DK150308B - DEVICE FOR CONTINUOUS GRAINING OF CEREALS (CERALS) - Google Patents

DEVICE FOR CONTINUOUS GRAINING OF CEREALS (CERALS) Download PDF

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DK150308B
DK150308B DK278483A DK278483A DK150308B DK 150308 B DK150308 B DK 150308B DK 278483 A DK278483 A DK 278483A DK 278483 A DK278483 A DK 278483A DK 150308 B DK150308 B DK 150308B
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grain
floor
shelf
malt
shaped
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DK278483A
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Danish (da)
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DK278483A (en
DK278483D0 (en
DK150308C (en
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Willi Frei
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Froehlich Air Ag
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    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12CBEER; PREPARATION OF BEER BY FERMENTATION; PREPARATION OF MALT FOR MAKING BEER; PREPARATION OF HOPS FOR MAKING BEER
    • C12C1/00Preparation of malt
    • C12C1/027Germinating
    • C12C1/0275Germinating on single or multi-stage floors
    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12CBEER; PREPARATION OF BEER BY FERMENTATION; PREPARATION OF MALT FOR MAKING BEER; PREPARATION OF HOPS FOR MAKING BEER
    • C12C1/00Preparation of malt
    • C12C1/067Drying
    • C12C1/073Processes or apparatus specially adapted to save or recover energy
    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12CBEER; PREPARATION OF BEER BY FERMENTATION; PREPARATION OF MALT FOR MAKING BEER; PREPARATION OF HOPS FOR MAKING BEER
    • C12C1/00Preparation of malt
    • C12C1/125Continuous or semi-continuous processes for steeping, germinating or drying
    • C12C1/13Continuous or semi-continuous processes for steeping, germinating or drying with vertical transport of the grains

Description

150308 i150308 i

Den foreliggende opfindelse angår en indretning til kontinuerlig spiring/tørring (maltning) af korn (ceralier) og af den i krav l's indledning angivne art.The present invention relates to a device for continuous germination / drying (malting) of cereals (cereals) and of the kind specified in the preamble of claim 1.

5 Opfindelsen angår altså et såkaldt vertikal malteri. Sådanne indretninger kendes foruden vandret arbejdende anlæg, såkaldte horisontale malterier, i forskellige udførelsesformer.The invention thus relates to a so-called vertical painting. Such devices are known in addition to horizontal working systems, so-called horizontal moldings, in various embodiments.

Således viser f.eks. DE-fremlæggelsesskrift 16 42 617 et anlæg til kontinuerlig maltning, ved hvilken korngodset transporteres i det væsentlige lodret oppefra og nedefter, og hvor alle behandlingstrin fra vask over blødgøring, kimning indtil tørring, styres og reguleres automatisk. I denne forbindelse benyttes flere med vandrette bånd sammenkoblede skråslidsker, og hvor der til hvert bånd individuelt er tilknyttet varmezone og 15 reguleringsorgan henholdsvis køleapparat og beluftningsanlæg, befugtningsindretning osv. Ved overføring af et gods fra et bånd til et andet via den tilhørende slidsk kastes godset delvis om, således at der sker en omlagring af korngodset. Dette medfører den ulempe, at der ikke er sikret nogen ensmæssig 20 gennemstrømning af korngodset, altså at ikke hvert korn i alle behandlingstrin underkastes de samme ens betingelser. Yderligere er dette kendte anlæg meget dyrt, da det er sammensat af et stort antal indretninger.Thus, e.g. DE Patent Specification 16 42 617 is a continuous malting plant in which the grain goods are transported substantially vertically from top to bottom, and in which all processing steps from washing over softening, germination to drying, are controlled and controlled automatically. In this connection, several inclined slides interconnected with horizontal strips are used, and where each strip is individually associated with heating zone and regulating means, respectively cooling unit and aeration system, humidifier, etc. When transferring a goods from one belt to another via the associated sliding part about, so that the grain goods are rearranged. This causes the disadvantage that no uniform flow of the grain goods is ensured, ie not every grain in all treatment stages is subjected to the same conditions. Furthermore, this known plant is very expensive as it is composed of a large number of devices.

25 En anden indretning til kontinuerlig maltning af korngods (ceralier) fremgår af DE-offentliggørelsesskrift 30 20 511.25 Another device for the continuous malting of cereal goods (cereals) is disclosed in DE Publication 30 20 511.

Dette vertikal-maltningssystem består i det væsentlige af en som behandlingsrum fungerende skakt, hvori der sik-sak-formet er anbragt perforerede slidske, hvorpå korngodset kontinuerlig 30 transporteres oppefra og nedefter, og afhængig af de gennem-vandrede zoner påvirkes med tilsvarende behandlingsmedier, hvilket sker i krydsstrøm til transportretningen. Herved bliver korngodsets opholdstid på slidskene bestemt af en i udtagningskanalen placeret transportør. Ved hjælp af de sik-sak-35 formede anbragte slidske er det ved et forudgivet antal trin pr. zone nødvendigt med en forholdsvis stor skakthøjde. Således skal et vertikalt malteri efter den her anviste udførelsesform have en højde på ca. 80 m. Endvidere er der den ulem- 2 150308 pe, at der ved korngodsstrømmens overgang fra en slidske til den næste henholdsvis ved den derved resulterende retningsændring sker en omlagring af korngodset. Endvidere foreligger en tværsnitsindsnævring ved denne overgang, hvorved der fremkom-5 mer og tilsigtes en relativ forskydning af godskornene henholdsvis, at godsstrømmens korn trækkes ud fra hinanden. Fra litteraturen ("Die Technologie der Malzbereitung", 6. oplag, Ferdinand Enke Verlag Stuttgart 1976, side 304) er det imidlertid kendt, at så længe korngodsets vandindhold er stort, må 10 der ikke vendes under tørringen, da der ellers forekommer en forsinkelse af tørringsprocessen. Maltlaget tørrer nemlig langsomt igennem franeden og opefter. Efter f.eks. 4 til 5 timers svelkningstid er det umiddelbart på hylden liggende malt følgelig tørrere end det, der befinder sig på det øvre lag.This vertical-malting system consists essentially of a shaft acting as a treatment room, in which the zig-zag-shaped perforated slit is arranged, upon which the grain goods are continuously transported from top to bottom and, depending on the traversed zones, are affected by corresponding treatment media, which occurs in cross flow to the transport direction. In this way, the residence time of the grain goods on the slides is determined by a conveyor located in the removal channel. By means of the zig-zak-shaped arranged slots, at a predetermined number of steps per zone required with a relatively large shaft height. Thus, according to the embodiment disclosed herein, a vertical painting must have a height of approx. 80 m. Furthermore, there is the disadvantage that upon the transition of the grain cargo stream from one slit to the next and the resulting change of direction, respectively, a rearrangement of the grain goods takes place. Furthermore, there is a cross-sectional narrowing at this transition, whereby a relative displacement of the grain of grain is obtained and intended, respectively, that the grain of the freight stream is pulled apart. However, from the literature ("Die Technologie der Malzbereitung", 6th edition, Ferdinand Enke Verlag Stuttgart 1976, page 304), it is known that as long as the water content of the grain goods is large, 10 must not be reversed during drying, as there is otherwise a delay of the drying process. The malt layer dries slowly through the front and upwards. After e.g. Accordingly, immediately after the 4 to 5 hour swallowing time, the paint immediately lying on the shelf is drier than that on the upper layer.

