序号 专利名 申请号 申请日 公开(公告)号 公开(公告)日 发明人
121 Method for conditioning process gases for the heat treatment of metallic work pieces in industrial furnaces US12862898 2010-08-25 US08333852B2 2012-12-18 Werner Hendrik Grobler; Peter Haase; Bernd Edenhofer; Jens Bechthold; Thorsten Requardt; Thomas Eversmann
In a method and with a device for preparing process gases (3) for heat treatments of metallic materials/workpieces, the respective process gas (3) is to be fed into at least one treatment chamber (1.1) in an industrial furnace (1) having been practically fully prepared, homogenised and heated, and the method is to be carried out both with newly built and particularly with already existing installations of industrial furnaces (1) with the aid of the device, wherein the process gas (3) is prepared with compression at temperatures uncoupled from the temperature in the treatment chamber (1.1), in a process separate from the heat treatment process in the treatment chamber (1.1), and in a temperature range up to about 1250° C., and is rendered usable for economical and low-emission heat treatment (FIG. 3).
122 Method of production of secondary steel based on scrap US12798420 2010-04-01 US07909909B2 2011-03-22 Matthias Meyn
With the production of the secondary steel based on scrap, wherein the scrap (10) is fed in a scrap preheater (2) through a charging device (1), is preheated there and, finally, is brought into a smelting unit (3) and is melted there with primary energy only, the process gases (19), which leave the smelting unit (3), are not used for directly preheating the scrap (10) but are rather used indirectly by heating a gaseous preheatable medium, e.g., air (18) or inert gas, so that energetic, fluidic, and spatial decoupling of preheating and melting and of post-combustion and preheating is achieved.
123 METHOD FOR MANUFACTURING MOLTEN METAL US12989347 2009-04-22 US20110036201A1 2011-02-17 Masahiko Tetsumoto
A method for manufacturing molten metal by using a stationary non-tilting electric furnace including: a raw material charging chute that is provided in one end of the furnace in the width direction, and is connected to the interior of the furnace from the upper part of the furnace, an electrical heater that heats a lower position of the furnace in the height direction is located in the other end of the furnace in the width direction, and a secondary combustion burner that is provided at the furnace top and between the two ends of the furnace. The method comprising: forming a raw material layer by charging a particular amount of a carbonaceous material and/or metal oxide agglomerates with carbonaceous material containing a nonvolatile metal element that forms molten metal into the furnace from the raw material charging chute, and having a sloping surface extending downward from the one end of the furnace toward the other end of the; subsequently forming an agglomerate layer on the sloping surface of the raw material layer by charging a particular amount of the metal oxide agglomerates with carbonaceous material into the furnace from the raw material charging chute; and subsequently forming a molten metal layer and a molten slag layer in the furnace by heating the lower end of the agglomerate layer with the heater while allowing the agglomerate layer to descend along the sloping surface of the raw material layer toward the lower end by melting; and concurrently thermally reducing the agglomerate layer by radiant heat from secondary combustion by blowing oxygen-containing gas into the furnace from secondary combustion burner to burn CO-containing gas generated from the agglomerate layer.
124 Method of production of secondary steel based on scrap US12798420 2010-04-01 US20100263488A1 2010-10-21 Matthias Meyn
With the production of the secondary steel based on scrap, wherein the scrap (10) is fed in a scrap preheater (2) through a charging device (1), is preheated there and, finally, is brought into a smelting unit (3) and is melted there with primary energy only, the process gases (19), which leave the smelting unit (3), are not used for directly preheating the scrap (10) but are rather used indirectly by heating a gaseous preheatable medium, e.g., air (18) or inert gas, so that energetic, fluidic, and spatial decoupling of preheating and melting and of post-combustion and preheating is achieved.
125 SYSTEM AND METHOD OF PRODUCING METALLIC IRON US12444505 2007-10-04 US20100031776A1 2010-02-11 David Englund; Rodney Bleifuss; Iwao Iwasaki; Donald Fosnacht; Mark Brandon; Bradford True
A hearth furnace 10 for producing metallic iron material has a furnace housing 11 with a drying/preheat zone 12 capable of providing a drying/preheat atmosphere for reducible material, a conversion zone 13 capable of providing a reducing atmosphere for reducible material, a fusion zone 14 capable of providing an atmosphere to at least partially reduced metallic iron material, and optionally a cooling zone 15 capable of providing a cooling atmosphere for reduced material containing metallic iron material. A hearth 20 is movable within the furnace housing 11 in a direction through the drying/preheat zone 12, then the conversion zone 13, then the fusion zone 14, and then the cooling zone 15. A separation barrier 30 is positioned within at least a portion of the conversion zone 13, the separation barrier 30 separating the conversion zone 13 into a combustion region 32 and a reducing region 31 with the reducing region 31 adjacent the hearth 20 and the combustion region 32 adjacent the reducing region 31 and spaced from the hearth 20.
