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    SOLAR THERMAL POWER PLANT
    24.
    发明公开
    SOLAR THERMAL POWER PLANT 审中-公开
    太阳能热电站

    公开(公告)号：EP2561226A2

    公开(公告)日：2013-02-27

    申请号：EP11717716.2

    申请日：2011-04-14

    申请人： Dow Corning Corporation

    发明人： DAVIES, Keith ,  BENT, David

    IPC分类号： F03G6/00 ,  F22B1/00

    CPC分类号： F03G6/00 ,  F01K13/00 ,  F01K25/10 ,  F03G6/067 ,  F22B1/006 ,  F22D1/003 ,  F22G1/06 ,  F22G1/16 ,  Y02E10/46

    摘要： There is disclosed a method of generating superheated steam for use in power generation. The method comprises: (a) preheating feed water to a temperature below its boiling point; (b) boiling the preheated feed water to produce steam; and (c) superheating the steam. The feed water is boiled by heat exchange with a heat transfer fluid which has been heated by heat collected in a first solar radiation absorption device. In addition, one or other or both of the preheating and superheating is carried out by direct heating in a further solar radiation absorption device or devices. The invention also relates to an apparatus for generating superheated steam for use in power generation. The apparatus comprises: (1)a superheated steam generating portion for generating superheated steam, comprising: (a)a preheater zone for preheating a feed water to a temperature below its boiling point; (b)a boiler zone downstream of the preheater zone for boiling the preheated feed water to produce steam; and (c)a superheater zone downstream of the boiler zone, for superheating the steam; and (2)a heat transfer fluid portion comprising a first solar radiation absorption device for heating a heat transfer fluid and being configured to transfer heat from the heated heat transfer fluid to the feed water in the boiler zone. One or other of the preheater zone and the superheater zone comprises a further solar radiation absorption device for direct heating of the feed water or the steam, or wherein each of the preheater zone and the superheater zone comprises a further solar radiation absorption device for direct heating respectively of the feed water and the steam.

    Module-based oxy-fuel boiler
    25.
    发明公开
    Module-based oxy-fuel boiler 有权
    在模块化基础上氧燃料锅炉

    公开(公告)号：EP2505792A1

    公开(公告)日：2012-10-03

    申请号：EP12174108.6

    申请日：2006-03-01

    申请人： Jupiter Oxygen Corp.

    发明人： Patrick, Brian R. ,  Ochs, Tom L. ,  Oryschyn, Danylo B. ,  Summers, Cathy A.

    IPC分类号： F01K3/24 ,  F01K7/22 ,  F22G1/16 ,  F22G7/06 ,  F23C9/00 ,  F23L7/00

    CPC分类号： F22B31/04 ,  F01K3/24 ,  F01K7/22 ,  F22G1/16 ,  F22G3/00 ,  F23C9/00 ,  F23L7/007 ,  Y02E20/344

    摘要： A module based oxy-fuel boiler system comprising a first boiler (112) configured as a main boiler and a second boiler (216) configured as a reheat boiler, said first boiler including: plurality of first boiler tubes (T) for carrying water, the tubes forming at least one water wall,
    a feedwater inlet line (230) in flow communication with said plurality of first boiler tubes (T), said feedwater inlet line (230) configured to be connected to an external source of water,
    a steam outlet line (246) in flow communication with said plurality of first boiler tubes and configured to be connected to a first turbine (238), said turbine (238) having a steam outlet that is configured to be coupled to a reheat line (248) of said second boiler (216),
    the first boiler (212) configured to substantially prevent the introduction of air,
    a first boiler oxygen supply (218) for supplying oxygen having a purity of greater than 21 percent;
    a first boiler carbon based fuel supply (220) for supplying a carbon based fuel;
    at least one first boiler oxy-fuel burner system (222) coupled to said first boiler oxygen supply (218) and said first boiler carbon based supply (220), the first boiler oxy-fuel burner system (222) configured to feed the oxygen and the carbon based fuel into the first boiler (212) in a near stoichiometric proportion to one another to limit an excess of either the oxygen or the carbon-based fuel to a predetermined tolerance,
    a first boiler flue gas exit line (213) for discharging exhaust gas generated as a result of the combustion in said first boiler (212),
    wherein the first boiler tubes (T) are configured for direct, radiant energy exposure for energy transfer to the water to produce steam;
    a second boiler (216) having a a reheat inlet line (248) in flow communication with the steam outlet of said turbine (238);
    a reheat steam outlet line (250) in flow communication with a second turbine (240),
    a second boiler flue gas exit line (217) for discharging exhaust gas generated as a result of the combustion in said second boiler (216), wherein the second boiler(216) is configured to carry out a different energy transfer function than the first boiler (212) and is configured to substantially prevent the introduction of air;
    a second boiler supply (218) for supplying oxygen having a purity of greater then 21 percent;
    a second boiler carbon based fuel supply (20, 120) for supplying a carbon based fuel;
    at least one second boiler oxy-fuel burner system(226), the second boiler oxy-fuel burner system (226) configured to feed the oxygen and the carbon based fuel into the second boiler (216) in a near stoichiometric proportion to one another to limit an excess of either the oxygen or the carbon based fuel to a predetermined tolerance.

