US2676575A - Steam superheat control - Google Patents
Steam superheat control Download PDFInfo
- Publication number
- US2676575A US2676575A US172700A US17270050A US2676575A US 2676575 A US2676575 A US 2676575A US 172700 A US172700 A US 172700A US 17270050 A US17270050 A US 17270050A US 2676575 A US2676575 A US 2676575A
- Authority
- US
- United States
- Prior art keywords
- steam
- temperature
- superheater
- header
- superheat
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
Images
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F22—STEAM GENERATION
- F22G—SUPERHEATING OF STEAM
- F22G5/00—Controlling superheat temperature
- F22G5/12—Controlling superheat temperature by attemperating the superheated steam, e.g. by injected water sprays
- F22G5/14—Controlling superheat temperature by attemperating the superheated steam, e.g. by injected water sprays by live steam
Definitions
- This invention relates to a steam superheat control and particularly to a control to maintain a uniform superheat temperature under varying loads.
- the superheat temperature tends to be higher at high loads than at low loads. It has been the usual practice to design and adjust the superheater to produce the desired superheat at approximately half load and to desuperheat at higher loads. At lower loads the steam has been used at reduced superheat.
- Another object is to provide a steam superheat control in which steam is recirculated through the superheater at lower loads.
- Still another object is to provide a steam superheat control in which the amount of steam recirculation is controlled in response to a function, preferably the temperature, of the steam at the outlet side of the superheater.
- a function preferably the temperature
- an adjustable injector is employed to produce the recirculation and is adjusted in response to variations in the selected steam function.
- a further object is to provide an adjustable steam injector.
- FIG. 1 is a diagrammatic view of a steam superheat control embodying the invention.
- Figure 2 is a sectional View through the adjustable injector.
- the invention is applied to a steam generator or boiler having a. steam drum I0. Steam from the drum flows through a superheater H to a header 12 from which the steam is withdrawn for any desired use.
- These parts represent a conventional boiler construction except that the superheater, according to the present invention, is designed and adjusted to produce the desired superheat of the steam in the header 12 at some predetermined high load approaching maximum load, that is, when the maximum quantity of steam is flowing from the boiler and the header in the normal operating range. With the superheater so designed and adjusted, the superheat temperature of the steam will be lower than the designed temperature at all load conditions other than maximum load.
- a recirculating connection 13 is provided from the header [2 at the outlet side of the superheater to the inlet side of the superheater between the superheater and the boiler drum I8.
- the recirculating connection l3 leads to an injector I4 which functions in response to flow of steam from the boiler drum to the superheater to induce a flow of steam through the recirculating connection.
- the injector is constructed as best seen in Fig ure 2 with a hollow body l5 providing an enlarged chamber it having an inlet connection at I! for connection to the boiler drum and an outlet 18 for connection to the superheater inlet.
- the inlet connection ll preferably opens into the side of the chamber, and the chamber tapers toward the outlet connection as indicated at 19.
- An inlet chamber 2! i provided at one end of the chamber it and is separated therefrom by a wall 22 having a circular central opening therethrough opposite to the outlet 18.
- An injector nozzle 23 extends slidably through this opening in alignment with the outlet [8 and is shiftable axially toward and away from the opening it. With this construction the area of the passage around the nozzle 23 and within the tapered portion is can be varied to vary the injector effect and the quantity of steam circulating through the recirculating connection.
- the nozzle is formed with lateral inlet openings 24 communieating with the inlet chamber to receive steam from the bypass H3.
- the nozzle is adapted to be shifted by an operating rod 25 extending through the outer end of the inlet chamber and sealed by means of a packing 26.
- the rod 25 is moved by a control device indicated generally at 26 which may be any de sired type of regulator or controller capable of shifting the rod in response to a controlling force.
- the regulator 25 is preferably responsive to a function of the steam in the header I2 such, for example, as the rate of flow of steam through the header, the pressure in the header, or the temperature in the header. As shown, the regulator is responsive to the header steam temperature, and for this purpose a bulb 21 is mounted in the header and is connected by a tube 28 to the regulator 26. As the temperature in the header increases, the regulator will move the nozzle 23 to the left, as seen in Figure 2, and as the temperature decreases, the regulator will move the nozzle to the right.
- the injector provides a minimum degree of suction on the nozzle so that there will be a minimum or zero return flow of steam through the recirculating connection.
