EP0796651A1 - Mixing device - Google Patents

Mixing device Download PDF

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Publication number
EP0796651A1
EP0796651A1 EP97200806A EP97200806A EP0796651A1 EP 0796651 A1 EP0796651 A1 EP 0796651A1 EP 97200806 A EP97200806 A EP 97200806A EP 97200806 A EP97200806 A EP 97200806A EP 0796651 A1 EP0796651 A1 EP 0796651A1
Authority
EP
European Patent Office
Prior art keywords
housing
additive
mixing
pushing action
liquid
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
EP97200806A
Other languages
German (de)
French (fr)
Other versions
EP0796651B1 (en
Inventor
Coen Hendrik Decnop
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.)
Typhoon Group BV
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to US08/920,150 priority Critical patent/US5964527A/en
Publication of EP0796651A1 publication Critical patent/EP0796651A1/en
Application granted granted Critical
Publication of EP0796651B1 publication Critical patent/EP0796651B1/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F27/00Mixers with rotary stirring devices in fixed receptacles; Kneaders
    • B01F27/50Pipe mixers, i.e. mixers wherein the materials to be mixed flow continuously through pipes, e.g. column mixers
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F27/00Mixers with rotary stirring devices in fixed receptacles; Kneaders
    • B01F27/80Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis
    • B01F27/90Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis with paddles or arms 
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F27/00Mixers with rotary stirring devices in fixed receptacles; Kneaders
    • B01F27/80Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis
    • B01F27/91Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis with propellers
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F35/00Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
    • B01F35/50Mixing receptacles

Definitions

  • the device according to the invention is distinguished in that the mixing gear is formed by at least one rotatingly driven blade assembly, the rotation shaft of which is received centrally in the cross sectionally non-round housing, wherein the mixing gear exerts a pushing action on the liquid in the direction toward the inlet opening.
  • the port for the additive is preferably arranged in the side wall of the housing, i.e. it is directly entrained in the main flow which is subsequently fed back into the counterflow in the central part. It is herein also possible to introduce the additive via a guide tube directed from the port toward the central shaft so that this additive directly enters the counterflow.
  • the blade assembly is constructed from two groups of blades which are fixed at a mutual distance to the rotation shaft thereof, it is recommended to have the guide tube debouch on the side of at least the leading blade assembly remote from the feed opening for the carrier liquid.
  • leading blade assembly consists of a part which has an axial pushing action and a part which has a radial pushing action. Intensive mixing is hereby improved still further.
  • Designated in fig. 1 with the numeral 1 is the housing of the device which has a non-round cross section and is embodied here with a rectangular section.
  • connection flange 7 Fixed on the opposite side of the housing by means of bolts 3 via a connecting flange 2' is a connection flange 7 which serves via the bearing 8 as mounting for a rotation shaft 9 extending co-axially in housing 1.
  • Flange 7 bears a plurality of (here four) spacers 10 for fixing a flange 11 of a drive, for instance electric motor 13. This latter is coupled directly to rotation shaft 9 of the mixing gear.
  • the mixing gear consists of a blade assembly formed here by two blade rotors 14, 15 placed at a mutual distance on rotation shaft 9. The blades are adjusted such that when caused to rotate in the direction of arrow P1 a pushing action as according to arrow P2 results, i.e. in the direction of inlet opening 6.
  • the operation of the above described device is as follows.
  • the carrier liquid is fed into housing 1 under pressure through inlet opening 6 via the pipe 5.
  • the additive is simultaneously introduced via the pipes 16 and a first mixing will take place.
  • the main flow will separate into four part-flows which are situated substantially in the corners of the housing.
  • a part of the liquid is fed back in the direction of arrow P2 by the axial pushing action of mixing gear 14, 15.
  • Flows P2 and P3 will be mixed once again wherein a strong turbulent flow is formed.
  • the intensively mixed carrier flow and additives leave the housing via pipes 18.
  • Fig. 2 shows an alternative embodiment wherein the same elements are however designated with the same reference numerals.
  • a pipe 24 for an additive is fed through into the housing 1, the outer end of which debouches in the dish-shaped rotor 21. This ensures that the additive first acquires a radial flow path and is subsequently entrained in the axial flow paths.

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Mixers Of The Rotary Stirring Type (AREA)

Abstract

A device for mixing a carrier liquid with one or more additives comprising a closed housing with an inlet and an outlet opening for the liquid and an infeed port for the or each additive in addition to a mixing gear accommodated therein, wherein the mixing gear is formed by at least one rotatingly driven blade assembly, the rotation shaft of which is received centrally in the cross sectionally non-round housing, wherein the mixing gear exerts a pushing action on the liquid in the direction toward the inlet opening, whereby due to a vigorous shearing action between the generated liquid flows the or each additive is intensively mixed.

