EP3102318A1 - Procédé et dispositif de mélange et de dosage de matières à doser solides dans un liquide porteur - Google Patents

Procédé et dispositif de mélange et de dosage de matières à doser solides dans un liquide porteur

Info

Publication number
EP3102318A1
EP3102318A1 EP15705190.5A EP15705190A EP3102318A1 EP 3102318 A1 EP3102318 A1 EP 3102318A1 EP 15705190 A EP15705190 A EP 15705190A EP 3102318 A1 EP3102318 A1 EP 3102318A1
Authority
EP
European Patent Office
Prior art keywords
solid
air
volume flow
container
volume
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
EP15705190.5A
Other languages
German (de)
English (en)
Other versions
EP3102318B1 (fr
Inventor
Wolfgang SCHLÖSSER
Ludger LÜTKE SUNDERHAUS
Jürgen GEHLING
Erwin Süthold
Uwe Schwenzow
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
GEA TDS GmbH
Original Assignee
GEA TDS GmbH
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by GEA TDS GmbH filed Critical GEA TDS GmbH
Publication of EP3102318A1 publication Critical patent/EP3102318A1/fr
Application granted granted Critical
Publication of EP3102318B1 publication Critical patent/EP3102318B1/fr
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
    • B01F23/50—Mixing liquids with solids
    • B01F23/53—Mixing liquids with solids using driven stirrers
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
    • B01F23/50—Mixing liquids with solids
    • B01F23/56—Mixing liquids with solids by introducing solids in liquids, e.g. dispersing or dissolving
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
    • B01F25/10—Mixing by creating a vortex flow, e.g. by tangential introduction of flow components
    • B01F25/103—Mixing by creating a vortex flow, e.g. by tangential introduction of flow components with additional mixing means other than vortex mixers, e.g. the vortex chamber being positioned in another mixing chamber
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
    • B01F25/20—Jet mixers, i.e. mixers using high-speed fluid streams
    • B01F25/27—Mixing by jetting components into a conduit for agitating its contents
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F33/00—Other mixers; Mixing plants; Combinations of mixers
    • B01F33/40—Mixers using gas or liquid agitation, e.g. with air supply tubes
    • B01F33/402—Mixers using gas or liquid agitation, e.g. with air supply tubes comprising supplementary stirring elements
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F35/00—Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
    • B01F35/20—Measuring; Control or regulation
    • B01F35/22—Control or regulation
    • B01F35/221—Control or regulation of operational parameters, e.g. level of material in the mixer, temperature or pressure
    • B01F35/2212—Level of the material in the mixer
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F35/00—Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
    • B01F35/71—Feed mechanisms
    • B01F35/711—Feed mechanisms for feeding a mixture of components, i.e. solids in liquid, solids in a gas stream