126 WIND AND UPDRAFT TURBINE US12298472 2007-04-20 US20090302614A1 2009-12-10 Barry Ross Ireland
The invention relates to the field of electrical generation and more specifically to the use of a wind turbine for generating electricity. A vertical axis wind turbine is mounted on the upper portion of a chimney. Rotor blades are disposed on the outside of the chimney and the mechanical energy produced by the rotating rotor blades is transferred to a generator by means of a short drive shaft. The drive shaft is used to drive the rotor within the generator to induce a voltage in the stator. In an alternate configuration, the wind turbine and generator are integrated. The rotor blades are coupled directly to a rotating, current inducing set of permanent magnets or rotor for rotation about a stationary, current generating stator. In either configuration, the rotor blades are rotated using the updraft associated with the chimney or the prevailing wind.
127 STEAM REFORMING APPARATUS AND METHOD FOR STEAM REFORMING USING THE SAME, AND INDUSTRIAL FURNACE US11738093 2007-04-20 US20070186471A1 2007-08-16 Yoshihiko Kurashima; Toshihiko Honda
A steam reforming apparatus (21) is configured to be placed in an industrial furnace (100) sintering an article to be sintered with a heat generated by fusing a fuel and to use a fed hydrocarbon and fed steam as raw materials. The apparatus (21) includes a low-temperature reforming section (23) and a high-temperature reforming section (22). The low-temperature reforming section (23) includes a metal tubular reactor (25) or a ceramic tubular reactor each housing a reforming catalyst for accelerating a steam reforming reaction, and the high-temperature reforming section (22) includes a ceramic tubular reactor (24) to cause a steam reforming reaction inside thereof. There is provided a steam reforming apparatus capable of recovering waste heat by using part of the combustion heat (waste heat) of the industrial furnace efficiently in accordance with the temperature range thereof.
128 Steel for exhaust gas processing equipment and exhaust gas duct excellent in wear resistance or wear resistance and gas cutting property US10579172 2004-11-12 US20070122650A1 2007-05-31 Akira Usami
A steel for exhaust gas processing equipment excellent in wear resistance containing, by mass%, C: 0.001 to 0.2%, Cu: 0.1 to 1%, Ni: 0.01 to 0.5%, Cr: 4.0 to 9.0%, and Sb: 0.01 to 0.2% and containing one or both of Mo: 0.005 to 0.5% and W: 0.005 to 0.5% and the balance of Fe and unavoidable impurities, and an exhaust gas duct configured using that steel.
129 METHOD AND APPARATUS FOR PREHEATING PARTICULATE MATERIAL US10676885 2003-09-30 US20050069832A1 2005-03-31 John Townsend; Charles Euston; Douglas Freeman; Michael Prokesch
An apparatus for preheating particulate material in which the particulate material is transferred from one or more upper storage bins to a circular lower chamber that has an outer, essentially annular, portion which serves as a gas flow passage. The particulate material is directed from the feed bin or bins into a plurality of essentially vertical cylindrical feed cassettes via intermediate feed ducts. The lower chamber has a flat roof which is in contact with the bottom portion of the vertical feed cassettes. The vertical feed cassettes are approximately evenly spaced on top of the outer perimeter of the flat roof. The particulate material is preheated in the annular flow passage by hot kiln gases flowing in countercurrent heat exchange relationship with the particulate material. Each feed cassette is completely segregated from its adjacent cassettes, and the bottom of each cassette is positioned over a hole in the flat roof of the lower chamber to thereby enable the particulate material to fall from each cassette into the annular flow passage section of the lower chamber. A plurality of particulate discharge mechanisms, the number of which correspond to the number of cassettes, discharges particulate material that has fallen into the annular flow chamber from the overhanging cassettes into a material outlet located in the floor located at the center of the lower chamber.
130 Low dew point gas generator cooling system US456490 1995-06-01 US5554230A 1996-09-10 Michael J. Huber; Jerry P. Jason; Garry W. Barbee
A drying system is disclosed for drying wet gases, typically produced by a gas generator to dew points less than 32.degree. F. The system uses a refrigeration cycle having a single compressor to dry the wet gas in a first evaporator while simultaneously defrosting the ice buildup on a second evaporator. The cycle then switches from the first evaporator to the second evaporator after the second evaporator is defrosted. The switching is preceded by a changeover phase in which cooled refrigerant is pulsed to the defrosted evaporator and both evaporators go on line for a short time before the system phase change occurs thus assuring control of the dried gas temperature while avoiding shock to the refrigeration system.
