EP3983191A1 - Device for producing a multi-component mixture and method for operating said type of device - Google Patents
Device for producing a multi-component mixture and method for operating said type of deviceInfo
- Publication number
- EP3983191A1 EP3983191A1 EP20732183.7A EP20732183A EP3983191A1 EP 3983191 A1 EP3983191 A1 EP 3983191A1 EP 20732183 A EP20732183 A EP 20732183A EP 3983191 A1 EP3983191 A1 EP 3983191A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- stirrer
- temperature control
- shaft
- channel system
- mixing chamber
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B7/00—Mixing; Kneading
- B29B7/30—Mixing; Kneading continuous, with mechanical mixing or kneading devices
- B29B7/34—Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices
- B29B7/38—Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices rotary
- B29B7/40—Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices rotary with single shaft
- B29B7/401—Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices rotary with single shaft having a casing closely surrounding the rotor, e.g. with a plunger for feeding the material
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders
- B01F27/05—Stirrers
- B01F27/09—Stirrers characterised by the mounting of the stirrers with respect to the receptacle
- B01F27/092—Stirrers characterised by the mounting of the stirrers with respect to the receptacle occupying substantially the whole interior space of the receptacle
-
- 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
- B01F35/90—Heating or cooling systems
- B01F35/95—Heating or cooling systems using heated or cooled stirrers
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B7/00—Mixing; Kneading
- B29B7/30—Mixing; Kneading continuous, with mechanical mixing or kneading devices
- B29B7/34—Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices
- B29B7/38—Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices rotary
- B29B7/40—Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices rotary with single shaft
- B29B7/405—Mixing heads
- B29B7/407—Mixing heads with a casing closely surrounding the rotor, e.g. with conical rotor
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B7/00—Mixing; Kneading
- B29B7/80—Component parts, details or accessories; Auxiliary operations
- B29B7/802—Constructions or methods for cleaning the mixing or kneading device
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B7/00—Mixing; Kneading
- B29B7/80—Component parts, details or accessories; Auxiliary operations
- B29B7/82—Heating or cooling
- B29B7/826—Apparatus therefor
-
- 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
- B01F35/90—Heating or cooling systems
- B01F2035/98—Cooling
-
- 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
- B01F35/90—Heating or cooling systems
- B01F2035/99—Heating
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F2101/00—Mixing characterised by the nature of the mixed materials or by the application field
- B01F2101/2805—Mixing plastics, polymer material ingredients, monomers or oligomers
Definitions
- the invention relates to a device for producing a multicomponent mixture with a mixing chamber and a mixing device, the mixing device having a stirrer arranged in the mixing chamber and rotatably driven about an axis of rotation. It also relates to a method for operating such a device.
- Multi-component mixture is known in which the mixing chamber can be rinsed by means of water channels let into the chamber wall and can also be tempered.
- Mixing devices of this type serve to mix several components of a plastic mixture with one another immediately before use and to make them available for processing.
- the mixing chamber can have an outlet through which a strand of the finished mixture can be dispensed and applied to a surface, for example by means of a robot arm.
- the object of the invention is to provide an apparatus for producing a
- Multi-component mixture specified with a mixing chamber and a mixing device having a stirrer arranged in the mixing chamber, rotatably driven about an axis of rotation, a temperature control channel system through which a temperature control medium can flow for controlling the temperature of the stirrer is arranged inside the stirrer.
- the temperature control channel system is conceivable to design the temperature control channel system as a heating channel system through which a heating medium can flow as a temperature control medium and is provided for heating the stirrer. In this way, for example, reactions of the components can be influenced and, in particular, accelerated.
- the The temperature control channel system is conceivable as a cooling channel system through which a cooling medium can flow as the temperature control medium and is provided for cooling the stirrer.
- Such a device has the advantage that a reaction of the components with one another can be slowed down at least on the surface of the stirrer when the stirrer is at a relatively low temperature.
- the reaction in the mixing chamber essentially takes place according to the van-'t-Hoff rule. It has been found that reducing the temperature by 10 ° C increases the pot life locally by a factor of 2 to 3. Dirt on the stirrer can thus be reduced.
- the stirrer is arranged on a shaft which is connected to the stirrer in the area of its first end and is rotatably driven in the area of its second end.
- the stirrer is designed to be axially movable within the mixing chamber so that it can be lowered and raised in the direction of the axis of rotation in order to close or open an outlet arranged at the bottom of the mixing chamber. In this way, a fully prepared multi-component mixture can be dispensed for further use after the mixing process.
- the speed of the stirrer can particularly preferably be set to a value between 1 rpm and 6000 rpm. Very particularly preferably to a value between 800 rpm and 3000 rpm.