Definitions

  • the invention relates to a method for mixing and dosing solid doses, such as at least one cereal, in particular a solid-like, particulate, swellable cereal, and / or at least one other small admixture, in a carrier liquid with which a mixture of the carrier liquid and the at least one solid dosage material is produced, in which a volume of carrier liquid and the at least one solid Dosiergut respectively fed forcibly in stationary operation and all mixing components are mixed together in a stationary volume of the mixture, in which the mixture with a constant volume flow mixture steadily and forcibly from the volume presented is removed, in which the presented volume, which has a free level, regulated by this free level and thus kept constant, in which the volume flow carrier liquid and optionally a volume flow of air kept constant and steady and continuously provided and in each case quantitatively presettable and can be changed within limits, in which the volume flow carrier liquid is introduced below the free level in the mixture, that in this flow-mechanically a rotational flow is generated, in which the supply of at least one solid metered
  • the invention further relates to a device for carrying out the method.
  • the mixture is at the end of its further treatment in a metering downstream process plant to a drinkable mixture, preferably consisting of drinking milk as a carrier liquid and the at least one solid Dosiergut, such as rice or / and oats as Zerealie / n, prepared by application of the method and the device according to the invention.
  • Drinkable mixture means in the present case that these are not in spoonable or spoon-solid consistency must be consumed, but can be easily absorbed with a straw or drinking straw.
  • cereals should also include, for example, wheat grains that are only watered with cold water, as well as other solids-like, small-sized admixtures such as fruits, nuts or seeds. Solid-like should be considered a cereal or admixture, if it is not destroyed by heat or mechanical action in the treatment process and thus, for example, largely retains its grain structure.
  • small piece is intended to quantify a cereal or admixture which is still perceptible with a minimum amount when drinking (for example seeds or the like with a largest particle diameter of 1 to 2 mm) or which can still be drinkable with a maximum particle size of not more than 5 mm is, especially with a straw or drinking straw.
  • An apparatus for carrying out the method of the generic type is known from DE 38 03 217 A1. It discloses a device for mixing and dosing solid and liquid doses, such as powders, granules or the like. In water and liquid dosing, such as dispersions, emulsions, with difficult-to-mix properties with water.
  • the device has a mixing reactor chamber, wherein the metered goods are introduced by means of air in the closed, pressurized mixing reactor chamber and a distance air cushion between the water and the Dosiergut is maintained.
  • the forced metering of the metered goods via a metering device in which a driven ball is arranged, in which three blind holes are incorporated, whose positions are arranged to overlap a solids inlet and a solids outlet.
  • the metering device has a connection for a ventilation line and the mixing reactor chamber has a connection for a supply line, is supplied via the air and thus the solids dosage is conveyed into the mixing reactor chamber. It is a quasi-portioned entry of the solid in a space in the metering device, which also air is supplied. In which way, after the solid has been introduced into the metering device, is mixed with the air supplied via the vent line and then further treated on the way to exit from the metering device is not disclosed.
  • the portionwise delimitation of, for example, moist rice grains in blind holes and their subsequent emptying by gravity alone does not seem suitable for metering a dosing material of this kind safely and with the necessary quantity-proportional accuracy into a carrier liquid.
  • DE 602 18 450 T2 relates to the dissolution of powder in water, wherein a water stream is used in conjunction with a jet apparatus to suck the powder and convey it into a stirred tank.
  • the latter is divided by a plurality of transverse to the longitudinal axis of the container baffles arranged in superimposed chambers, which are each connected by a central opening. Through the central openings extends a stirrer shaft, which drives an impeller in each chamber.
  • Powder should also be understood to mean swellable particulate material in water.
  • DE 602 23 586 T2 relates to a product made from cereals, the nature of a cereal being specified in terms of color, shape and outer and inner coating.
  • drinkable mixtures of drinking milk as carrier liquid and rice and / or oats as cereal (s) are desired.
  • the cereals added to the carrier liquid for example rice and / or oats, do not completely dissolve, but rather that their lumpiness, as uniformly distributed and isolated as possible, remains palpable when they are being consumed. This requirement also relates to other small-sized admixtures that can be accommodated in the carrier liquid.
  • solid doses such as at least one cereal, in particular a solid-like, particulate, swellable cereal, and / or at least one other small amount of admixture
