk of the metal piece, or the passages can be cast inside using thin wall techniques as is conventional in automobile engine blocks. For example, a copper-nickel pipe can be cast inside a bulk copper piece.
Drilling is usually not appropriate when complex cooling patterns are needed, so drilling has been limited to straight line passages. Cast-in-pipes provide excellent liquid conduits for the reliable containment of cooling mediums, but the passage shapes and layouts obtainable with piping are constrained by pipe size, coupling, bending, and welding considerations.
The amount of cooling possible in cast-in-pipe implementations is further limited by standard bend dimensions. For example, in a one inch Schedule-40 diameter pipe with a short radius 180° return, the center-to-center distance between the pipes is two times the nominal diameter, or two inches. But the inside diameter of the pipe is only 1.049 inches. So, if the pipe is bonded to a casting, then the width of the cooling channel is less than 50% of the bulk, based on minimum center-to-center spacing constraints.
The round cross section of pipes further reduces the effective cooling channel area, and thus the flow volume. A rectangular cross section would better fill the bulk area available.
Castings can employ cored or machined patterns, and typical cooling passages most commonly use a serpentine pattern implemented with thin-wall baffles. However, these simple designs can produce significant eddies in the coolant flow just past where the coolant is turned in each loop, and problems in cooling uniformity due to these eddies are amplified when the coolant velocity is pushed to high levels.
Equipment pieces with cored water passages can be manufactured in a single piece. But, the sand cores themselves must somehow be suspended in the piece mold to define the water passages during the casting pour. Any points where the sand core supports passed through the casting walls for containing the molten metal in the pour must be closed over later using plugs or welds.
The leak tightness in a metallic gas or fluid cooled piece can be improved by hot working or forging the hot face to refine the metal crystal grain size. For example, the average grain size for cast copper can be reduced from approximately ten millimeters to less than one millimeter using hot rolling, hot pressing, etc. The water passages are then milled in to the face of the worked part. A cover plate or second piece is required to complete the water passage and finish the milled piece.
Rectangular cross-section coolant passages with rounded corners are entirely possible and practical to do in castings with cored or machined cooling channels. The cooling medium can thereby occupy a large percentage of the available height and width inside the piece. Less metal would therefore be necessary, and cooling efficiencies would increase proportionately.
The large surface areas of the coolant passageways inside a cored or machined pattern can significantly increase the amount of heat transfer possible. However, the flow regime within the fluid coolant in conventional castings is typically quite poor. Eddies tend to form in the coolant flows aft of where they are being turned by the baffle ends. Hot spots can then build up because the coolant is ineffectually spinning around in small circles and can not carry any absorbed heat away. The heat at those spots can build up high enough to boil the coolant, and that can lead to the failure of the part and the connecting piping.
What is needed is a better baffle and passageway design that eliminates the inefficient eddies and their disastrous consequences in fast flowing coolants.
Briefly, a cooling system embodiment of the present invention comprises serpentine cooling fluid passages cast or milled into a work piece with carefully controlled turning radii and profiles. Individual interdigitated baffles are contoured in the plane of coolant flow to have walls that thicken and then round off at their distal ends. The outside radii at these turns are similarly rounded and controlled such that the coolant flow will not be swirled into eddies.
These and other objects and advantages of the present invention will no doubt become obvious to those of ordinary skill in the art after having read the following detailed description of the preferred embodiments which are illustrated in the various drawing figures.
While the invention is amenable to various modifications and alternative forms, specifics thereof have been shown by way of example in the drawings and will be described in detail. It should be understood, however, that the intention is not to limit the invention to the particular embodiments described. On the contrary, the intention is to cover all modifications, equivalents, and alternatives falling within the spirit and scope of the invention as defined by the appended claims.
In general, making the turning radii broader and wider will, at some point, eliminate eddies 112 in the coolant flow, but this must be balanced with the negative effects that thickening the walls of casting material to accommodate the rounded geometry will have on heat transfer performance. One way to find the optimum balance point is to employ computational fluid dynamics modeling software in simulations.
A first serpentine loop 114 turns around a first baffle 116 into a second serpentine loop 118. Baffle 116 is thickened toward a radius end 119 facing two outside radius corners 120 and 121. Such radius end 119, and radius corners 120 and 121, are proportioned to eliminate any eddy 124 that would otherwise form in the coolant flow if the turns were too sharp and abrupt.