- the temperature in the header tends to drop so that the nozzle 23 will be shifted to the right. This increases the injector effect causing a circulation of steam from the header through the recirculating connection to recirculate through the superheater.
- the steam recirculates through the heater, its temperature will be increased and by properly adjusting the regulator the correct amount of steam can be recirculated to maintain the desired superheat temperature in the header under all load conditions.
- a superheater control comprising, a direct recirculating connection from the steam outlet to the steam inlet, control means to control the quantity of steam flowing through the recirculating connection, and a control device including a sensing element responsive to the temperature of the superheated steam to regulate the control means to maintain a uniform superheat temperature at said steam outlet under varying load conditions by increasing the quantity of steam flowing through said recirculating connection when said temperature decreases and decreasing said quantity when said temperature increases.
- a superheater control comprising, a
- a steam generator including combustion means for steam generation, a convection superheater connected to the generator and heated by said combustion means and designed to produce the desired superheat at a predetermined high load, a steam header connected to the superheater, a direct recirculating connection from the steam header around the superheater, and means responsive to the temperature of the steam flowing from said superheater to said header to maintain a uniform superheat temperature at said header under varying load conditions by increasing the quantity of steam flowing through said recirculating connection when said temperature decreases and decreasing said quantity when said temperature increases.
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Control Of Steam Boilers And Waste-Gas Boilers (AREA)
Description
April 27, 1954 A. J. ROSENBERGER STEAM SUPERHEAT CONTROL 7 Filed July 8, 1950 ATTORNEYS Patented Apr. 27, 1954 STEAM SUPERHEAT CONTROL Albert J. Rosenberger, Chicago, 111., assignor to Republic Flow Meters Company, Chicago, 111., a corporation of Illinois Application July 8, 1950, Serial No. 172,700
3 Claims.
This invention relates to a steam superheat control and particularly to a control to maintain a uniform superheat temperature under varying loads.
In boiler equipped with superheaters, the superheat temperature tends to be higher at high loads than at low loads. It has been the usual practice to design and adjust the superheater to produce the desired superheat at approximately half load and to desuperheat at higher loads. At lower loads the steam has been used at reduced superheat.
It is one of the objects of the present invention to provide a steam superheat control which will maintain a uniform superheat temperature under varying load conditions.
Another object is to provide a steam superheat control in which steam is recirculated through the superheater at lower loads.
Still another object is to provide a steam superheat control in which the amount of steam recirculation is controlled in response to a function, preferably the temperature, of the steam at the outlet side of the superheater. Preferably an adjustable injector is employed to produce the recirculation and is adjusted in response to variations in the selected steam function.
A further object is to provide an adjustable steam injector.
The above and other objects and advantages of the invention will be more readily apparent from the following description when read in connection with the accompanying drawing, in which Figure 1 is a diagrammatic view of a steam superheat control embodying the invention; and
Figure 2 is a sectional View through the adjustable injector.
As shown in Figure l, the invention is applied to a steam generator or boiler having a. steam drum I0. Steam from the drum flows through a superheater H to a header 12 from which the steam is withdrawn for any desired use. These parts represent a conventional boiler construction except that the superheater, according to the present invention, is designed and adjusted to produce the desired superheat of the steam in the header 12 at some predetermined high load approaching maximum load, that is, when the maximum quantity of steam is flowing from the boiler and the header in the normal operating range. With the superheater so designed and adjusted, the superheat temperature of the steam will be lower than the designed temperature at all load conditions other than maximum load.
To correct for the lower temperature at the lower load conditions, a recirculating connection 13 is provided from the header [2 at the outlet side of the superheater to the inlet side of the superheater between the superheater and the boiler drum I8. The recirculating connection l3 leads to an injector I4 which functions in response to flow of steam from the boiler drum to the superheater to induce a flow of steam through the recirculating connection.
The injector is constructed as best seen in Fig ure 2 with a hollow body l5 providing an enlarged chamber it having an inlet connection at I! for connection to the boiler drum and an outlet 18 for connection to the superheater inlet. The inlet connection ll preferably opens into the side of the chamber, and the chamber tapers toward the outlet connection as indicated at 19.
