DK153104B - SPRAY DRYING APPLIANCE OF A FLUID - Google Patents

SPRAY DRYING APPLIANCE OF A FLUID Download PDF

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Publication number
DK153104B
DK153104B DK365075AA DK365075A DK153104B DK 153104 B DK153104 B DK 153104B DK 365075A A DK365075A A DK 365075AA DK 365075 A DK365075 A DK 365075A DK 153104 B DK153104 B DK 153104B
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DK
Denmark
Prior art keywords
shaft
liquid
drying
wall
openings
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Application number
DK365075AA
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Danish (da)
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DK153104C (en
DK365075A (en
Inventor
Geert De Boer
Original Assignee
Stork Amsterdam
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Publication of DK153104B publication Critical patent/DK153104B/en
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Publication of DK153104C publication Critical patent/DK153104C/en

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Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26DRYING
    • F26BDRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B17/00Machines or apparatus for drying materials in loose, plastic, or fluidised form, e.g. granules, staple fibres, with progressive movement
    • F26B17/10Machines or apparatus for drying materials in loose, plastic, or fluidised form, e.g. granules, staple fibres, with progressive movement with movement performed by fluid currents, e.g. issuing from a nozzle, e.g. pneumatic, flash, vortex or entrainment dryers
    • F26B17/107Machines or apparatus for drying materials in loose, plastic, or fluidised form, e.g. granules, staple fibres, with progressive movement with movement performed by fluid currents, e.g. issuing from a nozzle, e.g. pneumatic, flash, vortex or entrainment dryers pneumatically inducing within the drying enclosure a curved flow path, e.g. circular, spiral, helical; Cyclone or Vortex dryers
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D1/00Evaporating
    • B01D1/16Evaporating by spraying
    • B01D1/18Evaporating by spraying to obtain dry solids

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  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
  • Drying Of Solid Materials (AREA)
  • Cyclones (AREA)

Description

DK 153104 BDK 153104 B

Opfindelsen angår et apparat af den i kravets indledning angivne art til forstøvningstørring af en væske. Sådanne apparater er kendt i mange forskellige udførelsesformer og især beregnet til fremstilling af tørmælk, såkaldt mælkepulver.The invention relates to an apparatus of the kind specified in the preamble of the claim for spray drying of a liquid. Such appliances are known in many different embodiments and especially intended for the preparation of dry milk, so-called milk powder.

I apparater af denne type dannes ofte tilsigtet pulverpartikler med en vis fugtighed, hvilket er vigtigt med henblik på en efterfølgende tørringsproces. Pulverpartikler med et vist fugtigheds-indhold er imidlertid tilbøjelige til at hænge fast ved den nedre koniske skaktdels væg og danne påbagninger på denne. Man har søgt at undgå dette ved at bibringe tørregassen en roterende bevægelse i skakten ved tilførsel af tørregassen i tangential retning. Denne tørregas udblæses dernæst i det koniske skakt-In appliances of this type, intentional powder particles are often formed with some moisture, which is important for a subsequent drying process. However, powder particles with a certain moisture content tend to adhere to the wall of the lower conical shaft portion and form coatings thereon. This has been attempted to avoid this by imparting a rotary movement in the shaft to the drying gas by supplying the drying gas in a tangential direction. This drying gas is then blown into the conical shaft.

2 DK 153104B2 DK 153104B

partis centrale del, hvilket imidlertid forudsætter et centralt i skaktens nedre del placeret, strømningen hindrende legeme, der medfører forstyrrelser i strømningen..the central part of the portion, however, which requires a central position located in the lower part of the shaft, the flow obstructing body which causes disturbances in the flow.

Opfindelsen tager sigte på at undgå påbagninger af pulverpartikler i skaktens koniske nedre del på en mere hensigtsmæssig og effektiv måde, hvilket opnås ved det i patentkravets kendetegnende del angivne. Ved kombinationen af disse træk opnås nemlig, at tørreprocessen finder sted i et centralt område i for-støvningstørreskakten, medens skyllegassen strømmer omkring dette centrale tørreområde på en skruelinieformet strømningsbane og derved hindrer pulverpartiklerne i at sætte sig fast på skaktens væg.The invention aims at avoiding dusting of powder particles in the tapered lower part of the shaft in a more convenient and efficient manner, which is achieved by the characterizing part of the patent claim. Namely, by combining these features, the drying process is accomplished in a central region of the spray-drying shaft, while the flushing gas flows around this central drying region on a helical flow path, thereby preventing the powder particles from adhering to the wall of the shaft.

