US2124254A - Method of high pressure steam generation - Google Patents
Method of high pressure steam generation Download PDFInfo
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- US2124254A US2124254A US10926A US1092635A US2124254A US 2124254 A US2124254 A US 2124254A US 10926 A US10926 A US 10926A US 1092635 A US1092635 A US 1092635A US 2124254 A US2124254 A US 2124254A
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- steam
- water
- boiler
- superheated
- introducing
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F22—STEAM GENERATION
- F22B—METHODS OF STEAM GENERATION; STEAM BOILERS
- F22B1/00—Methods of steam generation characterised by form of heating method
- F22B1/02—Methods of steam generation characterised by form of heating method by exploitation of the heat content of hot heat carriers
- F22B1/08—Methods of steam generation characterised by form of heating method by exploitation of the heat content of hot heat carriers the heat carrier being steam
- F22B1/14—Methods of steam generation characterised by form of heating method by exploitation of the heat content of hot heat carriers the heat carrier being steam coming in direct contact with water in bulk or in sprays
- F22B1/146—Loffler boilers
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F22—STEAM GENERATION
- F22B—METHODS OF STEAM GENERATION; STEAM BOILERS
- F22B1/00—Methods of steam generation characterised by form of heating method
- F22B1/02—Methods of steam generation characterised by form of heating method by exploitation of the heat content of hot heat carriers
- F22B1/08—Methods of steam generation characterised by form of heating method by exploitation of the heat content of hot heat carriers the heat carrier being steam
- F22B1/14—Methods of steam generation characterised by form of heating method by exploitation of the heat content of hot heat carriers the heat carrier being steam coming in direct contact with water in bulk or in sprays
Definitions
- the invention relates to high pressure steam generators with boiler drums and to the generation of steam by injecting into the water to be evaporated superheated steam which preferably is maintained in circulation.
- the object of the invention is to effect a material increase in the capacity of such boilers in excess of normal load and to reduce the cost of high peak loads.
- the superheated steam is preferably divided in dependence upon the consumption of steam from the boiler of a suitable magnitude indicative thereof, and in the culation the division ence upon the quantity p case of boilers with steam cirmay be effected in dependassing through the circulating pump.
- This regulation is advantageously effected in such manner load of the system, the steam introduced into boiler drums is maintained constant and the admixture of superheated steam with the feed water flowing to the boiler drums is not commenced until the load exceeds the normal load.
- the resulting distribution of then preferably also upon the quantity of the superheated steam is controlled in dependence feed water flowing into the boiler or a magnitude dependent thereon, in such manner that independently of the values of other magnitudes, the quantity of superheated steam admixed boiler drums cannot The capacity in excess with the feed water prior to entering the exceed a certain upper limit.
- Figure 1 is a diagrammatic view illustrating the invention
- Figure 2 is an enlarged cross sectional view of a valve.
- I is the heating surface system includboilers. ing the steam superheater 2 and the feedwater preheater 3 heated bythe burner 4, 5 is the boiler drum and 6 the steam circulating 'pump of the Lofiler system.
- I is the superheated steam conduit leading to the water space of the boiler drum 5 and 8 is the conduit-through which the working steam is drawn off.
- the feed water which the pump 9 conveys through the preheater 3 is introduced into the boiler drum; 5 through the conduits I0 and II.
- the conduit II terminates in a distributor tube I2 in the steam-space of the boiler drum 5.
- a secondsuperheated steam conduit I3 with regulating device I4 which leads to the conduit II and thus to the steam space of the boiler drum 5.
- the feed water conduit Ill terminates in a sprinkler I5 or the like which allows the feed water to enter the conduit I I in finely divided form.
- the part of the superheated steam controlled by the regulating device I4 mixes with the feed water at this point and in fact with the entire quantity of the feed water and evaporates a corresponding part thereof. The resultant water-steam mix-.
