US2800887A - Control system for forced flow vapor generators - Google Patents
Control system for forced flow vapor generators Download PDFInfo
- Publication number
- US2800887A US2800887A US337607A US33760753A US2800887A US 2800887 A US2800887 A US 2800887A US 337607 A US337607 A US 337607A US 33760753 A US33760753 A US 33760753A US 2800887 A US2800887 A US 2800887A
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- tubes
- temperature
- control system
- forced flow
- tube
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- 239000007788 liquid Substances 0.000 description 11
- 230000001276 controlling effect Effects 0.000 description 7
- 239000000446 fuel Substances 0.000 description 4
- 238000010438 heat treatment Methods 0.000 description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- 238000012986 modification Methods 0.000 description 3
- 230000004048 modification Effects 0.000 description 3
- 238000009834 vaporization Methods 0.000 description 3
- 230000008016 vaporization Effects 0.000 description 3
- VJYFKVYYMZPMAB-UHFFFAOYSA-N ethoprophos Chemical compound CCCSP(=O)(OCC)SCCC VJYFKVYYMZPMAB-UHFFFAOYSA-N 0.000 description 2
- 230000001105 regulatory effect Effects 0.000 description 2
- 241001417495 Serranidae Species 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- 229920006395 saturated elastomer Polymers 0.000 description 1
- 230000007704 transition Effects 0.000 description 1
Images
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F22—STEAM GENERATION
- F22B—METHODS OF STEAM GENERATION; STEAM BOILERS
- F22B35/00—Control systems for steam boilers
- F22B35/06—Control systems for steam boilers for steam boilers of forced-flow type
- F22B35/10—Control systems for steam boilers for steam boilers of forced-flow type of once-through type
- F22B35/102—Control systems for steam boilers for steam boilers of forced-flow type of once-through type operating with fixed point of final state of complete evaporation, e.g. in a steam-water separator
Definitions
- the present invention relates to rforced flow vapor generators of the kind in'which the heating surface is formed by a plurality of tubes connected in parallel, at least in the zones of vaporization and of the beginning of ,superheating, and which generators comprise a device v the supply of working medium to one of the parallelconnected tubes of forced flow steam generators differently from the supply to the other tubes, so that either the still liquid working medium is heated longer-or superheating of the steam begins sooner than in the other tubes.
- the regulating device is actuated by the temperature of the diiferently adjusted tube.
- a temperature sensitive device is connected with each tube or a plurality of the tubes of a set of tubes which are arranged parallel with respect to fluid flow and all temperature sensitive devices are connected with a selector which passes on impulses only which come from the device connected with the tube of highest temperature and interrupts all other impulses.
- Fig. 1 is a diagram illustrating the tube system of a forced flow steam generator at the evaporation zone and at the beginning of the superheating zone;
- Fig. 2 is a diagrammatic illustration of a selector and pilot valve actuator forming part of the control system according to the invention
- Fig. 3 is .a diagrammatic illustration of a modified system according to the invention.
- Fig. 4 is a diagrammatic illustration of a further modification of the system according to the invention.
- Fig. 5 is a diagrammatic illustration of a modification of the system according to Fig. 4;
- Fig. dis a diagrammatic sectional view of a servomotor as may be used in the system according to the invention.
- the steam generator shown in Fig. 1 comprises four parallel-connectedtubes-1-to4:in the zones of vaporization and of the beginning'of superheating. Feed water is supplied as uniformly as possible to these tubes by means of a feed pump -5 through a'conduit 35. Heating of the tubes is eifected as uniformly as possible by suitable arrangement of the-tubes in the generator. In the :area of the transition from the vaporization zone to the superheating zone the tubes 1 to 4 are connected to a collector 6 from which a pipe .7 leads to a superheater, notshown.
- the regulationiof the amount of feed water supplied to tubes "1 to '4 is effected by adjusting the speedof'thepumpS bygmeanslof a regulator or servomotor 8 which may be of the type shown in Fig. 6.
