US3092180A - Heat exchange apparatus - Google Patents

Heat exchange apparatus Download PDF

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Publication number
US3092180A
US3092180A US837534A US83753459A US3092180A US 3092180 A US3092180 A US 3092180A US 837534 A US837534 A US 837534A US 83753459 A US83753459 A US 83753459A US 3092180 A US3092180 A US 3092180A
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US
United States
Prior art keywords
rotor
channels
housing
heat
chamber
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 - Lifetime
Application number
US837534A
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English (en)
Inventor
Dahlgren Sven Alfred Bertil
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Alfa Laval Holdings Amsterdam AB
Original Assignee
Separator AB
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Separator AB filed Critical Separator AB
Application granted granted Critical
Publication of US3092180A publication Critical patent/US3092180A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D1/00Evaporating
    • B01D1/22Evaporating by bringing a thin layer of the liquid into contact with a heated surface
    • B01D1/222In rotating vessels; vessels with movable parts
    • B01D1/223In rotating vessels; vessels with movable parts containing a rotor
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B04CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
    • B04BCENTRIFUGES
    • B04B1/00Centrifuges with rotary bowls provided with solid jackets for separating predominantly liquid mixtures with or without solid particles
    • B04B1/04Centrifuges with rotary bowls provided with solid jackets for separating predominantly liquid mixtures with or without solid particles with inserted separating walls
    • B04B1/08Centrifuges with rotary bowls provided with solid jackets for separating predominantly liquid mixtures with or without solid particles with inserted separating walls of conical shape
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B04CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
    • B04BCENTRIFUGES
    • B04B5/00Other centrifuges
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B04CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
    • B04BCENTRIFUGES
    • B04B7/00Elements of centrifuges
    • B04B7/08Rotary bowls
    • B04B7/12Inserts, e.g. armouring plates
    • B04B7/14Inserts, e.g. armouring plates for separating walls of conical shape
    • 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
    • F28D11/00Heat-exchange apparatus employing moving conduits
    • F28D11/02Heat-exchange apparatus employing moving conduits the movement being rotary, e.g. performed by a drum or roller
    • 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
    • Y10S165/135Movable heat exchanger
    • Y10S165/139Fully rotatable
    • Y10S165/14Rotating heat exchanger having rotating flow confining structures or chambers for two separate heat exchange fluids

