US3018764A - Marine boiler exhibiting small variations of level - Google Patents
Marine boiler exhibiting small variations of level Download PDFInfo
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- US3018764A US3018764A US741815A US74181558A US3018764A US 3018764 A US3018764 A US 3018764A US 741815 A US741815 A US 741815A US 74181558 A US74181558 A US 74181558A US 3018764 A US3018764 A US 3018764A
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- 230000001747 exhibiting effect Effects 0.000 title description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 50
- 239000012530 fluid Substances 0.000 description 31
- 238000010438 heat treatment Methods 0.000 description 30
- 238000001704 evaporation Methods 0.000 description 4
- 239000000203 mixture Substances 0.000 description 4
- 230000000694 effects Effects 0.000 description 2
- 238000009413 insulation Methods 0.000 description 2
- 238000005192 partition Methods 0.000 description 2
- 230000007423 decrease Effects 0.000 description 1
- 230000002349 favourable effect Effects 0.000 description 1
- 239000011491 glass wool Substances 0.000 description 1
- 239000011810 insulating material Substances 0.000 description 1
- 229910001338 liquidmetal Inorganic materials 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- 238000000638 solvent extraction Methods 0.000 description 1
- 238000010408 sweeping Methods 0.000 description 1
- 230000008016 vaporization Effects 0.000 description 1
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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
- F22B1/021—Methods of steam generation characterised by form of heating method by exploitation of the heat content of hot heat carriers with heating tubes in which flows a non-specified heating fluid
Definitions
- the present invention has for its object a marine boiler specially designed so that the water levels which are established in the different parts of the boiler are of rather limited area, so that when there are changes in the list of the ship, which may reach 40 and more, the inclination resulting therefrom in these levels cannot produce any interference with the efliciency and reliability of operation of the boiler.
- the evaporating portion of the boiler is subdivided into a large number of identical elements constituted by double-circuit heat-exchanging tubes fed by the heating fluid and by the water to be vaporized, which exchange their heat in these tubes, the variations of level which are produced inside the tubes for the water to be vaporized therefore affecting only a relatively small area by reason of the large number of these tubes.
- Partitioning inside the jacket serving as an economizer for the preliminary heating of the water to be vaporized likewise enables the water levels which may be established inside the economizer to be subdivided.
- FIG. 1 is a View in elevation of a unit of the boiler.
- FIG. 2 is a cross-section through the median portion II of the boiler.
- FIG. 3 is a longitudinal section of one of the doublecircui-t heat-exchanging tubes provided inside the unit.
- FIG. 4 is a section on the line IVIV of FIG. 3.
- FIG. 5 is a section on the line VV of FIG. 1 showing the sub-headers of the heat-exchanging tubes.
- the boiler is constituted by a certain number of identical units, such as the one shown in FIG. 1.
- Each of these units comprises an outer shell a, which is preferably cylindrical and has a vertical axis, containing a large number of double-circuit heat-exchanging tubes which form the evaporating portion of the boiler.
- the number of these tubes inside the shell 11 in the example shown is about sixty and they have a length adapted to the power of the boiler.
- a heat-insulating material, such as glass wool or some other material, is packed between them to reduce the internal air currents circulating between the tubes.
- Each of the latter is constituted, as shown in section in FIG. 3, by an outer tube b, the wall of which may be smooth or comprise corrugations c, as shown in the left-hand part of FIG.
- the heating fluid B may either be water under high pressure. or a gas, or a liquid metal.
- the fluid enters each unit 'a throu h the inlet nine f supplying a feeder he d g at the top, into which feeder head there are inserted in the form of a cross four subheaders, such as shown at h, from which there depart the tubes such as shown at i, feeding each tube 11 of the evaporator at the top.
- the tubes 1' are connected in similar manner to sub-headers k arranged in the form of a cross and terminating at a feeder head I from which 3,018,764 Patented Jan 30 1962 the outlet pipe in for the hot fluid departs, the outlet pipe leaving the shell a at n after making a turn permitting expansion.
- Thewater is admitted into the shell a through the connection 0, which feeds a double jacket q surrounding the shell a externally, and the space between the jacket q and the shell a, which space is preferably partitioned at r, constitutes a heat insulation and, if necessary a first economizer heating the feed water.
