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GB1441658A - Carbonators - Google Patents

Carbonators

Info

Publication number
GB1441658A
GB1441658A GB3164673A GB3164673A GB1441658A GB 1441658 A GB1441658 A GB 1441658A GB 3164673 A GB3164673 A GB 3164673A GB 3164673 A GB3164673 A GB 3164673A GB 1441658 A GB1441658 A GB 1441658A
Authority
GB
United Kingdom
Prior art keywords
water
pressure
chamber
throat
stage
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
Application number
GB3164673A
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.)
STRENGER ASSOCIATES
Original Assignee
STRENGER ASSOCIATES
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 STRENGER ASSOCIATES filed Critical STRENGER ASSOCIATES
Publication of GB1441658A publication Critical patent/GB1441658A/en
Expired legal-status Critical Current

Links

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
    • B01F23/20Mixing gases with liquids
    • B01F23/23Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids
    • B01F23/237Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids characterised by the physical or chemical properties of gases or vapours introduced in the liquid media
    • B01F23/2376Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids characterised by the physical or chemical properties of gases or vapours introduced in the liquid media characterised by the gas being introduced
    • B01F23/23762Carbon dioxide
    • B01F23/237621Carbon dioxide in beverages
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F25/00Flow mixers; Mixers for falling materials, e.g. solid particles
    • B01F25/30Injector mixers
    • B01F25/31Injector mixers in conduits or tubes through which the main component flows
    • B01F25/314Injector mixers in conduits or tubes through which the main component flows wherein additional components are introduced at the circumference of the conduit
    • B01F25/3142Injector mixers in conduits or tubes through which the main component flows wherein additional components are introduced at the circumference of the conduit the conduit having a plurality of openings in the axial direction or in the circumferential direction
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F25/00Flow mixers; Mixers for falling materials, e.g. solid particles
    • B01F25/30Injector mixers
    • B01F25/31Injector mixers in conduits or tubes through which the main component flows
    • B01F25/314Injector mixers in conduits or tubes through which the main component flows wherein additional components are introduced at the circumference of the conduit
    • B01F25/3142Injector mixers in conduits or tubes through which the main component flows wherein additional components are introduced at the circumference of the conduit the conduit having a plurality of openings in the axial direction or in the circumferential direction
    • B01F25/31423Injector mixers in conduits or tubes through which the main component flows wherein additional components are introduced at the circumference of the conduit the conduit having a plurality of openings in the axial direction or in the circumferential direction with a plurality of perforations in the circumferential direction only and covering the whole circumference
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F25/00Flow mixers; Mixers for falling materials, e.g. solid particles
    • B01F25/40Static mixers
    • B01F25/42Static mixers in which the mixing is affected by moving the components jointly in changing directions, e.g. in tubes provided with baffles or obstructions
    • B01F25/43Mixing tubes, e.g. wherein the material is moved in a radial or partly reversed direction
    • B01F25/432Mixing tubes, e.g. wherein the material is moved in a radial or partly reversed direction with means for dividing the material flow into separate sub-flows and for repositioning and recombining these sub-flows; Cross-mixing, e.g. conducting the outer layer of the material nearer to the axis of the tube or vice-versa
    • B01F25/4323Mixing tubes, e.g. wherein the material is moved in a radial or partly reversed direction with means for dividing the material flow into separate sub-flows and for repositioning and recombining these sub-flows; Cross-mixing, e.g. conducting the outer layer of the material nearer to the axis of the tube or vice-versa using elements provided with a plurality of channels or using a plurality of tubes which can either be placed between common spaces or collectors

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Dispersion Chemistry (AREA)
  • Non-Alcoholic Beverages (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)
  • Carbon And Carbon Compounds (AREA)

