EP0220788B1 - Liquid flow mixer - Google Patents

Liquid flow mixer Download PDF

Info

Publication number
EP0220788B1
EP0220788B1 EP86202094A EP86202094A EP0220788B1 EP 0220788 B1 EP0220788 B1 EP 0220788B1 EP 86202094 A EP86202094 A EP 86202094A EP 86202094 A EP86202094 A EP 86202094A EP 0220788 B1 EP0220788 B1 EP 0220788B1
Authority
EP
European Patent Office
Prior art keywords
chamber
impeller
drive shaft
shaft
cylindrical
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.)
Expired - Lifetime
Application number
EP86202094A
Other languages
German (de)
French (fr)
Other versions
EP0220788A3 (en
EP0220788A2 (en
Inventor
Garry Hoyland
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.)
Water Research Centre
Original Assignee
Water Research Centre
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 Water Research Centre filed Critical Water Research Centre
Priority to DE8686202094T priority Critical patent/DE3586721D1/en
Priority to AT86202094T priority patent/ATE81031T1/en
Priority to EP86202094A priority patent/EP0220788B1/en
Publication of EP0220788A2 publication Critical patent/EP0220788A2/en
Publication of EP0220788A3 publication Critical patent/EP0220788A3/en
Application granted granted Critical
Publication of EP0220788B1 publication Critical patent/EP0220788B1/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F23/00Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
    • B01F23/40Mixing liquids with liquids; Emulsifying
    • B01F23/43Mixing liquids with liquids; Emulsifying using driven stirrers
    • 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
    • B01F27/60Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a horizontal or inclined axis
    • B01F27/70Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a horizontal or inclined axis with paddles, blades 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
    • B01F27/05Stirrers
    • B01F27/11Stirrers characterised by the configuration of the stirrers
    • B01F27/112Stirrers characterised by the configuration of the stirrers with arms, paddles, vanes or blades
    • B01F27/1125Stirrers characterised by the configuration of the stirrers with arms, paddles, vanes or blades with vanes or blades extending parallel or oblique to the stirrer axis