- the annular space between the jacket q and the shell a is connected at the bottom by tubes s to the bottom part of the evaporating tubes d.
- In said bottom part of the tubes d there are provided slightly constricted inlet orifices t having helical ribs u, the eflect of which is to give the water entering in the direction of the arrows A a gyratory movement.
- the constriction has the elfect of injecting the water under pressure irrespective of the angular position which may be adopted by the device as a result of the rocking of the ship.
- each tube d is provided internally with a core 1 comprising helical rib devices 2 and the assembly formed by this lower part of the tube d functions as an economizer for first heating the water entering the tube and bringing it to the desired temperature.
- a core 1 comprising helical rib devices 2
- the assembly formed by this lower part of the tube d functions as an economizer for first heating the water entering the tube and bringing it to the desired temperature.
- the part of the tube functioning as an evaporator.
- surfaces devices a in the form of a spiral, the pitch of which preferably continually decreases in theascending direction of the tube d and the effect of which is to impart a gyratory movement to the rising mass of water and steam.
- the water is conveyed along the inner wall of the tube a, while the steam produced rises along the axis of the tube where the helical deflecting surfaces come to an end, before being released at the top of the tube d.
- the gyratory movement likewise stabilizes the water level inside the tube.
- the steam-evacuating pipe y penetrates somewhat deeply into the tube d and its end is perforated like a sprinkler or has slots v as can be seen in FIG. 3, so as to form a device acting as a water and steam separator.
- Each of the pipes v is connected to sub-headers w arranged in the form of a cross and terminating at a central feeder head x, from which the steam leaves through the double pipe y, which describes a turn facilitating expansion, before leaving the shell a and being conducted to the place of use.
- each exchanger tube d there is also provided a device enabling anywater not yet vaporized to be absorbed, the water being conveyed through a pipe 3 to a water and steam separator 4 common to all the tubes of a unit a. for example.
- the steam leaving the circuits y of all the units a may also pass through a supplementary general water and steam separator formed by a dome of known type (not shown) before reaching the turbine.
- the partitions r which are provided between the jacket q and the shell a have the eifect of dividing the water space acting as a heat insulation into cornpartments and, when changes are produced in the list of the ship, the resultant inclinations in the level are limited to each of the compartment provided between the partitions r and consequently atfect only a limited area of water, so that the effect of the inclination is limited equally.
- the fins e of the tube d may be slit at z and turned down, as can be seen at 2 (FIG. 4), so that the hot fluid, circulating in the space between the two tubes b and d divided into compartments by the fins e, passes from time to time from the space between two adjacent fins e to the neighboring space, which ensures a powerful sweeping action on the fins and on the outer surface of the tube d, thus securing a better exchange of heat.
- a marine boiler effective to undergo only small variations of water level in response to movements of the ship in which it is mounted comprising, in combination, a shell, a plurality of vertical double-circuit heatexchanging tubes disposed in said shell and adapted to be fed by the heating fluid and by the water to be vaporized, each heat-exchanging tube comprising a single unidirectional inner tube and an outer coaxial tube defining an annular space between them providing a flow passage for the heating fluid, the inner tube being formed with an inlet at its lower end to receive the water to be vaporized and the outer tube being formed with an inlet at its upper end to receive the heating fluid and an outlet at its lower end for evacuation of said heating fluid, said heating fluid thereby being adapted to enter said outer tube at its upper end, to circulate through said annular space between the two coaxial tubes and to leave said outer tube at its lower end, means providing helical surfaces interiorly of the inner tube to impart a gyratory movement to the mixture of water and steam contained in the inner tube, and steam outlet means in the upper portion
- a marine boiler effective to undergo only small variations of water level in response to movements of the ship in which it is mounted comprising, in combination, a shell, a plurality of vertical double-circuit heat-exchanging tubes disposed in said shell and adapted to be fed by the heating fluid and by the water to be vaporized, each heat-exchanging tube comprising a single unidirectional inner tube and an outer coaxial tube defining an annular space between them providing a flow passage for the heating fluid, the inner tube being formed with an inlet at its lower end to receive the water to be vaporized and the outer tube being formed with an inlet at its upper end to receive the heating fluid and an outlet at its lower end for evacuation of said heating fluid, said heating fluid thereby being adapted to enter said outer tube at its upper end, to circulate through said annular space between the two coaxial tubes and to leave said outer tube at its lower end, means providing helical surfaces interiorly of the inner tube to impart a gyratory movement to the mixture of water and steam contained in the inner tube, and steam outlet means in the upper
- a marine boiler as defined in claim 1, wherein said separator of steam and water comprises a steam discharge tube extending coaxially into each inner tube, said steam discharge tube being formed with a plurality of apertures for receiving the steam.