- the pressure in the mixing chamber is preferably in a range between 0.5 bar and 4.0 bar, preferably in a range between 1.5 bar and 3.0 bar.
- applications can also come into consideration in which the pressure in the mixing chamber is up to 50 bar, so that the mixing chamber is preferably designed and configured to withstand an internal pressure which has a value in a range between 0.5 bar and 50 bar.
- the temperature control channel system is arranged in cavities of the stirrer and walls of the cavities form walls of the temperature control channel system.
- This arrangement in which, in particular, an axially extending cavity can be provided as the temperature control channel, has the advantage that the temperature control is particularly efficient, since the temperature control medium is in direct contact with the stirrer.
- the shaft has a temperature control channel system that is connected to the The temperature control channel system of the stirrer is in fluid connection, an inlet and an outlet for the temperature control medium being provided in the region of the second end of the shaft.
- the inlet and the outlet are accordingly provided outside the mixing chamber in the region of the second end of the shaft, for example the inlet and the outlet are arranged in chambers filled with the temperature control medium, in which a
- the flow can be directed in that a tube is arranged within the at least one temperature control channel and is connected to the outlet.
- a second end of the tube can be arranged in the temperature control channel system of the stirrer and in particular in a distal area of the temperature control channel system, so that the temperature control medium in the temperature control channel system is outside the Pipe flows back and forth within the pipe.
- the temperature control channel system is formed in a temperature control lance which is arranged in a cavity of the stirrer.
- This embodiment has the advantage that the frequently, for example with everyone
- the temperature control medium must be sealed. Rather, the temperature control medium only circulates within the temperature control lance.
- the temperature control lance can be guided in a cavity of the shaft up to its second end and an inlet and an outlet for the temperature control medium can be provided in the area of the second end of the shaft.
- the temperature control medium circulates only within the
- Tempering lance that is plugged or screwed into the stirrer.
- a gap between an outer wall of the temperature control lance and the walls of the cavity of the stirrer can be kept particularly small in order to achieve the best possible heat transfer and thus the best possible temperature control.
- the temperature control channel system is formed by means of a heat pipe which is arranged in a cavity of the stirrer.
- Embodiment also has the advantage that a seal between the stirrer and the shaft does not have to be liquid-tight.
- the heat pipe can be guided in particular in a cavity of the shaft up to its second end, with active temperature control of the heat pipe being provided in the area of the second end of the shaft, for example air or water temperature control.
- stirrer arranged, rotatably driven about an axis of rotation stirrer, wherein the stirrer is tempered.
- the stirrer is tempered for cooling in particular by removing heat from the interior of the stirrer by means of a cooling medium or, alternatively, for a
- Heating in particular by supplying heat from inside the stirrer by means of a heating medium.
- the speed of the stirrer is preferably adjustable and can be set to a value between 1 rev / min and 6000 rev / min.
- the speed is very particularly preferably set to a value between 800 rpm and 3000 rpm
- the mixing chamber is preferably subjected to a pressure in the range between 0.5 bar and 4.0 bar, preferably in a range between 1.5 bar and 3.0 bar.
- a pressure in the mixing chamber is up to 50 bar, so that the mixing chamber is preferably designed and configured to withstand an internal pressure which has a value in a range between 0.5 bar and 50 bar.
- the method has the advantages described in connection with the device.
- FIG. 1 shows an apparatus for producing a multicomponent mixture according to a first embodiment of the invention
- FIG. 2 shows an apparatus for producing a multicomponent mixture according to a second embodiment of the invention
- FIG. 3 shows an apparatus for producing a multicomponent mixture according to a third embodiment of the invention.
- the device 1 for producing a multicomponent mixture according to FIG. 1 has a mixing chamber 2 and a mixing device 3.
- the mixing device 3 comprises one in Mixing chamber 2 arranged stirrer 4, which is rotatably driven about a longitudinal axis L by a shaft 12.
- the stirrer 4 has the task of various components of a
- the multi-component mixture is in particular a plastic.
- the ready-made multi-component mixture can through an outlet 15 from the
- Mixing chamber can be removed, the outlet 15 being closed and released by the stirrer 4, which is movable in the axial direction.
- the stirrer 4 has a first end 10, by means of which the outlet 15 can be closed. It also has a second end 11, which is connected to a first end 13 of the shaft 12. A second end 14 of the shaft 12 has a drive (not shown).
- the stirrer 4 In order to keep the stirrer 4 soiled by crosslinking the material in the mixing chamber 2, the stirrer 4 is cooled from the inside.
- the walls of the mixing chamber 2 can also be equipped with cooling channels that enable the mixing chamber 2 to be cooled.