  • the inventive idea is, and the inventive solution manifests itself most obvious in the most difficult task, namely the dosage of the pre-cooked rice grains in the carrier liquid, which is exemplified below, starting from a method of the generic type that the at least one solid Dosing, for example cereal rice, in each case in the form of a continuous volume flow of at least one solid dosage material is pronounced, and that the volume flow of air, seen in the flow direction to the volume presented, to the continuous volume flow of at least one solid metered material strikes such that the volume flow of air acts as a mixing, drying, discharge and carrier medium for the respective at least one solid dosage material.
  • the mixture thus prepared is then introduced over the free level in the initial volume.
  • the air velocity given by the volume flow of air is dimensioned in relation to a feed rate of the at least one solid metering material so that the air promotes and intensifies the mixing and moreover functions as a carrier and discharge medium for the respective at least one solid metered product.
  • the at least one solid dosage material is a cereal in the form of a moist, pre-cooked rice
  • the air which is significantly colder than the rice, causes the rice grains to dry in addition to their carrier function and thus counteract adhesion and conglomerate of the rice grains ,
  • solubility characteristics in connection with the cereal rice dosage are analogously also applicable to other cereals or other solid-like, small-particle admixtures, if comparable behavior, such as adhesion and conglomeration, occurs here.
  • cereal also admixtures of the type described above are subsumed.
  • the volume flow of carrier liquid and a volume flow of air are kept constant in a manner known per se and provided continuously and continuously.
  • the volumetric flow mixture is also forcibly discharged from the initially introduced volume at a constant volumetric flow rate and is continuously pronounced over the entire duration of the production time of the mixture and thus of the final result of the production process, a drinkable mixture which can be filled or stored. This ensures a clearly defined discharge of the mixture from the volume presented and at the same time an approximately constant and steady flow, seen in the direction of flow, in the volume presented subordinate areas of further treatment of the mixture reaches as free as possible from stagnant and / or uncontrolled oscillating flow areas.
  • the presented volume of the mixture which has a free level, is regulated above this level and thus kept constant.
  • the at least one solid dosing material, the cereal to be dosed preferably enters the carrier liquid, whereby a trouble-free dosing is conveyed.
  • volume flow carrier liquid and optionally a volume flow of air and the supply of at least one solid dosage material are each quantitatively presettable and can be changed within limits.
  • the presettableness of these sizes makes it possible to set the proportion of the at least one solid metered material to a desired quantitative value.
  • the variability makes it possible under changing operating conditions, e.g. in the event of fluctuations in the volume flows, to adjust the desired and / or required residence time. Safety and reliability of the mixing and dosing process are improved if the at least one solid dosage material is forcibly supplied.
  • the carrier liquid is introduced in a manner known per se into the mixture in such a way that a rotational flow is generated in it by flow mechanics.
  • a rotational flow is generated in it by flow mechanics.
  • the above procedural steps ensure that the respectively metered at least one solid dosage remains a clearly defined mean residence time in the volume presented and mixed there according to this average residence time together with the supplied carrier liquid and the vorge set volume mixture and evenly distributed in this mixture becomes. Since the residence time is defined as the quotient of the volume presented and the volume of air passing through it, the planned volume and the volume flows entering the volume presented are planned kept constant and provided continuously and continuously and continue the forcibly evacuated from the volume presented volume flow mixture is also kept constant and steadily pronounced, the residence time is clearly defined and constant in trouble-free dosing. The dosing conditions are therefore clearly defined, reproducible at any time and constant in scheduled and trouble-free operation.
  • the invention provides that the presented volume of the mixture can be preset within limits.
  • An essential feature of the invention is that the supplied air serves as a mixing, carrier and discharge medium and optionally additionally as a drying medium for the metered and optionally moist at least one solid Dosiergut.
  • the introduced from top to bottom in the direction of volume presented air flow additionally prevents that rising from the carrier liquid vapors (hot steam) reaches the point of merging the volume flow of at least one solid dosing with the flow of air and there in its initial state in the Usually relatively dry dosing material glued.
  • an air speed given by the volume flow of air is larger by a factor of 50 to 100 than a supply speed given by the volume flow of the at least one solid metered metering material.
  • the invention Permitted method that the at least one solid Dosiergut is introduced without admixing air in the submitted volume.
  • the dosing at least one dosing divided into more than one volume flow and is introduced separately from each other in the submitted volume.
  • this process variant increases the reliability and safety of the metering process when metering only a single solid metering material, because the registration surface of the presented volume inevitably increased accordingly.