- a marine boiler as defined in claim 2, wherein said separator of steam and water comprises a steam discharge tube extending coaxially into each inner tube, said steam discharge tube being formed with a plurality of apertures for receiving the steam.
- a marine boiler effective to undergo only small variations of water level in response to movements of the ship in which it is mounted comprising, in combination, a shell, a plurality of vertical double-circuit heatexchanging tubes disposed in said shell and adapted to be fed by the heating fluid and by the water to be vaporized, each heat-exchanging tube comprising a single unidirectional inner tube and an outer coaxial tube defining an annular space between them providing a flow passage for the heating fluid, the inner tube being formed with an inlet at its lower end to receive the water to be vaporized and the outer tube being formed with an inlet at its upper end to receive the heating fluid and an outlet at its lower end for evacuation of said heating fluid, said heating fluid thereby being adapted to enter said outer tube at its upper end, to circulate through said annular space between the two coaxial tubes and to leave said outer tube at its lower end, means providing helical surfaces interiorly of the inner tube to impart a gyratory movement to the mixture of water and steam contained in the inner tube, and steam outlet means in the upper portion
- a marine boiler effective to undergo only small variations of water level in response to movements of the ship in which it is mounted comprising, in combination, a shell, a plurality of vertical double-circuit heatexchanging tubes disposed in said shell and adapted to be fed by the heating fluid and by the water to be vaporized, each heat-exchanging tube comprising a single unidirectional inner tube and an outer coaxial tube defining an annular space between them providing a flow passage for the heating fluid, the inner tube being formed with an inlet at its lower end to receive the water to be vaporized and the outer tube being formed with an inlet at its upper end to receive the heating fluid and an outlet at its lower end for evacuation of said heating fluid, said heating fluid thereby being adapted to enter said outer tube at its upper end, to circulate through said annular space between the two coaxial tubes and to leave said outer tube at its lower end, means providing helical surfaces interiorly of the inner tube to impart a gyratory move: ment to the mixture of water and steam contained in the inner tube, and steam outlet means in
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Description
Jan. 30, 1962 A. HUET 3,018,764
MARINE BOILER EXHIBITING SMALL VARIATIONS OF LEVEL Filed June 13, 1958 INYENTOR. ANDRE HUET his ATTORNEY United States Patent Claims The present invention has for its object a marine boiler specially designed so that the water levels which are established in the different parts of the boiler are of rather limited area, so that when there are changes in the list of the ship, which may reach 40 and more, the inclination resulting therefrom in these levels cannot produce any interference with the efliciency and reliability of operation of the boiler.
To this end, the evaporating portion of the boiler is subdivided into a large number of identical elements constituted by double-circuit heat-exchanging tubes fed by the heating fluid and by the water to be vaporized, which exchange their heat in these tubes, the variations of level which are produced inside the tubes for the water to be vaporized therefore affecting only a relatively small area by reason of the large number of these tubes.
Partitioning inside the jacket serving as an economizer for the preliminary heating of the water to be vaporized likewise enables the water levels which may be established inside the economizer to be subdivided.
Other details of the boiler forming the object of the invention will appear in the course of the following description given with reference to the drawings, which are given by way of example.
FIG. 1 is a View in elevation of a unit of the boiler.
FIG. 2 is a cross-section through the median portion II of the boiler.
FIG. 3 is a longitudinal section of one of the doublecircui-t heat-exchanging tubes provided inside the unit. FIG. 4 is a section on the line IVIV of FIG. 3.
