US1178667A - Heat-accumulator. - Google Patents
Heat-accumulator. Download PDFInfo
- Publication number
- US1178667A US1178667A US79641813A US1913796418A US1178667A US 1178667 A US1178667 A US 1178667A US 79641813 A US79641813 A US 79641813A US 1913796418 A US1913796418 A US 1913796418A US 1178667 A US1178667 A US 1178667A
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- US
- United States
- Prior art keywords
- sand
- heat
- series
- ovens
- gases
- 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.)
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/18—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
- B01J8/1836—Heating and cooling the reactor
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28C—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA COME INTO DIRECT CONTACT WITHOUT CHEMICAL INTERACTION
- F28C3/00—Other direct-contact heat-exchange apparatus
- F28C3/10—Other direct-contact heat-exchange apparatus one heat-exchange medium at least being a fluent solid, e.g. a particulate material
- F28C3/12—Other direct-contact heat-exchange apparatus one heat-exchange medium at least being a fluent solid, e.g. a particulate material the heat-exchange medium being a particulate material and a gas, vapour, or liquid
- F28C3/14—Other direct-contact heat-exchange apparatus one heat-exchange medium at least being a fluent solid, e.g. a particulate material the heat-exchange medium being a particulate material and a gas, vapour, or liquid the particulate material moving by gravity, e.g. down a tube
Definitions
- My invention relates particularly to that form of accumulatorin which the vheat is stored up by means of minute particles, such as sand.
- the present invention comprises a system which has a large thermal capacity, and also readily gives up its heat.
- the action of the accumulator can also be made continuous or alternating.
- the apparatus shown in the drawings is a continuous apparatus. However,it may be made alternating by separating the lower half.
- Figure 1 is a vertical longitudinal section of the apparatus
- Fig. 2 is a vertical longitudinal section of is a verticaltransverse section of a fragment of the apparatus showing a dierent arrangement of pipes connecting the ovens
- Fig. 4 is a vertical transverse section of a fragment of the apparatus shown in Fig. 1.
- Fig. 5 is a vertical transverse section of a fragment of the apparatus showing the sand pipes in stillanother relation.
- Fig. 6 is a horizontal section of the floor of an oven.
- the apparatus comprises two superposed series of ovens, each series having a plurality of ovens arranged vertically.
- the upper series serves to absorb heat from the gaseous products of combustion and the lower series serves to heat the cold air admitted.
- the number of ovens is immaterial, and they may be divided in any proportion.
- a chamber Q beneath the lowest oven, and a chamber O above the uppermost oven, which serve to hold the sand.
- 'Between the eleventh and twelfth oven is a similar chamber P, which serves to hold a larger ⁇ part of the sand, and separates the upper part of the battery from the lower part, the sand operating as a closure, as well as a heat transferring medium.
- the sand also serves as an automatic valve in the con- Specication of Letters Eatent.
- a conveyer such as an Archimedean screw W, which carries the sand to an elevator of any suitable type such as an Archiniedean screw in pipe F that raises it to a sifting and cleanslng means V of any suitable type, which is preferably above the accumulator.
- This sifting and cleansing means which is fed by means of pipe S and hopper E frees the sand from dust and coarse impurities, so that the sand is carried to the uppermost chamber O, while the dust and impurities are removed.
- the location of this sifting and cleansing means, as well as the character of the elevating means, may be varied.
- the distance of the ends of these pipes from the bottom of the oven underneath depends on 'the following considerations: If sand is of the sand stops.
- the length of the pipes and the distance between the bottoms of the ovens is so calculated, so that too much sand does not cover these oven-bottoms, and there is enough room to permit the passage of the gasesv Aover the sand, so as to permit an effective contact of the gases with the sand.
- the workings lof the system are as follows: When theaccumulator is empty, the sand falls from above through the entire ap paratus. First of all, the lowermost chamthe one containing the Archimedean screw has been reached the iow of sand to the low,-
- the hot gases are led in through C. These hot gases are either by-products or the d1- rect results of combustion. These gases flow through the upper eleven ovens, by means of the lateral. openings M shown, until. they emerge through the pipe D. The sand 1n the accumulator rapidly abstracts the heat of the gases, so that the gases leaving D are cooled. These heated gases must sweep through the upper eleven chambers, as the draft is so arranged, and besides, the chamber P between the upper and lower parts of the battery, which containsa large amount of sand, acts as a closure or valve, and does not permitany descent of the heated gases.
