• 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:
    To prevent disruptions in downstream processes due to non-uniform flows arising from the switching operation in two interchangeable regenerator systems, both the feed of a cold fluid to the cooled regenerator and the feed of a hot fluid to the heated regenerator are interrupted, the hot fluid is then introduced into the cooled regenerator while the cold fluid is first conducted through a heat accumulator connected in parallel with the regenerators; a portion of the fluid heated in the heat accumulator is fed into the heated regenerator to purge residual hot fluid therefrom and subsequently the cold fluid is passed in its entirety through the heated regenerator. Particular application is in preventing disruption in the flow, composition and temperature of air of combustion preheated by flue gas.
    公开号:SU1324594A3
    申请号:SU823496036
    申请日:1982-09-30
    公开日:1987-07-15
    发明作者:Линде Герхард
    申请人:Линде Аг (Фирма)；
    IPC主号:
    专利说明:

    variable technology and can be used in power and ferrous metallurgy.
    The purpose of the invention is to increase the efficiency of the heated fluid by preventing it from mixing with the heating fluid.
    The drawing shows schematically a heat exchange system with which the proposed method is carried out.
    The heat exchange system contains regenerators 1 and 2 with inlet and outlet pipes 3-6 of heated fluid, connected by-pass pipe 7, as well as inlet and outlet pipes of 8, 9 and 10, 11 heating fluid. In the bypass pipeline 7 is installed heat. Akkulul torus 12.
    The supply nozzles 3 and 4 of the heated fluid are connected to the supply line 13 of the heated fluid 1
    the opening of the valves 18 and 20, and the regenerator 2 is disconnected from the
    5 lines 13 and 14 of supply and removal of heated fluid and. Connect to lines 15 and 16 of supply and removal of heating fluid by opening valves 23 and 25. In addition, through
    fO battery 12 passes a portion of the heated medium that is preheated in the regenerator 1, taken from line 14 and discharged after battery 12 through an additional element 15 in line 16 of the heating fluid. To do this, the valve 27 is closed, and the valve 26 is opened.
    20
    At. This turning on the regenerators 1 and 2 and the heat accumulator 12 cools the regenerator 1, and the heating of the regenerator 2 and the heat accumulator 12.
    After cooling, the day of regenerator 1 d (
    and sludge outlet pipes 5 and 6 are heated - 25 of the maximum heat exchange value
    my fluid is connected to the line the system is switched to heat regen
    The rator 1 and the cooling of the regenerator 2, E1l of this close the valves 18 and 20 by disconnecting the regenerator from lines 13 and 14 supplying and discharging heated Tet-: y whose medium, valve 23, disconnecting the regenerator 2 from line 15 for supplying heating fluid, and valve 26, turning off the heat accumulator 12 from. The lipovir 7 is provided with an additional patent 16 for discharging heating fluid.
    17, connecting it to the line. At the same time, by opening the valve 27,
    let the heated fluid flow through the battery 12, heat it
    in it and fed through line 14 to the customer. At the same time, a portion of the fluid heated in the battery 12 is passed through the regenerator 2 in order to flush it off from the remnants of the heating medium, for which purpose open the slide valve 21, which is provided with the discharge branch 6 of the heated fluid. Exit rga from the regenerator 2 purge 14 removal of the heated fluid to the consumer.
    The inlet pipes 8 and 9 of the heating fluid are connected to the fluid supply line 15 30, and the outlet pipes 10 and 11 of the heating fluid are connected to the heating outlet line 16. common fluid. A bypass pipe 16 for removing the heating fluid and connected to the pipeline 7 in the zone between its connection point with the inlet pipes 3 and 4 of the heated fluid and the heat accumulator 12. All pipes 3, 4, 5, 6, 8, 9, 10, 11, and 17, as well as the bypass pipeline 7, are provided with valves 18-27, respectively, the valve 27 being installed in the pipeline section 7 between its connection points with the branch pipe 17 on one side of the medium is removed through line 16 and the branch pipe 3 and 4 on the other; removal of the heating fluid.
    CQ At the end of the purge close
    The operation of the heat-vented system is carried out as follows.