- the regulating member I4 is most simply and conveniently constructed-as a valve which commences to open under the reduced pressure 00- normal load is exceeded and then continues to open in dependence uponthe pressure difference so that the entire quantity of superheated. steam requisite as heating medium for producing the quantity of steam in excess of the normal load, passes into the conduit I3. the boiler operates purely on the Lofller principle. and above normalload the entire quantity of steam in excess of normal load is generated from the feed water prior to entering the boiler drum 5.
- the setting of the regulating member I4 is also supervised by the member I! which responds to the temperature in the conduit I I, more particularly on exceeding the saturated steam temperature at which said mem-.
- ber I1 is preferably preliminarily set, in such Up to normal load manner that independently of the adjustment in dependence upon other magnitudes, the part of the superheated steam passing through the conduit l3 cannot exceed an upper limit at any time and the conduit I3 is completely shut 01f if no feed water is introduced.
- a method for producing high pressure steam by introducing superheated and more particularly circulated superheated steam serving as a heat carrier into the water to be evaporated in boiler drums consisting in dividing the superheated steam, introducing one part into the Water space of the boiler drums, mixing the other part with feed water in 'such proportion that a production of steam takes place and introducing the mixture into the steam space of the boiler drums.
- a method for producing high pressure steam by introducing superheated and more particularly circulated superheated steam serving as a heat carrier into the water to be evaporated in boilerdrums consisting in dividing the superheated steam, introducing one part into thewater space of the boiler drums, mixing the other part with the feed water in such proportion that a mixture of water and steam is produced and introducing this mixture of water and steam into the steam space of the boiler drums.
- a method for producing high pressure steam by introducing superheated and more particularly circulated superheated steam serving as a heat carrier into the water to be evaporated in boiler drums consisting in dividing the superheated steam, introducing one part into the water space of the boiler drums, mixing the other part with the total amount of the feed water before its entry into the boiler drums, this part of the superheated steam being so dimensioned, that a production of steam takes place, and introducing the produced mixture of Water and steam into the steamspace of the boiler drums.
- a method for producing high pressure steam by introducing superheated and more particularly circulated superheated steam serving as a heat carrier into the water to be evaporated in boiler drums consisting in dividing the superheated steam, introducing one part into the water space of the boiler drums, mixing the other part with the feed water in such proportion that a mixture of water and steam is produced, introducing this mixture into the steam space of the boiler drums and at boiler ratings above normal load, keeping that part of the superheated steam constant, which is introduced into the water space of the boiler drums.
- a method for producing high pressure steam by introducing superheated and more particularly circulated superheated steam serving as a heat carrier into the water to be evaporated in boiler drums consisting in dividing the superheated steam, introducing one part into the water space of the boiler drums, mixing the other controllable part with the feed water in such proportion that a mixture of Water and steam is produced and introducing this mixture of water and steam into the steam space of the boiler drums.
- a method for producing high pressure steam by introducing superheated and more particularly circulated superheated steam serving as a heat carrier into the Water to be evaporated in boiler drums consisting in dividing the superheated steam, introducing one part into the Water space of the boiler drums, mixing the other controllable part with the feed water in such proportion that a mixture of steam and water is produced, introducing this mixture into the steam space of the boiler drums and at boiler ratings above normal load, keeping that part of the superheated steam constant, which is introduced into the water space of the boiler drums.
- a method for producing high pressure steam by introducing superheated and more particularly circulated superheated steam serving as a heat carrier into the water to be evaporated in boiler drums consisting in dividing the superheated steam in cases of excessive load introducing that part of the superheated steam, which is requisite as heating medium for generating the normal load portion of the useful steam, into the water space of the boiler drums, mixing the other part with the feed water in such proportion that a mixture of steam and water is produced and introducing this mixture of water and steam into the steam space of the boiler drums.
