Claims
- 1. A once-through steam generator, comprising:
- a vertical gas flue formed of a plurality of tubes, said tubes being welded to one another in a gas-tight manner, and burners for fossil fuel disposed at said tubes;
- said plurality of tubes being oriented substantially vertically and being connected in parallel for guiding a flow of flow medium therethrough;
- said tubes each having a longitudinal axis and a wall with an inner wall surface, and a surface structure formed on said inner wall surface for causing flow turbulence in the flow medium;
- said surface structure on said inner wall surface including first and second, mutually superimposed, contrary ribbings, said first ribbing forming an acute angle with said tube axis, and said second ribbing extending substantially parallel to said tube axis; and
- said first ribbing forming an onflow flank angle and a flow-off flank angle with said tube wall, said onflow flank angle being flatter than said flow-off flank angle for the formation of longitudinal eddies.
- 2. The steam generator according to claim 1, wherein said surface structure includes elevations on said tube wall defined by said ribbings, said elevations having a height from said inner wall surface of at least 0.7 mm.
- 3. A method of operating a continuous steam generator, which comprises:
- providing a steam generator with a vertical gas flue formed of a plurality of parallel-connected tubes, and combusting a fossil fuel in burners disposed at said tubes;
- providing the tubes with a surface structure on an inner wall surface thereof, and forming the surface structure of first and second, mutually superimposed, contrary ribbings;
- guiding a flow medium in parallel flow through the plurality of tubes and adjusting a mass flow density of the medium in the tubes as a function of an inner tube diameter, by determining an operating point with a pair of values of the mass flow density and the inner tube diameter being located in a cartesian coordinate system between the abscissa and a curve containing the following operating points:
- d.sub.1 =10 mm at m.sub.1 =1600 kg/m.sup.2 .multidot.s
- d.sub.2 =25 mm at m.sub.2 =1600 kg/m.sup.2 .multidot.s
- d.sub.3 =40 mm at m.sub.3 =1300 kg/m.sup.2 .multidot.s
- where d is the inner tube diameter and m is the mass flow density of the flow medium in the tubes.
Priority Claims (1)
Number |
Date |
Country |
Kind |
43 33 404.0 |
Sep 1993 |
DEX |
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CROSS-REFERENCE TO RELATED APPLICATION
This application is a continuation of our international application PCT/DE94/01086, filed Sep. 19, 1994, which designated the United States.
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