US3900958A - Method and apparatus for continuously drying a dripping wet, granular or lumpy material - Google Patents

Method and apparatus for continuously drying a dripping wet, granular or lumpy material Download PDF

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Publication number
US3900958A
US3900958A US401137A US40113773A US3900958A US 3900958 A US3900958 A US 3900958A US 401137 A US401137 A US 401137A US 40113773 A US40113773 A US 40113773A US 3900958 A US3900958 A US 3900958A
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United States
Prior art keywords
trough
drying
flow
enclosure
chamber
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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
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US401137A
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English (en)
Inventor
Wilhelm Bongert
Horst Kuhn
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Kloeckner Humboldt Deutz AG
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Kloeckner Humboldt Deutz AG
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    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26—DRYING
    • F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B17/00—Machines or apparatus for drying materials in loose, plastic, or fluidised form, e.g. granules, staple fibres, with progressive movement
    • F26B17/26—Machines or apparatus for drying materials in loose, plastic, or fluidised form, e.g. granules, staple fibres, with progressive movement with movement performed by reciprocating or oscillating conveyors propelling materials over stationary surfaces; with movement performed by reciprocating or oscillating shelves, sieves, or trays
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D33/00—Filters with filtering elements which move during the filtering operation
    • B01D33/01—Filters with filtering elements which move during the filtering operation with translationally moving filtering elements, e.g. pistons
    • B01D33/03—Filters with filtering elements which move during the filtering operation with translationally moving filtering elements, e.g. pistons with vibrating filter elements
    • B01D33/0346—Filters with filtering elements which move during the filtering operation with translationally moving filtering elements, e.g. pistons with vibrating filter elements with flat filtering elements
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D33/00—Filters with filtering elements which move during the filtering operation
    • B01D33/58—Handling the filter cake in the filter for purposes other than for regenerating the filter cake remaining on the filtering element
    • B01D33/62—Handling the filter cake in the filter for purposes other than for regenerating the filter cake remaining on the filtering element for drying
    • B01D33/66—Handling the filter cake in the filter for purposes other than for regenerating the filter cake remaining on the filtering element for drying by gases or by heating
    • B01D33/663—Handling the filter cake in the filter for purposes other than for regenerating the filter cake remaining on the filtering element for drying by gases or by heating by direct contact with a fluid
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D33/00—Filters with filtering elements which move during the filtering operation
    • B01D33/70—Filters with filtering elements which move during the filtering operation having feed or discharge devices
    • B01D33/72—Filters with filtering elements which move during the filtering operation having feed or discharge devices for feeding
    • B01D33/722—Filters with filtering elements which move during the filtering operation having feed or discharge devices for feeding containing fixed liquid displacement elements or cores