  • the proposed method is particularly suitable for the preparation of a mixture consisting of a drinking milk as a carrier liquid and at least cereal oats or rice or wheat grains, prepared by the method according to one of claims 1 to 9.
  • the necessary properties of oats and Rice has already been partially defined above, it being advantageous to use the oats as a grain and not pre-cooked and dosed so natively, cold and dry.
  • the rice is used pre-cooked and dosed warm at 70 ° C and preferably under laminar aeration.
  • the wheat grains are dosed only pretreated by washing in cold water. device
  • the device for carrying out the method according to the invention is designed as a metering device and consistently implements the procedural solution features into representational features.
  • the metering device is usually arranged in a UHT (UHT: ultra-high temperature) system and is usually located between a preheating zone and a preheater zone with a subsequent high-temperature zone, a holding zone and a cooling zone, in the latter the end product, a drinkable mixture prepared from the mixture by UHT treatment, cooled to the filling or storage temperature.
  • UHT ultra-high temperature
  • the metering device is formed in a conventional manner with a container for a presented volume of a mixture having a free level.
  • the container has an inlet connection for a carrier liquid below the free level for generating a rotational flow in the container, an inlet opening for at least one solid dosing material and an outlet connection for the mixture consisting of the carrier liquid and the at least one solid dosage.
  • the container has a level control device for the free level and it has a pre-chamber, which opens via an inlet opening in a headspace located above the free level of the container.
  • the prechamber has a connection for supplying the at least one solid dosing material and a connection for air for supplying a volumetric flow of air in each case into the prechamber.
  • the metering device has at least one prechamber with the connection for supplying the at least one solid metered material, which is set up such that the at least one solid metered material enters the prechamber in the form of a steady volume flow of the at least one solid metered material.
  • the above-mentioned connection and the connection for air are arranged such that the volume flow of air, after leaving the connection for air and on the way to the inlet opening of the container, to the continuous volume flow of the at least one fixed Dosing material meets and thereby as Naturalmi- schungs, drying, discharge and carrier medium for the respective at least one solid Dosiergut acts.
  • a mechanical stirring device is provided in the container.
  • the container In order to prevent the container on the one hand crowded and on the other hand is drained too far, so on the one hand, the necessary residence time is too long or too short and on the other hand, the container either overflows or empty, it has a third connection for an upper level limit detection device and a fourth terminal for a lower level limit detecting device.
  • the container pre-chamber, preferably four pre-chambers opening into its head space via an associated inlet opening in each case.
  • the at least one inlet opening or, if appropriate, more than one of these inlet openings is or are arranged in a container lid delimiting the head of the container.
  • Foaming during the feeding of the carrier liquid into the mixture is avoided and the stirring and mixing movement in the mixture is additionally intensified if, as a further proposal, the inlet connection for the supply of the carrier liquid at the circumference and in the tangential direction to Scope of the container is arranged.
  • a trouble-free and clog-free removal of the mixture from the container is facilitated by an embodiment in which the container in its foot region of a conical bottom with a first cone angle and then extending to the outlet port for the discharge of the mixture towards conical taper neck with a second cone angle is limited, wherein the first cone angle is made significantly larger than the second cone angle.
  • a positive displacement pump preferably a rotary positive displacement pump in the form of a screw-spindle pump is arranged.
  • a ventilation device is connected to the headspace of the container.
  • the proposed device is particularly suitable for the preparation of a mixture of drinking milk as a carrier liquid and rice and / or oats or wheat grains cereal / s and / or at least one other solid-like, small-sized admixture such as nuts, fruits, seeds or the like, prepared by means of the device according to any one of claims 10 to 19.
  • a metering device 100 (FIGS. 1 and 2) is, for example, arranged downstream of the last heat exchanger of a preheating zone of a UHT installation, viewed in the flow direction of a carrier liquid TF.
  • the carrier liquid TF flows with a volume flow of carrier liquid Q T F with an inlet velocity CTF via an inlet connection 16 into a container 2 of the dosing device 100, wherein the inlet connection 16 preferably at the periphery and in the tangential direction to the periphery of the container 2 and below a liquid level of a mixture G stored in the container 2, characterized by the carrier liquid TF and at least one solid dosage material Z, B, for example at least one solid-like, particulate, swellable cereal Z, is arranged.
  • the container 2 forms an interior for receiving the mixture G, wherein a submitted volume V of the mixture G is to be limited by the free level N with respect to a head space 5 of the container 2.