- a thermostat, 9m :12, : is connected with each of the tubes 1 [04, respectively, which tubes are connected in parallel relation :with respect to medium flow.
- the thermostats are preferablyaconnected-with:thetubes in the proximity of the header 6 and are individually connected by conventionaltemperature impulse transmitting means, 9' to 11 respectively, withta selector 13 from which control impulses are transmitted 'by conventional means 14 to the .regulator or .servomotor 8.
- the selector 13 which is interposed between the thermostats 9 to 12 and the servomotor 8 comprises four bellows .15 :to 18 which are individually connected by the impulse transmitting means '9' to 11,
- thermostat 11 has the highest temperature and the pin of bellows 17 abuts against the cross bar 19.
- the pins of the other bellows cannot reach the cross bar because they are actuated by thermostats having relatively low temperatures.
- the system can be so set that only that one of the tubes 1 to 4 which has the highest temperature will discharge slightly superheated steam into the header 6, the other tubes discharging dry saturated or slightly wet steam into the header.
- actuation of regulator 8 will be affected by the temperature of different tubes 1 to 4 at difierent times depending on the heat transfer condition at the outside and inside surfaces of the tubes and other changing operating conditions.
- the system according to the invention prevents exces- 3 sive heating of an individual tube, for example, caused by excessive scale deposit.
- each of the tubes designated by the numerals 1 to 4 may represent a group of tubes which are so arranged that they are subjected to substantially the same operating conditions, each group being provided with a thermostat.
- a steam separator26 may be provided between the points where the thermostats are connected to the tubes 1 to 4 and the superheater, not shown, which is connected with the header 6 by means of a conduit 7.
- the steam separator is preferably connected with the conduit 7. V a
- the fuel supply may be controlled.
- Fig. 3 in which the selector 13 actuates a conventional servoniotor 36 which may be of the type shown in Fig. 6 and which controls a valve the vapor generated in the .the vapor generated in the tubes, said system comprising a temperature measuring means connected with each tube;
- a selector including a plurality of temperature indicating means which are individually connected with and actuated by said temperature measuring means for indicating the temperature measured by said temperature measuring means, and an element adapted to be actuated by that one of said temperature indicating means which indicates the relatively highest temperature; means for con- 27 in the fuel conduit between a fuel pump 5 and a burner 26.
- a portion of the feed water supplied by pump 5 may be diverted into a conduit 28 (Fig. 4) and the diverted stream may be divided into a plurality of 'conduits 29, 30, 31, 32 corresponding in number and being individually connected to the conduits 1 to 4 of the steam generator.
- a valve 29', 30', 31', 32 is provided in each conduit, 29, 30, 31, 32, respectively. All valves 29' to 32' are connected to a servomotor 33 which is actuated by the selector 13.
- the system illustrated in Fig. 4 may be modified by omitting the valves 29 to 32' in the conduits 29 to 32 and arranging a valve 34 in conduit 28 as shown in Fig.
- Valve 34 is connected to and operated by a regulator 33 actuated by the selector 13 as trated embodiments.
- V 1 The method of controlling the liquid supply to a 'forced flow vapor generator in'which the liquid is forced through a plurality of heated tubes which are arranged in parallel with respect to the flow of the liquid and of 'measuring means and said control means, and impulse for interrupting all temperature impulses emanating from V 'said temperature measuring means except the impulse which emanates from that of said measuring means which interrupting means interposed in said transmitting means measures the highest temperature.
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- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Description
July 39, 1957 P. PROFOS 2,800,887
CONTROL SYSTEM FOR FORCED FLOW VAPOR GENERATORS Filed Feb. 18, 1955 INVENTOR. PAUL Pea/ as.