Åbningerne til tilførsel af skyllegas er hensigtsmæssigt således udformet og har en sådan retning, at skyllegassen fra åbningerne strømmer langs med skaktvæggens koniske parti.Conveniently, the openings for supplying flushing gas are designed and have such a direction that the flushing gas from the openings flows along the conical wall of the shaft wall.

Ved behandling af et termoplastisk materiale bør luften have en kølevirkning, medens luften i andre tilfælde bør have en tørrevirkning. Som regel er forstøvningstørreapparatet ifølge opfindelsen derfor forsynet med organer til konditionering af denne luft.When treating a thermoplastic material, the air should have a cooling effect, while in other cases the air should have a drying effect. As a rule, the spray dryer according to the invention is therefore provided with means for conditioning this air.

I det følgende forklares opfindelsen nærmere ved hjælp af tegningen, hvor fig. 1 er et lodret snit gennem en udførelsesform for forstøvnings tørreapparat ifølge opfindelsen, og fig. 2 og 3 viser to forskellige udførelsesformer for en detalje i fig. 1.In the following, the invention is explained in more detail with reference to the drawing, in which fig. 1 is a vertical section through an embodiment of an atomizer dryer according to the invention; and FIG. 2 and 3 show two different embodiments of a detail of FIG. First

Det i fig. 1 viste apparat til forstøvningstørring af en væske har en hovedsagelig cylindrisk søjle eller skakt 1 med en nedadtil konisk indsnævrende nedre skaktdel 2 med en nedre udløbsåbning 3, gennem hvilken fra væskens forstøvning hidrørende, helt eller delvis tørret pulver kan fjernes fra apparatet. Skakten 1 har foroven en topvæg 4 med et i og for sig kendt centralt beliggende indløb 5 med et organ til forstøvning af den væske,The FIG. 1, a liquid cylindrical column or shaft 1 having a downwardly conical narrowing lower shaft portion 2 having a lower outlet opening 3 through which liquid, partially or completely dried powder can be removed from the apparatus, is shown. The shaft 1 has at the top a top wall 4 with a centrally located inlet 5 known per se with a means for atomizing the liquid.

3 DK 153104 B3 DK 153104 B

der skal tørres. Apparatet har endvidere en indløbet 5 koncentrisk omgivende ring 6 af nedad rettede indstrømningsåbninger til tilførsel af tørregas. Tørregassen strømmer derfor koncentrisk omkring indløbet 5. I den koniske nedre skaktdel 2's væg findes et antal tangentialt rettede åbninger 7, der står i forbindelse med et rør 8 til tilførsel af skyllegas, f.eks. luft, der tilføres ved hjælp af en blæser 9. Umiddelbart ved topvæggen 4 findes i skaktens cylindriske vægparti en udstrømningsåbning 10 til fjernelse af spildgassen. Denne åbning 10 står i forbindelse med en cyklonudskiller 11 med en blæser 12 til udskillelse af i spildgassen endnu tilstedeværende fine tørstofpartikler.that must be dried. The apparatus further has an inlet 5 concentric surrounding ring 6 of downwardly directed inflow openings for supply of dry gas. The drying gas therefore flows concentrically around the inlet 5. In the wall of the conical lower shaft part 2 there are a number of tangentially directed openings 7 which are connected to a pipe 8 for supply of flushing gas, e.g. air supplied by a blower 9. Immediately at the top wall 4, in the cylindrical wall portion of the shaft, there is an outlet opening 10 for removing the waste gas. This aperture 10 communicates with a cyclone separator 11 with a fan 12 for the separation of still fine solids present in the waste gas.