131 Recirculation device US294202 1981-08-19 US4427374A 1984-01-24 John W. Miller
A recirculation device for recirculating a selected volume of preheated gas exhausted from a heating chamber in a mixture with fresh air back to the heating chamber. The device comprises a first passageway having an entrance and a pair of exits; a second passageway having a pair of inlets and an outlet; and a third passageway connecting one exit and one inlet. The other exit communicates with a preheated gas exhaust, and the other intake communicates with a source of fresh air. A back pressure damper is secured adjacent the other exit. A manual control assembly is connected to the back pressure damper so that the volume of preheated gas flowing into the preheated gas exhaust may be selectively determined. A mixing damper is secured adjacent the other intake. An automatic temperature dependent control assembly is connected to the mixing damper so that the mixture of preheated gas and fresh air entering the heating chamber is dependent upon the temperature in the heating chamber.
132 Apparatus for preheating a steel scrap US292678 1981-08-13 US4373911A 1983-02-15 Takasaburo Date; Toshimichi Maki; Mitsuya Iguchi; Sumifusa Iwamaru; Hisashi Watanabe
An apparatus for preheating steel scrap comprises: a preheating vessel, having an open top and a bottom lid capable of being opened and closed, for receiving and preheating steel scrap, said preheating vessel being adapted to receive steel scrap to be preheated from said open top and to discharge the steel scrap preheated in said preheating vessel by opening said bottom lid; a hood downwardly flaring for covering said open top of said preheating vessel, said hood being movable from said open top of said preheating vessel and adapted to introduce high-temperature waste gases discharged from a steel-refining metallurgical furnace into said preheating vessel; a pit for housing said preheating vessel, said pit being provided with a duct for discharging to the outside said waste gases discharged into said pit from the bottom of said preheating vessel after preheating said steel scrap received in said preheating vessel; and, a canopy for sealing the gap between said pit and said preheating vessel housed in said pit, the gap between the periphery of said canopy and said pit being liquid-sealed. The apparatus is characterized in that: said canopy is gas-tightly fixed to said hood; and, the gap between said canopy and said preheating vessel housed in said pit is sealed by an expansion bellows fixed at an end thereof to said canopy.
133 Method for collecting the flue gases produced upon the charging of scrap and tapping of steel from electric furnaces US27051972 1972-07-10 US3876418A 1975-04-08 BAUM JORG PETER
This disclosure teaches a method and related system for collecting gases generated upon charging of scrap to and tapping of steel from an electric furnace. A charging basket is brought into sealed engagement with the furnace and is subjected to a vacuum. The top of a ladle is provided with an opening which is also subjected to a vacuum. Gases from the charging basket and from the ladle are delivered to a main aspirator duct to join gases generated during furnace operation for subsequent treatment.
134 Refractory members for use in terminal regenerators or recuperators US3777805D 1972-06-21 US3777805A 1973-12-11 RACASENS J; BLANCHET P; DUCHENOY J
The invention relates to refractory members for use in the construction, by stacking of a number of such members, thermal regenerators or recuperators, such as those used in conjunction with glass or metallurgical furnaces, for recovering the heat contained in flue gases. The invention provides that the refractory member is formed of a monolithic structure cast from fused refractory oxides. The member is in plan aspect shape composed predominantly of elongated portions, each having over the greater part of its length a maximum width which does not exceed 50 mm. The overall dimensions of the refractory member are sufficient to afford stability in stacking. The member may be star-shaped in plan aspect and it is advantageously formed by a number of parallelepipedal members joined together by casting into a monolith.
135 Smoke elbow for electric furnace US3772448D 1973-02-05 US3772448A 1973-11-13 BOWERMASTER R; BECKER R
A tiltable electric furnace comprising an open-top chamber and a roof adapted to be lifted off the top of the chamber and movable between an operating position in which it is at least partially clear of the chamber for charging said chamber from the top. The roof has a smoke outlet for discharge of gases from within said chamber when the furnace is in operation with the roof in its operating position. A smoke elbow is provided for conducting gases from the smoke outlet in the roof to a duct, the elbow being mounted independently of the roof for movement relative to the chamber between an operating position wherein its inlet end is in communication with said smoke outlet for conducting gases from the outlet to the duct, and a retracted position wherein its inlet end is clear of the roof for movement of the roof to its said retracted position, the duct being movable between an operating position wherein its inlet end is engaged with the outlet end of the elbow when the elbos is elbow its operating position, and a retracted position wherein its outlet end is clear of the elbow for movement of the elbow to its said retracted position.