Definitions

  • the hot gases are isolated in the drying zone by aprons [52] 34/164; 34/216 34/217 between the drying zone and both the dehydration CL I Zone and a discharge chamber.
  • the apparatus also [58] new of Search 34/164 preferably includes a distribution chamber having 21 34/217 flexible and elastic incline bottom to prevent breaking of fragile materials as they are being introduced onto [56] References Cited the conveyor trough at the beginning of the dehydra- UNITED STATES PATENTS tion Z0ne 2,215,201 9/1940 Jorgenscn 34/164 3,010,215 11/1961 Kayatz 34/164 5 Clams, 2 Drawmg Flgul'es 26 z n E 2s 23 M L y 4 t 19 15 w I [I 3 1 X g a; 4 r" ⁇ k" 8 28 a 6 8 6 7 1 l j l 1 v METHOD AND APPARATUS FOR CONTINUOUSLY DRYING A DRIPPING
  • the invention relates to a method and apparatus for the continuous drying of dripping wet, granular and/or lumpy materials with the aid of a vibrating conveyor chute or trough, which has a perforated bottom and extends from a material charging inlet to a material dis charging aperture as it passes through a dehydration zone and drying zone.
  • the present invention obviates the disadvantages of the known drying method and, particularly for the chemical industry, makes possible the withdrawal of liquid and the drying of dripping wet, granular and/or lumpy or caked materials in a simple and economical manner with the aid of a single machine unit or apparatus.
  • the problem is solved in that the liquid is first drawn or drained from the materials in the conveyor trough with reference to the direction of feed in a dehydration zone and subsequently the remaining moisture is dried off with the aid of hot gases.
  • the individual steps of the method which are required for the drying of dripping wet materials are substantially stretched out or extended in their timely sequence, so that a greater output of materials and therewith a more economical establishment of the drying method can be attained.
  • the method of the invention enables the unitary control of the drying operation by means of a single technically controlled installation, which in accordance with experience permits a more simple manipulation for the attendant personnel, so that frequent encroachments proportionate thereto which could disadvantageouly influence the drying process are prevent.
  • the hot drying gases are substantially isolated to the drying zone.
  • the entire heat content of the hot gases may be utilized for the removal of the remaining moisture of the material being dried.
  • This isolation also prevents any flow of the gases into the dehydration zone in which the gases would cause a non-desirable evaporation of particles of liquid and accordingly an appreciable loss of heat energy.
  • the method includes the steps of controlling the feed and withdrawal of the hot gases with respect to one another so that in the drying zone, practically the ambient pressure prevails.
  • the step of controlling the pressure in the drying 2one the method is advantageously attained and almost no steam of gases escapes along the conveyor trough' which escaping gas may contain injurious particles of dust.
  • the control of the pressure in the drying zone prevents the entry of cold air which would disadvantageously affect the degree of efficiency of the drying process.
  • the step of controlling also enables the step of isolating to be accomplished with the provision of simple constructive measures, such as sealing of the dehydration zone from the drying zone as well -as also a sufficient sealing of the drying zone with respect to the atmosphere.
  • the invention relates additionally to a single device or apparatus which dehydrates the dripping wet material and dries the material to perform the method.
  • the apparatus includes an enclosure having a vibrating conveyor trougl'i with perforated bottom, means for charging material, means for discharging material and means for creating a flow of hot gases in a drying zone.
  • oneend of the conveyor trough is disposed beneath the means for charging and is adjacent a dehydration zone which is defined by a water collection device provided with a discharge aperture disposed beneath the one end.
  • the other end of the conveyor trough is in a drying zone which is defined by the means creating a flow of hot gases which includes a gas distribution device provided with at least one gas inlet which distribution device is preferably arranged beneath the trough.
  • the apparatus has a compact construction so that an economical installation is made possible even with restricted space conditions. The relatively high investment costs of the previously known drying installations, which consisted of at least one dehydration unit and one drying unit, are thereby substantially diminished.
  • the dehydration chamber or zone is separated from the drying chamber or zone by means for isolating which preferably is a flexible apron extending transverselylto the longitudinal axis of the trough and reaching approximately the surface of the material.
  • means for isolating which preferably is a flexible apron extending transverselylto the longitudinal axis of the trough and reaching approximately the surface of the material.
  • the charging means with a material charging aperture which is in communication with the dehydration zone or chamber of the conveyor trough through a distributing chamber which has an inclined bottom consisting advantageously of an elastic or flexible material.
  • Another advantage of the construction of the embodiment of the invention is that the elastic or flexible bottom of the distributing chamber also vibrates so that 5 caking of material during distribution on the conveyor trough are prevented and an even distribution of mate rial can be obtained.