  • the container 2 is above its Headspace 5 by a container lid 4 and limited in its foot by a conical bottom 6 with a first cone angle W1 and a subsequent conical taper neck 8 with a second cone angle W2.
  • the first cone angle W1 is made larger than the second cone angle W2, and it is advantageous if the cone angle W1 is slightly less than three times as large as the cone angle W2.
  • the taper neck 8 opens into an outlet port 18 for the mixture G, to which a positive displacement pump 48, preferably in the form of a screw-spindle pump, is arranged directly.
  • the mixture G is discharged from the container 2 with a volume flow mixture Q G and a discharge rate CG.
  • the container 2 further comprises at least one inlet opening 34 for the at least one solid dosage Z, B, in the embodiment, the cereal Z, and / or the at least one other small-sized admixture B (not labeled), wherein the inlet opening 34 the is preferably arranged in the container lid 4.
  • At least one pre-chamber 50 is provided on the container 2, which opens via the at least one inlet opening 34 in the headspace 5 located above the free level N.
  • the pre-chamber 50 has a connection 54 for supplying a volume flow of the at least one solid metered product Q * , the volume flow cereal Qz and / or a volume flow admixture Q B (not designated), and a connection for air 56 for supplying a volume flow air Q L.
  • the prechamber 50 with at least one solid metered Z, B and the connection for air 56 the pre-chamber 50 can be acted upon with air L.
  • connection for air 56 is arranged such that the volume flow of air QL on the way to the inlet opening 34 meets the volume flow of the at least one solid metered product Q * , the volume flow cereal Qz or the volume flow admixture Q B. From the volume flow air Q L results with a passage cross section of the prechamber 50 there for a preferably dry, relatively cold air L an air speed c L , and the cereal Z or admixture B is under the given cross-sectional ratios with a feed rate Cz and CB fed.
  • a level control device 38 is provided, which engages over a preferably arranged in the container lid 4 second port 26 in the free level N and serves to control its. Furthermore, the container 2 engages, preferably in each case again via the container lid 4, via a first connection 24 an agitating device 36, via a third connection 28 an upper level limit detection device 40 and via a fifth connection 32 a container cleaning device 44, wherein the agitator 36 extends far into the presented volume V.
  • a ventilation device 20 via which a generally warm, moist first air L * and possibly other gas or vapor components are removed.
  • a condensate k which optionally separates from the first air L *, is discharged via a connected to the ventilation device 20 overflow pipe 22 in the vicinity of the container 2 as well as a then correspondingly dehumidified second air L ** .
  • a lower level limit detection device 42 engages in the foot region of the container 2 via a fourth connection 30.
  • a first cleaning liquid C1 is discharged into the entire interior of the container 2 when it is completely emptied of the mixture G.
  • a secure and targeted cleaning of the pre-chamber 50 is ensured by a chamber cleaning device 46, which via a connection for chamber cleaning 58 at a chamber lid 52 of the prechamber 50 is inserted into the latter, and over which a second cleaning liquid C2 is applied in the cleaning step.
  • the container 2 preferably rests on a support frame 14 which is preferably supported by three legs on a substrate, it has a manhole 10 for inspection and maintenance work in its interior, and it is equipped with a plurality, preferably three, sight glasses 12, which are preferably distributed in a vertical arrangement over a lateral surface of the container 2.
  • the container 2 has four prechambers 50 opening into its head space 5 via an associated inlet opening 34 in each case. Either different cereals Z and / or admixtures B can be simultaneously introduced into the initially introduced volume V or partial streams of identical or different cereals Z and / or admixtures B either simultaneously via these prechambers 50.
  • the cereal Z may preferably be rice R and here preferably a "world rice" or oats H or wheat grains W (not designated)
  • the oat H is preferably in the form of grain, not pre-cooked and native , dosed cold and dry, while the rice R is pre-cooked and dosed at 70 ° C.
  • the wheat grains W only pretreated by dehydration in cold water, dosed in the mixture G and thus at the end a heat treatment reaches a drinkable product with a proportion Zerealie (n) Z, based on the carrier fluid TF, of 4% and more.
  • the dry and generally relatively cold air L in relation to the cereal Z functions on the one hand as a mixing, carrier and delivery medium for the cereal Z and on the other hand causes drying, in particular with warm, moist preformed rice R, drying as the drying medium Gluing and conglomerating rice grains prevented.
  • the cereals Z are blown to the free level N, penetrate over the entire surface of the free level N in the submitted volume V of the mixture G and are uniformly distributed there with continuous supply of an associated volume flow carrier liquid QTF.
  • the proposed metering device 100 is particularly suitable for the preparation of a mixture G of drinking milk M as carrier liquid TF and rice R and / or oat H as cereal / Z, produced by means of the device according to one of claims 10 to 19.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Dispersion Chemistry (AREA)
  • Cereal-Derived Products (AREA)
  • Accessories For Mixers (AREA)
  • Food-Manufacturing Devices (AREA)