15 Hvis man nu vender, så kommer den fugtige malt nederst og de allerede tørre foroven. Herved gennemtrænges det allerede tørrede malt igen af fugt, medens den fugtige igen kommer i området med højere temperatur og således udsættes for den risiko, at det skrumper henholdsvis taber noget skørhed.15 If you turn now, the damp malt will come at the bottom and they will already dry at the top. In this way, the already dried malt is permeated again by moisture, while the moist again comes into the higher temperature range and thus is exposed to the risk of shrinking and losing some brittleness respectively.

2020

Et andet vertikalt malteri kendes fra BE-patentskrift 871.899.Another vertical painting is known from BE Patent Specification 871,899.

Ved dette anlæg indføres korngodset i et behandlingsrum med flere lodret over hinanden anbragte hylder, og bevæges i dette behandlingsrum oppefra og nedefter. Til dette er hver af hyl-derne anbragt drejelig. Til hver af de således udformede hylder er der knyttet en faststående rømmesnegl og en lodret snegl. Ved hjælp af den pågældende faststående rømmesnegl, rømmes i forbindelse med den tilhørende drejelige hylde det nederste dellag fra det på hylden værende korngodslag. Dette 30 dellags korngods når så via en uden for behandlingsrummet beliggende skakt til den derunder beliggende hyldes fordelingssnegl ved hjælp af hvilken det transporterede dellags korngods igen indføres i behandlingsrummet og lægges på den derunder beliggende hyldes korngodslag.At this plant, the grain goods are introduced into a treatment room with several vertical shelves arranged one above the other, and are moved in this treatment room from top to bottom. For this, each of the shelves is arranged pivotally. To each of the shelves thus formed is attached a fixed escape auger and a vertical auger. By means of the fixed escaping auger in question, in connection with the associated rotating shelf, the lower sub-layer is escaped from the grain cargo on the shelf. This 30-part grain cargo then reaches via a shaft located outside the treatment room to the distribution screw of the shelf underneath, by means of which the transported sub-layer grain cargo is again introduced into the treatment room and placed on the grain cargo of the shelf located below.

3535

Ved dette kendte anlæg sker afrømningen af det pågældende nederste dellag af korngodslaget på hver hylde og påføringen af dette afrømmede dellagskorngods på den næste derunder belig- 3At this known facility, the discharge of the respective sub-layer of the grain cargo layer is effected on each shelf and the application of this discharged sub-layer grain cargo to the next below is located.

15 O 3 O S15 O 3 O S

gende hyldes korngodslag, altså på en forholdsvis kompleks og kostbar måde. Det pågældende hyldegulv sammen med det derpå værende korngodslag bliver i sin helhed sat i rotation. Der må altså sættes forholdsvis store masser i bevægelse. Ved hyldens 5 drejning remmer den faststående rømmesnegl dellaget "linieformet" under forløbet af en komplet omdrejning, dvs. i løbet af et vist tidsrum. Det på denne måde bortførte dellag bringes så radialt ud af behandlingsrummet, transporteres aksialt en etage ned og indføres i tilslutning hertil igen radialt i behand-10 lingsrummet og påføres slutteligt ved hjælp af den pågældende fordelersnegl på den derunder beliggende hyldes godslag. Dette betyder, at korngodsets lagdannelse ødelægges, og der dermed er risiko for, at korngodset i forløbet af sin transport gennem det tårnlignende behandlingsrum ikke altid i sin helhed 15 underkastes identiske behandlingsbetingelser med det resultat, at maltens kvalitet nedsættes. Det beskrevne komplekse bevægelsesforløb over flere transportelementer kan desuden føre til en mekanisk beskadigelse af korngodset. Endelig resulterer de forklarede bevægelsesforløb og de deri deltagende aggrega-20 ter i en bekostelig konstruktion for det kendte anlæg.Grain goods are paid homage, in a relatively complex and expensive way. The shelf floor in question, together with the grain grain that is then on, is completely rotated. Thus, relatively large masses must be set in motion. At the turn of the shelf 5, the fixed escape auger brakes the sub-layer "linearly" during the course of a complete rotation, ie. over a certain period of time. The thus removed sub-layers are then radially brought out of the treatment room, axially transported one floor down and subsequently introduced radially into the treatment room and finally applied by means of the respective distributor screw to the goods shelf underneath. This means that the layer formation of the grain goods is destroyed, and there is thus a risk that during the course of its transport through the tower-like treatment room, the grain goods will not always be subjected to identical treatment conditions with the result that the quality of the malt is reduced. Furthermore, the complex movement process described over several transport elements can lead to mechanical damage to the grain. Finally, the explained movements and the units involved therein result in a costly construction for the known plant.