  • the elastic construction of the bottom also provides an additional protection for brittle materials which are to be dried and which during charging are especially inclined to brittle-breakage.
  • the drying chamber or zone is in connection with a discharge chamber and an apron, which is preferably adjustable and is preferably flexible, is located between the drying zone and discharge chamber and extends approximately to the material surface.
  • an apron which is preferably adjustable and is preferably flexible, is located between the drying zone and discharge chamber and extends approximately to the material surface.
  • FIG. 1 is a diagrammatic illustration with parts in section of the apparatus of the present invention.
  • FIG. 2 is a front view of the apparatus of FIG. 1.
  • the principles of the present invention are particularly useful in a drying apparatus having a conveyor trough 1 which has a perforated bottom 2 having holes of a size determined by the grain size of the material being dried.
  • the trough 1 is closed on all sizes to form an enclosure of the apparatus.
  • the enclosure is oscillatably connected by a plurality of spring guides or suspensions 6 to a countermass or frame 7 which is suspended by rubber buffers 8 on supports 9 which extend from a base frame 10.
  • an oscillating drive 28 which may be either an eccentric or inertia drive, is mounted as the base 10 and connected to the enclosure for the trough l.
  • the enclosure for the conveyor trough 1 is provided with means for charging which includes a material charging aperture or opening and means for discharging a material which includes a material discharge aperture or opening 16.
  • the trough 1 extends along the length of the enclosure and conveys material in direction 11 through four individual zones or chambers.
  • a material distribution chamber or zone 22 is arranged directly beneath the aperture 15 and distributes the wet material to the trough l which conveys the material through a dehydration zone or chamber 17 into a drying zone or chamber 20. From the drying zone 20, the trough 1 conveys the material into a discharge zone or chamber 24 which is attached by a flange to the drying chamber and has the aperture 16.
  • a water collection device 19 which preferably consists of a simple container with slanting or inclined bottom 14 and which device prevents the flow of hot gases through the overlying perforated bottom and isolates the dripping or draining liquid from the hot gases.
  • the device In the lower area of the water collection device 19 (FIG. 2) the device has a water-flow-off device 18, which has a discharge aperture 13 which may, for example, be connected to a waste-water conduit 27.
  • a hot gas distribution device or means 3 is arranged beneath the perforated bottom 2 of the trough.
  • the distribution device may be a windbox with hot gas inlets 4 which are in communication with a source of hot gas, such as a hot gas producer (not shown).
  • the enclosure above the bottom 2 includes a gas discharge hood 5 to close the drying zone 20 and the hood has an upwardly extending portion which terminates with a gas-discharge conduit 12 which is connected to a suction blower (not shown).
  • the distribution chamber 22 has an inclined bottom 23, which advantageously is constructed of a rubber or elastic material and extends transversely to the longitu-.
  • a separating apron 21 extends transversely to the longitudinal axis of the trough and extends from the upper wall of the enclosure to approximately the surface of the material on the bottom 2.
  • the apron 21 separates or isolates the dehydration zone 17 and drying zone from one another.
  • This separating apron 21 consists advantageously of an elastic material, for example, rubber or the like.
  • a stoppage apron 25 which is preferably of a flexible construction, is provided to extend transversely to the direction 11 and to reach approximately to the material surface.
  • the stoppage apron 25 covers the cross section of the discharge chamber 24 and accordingly seals the drying chamber 20 with respect to the surrounding atmosphere.
  • the inclined bottom 23, the separating apron 21 and the stoppage apron 25 each may extend through a separate closable mounting slot 26 which extend transversely to the axis of the trough.
  • Each of the mounting slots 26 may be provided with means to enable adjusting the length of the aprons '21 and 25 or the length of the bottom 23 according to the characteristics of the material to be dried.
  • the dripping wet, granular and/or lumpy materials are continuously supplied through the material supply opening 15 of the distribution chamber 22 onto the one end of the conveyor trough 1.
  • the wet materials first encounter the inclined, elastic bottom 23 of the distribution chamer 22 which uniformly distributed the material over the width of the trough 1 as it reaches the perforated bottom 2 of the dehydration chamber 17. Due to the vibrating movements of the trough 1, the material is almost completely dehydrated in a short time.
  • the liquid derived from the dripping wet material drains through the perforated bottom into the water collection device 19 and then flows along bottom 14 to the water discharge device 18.
  • the water discharge device 18 discharges the liquid through opening 13 into a waste-water conduit 27 which may convey the liquid to a liquid purification system (not shown).