A continuing series of baffles 126-131 are disposed in the serpentine passageway 106 to provide for additional turning of the circulating fluid coolant into each of a following series of serpentine loops 132-137. Each such turn invites the formation of more eddies 138-143 in the coolant flow that will swirl in the same plane as the serpentine passageway 106. Any such eddie formation can reduce the cooling performance in its immediate vicinity in the cast metal workpiece 102. In the applications contemplated for embodiments of the present invention, such loss of cooling performance at any spot can provoke a catastrophic failure incited by the high environmental heats surrounding it.
Each of baffles 126-131 is also thickened at their distal ends 144-149 and finished in a radius end. The corresponding outside corners that each faces are similar to radius corners 120 and 121. The coolant eventually exits to a chiller through an outlet 150.
Computational fluid dynamics (CFD) is a branch of fluid mechanics that uses numerical methods and algorithms to solve and analyze problems that involve fluid flows. Computers are used to perform the many calculations required to simulate interactions of fluids with surfaces defined by boundary conditions. Specialized software is commercially available that can report to a user the heat transfer performance and fluid velocities at selected points or modeling cells in a cooling system. For example, the ANSYS CFX software product marketed by ANSYS, Inc. (Canonsburg, Pa.) provides passage fluid flow modeling CFD software and engineering services. See, www.ansys.com/products/fluid-dynamics/cfx/. When used to construct embodiments of the present invention, the prospect of any eddies 112, 124, and 138-143 in the coolant are revealed by the modeling cells which are calculated to have zero velocity or whirling flows.
In
Otherwise, if the design is finalized, then sand casting cores can be constructed in a step 214. The castings are poured in a step 216, and machined in a step 218. The sand casting cores probably need stems to support them in position, and after the casting and machining is complete the residual holes in the castings can be plugged in a step 220. A step 222 is used to inspect, test, and ship the final cooling system. These workpieces are installed in their particular applications in a step 224.
A principal advantage of the present invention is that workpiece embodiments will have an extended service life that can be budgeted and maintained in a step 226.
At this point method 228 differs, if the design is finalized, then a piece is found or worked to obtain fine grain sizes in a step 230. The passages are milled in a step 232, and a passageway cover is machined in a step 234. The cover is welded on in a step 236. As in method 200, a step 222 is used to inspect, test, and ship the final cooling system. These workpieces are installed in their particular applications in a step 224. The embodiments will have an extended service life that is budgeted and maintained in a step 226.
Blast furnaces chemically reduce and physically convert iron oxides into liquid iron. Blast furnaces are very large, steel stacks lined with refractory brick that are fed a mixture of iron ore, coke and limestone from the top. Preheated air is blown into the bottom through tuyeres. Liquid iron droplets descend to the bottom of the furnace where they collect as slag and liquid iron. These are periodically drained from the furnace as the bottom fills up.
The hot air blown into the furnace at the bottom gets involved in many chemical reactions as it percolates to the top. Blast furnaces are run continuously for years with only short interrupts for maintenance. A common reason to interrupt the otherwise continuous operation of an iron smelting blast furnace is to change out its worn or damaged tuyeres. Tuyeres that last longer and suffer fewer injuries are therefore highly desirable.
Raw ore removed from the earth includes Hematite (Fe2O3) or Magnetite (Fe3O4) with an iron content of 50% to 70%, and is sized into small pieces about an inch in diameter. An iron-rich powder can be rolled into balls and fired in a furnace to produce marble-sized pellets with 60% to 65% iron. Sinter can also be used which is produced from fine raw ore, coke, sand-sized limestone and waste materials with iron. The fines mixed together for a desired product chemistry. The raw material mix is then placed on a sintering strand and ignited by a gas fired furnace to fuse the coke fines into larger size pieces. The iron ore, pellets and sinter are smelted into the liquid iron produced by the blast furnace. Any of remaining impurities go in to the liquid slag.
Hard pieces of coke with high energy values provide the permeability, heat, and gases needed to reduce and melt the iron ore, pellets and sinter.
The final raw material in the iron making process is limestone. The limestone is removed from the earth by blasting with explosives. It is then crushed and screened to a size that ranges from 0.5 inch to 1.5 inch to become blast furnace flux. This flux can be pure high calcium limestone, dolomitic limestone containing magnesia or a blend of the two types of limestone.
