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    • 2. 发明授权
    • Exhaust gas heat recovery boiler
    • 废气热回收锅炉
    • US4664067A
    • 1987-05-12
    • US829815
    • 1986-02-14
    • Hisao HanedaMasamichi KashiwazakiToshiki Motai
    • Hisao HanedaMasamichi KashiwazakiToshiki Motai
    • F22B1/18F22G7/12F22G7/14F22D1/00
    • F22G7/14F22B1/1815F22B1/1869
    • An exhaust gas boiler including a plurality of superheaters and reheaters disposed separately in a side-by-side relationship with each other in the upstream of exhaust gas flow and in a plane across the complete of said exhaust gas boiler, which comprises in combination a plurality of superheater means and reheater means separated into primary and secondary groups respectively in such a manner that the secondary superheater means and secondary reheater means are disposed side by side with each other, the primary reheater means being in the downstream of the secondary superheater means and the primary superheater means in the downstream of the secondary reheater means, the primary superheater means and the secondary superheater means being connected with each other, the primary reheater means and the secondary reheater means being connected with each other, respectively, and that there are provided a plurality of pass partition means between the superheater means and the reheater means.
    • 一种废气锅炉,包括多个过热器和再热器,它们在废气流的上游和穿过所述废气锅炉的整个的平面中彼此并排地分开设置,其包括多个 过热器装置和再热器装置分别以分开的方式分开成二级过热器装置和次级再热器装置并排配置成一级和二级组,一级再热器装置位于次级过热器装置的下游, 初级过热器装置在次级再热器装置的下游,初级过热器装置和次级过热器装置彼此连接,主再热器装置和次级再热器装置分别相互连接,并且设置有一个 多个通过分隔装置在过热器装置和再热装置之间。
    • 3. 发明授权
    • Reheat type exhaust gas boiler
    • 再热式排气锅炉
    • US4944252A
    • 1990-07-31
    • US412323
    • 1989-09-25
    • Toshiki MotaiMasamichi Kashiwazaki
    • Toshiki MotaiMasamichi Kashiwazaki
    • F22B1/18F22B37/40F22G7/14
    • F22B1/1815F22G7/14
    • A known reheat type exhaust gas boiler of the type having superheaters and reheaters disposed in parallel in the most upstream portion of an exhaust gas boiler main body, is improved by simplifying the structure and providing more effective recovery of heat from the exhaust gas. The superheaters and reheaters are divided into a plurality of stages. A high-temperature side superheater and a high-temperature side reheater are disposed in parallel in the most upstream portion of the gas flow. A low-temperature side reheater is disposed on the downstream side of the high-temperature side superheater, while a low-temperature side superheater is disposed on the downstream side of the high-temperature side reheater. The high-temperature side superheater and the high-temperature side reheater are formed so as to have an identical heat transfer tube outer diameter, an identical tube pitch in the transverse direction of the main body, an identical tube pitch in the longitudinal direction and an identical number of tube rows in the longitudinal direction. Likewise, the low-temperature side reheater and the low-temperature side superheater are formed so as to have an identical heater transfer tube outer diameter, an identical tube pitch in the transverse direction of the main body, an identical tube pitch in the longitudinal direction and an identical number of tube rows in the longitudinal direction.
    • 通过简化结构并提供更有效地从废气中回收热量,已经提高了在排气锅炉主体的最上游部分平行布置的具有过热器和再热器的类型的再热式排气锅炉。 过热器和再热器分为多个阶段。 高温侧过热器和高温侧再热器平行配置在气流的最上游部分。 低温侧再热器设置在高温侧过热器的下游侧,而低温侧过热器设置在高温侧再热器的下游侧。 高温侧过热器和高温侧再热器形成为具有相同的传热管外径,在主体的横向方向上具有相同的管间距,在纵向上具有相同的管间距, 相同数量的管排在纵向上。 同样地,低温侧再热器和低温侧过热器形成为具有相同的加热器传送管外径,在主体的横向上具有相同的管间距,在纵向上具有相同的管间距 并且在纵向上具有相同数量的管排。