  • the dripping wet material which has a tendency for caking, is centrifuged again by the bottom 23 and this self-purification effect results and clogging in the area of the material inlet is permanently prevented.
  • the elastic apron 21 which is arranged approximately in the middle of the conveyor trough 1, between the dehydration zone 17 and drying zone 20, prevents any mist or water spray present in the dehydration chamber from entering the drying zone 20.
  • the apron 21 also retains the material and aids in uniformly distributing it over the surface of the perforated bottom, so that a rapid dehydration of the charged material is achieved.
  • the drying zone 20 After the material has been almost completely dehydrated in the dehydration zone 17, it is conveyed into the drying zone 20, in which the remaining moisture is dried off.
  • hot gases are introduced through the openings 4 of the wind-box 3, to flow through the openings in the perforated bottom 2 of the drying chamber and through the layer of material disposed on the bottom.
  • the hot gases will absorb the residual moisture and are then discharged through the gas discharge conduit of hood 5 which conduit is connected to a suction device.
  • the hot gas supply and hot gas discharge are controlled and proportioned to one another so that the pressure in the drying zone is substantially the same as the surrounding pressure.
  • the material completely dried upon passage through the drying chamber 20 is conveyed into the discharge chamber 24 and conveyed through the discharge opening 16 to a collecting device or container (not shown).
  • a collecting device or container (not shown).
  • the drying chamber 20 is sealed against the surrounding atmosphere and at the same time the material being dried is held back.
  • a uniformly high layer of material is produced on the bottom 2 of the drying chamber 20, so that a uniform distribution and flow-through of the hot gases is attained through the entire material to be dried which material is disposed on the bottom 2.
  • the period of time in the drying zone can be changed or adjusted.
  • the duration of time necessary for the material in the drying chamber can be adjusted in a simple manner, so that for the individual particles of material, almost the same drying periods are insured.
  • the construction of the vibration dryer according to the invention is not limited solely to the embodiment illustrated as a sample construction.
  • the position of the separating apron 21 between the dehydration zone 17 and the drying zone 20 may be adapted to the characteristics in each case of the goods or materials to be dried.
  • the inclined bottom 23 of the distribution chamber 22 may be at least partially perforatedin' a sievedike manner, so that the advantage of the compact construction of the dryer according to the invention is more clearly apparent.
  • An apparatus for the continuous drying of dripping wet granular material comprising an enclosure having a vibrating conveyor trough with a perforated bottom, said enclosure having means for charging the material to be dried onto one end of the conveyor trough and means for discharging dried material from the other end of the trough, means disposed in the enclosure beneath said one end of the conveyor trough for collecting liquid dripping through the perforated bottom of the trough, said collecting means including a liquid discharge opening, and means for creating a flow of hot gases through a portion of the conveyor troughs to form a drying zone to dry material thereon, said means for creating including a gas distribution device having at least one hot gas inlet on one side of the trough and a hot gas outlet on the opposite side, said collecting means isolating the dripping liquid from the flow of hot gases, said means for discharging material comprising a discharge chamber having a material discharge opening, said discharge chamber being in connection with the drying zone by an opening having means for isolating the flow of hot gases
  • the means for charging material include a material charging opening in connection with a distribution chamber having an incline bottom of elastic material, said distribution chamber distributing material from the charging opening onto the one end of the conveyor trough.
  • An apparatus for the continuous drying of dripping wet granular material comprising an enclosure having a vibrating conveyor trough with a perforated bottom, said enclosure having means for charging the material to be dried onto one end of the conveyor trough and means for discharging dried material from the other end of the trough, means disposed in the enclosure beneath said one end of the conveyor trough for collecting liquid dripping through the perforated bottom of the trough, said collecting means including a liquid discharge opening, means for creating a flow of hot gases through a portion of the conveyor troughs to form a drying zone to dry material thereon, said means for creating including a gas distribution device having at least one hot gas inlet on one side of the trough and a hot gas outlet on the opposite side, and said enclosure including means for isolating a flow of gas in the drying zone from the portion of the enclosure containing the means for collecting liquid, said means for isolating including a flexible apron extending transversely to the longitudinal axis of the trough and
  • the means for charging material include a material charging opening in connection with a distribution chamber having an incline bottom of elastic material, said distribution chamber distributing material from the charging opening onto the one end of the conveyor trough.