- a method for producing high pressure steam by introducing superheated and more particularly circulated superheated steam serving as a heat carrier into the boiler drums consisting in dividing the superheated steam, at a certain pre determined pressure, introducing one part of the same into the water space of the boiler, introducing the other part divided off at a certain predetermined pressure into a space for admixture with feed water before its entry into the boiler drums in such proportion that a production .of
- a method for producing high pressure steam by introducing superheated circulated steam into the water to be evaporated in boiler drums consisting in dividing off a part of the superheated steam by a controlling element opening at a predetermined steam pressure, admixing the same with feed water in such a manner that a mixture of water and steam is produced, introducing this mixture into the steam space of the boiler drums and introducing the remaining quantity of the superheated steam into the water space of the boiler drums.
Description
July 19, 1938. M. LEblNEGC; I 2,124,254
METHOD OF HIGH PRESSURE. STEAM GENERATION Filed March 13, 1955 Patented July 19, 1
PATENT oFFicE METHOD OF HIGH PRESSURE STEAM GENERATION Max Ledinegg, Mahrisch-Ostrau, Czechoslovakia Application The invention relates to high pressure steam generators with boiler drums and to the generation of steam by injecting into the water to be evaporated superheated steam which preferably is maintained in circulation. The object of the invention is to effect a material increase in the capacity of such boilers in excess of normal load and to reduce the cost of high peak loads.
constructing boilers for In accordance with the invention, this object is attained by means of the method of generating steam which is described below.
Only a part of the superheated steam serving as heating medium is mtroduced into the water space of the boiler drums.
preferably is regulable, is mixed with The other part, which the feed water before the latter enters the boiler drums and the resulting water-steam mixture is in troduced into the steam space of the boiler drums. The superheated steam is preferably divided in dependence upon the consumption of steam from the boiler of a suitable magnitude indicative thereof, and in the culation the division ence upon the quantity p case of boilers with steam cirmay be effected in dependassing through the circulating pump. This regulation is advantageously effected in such manner load of the system, the steam introduced into boiler drums is maintained constant and the admixture of superheated steam with the feed water flowing to the boiler drums is not commenced until the load exceeds the normal load. The resulting distribution of then preferably also upon the quantity of the superheated steam is controlled in dependence feed water flowing into the boiler or a magnitude dependent thereon, in such manner that independently of the values of other magnitudes, the quantity of superheated steam admixed boiler drums cannot The capacity in excess with the feed water prior to entering the exceed a certain upper limit.
of normal load can be still further increased by introducing the mixture obtained from the entire quantity of the feed water and the corresponding part of the superheated. steam into the boiler drums so. as to be distributed over the entireextent of the water surface.
Figure 1 is a diagrammatic view illustrating the invention, and
Figure 2 is an enlarged cross sectional view of a valve.
shown by way of examp 1e as applied to Loiiler that above the normalquantity of superheated the water space of the March 13, 1935, Serial No. 10,926. Germany March 15, 1934 12 Claims. (01. 122 m.
I is the heating surface system includboilers. ing the steam superheater 2 and the feedwater preheater 3 heated bythe burner 4, 5 is the boiler drum and 6 the steam circulating 'pump of the Lofiler system. I is the superheated steam conduit leading to the water space of the boiler drum 5 and 8 is the conduit-through which the working steam is drawn off. The feed water which the pump 9 conveys through the preheater 3 is introduced into the boiler drum; 5 through the conduits I0 and II. The conduit IIterminates in a distributor tube I2 in the steam-space of the boiler drum 5. Connected in parallel with the superheated steam conduit 1 leading to the boiler drum 5 is a secondsuperheated steam conduit I3 with regulating device I4 which leads to the conduit II and thus to the steam space of the boiler drum 5. At the junction of this superheated steam conduit I3 with the conduit II the feed water conduit Ill terminates in a sprinkler I5 or the like which allows the feed water to enter the conduit I I in finely divided form. The part of the superheated steam controlled by the regulating device I4 mixes with the feed water at this point and in fact with the entire quantity of the feed water and evaporates a corresponding part thereof. The resultant water-steam mix-. ture is introduced into the steam space of the boiler drum 5 through the conduit II and there is sprayed on the water surface over the entire extent thereof from the tube l2 through corresponding nozzles or the like. The water then passes to the water space and the steam together with the steam generated in the drum 5 is again drawn off by the circulating pump 6.