- the stirrer 4 has a cavity 23 which is delimited by walls 9 and which extends from the second end 11 of the stirrer 4 almost to its first end 10.
- a cooling channel system 5 is designed as a temperature control channel system, wherein in the embodiment shown in Figure 1, the walls 9 of the cavity also walls of the
- the cooling channel system 5 is thus formed by the walls 9 of the cavity 23 and additionally by a tube 8 which is arranged coaxially in the cavity 23.
- a heating channel system as a temperature control channel system which heats the stirrer from the inside. This can have comparable features with regard to the cooling channel system 5 shown, a flow of a heating medium being expedient here.
- both a flow 6 is formed in the cavity 23, which is connected to an inlet 16 in the region of the second end 14 of the shaft 12, and a return 7, which is connected to an outlet 17 in the region of the second end 14 of the Shaft 12 is in communication.
- the cooling channel system 5 formed in this way, as indicated by the arrows 25, is flowed through by a temperature control medium, for example water, which is used as the cooling medium.
- the cooling medium flows through the inlet 16 into a cavity 27 running inside the shaft 12 and flows from there into the cavity 23 of the stirrer 4, which is in fluid connection with the cavity 27.
- the cooling medium flows between the tube 8 and the walls 9 of the cavity 27, 23 to the area of the first end 10 of the stirrer 4, where it flows into the tube 8, from there into the tube 28 within the shaft 12 and from there flows to the outlet 17.
- the cooling medium absorbs heat from the material of the stirrer 4 and thereby cools its surface 29.
- heated cooling medium is transported away.
- FIG. 2 shows a second embodiment of the device 1, which differs from that shown in FIG. 1 in that a cooling lance 18 designed as a cooling lance in the cavity 23, 27
- Termperierlanze is arranged. This extends from the area of the first end 10 of the stirrer 4 to the area of the second end 14 of the shaft 12.
- the cooling lance 18 also has a tube 19 in its interior, with a flow 6 of the cooling channel system 5 outside the tube 19 and a Return 7 is formed within the tube 19.
- the cooling lance 18 has openings of an inlet 20 and an outlet 21.
- the cooling lance 18 can for example be inserted or screwed into the stirrer 4 and / or the shaft 12. When the stirrer 4 is replaced, the cooling lance 18 can remain connected to the shaft 12.
- a gap between the outer walls of the cooling lance 18 and the walls 9 delimiting the cavity 23 is designed to be as small as possible.
- FIG 3 shows a third embodiment of the device 1, which differs from the embodiments shown in Figures 1 and 2 in that the cooling channel system 5 is formed by means of a heat pipe 22, which is arranged in the cavity 23, 27 and extends from the area of the first end 10 of the stirrer 4 extends into the region of the second end 14 of the shaft 12.
- a distal end 26 of the heat pipe 22 can have an active cooling 24.
- the heat pipe 22 is shown only schematically in the embodiment shown. This is a heat transport medium known to those skilled in the art, in which, during operation, a working medium stored in the heat pipe 22 evaporates in the area of the stirrer 4 and flows into a cooling zone located in the area of the distal end 26, where it gives off heat and condenses again.
- the heat pipe 22 forms a closed system which can be integrated particularly easily into the stirrer 4 and the shaft 12.
- the heat pipe 22 like the cooling lance 18 according to FIG. 2, can be screwed or plugged into the stirrer 4 or the shaft 12 and remain connected to the shaft 12 when the stirrer 4 is replaced.
- a gap between the outer walls of the heat pipe 22 and the walls 9 delimiting the cavity 23 is designed to be as small as possible for efficient cooling.
