US2701130A - Element set for heat exchangers - Google Patents

Element set for heat exchangers Download PDF

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Publication number
US2701130A
US2701130A US202869A US20286950A US2701130A US 2701130 A US2701130 A US 2701130A US 202869 A US202869 A US 202869A US 20286950 A US20286950 A US 20286950A US 2701130 A US2701130 A US 2701130A
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United States
Prior art keywords
wires
elements
gratings
heat exchangers
grating
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US202869A
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Boestad Gustav Karl William
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JARVIS C MARBLE
LESLIE M MERRILL
PERCY H BATTEN
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JARVIS C MARBLE
LESLIE M MERRILL
PERCY H BATTEN
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    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28DHEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D17/00Regenerative heat-exchange apparatus in which a stationary intermediate heat-transfer medium or body is contacted successively by each heat-exchange medium, e.g. using granular particles
    • F28D17/02Regenerative heat-exchange apparatus in which a stationary intermediate heat-transfer medium or body is contacted successively by each heat-exchange medium, e.g. using granular particles using rigid bodies, e.g. of porous material
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10STECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S165/00Heat exchange
    • Y10S165/009Heat exchange having a solid heat storage mass for absorbing heat from one fluid and releasing it to another, i.e. regenerator
    • Y10S165/042Particular structure of heat storage mass

Definitions

  • the present invention relates to heat transfer elements in heat exchangers for air or other gaseous mediums and has particular reference to regenerative air-preheaters.
  • the heat exchanging mass of such heat exchangers is ordinarily built up of plate packs composed of smooth and/or undulated plates, spaced by notches pressed up in the plates or by means of other distance elements, said plates forming walls of flow channels for the heat exchanging gases. It is found that favourable effects can be obtained it these gases are given a helical path of flow through the channels. In doing so the creation of a heat insulating boundary layer nearest to the heat exchanging surfaces is reduced. A flow of this character also prevents soot and other impurities in the gases from depositing in the preheater reducing the heat transmission coefficient. Heat exchangers built according to the above principles have a relatively good ratio between the heat transmission coefficient and the pressure drop of the through-flow.
  • the favourable result has substantially been attained by using heat transfer elements in the form of substantially parallel and spaced wires forming an acute angle (preferably less than 45) to the main direction of flow of the gases.
  • These wires are preferably arranged to form gratings spaced by thicker wires, bent metal strips or similar distance elements.
  • Fig. l is a plan view of gratings according to the invention.
  • Fig. 2 is an end View of these gratings.
  • Fig. 3 is a plan view of gratings having wires arranged cross-wise.
  • Fig. 4 shows a grating and a smooth plate in combination.
  • Fig. 5 shows an undulated plate in combination with a grating, of the type shown in Fig. 1.
  • Fig. 6 shows a modification of the embodiment shown in Fig. 5.
  • Figs. 1 and 2 show two gratings placed parallel to each other, each of them consisting of wires 1 disposed in parallel and at an acute angle to the main direction of flow of the gases.
  • the wires 1 are interconnected by distance wires 2 holding the two gratings apart.
  • the cross section of the distance wires may have any suitable form.
  • the distance elements 2 are substantially parallel to the main direction of flow of the gases.
  • the value of the angle between the wires 1 and the distance elements 2 as above is of the order of 30. It is suitable to secure the wires 1 to the distance elements 2 by welding, riveting or the like.
  • the gas column therebetween is divided into two currents having helical paths of opposite sense. This results in a favourable increase of the heat trans- ICC mission coefiicient.
  • the cross-section of the wires 1 it may be round or oval. Other suitable cross-sections as polygonal, for example, may also be used.
  • Fig. 3 shows a second embodiment of the invention characterized by parallel wires 1 in one grating which wires have a direction crossing that of corresponding wires in' an adjacent grating, which in some cases may be appropriate to produce a single-directed rotation of the gas flow between two gratings.
  • Fig. 4 is a grating of the above described type provided with distance members 2, which bear against intermediate heat exchanging plates 3, which in this case are smooth.
  • Fig. 5 shows another plate 4 having undulations running parallelly to the direction of the wires 1
  • Fig. 6 is a modification of the embodiment in Fig. 5, having said directions provided cross-wise.
  • Regenerative heat exchange mass comprising a multiplicity of spaced and generally parallel heat exchange elements forming a pack and including between each two adjacent elements parallel spaced elongated and substantially straight spacing means for providing between each two adjacent elements a plurality of contiguous and substantially straight and unobstructed channels open at their ends for flow of columns of the same gaseous fluid from end to end of the several channels of the pack, each of said channels being defined by two adjacent elements and two adjacent spacing means between the said two adjacent elements and each of said channels being of generally rectangular cross-section having a width at least several times the distance between said adjacent elements, at least one of the elements defining a side of each of said channels being in the form of a grating consisting of a multiplicity of substantially parallel spaced wires obliquely disposed in the same sense with respect to the lengths of the channels and certain other of said elements consisting of plates 2. Structure as defined in claim 1 in which said spacing means comprises distance pieces connecting the wires of each of said gratings.