En indretning af den indledningsvist omtalte art kendes endvidere fra DE-patentskrift 60.371. Ved dette anlæg til produktion af malt er der i et skaktlignende behandlingsrum anbragt et antal over hinanden anbragte spiringsbeholdere. Spiringsbe- 25 holderne har alle højt optrukne vægge. De langsgående vægge er i denne forbindelse udformet som kanaler, der står i forbindelse med på beholdergulvene liggende tværkanaler af gennemhullede tagformet anbragte metalplader. Beholderbundens mellem 30 tværkanalerne beliggende afsnit har passager, der nedadtil kan lukkes ved hjælp af skydere henholdsvis jalousier. Ved åbning af skyderne transporteres hele det i spiringsbeholderen tilstedeværende korngodslag til den derunder beliggende spiringsbeholder .A device of the kind mentioned above is further known from DE patent specification 60.371. In this plant for the production of malt, a number of germination containers are arranged in a shaft-like treatment room. The germination containers all have high drawn walls. The longitudinal walls are in this connection formed as ducts which are connected to transverse channels of perforated roof-shaped metal plates lying on the container floors. The sections of the container bottom located between the 30 cross-channels have passages that can be closed downwards by means of sliders and shutters respectively. When the sliders are opened, the whole grain cargo present in the germination container is transported to the germination container located below.

35 I forhold til dette stade for teknikken er det den foreliggende opfindelses formål at videreudvikle den indledningsvist omtalte indretning således, at korngodset i en sådan indretning 4 150308 holdes i en i det væsentlige stadig bevægelse, således at det derved i de enkelte trin kan underkastes en så vidt mulig ens forblivende behandling.In relation to this state of the art, the object of the present invention is to further develop the device mentioned in the introduction so that the grain goods in such a device are kept in a substantially still movement, so that it can thereby be subjected to a single step. as far as possible one's lasting treatment.

5 Dette formål opnås ved, at den indledningsvist omtalte indretning er ejendommelig ved det i den kendetegnende del af krav 1 anførte. Ved hjælp af indretningen ifølge opfindelsen opnås, at korngodset under bibeholdelse af dens dellags relative positioner i det væsentlige kan holdes i en stadig lodret nedadgående bevægelse. Herved underkastes samtlige korngodsan-dele i de enkelte trin en i det væsentlige identisk behandling med det resultat, at man får en ensartet god kvalitet for den på denne måde fremstillede malt. Efter at korngodset uden omstyring holdes i en stadig lodret nedadgående bevægelse, und-går man også i stor udstrækning korngodsets mekaniske beskadigelse. Alt efter udformningen af indretningen ifølge opfindelsen kan lagtykkelsen vælges med hensyn til det nederste dellag, der skal rømmes væk fra den pågældende hylde for så vidt muligt at simulere den tilstræbte stadige lodret nedadgående 20 bevægelse for korngodset.This object is achieved by the fact that the device referred to in the introduction is peculiar to that of the characterizing part of claim 1. By means of the device according to the invention it is obtained that while maintaining the relative positions of its sub-layers, the grain goods can be substantially held in a still vertical downward movement. In this way, all the cereal parts in the individual stages are subjected to a substantially identical treatment with the result that a uniformly good quality is obtained for the malt thus produced. After the grain goods are kept in a still vertical downward movement without steering, the mechanical damage of the grain goods is also largely avoided. Depending on the design of the device according to the invention, the layer thickness may be selected with respect to the lower part layer to be removed from the shelf concerned in order to simulate as far as possible the desired continuous vertical downward movement of the grain goods.

Den med indretningen ifølge opfindelsen opnåede stadige lodrette nedadgående bevægelse for korngodset giver endvidere mulighed for at gennemtrænge dette på denne måde lodret transporterede korngods med tørrings- henholdsvis gennemluftnings-25 mediet ligeledes lodret - enten i medstrøm eller i modstrøm.The continuous vertical downward movement of the grain goods obtained by the device according to the invention furthermore permits to permeate this grain transported in this way vertically with the drying or aeration medium, also vertically - either in co-current or in counter-current.

Herved påvirkes hver korngodsandel for det pågældende dellag af et identisk indstillet medium, f.eks. luft med en forudgiven temperatur og fugtighed. På grund af den stadige lodrette nedadgående transport af korngodset i en relativt fra hinanden 3 0 trukken eller udbredt form sker herved en særlig intim omskylning af korngodset ved hjælp af tørrings- og gennemluftnings-mediet. Hensigtsmæssige videre udformninger for indretningen ifølge opfindelsen fremgår af de uselvstændige krav.Hereby, each grain cargo fraction for that sub-layer is affected by an identical set medium, e.g. air with a predetermined temperature and humidity. Due to the constant vertical downward transport of the grain goods in a relatively apart or widespread form, a particularly intimate rinsing of the grain goods is done by means of the drying and aeration medium. Suitable further designs for the device according to the invention appear from the dependent claims.

35 Nedenfor beskrives opfindelsen yderligere på grundlag af udførelseseksempler under henvisning til tegningen; på denne viser fig. 1 en skematisk gengivelse af et tværsnit gennem et komplet vertikalt maltgøreri, ved hvilken spire- og tørresektionen er udformet ifølge opfindelsen, 5 150308 fig. 2 et tværsnit gennem køllezonen af anlægget, fig. 3 et tværsnit i skematisk gengivelse gennem kølezonen for vertikalkøllen ifølge opfindelsen, fig. 4 et tværsnit gennem en skubbeindretning, som den eksem- 5 pelvis benyttes ved en af sluserne i kølezonen, med U-formet maltskubber og på en akse fastgjort sluseskyder, fig. 5 et snit svarende til fig. 4 med listeformet maltskubber og kun ensidigt via skydeakselen medtagelig sluse- 10 . , skyder, fig. 6 en skematisk gengivelse af et tværsnit gennem et hyldegulv i anlægget ifølge opfindelsen med U-formede gulvelementer, tagformet sammenlukkede indløbsskråflader, en listeformet 15 maltskubber og et under gulvelementet tilvejebragt tilgangs luf trør, fig. 7 en skematisk gengivelse af et tværsnit gennem et hyldegulv i anlægget ifølge opfindelsen svarende til fig. 6, men dog 20 med udelukkende af hulprofiler dannede gulvelementer, der hver danner en tilgangsluftkanal, fig, 8 et snit svarende til fig. 6 med et en tilgangsluftkanal dannende lukket indløbsskråfladetag og med slusesky-25 der.The invention is further described below on the basis of exemplary embodiments with reference to the drawings; FIG. 1 is a schematic representation of a cross-section through a complete vertical malting process in which the sprouting and drying section is designed according to the invention; FIG. 2 is a cross-section through the cooling zone of the plant; FIG. 3 shows a cross-section in schematic representation through the cooling zone of the vertical club according to the invention; FIG. 4 is a cross-section through a pushing device, such as is used, for example, by one of the locks in the cooling zone, with U-shaped malt pushers and a lock slider attached to an axis; FIG. 5 is a sectional view similar to FIG. 4 with molded malt blades and only unilaterally lockable via the shaft 10. , slider, fig. 6 is a schematic representation of a cross-section through a shelf floor of the system according to the invention with U-shaped floor elements, roof-shaped enclosed inlet oblique surfaces, a molded 15 malt pushers and an inlet pipe provided under the floor element; FIG. 7 is a schematic representation of a cross-section through a shelf floor of the system according to the invention corresponding to FIG. 6, but 20 with floor elements formed solely of hollow profiles, each forming an inlet air duct; FIG. 8 is a section similar to FIG. 6 with an inlet air duct forming a closed inlet oblique roof and with locking slides.