    HIGH EFFICIENCY WASTE TO ENERGY POWER PLANTS COMBINING MUNICIPAL SOLID WASTE AND NATURAL GAS
    26.
    发明公开
    HIGH EFFICIENCY WASTE TO ENERGY POWER PLANTS COMBINING MUNICIPAL SOLID WASTE AND NATURAL GAS 审中-公开
    HOCHLEISTUNGS-WTE-KRAFTWERKE（WTE-WASTE TO ENERGY）UNTER KOMBINATION VON FESTEMHAUSMÜLLUND ERDGAS

    公开(公告)号：EP2401478A1

    公开(公告)日：2012-01-04

    申请号：EP08878195.0

    申请日：2008-11-24

    申请人： Ribeiro, Sergio Vieira Guerreiro

    发明人： Ribeiro, Sergio Vieira Guerreiro

    IPC分类号： F01K3/24 ,  F01K23/10 ,  F22G1/16

    CPC分类号： F01K7/22 ,  F01K13/00 ,  F22B1/1807 ,  F22B1/1861 ,  F22D1/36 ,  F22G1/16 ,  Y02E20/12 ,  Y02E20/16 ,  Y02E20/363

    摘要： Corrosion is avoided by using an external superheater heated by the clean gas exhaust coming from the internal combustion machine (ICM) mixed with pure air, with duct firing to adjust the steam superheating temperature, in the same way the existing natural gas/waste power plant do. The difference in the proposed patent is that the ICM is chosen not to match the steam amount produced in the waste boiler, which is superheated to a corrosion safe temperature say 400 C or less, but just to provide the plant own power consumption. We need to increase this ICM exhaust flow with pure air and use duct firing (11,12) to raise the gas mixture temperature, say between 600 C and 700 C, high enough to superheat the steam in the external superheater (3) to approximately 500 C. If we use pure air at ambient temperature, the amount of natural gas in the duct burners (11,12) will be very high decreasing the natural gas efficiency. To reduce the natural gas consumption in the duct burner (11,12) we use the hot gas leaving the external superheater (3), around 420 C, to preheat the ambient air to say 390 C, in a air/gas heat exchanger (13), before it is mixed with the ICM exhaust, increasing the mixture temperature to a value close to 400 C, reducing drastically the natural gas consumption in the duct firing (11,12).

    摘要翻译： 通过使用由与纯空气混合的内燃机（ICM）的清洁气体排气加热的外部过热器，通过管道燃烧来调节蒸汽过热温度，以与现有天然气/废物发电厂相同的方式避免腐蚀 做。 提出的专利的不同之处在于，ICM被选择为不匹配在废锅炉中产生的蒸汽量，其过热到400℃或更低的腐蚀安全温度，而仅仅是为了提供设备自身的功率消耗。 我们需要用纯净空气和使用风管（11,12）来增加这个ICM排气流量，以提高气体混合物的温度，例如在600摄氏度到700摄氏度之间，足够高以使外部过热器（3）中的蒸汽过热至约 500℃。如果在环境温度下使用纯净空气，管道燃烧器（11,12）中的天然气量将非常高，从而降低了天然气的效率。 为了减少管道燃烧器（11,12）中的天然气消耗，我们使用离开外部过热器（3）的大约420℃的热气体将空气/气体热交换器（ 13），在与ICM排气混合之前，将混合物温度提高到接近400℃，大大降低了管道燃烧中天然气的消耗（11,12）。

    REHEAT BOILER
    27.
    发明公开
    REHEAT BOILER 有权
    WIEDERERWÄRMUNGSKESSEL

    公开(公告)号：EP2325560A1

    公开(公告)日：2011-05-25

    申请号：EP09814438.9

    申请日：2009-08-26

    申请人： Mitsubishi Heavy Industries, Ltd.

