Method and apparatus for the superheating of steam
AssigneeSiemens Aktiengesellschaft
InventorJohann Meseth
Life of this patent
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Abstract
An apparatus and a method for the superheating of steam is used, in particular, for converting saturated steam into hot steam in the field of nuclear energy generation. As a result of at least partial conversion of pressure energy of the steam into kinetic energy, in particular into kinetic energy of a rotational flow, the steam cools and condensate and residual steam are generated. After the condensate has been separated from the residual steam, the latter is superheated as a result of a reduction of its kinetic energy and is converted into hot steam.
Claims17
A method for the superheating of steam, which comprises:
- a) at least partially converting a pressure energy of steam into a rotational flow about an axis of rotation and into an axial flow superposed on the rotational flow and flowing in direction of the axis of rotation;
- b) increasing a rotational velocity of the steam in the direction of the axis of rotation by reducing a flow cross-section while generating condensate and residual steam;
- c) separating the condensate from the residual steam upstream of the reduction of the flow cross-section and subsequently discharging the condensate essentially radially outward;
- and
- d) further conveying the residual steam in the direction of the axis of rotation while reducing the rotational velocity of the residual steam and superheating and converting the residual steam into hot steam.
A method for generating hot steam from saturated steam in a nuclear power plant, which comprises:
- a) generating saturated steam in a reactor pressure vessel of a boiling water reactor plant;
- b) at least partially converting pressure energy of the saturated steam into kinetic energy of a rotational flow of the saturated steam while generating residual steam and condensate;
- c) at least partially separating the condensate from the residual steam;
- and
- d) subsequently reducing the kinetic energy of the rotational flow of the residual steam and superheating and converting the residual steam into hot steam.
An apparatus for the superheating of steam, comprising:
- a) a chamber having an axis of rotation and extending in direction of said axis of rotation;
- b) said chamber having an entry region for at least partially converting pressure energy of steam into kinetic energy of the steam and for separating a condensed-out condensate from remaining residual steam, said entry region having a given cross-sectional area;
- c) said chamber having a transitional region following said entry region for increasing the kinetic energy, said transitional region having a cross-sectional area smaller than said given cross-sectional area;
- d) said chamber having an exit region following said transitional region for reducing kinetic energy of the residual steam and for converting the residual steam into hot steam, said exit region having a cross-sectional area larger than said cross-sectional area of said transitional region;
- and
- e) said exit region having a first outlet for the hot steam, said entry region having a second outlet for the condensate, and said second outlet spaced radially from said axis of rotation.
A nuclear power station, comprising:
- an apparatus for superheating steam and for converting saturated steam into hot steam and condensate, said apparatus including:
- a) a chamber having an axis of rotation and extending in direction of said axis of rotation;
- b) said chamber having an entry region for at least partially converting pressure energy of steam into kinetic energy of the steam and for separating a condensed-out condensate from remaining residual steam, said entry region having a given cross-sectional area;
- c) said chamber having a transitional region following said entry region for increasing the kinetic energy, said transitional region having a cross-sectional area smaller than said given cross-sectional area;
- d) said chamber having an exit region following said transitional region for reducing kinetic energy of the residual steam and for converting the residual steam into hot steam, said exit region having a cross-sectional area larger than said cross-sectional area of said transitional region;
- and
- e) said exit region having a first outlet for the hot steam, said entry region having a second outlet for the condensate, and said second outlet spaced radially from said axis of rotation.
Dependencies are inferred from the claim text.