Indretningen til kontinuerlig maltning af korn (ceralier) består som vist i fig. 1 af et lodret behandlingsrum 1, der ved hjælp af vandrette hyldegulve 2 er opdelt i zoner med 30 et eller flere trin. Det via kendte transportmidler 3 til behandlingsrummet indførte korn 4, f.eks. byg, lagres i kornbufferlageret 5. Fra dette kornbufferlager 5 når materialet ned på den derunder beliggende hylde, støbekarret 6, hvori kornet enten opblødes med blødgøringsmiddel nede-35 fra eller besprøjtes oppefra. Blødgøringsmidlet. kan imid lertid også indføres i kornlagets indre og fordeles derfra.The device for continuous malting of cereals (cereals) consists as shown in FIG. 1 of a vertical treatment room 1, which is divided into zones with 30 one or more steps by means of horizontal shelf floors 2. The grain 4 introduced via known transport means 3 into the treatment room, e.g. barley, is stored in the grain buffer layer 5. From this grain buffer layer 5, the material reaches down onto the shelf below it, the molding vessel 6, in which the grain is either softened with a plasticizer down or sprayed from above. The plasticizer. however, may also be introduced into the interior of the grain layer and distributed therefrom.

Efter at kornet således er blevet opblødt eller støbt, bringes det på den første af de derunder liggende spiregulve 7 af spirezonen 8. Her vandrer nu det spirende korn fra et 150308 6 gulv til det næste,til det efter opholdet på det sidste spiregulv via under dette anbragte indløbsslidske 9 når ind i køllezonen 10. Køllezonen 10 består af en fortørrer 11, også kaldet grønmaltbufferlageret, en svelkkølleflage 12, en opvarmningskølleflage 13 og en tørrekølleflage 14. Der-5 e efter nar den færdige malt ind i kølezonen 15,der har skrå indløbsvægge og er gennemstrømmet af friskluft og slutteligt via et cellehjul 22 ikke viste udtageindretninger.After the grain has thus been softened or molded, it is brought onto the first of the germinating floors 7 below of the sprout zone 8. Here, the germinating grain now migrates from one floor to the next, until after the last germination floor, via this disposed inlet slit 9 reaches into the cooling zone 10. The cooling zone 10 consists of a pre-dryer 11, also called the green malt buffer storage, a cooling cooling flange 12, a heating cooling flange 13 and a drying cooling flange 14. There, when the finished malt enters the cooling zone 15 which has oblique inlet walls and is flowed in by fresh air and finally via outlet cells 22 not shown.

På højde med det første spiregulv er der tilvejebragt en 10 frisklufttilførsel 16, hvorigennem friskluft ledes til indretningens indre. Til hver to spiregulve 7 er der tilknyttet en ventilator 17 til at tilføre spiregulvene luft og dermed til gennemluftning af materialet. Den friske luft når fra frisklufttilførslen 16 vertikalt ned, hvor den, forvarmet 15 af afgangsluften ved hjælp af en varmeveksler 18, når ind i tørrelufttilberedningen 19. Tørrelufttilberedningen 19 består i det væsentlige af en blæser 20, der driver den forvarmede friskluft gennem en luftopvarmer 21. Fra luftop-varmeren 21 når luften gennem tørrekølleflagen 14, opvarm- 20 ningskølleflagen 13 og svelkkølleflagen 12 for at strømme ud til den ydre luft via den gennem varmeveksleren 18 førte afgangsluftledning 23.At the level of the first sprout floor, a fresh air supply 16 is provided, through which fresh air is conducted to the interior of the device. To each of two sprout floors 7, a fan 17 is connected to supply air to the sprout floors and thus to ventilate the material. The fresh air reaches vertically from the fresh air supply 16 where it, preheated 15 by the exhaust air by means of a heat exchanger 18, enters the dry air preparation 19. The dry air preparation 19 consists essentially of a blower 20 which drives the preheated fresh air through an air heater 21 From the air heater 21, the air reaches through the drying cooling flange 14, the heating cooling flange 13 and the swell cooling flange 12 to flow to the outside air via the exhaust air line 23 passed through the heat exchanger 18.