FIG. 5 is a section on the line VV of FIG. 1 showing the sub-headers of the heat-exchanging tubes.
The boiler is constituted by a certain number of identical units, such as the one shown in FIG. 1. Each of these units comprises an outer shell a, which is preferably cylindrical and has a vertical axis, containing a large number of double-circuit heat-exchanging tubes which form the evaporating portion of the boiler. The number of these tubes inside the shell 11 in the example shown is about sixty and they have a length adapted to the power of the boiler. A heat-insulating material, such as glass wool or some other material, is packed between them to reduce the internal air currents circulating between the tubes. Each of the latter is constituted, as shown in section in FIG. 3, by an outer tube b, the wall of which may be smooth or comprise corrugations c, as shown in the left-hand part of FIG. 3, and into which there is inserted a tube d carrying external fins c. There is thus produced a double circuit heat-exchanging tube through which the water to be vaporized flows from bottom to top in the direction of the arrow A, while the heating fluid flows therethrough from top to bottom in the direction of the arrow B and circulates in the space contained between the two tubes b and a.
The heating fluid B may either be water under high pressure. or a gas, or a liquid metal. The fluid enters each unit 'a throu h the inlet nine f supplying a feeder he d g at the top, into which feeder head there are inserted in the form of a cross four subheaders, such as shown at h, from which there depart the tubes such as shown at i, feeding each tube 11 of the evaporator at the top.
At the bottom of the tubes b, the tubes 1' are connected in similar manner to sub-headers k arranged in the form of a cross and terminating at a feeder head I from which 3,018,764 Patented Jan 30 1962 the outlet pipe in for the hot fluid departs, the outlet pipe leaving the shell a at n after making a turn permitting expansion.
Thewater is admitted into the shell a through the connection 0, which feeds a double jacket q surrounding the shell a externally, and the space between the jacket q and the shell a, which space is preferably partitioned at r, constitutes a heat insulation and, if necessary a first economizer heating the feed water. The annular space between the jacket q and the shell a is connected at the bottom by tubes s to the bottom part of the evaporating tubes d. In said bottom part of the tubes d there are provided slightly constricted inlet orifices t having helical ribs u, the eflect of which is to give the water entering in the direction of the arrows A a gyratory movement. The constriction has the elfect of injecting the water under pressure irrespective of the angular position which may be adopted by the device as a result of the rocking of the ship.
The lower part of each tube d is provided internally with a core 1 comprising helical rib devices 2 and the assembly formed by this lower part of the tube d functions as an economizer for first heating the water entering the tube and bringing it to the desired temperature. Following this first part of the tube functioning as an economizer there is the part of the tube functioning as an evaporator. In this evaporating portion of the tube d there areprovided surfaces devices a in the form of a spiral, the pitch of which preferably continually decreases in theascending direction of the tube d and the effect of which is to impart a gyratory movement to the rising mass of water and steam. Owing to this movement, the water is conveyed along the inner wall of the tube a, while the steam produced rises along the axis of the tube where the helical deflecting surfaces come to an end, before being released at the top of the tube d. The gyratory movement likewise stabilizes the water level inside the tube. In this upper part, the steam-evacuating pipe y penetrates somewhat deeply into the tube d and its end is perforated like a sprinkler or has slots v as can be seen in FIG. 3, so as to form a device acting as a water and steam separator. Each of the pipes v is connected to sub-headers w arranged in the form of a cross and terminating at a central feeder head x, from which the steam leaves through the double pipe y, which describes a turn facilitating expansion, before leaving the shell a and being conducted to the place of use.
At the top. for example, of each exchanger tube d there is also provided a device enabling anywater not yet vaporized to be absorbed, the water being conveyed through a pipe 3 to a water and steam separator 4 common to all the tubes of a unit a. for example.
Any water which may be delivered by the pump 5 to the pipe 6 rejoins the water being fed to the shell a, while any steam which may be separated in the separator 4 rejoins the steam outlet circuit y through the pipe 8.
The steam leaving the circuits y of all the units a may also pass through a supplementary general water and steam separator formed by a dome of known type (not shown) before reaching the turbine. V 7
Moreover, it is also possible to make the steam pass through a superheater (not shown).