- the air to be warmed is allowed to enter, by means of A, into the battery of the lower eleven ovens, )asses through them, as above explained, an emerges in a heated condition through B.
- the upper battery 1s traversed by hot gases, whereby the sand therein is heated.
- the lower battery of ovens, which are traversed by the air to be warmed, would, however, not be changed without further action.- If, however,.the Archimedean screw W andthe elevator are operated, all the sand in the apparatus is set into'motion, the very warm sand of the upper battery of ovens enters the lower battery, whereby the air traversing the lower battery is heated at the expense of the heat of the sand, which has entered from the upper'battery. This sand is thereby cooled and is cold when it enters the chamber connected to the Archimedean screw.
- the sand which has been uppermost in one oven will be lowermost in the tive communication of this heat to the air.
- sand Other materials may be used instead of sand, as for instance, pulverized fire brick, or pebbly or basic substances, etc.
- the streaming of the sand may be checked or controlled by mechanical means.
- a series of super posed and communicating receptacles means l0@ for passing minute i refractory particles through said receptacles, means for heating said particles while they pass through said receptacles, 'and means for cleansing said particles of. dust and impurities, during the 105 movement thereof.
- a series of superposed and communicating receptacles means for passing minute refractory ,particles through said receptacles, a second series of 11@ superposed communicating receptacles underneath said firstseries, a large chamber intermediate said first and second series and communicating with both of said series, means for passing minute refractory parti- 115 cles through said first series into said intermediate chamber, and from said intermediate chamber into said second series, and means for passing gases into and out of each said series of chambers separately.
- a series of superposed and communicating receptacles means for passing minute refractory particles through said receptacles, a second series of superposed communicating receptacles un- 1255 derneath said first series, a large chamber intermediate said first and second series and communicating with both of said series, means for passing minute refractory particles through said first series into said interl5@ length of said pipes intermediate said re ceptacles being less than the distance intcrmediate said receptacles.
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- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Combustion & Propulsion (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Road Paving Machines (AREA)
Description
. H. NIEWERTH. -HEAT ACCUMULATOR.
APPLlcATloNHLED ocT. 2|. 1913.
1478,66?. Patented Apr. 11, 1916;
HERMANN NIEWEBTH, OF BERLIN', GERMANY.
HEAT-ACCUMULATOR.
To all whom t may concern Be it known that I, HERMANN NIEWERTH, a citizen of the German Empire, residing in Berlin, in said German Empire, have invented a new and useful Improvement inq Heat-Accumulators, of which the following is a description.
My invention relates particularly to that form of accumulatorin which the vheat is stored up by means of minute particles, such as sand.
The present invention comprises a system which has a large thermal capacity, and also readily gives up its heat. The action of the accumulator can also be made continuous or alternating.
The apparatus shown in the drawings is a continuous apparatus. However,it may be made alternating by separating the lower half.
Figure 1 is a vertical longitudinal section of the apparatus, Fig. 2 is a vertical longitudinal section of is a verticaltransverse section of a fragment of the apparatus showing a dierent arrangement of pipes connecting the ovens. Fig. 4 is a vertical transverse section of a fragment of the apparatus shown in Fig. 1. Fig. 5 is a vertical transverse section of a fragment of the apparatus showing the sand pipes in stillanother relation. Fig. 6 is a horizontal section of the floor of an oven.
The apparatus comprises two superposed series of ovens, each series having a plurality of ovens arranged vertically. In the drawings twenty two ovensare shown, eleven in each series. The upper series serves to absorb heat from the gaseous products of combustion and the lower series serves to heat the cold air admitted. The number of ovens is immaterial, and they may be divided in any proportion.