An inlet chamber 2! i provided at one end of the chamber it and is separated therefrom by a wall 22 having a circular central opening therethrough opposite to the outlet 18. An injector nozzle 23 extends slidably through this opening in alignment with the outlet [8 and is shiftable axially toward and away from the opening it. With this construction the area of the passage around the nozzle 23 and within the tapered portion is can be varied to vary the injector effect and the quantity of steam circulating through the recirculating connection. The nozzle is formed with lateral inlet openings 24 communieating with the inlet chamber to receive steam from the bypass H3.
The nozzle is adapted to be shifted by an operating rod 25 extending through the outer end of the inlet chamber and sealed by means of a packing 26. The rod 25 is moved by a control device indicated generally at 26 which may be any de sired type of regulator or controller capable of shifting the rod in response to a controlling force.
The regulator 25 is preferably responsive to a function of the steam in the header I2 such, for example, as the rate of flow of steam through the header, the pressure in the header, or the temperature in the header. As shown, the regulator is responsive to the header steam temperature, and for this purpose a bulb 21 is mounted in the header and is connected by a tube 28 to the regulator 26. As the temperature in the header increases, the regulator will move the nozzle 23 to the left, as seen in Figure 2, and as the temperature decreases, the regulator will move the nozzle to the right.
In operation, when the apparatus is operating at full load, the temperature in the header will be high at the desired superheat value, and the 3 nozzle 23 will be shifted fully to the left. At this time the injector provides a minimum degree of suction on the nozzle so that there will be a minimum or zero return flow of steam through the recirculating connection. At lower loads the temperature in the header tends to drop so that the nozzle 23 will be shifted to the right. This increases the injector effect causing a circulation of steam from the header through the recirculating connection to recirculate through the superheater. As the steam recirculates through the heater, its temperature will be increased and by properly adjusting the regulator the correct amount of steam can be recirculated to maintain the desired superheat temperature in the header under all load conditions.
While one embodiment of the invention has been shown and described in detail herein, it will be understood that this is illustrative only and is not to be taken as a definition of the scope of the invention, reference being had for this purpose to the ap ended claims.
What is claimed is:
1. In a steam generator including combustion means for steam generation and a convection superheater heated by said combustion means and having a steam inlet connected to said generator and a steam outlet and designed to produce the desired superheat at a predetermined high load, a superheater control comprising, a direct recirculating connection from the steam outlet to the steam inlet, control means to control the quantity of steam flowing through the recirculating connection, and a control device including a sensing element responsive to the temperature of the superheated steam to regulate the control means to maintain a uniform superheat temperature at said steam outlet under varying load conditions by increasing the quantity of steam flowing through said recirculating connection when said temperature decreases and decreasing said quantity when said temperature increases.
2. In a steam generator including combustion means for steam generation and a convection superheater heated by said combustion means and having a steam inlet connected to said generator and a steam outlet and designed to produce the desired superheat at a predetermined high load, a superheater control comprising, a
direct recirculating connection from the steam outlet to the steam inlet, an injector connected to the steam inlet and the recirculating connection to draw steam from the steam outlet through the recirculating connection into the steam inlet, adjustable means to control the quantity of steam flowing through the recirculating connection, and a control device including a sensing element responsive to the temperature of the superheated steam to adjust said adjustable means to maintain a uniform superheat temperature at said steam outlet under varying load conditions by increasing the quantity of steam flowing through said recirculating connection when said temperature decreases and decreasing said quantity when said temperature increases.
3. In combination, a steam generator including combustion means for steam generation, a convection superheater connected to the generator and heated by said combustion means and designed to produce the desired superheat at a predetermined high load, a steam header connected to the superheater, a direct recirculating connection from the steam header around the superheater, and means responsive to the temperature of the steam flowing from said superheater to said header to maintain a uniform superheat temperature at said header under varying load conditions by increasing the quantity of steam flowing through said recirculating connection when said temperature decreases and decreasing said quantity when said temperature increases.