    At first, the heated fluid is heated in the regenerator 1, and the regenerator 2 is heated by the heated fluid medium heated by its heating fluid, which is the medium. Dp of this regenerator 1c pa passes through the regenerator 2, using valves 22 and 24, turn off the heating in it and feed it through a sheet of lines 15 and 16 supplying and discharging glue 14 to the consumer. Then the closing fluid is connected to the latch valve 27, disconnecting the battery
    the valve 25, disconnecting the regenerator 2 from the heating fluid discharge line 16, and opening the valve 19, connecting the regenerator 2 to the line 13 of the fluid flow by opening the valves 18 and 20, and disconnecting the regenerator 2 with the help of valves 19 and 21
    lines 13 and 14 of the supply and removal of the heated fluid and. connect to lines 15 and 16 of the supply and removal of the heating fluid by opening the valves 23 and 25. In addition, through
    The battery 12 passes a portion of the heated medium that is preheated in the regenerator 1 and is withdrawn from line 14 and discharged after battery 12 through an additional pipe 17 in the heating fluid outlet line 16. To do this, the valve 27 is closed, and the valve 26 is opened.
     At the end of the purge close
    The water of the heated fluid, which passes through the regenerator 2, is heated therein and is fed through line 14 to the consumer. Then close the valve 27, disconnecting the battery
    valve 25, disconnecting the regenerator 2 from line 16 for discharging heating fluid, and opening valve 19, connecting regenerator 2 to line 13 under 12 from line 13 for supplying heated fluid and opening valve 26, connecting battery 12 to line 16 for discharging heating fluid, AT; As a result, a portion of the heated fluid heated in the generator 2 from line 14 enters the battery 12, heats it and is removed through line 16 to drain the heating fluid. After that, by opening the valves 2.2 and 24, the regenerator 1 is connected to the lines 15 and 16 of the handouts and the removal of the heating fluid, thereby turning it on in the heating mode.
    At this time, the switching time of the regenerators 1 and 2 was over. As a result of the described sequence of operations for switching regenerators 1 and 2, the consumer is continuously supplied with a heated heated medium and prevents (by blowing) the displacement of the heated medium supplied to that regenerator, which is transferred to its heating mode with the remaining heating medium in this regenerator .
    All this ensures the effectiveness of heated
    environment and allows continuous supply of the consumer with heated heated medium with the required characteristics (temperature, composition), which in a chain increases the efficiency of the thermal installation, including the heat exchange system for heating the fluid.
    20
    Editor Y. Sereda
    Compiled by Petrov Tehred N.Glushchenko
    Order 2976/39
    Tirahs 611 Subscription
    VNIIGSh of the USSR State Committee
    for inventions and discoveries 113035, Moscow, Zh-35, Raushsk nab. 4/5
    Production and Printing Enterprise, Uzhgorod, st. Design, 4.
    Proofreader A. Ilyin
    权利要求:
    Claims (2)
    [1]
    1. METHOD OF OPERATION OF A HEAT EXCHANGE SYSTEM containing regenerators with inlet and outlet pipes of a heated fluid connected by a bypass pipe, which consists in passing heating fluid through the first regenerator, and the heated fluid through the second regenerator, and then the regenerators are switched through the first pass the heated fluid, and through the second heating fluid, characterized in that, in order to increase the heating efficiency of the heated fluid by preventing it from being mixed With a heating fluid, a heat accumulator is additionally installed in the bypass pipeline and heat is supplied to it during the period of operation of the regenerators between the switchings, and during the period of their switching through it, a fluid epees is passed through it, it is heated and part is supplied to the generator, heated by a heating fluid to purge it from it.
    [2]
    2. The method according to π.1, characterized in that the heat is supplied to the battery from a part of the stream of preheated heated fluid in the regenerator.