There is a chamber Q, beneath the lowest oven, and a chamber O above the uppermost oven, which serve to hold the sand. 'Between the eleventh and twelfth oven is a similar chamber P, which serves to hold a larger` part of the sand, and separates the upper part of the battery from the lower part, the sand operating as a closure, as well as a heat transferring medium. The sand also serves as an automatic valve in the con- Specication of Letters Eatent.
a fragment thereof, Fig. 3`
ber Q,
Patented Apr. 11, 1916.
Appli-cation led October 21, 1918. Serial No. 796,418.
ltaining ovens. This is a very important feature of the system. y
In the chamber beneath the lowermost ovenis a conveyer, such as an Archimedean screw W, which carries the sand to an elevator of any suitable type such as an Archiniedean screw in pipe F that raises it to a sifting and cleanslng means V of any suitable type, which is preferably above the accumulator. This sifting and cleansing means which is fed by means of pipe S and hopper E frees the sand from dust and coarse impurities, so that the sand is carried to the uppermost chamber O, while the dust and impurities are removed. The location of this sifting and cleansing means, as well as the character of the elevating means, may be varied.
The vertically arranged voven-bottoms vare perforated in a regular manner yfor pipes L, which project to a given distance from the bottom of the oven underneath. The distance of the ends of these pipes from the bottom of the oven underneath depends on 'the following considerations: If sand is of the sand stops. The length of the pipes and the distance between the bottoms of the ovens is so calculated, so that too much sand does not cover these oven-bottoms, and there is enough room to permit the passage of the gasesv Aover the sand, so as to permit an effective contact of the gases with the sand.
The workings lof the system are as follows: When theaccumulator is empty, the sand falls from above through the entire ap paratus. First of all, the lowermost chamthe one containing the Archimedean screw has been reached the iow of sand to the low,-
W, will be filled. When this point ermost chamber Q, will cease; and the lowest oven will be filled in the manner previously described. This goes on until the entire apparatus is filled with sand. Then the movement of sand ceases. When the Archi- `medean screw W and the elevator are operated, a renewed movement of the sand will result, proportionate to the rate of movement of.' the screw. The screw W and the elevator thus regulate the rapidity of the action of the apparatus.
The hot gases are led in through C. These hot gases are either by-products or the d1- rect results of combustion. These gases flow through the upper eleven ovens, by means of the lateral. openings M shown, until. they emerge through the pipe D. The sand 1n the accumulator rapidly abstracts the heat of the gases, so that the gases leaving D are cooled. These heated gases must sweep through the upper eleven chambers, as the draft is so arranged, and besides, the chamber P between the upper and lower parts of the battery, which containsa large amount of sand, acts as a closure or valve, and does not permitany descent of the heated gases.
Now the air to be warmed is allowed to enter, by means of A, into the battery of the lower eleven ovens, )asses through them, as above explained, an emerges in a heated condition through B. The upper battery 1s traversed by hot gases, whereby the sand therein is heated. The lower battery of ovens, which are traversed by the air to be warmed, would, however, not be changed without further action.- If, however,.the Archimedean screw W andthe elevator are operated, all the sand in the apparatus is set into'motion, the very warm sand of the upper battery of ovens enters the lower battery, whereby the air traversing the lower battery is heated at the expense of the heat of the sand, which has entered from the upper'battery. This sand is thereby cooled and is cold when it enters the chamber connected to the Archimedean screw.
If the screw and elevator are properly regulated, as well as the passage of the hot and the cool gases, then there is cold sand and cold air near A, for the temperature of the sand rises and is highest at B, as well as the temperature of the air. The sand at A, however, has given its heat to the blast of air. The reverse condition prevails at C. The sand adjacent thereto in the uppermost part is the warmest, and is coldest at D, where the heated gases emerge, so that the heat of the gases is used effectively. The outwardlyy emerging cooled sand is raised by the elevator, and used again. Cold air enters at A and leaves the apparatus at B highly heated, while heated gases enter at C andleave the apparatus at D in a cooled condition. This is the ideal cycle for continuous operation.
As the pipes through which the sand streams are preferably arranged one above the. other, the sand which has been uppermost in one oven will be lowermost in the tive communication of this heat to the air.
oven beneath. This permits a long use of the sand and the rapid and effective abstraction of the heat of the heated gases, and, on the other hand, a rapid and effec- Through the streaming and agitation of the sand the creation of a crust is prevented. Impurities which enter the sand in spite of this, are removed by the sieve and cleansing means.