References Cited in the file of this patent UNITED STATES PATENTS Number Name Date 123,264 Korting Jan. 30, 1872 395,456 Sauer Jan. 1, 1889 1,014,919 Sweeny et a1. Jan. 16, 1912 1,449,228 Hasegawa et a1. Mar. 20, 1923 1,661,106 Broido Feb. 28, 1928 1,934,724 Lucke Nov. 14, 1933 1,973,517 Armacost Sept. 11, 1934 1,992,115 Belohlavek Feb. 19, 1935 2,257,805 Kolling Oct. '7, 1941 2,594,818 Sprague et al Apr. 29, 1952 2,594,962 McDonald Apr. 29, 1952
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US172700A US2676575A (en) | 1950-07-08 | 1950-07-08 | Steam superheat control |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US172700A US2676575A (en) | 1950-07-08 | 1950-07-08 | Steam superheat control |
Publications (1)
Publication Number | Publication Date |
---|---|
US2676575A true US2676575A (en) | 1954-04-27 |
Family
ID=22628819
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US172700A Expired - Lifetime US2676575A (en) | 1950-07-08 | 1950-07-08 | Steam superheat control |
Country Status (1)
Country | Link |
---|---|
US (1) | US2676575A (en) |
Cited By (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2855151A (en) * | 1955-03-23 | 1958-10-07 | Robertshaw Fulton Controls Co | Mixing valve |
US2932452A (en) * | 1956-11-23 | 1960-04-12 | Garrett Corp | Mixing valve for gas turbine compressor |
US3417914A (en) * | 1966-06-09 | 1968-12-24 | Tokyo Shibaura Electric Co | Top nozzle of multistage diffusion pump |
US3423011A (en) * | 1967-01-10 | 1969-01-21 | Bell Aerospace Corp | Jet pump |
US3531218A (en) * | 1968-06-27 | 1970-09-29 | United Aircraft Corp | Ejector |
DE2225263A1 (en) | 1972-05-24 | 1973-12-06 | Baelz Gmbh Helmut | HOT WATER HEATING OR HEATING SYSTEM |
US4159735A (en) * | 1977-10-28 | 1979-07-03 | Sea Solar Power | Plate-fin heat exchanger with controls therefor |
US4184806A (en) * | 1977-03-16 | 1980-01-22 | Commissariat A L'energie Atomique | Pumping ejector |
US4422833A (en) * | 1981-05-11 | 1983-12-27 | Free Flow, Inc. | Pneumatic transfer system and a fluid flow control device therefor |
DE2265738C3 (en) * | 1972-05-24 | 1987-01-22 | Bälz, Helmut, 7100 Heilbronn | Return mixing device for a hot water heating system or a domestic hot water system |
US4773827A (en) * | 1987-07-23 | 1988-09-27 | Hydro-Thermal Corporation | Liquid heating apparatus with temperature control system |
Citations (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US123264A (en) * | 1872-01-30 | Improvement in combined injectors, feed-water heaters, and condensers | ||
US395456A (en) * | 1889-01-01 | Attachment for compressed-air engines | ||
US1014919A (en) * | 1909-06-28 | 1912-01-16 | Jared S Sweeny | Feed-water heater. |
US1449228A (en) * | 1918-09-12 | 1923-03-20 | Hasegawa Seigo | Locomotive boiler |
US1661106A (en) * | 1924-10-30 | 1928-02-28 | Superheater Co Ltd | Method of controlling flow through superheaters |
US1934724A (en) * | 1931-03-24 | 1933-11-14 | Babeock & Wilcox Company | Steam boiler with superheater |
US1973517A (en) * | 1931-09-29 | 1934-09-11 | Superheater Co Ltd | Radiant and convection superheater |
US1992115A (en) * | 1931-05-29 | 1935-02-19 | Belohlavek Bruno | Safeguarding of superheaters |
US2257805A (en) * | 1936-07-07 | 1941-10-07 | Babcock & Wilcox Co | Means for regulating the temperature of superheated steam |
US2594962A (en) * | 1948-04-30 | 1952-04-29 | Babcock & Wilcox Co | Aspirating two-way control valve |
US2594818A (en) * | 1948-02-03 | 1952-04-29 | Babcock & Wilcox Co | Temperature control system for a fluid under pressure |
-
1950
- 1950-07-08 US US172700A patent/US2676575A/en not_active Expired - Lifetime
Patent Citations (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US123264A (en) * | 1872-01-30 | Improvement in combined injectors, feed-water heaters, and condensers | ||
US395456A (en) * | 1889-01-01 | Attachment for compressed-air engines | ||
US1014919A (en) * | 1909-06-28 | 1912-01-16 | Jared S Sweeny | Feed-water heater. |
US1449228A (en) * | 1918-09-12 | 1923-03-20 | Hasegawa Seigo | Locomotive boiler |
