Abstract: A heating flue for a coke oven includes a wedge-shaped refractory brick having at least one oblique surface and vertical cylindrical bores when the brick is inserted into the vertical portion of a duct at the bottom of the heating flue. This part of the duct has an increased diameter to support the brick so that the vertical sides abut the inner duct walls and the bottom oblique surface extends toward the mouth of an obliquely-rising portion of the duct. The sum of the cross-sectional areas of the cylindrical bores in the brick is from 0.75 to 1.5 times the flow cross section of the obliquely-rising duct portion. The cross-sectional area of the top of a wedge-shaped brick which is coplanar with the flue base is in a range of between 20 and 200 with the cross section of the cylindrical bore in the brick. The diameter of the bore is between 10 and 60 millimeters. A ratio of 0.3 to 1.

Abstract: The furnace system has a heating chamber wherein a rich combustion mixture is fed. The mixture has been preheated within a regenerator and the flue gas is ducted to another regenerator which is also fed with secondary air to more completely oxidize the flue gas. Part of the hot flue gas leaving the second regenerator is tapped and recirculated to the heating chamber and the remaining flue gas being fully oxidized is vented to the atmosphere. When the first mentioned regenerator becomes too cold to preheat the combustion mixture, given valves are opened and closed so that the combustion mixture first is preheated within the second regenerator, then burned, and directed to the heating chamber and the incomplete combustion flue gases are now ducted to the first mentioned regenerator to be completely oxidized as described before, and, in turn, to heat this regenerator.

Abstract: NO.sub.x emissions from a glass melting furnace are reduced by injecting ammonia into the exhaust gas stream on a flue between primary and secondary regenerator chambers in one embodiment, and in staged zones within a regenerator in another embodiment.

Abstract: A burner tip for passing fuel into a glass melting chamber having a fuel passageway and discrete cooling fluid passageways therein for cooling and shielding the burner tip from attack by a hostile gaseous chamber environment. A ceramic collar member is provided for minimizing inspirated air and cooling fluid may be passed through the burner tip during both the firing cycle and off-firing cycle. The burner tip is provided with small diameter cooling fluid passageways to establish a low volume, high velocity flow of cooling fluid sufficient to shield the burner tip from sting-out attack.

Abstract: A system for recovering heat from combustion flue gas, which transfers heat from the flue gas into combustion-supporting air, which is then used to burn a fuel in a combustion zone in a furnace or the like, so that useful heat is generated and a hot combustion flue gas is formed. Two heat sinks are provided, each for alternate absorption of heat from the hot flue gas, and desorption of heat into ambient combustion air so that the air is preheated. A reversible fan or blower is associated with each sink. The hot flue gas is passed successively through one heat sink and fan to atmospheric discharge for a finite time interval, while concomitantly passing cold and usually ambient combustion air successively through the other fan and heat sink so that the air is heated and a preheated combustion air stream is formed, which is subsequently passed to the combustion zone. After the finite time interval, the reversible fans are reversed for another finite time interval usually equal to the first time interval.

Abstract: In a coking operation where the heating medium is introduced into the furnace by way of a bottom fire box and wherein heat exchangers are provided for the waste gases, the waste gas is passed through a plurality of parallel channels serving as said heat exchangers and the useful portion of the total system available for such exchange is reduced when the coking time is increased beyond the time required at normal operation.

Abstract: A system for recovering the waste heat normally exhausted into the atmosphere by chemical or other processing plants. The invented system comprises a substantially self-contained apparatus for receiving hot exhaust gases and extracting the waste heat therefrom for some beneficial use, such as pre-heating inlet air in an inlet plenum. The system may include temperature and pressure controls which enhance the safety and efficiency of the system's operation, and further may include flow controls in a multiple burner installation so that the desired fuel air ratios and heat distribution may be achieved. By building the present invention as a substantially self-contained and self-supporting assembly, on site installation time and the required alteration of pre-existing on site equipment may be minimized, thereby affecting substantial economic savings by minimizing the resulting down time of the processing plant.

Abstract: A system for recovering the waste heat normally exhausted into the atmosphere by chemical or other processing plants. The invented system comprises a substantially self-contained apparatus for receiving hot exhaust gases and extracting the waste heat therefrom for some beneficial use, such as pre-heating inlet air in an inlet plenum. The system may include temperature and pressure controls which enhance the safety and efficiency of the system's operation, and further may include flow controls in a multiple burner installation so that the desired fuel air ratios and heat distribution may be achieved. By building the present invention as a substantially self-contained and self-supporting assembly, on site installation time and the required alteration of pre-existing on site equipment may be minimized, thereby affecting substantial economic savings by minimizing the resulting down time of the processing plant.