Gassens strømningsbane i skakten l's øvre del og dens nedre koniske del 2 er antydet ved pile, der viser, at tørregassen passerer nedad i kammeret i form af et hovedsageligt cylindrisk forhæng og herved tørrer de forstøvede væskedråber fra indløbet 5. Når gassen er nået ned til et vist niveau i skaktens koniske del 2, strømmer gassen radialt udad til alle sider og dernæst i en bue opad, hvorefter gassen passerer ud gennem udstrømningsåbningen 10. Skyllegassen indføres i skakten med en strømningshastighed på over 10 m/sek. og tilnærmelsesvis i det koniske skaktparti 2's halve højde. Denne gas strømmer turbulent opad på en skruelinieformet strømningsbane umiddelbart inden for skaktens væg og passerer ligeledes ud gennem åbningen 10. Den tilførte skyllegas hindrer pulverpartiklerne i at komme i berøring med indersiden af det koniske skaktparti 2's væg, så at pulveret ikke vil kunne hænge fast på væggen og danne påbagninger på denne. På denne måde holdes materialeudløbsåbningen 3 åben, så at apparatet kan arbejde kontinuerligt i lang tid.The flow path of the gas in the upper portion of the shaft 1 and its lower tapered portion 2 is indicated by arrows showing that the drying gas passes downwardly into the chamber in the form of a substantially cylindrical drape, thereby drying the atomized liquid droplets from the inlet 5. When the gas has reached at a certain level in the tapered portion 2 of the shaft, the gas flows radially outward to all sides and then into an arc upwards, after which the gas passes out through the outlet opening 10. The flushing gas is introduced into the shaft at a flow rate of more than 10 m / sec. and approximately half the height of the tapered shaft portion 2. This gas flows turbulently upwardly on a helical flow path immediately within the wall of the shaft and also passes out through the opening 10. The added rinsing gas prevents the powder particles from contacting the inside of the conical shaft portion 2 wall so that the powder will not be able to adhere to the the wall and make embossings on this one. In this way, the material outlet opening 3 is kept open so that the apparatus can operate continuously for a long time.

Fig. 2 og 3 viser de tangentialt rettede åbninger 7 til tilførsel af skyllegassen i en anden udførelsesform. I fig. 1 udmunder tilførselsrøret 8 i en skaktens koniske nedre del 2 omgivende ringkanal 13, med hvilken åbningerne 7 står i forbindelse. I fig. 2 har det i sin helhed nedadtil konisk indsnæv-rende nedre skaktdel 2 et cylindrisk midterste vægparti 14, der er omsluttet et ringformet hus 15. Åbningerne 7 er beliggende i det cylindriske vægparti, så at ringkanalen 15’s indre gen-FIG. 2 and 3 show the tangentially directed apertures 7 for supplying the flushing gas in another embodiment. In FIG. 1, the supply pipe 8 opens into a ring channel 13 surrounding the conical lower part 2 of the shaft, with which the openings 7 are connected. In FIG. 2, the entire downwardly tapered lower shaft portion 2 has a cylindrical middle wall portion 14 enclosed in an annular housing 15. The apertures 7 are located in the cylindrical wall portion so that the inner channel 15

4 DK 153104 B4 DK 153104 B

nem åbningerne står i forbindelse med den koniske nedre skaktdels indre.the openings are easily connected to the interior of the tapered lower shaft.

Fig. 3 viser en ændret version med afbrydelser i den koniske skaktdel 2*s væg til dannelse af tangentiale åbninger 7. .FIG. 3 shows a modified version with interruptions in the wall of the tapered shaft part 2 * to form tangential apertures 7..

Ved alle tre udførelsesformer er åbningerne 7 beliggende i ét og samme niveau. Disse åbninger 7 til tilførsel af skylleluft kan dog også være placeret i forskellig højde i den nedre skaktdel 2*s væg. Under alle omstændigheder bør åbningerne 7 være placeret i et område af væggen, der er beliggende i det mindste et til en femtedel af skaktdelen 2's samlede højde svarende stykke under den koniske skaktdels øvre ende, hvor skaktdelen har sin største diameter.In all three embodiments, the openings 7 are located in one and the same level. However, these openings 7 for supplying rinsing air may also be located at different heights in the wall of the lower shaft portion 2 *. In any case, the openings 7 should be located in an area of the wall located at least one-fifth of the overall height of the shaft portion 2 corresponding to the upper end of the tapered shaft portion, the shaft portion having its largest diameter.

Skylleluftens beskaffenhed, d.v.s. dens temperatur og fugtigheds-indhold bør være således afpasset efter pulverpartiklernes egenskaber, at der ved behandling af partikler af et termoplastisk materiale opnås en køleeffekt, eller en tørreeffekt, såfremt pulverpartiklerne er fugtige. Skyilelufttilførselsåbningerne 7 skal ikke nødvendigvis være rettet nøjagtigt tangentielt, når blot den ind gennem disse passerende skylleluft strømmer langs med den koniske skaktvægs inderside til opnåelse af den tilsigtede "luftfejningseffekt" langs med væggen.The nature of the rinsing air, i.e. its temperature and moisture content should be so adapted to the properties of the powder particles that, when treating particles of a thermoplastic material, a cooling effect or a drying effect is obtained if the powder particles are moist. The sky air supply openings 7 do not necessarily have to be exactly tangentially aligned as it flows in through these passing rinse air along the inside of the conical shaft wall to obtain the intended "air sweep effect" along the wall.