In Fig. 3 the pipes L through which the sand falls from one oven to another are bent below the horizontal partitions, in some of the ovens their bent ends projecting toward each other and in other ovens away from each other whereby the sand is differently distributed in the respective ovens.
VIn Fig. 5 the sand pipes L2 connecting the ovens are vertical but disposed in staggered relation.
Other materials may be used instead of sand, as for instance, pulverized fire brick, or pebbly or basic substances, etc.
If continuous operation is not desired, the lower' part of the apparatus is removed, and a correspondingly greater number of pieces of apparatus are set up, so that their action can be reversed.
In accumulators to be operated at stated periods, the streaming of the sand may be checked or controlled by mechanical means.
What I claim and desire to secure by Letters Patent is:
l. In a heat accumulator, a series of super posed and communicating receptacles, means l0@ for passing minute i refractory particles through said receptacles, means for heating said particles while they pass through said receptacles, 'and means for cleansing said particles of. dust and impurities, during the 105 movement thereof. l
2. In a heat accumulator, a series of superposed and communicating receptacles, means for passing minute refractory ,particles through said receptacles, a second series of 11@ superposed communicating receptacles underneath said firstseries, a large chamber intermediate said first and second series and communicating with both of said series, means for passing minute refractory parti- 115 cles through said first series into said intermediate chamber, and from said intermediate chamber into said second series, and means for passing gases into and out of each said series of chambers separately.
3. In a heat accumulator, a series of superposed and communicating receptacles, means for passing minute refractory particles through said receptacles, a second series of superposed communicating receptacles un- 1255 derneath said first series, a large chamber intermediate said first and second series and communicating with both of said series, means for passing minute refractory particles through said first series into said interl5@ length of said pipes intermediate said re ceptacles being less than the distance intcrmediate said receptacles.
l AIn testimony that I claim the foregoing as myvinvention, I have signed my name in presence of two subscribing Witnesses.
HERMANN NIEWERTH.
Witnesses I WOLDEMAR HAUPT, HENRY I-IASPER.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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US79641813A US1178667A (en) | 1913-10-21 | 1913-10-21 | Heat-accumulator. |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
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US79641813A US1178667A (en) | 1913-10-21 | 1913-10-21 | Heat-accumulator. |
Publications (1)
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US1178667A true US1178667A (en) | 1916-04-11 |
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US79641813A Expired - Lifetime US1178667A (en) | 1913-10-21 | 1913-10-21 | Heat-accumulator. |
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Cited By (18)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2417049A (en) * | 1943-10-18 | 1947-03-11 | Babcock & Wilcox Co | Control system |
US2420542A (en) * | 1942-12-24 | 1947-05-13 | Standard Oil Dev Co | Carrying out chemical reactions in the presence of finely-divided solids |
US2422791A (en) * | 1945-07-30 | 1947-06-24 | Universal Oil Prod Co | Endothermic catalytic conversion of hydrocarbons |
US2443210A (en) * | 1943-12-20 | 1948-06-15 | Phillips Petroleum Co | Quenching of hot gases |
US2447306A (en) * | 1943-09-16 | 1948-08-17 | Babcock & Wilcox Co | Fluid heater |
US2468712A (en) * | 1944-12-21 | 1949-04-26 | Babcock & Wilcox Co | Heat exchanger |
