• 专利附录
  • 专利说明
  • 权利要求
  • 类似技术
  • 同族专利
  • 引用文献
  • 法律状态
  • 优先权
    • 专利摘要:
    A process and regenerative heat exchange apparatus for heating gases, it being the case that, in turn, the heat carrier, preferably a bed of heat-carrying bodies, is firstly heated and subsequently this energy, stored by the heat carriers, is used to heat cold gases. Located between two gratings (2, 4) arranged coaxially and equidistantly from the regenerative heat exchanger apparatus is a loose bed of heat carriers (6), and this bed is traversed in the heating phase of the regenerative heat exchange apparatus by the hot gas from inside to outside, and vice versa in the gas heating phase by the cold gas from outside to inside. …<IMAGE>…
    公开号:SU1739857A3
    申请号:SU894742577
    申请日:1989-12-08
    公开日:1992-06-07
    发明作者:Фасбиндер Ханс-Георг
    申请人:Клекнер Кра Патент Гмбх (Фирма)；
    IPC主号:
    专利说明:

    The invention relates to devices for heating gases by alternately first heating the heat carriers, and then using this energy stored in heat carriers for heating cold gases, in particular, can be used for the recovery in the melt, iron ore, in electric furnaces and blast furnaces.
    The aim of the invention is to reduce energy losses.
    The drawing shows schematically a regenerator, a slit.
    The regenerator contains an outer steel lining 1 of approximately spherical shape. Although the external shapes of the regenerator are not important and can be arbitrary, certain shapes, such as vertical cylinders, balls or double truncated cones one above the other with a cylindrical section between them or without them, are
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    preferred mainly for reasons of ease of manufacture.
    The steel sheath 1 comprises a cylindrical outer lattice 2 with round and / or slit-like openings. Between this grid 2 and the outer steel shell 1 there is an annular gas collector chamber
    3d cold gas.
    The internal grid 4 is made of refractory bricks with suitable gas passages. The coaxial arrangement of the two grids 2 and 4 defines a cavity 5 between them with the same distance between the two grids along the entire circumference. The cavity 5 is of circular cross section; it accommodates heat carriers 6, for example, tablets made of ceramic material. In the center of the regenerator there is a chamber 7 of hot gas of circular cross section. At the lower end of chamber 7 there are hot kiln gases generated in the furnace 8, they flow during the heating phase of the regenerator. The furnace 8 is available through the lid of the vessel 9.
    Hot combustion gases flow from chamber 7 of hot gas through the grate.
    4 and the layer of coolants 6 into the chamber 5, then through the grid 2 - into the collector chamber 3 of the gas at approximately normal temperature. They leave the collector chamber, and therefore from the regenerator through the nozzle 10. During the gas heating phase, the compressed gas flows through the nozzle 11 into the collector chamber 3, then through the grid 2 and the layer of heat carriers 6 into the chamber 5, through the internal grid 4 into 7 hot gas chamber. On its way, the gases are directed from hot coolants.
    6 and exit from the regenerator through nozzle 12С
    Holes 13 and 14, adapted for closing with flanges, are also visible on the regenerator vessel. Through fittings 14, heat carriers 6 can be removed from chamber 5 and at the same time replenished through openings 13 during operation, maintenance or repair. Thus it is possible to replace all the coolants 6 in the chamber 5 intermittently or
    continuously,
    Under various conditions of industrial use, materials for gratings and heat transfer media can be matched to temperature requirements. / The form of the regenerator can also be
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    changed according to use, but the principle of radial flow through the coolant layer must be maintained
    The invention has several advantages compared with the known solutions from a thermal point of view, as well as in terms of the design of such systems. In particular, the heat loss is reduced due to a clearly lower heat flux to the outer wall of the regenerator, since the high temperature region is located in center, and the outer wall is in contact only with cold gas. This increases thermal efficiency and saves the amount of steel and refractory lining due to its smaller size and lower temperature loads compared to the known bubbled systems having the same heating capacity, i.e. flow rate, the gas temperature and gas
    When the gases are heated in the regenerator, uniform temperatures of the hot gas are reached, so that appropriate control of the temperature is not necessary in many applications. For example, stumps using a blast furnace gas can be expected to range from 20 to 40 ° C at a blowing temperature of 1200 ° C and switching time to the gas heating phase after 30 minutes.
    A relatively small temperature difference between heat carriers and gases is required. This applies both to the heating of the coolants themselves and to the final temperature of the gases to be heated, for example air. Thus, for heating the heat transfer fluids, only flue gases with a flame temperature slightly higher than the required temperature of the heated gases are required. For example, blast furnace gas from the blast furnace or only a slightly enriched blast furnace gas may be used to heat the air for blast furnace air.
    When the proposed method was used for preheating blowing up to 1150 ° C, the heat transfer media was heated in a regenerator using furnace gas, which had a calorific value of about 750 kcal / nm3 with a resulting flame temperature of about 1200 ° C. Almost the same heating temperatures can be achieved with the specified parameters at
    heating other gases, such as nitrogen, argon, air enriched with oxygen, oxygen, and combustion gases.
    Coolants, like a cowper packing, consist of free bodies with approximately the same grain size. Due to their layer between equidistant lattices, the thickness of the layer is constant in the direction of gas flow. In the proposed regenerator, heat transfer media cannot move under the action of gases, so there is no danger of gas breakthrough if, for example, a local excess occurs over the fluidization point.