Abstract

L'invention concerne un procédé de mélange et de dosage de matières à doser solides (Z, B), par exemple au moins une céréale (Z), notamment une céréale (Z) particulaire de type solide capable de gonfler, et/ou au moins un autre ingrédient (B) en petits morceaux, dans un liquide porteur (TF), afin de former un mélange (G) composé du liquide porteur (TF) et de la ou des matières à doser solides (Z, B). L'invention concerne également un dispositif destiné à la mise en œuvre du procédé. Le procédé selon l'invention est caractérisé en ce que ladite matière à doser solide (Z, B) est à chaque fois exprimée sous la forme d'un flux volumique constant de ladite matière à doser solide (Q*), et en ce que le flux volumique d'air (QL), vu dans le sens de l'écoulement vers le volume (V) chargé, rencontre le flux volumique constant de ladite matière à doser solide (Q*) de telle sorte que le flux volumique d'air (QL) fait office de fluide de mélange, de séchage, de décharge et de transport pour la ou les matières à doser solides (Z, B) correspondantes.
EP15705190.5A 2014-02-05 2015-01-29 Procédé et dispositif de mélange et de dosage de matières à doser solides dans un liquide porteur Active EP3102318B1 (fr)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE102014001574.2A DE102014001574B4 (de) 2014-02-05 2014-02-05 Verfahren und Vorrichtung zur kontinuierlichen Dosierung von wenigstens einer festkörperartigen, kleinstückigen Beimengung in eine Trägerflüssigkeit
PCT/EP2015/000175 WO2015117739A1 (fr) 2014-02-05 2015-01-29 Procédé et dispositif de mélange et de dosage de matières à doser solides dans un liquide porteur

Publications (2)

Publication Number Publication Date
EP3102318A1 true EP3102318A1 (fr) 2016-12-14
EP3102318B1 EP3102318B1 (fr) 2019-01-16

Family

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Family Applications (1)

Application Number Title Priority Date Filing Date
EP15705190.5A Active EP3102318B1 (fr) 2014-02-05 2015-01-29 Procédé et dispositif de mélange et de dosage de matières à doser solides dans un liquide porteur

Country Status (5)

Country Link
EP (1) EP3102318B1 (fr)
CN (1) CN106457172B (fr)
DE (1) DE102014001574B4 (fr)
PH (2) PH12016501565A1 (fr)
WO (1) WO2015117739A1 (fr)

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CN106362621A (zh) * 2016-11-01 2017-02-01 四川鑫康源生物科技有限公司 用于保健品搅拌杀菌的多功能装置
CN113600056B (zh) * 2021-09-06 2023-10-10 李耀辉 一种可连续供料的畜牧饲料搅拌装置

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CN100441100C (zh) * 2007-02-13 2008-12-10 内蒙古蒙牛乳业（集团）股份有限公司 一种含有坚果颗粒的谷物调味奶及其生产方法

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EP3102318B1 (fr) 2019-01-16
DE102014001574B4 (de) 2017-07-27
CN106457172A (zh) 2017-02-22
CN106457172B (zh) 2019-11-05
PH12016501565A1 (en) 2016-09-14
DE102014001574A1 (de) 2015-08-06
PH12020500251A1 (en) 2021-05-31
WO2015117739A1 (fr) 2015-08-13

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