Definitions

  • the present invention relates to heat exchange apparatus for concentration or evaporation of a liquid or for heat exchange between the liquid and a heat-emitting medium.
  • the invention relates more particularly to such an apparatus of the type which is provided with a rotor enclosed in a housing.
  • the rotor In heat exchange apparatus of this type as proposed heretofore, the rotor consists of a hollow (usually coneshaped) body on the inside of which the material to be heat-treated is introduced at the center and from which it is discharged at the periphery, while the heat-emitting medium is supplied on the outside of the rotor.
  • the volume of the apparatus in relation to the heat-transmission surface is rather great. It has therefore been proposed to make the rotor of two opposed, cone-shaped surfaces and provide a plurality of chambers formed of such surfaces, these chambers being connected in parallel and being in axially superposed relation to each other.
  • no appreciable saving of space has been obtained in this way, which is primarily due to me design of the heat-transmission surfaces and the interspaces between them.
  • the principal object of the present invention is to overcome the above-noted difficulty.
  • the rotor is provided with a number of uniform, coaxial partitions, preferably conical, which are fitted in each other and between which are channels or slots, every second of which is arranged to be passed through by the heat-receiving medium, while the rest of them are arranged to be passed through by the heat-emitting medium.
  • the channels or slots for the heat-receiving medium have their inlets situated at the center and their outlets situated at the periphery, while the channels for the heat-emitting medium have both their inlets and their outlets situated at the periphery.
  • FIGS. 1 and 2 are vertical sectional views of two preferred embodiments of the invention.
  • the apparatus according to FIG. 1 comprises a housing made of lower and upper parts 1 and 2, respectively.
  • the housing 12 also serves as a frame, and its two parts are held together by means of screws 3.
  • the housing contains a rotor which likewise is made of upper and lower parts 5-6 held together by means of two bolts 4, and which contains a nest of conical partitions 7.
  • the latter are joined in pairs by means of ring-shaped parts 8 and 9, alternately at the outer and inner edges, so that channels or slots are formed between the partitions, every second channel 10 being opened inwards towards the center, while the other channels 11 are closed at the center by the rings 8.
  • the rings 89 are in conaaaaisa centric relation to the rotor axis.
  • the rotor part 6 is fitted on a hollow vertical shaft 12 which is supported by two ball bearings 14, 15 arranged in a bearing box 13 secured to the part 1 by means of screws, the shaft being provided with a driving pulley 16.
  • the rings 9 are superposed in relation to each other and provided with intermediate sealing rings 17 and with channels 18, 19 which cross each other.
  • the channels 18 are axially directed and are arranged inside the sealing rings 17 and situated opposite each other in the various rings. They are in communication through grooves 20 with the slots 10, and open at their lower ends into a common collecting trough 21 arranged in the bottom of the part 6.
  • a paring tube 22 which communicates with a central outlet 23 extending through the hollow shaft 12.
  • the part 6 surrounds the rings 9 and centers them.
  • the rings 9 rest together with a conical bottom disc 24 against a flange 25 in the part 6 and are jammed between this flange and the part 5 by means of the bolts 4.
  • the part 6 has holes 26 which correspond with grooves 27 arranged in the rings 9 and with the channels 19, and these holes, together with the channels 19, join the slots 11 with a chamber 28 between the rotor and the surrounding housing.
  • the chamber 28 is provided with a steam inlet 29 and a condensate outlet 39.
  • sealing means 31, 32 Between the rotor and the non-rotary parts are sealing means 31, 32.
  • the interior of the rotor can be connected by an outlet 33 with a vacuum source and has an inlet 34 for the material to be heat-treated. Extending radially from the inlet 34 are distributing pipes 35 by means of which the material to be heat-treated is introduced into the chambers or slots 10 at the center, and from there it is spread over the outer surfaces formed of the partitions 7 and defining these chambers.
  • the material is thrown outwards in thin layers along these defining surfaces while receiving that heat which the steam, passing into the slots 11 from the chamber 28, gives off during condensation to the outside of the partitions 7.
  • the condensate depositing on the partitions 7 is immediately thrown away from them by the centrifugal force, so that a good heat transmission from the steam to the partitions is always maintained.
  • the ring-shaped parts 44 ⁇ are provided with sealing rings 46 located in grooves and are pressed against each other and against the bottom of the bowl 44 by means of a ring 47 and bolts 48.
  • the ring 47 is shaped in such a way that it forms a collecting trough 49' for the concentrate which is thrown out from the interspaces 42 through channels 50 arranged in the rings 40'.
  • the bowl 44 is sunk into a wider bowl '51 having a flange 52, a sealing ring 53 being inserted bet-ween the bowls 44 and 51 and held by means of bolts 54.
  • the parts 44 and l--5253 thus form a separate chamber 55.
  • a paring tube 66 which is in communication with an outlet 67 through the wall of the upper housing part 37.
  • the chamber 68 between the rotorand the surrounding housing is provided with a vacuum'oonnection 69 and with a vertical inlet tube 70 for the material which is to be heat-treated and which, by means of radial distributing pipes 71, is led into the interspaces 42.
  • the housing surrounding the rotoris also provided with a bottom outlet 72 which normally should be closed.
  • a sealing ring 73 is arranged between the shaft 56 and the lower part so of the surrounding housing.
  • a similar sealing means 74 is arranged between the shaft 56 and the connection 62. No further sealing means are required between rotary and stationary 'parts in the embodiment of the apparatus shown in FIG.
  • the parts 34--35 and 7 tl--71 form means for feeding the heat-receiving medium to the inlets :of the alternate channels it) and 42., respectively; and the parts 2@2i--2223 and ss 49 se-s7 form means for discharging fromthe housing the heatreceiving medium passing through the peripheral outlets of the alternate channels it and 42, respectively.
  • a heat exchange apparatus of the centrifugal type comprising a stationary housing, a rotormounted in the housing for rotation about an axis, a nest of coaxial conical partitions secured in the rotor for rotation therewith and defining a series of axially spaced rotor channels between the partitions, alternate rotor channels serving for flow of a heatereceiving medium While the other channels serve for flow of a heatemitting medium, said alternate channels each having an inlet located near the rotor axis and an outlet at the peripheral portion of the rotor,
  • said other channels having openings located at said pe ripheral portion and forming both inlets and outlets for said other channels, the housing having an inlet for admitting said heat-emitting medium into said other chanels by way of said peripheral openings, means for feeding a,
  • said discharging means include a collecting chamber in the rotor communicating with said peripheral outlets of said alternate channels, and a paring device in said collecting chamber.
  • said discharging means include a collecting chamber in the rotor communicating with said peripheral outlets of said alternate channels, and a paring device in said collecting chamher, the housing having an'evacuation outlet in open communication With said collecting chamber.
  • Apparatus according. to claim 1 comprising also sealing means located between the housing and rotor and sealing said alternate channels and discharge means from said space between the housing and rotor.
  • Apparatus according to claim 1 comprising also sealing means located between the housing and rotor and sealing said alternate channels and discharge means from said space between the housing and rotor, said space having a steam inlet and a condensate outlet for the heatemitting medium.
  • said discharging means include a collecting chamber in the rotor communicating with said peripheral outlets of said alternate channels, and a paring device in said collecting chamber, said collecting chamber being in direct communication with said space between the housing and rotor, the rotor having a second chamber separate from said collecting chamber and communicating with said peripheral openings of said other channels, the second chamber being provided with a central steam inlet and a central condensate outlet for the heat-emitting medium, the apparatus also including a paring device located in said second chamber and connected to said condensate outlet.
  • a heat exchange apparatus of the centrifugal type comprising a stationary housing, a rotor mounted in the housing for rotation about an axis, the housing forming a peripheral portion, alternate channels serving forflow of a heat-receiving medium and the other channels serving for flow of a heat-emitting medium, each of the alternate channels having an annular inlet located near and extending round the rotor axis, a stationary distributing member facing each of said annular inlets and disposed in the rotor to distribute heat-receiving medium into each alternate channel through its annular inlet, the rotor having a collecting channel communicating with the outer portions of said alternate channels, means for discharging the heat-.
  • one of said discharging means includes a paring member in said rotor chamber.
  • Apparatus according to claim 8 in which the housing has an evacuation outlet in open communication with said stationary housing chamber but sealed from said rotor chamber.
  • Apparatus according to claim 13 in which said housing and rotor chambers are sealed from each' other, said openings leading to and from the rotor chamber, said housing chamber having an evacuation outlet and being in open communication with said annular inlets and said collecting channel.
  • Apparatus according to claim 8 in which said housing and rotor chambers are sealed from each other, said openings leading to and from the rotor chamber, said housing chamber having an evacuation outlet and being in open communication with said annular inlets and said collecting channel, said discharging means for the heat- Ieceiving medium including a paring device fixed to the housing and located in said housing chamber.