    发明人： IMADA, Junji ,  UCHIDA, Isao ,  SATO, Syuji ,  FUKUDA, Hideo

    IPC分类号： F22B37/40 ,  F22G1/04 ,  F22G1/16

    CPC分类号： F22B37/40 ,  F22G1/04 ,  F22G1/16

    摘要： Provided is a reheat boiler in which the imbalance in temperature distribution of the temperature of the combustion gas at the outlet of a reheat furnace is reduced by changing the gas flow pattern in the reheat burner. A reheat boiler (10A) includes a main boiler (106) configured such that main combustion gas generated in combustion in a burner (101) flows from a furnace (102) through a superheater (104) and evaporator tubes (105), a reheat furnace (108) that is disposed on the downstream of the evaporator tubes (105) and produces reheat combustion gas by combustion in a reheat burner (107), and a reheater (109) disposed above the reheat furnace (108). A closing plate (130), serving as a drift preventing portion, is provided at a reheat furnace outlet (120) that connects the reheat furnace (108) and the reheater (109) to form a flow path for the combustion gas and the reheat combustion gas so as to narrow the cross-sectional area of the flow path for the combustion gas.

    摘要翻译： 提供了一种再热锅炉，其中通过改变再热燃烧器中的气体流动模式来减少再热炉出口处的燃烧气体的温度分布的不平衡。 再热锅炉（10A）包括主锅炉（106），其构造成使得在燃烧器（101）中燃烧产生的主燃烧气体从炉（102）流过过热器（104）和蒸发器管（105），再热 设置在蒸发器管（105）的下游并通过在再热燃烧器（107）中燃烧产生再热燃烧气体的炉（108）和设置在再热炉（108）上方的再热器（109）。 在连接再热炉（108）和再热器（109）的再热炉出口（120）处设置有用作防漂移部分的封闭板（130），以形成用于燃烧气体和再热的流路 燃烧气体，以便缩小用于燃烧气体的流路的横截面积。

    Heat pump system, operation procedure therefor and evaporator system
    28.
    发明公开
    Heat pump system, operation procedure therefor and evaporator system 审中-公开
    Wärmepumpensystem，entsprechendes Betriebsverfahren und Verdampfersystem

    公开(公告)号：EP2136039A2

    公开(公告)日：2009-12-23

    申请号：EP08015260.6

    申请日：2008-08-29

    申请人： Hitachi Ltd.

    发明人： Kishibe, Tadaharu ,  Nakano, Susumu ,  Shibata, Takanori

    IPC分类号： F01K17/00

    CPC分类号： F25B30/02 ,  F01K17/005 ,  F22G1/16 ,  Y10S203/04

    摘要： In a heat pump system including a water purifier (1) and an evaporator (2) for evaporating feed-water (10) to produce steam (12), water (11) used for spray cooling is effectively used and productivity of purified water used for the spray cooling is increased.
    Discharged water (21) from the water purifier (1) is supplied to the evaporator (2) when water used for spray cooling is produced by use of the water purifier (1). Otherwise, drain (22) of the evaporator (2) having higher temperature is supplied to the water purifier (1) by using such a fact that in a reverse osmosis membrane type water purifier (1), the higher the temperature of feed-water (10) is, the higher the purified water productivity becomes.

    摘要翻译： 在包括用于蒸发给水（10）以产生蒸汽（12）的净水器（1）和蒸发器（2）的热泵系统中，有效地使用用于喷雾冷却的水（11），并且使用纯化水的生产率 为喷雾冷却增加。 当通过使用净水器（1）产生用于喷雾冷却的水时，将来自净水器（1）的排出的水（21）供应到蒸发器（2）。 否则，通过使用在反渗透膜型净水器（1）中的这样的事实，将具有较高温度的蒸发器（2）的排水口（22）供给到净水器（1）中，供水温度越高 （10）中，净化水的生产率越高。