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    • 2. 发明授权
    • Heat recovery system and power generation system
    • 热回收系统和发电系统
    • US06301896B1
    • 2001-10-16
    • US09379903
    • 1999-08-24
    • Norihisa MiyoshiShosaku FujinamiTetsuhisa HiroseMasaaki IrieKazuo TakanoTakahiro Oshita
    • Norihisa MiyoshiShosaku FujinamiTetsuhisa HiroseMasaaki IrieKazuo TakanoTakahiro Oshita
    • F01K100
    • F23G5/006F01K23/067F22B31/045F23G5/027F23G5/46F23G5/48F23G2201/303F23G2201/304F23G2201/40F23G2201/70F23G2202/103F23G2202/20F23G2203/30F23J15/025F23J2215/30F23J2217/104F23J2219/10Y02E20/12Y02E20/16Y02E20/18
    • In an improved system for recovering heat from a combustion gas produced by burning wastes, the combustion gas or combustible gas produced by partial burning of the wastes subjected to dust filtration in a temperature range of 450-650° C. at a filtration velocity of 1-5 cm/sec under a pressure of from −5 kPa (gage) to 5 MPa before heat recovery is effected. The dust filtration is preferably performed using a filter medium which may or may not support a denitration catalyst. Heat recovery is preferably effected using a steam superheater. The dust-free gas may partly or wholly be reburnt with or without an auxiliary fuel to a sufficiently high temperature to permit heat recovery. The combustion furnace may be a gasifying furnace which, in turn, may be combined with a melting furnace. If desired, the reburning to a higher temperature may be performed under pressure and the obtained hot combustion gas is supplied to a gas turbine to generate electricity, followed by introduction of the exhaust gas from the gas turbine into a steam superheater for further heat recovery. The system can raise the temperature of superheated steam to a sufficient level to enhance the efficiency of power generation without possibility of corrosion of heat transfer pipes by the combustion gas or combustible gas.
    • 在用于从燃烧废物产生的燃烧气体中回收热量的改进系统中,通过在过滤速度为1的450-650℃的温度范围内进行灰尘过滤的部分燃烧部分燃烧产生的燃烧气体或可燃气体 -5厘米/秒,压力为-5千帕(表压)至5MPa。 灰尘过滤优选使用可以或可以不支持脱硝催化剂的过滤介质进行。 热回收优选使用蒸汽过热器进行。 无尘气体可以部分或全部地被反燃,有或没有辅助燃料到足够高的温度以允许热回收。 燃烧炉可以是气化炉,其又可以与熔炉组合。 如果需要,可以在压力下进行再燃烧到更高的温度,并且将获得的热燃烧气体供应到燃气轮机以产生电力,然后将来自燃气轮机的废气引入蒸汽过热器中以进一步热回收。 该系统可以将过热蒸汽的温度升高到足够的水平,以提高发电效率,而不会由燃烧气体或可燃气体导致传热管的腐蚀。
    • 5. 发明授权
    • Economizer system
    • 节能器系统
    • US5787844A
    • 1998-08-04
    • US609041
    • 1996-02-29
    • Raimo Paju
    • Raimo Paju
    • F22B31/04F22D1/04F22D1/28F22G1/04
    • F22D1/04F22B31/045Y02E20/12
    • An otherwise conventional recovery boiler for burning black liquor (e.g. with a consistency of between about 70-90%) requires less capital investment and takes up less space by constructing the economizers in a particular manner. At least first and second economizers are provided for preheating feed water utilizing flue gas from combustion of the black liquor. The economizers are positioned substantially adjacent each other and connected in such a way that flue gas leaving the first economizer passes substantially directly (i.e. without going through a conventional accessory passage) into the second economizer. The economizer inlets and outlets are substantially at the same level as the adjacent economizer outlets and inlets, or vertically spaced less than about one-third the length of the previous economizer. A boiler bank may be connected between the superheater section of the recovery boiler and the first economizer, and any number of economizers can be utilized. The flue gas flowing through one economizer are turned after exiting so that it flows in a substantially opposite direction while passing through the adjacent economizer.
    • 用于燃烧黑液(例如,约70-90%的稠度)的另外常规的回收锅炉需要较少的资本投资,并且通过以特定方式构造节能器而占用更少的空间。 提供至少第一和第二节能器用于利用来自黑液燃烧的烟道气预热给水。 经济器基本上彼此相邻地定位并且以使得离开第一节能器的烟道气基本上直接(即,不经过常规附件通道)进入第二节能器的方式连接。 节能器入口和出口基本上处于与相邻的经济器出口和入口相同的水平面,或者垂直间隔小于前一个节能器的长度的三分之一。 锅炉组可以连接在回收锅炉的过热器部分和第一节能器之间,并且可以使用任何数量的节能器。 流经一个节能器的烟道气在离开之后转动,使得其在通过相邻的节能器的同时沿着基本相反的方向流动。
    • 6. 发明授权
    • Steam generator
    • 蒸汽发生器
    • US5568793A
    • 1996-10-29
    • US370785
    • 1995-01-10
    • Georg Ziegler
    • Georg Ziegler
    • F22B1/18F22B31/04F22G3/00
    • F22B31/045Y02E20/12
    • In a steam generator having a convective part arranged downstream of the furnace chamber and essentially consisting of final superheater (1), pre-superheater, evaporator and economizer connected in series on the flue-gas side, a further contact heat exchanger (5) having a plurality of tube banks (10) is arranged upstream of the final superheater (1). This contact heat exchanger (5) is connected to the steam drum (6) in such a way that it can be operated as both an evaporator and a superheater. The working medium to be heated flows in parallel from the bottom to the top through the tube banks (10), as a rule arranged vertically or inclined, of the contact heat exchanger in the evaporator circuit and flows in series through said tube banks (10) of the heat exchanger in the superheater circuit.
    • 在蒸汽发生器中,具有布置在炉室下游的对流部分,并且基本上由最终过热器(1),串联在烟道气侧的预过热器,蒸发器和节能器组成的另外的接触热交换器(5) 多个管组(10)布置在最终过热器(1)的上游。 该接触式热交换器(5)以蒸发器和过热器的方式连接到蒸汽鼓(6)。 待加热的工作介质通过管排(10)从底部到顶部平行流动,其规则布置为在蒸发器回路中垂直或倾斜的接触式热交换器,并通过所述管组(10 )过热器电路中的热交换器。