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  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)
  • Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
  • Centrifugal Separators (AREA)
US837534A 1958-09-17 1959-09-01 Heat exchange apparatus Expired - Lifetime US3092180A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
SE879158 1958-09-17

Publications (1)

Publication Number Publication Date
US3092180A true US3092180A (en) 1963-06-04

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ID=20275036

Family Applications (1)

Application Number Title Priority Date Filing Date
US837534A Expired - Lifetime US3092180A (en) 1958-09-17 1959-09-01 Heat exchange apparatus

Country Status (8)

Country Link
US (1) US3092180A (xx)
BE (1) BE582149A (xx)
CH (2) CH373355A (xx)
DE (1) DE1114783B (xx)
ES (1) ES251191A1 (xx)
FR (1) FR1236706A (xx)
GB (1) GB880990A (xx)
NL (2) NL242034A (xx)

Cited By (17)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3204687A (en) * 1963-07-23 1965-09-07 Ralph G Sargeant Centrifugal electrical apparatus for treating liquids
US3221807A (en) * 1962-03-23 1965-12-07 Separator Ab Apparatus for heat treatment of liquids
US3241598A (en) * 1961-03-15 1966-03-22 Separator Ab Method and apparatus for evaporating liquids
US3274756A (en) * 1962-10-08 1966-09-27 Stern Bengt Evert Apparatus for degassifying a liquid
US3282798A (en) * 1963-01-30 1966-11-01 Baldwin Lima Hamilton Corp Apparatus for compressing vapors in the distillation of a rotary conical film
US3303877A (en) * 1963-06-05 1967-02-14 Ramen Corp A B Heat exchanger
US3412777A (en) * 1966-07-13 1968-11-26 Alfa Laval Ab Frusto-conical film type evaporator
US3430690A (en) * 1965-11-08 1969-03-04 Alfa Laval Ab Centrifugal apparatus for heat exchange
US3921709A (en) * 1973-01-17 1975-11-25 Liquid Processing Ab Apparatus for indirect heat treatment of liquids
US3981437A (en) * 1974-05-14 1976-09-21 Westfalia Separator Ag Centrifuge having a system for controlling the temperature of the liquid to be centrifuged or of one of the components thereof
US4153500A (en) * 1974-02-28 1979-05-08 Vaclav Feres Thin film coating evaporator
US4597835A (en) * 1983-12-14 1986-07-01 John Moss Still
US4627890A (en) * 1981-11-24 1986-12-09 Imperial Chemical Industries Plc Centrifugal device
US5513697A (en) * 1991-04-17 1996-05-07 Gudmundsson; Bjorn Method and device for transfer of heat
US20120058023A1 (en) * 2009-03-10 2012-03-08 Alfa Laval Corporate Ab Multifunctional module
CN105849494A (zh) * 2013-12-19 2016-08-10 达纳加拿大公司 圆锥形热交换器
JPWO2021106135A1 (xx) * 2019-11-28 2021-06-03

