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1. 发明授权

US5236354A Power plant with efficient emission control for obtaining high turbine inlet temperature 失效
标题翻译：具有高效涡轮机入口温度的高效排放控制装置
公开(公告)号：US5236354A
公开(公告)日：1993-08-17
申请号：US672067
申请日：1991-03-18
申请人： Gerhardt O. Goldbach , John C. Haas , Frank Walton
发明人： Gerhardt O. Goldbach , John C. Haas , Frank Walton
IPC分类号： B01D53/34 , B01D53/60
CPC分类号： B01D53/60 , B01D53/343 , F23J2215/10 , F23J2215/20 , Y02E20/12 , Y02T10/16
摘要： A power plant with efficient emission control and high turbine inlet temperatures is disclosed. The power plant includes a combustor for the combustion of carbonaceous sulfur-bearing fuel. The combustion of this fuel produces a hot gas with SO.sub.x and NO.sub.x contaminants. This gas is conveyed to a refractory heat exchanger where some of the heat from the gas is transferred to a pressurized air stream. The gas is then conveyed to a fluidized bed reactor. The fluidized bed reactor includes a central chamber with a fluidized bed positioned at the base of the chamber. Heat exchangers are positioned within the fluidized bed. These heat exchangers preheat the pressurized air stream which is then conveyed to the refractory heat exchanger and later conveyed to a turbine assembly. The fluidized bed reactor also includes circulating particulate matter, such as CaO. Ammonia may also be injected into the fluidized bed reactor. When operating at a temperature of at least 1,500.degree. F., the fluidized bed reactor facilitates chemical reactions between the CaO and the SO.sub.x contaminants. The fluidized bed reactor also facilitates chemical reactions between the ammonia and NO.sub.x contaminants. These reactions significantly reduce the contaminants originally found in the hot, dirty gas.

2. 发明授权

US4519810A Circulation loop for carrying out two-stage reactions 失效
标题翻译：用于进行两级反应的循环回路
公开(公告)号：US4519810A
公开(公告)日：1985-05-28
申请号：US505529
申请日：1983-06-17
申请人： John C. Haas
发明人： John C. Haas
IPC分类号： C10J3/54
CPC分类号： C10J3/54 , C10J3/482 , C10J3/723 , C10J3/74 , C10J2300/093 , C10J2300/0956 , C10J2300/0959 , C10J2300/0976 , C10J2300/0986 , C10J2300/0993 , C10J2300/1606 , C10J2300/1807
摘要： A method of controlling the solids circulation between a downflow reactor and an entrained bed reactor is disclosed wherein at least some of the solids are transferred from the downflow reactor to a crossflow fluidized bed through a first seal leg, wherein the crossflow fluidized bed has a baffle separating the crossflow fluidized bed into two zones. Then the solids are transferred from the crossflow fluidized bed to the entrained bed reactor, and the solids are transferred from the entrained bed reactor to the downflow reactor through a second seal leg. The solids circulation rate is controlled by adjusting the rate of fluidizing gas entering the crossflow fluidized bed.
摘要翻译：公开了一种控制下流式反应器和夹带床反应器之间的固体循环的方法，其中至少一些固体从下流式反应器转移到通过第一密封支腿的交叉流动流化床，其中交叉流动床具有挡板将交叉流动床分离成两个区域。然后将固体从交叉流动床转移到夹带床反应器，并且固体通过第二密封腿从夹带床反应器转移到下流反应器。通过调节进入交叉流动床的流化气体的速率来控制固体循环速率。

3. 发明授权

US4444569A Gasification process for carbonaceous materials 失效
标题翻译：碳质材料的气化过程
公开(公告)号：US4444569A
公开(公告)日：1984-04-24
申请号：US457855
申请日：1983-01-14
申请人： John C. Haas
发明人： John C. Haas
IPC分类号： C10J3/12 , C10J3/46 , C10J3/54
CPC分类号： C10J3/54 , C10J3/12 , C10J3/466 , C10J2300/0993
摘要： A carbonaceous material, such as coal, is gasified in a vertically elongated reaction vessel having a lower portion, an upper portion, and a re-entrainment zone which is located above the upper portion. The effective diameter of the upper portion of the vessel is larger than that of the lower portion of the vessel and the re-entrainment zone. A gasification agent is passed upwardly through the vessel at a rate sufficient to entrain the coal and fluidize a heat-transfer material in the lower portion of the vessel. The gasification agent reacts with the coal to form a hot char and a gaseous product, with the necessary heat being supplied by the heat-transfer material. In this process, the heat-transfer material substantially flows downwardly in the reaction vessel, in a fluidized state or an unfluidized state through the upper portion of the vessel and in a fluidized state through the lower portion of the vessel. The coal substantially flows upwardly in the reaction vessel, in an entrained state through the lower portion of the vessel and the re-entrainment zone, and in a fluidized state through the upper portion of the vessel. An advantage of this process is that the upper portion serves to increase the residence time of the carbonaceous solids in the reaction vessel thereby increasing yields and lowering the average height of the reaction vessel, and the sensible heat is extracted from the product gas before it leaves the reactor.
摘要翻译：诸如煤的碳质材料在具有位于上部上方的下部，上部和再夹带区的垂直伸长的反应容器中气化。容器上部的有效直径大于容器下部和再夹带区的有效直径。气化剂以足以夹带煤并将热传递材料流体流入容器下部的速率向上通过容器。气化剂与煤反应形成热炭和气态产物，所需热量由传热材料供应。在该方法中，传热材料在反应容器中基本上以流化状态或非流动状态向下流过容器的上部，并以流化状态流过容器的下部。煤在反应容器中基本上向上流动，夹带状态通过容器的下部和再夹带区，并以流化状态流过容器的上部。该方法的优点是上部用于增加碳质固体在反应容器中的停留时间，从而增加反应容器的产量并降低其平均高度，并且在产物气体离开之前从产物气体中提取显热反应堆。

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