Description

  • The invention relates to a device for mixing a carrier liquid with one or more additives comprising a closed housing with an inlet and an outlet opening for the liquid and an infeed port for the or each additive in addition to a mixing gear accommodated therein.
  • Such a mixer is applied in many processes wherein use is made of for instance static mixers, i.e. a carrier liquid is transported along a static body together with a pre-admitted additive such that a mixing takes place as a result of the differing flows between additive and carrier liquid. For particular substances as additive this does not work well and use is therefore also often made of active mixers in the form of a fixed quantity of carrier liquid which is mixed with the additive in a vessel by means of stirring apparatus. The drawback here is that a fixed quantity of liquid is mixed at a time, this being disadvantageous for continuous processes.
  • The invention has for its object to provide a device with which a continuous mixing process is realized with a considerably higher efficiency so that a perfect mixing is brought about, also for substances which are difficult to mix.
  • The device according to the invention is distinguished in that the mixing gear is formed by at least one rotatingly driven blade assembly, the rotation shaft of which is received centrally in the cross sectionally non-round housing, wherein the mixing gear exerts a pushing action on the liquid in the direction toward the inlet opening.
  • Due to the counterflow effect of the stirring apparatus on the carrier liquid there occurs in the mixing housing on the one hand a flow in the main flow direction and on the other a part-flow in opposing direction whereby the additive is mixed vigorously with the carrier liquid. Because of the non-round form of the housing the main flow will be situated along the outside of the housing while the counterflow takes place centrally in the housing. The good mixing of the substances results from the vigorous shearing action between both flows.
  • The port for the additive is preferably arranged in the side wall of the housing, i.e. it is directly entrained in the main flow which is subsequently fed back into the counterflow in the central part. It is herein also possible to introduce the additive via a guide tube directed from the port toward the central shaft so that this additive directly enters the counterflow.
  • If the blade assembly is constructed from two groups of blades which are fixed at a mutual distance to the rotation shaft thereof, it is recommended to have the guide tube debouch on the side of at least the leading blade assembly remote from the feed opening for the carrier liquid.
  • In a further development the leading blade assembly consists of a part which has an axial pushing action and a part which has a radial pushing action. Intensive mixing is hereby improved still further.
  • Above mentioned and other features of the invention will be further elucidated hereinbelow in the figure description of two embodiments. In the drawing:
    • fig. 1 shows a perspective view of a first embodiment of the device according to the invention with partly broken away parts of the mixing housing;
    • fig. 2 shows a view corresponding with fig. 1 of a second embodiment of the device according to the invention;
    • fig. 3 shows a perspective view of a part of the blade assembly of fig. 2.
  • Designated in fig. 1 with the numeral 1 is the housing of the device which has a non-round cross section and is embodied here with a rectangular section.
  • On the right-hand side the rectangular wall connects onto an end flange 2 which can be connected by means of bolts 3 to a connecting flange 4 of a pipe system 5, this such that this latter connects onto the inlet opening 6.
  • Fixed on the opposite side of the housing by means of bolts 3 via a connecting flange 2' is a connection flange 7 which serves via the bearing 8 as mounting for a rotation shaft 9 extending co-axially in housing 1. Flange 7 bears a plurality of (here four) spacers 10 for fixing a flange 11 of a drive, for instance electric motor 13. This latter is coupled directly to rotation shaft 9 of the mixing gear. The mixing gear consists of a blade assembly formed here by two blade rotors 14, 15 placed at a mutual distance on rotation shaft 9. The blades are adjusted such that when caused to rotate in the direction of arrow P1 a pushing action as according to arrow P2 results, i.e. in the direction of inlet opening 6.
  • The additives are added to the housing via pipes 16, this being done into the flow P3 of the carrier liquid from inlet opening 6. After the mixing the mix leaves the housing via outlet opening 17 and discharge pipe 18.
  • The operation of the above described device is as follows. The carrier liquid is fed into housing 1 under pressure through inlet opening 6 via the pipe 5. The additive is simultaneously introduced via the pipes 16 and a first mixing will take place. The main flow will separate into four part-flows which are situated substantially in the corners of the housing. A part of the liquid is fed back in the direction of arrow P2 by the axial pushing action of mixing gear 14, 15. Flows P2 and P3 will be mixed once again wherein a strong turbulent flow is formed. The intensively mixed carrier flow and additives leave the housing via pipes 18.
  • Fig. 2 shows an alternative embodiment wherein the same elements are however designated with the same reference numerals.
  • The difference from the embodiment according to fig. 1 is the different embodiment of the mixing gear, consisting here of two rotors 20 and 21 which are placed at a mutual distance and likewise rotated by a rotation shaft 9 in the direction of arrow P1. The left-hand rotor 20 consists of a closed disc on which are placed blades which cause a radial pushing action in the direction of arrow P5.
  • The right-hand rotor 21 consists of a dish-shaped disc, the outer flange of which is provided with blades 22 (see fig. 3) which cause an axial pushing action in the direction of arrow P2. The outer edge of the dish is provided with a plurality of passage openings 23 placed such that a radial pushing action as according to arrow P6 is created there. Extra turbulent flows are herewith obtained along the corner parts of housing 1 and a stronger shearing action is brought about between these flow parts whereby a highly intensive mixing is obtained.
  • Another difference from the embodiment according to fig. 1 is that a pipe 24 for an additive is fed through into the housing 1, the outer end of which debouches in the dish-shaped rotor 21. This ensures that the additive first acquires a radial flow path and is subsequently entrained in the axial flow paths.
  • The invention is not limited to the above described embodiments. The housing does not for instance have to have a square cross-sectional form but may have more than four corners such as a hexagon or octagon. The housing may also have an oval form, this such that within the inventive concept one or more flow spaces are created between the imaginary peripheral cylinder of the rotors of the mixing gear and the inner side of the housing.
  • The position of the feed pipes 16 in the housing can also be random, wherein an additive may also be already added in the feed pipe 5 for the carrier liquid.