It will be seen that with the arrangement adopted no clearly defined water level is established inside the tubes d and that, furthermore, if such a level is established, the listing of the ship producing an inclination in these levels aifects an area of water which is so small that the functioning of the vaporizing tube is not thereby impeded.
Likewise, the partitions r which are provided between the jacket q and the shell a have the eifect of dividing the water space acting as a heat insulation into cornpartments and, when changes are produced in the list of the ship, the resultant inclinations in the level are limited to each of the compartment provided between the partitions r and consequently atfect only a limited area of water, so that the effect of the inclination is limited equally.
In the space comprised between the tubes 11 and d, the fins e of the tube d may be slit at z and turned down, as can be seen at 2 (FIG. 4), so that the hot fluid, circulating in the space between the two tubes b and d divided into compartments by the fins e, passes from time to time from the space between two adjacent fins e to the neighboring space, which ensures a powerful sweeping action on the fins and on the outer surface of the tube d, thus securing a better exchange of heat.
When a tube [1 exhibiting changes of cross-section, as shown at c on the left in FIG. 3, is used, these changes of cross-section cause changes of direction, pressure and velocity in the flow of the hot fluid and these changes are favorable to the exchange of heat. It is possible to substitute -for these corrugations c a tube [2 which is completely smooth externally and to arrange inside the space parting from the scope thereof.
What I claim is:
1. A marine boiler effective to undergo only small variations of water level in response to movements of the ship in which it is mounted comprising, in combination, a shell, a plurality of vertical double-circuit heatexchanging tubes disposed in said shell and adapted to be fed by the heating fluid and by the water to be vaporized, each heat-exchanging tube comprising a single unidirectional inner tube and an outer coaxial tube defining an annular space between them providing a flow passage for the heating fluid, the inner tube being formed with an inlet at its lower end to receive the water to be vaporized and the outer tube being formed with an inlet at its upper end to receive the heating fluid and an outlet at its lower end for evacuation of said heating fluid, said heating fluid thereby being adapted to enter said outer tube at its upper end, to circulate through said annular space between the two coaxial tubes and to leave said outer tube at its lower end, means providing helical surfaces interiorly of the inner tube to impart a gyratory movement to the mixture of water and steam contained in the inner tube, and steam outlet means in the upper portion of said inner tube for withdrawing steam directly from the upper portion of said inner tube, headers to admit the heating fluid to the inlet at the top of each of the outer tubes, headers to collect the heating fluid at the bottom of the outer tubes, tubes to admit water to the inlet at the bottom of each of the inner tubes, said steam outlet means comprising a separator of steam and water at the top of each inner tube, means to recirculate the separated water, and headers to collect the steam from said steam outlet means.
2. A marine boiler effective to undergo only small variations of water level in response to movements of the ship in which it is mounted comprising, in combination, a shell, a plurality of vertical double-circuit heat-exchanging tubes disposed in said shell and adapted to be fed by the heating fluid and by the water to be vaporized, each heat-exchanging tube comprising a single unidirectional inner tube and an outer coaxial tube defining an annular space between them providing a flow passage for the heating fluid, the inner tube being formed with an inlet at its lower end to receive the water to be vaporized and the outer tube being formed with an inlet at its upper end to receive the heating fluid and an outlet at its lower end for evacuation of said heating fluid, said heating fluid thereby being adapted to enter said outer tube at its upper end, to circulate through said annular space between the two coaxial tubes and to leave said outer tube at its lower end, means providing helical surfaces interiorly of the inner tube to impart a gyratory movement to the mixture of water and steam contained in the inner tube, and steam outlet means in the upper portion of said inner tube, headers to admit the heating fluid to the inlet at the top of each of the outer tubes, headers to collect the heating fluid at the bottom of the outer tubes, tubes to admit Water to the inlet at the bottom of each of the inner tubes, said steam outlet means comprising a separator of steam and water at the top of each inner tube, a tube to collect the Water from the separator, a second separator common to all the coaxial heat exchanging tubes, said last-named tube leading to said second separator, a tube to recirculate the water separated in said second separator, and a tube to collect the steam separated in said second separator.
