USRE19140E - Metallic filling fob cold - Google Patents
Metallic filling fob cold Download PDFInfo
- Publication number
- USRE19140E USRE19140E USRE19140DA USRE19140E US RE19140 E USRE19140 E US RE19140E US RE19140D A USRE19140D A US RE19140DA US RE19140 E USRE19140 E US RE19140E
- Authority
- US
- United States
- Prior art keywords
- cold
- strips
- accumulator
- gas
- corrugations
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired
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Images
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J5/00—Arrangements of cold exchangers or cold accumulators in separation or liquefaction plants
- F25J5/002—Arrangements of cold exchangers or cold accumulators in separation or liquefaction plants for continuously recuperating cold, i.e. in a so-called recuperative heat exchanger
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J2205/00—Processes or apparatus using other separation and/or other processing means
- F25J2205/24—Processes or apparatus using other separation and/or other processing means using regenerators, cold accumulators or reversible heat exchangers
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J2290/00—Other details not covered by groups F25J2200/00 - F25J2280/00
- F25J2290/42—Modularity, pre-fabrication of modules, assembling and erection, horizontal layout, i.e. plot plan, and vertical arrangement of parts of the cryogenic unit, e.g. of the cold box
Definitions
- the strips of sheet metal should be corrugated and so arranged that a brisk whirling'o the gas, as air owing through the channels formed by them is brought about.
- the strips should touch one another only at points, and in no case along a line or plane, because the gas cannot reach places v where the strips touch, so that those portions of the cold exchanging surface are thereby rendered ineffective.
- Fig. 1 shows the shell cut open in three places to expose the filling to view; on the left-hand side the front strip' is seen, while at the right is shown the strip which lies behind.
- the corrugations of the upper strips b and 0" are higher than those of the middle strips d and e and of the lowest f" and g, as seen in Figs. 1 and 2.
- the flow of gas is reversed, and the gas to be treated is ied nrst through the second accumulator and passed out through the rst accumulator, so that it is cooled in the second and gives up its cold to the nrst accumulator.
- the operation is again reversed and the gas to be treated is again introduced into the first accumulator.
- the accumulator described above thus operates alternately as cold accumulator and cold exchanger in .a regenerative retrigerating system, and is thus to be distinguished from the known forms of tubular cold exchangers which operate continuously.
- a cold accumulator comprising a shell, the inside space oi said shell being divided into a number of zones, disks positoned in said zones and composed of two parallel strips of sheet metal adapted to be chilled by a stream of cold gas passing through the accumulator and to cool a subsequent stream ⁇ of warmer gas, said strips being wound spirally and being provided with corrugations aslant to the direction o! the gas current, the corrugations of each pair of said strips lying cross-ways and contacting only at oi warmer gas, said strips being wound spirally and provided with corrugations aslant to the direction of the gas current.
- the corrugations ci each pair of said strips lying cross-ways and contacting only at points, and said spirally wound strips being disposed in such a way that from' zone to zone themass of metal becomes greater toward the colder end.
- a metallic filling for cold accumulators which consists of two corrugated metal strips having corrugations running aslant towards the edges of the strips Wound together spirally to form a. disk in such a manner that the corrugations of each pair of adjacent sheets cross each other and Contact only at points.
Description
A 17, 1934. M. FRANKI..
IB'I'ALLIG FILLING FOR COLD ACCUIULATORS original Filed July 2'1. 192s v .K INVENTOR Mir/m5 Fmvz Y y BY E 'm7 Z'Mgvls Reissued Apr. 17, 1934 PATENT OFFICE METALLIC FILLING FOB COLD ACCUMULATORS Mathias Friinkl, Augsburg,
to American Oxythermic York,
Germany, assignor Corporation, New
N. Y., a corporation of Delaware Original No. 1,808,921, dated June 9,- 1931, Serial No. 294,356, July 21, 1928. Applicationy for reissue May 9, 1933, Serial No. 670,086. In Germany August 1, 1927 13 Claims.
'I'he object of the present invention is to provide a cold accumulator suitable for use in the process described in patent application Serial No. 81,723, granted as Patent 1,890,646, Process for separation of gas mixtures, especially of air, in which the exchange of cold is eiiected by means of regenerators arranged for reversed operation. The cold accumulator used in this process consists of a cylindrical or square shell of sheet metal through which the air or other gaseous mixture ilows in axial direction between a number of strips of sheet metal disposed inside the shell at a distance of from 0.5 to 2.5 mm. apart from one another, whereby an exchange of cold or heat is effected.