US2537044A (en) * | 1946-11-29 | 1951-01-09 | Hydrocarbon Research Inc | Continuous method of producing oxygen involving the use of a thermophore and the purging thereof |
US2556430A (en) * | 1945-04-21 | 1951-06-12 | Pure Oil Co | Method and apparatus for preparing mixed sulfur-hydrocarbon vapors |
US2560469A (en) * | 1946-10-12 | 1951-07-10 | Standard Oil Dev Co | Oxygen process |
US2635864A (en) * | 1948-12-28 | 1953-04-21 | Phillips Petroleum Co | Pebble heating and reaction chamber |
US2641450A (en) * | 1946-10-19 | 1953-06-09 | Hydrocarbon Research Inc | Method of transferring heat by a powdered thermophore in a state of dense phase fluidization |
US2680692A (en) * | 1954-06-08 | Stabilized alumina heat exchange | ||
US2696718A (en) * | 1947-02-20 | 1954-12-14 | Hydrocarbon Research Inc | Use of thermophore pellets in air rectification |
US2823864A (en) * | 1953-04-09 | 1958-02-18 | Bahco Ab | Ventilation systems for shelters |
US3061194A (en) * | 1958-07-09 | 1962-10-30 | Hazen Engineering Company | Two-stage system for preheating combustion air |
US3831668A (en) * | 1972-05-17 | 1974-08-27 | P Weissenburg | Tower type heat exchangers for heat interchange between gases heated to different temperatures |
US20140272729A1 (en) * | 2013-03-15 | 2014-09-18 | James L. Nester | Fluid bed regenerative thermal oxidizer and a method for its use |
CN104697358A (en) * | 2013-12-05 | 2015-06-10 | 北新集团建材股份有限公司 | Vertical-type powder cooler |
-
1913
- 1913-10-21 US US79641813A patent/US1178667A/en not_active Expired - Lifetime
Cited By (20)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2680692A (en) * | 1954-06-08 | Stabilized alumina heat exchange | ||
US2420542A (en) * | 1942-12-24 | 1947-05-13 | Standard Oil Dev Co | Carrying out chemical reactions in the presence of finely-divided solids |
US2447306A (en) * | 1943-09-16 | 1948-08-17 | Babcock & Wilcox Co | Fluid heater |
US2417049A (en) * | 1943-10-18 | 1947-03-11 | Babcock & Wilcox Co | Control system |
US2443210A (en) * | 1943-12-20 | 1948-06-15 | Phillips Petroleum Co | Quenching of hot gases |
US2468712A (en) * | 1944-12-21 | 1949-04-26 | Babcock & Wilcox Co | Heat exchanger |
US2556430A (en) * | 1945-04-21 | 1951-06-12 | Pure Oil Co | Method and apparatus for preparing mixed sulfur-hydrocarbon vapors |
US2422791A (en) * | 1945-07-30 | 1947-06-24 | Universal Oil Prod Co | Endothermic catalytic conversion of hydrocarbons |
US2560469A (en) * | 1946-10-12 | 1951-07-10 | Standard Oil Dev Co | Oxygen process |
US2641450A (en) * | 1946-10-19 | 1953-06-09 | Hydrocarbon Research Inc | Method of transferring heat by a powdered thermophore in a state of dense phase fluidization |
US2537044A (en) * | 1946-11-29 | 1951-01-09 | Hydrocarbon Research Inc | Continuous method of producing oxygen involving the use of a thermophore and the purging thereof |
US2696718A (en) * | 1947-02-20 | 1954-12-14 | Hydrocarbon Research Inc | Use of thermophore pellets in air rectification |
US2635864A (en) * | 1948-12-28 | 1953-04-21 | Phillips Petroleum Co | Pebble heating and reaction chamber |
US2823864A (en) * | 1953-04-09 | 1958-02-18 | Bahco Ab | Ventilation systems for shelters |
US3061194A (en) * | 1958-07-09 | 1962-10-30 | Hazen Engineering Company | Two-stage system for preheating combustion air |
US3831668A (en) * | 1972-05-17 | 1974-08-27 | P Weissenburg | Tower type heat exchangers for heat interchange between gases heated to different temperatures |
US20140272729A1 (en) * | 2013-03-15 | 2014-09-18 | James L. Nester | Fluid bed regenerative thermal oxidizer and a method for its use |
US9488372B2 (en) * | 2013-03-15 | 2016-11-08 | James L Nester | Fluid bed regenerative thermal oxidizer and a method for its use |
US11262068B2 (en) * | 2013-03-15 | 2022-03-01 | James L. Nester | Fluid bed regenerative thermal oxidizer and a method for its use |
CN104697358A (en) * | 2013-12-05 | 2015-06-10 | 北新集团建材股份有限公司 | Vertical-type powder cooler |
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