Humidity control device
US-2024328712-A1 · Oct 3, 2024 · US
US2016348540A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2016348540-A1 |
| Application number | US-201615156632-A |
| Country | US |
| Kind code | A1 |
| Filing date | May 17, 2016 |
| Priority date | May 26, 2015 |
| Publication date | Dec 1, 2016 |
| Grant date | — |
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The invention relates to power plant with a steam water power cycle and a lignite dryer that uses steam from the steam water power cycle. The connection of the lignite dryer to the steam water power cycle includes a first extraction line and a second extraction line.
Opening claim text (preview).
1 . A power plant comprising: a water/steam power cycle comprising: a pressure series of steam turbines including: a high pressure steam turbine; an intermediate pressure steam turbine; a low pressure steam turbine; a re-heater fluidly located between the high pressure steam turbine and the intermediate pressure steam turbine; and a lignite dryer having: a heater connected to a steam portion of the steam/water power cycle so as enable utilisation of steam energy in the lignite dryer, wherein the connection to the steam portion of the steam water power cycle comprises: a first extraction line, fluidly connected to the water/steam power cycle between the high pressure turbine and the intermediate pressure steam turbine, the first extraction line further including an ejector; a second extraction line, fluidly connected to the water/steam power cycle between the intermediate pressure steam turbine and the low pressure steam turbine, wherein the configuration and location of the ejector and the connection of the second extraction line to the ejector enables a lower pressure steam in the second extraction line to be fed into the heater together with a higher pressure steam of the first extraction line. 2 . The power plant of claim 1 wherein the second extraction line includes a bypass fluidly connecting the first extraction line to the second extraction line so as to bypass the ejector. 3 . The power plant of claim 1 further comprises a de-superheater in the first extraction line upstream of the ejector. 4 . The power plant according to claim 1 further comprising a throttle valve fluidly between the connection of the second extraction line to the water/steam power cycle and the low pressure steam turbine. 5 . The power plant of claim 1 , wherein the first extraction line is connected to the water/steam power cycle between the re-heater and the intermediate pressure steam turbine. 6 . A method of controlling a power plant, comprising the steps of: providing a water/steam power cycle comprising: a pressure series of steam turbines including: a high pressure steam turbine; an intermediate pressure steam turbine; and a low pressure steam turbine; a re-heater fluidly between the high pressure steam turbine and the intermediate pressure steam turbine; a throttle valve fluidly between the intermediate pressure steam turbine and the low pressure steam turbine; and providing a lignite dryer having: a heater fluidly connected to a steam portion of the steam/water power cycle so as to utilise steam energy in the lignite dryer, wherein the connection to the steam portion of the steam water power cycle comprises: a first extraction line, connected to the water/steam power cycle between the high pressure turbine and the intermediate pressure steam turbine to the heater, including an ejector; and a second extraction line, fluidly connected to the water/steam power cycle between the intermediate pressure steam turbine and the throttle valve, and to the ejector, the second extraction line further including a bypass, with a bypass valve, to enable bypassing of the ejector; and controlling a flow-rate to the heater by adjusting a pressure in the second extraction line in conjunction with the bypass valve. 7 . The method of claim 6 including the further steps of: providing a first control valve in the first extraction line upstream of the ejector; providing a second control valve in the second extraction line upstream of the ejector; and controlling the flow-rate to the heater in further conjunction with the first control valve and the second control valve.
using gases other than air · CPC title
arrangements of devices for distributing fluidising gas, e.g. grids, nozzles (F26B3/0926 takes precedence; such devices per se B01J8/44) · CPC title
Returning energy of steam, in exchanged form, to process, e.g. use of exhaust steam for drying solid fuel or plant · CPC title
Use of two or more feed-water heaters in series · CPC title
Drying or removing water · CPC title
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