I fig. 2 ses en vertikal kølle, der foruden en dagtank til 25 grønmalt 24 har kølleflager for svelkning 12, opvarmning 13 og tørring 14 samt kølezonen 15. Fra luftopvarmeren 21 kan omløbsledninger 25 henholdsvis 26 føre til kølleflagerne 12 henholdsvis 13. Desuden kan den fra afgangskanalen 23 udledte afgangsluft via en ledning 27 føres til dagtanken 24 30 for at fortørre den deri værende grønmalt. 1 fig. 3 ses skematisk en fordelagtig udformning af kølezonen 15. Heraf fremgår, at der under tørrekølleflagen 14 findes af indløbsslidske 37 og 38 dannede kanaler, der via 35 nærmere nedenfor beskrevne sluser 40 transporterer materialet til en af perforerede indløbsslidske 39 bestående samleskakt 41. Køleluftrørene 42 gennemblæses med friskluft gennem ind-løbsslidskene 39's perforeringer, der afkøler der her værende, endnu forholdsvis varme materiale. Ved en samleskakt 41's bund er der anbragt en yderligere sluse, via hvilken materialet 7 150308 når til et cellehjul 22 og en til dette knyttet, roen ikke vist bortrydningsindretning. Under tørrekølleflegen 14 befinder der sig to til-gangsluftrør 43, via hvilken der tilføres varmluft til tørrekøllef lagen 14. Medens der i det viste tilfælde kun er anbragt et cellehjul 22 under den nederste sluse 40 kan det også 5 tænkes, at der ligeledes er anbragt cellehjul under de øvre sluser 40. Men der er også muligt udelukkende af fremstille sluserne ved tilsvarende udformede cellehjul.In FIG. 2 shows a vertical keel which, in addition to a day tank for 25 green malt 24, has cooling flakes for swallowing 12, heating 13 and drying 14 and the cooling zone 15. From the air heater 21, bypass lines 25 and 26 can lead to the cooling flaps 12 and 13. Furthermore, it can from the outlet duct 23 discharged exhaust air via a conduit 27 is fed to the day tank 24 30 to dry the green malt contained therein. 1 FIG. 3 shows schematically an advantageous design of the cooling zone 15. From this it can be seen that under the drying cooling flange 14 there are channels formed in inlet slots 37 and 38 which transport via 35 the locks 40 described in greater detail below to a collection shaft 41 of perforated inlet slots 39. with fresh air through the perforations of the inlet slides 39, which cools the still relatively warm material present here. At the bottom of an assembly shaft 41, an additional lock is arranged, through which the material 7 reaches a cell wheel 22 and an attachment device not shown, which is not shown. Under the drying heat sink 14 there are two supply air pipes 43, through which hot air is supplied to the drying heat sink 14. While in the case shown, only one cell wheel 22 is placed under the lower lock 40, it is also possible that 5 is also provided. cell wheels under the upper locks 40. But it is also possible only to manufacture the locks by similarly designed cell wheels.

I fig. 4 ses skematisk en sluse 40, der i det væsentlige be- 10 står af indløbsslidskene eller -væggene 37 og 38, hvis nedre kanter har en given afstand fra hinanden og således danner en maltpassage 44. Under denne passage er der anbragt en U-formet maltskubber 45, der med sine ben hviler forskydeligt på et nærmere nedenfor beskrevet gulvelement 46. Her er der tilvejebragt en aksel, der er ført gennem maltskubberen 45's to ben, og på hvilken maltskubberen 45 er fastgjort, f.eks. ved hjælp af skiver 48 og stifter 49. På begge sider af slusen 40 er der anbragt en væg 50, der begge har et trin 51 og et ben 52 anbragt på en sådan måde, at trinnet 51 ligger på samme højde 20 som gulvelementet 461 s vandrette del og benet 52 med gulvelementet 46's ben 53 danner en lodret passage i form af spalter 54. I væggene 50 er der tilvejebragt lejer 55 til at optage akselen 47. På akselen 47 er der midt over hver spalte 54 ved hjælp af skiver 48 og stifter 49 fastgjort sluseskydere 56, 25 der lukker passagerne oppefra. Indløbsslidskene 37 og 38 har ved deres nedre'ender i retning mod spaltene 54 pegende forlængelser 57. Forskydes akselen 47 med derpå værende maltskubbere 55 henholdsvis 56, skubbes malten, der er kommet ind i mellemrummet mellem maltskubberen og den ene skyder, hver gang 30 ind i en spalte 54, således at maltet falder gennem disse spalter 54 for at komme ned på det nedenunder liggende hyldegulv henholdsvis i den derunder beliggende samleskakt 41 (fig.In FIG. 4 is a schematic view of a lock 40 consisting essentially of the inlet slides or walls 37 and 38, the lower edges of which are at a given distance from each other and thus form a malt passage 44. Under this passage, a U-shaped is arranged. malt scrubber 45, which with its legs rests slidably on a floor element 46 described below. Here, there is provided a shaft which is passed through the two legs of malt scrubber 45 and to which the malt scrubber 45 is secured, e.g. by means of washers 48 and pins 49. On both sides of the lock 40 a wall 50 is provided, both having a step 51 and a leg 52 arranged in such a way that the step 51 is at the same height 20 as the floor element 461 s. the horizontal portion and the leg 52 with the leg 53 of the floor element 46 form a vertical passageway in the form of slots 54. In the walls 50, bearings 55 are provided for receiving the shaft 47. On the shaft 47 there is in the middle of each slot 54 by means of washers 48 and pins 49 attached lock sliders 56, 25 which close the passages from above. The inlet slides 37 and 38 have at their lower ends in the direction towards the slots 54 pointing extensions 57. If the shaft 47 is displaced by the malt pushers 55 and 56, respectively, the malt entered into the gap between the malt pusher and the one slider each time 30 is inserted. in a slot 54 so that the malt falls through these slots 54 to come down on the shelf floor below, respectively, in the collecting shaft 41 located below it (fig.

3).3).

35 Den i fig. 5 viste sluse 58 har i det væsentlige den samme konstruktion som slusen 40 vist i fig. 4. Haltskubberen 60 er udformet som en liste, medens sluseskyderne 59 er væsentlig større end sluseskyderen 56 vist i fig. 4. Desuden er den på- 8 150303 gældende sluseskyder 59 kun på én side forsynet med et anslag bestående af en skive 48 og en stift 49, således at den pågældende skyder 59 kun ved sin pågældende indadrettede forskydning medtages af akselen 47. Ved sin udadrettedeforskydning g føres skyderen 59 tilbage af den mellem maltskubberen 60 og skyderen 59 værende og af maltskubberen 60 skubbede malt langs med akselen 47. Denne udførelsesform har den fordel, at skyderen 59 forbliver i lukket stilling, fordi der ikke er noget materiale til stede, der ved maltskubberen 60's forskydning 10 medtager sluseskyderen 59. Derved bliver trods maltskubberens 60's forskydning spalten 54 lukket, når der udebliver materiale, således at der heller ikke finder nogen luftgennemstrømning sted.35 The embodiment of FIG. 5 locks 58 have essentially the same construction as the lock 40 shown in FIG. 4. The slider 60 is designed as a list, while the slider 59 is substantially larger than the slider 56 shown in FIG. 4. In addition, the lock slider 59 in force is provided on one side only with a stop consisting of a washer 48 and a pin 49, so that the slider 59 is included in the shaft 47 only with its inward displacement in question. g, the slider 59 is moved back by the sleeve 59 between the slider 60 and the slider 59 and the slider 59 is pushed along the shaft 47. This embodiment has the advantage that slider 59 remains in the closed position because no material is present which The displacement 10 of the malt pusher 60 includes the lock slider 59. Thus, despite the displacement of the malt pusher 60, the slot 54 is closed when no material is left, so that no air flow also takes place.