The regulating member I4 is most simply and conveniently constructed-as a valve which commences to open under the reduced pressure 00- normal load is exceeded and then continues to open in dependence uponthe pressure difference so that the entire quantity of superheated. steam requisite as heating medium for producing the quantity of steam in excess of the normal load, passes into the conduit I3. the boiler operates purely on the Lofller principle. and above normalload the entire quantity of steam in excess of normal load is generated from the feed water prior to entering the boiler drum 5.
As indicated by the conduit I6, the setting of the regulating member I4 isalso supervised by the member I! which responds to the temperature in the conduit I I, more particularly on exceeding the saturated steam temperature at which said mem-. ber I1 is preferably preliminarily set, in such Up to normal load manner that independently of the adjustment in dependence upon other magnitudes, the part of the superheated steam passing through the conduit l3 cannot exceed an upper limit at any time and the conduit I3 is completely shut 01f if no feed water is introduced.
By means of this new method it is attained that the boiler drums, which as is known represent a very considerable portion of the cost of manufacture of the boiler, no longer need to be dimensioned in accordance with the maximum capacity of the boiler but only for a fraction thereof. With the mode of control set forth the boiler drums need be dimensioned only for the normal load on the boiler. In spite of the normal load being exceeded, the load on the water surface in the boiler drums does not increase. At the same time all advantages of steam generation with superheated steam as heating medium are retained. In particular in the case of Lofiler boilers the purity of the steam generated is not detrimentally affected. In that in accordance with the invention only part of the superheated steam is mixed with a large quantity or the entire quantity of the feed water for evaporation outside the boiler drums, no impurities can pass from the water into the steam, because the water is in great excess in comparison with the steam so that the impurities remain in the water Where they merely accumulate correspondingly. At the same time a very rapid cooling of the superheated steam is ensured.
The reduction in size of the boiler drums permitted by the present method, affords a material economy in space and weight.
Throughout the specification diverse variations have been set forth; this invention is not to be limited to the precise details, but is to include within the scope of the accompanying claims all such equivalent constructions as may be possible to accomplish the same results in substantially the same way.
What is claimed is:
1. A method for producing high pressure steam by introducing superheated and more particularly circulated superheated steam serving as a heat carrier into the water to be evaporated in boiler drums consisting in dividing the superheated steam, introducing one part into the Water space of the boiler drums, mixing the other part with feed water in 'such proportion that a production of steam takes place and introducing the mixture into the steam space of the boiler drums.
2. A method for producing high pressure steam by introducing superheated and more particularly circulated superheated steam serving as a heat carrier into the water to be evaporated in boilerdrums consisting in dividing the superheated steam, introducing one part into thewater space of the boiler drums, mixing the other part with the feed water in such proportion that a mixture of water and steam is produced and introducing this mixture of water and steam into the steam space of the boiler drums.
3. A method for producing high pressure steam by introducing superheated and more particularly circulated superheated steam serving as a heat carrier into the water to be evaporated in boiler drums consisting in dividing the superheated steam, introducing one part into the water space of the boiler drums, mixing the other part with the total amount of the feed water before its entry into the boiler drums, this part of the superheated steam being so dimensioned, that a production of steam takes place, and introducing the produced mixture of Water and steam into the steamspace of the boiler drums.
4. A method for producing high pressure steam by introducing superheated and more particularly circulated superheated steam serving as a heat carrier into the water to be evaporated in boiler drums consisting in dividing the superheated steam, introducing one part into the water space of the boiler drums, mixing the other part with the feed water in such proportion that a mixture of water and steam is produced, introducing this mixture into the steam space of the boiler drums and at boiler ratings above normal load, keeping that part of the superheated steam constant, which is introduced into the water space of the boiler drums.
5. A method for producing high pressure steam by introducing superheated and more particularly circulated superheated steam serving as a heat carrier into the water to be evaporated in boiler drums consisting in dividing the superheated steam, introducing one part into the water space of the boiler drums, mixing the other controllable part with the feed water in such proportion that a mixture of Water and steam is produced and introducing this mixture of water and steam into the steam space of the boiler drums.