Definitions

  • This invention relates to a liquid flow mixer.
  • US-A-4341476, FR-A-1488593 and DE-B-1093335 all disclose apparatus comprising a generally cylindrical chamber, having an inlet and an outlet, the chamber having one or more rotatable, plate-like impellers, rotatable about the axis of the chamber and means for driving the impellers in rotation.
  • the impellers extend generally axially of the chamber.
  • FR-A-1488593 describes apparatus for mixing two liquid flows which comprises a cylindrical chamber having at one end an outlet for the mixture, said chamber including at least one plate-like impeller mounted on a drive shaft and rotatable about the axis of chamber and means for driving the impeller(s) in rotation.
  • none of these documents describes an apparatus for mixing two liquid flows whereby the liquids are subjected to immediate and thorough mixing as they pass quickly through the apparatus.
  • apparatus for mixing two or more liquid flows which comprises a cylindrical chamber having at one end an outlet for the mixture, said chamber including at least one plate-like impeller mounted on a drive shaft and rotatable about the axis of chamber and means for driving the impeller(s) in rotation, said impeller(s) extending axially in the chamber (51) and radially outwardly of the drive shaft (54); characterised in that said chamber has one open end forming an outlet coaxial with said cylindrical chamber and has no axial inlet but at least two radial inlets in the cylindrical wall of the chamber, whereby at least two separate incoming liquids can enter the chamber simultaneously to impinge directly on said rotating impeller(s).
  • the liquid flows to be mixed enter the chamber substantially radially, and exit axially.
  • the apparatus is used for dewatering a solids suspension as described in EP-A-172649, the suspension is mixed with flocculant by passing both radially into the cylindrical chamber with the impellers rotating therein, the mixture exiting from the open end of the chamber.
  • the drive shaft is mounted substantially axially in the cylindrical chamber, and the or each impeller preferably extends longitudinally of the chamber and radially outwardly of the shaft to terminate close to the walls of the chamber.
  • the mixer comprises a cylindrical body 50 constituting a mixing chamber 51.
  • the chamber is open at one end 52 (the right-hand end as shown in Figure 1) to provide an axial exit for the mixed liquids.
  • the other end of chamber 51 is closed by a low clearance impeller back-plate 53.
  • Extending through back-plate 53 and axially into chamber 51 is a drive-shaft 54 on which is mounted a circular disc 90 and three plate-like impellers 55,56,57 each extending longitudinally of the chamber at 120° with respect to the other two (see Figure 2).
  • each impeller extends radially outwardly from the shaft 54, almost to the inner wall 58 of body 50.
  • Disc 90 at one end of the impellers (the left-hand end as viewed in Figure 1), protects the seal 63 from any debris that may be present in the suspension.
  • the drive shaft 54 is connected to a drive motor/gear box combination 60, passing through bearing assemblies 61,62 and a mechanical seal 63 on the back-plate 53.
  • a disc 64 is mounted coaxially on shaft 54, to throw leak fluid centrifugally outwardly through drainage holes 65.
  • Bearing assembly 61 includes a support member 70 conveniently mounted between two coaxially arranged cylindrical bodies 71,72 containing the bearing assembly 62, fling plate 64 and seal 63, as shown schematically in Figure 1.
  • first liquid inlet pipe 80 eg. for sewage sludge
  • liquid includes not only liquids per se but mixtures, eg. of liquids and solids.
  • two further liquid supply pipes 81,82 are shown (in practice, only one will normally be used). These could for example be used for flocculant or other dosant.
  • Pipe 81 passes through the wall of pipe 80 and both terminate level with inner wall 58 of body 50.
  • Pipe 82 is downstream of pipe 80 and is disposed radially of body 50, again terminating at inner wall 58 of body 50.
  • the appropriate diameter of inlet 80 is 200 mm and the maximum speed of drive shaft 54 is about 500 rpm.
  • suspension and flocculant (the latter in controlled quantity) are fed into chamber 51 whilst the impellers are rotated to cause mixing of the suspension and flocculant.
  • the mixture passes out of chamber 51 via end 52, for example to the filter plate press. It is preferred to add the flocculant to the suspension either as the latter enters the mixing chamber 51 or immediately thereafter.
  • the motor used in the mixer of Figures 1 and 2 can be an induction motor, a variable speed reluctance motor or a DC motor. Best results are obtained from the flocculant when the motor speed is changed during a pressing cycle in accordance with the flowrate and viscosity of the suspension, i.e. when the motor speed is turned to suit the particular flocculant/suspension mixture being treated.
  • the or each impeller is so designed as to create maximum mixing without the problem of fouling with debris such as fibres that may be present in the suspension.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Mixers Of The Rotary Stirring Type (AREA)
  • Treatment Of Sludge (AREA)
  • Separation Of Suspended Particles By Flocculating Agents (AREA)

Abstract

A mixer for two liquid flows comprises a generally cylindrical chamber (51) having one open end (52) providing an axial flow outlet for the mixed liquids, and one or more radial inlets (80,81,82) for the liquid flows to be mixed. Within the chamber are one or more radially extending impeller plates (55,56,57) rotatable to cause thorough mixing of the liquids as they flow through the chamber. The impeller plates are preferably mounted on an axial drive shaft (54) and sweep substantially the whole volume of the chamber upon rotation of the shaft.