15 Fig. 6, 7 og 8 viser udførelsesformer på hyldegulve (støbekar, spiregulv, kølleflager), der i det væsentlige indeholder de samme grundelementer som sluserne vist i fig. 4 og 5, Hyldegulvene består af flere ved siden af hinanden anbragte gulvelementer, der i udførelseseksemplerne ifølge fig. 6 og 8 be-20 står af U-længdeprofiler 46, medens de som vist i fig. 7 består af hulprofiler 46a. Gulvelementerne 46, 46a's ben 53 er som vist anbragt med en sådan indbyrdes afstand, at der mellem dem dannes spalter 54. Som vist i fig. 6 er der i det væsentlige midt under hver gulvelement 46 anbragt et med dyser 61 25 udstyret tilgangsluftrør 52 på en sådan måde, at den fra dette rør under tryk udstrømmende luft strømmer gennem spalterne 54, hvorfra den strømmer igennem perforeringer i et tagformet afdækning eller tag 63, der danner indløbsskråflader, for at gennemstrømme materialet. Tagets indløbsslidske 37 og 38 er vist 30 i fig- 4 og 5. De danner altså en materialepassage 44, hvorigennem kornmaterialet når til den listeformede skubber 60 for af denne afhængig af slagretningen at skubbes til den ene eller anden spalte 54.FIG. Figures 6, 7 and 8 show embodiments of shelf floors (molding vessels, spiral floors, chill floors) containing substantially the same basic elements as the locks shown in FIG. 4 and 5, The shelf floors consist of several adjacent floor elements which in the exemplary embodiments of FIG. 6 and 8 consist of U-length profiles 46, while as shown in FIG. 7 consists of hole profiles 46a. As shown, the leg 53 of the floor elements 46, 46a is spaced apart so that slots 54 are formed between them. As shown in FIG. 6, an inlet air tube 52 equipped with nozzles 61 25 is disposed substantially in the middle of each floor element 46 in such a way that the air flowing from this pipe under pressure flows through the slots 54 from which it flows through perforations in a roof-shaped cover or roof. 63, forming inlet inclined surfaces, to flow through the material. The inlet slots 37 and 38 of the roof are shown 30 in Figures 4 and 5. Thus, they form a material passage 44 through which the grain material reaches the molded push 60 to be pushed to one or the other 54 depending on the direction of impact.

35 Som allerede nævnt er de i fig.7 viste gulvelementer 46a dannet af hulprofiler. Disse hulprofiler danner samtidigt en tilgangsluftkanal af lignende art som tilgangsluftrøret 62 for anordningen vist i fig.6 , hvorfor de er udstyret med dyser 61a.35 As already mentioned, the floor elements 46a shown in Fig. 7 are formed of hollow profiles. These hollow profiles simultaneously form an inlet air duct similar to the inlet air duct 62 for the device shown in Fig. 6, and therefore they are provided with nozzles 61a.

9.9th

150308150308

Det i fig. 8 viste hyldegulv har i sammenligning med det i fig. 6 viste en U-formet sluseskyder 56, der, når maltskubberen 60 er i midterstilling, lukker passagen 54. Desuden har taget 63 på sin underside en U-formet afslutning 65, 5 hvorved der dannes en lukket og i det væsentlige femkantet lufttilførselskanal 66. Denne lufttilførselskanal 66 oyer-tager nu den i fig.6 viste lufttilførselskanal 62's rolle kombineret med taget 63 fra denne figur. Herved realiseres en meget kompakt byggemåde. Materialepassagen 44, der er 10 dannet mellem afslutningen 65’s lodrette vægge, har i det væsentlige den samme bredde som et dobbeltslag for maltskubberen 60. Dermed sikres, at, når skubberen 60 befinder sig i den ene eller den anden endeposition 67 eller 68, vil materialet eller maltet hver gang i det væsentlige kun falde 15 på den ene side af skubberen, hvorved man undgår materiale ophobninger mellem skubberne.The FIG. 8, in comparison with the shelf floor shown in FIG. 6 shows a U-shaped lock slider 56 which, when the malt pusher 60 is in the center position, closes the passage 54. In addition, the roof 63 has on its underside a U-shaped end 65, 5 thereby forming a closed and substantially pentagonal air supply channel 66. This air supply channel 66 now takes on the role of air supply channel 62 shown in combination with the roof 63 of this figure. This results in a very compact construction method. The material passage 44 formed between the vertical walls of the end 65 has substantially the same width as a double stroke of the malt push 60. This ensures that when the push 60 is in either end position 67 or 68, the material will or the malt each time essentially only falls 15 on one side of the pusher, thereby avoiding material buildup between the pushers.

Indretningen til kontinuerlig maltning henholdsvis tørring af korn (ceralier) ifølge opfindelsen arbejder på følgende 20 måde;The device for continuous malting and drying of cereals (cereals) according to the invention operates in the following manner;