6. A method for producing high pressure steam by introducing superheated and more particularly circulated superheated steam serving as a heat carrier into the Water to be evaporated in boiler drums consisting in dividing the superheated steam, introducing one part into the Water space of the boiler drums, mixing the other controllable part with the feed water in such proportion that a mixture of steam and water is produced, introducing this mixture into the steam space of the boiler drums and at boiler ratings above normal load, keeping that part of the superheated steam constant, which is introduced into the water space of the boiler drums.
'7. A method for producing high pressure steam by introducing superheated and more particularly circulated superheated steam serving as a heat carrier into the water to be evaporated in boiler drums consisting in dividing the superheated steam in cases of excessive load introducing that part of the superheated steam, which is requisite as heating medium for generating the normal load portion of the useful steam, into the water space of the boiler drums, mixing the other part with the feed water in such proportion that a mixture of steam and water is produced and introducing this mixture of water and steam into the steam space of the boiler drums.
v8. A method according to claim 2, in which the mixture of steam and water is sprayed onto the water level in the boiler drums.
9. A process according to claim 2 wherein the quantity of superheated steam admixed with the feed water prior to the entry into the boiler drwns is varied in proportion to the amount offeed water.
10. A process according to claim 2 wherein the quantity of superheated steam admixed with the feed water prior to the entry into the boiler drums is controllable and is corrected in proportion to the amount of fed water in such a manner that the quantity of superheated steam proportional to the feed water rating forms the upper limit.
11. A method for producing high pressure steam by introducing superheated and more particularly circulated superheated steam serving as a heat carrier into the boiler drums consisting in dividing the superheated steam, at a certain pre determined pressure, introducing one part of the same into the water space of the boiler, introducing the other part divided off at a certain predetermined pressure into a space for admixture with feed water before its entry into the boiler drums in such proportion that a production .of
steam takes place and introducing the mixture of water and steam into the steam space of the boiler drums.
12. A method for producing high pressure steam by introducing superheated circulated steam into the water to be evaporated in boiler drums consisting in dividing off a part of the superheated steam by a controlling element opening at a predetermined steam pressure, admixing the same with feed water in such a manner that a mixture of water and steam is produced, introducing this mixture into the steam space of the boiler drums and introducing the remaining quantity of the superheated steam into the water space of the boiler drums.
MAX LEDINEGG.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE2124254X | 1934-03-15 |
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US2124254A true US2124254A (en) | 1938-07-19 |
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US10926A Expired - Lifetime US2124254A (en) | 1934-03-15 | 1935-03-13 | Method of high pressure steam generation |
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Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2877748A (en) * | 1955-06-27 | 1959-03-17 | Babcock & Wilcox Co | Once-through vapor generator |
US2947689A (en) * | 1953-12-03 | 1960-08-02 | Freeport Sulphur Co | Saline water heating processes and systems |
US6152085A (en) * | 1996-09-02 | 2000-11-28 | Cockerill Mechanical Industries S.A. | Method for operating a boiler with forced circulation and boiler for its implementation |
US6427636B1 (en) * | 1999-06-09 | 2002-08-06 | Alstom (Switzerland) Ltd | Method and plant for heating a liquid medium |
-
1935
- 1935-03-13 US US10926A patent/US2124254A/en not_active Expired - Lifetime
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2947689A (en) * | 1953-12-03 | 1960-08-02 | Freeport Sulphur Co | Saline water heating processes and systems |
US2877748A (en) * | 1955-06-27 | 1959-03-17 | Babcock & Wilcox Co | Once-through vapor generator |
US6152085A (en) * | 1996-09-02 | 2000-11-28 | Cockerill Mechanical Industries S.A. | Method for operating a boiler with forced circulation and boiler for its implementation |
US6427636B1 (en) * | 1999-06-09 | 2002-08-06 | Alstom (Switzerland) Ltd | Method and plant for heating a liquid medium |
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