3. A marine boiler as defined in claim 1, wherein said separator of steam and water comprises a steam discharge tube extending coaxially into each inner tube, said steam discharge tube being formed with a plurality of apertures for receiving the steam.
4. A marine boiler as defined in claim 2, wherein said separator of steam and water comprises a steam discharge tube extending coaxially into each inner tube, said steam discharge tube being formed with a plurality of apertures for receiving the steam.
5. A marine boiler effective to undergo only small variations of water level in response to movements of the ship in which it is mounted comprising, in combination, a shell, a plurality of vertical double-circuit heatexchanging tubes disposed in said shell and adapted to be fed by the heating fluid and by the water to be vaporized, each heat-exchanging tube comprising a single unidirectional inner tube and an outer coaxial tube defining an annular space between them providing a flow passage for the heating fluid, the inner tube being formed with an inlet at its lower end to receive the water to be vaporized and the outer tube being formed with an inlet at its upper end to receive the heating fluid and an outlet at its lower end for evacuation of said heating fluid, said heating fluid thereby being adapted to enter said outer tube at its upper end, to circulate through said annular space between the two coaxial tubes and to leave said outer tube at its lower end, means providing helical surfaces interiorly of the inner tube to impart a gyratory movement to the mixture of water and steam contained in the inner tube, and steam outlet means in the upper portion of said inner tube for withdrawing steam directly from the upper portion of said inner tube, said steam outlet means comprising a steam discharge tube extending coaxially into each inner tube, said steam discharge tube being formed with a plurality of apertures for receiving the steam.
6. A marine boiler effective to undergo only small variations of water level in response to movements of the ship in which it is mounted comprising, in combination, a shell, a plurality of vertical double-circuit heatexchanging tubes disposed in said shell and adapted to be fed by the heating fluid and by the water to be vaporized, each heat-exchanging tube comprising a single unidirectional inner tube and an outer coaxial tube defining an annular space between them providing a flow passage for the heating fluid, the inner tube being formed with an inlet at its lower end to receive the water to be vaporized and the outer tube being formed with an inlet at its upper end to receive the heating fluid and an outlet at its lower end for evacuation of said heating fluid, said heating fluid thereby being adapted to enter said outer tube at its upper end, to circulate through said annular space between the two coaxial tubes and to leave said outer tube at its lower end, means providing helical surfaces interiorly of the inner tube to impart a gyratory move: ment to the mixture of water and steam contained in the inner tube, and steam outlet means in the upper portion of said inner tube for withdrawing steam directly from the upper portion of said inner tube, and means defining corrugations on the surface of the outer tube, said separator of steam and water comprising a steam discharge tube extending coaxially into each inner tube, said steam discharge tube being formed with a plurality of apertures for receiving the steam.
1,951,403 Goddard Mar. 20, 1934 6 Noack Feb. 27, 1934 Murray Nov. 12, 1940 Schmidt Apr. 29, 1941 Stieger July 28, 1942 Sebald July 3, 1945 Rossi Feb. 26, 1952 Dunning et al. Jan. 29, 1957 Rehm June 18, 1957 FOREIGN PATENTS Great Britain Mar. 30, 1955 France Jan. 8, 1909 France May 5, 1947
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| FR3018764X | 1957-06-27 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US3018764A true US3018764A (en) | 1962-01-30 |
Family
ID=9690976
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US741815A Expired - Lifetime US3018764A (en) | 1957-06-27 | 1958-06-13 | Marine boiler exhibiting small variations of level |
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| Country | Link |