Kommer maltet eller materialet ned på et af de i fig. 6 eller 7 viste hyldegulve - almindeligvis findes der på hyldegulvene et lag på ca. 80 cm kornraateriale - og er opholdstiden 25 afsluttet for det nederste lag, sættes skubbeindretningen i gang. Via en ikke vist betjeningsindretning forskydes akselen 47 derved aksialt i retning af det i forvejen bestemte slag. Herved skubbes kornmaterialet, der via kornpassagen 44 er kommet ned ved siden af korn- eller maltskubberen 60 30 og befinder sig på bevægelsesretningens side, foran malt skubberen 60, indtil det falder ind i spalten 54. Det ind i spalten kommende kornmateriale eller malt 4 falder nu ved sin egen vægt gennem spalten 54, hvorunder det samtidigt omskylles af kraftigt strømmendeluft. Derved løsner korn-35 materialets enkelte korn sig fra hinanden og risler gennem det mellem det derunder beliggende kornmateriale- eller maltlag og det øvre hyldegulv værende, forholdsvis høje frie rum, indtil det kommer til at ligge på overfladen af korn- 150308 ίο materiale- eller maltlaget på det derunder liggende hylde-gulv. Herved har man fået den fordel, at kornmaterialet ellet maltet, der er under spiring, henholdsvis er spiret færdigt, med mellemrum flere gange skubbes gennem en passage og 5 risler ned i frit fald, således at der på grund af, at de enkelte korn løsner sig fra hinanden, ikke kan finde en sammenfiltring sted. Der foregår heller ikke en omlejring eller ændring af lagfølgen, hvilket kunne have en negativ virkning på kornets kvalitet. Da der ved hjælp af den forholds-10 vis smalle maltskubber f.eks. kun hver 8. min. gennemføres en forskydning eller skubning, altså et enkelt slag, borttransporteres kun et forholdsvis tyndt kornmateriale- eller maltlag, hvis korn ialt har den samme temperatur- og fugtig-hedsgrad. Kornmaterialet rasler altså så at sige eller tills nærmelsesvist kontinuerligt, f.eks. hvert 8. min., gennem de mellem gulvelementerne 46, 46a værende spalter 54, hvilket fortrinsvis sker samtidigt med alle hyldegulve, således at der i praksis foregår en kontinuerlig nedad bevægelse af kornmaterialet, hvorved hvert korn deltager i en i det væ-20 sentlige lodret faldvej til forneden i kølezonen. I modstrøm hertil ledes der især i køllezonen behandlingsmedium. Dette medfører en yderst ensartet behandling af alt kornmateriale. Ankommet i kølezonen ledes kornmaterialet eller maltet som vist i fig. 3 via de to indløbskanaler dannende indløbsslid-25 ske 37 og 38 til de pågældende to sluser, der arbejder på omtrent samme måde som hyldegulvskubbeindretningen. Kornmaterialet eller maltet skubbes ligeledes af en maltskubber 45 eller 60 afhængig af slaget mod venstre eller højre ind i en spalte 54 og risler derved ned i den nederste samle-30 skakt 41, hvor det endnu gennemskylles og afkøles ved hjælp af yderligere køleluft. Slutteligt når maltet til den sidste sluse 40, ved hvilken den ligeledes skubbes ved hjælp af en maltskubber af samme konstruktion i tilsvarende spalter 54 for slutteligt via en indløbsslidsk at falde på det langsomt, 35 f.eks. med én omdrejning pr. min. drejende, cellehjul og af dette blive skubbet ind på transportmidler.If the malt or material settles on one of the pipes in FIG. 6 or 7 shelves - usually a layer of approx. 80 cm grain material - and when the dwell time 25 is completed for the lower layer, the pushing device is started. By means of a control device (not shown), the shaft 47 is thereby displaced axially in the direction of the predetermined stroke. Hereby, the grain material, which has come down via the grain passage 44, descends next to the grain or malt scrubber 60 30 and is on the side of the direction of movement, in front of the malt scrubber 60 until it falls into the slot 54. The grain material or malt 4 which falls into the gap now at its own weight through the slot 54, under which it is simultaneously flushed by strong stream end air. Thereby, the single grain of the grain material detaches from one another and ripples through the relatively low free space between the grain material or malt layer and the upper shelf floor, until it lies on the surface of grain or material. the malt layer on the shelf floor below. This has the advantage that the grain material or malt, which is sprouted or germinated, respectively, is periodically pushed several times through a passage and 5 sprinkles into free fall, so that because of the individual grains loosening apart, no tangling can take place. There is also no rearranging or changing of the layer order, which could have a negative effect on the quality of the grain. Since, with the aid of the relatively narrow malt blocks, e.g. only every 8 min. For example, if a shear or shear, ie a single stroke, is carried out, only a relatively thin grain material or malt layer is transported away, the grain of which generally has the same degree of temperature and humidity. Thus, the grain material rattles, so to speak, or until almost continuously, e.g. every 8 minutes, through the gaps 54 between the floor elements 46, 46a, which preferably occur simultaneously with all shelf floors, so that in practice there is a continuous downward movement of the grain material, whereby each grain participates in a substantially vertical drop-down to the bottom of the cooling zone. In the countercurrent to this, treatment medium is directed especially in the cold zone. This results in a very uniform treatment of all grain material. Arriving in the cooling zone, the grain material or malt is guided as shown in FIG. 3 through the two inlet ducts 37 and 38 forming the respective two locks, which operate in much the same way as the shelf floor pushing device. The grain material or malt is also pushed by a malt scrubber 45 or 60, depending on the stroke to the left or right, into a slot 54, thereby rubbing down into the lower collecting shaft 41 where it is still flushed and cooled by further cooling air. Finally, the malt reaches the last lock 40, at which it is also pushed by means of a malt scrubber of the same construction in corresponding slots 54 for finally falling on it slowly via an inlet slit, e.g. with one revolution per mine. rotating, cell wheel and of this being pushed into means of transport.

Claims (4)