Since the limestone melts and becomes the slag that removes sulphur and other impurities, the blast furnace operator can adjust the blend accordingly to the desired slag chemistry. A blend target would be to create a low melting point, a high fluidity, and other optimum properties.
All of the raw materials are stored in an ore field and transferred to a nearby stock-house before charging. Once these materials are loaded into the furnace top, they go through numerous chemical and physical reactions as they descend to the bottom of the furnace.
The iron oxides drop through a series of purifying reactions to soften, melt and finally trickle out through the coke as liquid iron to the bottom of the furnace. The coke itself drops to the bottom of the furnace where preheated air and hot blasts from the tuyeres enters the blast furnace. The coke is ignited by the hot blast and immediately reacts to generate more heat.
The reaction takes place in the presence of excess carbon at a high temperature, so the carbon dioxide is reduced to carbon monoxide. The carbon monoxide reduces the iron ore in iron oxide reactions. The limestone also descends in the blast furnace, but it remains a solid while going through a first reaction, CaCO3=CaO+CO2. Such reaction requires energy and starts at about 875° C. The CaO formed from the reaction is used to remove sulphur from the iron, and is necessary before the hot metal can become steel. The sulphur removing reaction is, FeS+CaO+C=CaS+FeO+CO. The CaS becomes part of the slag. The slag is also formed from any remaining Silica (SiO2), Alumina (Al2O3), Magnesia (MgO) or Calcia (CaO) that entered with the iron ore, pellets, sinter or coke. The liquid slag then trickles through the coke bed to the bottom of the furnace where it will float on top of the more dense liquid iron.
Hot dirty gases exiting the top of the blast furnace proceed through gas cleaning equipment so particulate matter can be removed and the gas cooled. This gas has considerable energy value, so it is burned as a fuel in hot blast stoves that are used to preheat the air entering the blast furnace through the tuyeres. The tuyeres are therefore subjected to air temperatures that can well exceed 900° C. The melting point of copper is very near these temperatures at 1083° C. Any of the gas not burned in the stoves is sent to a boiler house to generate steam for turbo blowers that generate “cold blast” compressed air for the stoves.
The baffles that turn the coolant flow in the serpentine pattern, e.g., baffle 416, are like those described in
The serpentine passages 414 generally proceed in a curved plane within the conical body 402. A number of access holes 420 on an outside face of the cast metal body 402 allow the support of casting cores during metal cast, and that are sealed off with plugs 422. The plugs 422 may be conventionally pipe-threaded, welded, brazed, soldered, pressed, etc.
In one embodiment, angles “A” and “B” are each less than 90°, and A+B is less than 180°. In other words, the center lines of passageway loops 612 and 614 are not parallel to one another. Such an arrangement would help in packing the passageway loops 612 and 614 tighter, especially where every turn is like that of
Tuyeres and other coolers can be manufactured with or without surface coatings of refractory or overlays of metal. The type, location and thickness of such overlays are not part of the claims. Coolers can be manufactured with and without grooves or pockets filled with refractory. The shape and configuration of such grooves or pockets are not part of the claims. Tuyeres can be manufactured from either a casting or a fine grained metal part. With a casting, the water passages are cast in. With a machined part, the tuyere, for example, must be made in two parts. See, U.S. Pat. No. 3,840,219, FIG. 7. The outer or inner part would be machined, and a closure piece is used to complete the cooler and close the water passages. The tuyere may be fluid or gas injected.
In general, cooler embodiments of the present invention include profiling the coolant passages for the elimination of eddies where ever the cooler can be exposed to external heat loads.
Although the present invention has been described in terms of the presently preferred embodiments, it is to be understood that the disclosure is not to be interpreted as limiting. Various alterations and modifications will no doubt become apparent to those skilled in the art after having read the above disclosure. Accordingly, it is intended that the appended claims be interpreted as covering all alterations and modifications as fall within the “true” spirit and scope of the invention.
Number | Name | Date | Kind |
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6351381 | Bilski et al. | Feb 2002 | B1 |
20070267786 | Higgins et al. | Nov 2007 | A1 |
Number | Date | Country | |
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20110088600 A1 | Apr 2011 | US |