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Drying Of Solid Materials (AREA)
US401137A 1972-09-30 1973-09-27 Method and apparatus for continuously drying a dripping wet, granular or lumpy material Expired - Lifetime US3900958A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
DE19722248051 DE2248051A1 (de) 1972-09-30 1972-09-30 Verfahren zum kontinuierlichen trocknen von tropfnassen, koernigen und/oder stueckigen guetern und vorrichtung zur durchfuehrung des verfahrens

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US3900958A true US3900958A (en) 1975-08-26

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ID=5857873

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US401137A Expired - Lifetime US3900958A (en) 1972-09-30 1973-09-27 Method and apparatus for continuously drying a dripping wet, granular or lumpy material

Country Status (11)

Country Link
US (1) US3900958A (it)
JP (1) JPS4993954A (it)
AT (1) AT337614B (it)
BE (1) BE805513A (it)
DD (1) DD107528A5 (it)
DE (1) DE2248051A1 (it)
FR (1) FR2201750A5 (it)
GB (1) GB1441647A (it)
IT (1) IT997861B (it)
NL (1) NL7313498A (it)
RO (1) RO64689A (it)

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4062127A (en) * 1974-07-01 1977-12-13 Klockner-Humboldt-Deutz Aktiengesellschaft Method for the continuous drying of wet, granular and/or lumpy materials and device for carrying out the method
US4785551A (en) * 1987-05-28 1988-11-22 Kraft, Inc. Method for drying confection pieces
WO1991014910A1 (en) * 1988-11-23 1991-10-03 Seaford Nominees Pty Ltd. Dewatering and drying means for pulp
US5230163A (en) * 1991-04-23 1993-07-27 General Kinematics Corporation Weir gate assembly
US5331746A (en) * 1990-12-21 1994-07-26 Martin Gmbh Fur Umwelt-Und Energietechnik Process and an apparatus for removing water from ash
US5653044A (en) * 1996-03-22 1997-08-05 California Pellet Mill Company Horizontal cooler and dryer with solid pans
US5664338A (en) * 1996-03-22 1997-09-09 California Pellet Mill Company Inlet air seal for use with a cooler/dryer
US20070266590A1 (en) * 2006-04-06 2007-11-22 Econ Maschinenbau Und Steuerungstechnik Gmbh Drying device and method
WO2009152925A3 (de) * 2008-05-27 2010-04-01 Automatik Plastics Machinery Gmbh Trocknungsvorrichtung zum trocknen von granulatkörnern
CN111829317A (zh) * 2020-07-27 2020-10-27 湖北工业大学 果蔬烘干装置

Families Citing this family (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5286558A (en) * 1976-01-12 1977-07-19 Tamagawa Kikai Kinzoku Kk Method and apparatus for continuously drying viscous substance
JPS5465875A (en) * 1977-11-05 1979-05-26 Shinko Electric Co Ltd Heating and drying device
SE465996B (sv) * 1990-03-29 1991-12-02 Frigoscandia Food Process Syst Foerfarande och anordning foer avvattning av livsmedelsprodukter
CN112892368A (zh) * 2021-03-07 2021-06-04 李涛 一种建筑加工用结构胶的多级混合及过滤除杂设备
CN117906355B (zh) * 2024-03-18 2024-06-04 烟台双塔食品股份有限公司 一种粉丝干燥用码放盘

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2215201A (en) * 1938-02-24 1940-09-17 Smidth & Co As F L Distributing apparatus
US3010215A (en) * 1959-06-29 1961-11-28 Fuller Co Gas-solids heat exchanger
US3768174A (en) * 1971-04-19 1973-10-30 Escher Wyss Ag Fluidised bed device

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2215201A (en) * 1938-02-24 1940-09-17 Smidth & Co As F L Distributing apparatus
US3010215A (en) * 1959-06-29 1961-11-28 Fuller Co Gas-solids heat exchanger
US3768174A (en) * 1971-04-19 1973-10-30 Escher Wyss Ag Fluidised bed device

Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4062127A (en) * 1974-07-01 1977-12-13 Klockner-Humboldt-Deutz Aktiengesellschaft Method for the continuous drying of wet, granular and/or lumpy materials and device for carrying out the method
US4785551A (en) * 1987-05-28 1988-11-22 Kraft, Inc. Method for drying confection pieces
WO1991014910A1 (en) * 1988-11-23 1991-10-03 Seaford Nominees Pty Ltd. Dewatering and drying means for pulp
US5331746A (en) * 1990-12-21 1994-07-26 Martin Gmbh Fur Umwelt-Und Energietechnik Process and an apparatus for removing water from ash
US5230163A (en) * 1991-04-23 1993-07-27 General Kinematics Corporation Weir gate assembly
US5653044A (en) * 1996-03-22 1997-08-05 California Pellet Mill Company Horizontal cooler and dryer with solid pans
US5664338A (en) * 1996-03-22 1997-09-09 California Pellet Mill Company Inlet air seal for use with a cooler/dryer
US20070266590A1 (en) * 2006-04-06 2007-11-22 Econ Maschinenbau Und Steuerungstechnik Gmbh Drying device and method
WO2009152925A3 (de) * 2008-05-27 2010-04-01 Automatik Plastics Machinery Gmbh Trocknungsvorrichtung zum trocknen von granulatkörnern
US20110061261A1 (en) * 2008-05-27 2011-03-17 Automatik Plastics Machinery Gmbh Drying apparatus for drying pellets
US8424219B2 (en) 2008-05-27 2013-04-23 Automatik Plastics Michinery GmbH Drying apparatus for drying pellets
CN111829317A (zh) * 2020-07-27 2020-10-27 湖北工业大学 果蔬烘干装置

Also Published As

Publication number Publication date
ATA834973A (de) 1976-10-15
JPS4993954A (it) 1974-09-06
DD107528A5 (it) 1974-08-05
DE2248051A1 (de) 1974-04-04
GB1441647A (en) 1976-07-07
IT997861B (it) 1975-12-30
RO64689A (fr) 1979-03-15
BE805513A (fr) 1974-01-16
FR2201750A5 (it) 1974-04-26
NL7313498A (it) 1974-04-02
AT337614B (de) 1977-07-11

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