150308 Patentkrav.150308 Patent Claims. 1. Indretning til kontinuerlig spiring/tørring af korngods (ceralier) aed et skaktformet behandlingsrun (1), hvori der er 5 anbragt flere lodret over hinanden anbragte hyldegulve (2), i hver af hvilke der er tilvejebragt lodrette passager i fora af gennemgående længde- henholdsvis tværspalter (54), og hvor der til hver af gulvene er tilknyttet en skubbeindretning, således at korngodset kan transporteres fra et hyldegulv (2) 10 til et andet oppefra og nedefter gennem behandlingsrumaet (1), kendetegnet ved, at der til borttransport af det pågældende nederst på et hyldegulv (2) liggende dellag a) over hver spalte (54) i spirezonen er tilvejebragt en tag-15 formet perforeret afdækning (63), hvis nederste kanter har en sådan afstand fra hyldegulvet (2, 46, 46a), at der mellem den tagformede afdæknings (63) underkanter og hyldegulvet (2, 46, 46a) dannes en vandret korngodspassage, og 20 b) hyldegulvets (2, 46, 46a) skubbeindretning har flere på tværs af spalterne anbragte aksler (47), hvorpå korngods-skubbere (45, 60) er anbragt på en sådan måde, at disse med deres underside liggende an imod hyldegulvet (2, 46, 46a) kan forskydes på tværs af de lodrette spalter (54) på en n_ sådan måde, at korngodset kan skubbes gennem de vandrette 2 5 korngodspassager til de lodrette spalter (54).Device for continuous germination / drying of cereals (cereals) of a shaft-shaped treatment round (1), in which there are 5 vertically arranged shelf floors (2), in each of which vertical passages in forums of continuous length are provided. transverse slots (54), respectively, and to which each of the floors is connected a pushing device, so that the grain goods can be transported from one shelf floor (2) 10 to another from top to bottom through the treatment space (1), characterized in that for away transport a sub-layer (a) above each slit (54) in the sprout zone of the respective bottom of a shelf floor (2) is provided with a roof-shaped perforated cover (63), the lower edges of which have such a distance from the shelf floor (2, 46, 46a) ) that a horizontal grain cargo passage is formed between the lower edges of the roof-shaped cover (63) and the shelf floor (20) and the biasing device of the shelf floor (2, 46, 46a) has several shafts (47) arranged across the slots. . on which grain goods pushers (45, 60) are arranged in such a way that they with their underside abutting against the shelf floor (2, 46, 46a) can be displaced across the vertical slots (54) in such a way that the grain cargo can be pushed through the horizontal grain cargo passages to the vertical slots (54). 2. Indretning ifølge krav 1, kendetegnet ved, at kornmaterialeskubberne (60) har en i det væsentlige listeformet udformning og med deres smalside forskydeligt ligger an 30 mod det tilhørende gulvelement (2, 46, 46a).Device according to claim 1, characterized in that the grain material pushers (60) have a substantially molded configuration and with their narrow side slidably abut against the associated floor element (2, 46, 46a). 3. Indretning ifølge krav 1, kendetegnet ved, at kornmaterialeskubberne (45) er udformet U-formede og med deres ben ligger forskydeligt på det tilhørende gulvelement (2, 46, 35 46a).Device according to claim 1, characterized in that the grain material pushers (45) are formed U-shaped and with their legs are displaceable on the associated floor element (2, 46, 35 46a). 4. Indretning ifølge krav 1, kendetegnet ved, at der på gulvelementerne (2, 46, 46a)ikøledelen af tørrezonen er tilvejebragt U-formede sluseskydere (56), der hver kan ind-Device according to Claim 1, characterized in that on the floor elements (2, 46, 46a) the cooling part of the drying zone is provided with U-shaped lock sliders (56), each of which can be inserted.
DK278483A 1982-06-30 1983-06-16 DEVICE FOR CONTINUOUS GRAINING OF CEREALS (CERALS) DK150308C (en)

Applications Claiming Priority (2)

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DE3224471 1982-06-30
DE3224471A DE3224471C2 (en) 1982-06-30 1982-06-30 Device for continuous malting of cereal grain

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DK278483A DK278483A (en) 1983-12-31
DK150308B true DK150308B (en) 1987-02-02
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Families Citing this family (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE3346245C1 (en) * 1983-12-21 1985-04-04 Air Fröhlich AG für Energierückgewinnung, Arbon Device for the continuous malting of cereal grain
DE3407685C1 (en) * 1984-03-02 1985-08-14 Bühler-Miag GmbH, 3300 Braunschweig Process and plant for kilning green malt
DE3429041A1 (en) * 1984-08-07 1986-02-20 Gebr. Lausmann KG, 8400 Regensburg Process and device for kilning or drying germinated cereal grain material
JPH0334957Y2 (en) * 1985-06-17 1991-07-24
NL8602563A (en) * 1986-10-13 1988-05-02 Philips Nv DEVICE FOR RECORDING AND PLACING COMPONENTS.
DE3815845C1 (en) * 1988-05-09 1989-06-08 Air Froehlich Ag Fuer Energierueckgewinnung, Arbon, Ch
FR2701038B1 (en) * 1993-02-01 1995-04-14 Nordon & Cie Sa Malt kilning process.
ES2276548B1 (en) * 2001-07-12 2008-06-01 Seeger Industrial, S.A. TOWER OF GERMINATION AND / OR TOSTATION FOR MALTERIES.
KR101962919B1 (en) * 2018-11-22 2019-03-28 주식회사 대성마리프 Drying bogie device and drying system including thereof
WO2023017130A1 (en) 2021-08-11 2023-02-16 Bühler AG Method of energy-efficient drying of germinated seeds and apparatus for performing the method
CN117602396B (en) * 2023-11-29 2024-04-30 中国农业大学 Automatic following, throwing and filling method for green fodder harvester

Family Cites Families (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE60371C (en) * C. VOELCKNER und L. SlMONY in Wien IV Apparatus for the production of pneumatic barn malt
DE14071C (en) * N. J. «GALLAND in Paris Improved system of pneumatic soft floors and malt kilns
DE725739C (en) * 1939-12-12 1942-09-29 Metallgesellschaft Ag Device for discharging the adsorbent from adsorbers
US2654691A (en) * 1951-03-14 1953-10-06 Jr Edward E Frauenheim Malting apparatus
DE1221180B (en) * 1961-04-15 1966-07-21 Ottilie Charlotte Geys Geb Len Plant for malt preparation
DE1642617B2 (en) * 1968-02-07 1975-10-16 Forschungsinstitut Fuer Die Gaerungsindustrie, Enzymologie Und Technische Mikrobiologie, X 1017 Berlin Process for the automatic control and regulation of continuous malting processes and a system for carrying out this process
BE871899A (en) * 1978-11-10 1979-03-01 Somer A De KONTINU, DISKONTINU GERMINATION SYSTEM FOR MALT, KONTINU, DISKONTINU EEST OR DRYING SYSTEM FOR MALT, GRAIN AND OTHER GRANULAR OR FROSTY PRODUCTS.
DE3020511A1 (en) * 1980-05-30 1981-12-10 Bühler-Miag GmbH, 3300 Braunschweig METHOD AND DEVICE FOR CONTINUOUS MELTING OF CEREAL GRAINS

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ES8502155A1 (en) 1984-12-16
ES523366A0 (en) 1984-12-16
DE3224471C2 (en) 1984-07-26
AU1641983A (en) 1984-01-05
DK278483A (en) 1983-12-31
DE3224471A1 (en) 1984-01-05
EP0097965A3 (en) 1986-08-13
DK278483D0 (en) 1983-06-16
DK150308C (en) 1988-01-11
EP0097965A2 (en) 1984-01-11
JPS5917975A (en) 1984-01-30

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