136 INDUSTRIAL FURNACE AND METHOD FOR OPERATING AN INDUSTRIAL FURNACE PCT/DE2009000389 2009-03-26 WO2009121326A2 2009-10-08 HUSSLEIN MANFRED
The invention relates to an industrial furnace comprising a heatable interior chamber (1), a housing (2) enclosing the interior chamber (1), an insulating layer (3) which is at least partially lining the inner side of the housing (2), and thermal input means (4) for introducing thermal energy into the interior chamber (1). With respect to an energy-efficient operation, said industrial furnace is characterized by an insulating sleeve (7), which at least partially surrounds the housing (2) and is located at a distance from the housing wall, wherein a convection chamber (8) is formed between the housing wall and the insulating sleeve (2), and/or by a pre-heating and/or tempering furnace (10) in which the waste heat of the interior chamber (1) can be used. The invention further relates to a method for operating an industrial furnace.
137 METHODS OF THERMAL PROCESSING US15896343 2018-02-14 US20180231312A1 2018-08-16 Salvatore MORICCA; Simon Chung; Bruno Salvatore Angelico; Eric Stephens; Martin William Alexander Stewart
There is disclosed a vertical vibratory thermal treatment system, comprising a heating section for thermally treating material, a retort section that is located within or connected to the heating section and includes at least one elevator system for vertically moving the material to the heating section. The disclosed elevator system is isolated from other parts of the thermal treatment section by an enclosure thereby allowing for flexibility and simplicity in the design of the retort section. There is also disclosed a method of treating materials, including hazardous or radioactive materials, such as a powder, sand, granule, gravel, agglomerate or other form of particle or combinations thereof, using the system described herein.
138 METHOD FOR OPERATING BLAST FURNACE US15547891 2016-02-22 US20180023152A1 2018-01-25 Akinori MURAO; Naoki YAMAMOTO; Tomoyuki KAWASHIMA; Nobuyuki OOYAMA
To provide a method for operating a blast furnace with which the combustion efficiency of a solid fuel, such as pulverized coal, is improved, thereby making it possible to improve productivity and reduce CO2 emissions. Pulverized coal and oxygen are blown from an upstream lance 4 configured by a double tube, and LNG is blown from a downstream lance 6 on the downstream side in a hot air blast direction, so that oxygen to be used for combustion of the LNG is supplied from the upstream lance 4, and the pulverized coal whose temperature has been increased by the combustion of the LNG is combusted along with the supplied oxygen or oxygen in an air blast. When a direction perpendicular to the hot air blast direction is designated as 0°, and a downstream direction and an upstream direction therefrom in the hot air blast direction are designated as positive and negative, respectively, a blowing direction of the LNG from the downstream lance 6 with respect to the blast direction ranges from −30° to +45°, and a blowing position of the LNG from the downstream lance 6 with reference to a position at which the upstream lance 4 is inserted into a blast pipe 2 ranges from 160° to 200° in terms of a blast pipe circumferential direction angle.
139 CONTINUOUS HEATING FURNACE US14843195 2015-09-02 US20150377553A1 2015-12-31 Kimiyoshi SATOH; Kazuo MIYOSHI; Takahiro TANAKA
A continuous heating furnace includes one or a plurality of closed type gas heaters each having a combustion chamber, a guide section that guides an exhaust gas, a first radiation surface that extends in a direction perpendicular to a conveyance direction of a baking object, heated by combustion in the combustion chamber and heat from the guide section and transfers radiant heat to the baking object, and an exhaust hole that discharges the exhaust gas, and at least one of exhaust heat transfer unit juxtaposed with the gas heater in the conveyance direction, each having a second radiation surface that communicates with the exhaust hole and heated by the exhaust gas, and a heat transfer acceleration unit that accelerates heat transfer from the exhaust gas to the second radiation surface at one or the other end sides in a direction perpendicular to the conveyance direction of the second radiation surface.
140 HEATING FURNACE AND CONTINUOUS HEATING FURNACE US14183962 2014-02-19 US20140170582A1 2014-06-19 Kimiyoshi SATOH; Toshiyuki SUDA; Toshiro FUJIMORI; Masao AIHARA
A heating furnace includes a target space (212a) in which a burning target is disposed, and a furnace main body (212) that surrounds the target space. The heating furnace includes one or more closed gas heaters having an introduction hole configured to introduce a fuel gas into the main body, a combustion chamber in which the introduced fuel gas is combusted, a discharge section to which an exhaust gas generated by combustion is guided, a radiation surface heated by the exhaust gas flowing through the discharge section or combustion in the combustion chamber and configured to transfer radiant heat to the burning target, and an exhaust hole configured to exhaust the exhaust gas that heats the radiation surface to the outside of the main body, and disposed in the furnace main body, and an exhaust heat transfer section (an insulated pipe (222a)) in communication with the exhaust hole of the closed gas heater and to which the exhaust gas is guided. In addition, the exhaust heat transfer section is installed at any portion in the furnace main body except for a radiation space (212b) formed between the closed gas heater and the burning target disposed in the target space and configured to transfer the radiant heat to the burning target.
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