    SU <„, 1324594 A 5
    1324594 2
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    同族专利:
    公开号 | 公开日
    ATA347082A|1987-10-15|
    AT385844B|1988-05-25|
    US4424857A|1984-01-10|
    DE3139153A1|1983-04-14|
    引用文献:
    公开号 | 申请日 | 公开日 | 申请人 | 专利标题
    DE128275C|
    AT16721B|1903-07-28|1904-06-25|Adalbert Kurzwernhart|Process and device to avoid gas losses in Siemens regenerative furnaces.|
    FR484784A|1917-03-14|1917-11-06|Albert Maurice Aubert|Device for quickly obtaining high temperatures in industrial furnaces|
    US2139861A|1935-10-05|1938-12-13|United States Steel Corp|Regenerative furnace reversing means|
    FR1037511A|1950-05-25|1953-09-17|Ruhrstahl Ag|Process for eliminating losses from reversal of gas streams in regeneration furnaces|
    US2723842A|1951-03-15|1955-11-15|Morgan Construction Co|Regenerative furnace apparatus having flue gas separators|
    DE922296C|1951-12-01|1955-01-13|Otto & Co Gmbh Dr C|Process and device for converting regenerative ovens combined in batteries with regenerator chambers divided into halves|
    US3198413A|1962-02-12|1965-08-03|Taylor Winfield Corp|Apparatus for joining metal strip|
    DE1214822B|1962-02-16|1966-04-21|Koppers Gmbh Heinrich|Control device for regenerative gas or wind heater systems|
    DE1259915B|1963-08-21|1968-02-01|Linde Ag|Method and device for heat exchange or for heat exchange and for cleaning gas mixtures in periodically switchable regenerators|
    US3627014A|1969-02-20|1971-12-14|Mitsubishi Heavy Ind Ltd|Heat-exchanger system|
    DE2019113B2|1970-04-21|1972-12-28|Kurelia Kagaku Kogyo K K , Mitsubishi, Jyukogyo K K , Tokio|GAS HEATING SYSTEM WITH TWO REGENERATIVE HEAT EXCHANGERS|
    DE2135034C3|1971-07-14|1980-01-03|Kobe Steel, Ltd., Kobe, Hyogo |Reversing heat exchanger|
    GB1478419A|1975-01-28|1977-06-29|Air Prod & Chem|Reversible heat exchanger or regenerator systems|US4476684A|1982-11-18|1984-10-16|Phillips John R|Hot bed power|
    DE3325447C2|1983-07-14|1991-10-17|Linde Ag, 6200 Wiesbaden, De|
    SE448496B|1985-10-09|1987-02-23|Sten Zeilon|DEVICE FOR DRIVING THE TWO GAS FLOW PERIODIC EXCHANGE THROUGH TWO HEATING EXCHANGE MATERIALS|
    US4793974A|1987-03-09|1988-12-27|Hebrank William H|Fume incinerator with regenerative heat recovery|
    DK161037C|1988-10-17|1991-10-28|Topsoe Haldor As|PROCEDURE AND PLANT TO CONTINUOUSLY CLEAN AN OXYGEN GAS FOR FLAMMABLE POLLUTIONS|
    SE463940B|1989-06-28|1991-02-11|Adtec Ab|GAS PURIFICATION DEVICES TO DIRECTLY CHANGE PREVENTION TO PREVENT POLLUTION GAS EMISSIONS|
    US5098286A|1989-11-30|1992-03-24|Smith Engineering Company|Regenerative thermal incinerator apparatus|
    US5026277A|1989-11-30|1991-06-25|Smith Engineering Company|Regenerative thermal incinerator apparatus|
    US5129332A|1991-07-10|1992-07-14|Richard Greco|Valve actuation mechanism for incinerator|
    US5926969A|1997-06-13|1999-07-27|Universal Dynamics, Inc.|Method and apparatus for regenerating a moist absorption medium|
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    DE102007005331A1|2007-01-29|2008-07-31|Kba-Metalprint Gmbh & Co. Kg|Heat accumulator, has two accumulator elements, where hot medium rinsing stream withdrawing from one of hot ends of one of accumulator elements enters into another hot end of another element over rinsing path in loaded condition|
    US20130078583A1|2011-09-23|2013-03-28|Yu-Po Lee|Heat Recycling System for a High-Temperature Exhaust Gas|
    CN103363802A|2012-03-29|2013-10-23|中国石油化工股份有限公司|Flame heating furnace|
    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    DE19813139153|DE3139153A1|1981-10-01|1981-10-01|"METHOD FOR SWITCHING TWO REGENERATORS"|
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