As the specic heat of iron at very low temperatures is considerably less than at atmospheric temperature and as the volume of a gas decreases with lowering temperature, while the specic heat of a gas remains fairly even, a form of lling for the cold accumulator had to be devised which takes these facts into account. Inside the cold accumulators the temperature decreases from top to bottom, also the volume of gas and the specific heat of the iron filling of the accumulator decrease. This latter at minus 190 C. amounts only to 0.036 as compared to 0.11 at plus 20 C., that is two thirds less. The volume of gas decreases at about the same rate. The lling must, therefore, be so constituted that its mass towards the bottom or cold zone of the accumulator is greater than at the top or warmer zone and, therefore, the total flow area for the gas diminishes toward the colder end.
In the accompanying drawings, which show a preferred embodiment of the apparatus according to the invention,
Fig. 1 is a front view of a cold accumulator with parts of the shell removed to show the lling, e. g., strips of sheet metal;
Fig. 2 is a transverse section of the shell, the left side of the gure representing a section along a line A-B of Fig. 1, the right side of a section along a line C-D of Fig. 1;
Fig.l 3 is a side view of two sheet metal strips, one behind the other, the one in front being drawn in full lines, the rear one in dotted lines;
Fig. 4 is a top view of the same;
Fig. 5 is a side view of the same; the left side of the figure representing the back strip, the righthand side of the figure the strip lying in front, part of the front strip having been removed;
Fig. 6 shows a lling in course of manufacture.
According to this form of the invention strips of sheet metal are disposed inside the shell at distances apart which decrease by steps from top to bottom of the shell, as may be seen from Figs. 1 and 2, resulting in smaller spaces in the lower parts and forming narrower channels or passages appropriate to the diminishing air volume at lower temperatures. The shell a is shown cut open in three places to expose to View the strips of sheet metal constituting the lling. In cylindrical shells the strips are disposed in spirals forming disks of from 500 to 1500 mm. diameter, as shown in Figs. 2 and 6; in square shells the strips are put in singly, in which case they must be shaped in such a way, that intervening spaces of the desired dimensions result.
To attain the highest possible elect the strips of sheet metal should be corrugated and so arranged that a brisk whirling'o the gas, as air owing through the channels formed by them is brought about. The strips should touch one another only at points, and in no case along a line or plane, because the gas cannot reach places v where the strips touch, so that those portions of the cold exchanging surface are thereby rendered ineffective.
With a view to minimize losses from this cause, the strips are provided with corrugations running aslant towards the edges of the strips; by arranging the corrugations of neighboring strips to slant in opposite sense, the strips will touch only at the corrugations which is the desired Way, i. e., there will be point contact only. The crossing of the corrugations also causes lively whirls in the gas current, thus considerably increasing the cold exchanging effect.
Fig. 1 shows the shell cut open in three places to expose the filling to view; on the left-hand side the front strip' is seen, while at the right is shown the strip which lies behind. The corrugations of the upper strips b and 0" are higher than those of the middle strips d and e and of the lowest f" and g, as seen in Figs. 1 and 2.
Fig. 2 shows the filling of a cylindrical cold accumulator in transverse section. In this spirally Wound lling two strips with corrugatons slanting in opposite sense are always wound simultaneously, thus forming a double-warmed spiral with corrugations lying cross-ways. This is seen very plainly in Fig. 6 which shows the spiral winding in course of manufacture, that is in the unfinished state. The stripsfd and e are preliminarily drawn through pairs of furrowed rollers h and i, and k and l, to corrugate them. The strips are laid next to one another and then spirally wound around a spool or axle "m". The spool or axle of the spirally wound strips, when placed in the cold accumulator a, will lie in the vertical axis thereof, as shown in Fig.' 2.
The accumulator described above is of particular advantage in the regenerative refrigeration oi' gases for the purpose either oi' separating the components of a mixture of gases, or of removing the moisture or carbon dioxide therefrom. In such case, at least two cold accumulators of the type shown in Fig. l must be present. At the beginning of the process employing theabovedescribed accumulator, the metallic nling or packing of the accumulator is cooled by means of a reirigerating machine to the temperature at which the particulargas mixture being treated, tor example air, is to be separated into its components, or at which water vapor or carbon dioxide will precipitate from air or any other gas. The air or other gas is then introduced at the top oi the nrst accumulator. which at this stage of the process acts as a cold exchanger, and which gives up its cold to such air and cools the same to the 4desired temperature. Alter that the air is separated into its components, or water vapor or carbon dioxide is precipitated in a sultable apparatus, alter which the cold components or the cold gas is fed to a second accumlator from the bottom to the top thereof. This second accumulator now operates to storein its packing the cold of the discharging components or gas; in eilect, the cold oi' the first accumulator is in this manner transferred to the packing of the second accumulator. The components or gases escaping from the second accumulator are almost as warm as the gas introdud into the nrst accumlator.