    In the proposed regenerator, the free volume between the coolants and also in the hot gas chamber and in the collector chamber is relatively small so that there are only small pelvic losses when switching from the heating phase of the regenerator to the heating phase of the gases. Fluids can be replaced in the regenerator during its operation. Corresponding fittings or flanges on the top and bottom of the layer of coolants provide replenishment of coolants on one side and removing them on the other side.
    The regenerator often has only a uniform layer of one kind of heat transfer media, located between the inner and outer gratings. However, it is possible to use more than two coaxial lattices, thus forming several coaxial annular chambers. Between the two adjacent grids preferably use the same coolant. However, you can use different layers of coolants in each annular chamber. For example, ceramic beads that are resistant to high temperatures, such as corundum, can be used between two grids on the hot inside of the regenerator, and less expensive heat transfer fluids, such as mullite or / and chamotte, are used on the cooler side on the outside. An entire layer can be composed of two or more layers, not only for reasons of cost savings, but also for technical, especially thermal considerations. Variations are possible both in materials and in the sizes and shapes of heat carriers.
    The grates of the proposed regenerator can be made of various materials.
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    fishing For example, the inner grid on the hot side can be made of refractory material; such as refractory bricks with suitable gas passages, and an external lattice on the cold side of metal, such as steel, refractory steel or cast iron. If other gratings are used between the inner and outer gratings, the materials must also be selected in accordance with the temperature loads. Ceramic or metallic materials are mainly used.
    An essential feature of the invention is to provide a layer of coolants of even thickness and the movement of gases through it in the radial direction. This feature is retained if the layer of coolants is divided into several layers. Ceramic materials of various qualities, such as corundum, mullite, chamotte, magnesia, chromium oxide, zirconium oxide, silicon carbide, and any mixtures thereof, have shown themselves suitable materials for heat-transfer agents. Heat transfer materials should be selected in accordance with the heat load. The form of heat-transfer agents may be arbitrary, but some forms are preferred due to their economical and fast production, for example, execution in the form of tablets or briquettes, especially for ceramic materials. Geometrically oval or spherical shapes. However, you can use layers of any crushed and crushed structures.
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    权利要求:
    Claims (6)
    [1]
    1.Generator for heating gases, comprising a housing with a bulk nozzle made of ceramic material, a perforated partition, a burner, supply and discharge pipes with regulating valves, characterized in that it is equipped with an additional grate in order to reduce heat losses the grids are cylindrical, mounted coaxially with each other and the regenerator case and form with it the central and peripheral chambers, and the filling nozzle is located between the grids,
    [2]
    2. The regenerator according to claim 1, characterized in that the burner is located in the center of the lower part of the regenerator, and the internal grid is made of refractory material, for example, of refractory perforated bricks
    [3]
    3. The regenerator according to any one of the following: the external grid is made of metal, for example, steel.
    [4]
     4. The regenerator according to any one of the following: the filling of the packing is made of briquetted
    sintered ceramic materials of oval or spherical shape.
    [5]
    5. The generator according to claim 1, characterized in that it is provided with additional gratings of refractory material and metal, between which the bulk of the packing is located.
    [6]
    6. The regenerator is characterized in that the nozzle of each chamber is made of different materials.
    / J
    Compiled by L.Pannikova Editor A.Motyl Tekhred L.Oleksin Proofreader L.Patay
    Order 2013
    Circulation
    VNIIPI State Committee for Inventions and Discoveries at the State Committee on Science and Technology of the USSR 113035, Moscow, Zh-35, Raushsk nab. 4/5
    / J
    9 M
    Subscription
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    同族专利:
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    引用文献:
    公开号 | 申请日 | 公开日 | 申请人 | 专利标题
    NL298230A|1900-01-01|
    US2272108A|1940-01-19|1942-02-03|Research Corp|Regenerative stove|
    US3378244A|1966-01-12|1968-04-16|Dresser Ind|Pebble heat exchanger|
    AT327363B|1974-02-25|1976-01-26|Boehler & Co Ag Geb|REGENERATIVE HEAT EXCHANGER FOR GASES|
    DE2751621C2|1977-11-18|1986-08-21|Linde Ag, 6200 Wiesbaden|Hot blast stove|
    FR2473695B1|1980-01-09|1985-02-22|Pechiney Aluminium|
    JPS56130528A|1980-03-18|1981-10-13|Kikuko Kobayashi|Heat accumulating device|
    US4604051A|1984-08-16|1986-08-05|Gas Research Institute|Regenerative burner|
    GB2170584B|1985-02-04|1988-02-17|British Gas Plc|Regenerative heating systems|
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    DE4236619C2|1992-10-29|1996-11-28|Air Liquide|Process and regenerator for heating gases|
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    US6631754B1|2000-03-14|2003-10-14|L'air Liquide Societe Anonyme A Directoire Et Conseil De Surveillance Pour L'etude Et L'exploitation Des Procedes Georges Claude|Regenerative heat exchanger and method for heating a gas therewith|
    KR100463550B1|2003-01-14|2004-12-29|엘지전자 주식회사|cooling and heating system|
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    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    DE3841708A|DE3841708C1|1988-12-10|1988-12-10|
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