Description

  • This invention relates to a liquid flow mixer.
  • There are many instances in which it is desirable to mix two or more flowing liquid streams. One such instance occurs in sewage sludge dewatering processes which require the sludge to be flocculated by dosing with a flocculant such as polyelectrolyte.
  • US-A-4341476, FR-A-1488593 and DE-B-1093335 all disclose apparatus comprising a generally cylindrical chamber, having an inlet and an outlet, the chamber having one or more rotatable, plate-like impellers, rotatable about the axis of the chamber and means for driving the impellers in rotation. In the French and German specifications the impellers extend generally axially of the chamber. FR-A-1488593 describes apparatus for mixing two liquid flows which comprises a cylindrical chamber having at one end an outlet for the mixture, said chamber including at least one plate-like impeller mounted on a drive shaft and rotatable about the axis of chamber and means for driving the impeller(s) in rotation. However, none of these documents describes an apparatus for mixing two liquid flows whereby the liquids are subjected to immediate and thorough mixing as they pass quickly through the apparatus.
  • We have now devised apparatus for mixing two (or more) liquid flows which apparatus is useful particularly but not exclusively in filter plate pressing of sludges as described in EP-A-172649.
  • According to the present invention there is provided apparatus for mixing two or more liquid flows which comprises a cylindrical chamber having at one end an outlet for the mixture, said chamber including at least one plate-like impeller mounted on a drive shaft and rotatable about the axis of chamber and means for driving the impeller(s) in rotation, said impeller(s) extending axially in the chamber (51) and radially outwardly of the drive shaft (54); characterised in that said chamber has one open end forming an outlet coaxial with said cylindrical chamber and has no axial inlet but at least two radial inlets in the cylindrical wall of the chamber, whereby at least two separate incoming liquids can enter the chamber simultaneously to impinge directly on said rotating impeller(s).
  • In use of the apparatus of the invention, the liquid flows to be mixed enter the chamber substantially radially, and exit axially. When the apparatus is used for dewatering a solids suspension as described in EP-A-172649, the suspension is mixed with flocculant by passing both radially into the cylindrical chamber with the impellers rotating therein, the mixture exiting from the open end of the chamber.
  • Preferably, the drive shaft is mounted substantially axially in the cylindrical chamber, and the or each impeller preferably extends longitudinally of the chamber and radially outwardly of the shaft to terminate close to the walls of the chamber.
  • In order that the invention may be more fully understood, reference is made to the accompanying drawings, wherein:
    • FIGURE 1 is an axial section of one embodiment of in-line mixer of the present invention; and
    • FIGURE 2 is an end elevation of the mixer of Figure 1.
  • Referring to the drawings, the mixer comprises a cylindrical body 50 constituting a mixing chamber 51. The chamber is open at one end 52 (the right-hand end as shown in Figure 1) to provide an axial exit for the mixed liquids. The other end of chamber 51 is closed by a low clearance impeller back-plate 53. Extending through back-plate 53 and axially into chamber 51 is a drive-shaft 54 on which is mounted a circular disc 90 and three plate- like impellers 55,56,57 each extending longitudinally of the chamber at 120° with respect to the other two (see Figure 2). As can be seen, each impeller extends radially outwardly from the shaft 54, almost to the inner wall 58 of body 50. Disc 90, at one end of the impellers (the left-hand end as viewed in Figure 1), protects the seal 63 from any debris that may be present in the suspension.
  • The drive shaft 54 is connected to a drive motor/gear box combination 60, passing through bearing assemblies 61,62 and a mechanical seal 63 on the back-plate 53. To cope with any small fluid leakage through seal 63, a disc 64 is mounted coaxially on shaft 54, to throw leak fluid centrifugally outwardly through drainage holes 65. Bearing assembly 61 includes a support member 70 conveniently mounted between two coaxially arranged cylindrical bodies 71,72 containing the bearing assembly 62, fling plate 64 and seal 63, as shown schematically in Figure 1.
  • Communicating radially with chamber 51 is a first liquid inlet pipe 80 (eg. for sewage sludge). It is to be understood that the term liquid includes not only liquids per se but mixtures, eg. of liquids and solids. Also two further liquid supply pipes 81,82 are shown (in practice, only one will normally be used). These could for example be used for flocculant or other dosant. Pipe 81 passes through the wall of pipe 80 and both terminate level with inner wall 58 of body 50. Pipe 82 is downstream of pipe 80 and is disposed radially of body 50, again terminating at inner wall 58 of body 50.
  • In one preferred arrangement, the appropriate diameter of inlet 80 is 200 mm and the maximum speed of drive shaft 54 is about 500 rpm.
  • In operation of the mixer for dosing flocculant into aqueous suspensions, suspension and flocculant (the latter in controlled quantity) are fed into chamber 51 whilst the impellers are rotated to cause mixing of the suspension and flocculant. The mixture passes out of chamber 51 via end 52, for example to the filter plate press. It is preferred to add the flocculant to the suspension either as the latter enters the mixing chamber 51 or immediately thereafter.
  • The motor used in the mixer of Figures 1 and 2 can be an induction motor, a variable speed reluctance motor or a DC motor. Best results are obtained from the flocculant when the motor speed is changed during a pressing cycle in accordance with the flowrate and viscosity of the suspension, i.e. when the motor speed is turned to suit the particular flocculant/suspension mixture being treated. The or each impeller is so designed as to create maximum mixing without the problem of fouling with debris such as fibres that may be present in the suspension.