ATTOKNEK United States Patent @fiice 2,800,887 Patented July 30, 1957 amass? CONTRUL SYSTEMFGR FORCED FLOW VAPOR GENERATGRS Paul Profos, Wintertliur, Switzerland, assignor to Sulzer Freres, Societe Anonyme, Winter-titer, Switzerland, a corporation of Switzerland Application Fehruary 18,1953, Serial No. 337,607
v3 Clm'ms. ((11.122-448) The present invention relates to rforced flow vapor generators of the kind in'which the heating surface is formed by a plurality of tubes connected in parallel, at least in the zones of vaporization and of the beginning of ,superheating, and which generators comprise a device v the supply of working medium to one of the parallelconnected tubes of forced flow steam generators differently from the supply to the other tubes, so that either the still liquid working medium is heated longer-or superheating of the steam begins sooner than in the other tubes. The regulating device is actuated by the temperature of the diiferently adjusted tube. Due to nu merous smallchanges of operating'conditions, which cannot be controlled, individual tubes receive more or less heat than the other tubes, sometimes temporarily, sometimes for longer periods, or permanently, or receive more or less working medium so that at times one or another tube is favored with heat. Such disturbances may be caused by faulty operation of individual burners, slagging of individual tubes, disturbances in the supply of secondary combustionv air, .or .by .other-etfects which occur in every steam generator. Taking the temperature of a single tube for controlling fuel and/ or operating medium supply may cause serious changes of'the temperature of the total steam, if there is an irregularity in the heating of this single tube. Such temperature changes may cause damage, if they are not immediately discovered. Such damages occur particularly, if the measuring tube receives relatively little heat, because, in that case, all other tubes are supplied with too much heat.
It is an object of the present invention to provide a control system for forced fiow steam generators which avoids the aforedescribed disadvantages. In the system according to the invention a temperature sensitive device is connected with each tube or a plurality of the tubes of a set of tubes which are arranged parallel with respect to fluid flow and all temperature sensitive devices are connected with a selector which passes on impulses only which come from the device connected with the tube of highest temperature and interrupts all other impulses.
Further and other objects of the present invention will be hereinafter set forth in the accompanying specification and claims, and shown in the drawing which, by way of illustration, shows what I now consider to be preferred embodiments of my invention.
In the drawing:
Fig. 1 is a diagram illustrating the tube system of a forced flow steam generator at the evaporation zone and at the beginning of the superheating zone;
Fig. 2 is a diagrammatic illustration of a selector and pilot valve actuator forming part of the control system according to the invention;
Fig. 3 is .a diagrammatic illustration of a modified system according to the invention;
Fig. 4 is a diagrammatic illustration of a further modification of the system according to the invention;
Fig. 5 is a diagrammatic illustration of a modification of the system according to Fig. 4;
Fig. dis a diagrammatic sectional view of a servomotor as may be used in the system according to the invention.
Like parts are designated by like numerals in all figures of the drawing.
The steam generator shown in Fig. 1 comprises four parallel-connectedtubes-1-to4:in the zones of vaporization and of the beginning'of superheating. Feed water is supplied as uniformly as possible to these tubes by means of a feed pump -5 through a'conduit 35. Heating of the tubes is eifected as uniformly as possible by suitable arrangement of the-tubes in the generator. In the :area of the transition from the vaporization zone to the superheating zone the tubes 1 to 4 are connected to a collector 6 from which a pipe .7 leads to a superheater, notshown. The regulationiof the amount of feed water supplied to tubes "1 to '4 is effected by adjusting the speedof'thepumpS bygmeanslof a regulator or servomotor 8 which may be of the type shown in Fig. 6. A thermostat, 9m :12, :is connected with each of the tubes 1 [04, respectively, which tubes are connected in parallel relation :with respect to medium flow. The thermostats are preferablyaconnected-with:thetubes in the proximity of the header 6 and are individually connected by conventionaltemperature impulse transmitting means, 9' to 11 respectively, withta selector 13 from which control impulses are transmitted 'by conventional means 14 to the .regulator or .servomotor 8.