After about live minutes, the flow of gas is reversed, and the gas to be treated is ied nrst through the second accumulator and passed out through the rst accumulator, so that it is cooled in the second and gives up its cold to the nrst accumulator. After about ve minutes the operation is again reversed and the gas to be treated is again introduced into the first accumulator. The accumulator described above thus operates alternately as cold accumulator and cold exchanger in .a regenerative retrigerating system, and is thus to be distinguished from the known forms of tubular cold exchangers which operate continuously.
I claim:
l. A cold accumulator comprising a shell. the inside space of such shell being divided into a number of zones, strips o! sheet metal disposed in each of said zones and adapted to be chilled by a stream of cold gas through the accumulator and to cool a subsequent stream of warmer gas, said strips being disposed in such a way that from zone to zone the extent of their surface and the mass oi' metal toward the colder end become greater, while the total ilow area of the gas channels becomes smaller.
2. A cold accumulator comprising a shell, the inside space oi said shell being divided into a number of zones, disks positoned in said zones and composed of two parallel strips of sheet metal adapted to be chilled by a stream of cold gas passing through the accumulator and to cool a subsequent stream` of warmer gas, said strips being wound spirally and being provided with corrugations aslant to the direction o! the gas current, the corrugations of each pair of said strips lying cross-ways and contacting only at oi warmer gas, said strips being wound spirally and provided with corrugations aslant to the direction of the gas current. the corrugations ci each pair of said strips lying cross-ways and contacting only at points, and said spirally wound strips being disposed in such a way that from' zone to zone themass of metal becomes greater toward the colder end.
4; A cold accumulator comprising a shell, the inside space of saidshell being divided into a number of zones, a plurality o! units each composed of two parallel strips o! sheet metal adapted to be chilled by a stream of cold gas through the `accumulator and to cool a subsequent stream of warmer gas, said strips being positioned in said zones, spirally disposed and provided with corrugations aslant to the direction oi the gas' current, the corrugations oi each pair of said strips lying cross-ways and contacting only at points, the height of said corrugations decreasing step by step towards the colder end of the accumulator and said spirally wound strips being disposed in such a way that from zone to zone the mass of metal becomes greater toward the colder end.
5. A cold accumulator comprising in combina- 4 tion a shell, strips oi' sheet metal disposed within said shell and adapted to be chilled by a stream of cold gas passing through the accumulator and to cool a subsequent stream o! warmer gas, said strips being disposed in such manner that the surface and the mass of metal become greater and the total flow area oi' gas channels becomes smaller toward the colder end.
6. A cold accumulator comprising in combination a shell, disks composed oi' two parallel strips oi' sheet metal adapted to be chilled by a stream oi cold gas passing through the accumulator and spirally wound. said strips being provided with corrugations aslant to the direction of the gas current, the corrugations of each pair of said strips lying cross-ways contacting only at points and the height thereof decreasing towards the colder end o! the accumulator.
8. A cold accumulator comprising in combination a shell, a metallic illling disposed within said shell and adapted to be chilled by a stream of cold gas passing through the accumulator and to cool a subsequent stream oi' warmer gas, said vmetallic nlling being disposed in such a manner that the surface and the mass thereof are greater at the colder end of the accumulator.
9. A cold accumulator comprising a shell, a metallic lling disposed within said shell and adapted to be chilled by a stream 'of cold gas passing through the accumulator and to cool a subsequent stream of warmer gas, said metallic filling being disposed in such a manner that the surface and the mass thereof become gradually greater and the total flow area of the gas channels becomes gradually smaller toward the colder end of the accumulator.
10. A metallic lling for cold accumulators which comprises metallic strips disposed in such a manner that the surface and the mass of metal becomes greaterv and the total flow area of gas channels becomes smaller upon passing from the Warm to the cold end.
1l. A metallic filling for cold accumulators which comprises disks composed of two parallel strips of sheet metal wound spirally about a spool and provided with corrugations aslant towards the edges of the strips, said corrugatlons of each pair of said strips lying cross-ways and contacting only at points.
12. A metallic lling for cold accumulators which comprises strips of sheet metal disposed spirally and provided with corrugations aslant towards the edges of the strips, the corrugations of each pair of said strips lying cross-ways contacting only at points and the height thereof decreasing from one end to the other of the accumulator.
13. A metallic filling for cold accumulators which consists of two corrugated metal strips having corrugations running aslant towards the edges of the strips Wound together spirally to form a. disk in such a manner that the corrugations of each pair of adjacent sheets cross each other and Contact only at points.