Claims (7)

  1. Apparatus for mixing two or more liquid flows which comprises a cylindrical chamber (51) having at one end (52) an outlet for the mixture, said chamber (51) including at least one plate-like impeller (55,56,57) mounted on a drive shaft (54) and rotatable about the axis of chamber (51) and means (60) for driving the impeller(s) (55,56,57) in rotation, said impeller(s) (55,56,57) extending axially in the chamber (51) and radially outwardly of the drive shaft (54); characterised in that said chamber (51) has one open end (52) forming an outlet coaxial with said cylindrical chamber and has no axial inlet but at least two radial inlets (80,81,82) in the cylindrical wall of the chamber (51), whereby at least two separate incoming liquids can enter the chamber (51) simultaneously to impinge directly on said rotating impeller(s) (55,56,57).
  2. Apparatus according to claim 1, wherein the or each impeller (55,56,57) extends radially outwardly of the shaft (54) to terminate close to the cylindrical wall (58) of the chamber (51).
  3. Apparatus according to claim 2, wherein upon rotation of the shaft (54), the or each impeller (55,56,57) sweeps substantially the whole of the volume of the chamber (51).
  4. Apparatus according to claim 2 or 3, wherein, at the other end of the chamber from the outlet (52), the chamber (51) is substantially closed by a low clearance impeller back plate (53) through which the drive shaft (54) enters the chamber.
  5. Apparatus according to claim 4, wherein said back plate (53) includes a seal (63) around the drive shaft.
  6. Apparatus according to claim 4 or 5, wherein a circular disc (90) is mounted radially on the drive shaft (54) in the cylinder (51) adjacent the back plate (53).
  7. Apparatus according to any preceding claim, wherein one radial inlet (81) lies within another (80).
EP86202094A 1985-07-15 1985-07-15 Liquid flow mixer Expired - Lifetime EP0220788B1 (en)

Priority Applications (3)

Application Number Priority Date Filing Date Title
DE8686202094T DE3586721D1 (en) 1985-07-15 1985-07-15 LIQUID FLOW MIXER.
AT86202094T ATE81031T1 (en) 1985-07-15 1985-07-15 LIQUID FLOW MIXER.
EP86202094A EP0220788B1 (en) 1985-07-15 1985-07-15 Liquid flow mixer

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
EP86202094A EP0220788B1 (en) 1985-07-15 1985-07-15 Liquid flow mixer

Related Parent Applications (2)

Application Number Title Priority Date Filing Date
EP85305044A Division EP0172649A3 (en) 1984-07-26 1985-07-15 Dewatering solids suspensions
EP85305044.1 Division 1985-07-15

Publications (3)

Publication Number Publication Date
EP0220788A2 EP0220788A2 (en) 1987-05-06
EP0220788A3 EP0220788A3 (en) 1989-04-26
EP0220788B1 true EP0220788B1 (en) 1992-09-30

Family

ID=8195826

Family Applications (1)

Application Number Title Priority Date Filing Date
EP86202094A Expired - Lifetime EP0220788B1 (en) 1985-07-15 1985-07-15 Liquid flow mixer

Country Status (3)

Country Link
EP (1) EP0220788B1 (en)
AT (1) ATE81031T1 (en)
DE (1) DE3586721D1 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6715623B2 (en) 2002-02-26 2004-04-06 Stone Container Corporation Collapsible display shelving

Family Cites Families (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE580037C (en) * 1933-07-05 Walther Reuther Device for mixing powdery, fine and coarse-grained goods
DE1093335B (en) * 1954-10-14 1960-11-24 Albert Theysohn Mixing and kneading device for plastic materials
US3367126A (en) * 1966-05-19 1968-02-06 John D. Howell Floating agitator
FR1488593A (en) * 1966-08-02 1967-07-13 Ici Ltd Apparatus for chemical and physical processes
CH584269A5 (en) * 1973-12-21 1977-01-31 Sandoz Ag
US4341476A (en) * 1977-06-03 1982-07-27 Sollich Kg Spezialmaschinenfabrik Apparatus for treating materials containing cocoa butter
FR2443872A1 (en) * 1978-12-13 1980-07-11 Adler Sa Mixer partic. for preparing mastic - comprising support for mixing receptacle rotatable about vertical axis separate from vertical axis of agitator paddle, simplifying operation

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6715623B2 (en) 2002-02-26 2004-04-06 Stone Container Corporation Collapsible display shelving

Also Published As

Publication number Publication date
EP0220788A3 (en) 1989-04-26
DE3586721D1 (en) 1992-11-05
ATE81031T1 (en) 1992-10-15
EP0220788A2 (en) 1987-05-06

