发明公开
EP1876390A1 Method of producing steam in a gas tube steam boiler and gas tube steam boiler for implementing said method
审中-公开
用于蒸汽的产生在气体管道蒸汽锅炉和气体管道蒸汽锅炉这种方法的应用的方法
- 专利标题: Method of producing steam in a gas tube steam boiler and gas tube steam boiler for implementing said method
- 专利标题(中): 用于蒸汽的产生在气体管道蒸汽锅炉和气体管道蒸汽锅炉这种方法的应用的方法
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申请号: EP06388049.6申请日: 2006-07-05
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公开(公告)号: EP1876390A1公开(公告)日: 2008-01-09
- 发明人: Nielsen, Bodil Irene Mosekær , Pedersen, Thomas Paarup
- 申请人: Aalborg Industries A/S
- 申请人地址: Gasvæksvej 24 9100 Aalborg DK
- 专利权人: Aalborg Industries A/S
- 当前专利权人: Aalborg Industries A/S
- 当前专利权人地址: Gasvæksvej 24 9100 Aalborg DK
- 代理机构: Orsnes, Henrik Egede
- 主分类号: F22B1/18
- IPC分类号: F22B1/18 ; F22G3/00 ; F28D1/02 ; F28F9/22 ; F28F13/08 ; F22B9/04
摘要:
A gas tube steam boiler comprising a heat exchange compartment (2) filled with water forming a water surface (2A), a steam head space (8) above the water surface and delimited by a cylindrical wall (1) with a substantially vertical axis (10) and a top plate (4), a steam outlet (6) communicating with the steam head space (8), gas tubes (3) extending through the heat exchange compartment (2) and the steam head space (8), means for supplying heated gas to the gas tubes (3) for generating a flow of steam from said water surface (2A) by heat exchange between the gas tubes (3) and the water, and a steam flow conduit (7',7") arranged in the steam head space (8) for conducting the flow of steam from the water surface (2A) to the steam outlet (6), at least one of the gas tubes (3) extending transversely through the conduit such that the flow of steam flows in a direction transverse, preferably generally orthogonal, to the gas tubes (3), the configuration of the conduit being such that more than half, preferably substantially all, of the steam in the flow is constrained to flow along a flow path which when projected on a horizontal surface has a length at least equal to the shortest distance between a first point of the wall (1) and a second point of the wall (1) horizontally opposite the first point, said distance, in the case the wall (1) is circular cylindrical, being the diameter D of the circular cylindrical wall.
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