Method for operating a steam cycle process
US-9163530-B2 · Oct 20, 2015 · US
US9739474B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9739474-B2 |
| Application number | US-201214399618-A |
| Country | US |
| Kind code | B2 |
| Filing date | May 9, 2012 |
| Priority date | May 9, 2012 |
| Publication date | Aug 22, 2017 |
| Grant date | Aug 22, 2017 |
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A waste heat boiler has heat exchange tubes for indirect heat exchange of a relatively hot process gas and a cooling media, and a by-pass tube for by-passing a part of the process gas; a swirl mixer ensures mixing of the cooled process gas and the relative hot process gas exiting the heat exchange tubes and the by-pass tube.
Opening claim text (preview).
The invention claimed is: 1. Waste heat boiler for heat exchanging a relatively hot process gas with a cooling media comprising: a shell, at least two tube sheets located within the shell, a plurality of heat exchange tubes comprising a plurality of inlet and outlet ends that extend through said tube sheets; a heat exchange section enclosed by a part of said shell and said at least two tube sheets; a process gas inlet section in fluid connection with said inlet ends; a process gas outlet section in fluid connection with outlet ends; at least one by-pass tube extending though the shell comprising an open exit end which is in fluid connection with said gas outlet section; at least one cooling media inlet in fluid connection with a shell side of said heat exchange section; at least one cooling media outlet for removing media from said shell side of said heat exchange section, and a mixer section, said mixer section including a first duct and a second duct extending through and beyond the first duct, said first duct having an inlet end in fluid connection with said outlet ends of said plurality of heat exchange tubes and an annular outlet end with internally arranged swirl inducing elements, said second duct in fluid connection with said open exit end of said by-pass tube and having an outlet end formed with radially arranged nozzles to tangentially eject by-passed process gases into the path of process gas emanating from the swirl elements, the mixer section including a first valve to control the flow of process gas exiting the heat exchange tubes, wherein the first valve is located at the entrance of the first duct and slides around the second duct. 2. Waste heat boiler according to claim 1 , wherein the swirl mixer further comprising a flow straightening element located within the first duct and before the swirl inducing element relative to the axial flow direction of the cooled process gas in the first duct. 3. Waste heat boiler according to claim 1 , wherein the swirl mixer further comprises a second valve to control the flow of the relative hot process gas exiting the at least one by-pass tube. 4. Waste heat boiler according to claim 1 , wherein the first duct is fixed to the shell by means of a tube sheet. 5. Waste heat boiler according to claim 1 , wherein the swirl inducing elements comprise vanes. 6. Waste heat boiler according to claim 1 , wherein the inside wall of the by-pass tube and at least part of the second duct is lined with a ceramic liner. 7. Waste heat boiler according to claim 1 , wherein the cooling media is water or steam or both water and steam. 8. Waste heat boiler according to claim 1 , wherein said shell has a cylindrical shape and said at least two tube sheets have a circular shape.
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by creating turbulence, e.g. by stirring, by increasing the force of circulation (F28F13/08 takes precedence) · CPC title
the conduit assemblies having an annular shape; the conduits being assembled around a central distribution tube · CPC title
Derivation channels, e.g. bypass · CPC title
the heat carrier being a hot gas, e.g. waste gas such as exhaust gas of internal-combustion engines · CPC title
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