.As seen in Fig. .2, the selector 13 which is interposed between the thermostats 9 to 12 and the servomotor 8 comprises four bellows .15 :to 18 which are individually connected by the impulse transmitting means '9' to 11,
respectively, withthetthermostats 9 to 12. Rising tem- .peraturevof the thermostats causes expansion of the bel- 20. V Tothe other :end of lever .21, a rod 22 is pivoted which rod actuates the piston of a conventional hydraulic control valve 25 which controls the pressure in the impulse transmitting conduit 14, thereby controlling the regulator 8. A spring 23, whose one end is connected to the base plate 24 and whose other end is connected with the cross bar 19, pulls the latter against the pins extending from the movable ends of the bellows so that the pin of the bellows connected with the thermostat having the highest temperature is abutted by the bar 19. In the position shown in Fig. 2, thermostat 11 has the highest temperature and the pin of bellows 17 abuts against the cross bar 19. The pins of the other bellows cannot reach the cross bar because they are actuated by thermostats having relatively low temperatures. By proper adjustment of the length of rod 22, the system can be so set that only that one of the tubes 1 to 4 which has the highest temperature will discharge slightly superheated steam into the header 6, the other tubes discharging dry saturated or slightly wet steam into the header. During normal operation, actuation of regulator 8 will be affected by the temperature of different tubes 1 to 4 at difierent times depending on the heat transfer condition at the outside and inside surfaces of the tubes and other changing operating conditions. The system according to the invention prevents exces- 3 sive heating of an individual tube, for example, caused by excessive scale deposit.
Without departing from the scope of the invent on,
each of the tubes designated by the numerals 1 to 4 may represent a group of tubes which are so arranged that they are subjected to substantially the same operating conditions, each group being provided with a thermostat. Y
A steam separator26 may be provided between the points where the thermostats are connected to the tubes 1 to 4 and the superheater, not shown, which is connected with the header 6 by means of a conduit 7. The steam separator is preferably connected with the conduit 7. V a
Instead of controlling the supply of liquid to the vapor generator in dependence on the temperature of the hottest of a plurality of tubes which are arranged parallel V with respect to medium flow, the fuel supply may be controlled. This is shown in Fig. 3 in which the selector 13 actuates a conventional servoniotor 36 which may be of the type shown in Fig. 6 and which controls a valve the vapor generated in the .the vapor generated in the tubes, said system comprising a temperature measuring means connected with each tube;
a selector including a plurality of temperature indicating means which are individually connected with and actuated by said temperature measuring means for indicating the temperature measured by said temperature measuring means, and an element adapted to be actuated by that one of said temperature indicating means which indicates the relatively highest temperature; means for con- 27 in the fuel conduit between a fuel pump 5 and a burner 26.
Instead of controlling the total feed water stream as in Fig. l, a portion of the feed water supplied by pump 5 may be diverted into a conduit 28 (Fig. 4) and the diverted stream may be divided into a plurality of ' conduits 29, 30, 31, 32 corresponding in number and being individually connected to the conduits 1 to 4 of the steam generator. A valve 29', 30', 31', 32 is provided in each conduit, 29, 30, 31, 32, respectively. All valves 29' to 32' are connected to a servomotor 33 which is actuated by the selector 13.
The system illustrated in Fig. 4 may be modified by omitting the valves 29 to 32' in the conduits 29 to 32 and arranging a valve 34 in conduit 28 as shown in Fig.
trolling the supply of liquid to the tubes'of the vapor generator, said last'mentioned means being connected with said element for operation thereby and controlling the supply of liquid to the vapor generator tubes in ac? cordance with the temperature of the tube relatively highest temperature. a
3. A system for regulating the liquid supply to a forced which the 1 flow vapor generator in which the liquid is pumped through a plurality of heated tubes which are arranged in parallel with respect to the flow of the liquid and of the vapor generated in the tubes, said system comprising a temperature measuring means connected with each tube,
'controlrneans for controlling the supply of liquid, to the tubes of the vapor generator, temperature impulse 'transmitting means interconnecting said temperature 5. Valve 34 is connected to and operated by a regulator 33 actuated by the selector 13 as trated embodiments. I
While I believe the above described embodiments of my invention to be preferred embodiments, I wish it to be understood that I do not desire to be limited to the in the other illusexact details of design, and construction shown and described, for obvious modifications will occur to a person skilled in the art.