Claims (1)

DK 153104B Patentkrav : Apparat til forstøvningstørring af en væske, f.eks. mælk, og udformet som en hovedsagelig· cylindrisk skakt (1) med mindst én øvre udstrømningsåbning (10) for spildgas, en nedadtil konisk indsnævrende nedre skaktdel (2) med et antal tangen-tialt rettede åbninger (7) og en nederste udløbsåbning (3) for ved væskens tørring dannede pulverpartikler; en topvæg (4) med et centralt indløb (5) for væsken og en væskeindløbet (5) koncentrisk omgivende ring (6) af nedad rettede indstrømningsåbninger for tørreluft, samt med en blæser (9) til tilvejebringelse af en gennem skakten passerende gasstrøm, kendetegnet ved, at de tangentialt rettede åbninger (7) i den koniske nedre skaktdels (2) væg er sluttet til blæserens (9) trykside til indføring af en skyllegasstrøm, der under tryk på en skruelinieformet bane langs med skaktvæggens inderside strømmer op gennem skakten og sammen med tørreluften passerer ud gennem udstrømningsåbningen eller -åbningerne (10) i nærhéden af topvæggen (4).GB 153104B Patent claim: Apparatus for spray drying a liquid, e.g. milk, and formed as a substantially cylindrical shaft (1) having at least one waste gas upper outlet (10), a downwardly conical narrowing lower shaft portion (2) having a plurality of tangentially directed openings (7) and a lower outlet opening (3) ) for powder particles formed during the drying of the liquid; a top wall (4) with a central inlet (5) for the liquid and a liquid inlet (5) concentric surrounding ring (6) of downwardly directed inlet openings for drying air, and with a fan (9) for providing a gas flow passing through the shaft, characterized in that the tangentially directed openings (7) in the wall of the tapered lower shaft part (2) are connected to the pressure side of the blower (9) for introducing a flushing gas stream which flows under pressure on a helical path along the inside of the shaft and together with the drying air passing out through the outflow opening (s) (10) in the vicinity of the top wall (4).
DK365075A 1974-08-13 1975-08-12 SPRAY DRYING APPLIANCE OF A FLUID DK153104C (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
NLAANVRAGE7410860,A NL176018C (en) 1974-08-13 1974-08-13 DEVICE FOR SPRAY-DRYING A SUSPENSION.
NL7410860 1974-08-13

Publications (3)

Publication Number Publication Date
DK365075A DK365075A (en) 1976-02-14
DK153104B true DK153104B (en) 1988-06-13
DK153104C DK153104C (en) 1988-10-31

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ID=19821910

Family Applications (1)

Application Number Title Priority Date Filing Date
DK365075A DK153104C (en) 1974-08-13 1975-08-12 SPRAY DRYING APPLIANCE OF A FLUID

Country Status (8)

Country Link
CH (1) CH592285A5 (en)
DE (1) DE2535961C2 (en)
DK (1) DK153104C (en)
FR (1) FR2281777A1 (en)
GB (1) GB1514824A (en)
IT (1) IT1041228B (en)
NL (1) NL176018C (en)
ZA (1) ZA755152B (en)

Families Citing this family (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE2745078A1 (en) * 1977-10-07 1979-04-19 Bayer Ag METHOD OF DRYING WASTE COPPER CATALYST
FR2473360A1 (en) * 1980-01-09 1981-07-17 Commissariat Energie Atomique DEVICE FOR ATOMIZING A REACTIONAL MIXTURE
US5596817A (en) * 1992-05-21 1997-01-28 Niro Holding A/S Method and an apparatus for minimizing deposits in a drying chamber
CN100398422C (en) * 2003-03-28 2008-07-02 三得利株式会社 Mechanism and method of discharging solid object
JP5510029B2 (en) * 2009-05-25 2014-06-04 株式会社リコー Method for producing toner for developing electrostatic image and apparatus for producing resin particles
RU2459165C1 (en) * 2011-02-09 2012-08-20 Сергей Тихонович Антипов Oven for adsorbent thermal regeneration
EA201991201A1 (en) * 2019-06-14 2020-12-30 Скандсиб Холдингс Лтд CYCLONE EVAPORATOR AND RELATED SEPARATION METHOD
DE102019116770A1 (en) 2019-06-21 2020-12-24 Lübbers Anlagen- und Umwelttechnik GmbH Spray drying device for drying a material to be dried, method for spray drying and dried product