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Accessories For Mixers (AREA)
- Mixers Of The Rotary Stirring Type (AREA)
Abstract
Description
Claims
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE102019208473.7A DE102019208473A1 (en) | 2019-06-11 | 2019-06-11 | Device for producing a multicomponent mixture and method for operating such a device |
PCT/EP2020/065917 WO2020249541A1 (en) | 2019-06-11 | 2020-06-09 | Device for producing a multi-component mixture and method for operating said type of device |
Publications (1)
Publication Number | Publication Date |
---|---|
EP3983191A1 true EP3983191A1 (en) | 2022-04-20 |
Family
ID=71083628
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP20732183.7A Pending EP3983191A1 (en) | 2019-06-11 | 2020-06-09 | Device for producing a multi-component mixture and method for operating said type of device |
Country Status (4)
Country | Link |
---|---|
US (1) | US20220088830A1 (en) |
EP (1) | EP3983191A1 (en) |
DE (1) | DE102019208473A1 (en) |
WO (1) | WO2020249541A1 (en) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
AT519978B1 (en) * | 2017-12-19 | 2018-12-15 | Sonderhoff Eng Gmbh | Device for producing plastic parts |
Family Cites Families (25)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US172068A (en) * | 1876-01-11 | Improvement in apparatus for the manufacture of soap | ||
US1156851A (en) * | 1912-01-24 | 1915-10-12 | Miller Pasteurizing Machine Company | Heating or cooling apparatus. |
US1587840A (en) * | 1923-12-13 | 1926-06-08 | Pfaudler Co Inc | Impeller or agitator |
US1667944A (en) * | 1924-10-31 | 1928-05-01 | Pfaudler Co Inc | Agitator |
US2004009A (en) * | 1934-06-04 | 1935-06-04 | William A Moir | Method of and apparatus for conditioning chocolate or the like |
US2687830A (en) * | 1949-03-25 | 1954-08-31 | Henry H Doering | Feed roller attachment for butter print machinery and the like |
US3241606A (en) * | 1962-08-16 | 1966-03-22 | Shionogi & Co | Agitator |
US3310836A (en) * | 1964-09-25 | 1967-03-28 | George B Nichols | Extruder, etc. |
DE2113960C3 (en) * | 1970-11-24 | 1981-06-19 | Draiswerke Gmbh, 6800 Mannheim | Device for continuous mixing of solids with liquids |
JPS5265360A (en) * | 1975-11-25 | 1977-05-30 | Kishihiro Yamaoka | Continuous kneading machine |
US4142805A (en) * | 1976-02-02 | 1979-03-06 | Usm Corporation | Method for processing polymeric material |
US4183676A (en) * | 1976-12-03 | 1980-01-15 | Draiswerke Gmbh | Method of and apparatus for gluing wood chips |
DE3304129A1 (en) * | 1983-02-08 | 1984-08-09 | Draiswerke Gmbh, 6800 Mannheim | METHOD AND MIXER FOR CONTINUOUSLY GLUING FROM WOOD CHIPS, FIBERS OD. DGL. EXISTING MIXTURE |
JP2782192B2 (en) * | 1988-02-12 | 1998-07-30 | 鐘淵化学工業株式会社 | Stirring type mixing device |
JP2778797B2 (en) * | 1990-04-05 | 1998-07-23 | 株式会社神戸製鋼所 | Screw for plastic molding machine |
JP2723331B2 (en) * | 1990-04-05 | 1998-03-09 | 株式会社神戸製鋼所 | Plastic molding machine |
US5180225A (en) * | 1991-06-07 | 1993-01-19 | Farrel Corporation | Rotor zone cooling apparatus for rotors in continuous mixers of plastic materials |
JP2871959B2 (en) * | 1992-07-21 | 1999-03-17 | 三菱電機株式会社 | Thermosetting resin molding apparatus and molding method thereof |
JPH09300433A (en) * | 1996-05-20 | 1997-11-25 | Kobe Steel Ltd | Screw for extruder |
DE29723102U1 (en) * | 1997-12-13 | 1998-03-26 | Martin-Luther-Universität Halle-Wittenberg, 06108 Halle | Measuring arrangement for detecting the temperature and the axial temperature profile of the conveyed molding compound in screw conveyor and shear devices |
US7067088B2 (en) * | 2002-01-12 | 2006-06-27 | Saudi Basic Industries Corporation | Stratified flow chemical reactor |
EP1779923B1 (en) * | 2004-03-29 | 2007-12-26 | Kansai Paint Co., Ltd. | Mixer with a stirrer having tapered blades |
DE102012002047A1 (en) * | 2011-03-12 | 2012-09-13 | Oerlikon Textile Gmbh & Co. Kg | Dynamic mixer for blending polymer melt during melt spinning process for manufacturing synthetic threads, has sensor device arranged in region of outlet to measure physical parameters of melt and connected with control device |
DE102012103885B4 (en) * | 2012-05-03 | 2015-07-23 | Sonderhoff Engineering Gmbh | Apparatus for producing a multi-component mixture |
DE202017103837U1 (en) * | 2017-06-27 | 2018-10-01 | Hans Heidolph GmbH | Stirring device, in particular overhead stirrer |
-
2019
- 2019-06-11 DE DE102019208473.7A patent/DE102019208473A1/en not_active Withdrawn
-
2020
- 2020-06-09 WO PCT/EP2020/065917 patent/WO2020249541A1/en unknown
- 2020-06-09 EP EP20732183.7A patent/EP3983191A1/en active Pending
-
2021
- 2021-12-06 US US17/543,368 patent/US20220088830A1/en active Pending
Also Published As
Publication number | Publication date |
---|---|
WO2020249541A1 (en) | 2020-12-17 |
DE102019208473A1 (en) | 2020-12-17 |
US20220088830A1 (en) | 2022-03-24 |
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