What is claimed is: V 1. The method of controlling the liquid supply to a 'forced flow vapor generator in'which the liquid is forced through a plurality of heated tubes which are arranged in parallel with respect to the flow of the liquid and of 'measuring means and said control means, and impulse for interrupting all temperature impulses emanating from V 'said temperature measuring means except the impulse which emanates from that of said measuring means which interrupting means interposed in said transmitting means measures the highest temperature.
References Cited in the tile of this patent UNITED STATES PATENTS 4 1,928,010 Eglofl Sept. 26, 1933 1 FOREIGN PATENTS S 151,763 Switzerland Dec; 31, 1931 153,287 Switzerland Mar. 15, 1932 375,185 Great Britain June 23, 1932 681,458
Great Britain Oct. 22, 1952'
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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US337607A US2800887A (en) | 1953-02-18 | 1953-02-18 | Control system for forced flow vapor generators |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
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US337607A US2800887A (en) | 1953-02-18 | 1953-02-18 | Control system for forced flow vapor generators |
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US2800887A true US2800887A (en) | 1957-07-30 |
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US337607A Expired - Lifetime US2800887A (en) | 1953-02-18 | 1953-02-18 | Control system for forced flow vapor generators |
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Cited By (13)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3004529A (en) * | 1956-03-06 | 1961-10-17 | Comb Eugineering Inc | Method and apparatus for controlling fuel and/or feedwater flow in a oncethrough steam generator |
US3086504A (en) * | 1958-02-26 | 1963-04-23 | Sulzer Ag | Method and apparatus for controlling a forced flow steam generator |
US3108576A (en) * | 1958-03-15 | 1963-10-29 | Siemens Ag | Once-through steam generator |
US3126053A (en) * | 1959-02-02 | 1964-03-24 | Brunner | |
US3138143A (en) * | 1964-06-23 | Brunner | ||
US3154057A (en) * | 1963-07-03 | 1964-10-27 | Sulzer Ag | Regulating system for dividing a stream of fluid into at least two subsidiary streams |
US3230937A (en) * | 1960-06-21 | 1966-01-25 | Sulzer Ag | Method and apparatus for operating a forced flow steam generator |
US3240188A (en) * | 1961-10-06 | 1966-03-15 | Sulzer Ag | Method of and apparatus for distributing a fluid into at least two heated tubes arranged in parallel relation with respect to the flow of fluid therethrough |
US4440114A (en) * | 1983-04-18 | 1984-04-03 | Babcock & Wilcox Company | Bias bellows for thermohydraulic feedwater regulator |
US4526136A (en) * | 1984-05-29 | 1985-07-02 | The United States Of America As Represented By The United States Department Of Energy | Control system for fluid heated steam generator |
US5398644A (en) * | 1991-09-13 | 1995-03-21 | Abb Carbon Ab | Temperature measurement at evaporator outlet |
US20130180681A1 (en) * | 2012-01-17 | 2013-07-18 | Alstom Technology Ltd. | Start-up system for a once-through horizontal evaporator |
US9696098B2 (en) | 2012-01-17 | 2017-07-04 | General Electric Technology Gmbh | Method and apparatus for connecting sections of a once-through horizontal evaporator |
Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CH151763A (en) * | 1930-09-20 | 1931-12-31 | Sulzer Ag | Procedure for operating tubular steam generators. |