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| US (1) | US3018764A (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3116721A (en) * | 1961-02-17 | 1964-01-07 | Huet Andre | Water and steam separators for evaporators |
| US3227142A (en) * | 1961-12-11 | 1966-01-04 | Foster Wheeler Corp | Steam generator configurations |
| US3254633A (en) * | 1963-02-28 | 1966-06-07 | Babcock & Wilcox Co | Vapor generating and superheating unit |
| US3357409A (en) * | 1964-10-07 | 1967-12-12 | Atomic Energy Authority Uk | Vertical tube module once-through steam generator |
| US3431893A (en) * | 1965-11-08 | 1969-03-11 | Fives Penhoet | Single-tube forced-circulation heat transfer devices |
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|---|---|---|---|---|
| FR393877A (en) * | 1907-11-11 | 1909-01-08 | Andre Ripert | Improvements to steam boilers |
| US1948541A (en) * | 1929-12-16 | 1934-02-27 | Bbc Brown Boveri & Cie | Heater system |
| US1951403A (en) * | 1930-10-30 | 1934-03-20 | Robert H Goddard | Heat absorbing apparatus for use with solar energy |
| US2220944A (en) * | 1937-03-02 | 1940-11-12 | Jr Thomas E Murray | Furnace or boiler wall construction |
| US2240100A (en) * | 1935-07-17 | 1941-04-29 | Schmidt Martin | Water tube steam generator and parts thereof |
| US2291195A (en) * | 1938-09-06 | 1942-07-28 | Stieger George Friedrich | Steam generator of the high pressure type |
| US2379661A (en) * | 1939-06-07 | 1945-07-03 | Griscom Russell Co | High-pressure steam generator |
| FR921339A (en) * | 1942-10-09 | 1947-05-05 | Device for uniform heating of a liquid, particularly a lacquer | |
| US2587530A (en) * | 1948-03-13 | 1952-02-26 | Rossi Giovanni | Water and fire tube for steam boilers |
| GB727225A (en) * | 1953-11-04 | 1955-03-30 | Thermia Verken Ab | Improvements in or relating to calorifiers for a hot water system |
| US2779724A (en) * | 1955-04-05 | 1957-01-29 | Internat Basic Economy | High velocity film heat exchanger |
| US2796050A (en) * | 1954-04-22 | 1957-06-18 | Springfield Boiler Company | Exchanger vapor generators |
-
1958
- 1958-06-13 US US741815A patent/US3018764A/en not_active Expired - Lifetime
Patent Citations (12)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| FR393877A (en) * | 1907-11-11 | 1909-01-08 | Andre Ripert | Improvements to steam boilers |
| US1948541A (en) * | 1929-12-16 | 1934-02-27 | Bbc Brown Boveri & Cie | Heater system |
| US1951403A (en) * | 1930-10-30 | 1934-03-20 | Robert H Goddard | Heat absorbing apparatus for use with solar energy |
| US2240100A (en) * | 1935-07-17 | 1941-04-29 | Schmidt Martin | Water tube steam generator and parts thereof |
| US2220944A (en) * | 1937-03-02 | 1940-11-12 | Jr Thomas E Murray | Furnace or boiler wall construction |
| US2291195A (en) * | 1938-09-06 | 1942-07-28 | Stieger George Friedrich | Steam generator of the high pressure type |
| US2379661A (en) * | 1939-06-07 | 1945-07-03 | Griscom Russell Co | High-pressure steam generator |
| FR921339A (en) * | 1942-10-09 | 1947-05-05 | Device for uniform heating of a liquid, particularly a lacquer | |
| US2587530A (en) * | 1948-03-13 | 1952-02-26 | Rossi Giovanni | Water and fire tube for steam boilers |
| GB727225A (en) * | 1953-11-04 | 1955-03-30 | Thermia Verken Ab | Improvements in or relating to calorifiers for a hot water system |
| US2796050A (en) * | 1954-04-22 | 1957-06-18 | Springfield Boiler Company | Exchanger vapor generators |
| US2779724A (en) * | 1955-04-05 | 1957-01-29 | Internat Basic Economy | High velocity film heat exchanger |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3116721A (en) * | 1961-02-17 | 1964-01-07 | Huet Andre | Water and steam separators for evaporators |
| US3227142A (en) * | 1961-12-11 | 1966-01-04 | Foster Wheeler Corp | Steam generator configurations |
| US3254633A (en) * | 1963-02-28 | 1966-06-07 | Babcock & Wilcox Co | Vapor generating and superheating unit |
| US3357409A (en) * | 1964-10-07 | 1967-12-12 | Atomic Energy Authority Uk | Vertical tube module once-through steam generator |
| US3431893A (en) * | 1965-11-08 | 1969-03-11 | Fives Penhoet | Single-tube forced-circulation heat transfer devices |
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