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE3204262A1 (de) * 1982-02-08 1983-08-18 Vladimir Kazimirovič Moskva Čubukov Rotor-duennschichtverdampfer
DE102016118475A1 (de) * 2016-09-29 2018-03-29 Krones Ag Vorrichtung zum Verdampfen eines flüssigen Mediums in einer Füllproduktabfüllanlage

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1479088A (en) * 1921-04-16 1924-01-01 Schneible Joseph Heat exchanger
US2169601A (en) * 1934-10-04 1939-08-15 Frank H Cornelius Heating system
US2318293A (en) * 1940-12-26 1943-05-04 Cornell Machine Company Material treating process and apparatus
US2549968A (en) * 1948-07-30 1951-04-24 Phillips Petroleum Co Means and method for selective lowpressure desorption of liquids
FR1181588A (fr) * 1956-08-23 1959-06-17 Separator Ab échangeur de chaleur
US3010702A (en) * 1955-02-16 1961-11-28 Separator Ab Heat exchange for continuous throughflow of two media

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1479088A (en) * 1921-04-16 1924-01-01 Schneible Joseph Heat exchanger
US2169601A (en) * 1934-10-04 1939-08-15 Frank H Cornelius Heating system
US2318293A (en) * 1940-12-26 1943-05-04 Cornell Machine Company Material treating process and apparatus
US2549968A (en) * 1948-07-30 1951-04-24 Phillips Petroleum Co Means and method for selective lowpressure desorption of liquids
US3010702A (en) * 1955-02-16 1961-11-28 Separator Ab Heat exchange for continuous throughflow of two media
FR1181588A (fr) * 1956-08-23 1959-06-17 Separator Ab échangeur de chaleur

Cited By (20)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3241598A (en) * 1961-03-15 1966-03-22 Separator Ab Method and apparatus for evaporating liquids
US3221807A (en) * 1962-03-23 1965-12-07 Separator Ab Apparatus for heat treatment of liquids
US3274756A (en) * 1962-10-08 1966-09-27 Stern Bengt Evert Apparatus for degassifying a liquid
US3282798A (en) * 1963-01-30 1966-11-01 Baldwin Lima Hamilton Corp Apparatus for compressing vapors in the distillation of a rotary conical film
US3303877A (en) * 1963-06-05 1967-02-14 Ramen Corp A B Heat exchanger
US3204687A (en) * 1963-07-23 1965-09-07 Ralph G Sargeant Centrifugal electrical apparatus for treating liquids
US3430690A (en) * 1965-11-08 1969-03-04 Alfa Laval Ab Centrifugal apparatus for heat exchange
US3412777A (en) * 1966-07-13 1968-11-26 Alfa Laval Ab Frusto-conical film type evaporator
US3921709A (en) * 1973-01-17 1975-11-25 Liquid Processing Ab Apparatus for indirect heat treatment of liquids
US4153500A (en) * 1974-02-28 1979-05-08 Vaclav Feres Thin film coating evaporator
US3981437A (en) * 1974-05-14 1976-09-21 Westfalia Separator Ag Centrifuge having a system for controlling the temperature of the liquid to be centrifuged or of one of the components thereof
US4627890A (en) * 1981-11-24 1986-12-09 Imperial Chemical Industries Plc Centrifugal device
US4597835A (en) * 1983-12-14 1986-07-01 John Moss Still
US5513697A (en) * 1991-04-17 1996-05-07 Gudmundsson; Bjorn Method and device for transfer of heat
US20120058023A1 (en) * 2009-03-10 2012-03-08 Alfa Laval Corporate Ab Multifunctional module
US8961882B2 (en) * 2009-03-10 2015-02-24 Alfa Laval Corporate Ab Multifunctional module
CN105849494A (zh) * 2013-12-19 2016-08-10 达纳加拿大公司 圆锥形热交换器
CN105849494B (zh) * 2013-12-19 2018-07-10 达纳加拿大公司 圆锥形热交换器
JPWO2021106135A1 (xx) * 2019-11-28 2021-06-03
WO2021106135A1 (ja) * 2019-11-28 2021-06-03 大平洋機工株式会社 熱媒体が供給されるピンミキサ

Also Published As

Publication number Publication date
GB880990A (en) 1961-10-25
CH373355A (de) 1963-11-30
NL108059C (xx)
BE582149A (xx)
FR1236706A (fr) 1960-07-22
ES251191A1 (es) 1959-12-01
CH879158D (xx)
DE1114783B (de) 1961-10-12
NL242034A (xx)

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