MATHIAs
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE1808921X | 1927-08-01 |
Publications (1)
Publication Number | Publication Date |
---|---|
USRE19140E true USRE19140E (en) | 1934-04-17 |
Family
ID=7744197
Family Applications (2)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US294356A Expired - Lifetime US1808921A (en) | 1927-08-01 | 1928-07-21 | Metallic filling for cold accumulators |
USRE19140D Expired USRE19140E (en) | 1927-08-01 | 1933-05-09 | Metallic filling fob cold |
Family Applications Before (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US294356A Expired - Lifetime US1808921A (en) | 1927-08-01 | 1928-07-21 | Metallic filling for cold accumulators |
Country Status (3)
Country | Link |
---|---|
US (2) | US1808921A (en) |
BE (2) | BE331455A (en) |
FR (2) | FR613755A (en) |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2492788A (en) * | 1947-05-24 | 1949-12-27 | Air Reduction | Regenerator |
US2995344A (en) * | 1959-02-12 | 1961-08-08 | Parsons C A & Co Ltd | Plate type heat exchangers |
US3216484A (en) * | 1960-09-09 | 1965-11-09 | Ibm | Cryogenic regenerator |
US3276515A (en) * | 1964-04-09 | 1966-10-04 | Chrysler Corp | Gas turbine regenerator |
US3285326A (en) * | 1964-09-18 | 1966-11-15 | Int Harvester Co | Recuperative type heat exchanger |
Families Citing this family (15)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2422825A (en) * | 1943-11-18 | 1947-06-24 | American Machine & Metals | Delinting screen |
US2552937A (en) * | 1946-06-20 | 1951-05-15 | Power Jets Res & Dev Ltd | Heat exchanger and method of making the same |
US2602645A (en) * | 1948-04-09 | 1952-07-08 | Hydrocarbon Research Inc | Regenerator and packing therefor |
US3062509A (en) * | 1953-02-12 | 1962-11-06 | Philips Corp | Heat regenerator |
US2836398A (en) * | 1953-09-10 | 1958-05-27 | Linderoth Erik Torvald | Regenerative heat exchanger for gas turbines |
DE1903543U (en) * | 1964-07-16 | 1964-11-05 | Appbau Rothemuehle Brandt & Kr | STEPPED HEATING PLATE FOR REGENERATIVE HEAT EXCHANGER. |
US3373798A (en) * | 1965-11-19 | 1968-03-19 | Gen Motors Corp | Regenerator matrix |
US4010621A (en) * | 1974-01-04 | 1977-03-08 | Karlheinz Raetz | Stirling cycle heat pump |
US3910344A (en) * | 1974-03-27 | 1975-10-07 | Gen Motors Corp | Regenerator matrix |
US4061183A (en) * | 1977-02-16 | 1977-12-06 | General Motors Corporation | Regenerator matrix |
SE8207166D0 (en) * | 1982-12-15 | 1982-12-15 | Svante Thunberg | REGENERATIVE HEAT EXCHANGER WITH MOISTURIZING AND TEMPERATURES |
US4619112A (en) * | 1985-10-29 | 1986-10-28 | Colgate Thermodynamics Co. | Stirling cycle machine |
US5429177A (en) * | 1993-07-09 | 1995-07-04 | Sierra Regenators, Inc. | Foil regenerator |
US6745822B1 (en) * | 1998-05-22 | 2004-06-08 | Matthew P. Mitchell | Concentric foil structure for regenerators |
US6854509B2 (en) * | 2001-07-10 | 2005-02-15 | Matthew P. Mitchell | Foil structures for regenerators |
-
0
- BE BE353089D patent/BE353089A/xx unknown
- BE BE331455D patent/BE331455A/xx unknown
-
1926
- 1926-01-16 FR FR613755D patent/FR613755A/en not_active Expired
-
1928
- 1928-07-21 US US294356A patent/US1808921A/en not_active Expired - Lifetime
- 1928-07-30 FR FR35778D patent/FR35778E/en not_active Expired
-
1933
- 1933-05-09 US USRE19140D patent/USRE19140E/en not_active Expired
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2492788A (en) * | 1947-05-24 | 1949-12-27 | Air Reduction | Regenerator |
US2995344A (en) * | 1959-02-12 | 1961-08-08 | Parsons C A & Co Ltd | Plate type heat exchangers |
US3216484A (en) * | 1960-09-09 | 1965-11-09 | Ibm | Cryogenic regenerator |
US3276515A (en) * | 1964-04-09 | 1966-10-04 | Chrysler Corp | Gas turbine regenerator |
US3285326A (en) * | 1964-09-18 | 1966-11-15 | Int Harvester Co | Recuperative type heat exchanger |
Also Published As
Publication number | Publication date |
---|---|
FR35778E (en) | 1930-03-27 |
BE331455A (en) | |
FR613755A (en) | 1926-11-29 |
BE353089A (en) | |
US1808921A (en) | 1931-06-09 |
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