Similar Documents

Publication Publication Date Title
CA1263770A (en) Dewatering solids suspensions
US5316031A (en) Valve with independent control of discharge through plurality of orifices
MXPA06011844A (en) A method, an apparatus and a rotor for homogenizing a medium.
JP2900296B2 (en) Slow and fast stirring tank
US4347004A (en) Mixing apparatus
RU2634778C2 (en) Device for concentration of processed object
EP0220788B1 (en) Liquid flow mixer
US4334788A (en) Pin action mixing pump
KR102086681B1 (en) Centrifugal dehydrator equipped with sludge and coagulant mixture using centrifugal force
US4913806A (en) Apparatus for screening a suspension of fibrous cellulose pulp
WO2019221652A1 (en) Mixing apparatus comprising a rotor and a stator
US5624186A (en) Multi-chamber high pressure dispersion apparatus
EP3626336B1 (en) Mixing system for the introduction of chemical substances in a fluid to be treated
JP7519382B2 (en) Solid Ball Screw Centrifuge
US4455092A (en) Mixing apparatus
JP2005066455A (en) Solid/liquid separator
KR102545054B1 (en) High-speed mixer built-in centrifugal separation, concentration and dewatering device to improve sludge treatment efficiency
FI104621B (en) A method and apparatus for mixing a second medium with a first medium
WO1987000450A1 (en) Double sided mixer
EP0796651B1 (en) Mixing device
RU2084274C1 (en) Dispenser
JPS6135213Y2 (en)
EP0355082B1 (en) Jet ring
SU882573A1 (en) Mixer for liquids
CA2009543A1 (en) Method and apparatus for mixing liquid and coagulant

Legal Events

Date Code Title Description
PUAI Public reference made under article 153(3) epc to a published international application that has entered the european phase

Free format text: ORIGINAL CODE: 0009012

17P Request for examination filed

Effective date: 19861205

AC Divisional application: reference to earlier application

Ref document number: 172649

Country of ref document: EP

AK Designated contracting states

Kind code of ref document: A2

Designated state(s): AT BE CH DE FR GB IT LI NL SE

PUAL Search report despatched

Free format text: ORIGINAL CODE: 0009013

AK Designated contracting states

Kind code of ref document: A3

Designated state(s): AT BE CH DE FR GB IT LI NL SE

17Q First examination report despatched

Effective date: 19901221

GRAA (expected) grant

Free format text: ORIGINAL CODE: 0009210

AC Divisional application: reference to earlier application

Ref document number: 172649

Country of ref document: EP

AK Designated contracting states

Kind code of ref document: B1

Designated state(s): AT BE CH DE FR GB IT LI NL SE

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: NL

Effective date: 19920930

Ref country code: CH

Effective date: 19920930

Ref country code: IT

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRE;WARNING: LAPSES OF ITALIAN PATENTS WITH EFFECTIVE DATE BEFORE 2007 MAY HAVE OCCURRED AT ANY TIME BEFORE 2007. THE CORRECT EFFECTIVE DATE MAY BE DIFFERENT FROM THE ONE RECORDED.SCRIBED TIME-LIMIT

Effective date: 19920930

Ref country code: DE

Effective date: 19920930

Ref country code: SE

Effective date: 19920930

Ref country code: BE

Effective date: 19920930

Ref country code: FR

Effective date: 19920930

Ref country code: AT

Effective date: 19920930

Ref country code: LI

Effective date: 19920930

REF Corresponds to:

Ref document number: 81031

Country of ref document: AT

Date of ref document: 19921015

Kind code of ref document: T

REF Corresponds to:

Ref document number: 3586721

Country of ref document: DE

Date of ref document: 19921105

REG Reference to a national code

Ref country code: CH

Ref legal event code: PL

EN Fr: translation not filed
NLV1 Nl: lapsed or annulled due to failure to fulfill the requirements of art. 29p and 29m of the patents act
PLBE No opposition filed within time limit

Free format text: ORIGINAL CODE: 0009261

STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: NO OPPOSITION FILED WITHIN TIME LIMIT

26N No opposition filed
REG Reference to a national code

Ref country code: GB

Ref legal event code: IF02

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: GB

Payment date: 20030716

Year of fee payment: 19

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: GB

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20040715

GBPC Gb: european patent ceased through non-payment of renewal fee

Effective date: 20040715