CH153287A (en) * | 1931-02-07 | 1932-03-15 | Sulzer Ag | Steam generator. |
GB375185A (en) * | 1930-11-12 | 1932-06-23 | Sulzer Ag | Improvements in or relating to steam generators with tubular generating systems |
US1928010A (en) * | 1931-02-07 | 1933-09-26 | Sulzer Ag | Water tube steam generator |
GB681458A (en) * | 1949-06-23 | 1952-10-22 | Comb Eng Superheater Inc | Protective apparatus for steam generators |
-
1953
- 1953-02-18 US US337607A patent/US2800887A/en not_active Expired - Lifetime
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CH151763A (en) * | 1930-09-20 | 1931-12-31 | Sulzer Ag | Procedure for operating tubular steam generators. |
GB375185A (en) * | 1930-11-12 | 1932-06-23 | Sulzer Ag | Improvements in or relating to steam generators with tubular generating systems |
CH153287A (en) * | 1931-02-07 | 1932-03-15 | Sulzer Ag | Steam generator. |
US1928010A (en) * | 1931-02-07 | 1933-09-26 | Sulzer Ag | Water tube steam generator |
GB681458A (en) * | 1949-06-23 | 1952-10-22 | Comb Eng Superheater Inc | Protective apparatus for steam generators |
Cited By (17)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3138143A (en) * | 1964-06-23 | Brunner | ||
US3004529A (en) * | 1956-03-06 | 1961-10-17 | Comb Eugineering Inc | Method and apparatus for controlling fuel and/or feedwater flow in a oncethrough steam generator |
US3086504A (en) * | 1958-02-26 | 1963-04-23 | Sulzer Ag | Method and apparatus for controlling a forced flow steam generator |
US3108576A (en) * | 1958-03-15 | 1963-10-29 | Siemens Ag | Once-through steam generator |
US3126053A (en) * | 1959-02-02 | 1964-03-24 | Brunner | |
US3230937A (en) * | 1960-06-21 | 1966-01-25 | Sulzer Ag | Method and apparatus for operating a forced flow steam generator |
US3240188A (en) * | 1961-10-06 | 1966-03-15 | Sulzer Ag | Method of and apparatus for distributing a fluid into at least two heated tubes arranged in parallel relation with respect to the flow of fluid therethrough |
US3154057A (en) * | 1963-07-03 | 1964-10-27 | Sulzer Ag | Regulating system for dividing a stream of fluid into at least two subsidiary streams |
US4440114A (en) * | 1983-04-18 | 1984-04-03 | Babcock & Wilcox Company | Bias bellows for thermohydraulic feedwater regulator |
US4526136A (en) * | 1984-05-29 | 1985-07-02 | The United States Of America As Represented By The United States Department Of Energy | Control system for fluid heated steam generator |
US5398644A (en) * | 1991-09-13 | 1995-03-21 | Abb Carbon Ab | Temperature measurement at evaporator outlet |
US20130180681A1 (en) * | 2012-01-17 | 2013-07-18 | Alstom Technology Ltd. | Start-up system for a once-through horizontal evaporator |
US9151488B2 (en) * | 2012-01-17 | 2015-10-06 | Alstom Technology Ltd | Start-up system for a once-through horizontal evaporator |
US9696098B2 (en) | 2012-01-17 | 2017-07-04 | General Electric Technology Gmbh | Method and apparatus for connecting sections of a once-through horizontal evaporator |
US9746174B2 (en) | 2012-01-17 | 2017-08-29 | General Electric Technology Gmbh | Flow control devices and methods for a once-through horizontal evaporator |
US9989320B2 (en) | 2012-01-17 | 2018-06-05 | General Electric Technology Gmbh | Tube and baffle arrangement in a once-through horizontal evaporator |
US10274192B2 (en) | 2012-01-17 | 2019-04-30 | General Electric Technology Gmbh | Tube arrangement in a once-through horizontal evaporator |
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