Claims (8)

  1. Device for mixing a carrier liquid with one or more additives comprising a closed housing with an inlet and an outlet opening for the liquid and an infeed port for the or each additive in addition to a mixing gear accommodated therein, characterized in that the mixing gear is formed by at least one rotatingly driven blade assembly, the rotation shaft of which is received centrally in the cross sectionally non-round housing, wherein the mixing gear exerts a pushing action on the liquid in the direction toward the inlet opening.
  2. Device as claimed in claim 1, characterized in that the port for the additive is arranged in the side wall of the housing.
  3. Device as claimed in claim 2, characterized in that a guide tube directed toward the rotation shaft of the blade assembly connects onto the port for the additive.
  4. Device as claimed in claim 3, characterized in that the guide tube debouches on the side of at least the leading blade assembly remote from the feed opening for the carrier liquid.
  5. Device as claimed in claim 1, characterized in that the leading blade assembly is embodied with a part which has an axial pushing action and a part which has a radial pushing action.
  6. Device as claimed in claim 5, characterized in that the part with the axial pushing action lies concentrically round the part with the radial pushing action.
  7. Device as claimed in any of the foregoing claims, characterized in that the port for the additive is arranged in a wall part of the housing lying closest to the mixing gear.
  8. Device as claimed in any of the foregoing claims, characterized in that the cross section of the housing has a polygonal, preferably square form.
EP97200806A 1996-03-19 1997-03-19 Mixing device Expired - Lifetime EP0796651B1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
US08/920,150 US5964527A (en) 1997-03-19 1997-08-26 Mixing device

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
NL1002649 1996-03-19
NL1002649A NL1002649C2 (en) 1996-03-19 1996-03-19 Mixing device.

Publications (2)

Publication Number Publication Date
EP0796651A1 true EP0796651A1 (en) 1997-09-24
EP0796651B1 EP0796651B1 (en) 2004-08-04

Family

ID=19762522

Family Applications (1)

Application Number Title Priority Date Filing Date
EP97200806A Expired - Lifetime EP0796651B1 (en) 1996-03-19 1997-03-19 Mixing device

Country Status (3)

Country Link
EP (1) EP0796651B1 (en)
DE (1) DE69730068T2 (en)
NL (1) NL1002649C2 (en)

Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DD93948A (en) *
US2448042A (en) * 1943-09-14 1948-08-31 Girdler Corp Mixing apparatus
US2971748A (en) * 1957-07-03 1961-02-14 Bayer Ag Continuous mixer
US3179380A (en) * 1959-11-02 1965-04-20 Dow Chemical Co Apparatus for coagulation of colloidal dispersions
GB998329A (en) * 1962-08-03 1965-07-14 Neumo Ltd A mixer
EP0011559A1 (en) * 1978-11-15 1980-05-28 Societe Metallurgique Le Nickel - S.L.N. Process and apparatus for wet attrition
SU971453A1 (en) * 1981-02-20 1982-11-07 Дагестанский Научно-Исследовательский Ветеринарный Институт Apparatus for mixing liquids
EP0328154A1 (en) * 1988-02-12 1989-08-16 Kanegafuchi Kagaku Kogyo Kabushiki Kaisha Stirring-type mixer

Patent Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DD93948A (en) *
US2448042A (en) * 1943-09-14 1948-08-31 Girdler Corp Mixing apparatus
US2971748A (en) * 1957-07-03 1961-02-14 Bayer Ag Continuous mixer
US3179380A (en) * 1959-11-02 1965-04-20 Dow Chemical Co Apparatus for coagulation of colloidal dispersions
GB998329A (en) * 1962-08-03 1965-07-14 Neumo Ltd A mixer
EP0011559A1 (en) * 1978-11-15 1980-05-28 Societe Metallurgique Le Nickel - S.L.N. Process and apparatus for wet attrition
SU971453A1 (en) * 1981-02-20 1982-11-07 Дагестанский Научно-Исследовательский Ветеринарный Институт Apparatus for mixing liquids
EP0328154A1 (en) * 1988-02-12 1989-08-16 Kanegafuchi Kagaku Kogyo Kabushiki Kaisha Stirring-type mixer

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
DATABASE WPI Section Ch Week 8405, Derwent World Patents Index; Class B07, AN 84-027798, XP002018761 *

Also Published As

Publication number Publication date
NL1002649C2 (en) 1997-09-22
DE69730068T2 (en) 2005-03-24
DE69730068D1 (en) 2004-09-09
EP0796651B1 (en) 2004-08-04

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