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    • 1. 发明申请
    • SYSTEM AND METHOD FOR PROVIDING SUPERCRITICAL STEAM
    • 提供超临界蒸汽的系统和方法
    • WO2018083082A1
    • 2018-05-11
    • PCT/EP2017/077866
    • 2017-10-31
    • GENERAL ELECTRIC TECHNOLOGY GMBH
    • ZHANG, WeiLEVASSEUR, ArmandNIASS, TidjaniYOUNES, MouradJUKKOLA, GlenWILHELM, BrucePHILO, DarylMAIDENFORD, Timothy
    • F01K23/10F22B1/18F22B33/00
    • A system for providing supercritical steam including a first boiler (12) that generates steam via combusting a first fuel (52), and a second boiler (14) fluidly connected to the first boiler via a conduit (28) which heats the generated steam to supercritical steam temperatures via combusting a second fuel (60), wherein the term "supercritical steam" designates steam which is above a critical temperature with respect to corrosion. A first temperature of the conduit may be below a critical corrosion temperature and a second temperature of the conduit is greater than or equal to the critical corrosion temperature. A combined carbon emission rate of the first boiler and the second boiler may be less than a combined carbon emission rate of generating and heating the steam to supercritical steam temperatures using boilers that only combust the first fuel. The first boiler may be fluidly connected to a heat exchanger that heats the generated steam to a supercritical steam temperature via a flue gas produced by a gas turbine. (Figure 1)
    • 一种用于提供超临界蒸汽的系统,该系统包括通过燃烧第一燃料(52)产生蒸汽的第一锅炉(12)以及经由导管流体连接至第一锅炉的第二锅炉(14) 28),其通过燃烧第二燃料(60)将产生的蒸汽加热至超临界蒸汽温度,其中术语“超临界蒸汽” 表示高于关于腐蚀的临界温度的蒸汽。 导管的第一温度可以低于临界腐蚀温度并且导管的第二温度高于或等于临界腐蚀温度。 第一锅炉和第二锅炉的组合碳排放速率可小于使用仅燃烧第一燃料的锅炉产生蒸汽并将其加热至超临界蒸汽温度的组合碳排放速率。 第一锅炉可以流体连接到热交换器,该热交换器通过由燃气轮机产生的烟道气将生成的蒸汽加热到超临界蒸汽温度。 (图1)
    • 3. 发明申请
    • APPARATUS AND METHOD OF CONTROLLING THE THERMAL PERFORMANCE OF AN OXYGEN-FIRED BOILER
    • 控制氧燃烧锅炉的热性能的装置和方法
    • WO2018083043A1
    • 2018-05-11
    • PCT/EP2017/077677
    • 2017-10-27
    • GENERAL ELECTRIC TECHNOLOGY GMBH
    • LEVASSEUR, ArmandZHANG, WeiEDBERG, Carl
    • F23C5/08F23C5/32F23C9/08F23L7/00F23L9/00
    • A method of controlling the operation of an oxy-fired boiler includes combusting a fuel that comprises oil heavy residues in a boiler, the oil heavy residues including hydrocarbon molecules having a number average molecular weight from approximately 200 to approximately 3000 grams per mole, discharging flue gas from the boiler, recycling a portion of the flue gas to the boiler, combining a first oxidant stream with the recycled flue gas to form a combined stream, splitting the combined stream into a plurality of independent split streams, introducing each independent split stream at a different elevation of the boiler, and controlling independently a parameter of each of the independent split streams to adjust the heat release at each respective elevation of the boiler to vary the heat release profile of the boiler by adding a second oxidant stream to each respective independent split stream to form respective independent oxygen enriched split streams.
    • 控制氧燃烧锅炉的操作的方法包括在锅炉中燃烧包含油重残余物的燃料,所述油重残余物包括数均分子量为约200至约300的烃分子 大约3000克/摩尔,从锅炉排放烟道气,将一部分烟道气再循环至锅炉,将第一氧化剂流与再循环烟道气合并以形成合并流,将合并流分成多个独立的分流 在锅炉的不同高度处引入每个独立的分流,并且独立地控制每个独立分流的参数以调节锅炉每个相应高度处的热量释放,以通过增加 将第二氧化剂流送至各个独立的分流,以形成各自独立的富氧分流。