Description

Feb. 1, 1955 G. K- W. BOESTAD ELEMENT SET FOR HEAT EXCHANGERS Filed Dec. 27, 1950 United States Patent ELEMENT SET FOR HEAT EXCHANGERS Gustav Karl William Boestad, Lidingo, Sweden, assignor, by mesne assignments, to Jarvis C. Marble, New York, N. Y., Leslie M. Merrill, Westfield, N. J., and Percy H. Batten, Racine, Wis., as trustees Application December 27, 1950, Serial No. 202,869 Claims priority, application Sweden January 4, 1950 8 Claims. (Cl. 257-256) The present invention relates to heat transfer elements in heat exchangers for air or other gaseous mediums and has particular reference to regenerative air-preheaters.
The heat exchanging mass of such heat exchangers is ordinarily built up of plate packs composed of smooth and/or undulated plates, spaced by notches pressed up in the plates or by means of other distance elements, said plates forming walls of flow channels for the heat exchanging gases. It is found that favourable effects can be obtained it these gases are given a helical path of flow through the channels. In doing so the creation of a heat insulating boundary layer nearest to the heat exchanging surfaces is reduced. A flow of this character also prevents soot and other impurities in the gases from depositing in the preheater reducing the heat transmission coefficient. Heat exchangers built according to the above principles have a relatively good ratio between the heat transmission coefficient and the pressure drop of the through-flow.
This ratio, however, has further been improved by means of heat transfer elements according to the present invention.
The favourable result has substantially been attained by using heat transfer elements in the form of substantially parallel and spaced wires forming an acute angle (preferably less than 45) to the main direction of flow of the gases. These wires are preferably arranged to form gratings spaced by thicker wires, bent metal strips or similar distance elements.
These and other characteristics of the invention will be hereinafter described more in detail with reference to the accompanying drawings, showing some preferred embodiments by way of example.
Fig. l is a plan view of gratings according to the invention.
Fig. 2 is an end View of these gratings.
Fig. 3 is a plan view of gratings having wires arranged cross-wise.
Fig. 4 shows a grating and a smooth plate in combination.
Fig. 5 shows an undulated plate in combination with a grating, of the type shown in Fig. 1.
Fig. 6 shows a modification of the embodiment shown in Fig. 5.
Figs. 1 and 2 show two gratings placed parallel to each other, each of them consisting of wires 1 disposed in parallel and at an acute angle to the main direction of flow of the gases. In each grating the wires 1 are interconnected by distance wires 2 holding the two gratings apart. The cross section of the distance wires may have any suitable form. In air preheaters the distance elements 2 are substantially parallel to the main direction of flow of the gases. Preferably, the value of the angle between the wires 1 and the distance elements 2 as above is of the order of 30. It is suitable to secure the wires 1 to the distance elements 2 by welding, riveting or the like. Due to the parallel arrangement of the wires 1 in the two gratings, the gas column therebetween is divided into two currents having helical paths of opposite sense. This results in a favourable increase of the heat trans- ICC mission coefiicient. As to the cross-section of the wires 1, it may be round or oval. Other suitable cross-sections as polygonal, for example, may also be used.
Fig. 3 shows a second embodiment of the invention characterized by parallel wires 1 in one grating which wires have a direction crossing that of corresponding wires in' an adjacent grating, which in some cases may be appropriate to produce a single-directed rotation of the gas flow between two gratings.
Instead of making all of the heat exchanging mass of gratings as described above it is also possible to combine these gratings by plane or corrugated plates alternately provided between said gratings.
In Fig. 4 is a grating of the above described type provided with distance members 2, which bear against intermediate heat exchanging plates 3, which in this case are smooth.
Fig. 5 shows another plate 4 having undulations running parallelly to the direction of the wires 1, and Fig. 6 is a modification of the embodiment in Fig. 5, having said directions provided cross-wise.
What is claimed is:
1. Regenerative heat exchange mass comprising a multiplicity of spaced and generally parallel heat exchange elements forming a pack and including between each two adjacent elements parallel spaced elongated and substantially straight spacing means for providing between each two adjacent elements a plurality of contiguous and substantially straight and unobstructed channels open at their ends for flow of columns of the same gaseous fluid from end to end of the several channels of the pack, each of said channels being defined by two adjacent elements and two adjacent spacing means between the said two adjacent elements and each of said channels being of generally rectangular cross-section having a width at least several times the distance between said adjacent elements, at least one of the elements defining a side of each of said channels being in the form of a grating consisting of a multiplicity of substantially parallel spaced wires obliquely disposed in the same sense with respect to the lengths of the channels and certain other of said elements consisting of plates 2. Structure as defined in claim 1 in which said spacing means comprises distance pieces connecting the wires of each of said gratings.
3. Structure as defined in claim 1 in which the grating elements and plate elements alternate so that the opposite sides of each channel are defined respectively by solid and perforate elements.
4. Structure as defined in claim 3 in which the plate elements are plane.
5. Structure as defined in claim 3 in which the plate elements are undulated.
6. Structure as defined in claim 5 in which the undulations are oblique with respect to the direction of the length of the channels.
7. Structure as defined in claim 6 in which the undulations are oblique in the same direction as the wires of the grating elements.
8. Structure as defined in claim 6 in which the undulations of the plate elements and the wires of the grating elements are oppositely oblique.
References Cited in the file of this patent UNITED STATES PATENTS 902,812 Goetz et al Nov. 3, 1908 949,668 Swinscoe Feb. 15, 1910 1,803,746 Miller May 5, 1931 2,023,965 Lysholm Dec. 10, 1935 2,049,246 Brown July 28, 1936 2,157,744 Welty May 9, 1939 2,313,081 Ljungstrom Mar. 9, 1943 2,405,593 Melvill Aug. 13, 1946
US202869A 1950-01-04 1950-12-27 Element set for heat exchangers Expired - Lifetime US2701130A (en)