Abstract: Separate intake air and exhaust gas manifolds along each long checker-brick regenerator, each of which manifolds have separate adjustable sideports, valves, or gates in each branch duct that do not have to be readjusted each regeneration cycle, and which gates may be preadjusted and/or at-will adjusted from a common and even remote location.

Abstract: An industrial heating furnace wherein hot exhaust gases from the furnace are heat exchanged in a rotary ceramic heat exchanger with air which is supplied to burners in the furnace for combustion air. The temperature of the gases within the furnace is controlled and the ratio of the flow of gases through the two sides of the rotary heat exchanger is controlled at a predetermined value which is approximately one to maximize efficiency of the furnace operation and to minimize thermal stresses on the ceramic heat exchanger.

Abstract: In a regenerative furnace of the type used for melting glass, localized overheating of the regenerator packing is minimized, heating of the regenerator packing is made more uniform, and regenerator efficiency is improved by employing a movable baffle in the space beneath the regenerator packing and/or by a baffle in the plenum above the packing.

Abstract: Arrangement for preparing dry hot compressed air to be supplied to blast furnace, wherein a heat exchanger and a dehydrater assembly comprising a gas permeable regenerative moisture absorbing rotor are arranged in the air passage from blower to hot air furnaces so that the hot compressed air from the blower may be used to heat the dehydrated air and to regenerate the rotor. Air leakage between regenerating and dehydrating zones in the dehydrater is prevented by sealing those clearances where otherwise such leakage would occur by packing elements to form sealed spaces and externally introducing dry pressurized air into each of said spaces.

Abstract: Assembly for dehydrating atmospheric air at the input side of a blower for supplying air to a blast furnace comprising at least one gas permeable rotor containing a regenerative moisture absorbent wherein a hot combustion gas obtained by burning a waste gas from the blast furnace is utilized for regenerating the absorbent and wherein means for regulating the relative humidity of the moist air to be dehydrated, which does not need any external heat source, is provided to avoid deliquescence of the absorbent. The rotor preferably comprises a layer containing the absorbent and a layer of an adsorbent capable of adsorbing impurities contained in the air.

Abstract: In a regenerative furnace of the type used for melting glass, localized overheating of the regenerator packing is minimized, heating of the regenerator packing is made more uniform, and regenerator efficiency is improved by employing a movable baffle in the space beneath the regenerator packing and/or by a baffle in the plenum above the packing.

Abstract: An industrial heating furnace wherein heat in exhaust gases is transferred to combustion air for burners in the furnace through a rotary ceramic heat exchanger. In one embodiment, turbulating air pipes are positioned in the furnace and the heated combustion air is supplied to the turbulating air pipes as well. The turbulating air pipes may be juxtaposed to and positioned across an elongated heating chamber. Liquid fuel in atomized form can be injected into the heated combustion air upstream of the burner.

Abstract: A flue gas collector for coke ovens, particularly regeneratively-heated coke ovens, wherein the base, crown and side walls of the flue gas collector are formed from reinforced concrete in a generally rectangular cross-sectional configuration and are provided with insulating material on their interior surfaces. Additionally, insulating material is disposed between apertures in the flue gas collector and the ends of outlet pipes leading from changeover valves connected to the coke oven regenerators. The insulation is of such nature and thickness so as to insure that the reinforced concrete body of the collector assumes only negligible temperatures throughout, thereby eliminating cracks and leaks in the walls of the collector.

Abstract: A glass making furnace having a preheater and recycling structure including a tubular housing having a lower gas receiving stack section, a top in the form of an inverted cone, a glass batch pellet containing intermediate section, having a lower portion over the cone and about the intermediate section, gas ports in the side of the cone, shield means over the ports, a discharge valve in the lower portion below the cone part, a hot gas stack extending over the upper portion of the pellet section, a fan or hot gas ejector at the top of the stack, a damper above the fan or hot gas ejector connecting with a pressure controller within the furnace for maintaining the pressure in the furnace slightly above atmospheric, an inlet valve outwardly of the upper portion of the pellet section to control the entrance of the pellets, a regenerator on each side of the melting section and port and burner means communicating with each regenerator, a reversing valve connected with the regenerators and the melting section, and a p

Abstract: A glass making furnace having a preheater and recycling structure including a tubular housing having a lower gas receiving stack section, a top in the form of an inverted cone, a glass batch pellet containing intermediate section, having a lower portion over the cone and about the intermediate section, gas ports in the side of the cone, shield means over the ports, a discharge valve in the lower portion below the cone part, a hot gas stack extending over the upper portion of the pellet section, a fan or hot gas ejector at the top of the stack, a damper above the fan or hot gas ejector connecting with a pressure controller within the furnace for maintaining the pressure in the furnace slightly above atmospheric, an inlet valve outwardly of the upper portion of the pellet section to control the entrance of the pellets, a regenerator on each side of the melting section and port and burner means communicating with each regenerator, a reversing valve connected with the regenerators and the melting section, and a p