Citations (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1609993A (en) * 1922-11-03 1926-12-07 Ind Waste Products Corp Process of desiccation and products obtained thereby
US1634640A (en) * 1927-07-05 Spbay pbocessing appabatxts
US2081909A (en) * 1934-11-20 1937-06-01 Bowen William Spencer Apparatus for spray drying
US2415527A (en) * 1942-07-03 1947-02-11 Golden State Company Ltd Method of atomizing and desiccating substances and apparatus therefor
US2460546A (en) * 1942-10-01 1949-02-01 C H Wheeler Mfg Co Method and apparatus for treating materials
DE911596C (en) * 1940-07-12 1954-05-17 Cassella Farbwerke Mainkur Ag Method of drying
DE921318C (en) * 1951-01-11 1954-12-16 Degussa Spray dryer
US2703139A (en) * 1950-10-10 1955-03-01 George W Rappleyea Method and apparatus for the complete dehydration of molasses
DE932479C (en) * 1948-10-02 1955-09-01 Ernst Lucke Method and device for drying and cooling atomized material in free fall by means of air-conditioned gases
US2911036A (en) * 1955-01-03 1959-11-03 Melvin E Lazar Spray-drying apparatus
CH353609A (en) * 1956-12-04 1961-04-15 Afico Sa Process for manufacturing a soluble powdered extract of a plant material and installation for its implementation
DE1112015B (en) * 1958-03-28 1961-07-27 Metallgesellschaft Ag Device for keeping the inner wall of spray dryers clean
DE1138025B (en) * 1957-12-21 1962-10-18 Bayer Ag Process for drying silica and silicate fillers
DE1140874B (en) * 1959-12-12 1962-12-06 Wacker Chemie Gmbh Device for trouble-free material throughput in the production of redispersible, heat-sensitive powders in the spray dryer

Patent Citations (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1634640A (en) * 1927-07-05 Spbay pbocessing appabatxts
US1609993A (en) * 1922-11-03 1926-12-07 Ind Waste Products Corp Process of desiccation and products obtained thereby
US2081909A (en) * 1934-11-20 1937-06-01 Bowen William Spencer Apparatus for spray drying
DE911596C (en) * 1940-07-12 1954-05-17 Cassella Farbwerke Mainkur Ag Method of drying
US2415527A (en) * 1942-07-03 1947-02-11 Golden State Company Ltd Method of atomizing and desiccating substances and apparatus therefor
US2460546A (en) * 1942-10-01 1949-02-01 C H Wheeler Mfg Co Method and apparatus for treating materials
DE932479C (en) * 1948-10-02 1955-09-01 Ernst Lucke Method and device for drying and cooling atomized material in free fall by means of air-conditioned gases
US2703139A (en) * 1950-10-10 1955-03-01 George W Rappleyea Method and apparatus for the complete dehydration of molasses
DE921318C (en) * 1951-01-11 1954-12-16 Degussa Spray dryer
US2911036A (en) * 1955-01-03 1959-11-03 Melvin E Lazar Spray-drying apparatus
CH353609A (en) * 1956-12-04 1961-04-15 Afico Sa Process for manufacturing a soluble powdered extract of a plant material and installation for its implementation
DE1138025B (en) * 1957-12-21 1962-10-18 Bayer Ag Process for drying silica and silicate fillers
DE1112015B (en) * 1958-03-28 1961-07-27 Metallgesellschaft Ag Device for keeping the inner wall of spray dryers clean
DE1140874B (en) * 1959-12-12 1962-12-06 Wacker Chemie Gmbh Device for trouble-free material throughput in the production of redispersible, heat-sensitive powders in the spray dryer

Also Published As

Publication number Publication date
IT1041228B (en) 1980-01-10
GB1514824A (en) 1978-06-21
FR2281777B1 (en) 1982-05-07
CH592285A5 (en) 1977-10-31
DE2535961A1 (en) 1976-02-26
NL176018B (en) 1984-09-03
NL176018C (en) 1985-02-01
ZA755152B (en) 1976-07-28
NL7410860A (en) 1976-02-17
DE2535961C2 (en) 1985-01-31
DK153104C (en) 1988-10-31
DK365075A (en) 1976-02-14
FR2281777A1 (en) 1976-03-12

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