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Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2937010A (en) * 1956-01-16 1960-05-17 Gen Motors Corp Regenerative heat exchanger
US3046639A (en) * 1954-05-10 1962-07-31 Helmut A Freyholdt Method of making heat exchanger
US3100332A (en) * 1960-02-23 1963-08-13 Jr John R Gier Method of making a heat exchanger cross tied pin assembly
US3103971A (en) * 1958-08-08 1963-09-17 Helmut A Freyholdt Heat exchanger core structure
US3164891A (en) * 1960-03-02 1965-01-12 Jr John R Gier Method of forming pin fin assemblies
US3183963A (en) * 1963-01-31 1965-05-18 Gen Motors Corp Matrix for regenerative heat exchangers
US3313343A (en) * 1964-03-26 1967-04-11 Trane Co Heat exchange apparatus
US20030010473A1 (en) * 2001-07-10 2003-01-16 Mitchell Matthew P. Foil structure for regenerators

Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US902812A (en) * 1908-03-27 1908-11-03 Adolph Goetz Process of pasteurization.
US949668A (en) * 1907-05-23 1910-02-15 Clinton Wire Cloth Company Welded fabric.
US1803746A (en) * 1927-07-25 1931-05-05 Christman Matthias Lubricating device
US2023965A (en) * 1930-05-21 1935-12-10 Ljungstroms Angturbin Ab Heat transfer
US2049246A (en) * 1933-06-23 1936-07-28 Chemical Construction Corp Gauze
US2157744A (en) * 1938-03-22 1939-05-09 Welty Frank Heat exchanger
US2313081A (en) * 1937-02-02 1943-03-09 Jarvis C Marble Heat exchange
US2405593A (en) * 1944-02-04 1946-08-13 Francis L Melvill Packing for vapor and liquid contacting apparatus

Patent Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US949668A (en) * 1907-05-23 1910-02-15 Clinton Wire Cloth Company Welded fabric.
US902812A (en) * 1908-03-27 1908-11-03 Adolph Goetz Process of pasteurization.
US1803746A (en) * 1927-07-25 1931-05-05 Christman Matthias Lubricating device
US2023965A (en) * 1930-05-21 1935-12-10 Ljungstroms Angturbin Ab Heat transfer
US2049246A (en) * 1933-06-23 1936-07-28 Chemical Construction Corp Gauze
US2313081A (en) * 1937-02-02 1943-03-09 Jarvis C Marble Heat exchange
US2157744A (en) * 1938-03-22 1939-05-09 Welty Frank Heat exchanger
US2405593A (en) * 1944-02-04 1946-08-13 Francis L Melvill Packing for vapor and liquid contacting apparatus

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3046639A (en) * 1954-05-10 1962-07-31 Helmut A Freyholdt Method of making heat exchanger
US2937010A (en) * 1956-01-16 1960-05-17 Gen Motors Corp Regenerative heat exchanger
US3103971A (en) * 1958-08-08 1963-09-17 Helmut A Freyholdt Heat exchanger core structure
US3100332A (en) * 1960-02-23 1963-08-13 Jr John R Gier Method of making a heat exchanger cross tied pin assembly
US3164891A (en) * 1960-03-02 1965-01-12 Jr John R Gier Method of forming pin fin assemblies
US3183963A (en) * 1963-01-31 1965-05-18 Gen Motors Corp Matrix for regenerative heat exchangers
US3313343A (en) * 1964-03-26 1967-04-11 Trane Co Heat exchange apparatus
US20030010473A1 (en) * 2001-07-10 2003-01-16 Mitchell Matthew P. Foil structure for regenerators
US6854509B2 (en) * 2001-07-10 2005-02-15 Matthew P. Mitchell Foil structures for regenerators

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