US1661106A (en) * | 1924-10-30 | 1928-02-28 | Superheater Co Ltd | Method of controlling flow through superheaters |
US1934724A (en) * | 1931-03-24 | 1933-11-14 | Babeock & Wilcox Company | Steam boiler with superheater |
US1992115A (en) * | 1931-05-29 | 1935-02-19 | Belohlavek Bruno | Safeguarding of superheaters |
US1973517A (en) * | 1931-09-29 | 1934-09-11 | Superheater Co Ltd | Radiant and convection superheater |
US2257805A (en) * | 1936-07-07 | 1941-10-07 | Babcock & Wilcox Co | Means for regulating the temperature of superheated steam |
US2594818A (en) * | 1948-02-03 | 1952-04-29 | Babcock & Wilcox Co | Temperature control system for a fluid under pressure |
US2594962A (en) * | 1948-04-30 | 1952-04-29 | Babcock & Wilcox Co | Aspirating two-way control valve |
Cited By (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2855151A (en) * | 1955-03-23 | 1958-10-07 | Robertshaw Fulton Controls Co | Mixing valve |
US2932452A (en) * | 1956-11-23 | 1960-04-12 | Garrett Corp | Mixing valve for gas turbine compressor |
US3417914A (en) * | 1966-06-09 | 1968-12-24 | Tokyo Shibaura Electric Co | Top nozzle of multistage diffusion pump |
US3423011A (en) * | 1967-01-10 | 1969-01-21 | Bell Aerospace Corp | Jet pump |
US3531218A (en) * | 1968-06-27 | 1970-09-29 | United Aircraft Corp | Ejector |
DE2225263A1 (en) | 1972-05-24 | 1973-12-06 | Baelz Gmbh Helmut | HOT WATER HEATING OR HEATING SYSTEM |
DE2265738C3 (en) * | 1972-05-24 | 1987-01-22 | Bälz, Helmut, 7100 Heilbronn | Return mixing device for a hot water heating system or a domestic hot water system |
US4184806A (en) * | 1977-03-16 | 1980-01-22 | Commissariat A L'energie Atomique | Pumping ejector |
US4159735A (en) * | 1977-10-28 | 1979-07-03 | Sea Solar Power | Plate-fin heat exchanger with controls therefor |
US4422833A (en) * | 1981-05-11 | 1983-12-27 | Free Flow, Inc. | Pneumatic transfer system and a fluid flow control device therefor |
US4773827A (en) * | 1987-07-23 | 1988-09-27 | Hydro-Thermal Corporation | Liquid heating apparatus with temperature control system |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US2676575A (en) | Steam superheat control | |
US3331590A (en) | Pressure reducing control valve | |
US3017870A (en) | Steam or vapor generator having at least two firing systems | |
US2869517A (en) | Once through steam generating plant | |
ES354146A1 (en) | Apparatus for regulating the recirculation of working medium in a once-through force-flow steam generator | |
US3129564A (en) | Forced flow steam generating plants including a reheater | |
US3004529A (en) | Method and apparatus for controlling fuel and/or feedwater flow in a oncethrough steam generator | |
US2526898A (en) | Vapor temperature control | |
SU833175A3 (en) | Device for control of liquid flow in pipe | |
US2319223A (en) | Method and apparatus for temperature regulation | |
US2257805A (en) | Means for regulating the temperature of superheated steam | |
GB1007737A (en) | Forced flow vapour generators | |
US3117620A (en) | Temperature equalizing means for a plurality of conduits | |
US2412739A (en) | Apparatus for steam generator control | |
GB831175A (en) | Apparatus and method for controlling a forced flow once-through steam generator | |
US3092677A (en) | Desuperheater | |
GB1116706A (en) | Startup system for a steam actuated electric generator | |
US2526843A (en) | Temperature control system | |
US3133528A (en) | Tubular heating element for heating fluids | |
GB744797A (en) | Improvements in forced flow, once-through tubulous vapour generating and vapour heating units and to a method of operation thereof | |
US3893427A (en) | Gas heated steam generator | |
US3192908A (en) | Method and apparatus for controlling the temperature of vapor created in a vapor generator | |
US2074235A (en) | Tubular continuous-flow steam generator | |
US3364903A (en) | Steam generator with reheat temperature regulation | |
GB903012A (en) | An improved method of and apparatus for generating superheated vapour |