Abstract

1441658 Carbonating liquids STRENGER ASSOCIATES INC 3 July 1973 [20 July 1972] 31646/73 Heading B1C A water carbonator 16 comprises, in the direction of water flow, a first stage 72 in which CO 2 is drawn from a source at lower pressure than that of the water by aspiration into the water and partly absorbed therein, and a second stage 74 in which the water with partly absorbed CO 2 is accelerated, to decrease static pressure and increase turbulence, so that the surface area of the water exposed to the CO 2 is increased to achieve substantially complete CO 2 absorption. Preferably, the water pressure is 90-95 psi, the CO 2 is 2-5 psi less than the water pressure, and the water temperature is between 32-40‹F. The stage 72 comprises an annular chamber 88 receiving CO 2 through an entry port 68, an inner chamber 82 receiving CO 2 from the chamber 88 through radial ports 90, and axial water flow passages 78 communicating with a water inlet port 52 and each intersecting at least one radial CO 2 aspiration passage 80. The stage 74 comprises a conical chamber having a wall 92 tapering to a throat 94 which communicates with a collection chamber 96. The taper angle of the wall 92 is preferably less than 45‹. The cross sectional area of the water inlet port 52 exceeds the total cross sectional area of the passages 78 which in turn exceeds the cross sectional area of the throat 94. In operation, water passing through the passages 78 draws CO 2 radial inwards and outwards respectively from the chambers 88, 82, the entrainment of CO2 molecules causing water flow turbulence and part CO 2 absorption. Water streams ejected from the passages 78 are impinged against the chamber wall 92 and are then combined at the throat 94 to enter the collection chamber 96, the acceleration towards the throat causing decreased static pressure and increased turbulence. In the arrangement of Fig. 1, water from a tank 18 is pumped at 20 through a cooler 22 to a line 32 having carbonators 16 disposed in parallel. Pressure in the line 32 is determined by a pressure regulating valve 36 relieving to atmospheric pressure. As alternatives, the pump 20 may be disposed downstream of the cooler, and the latter may cool the water whilst in the tank. The valve 36 and a CO 2 pressure regulating valve 40 are operatively interconnected. The outlet from each distributor comprises a push button opened faucet 52 which may be fixed directly to the carbonator body. The cooled water and CO 2 may be fed to the carbonators through flexible lines. Cooled pressurised water for the carbonator may be provided from a coil in, or in the wall of, a conventional refrigerator.
GB3164673A 1972-07-20 1973-07-03 Carbonators Expired GB1441658A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US27350972A 1972-07-20 1972-07-20

Publications (1)

Publication Number Publication Date
GB1441658A true GB1441658A (en) 1976-07-07

Family

ID=23044230

Family Applications (1)

Application Number Title Priority Date Filing Date
GB3164673A Expired GB1441658A (en) 1972-07-20 1973-07-03 Carbonators

Country Status (15)

Country Link
JP (1) JPS4950172A (en)
AR (1) AR200653A1 (en)
AT (1) AT338605B (en)
BE (1) BE801399A (en)
BR (1) BR7305464D0 (en)
CA (1) CA1007156A (en)
CH (1) CH575343A5 (en)
DE (1) DE2336877A1 (en)
ES (1) ES415500A1 (en)
FR (1) FR2193791B1 (en)
GB (1) GB1441658A (en)
IT (1) IT985709B (en)
NL (1) NL7308839A (en)
SU (1) SU617002A3 (en)
ZA (1) ZA733022B (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4396529A (en) 1978-11-13 1983-08-02 Nordson Corporation Method and apparatus for producing a foam from a viscous liquid
US5071595A (en) * 1990-08-03 1991-12-10 Ebtech, Inc. Water carbonator system
US5480589A (en) * 1994-09-27 1996-01-02 Nordson Corporation Method and apparatus for producing closed cell foam
EP2070587A1 (en) * 2007-12-11 2009-06-17 Electrolux Home Products Corporation N.V. Beverage dispenser

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE4029982C2 (en) * 1990-09-21 2000-08-10 Steinecker Anton Entwicklung Device for gassing a liquid
DE4319526C2 (en) * 1993-06-14 1996-10-17 Puth Hans Edgar Method and device for carbonating beverages
AU3386995A (en) * 1994-08-23 1996-03-14 Shell Internationale Research Maatschappij B.V. Process and apparatus for mixing fluids
JP5065893B2 (en) * 2004-07-09 2012-11-07 ネステク ソシエテ アノニム System and apparatus for forming a mixture with liquid and diluent

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1768158A (en) * 1923-10-20 1930-06-24 Patrick W Shields Method and apparatus for carbonating
US2519533A (en) * 1946-08-08 1950-08-22 Square Mfg Company Carbonating and cooling means
JPS4923280U (en) * 1972-05-29 1974-02-27

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4396529A (en) 1978-11-13 1983-08-02 Nordson Corporation Method and apparatus for producing a foam from a viscous liquid
US5071595A (en) * 1990-08-03 1991-12-10 Ebtech, Inc. Water carbonator system
US5480589A (en) * 1994-09-27 1996-01-02 Nordson Corporation Method and apparatus for producing closed cell foam
EP2070587A1 (en) * 2007-12-11 2009-06-17 Electrolux Home Products Corporation N.V. Beverage dispenser

Also Published As

Publication number Publication date
IT985709B (en) 1974-12-20
AU5784073A (en) 1975-01-09
JPS4950172A (en) 1974-05-15
BE801399A (en) 1973-10-15
BR7305464D0 (en) 1974-09-05
AT338605B (en) 1977-09-12
DE2336877A1 (en) 1974-01-31
ATA626673A (en) 1976-12-15
ES415500A1 (en) 1976-06-16
CH575343A5 (en) 1976-05-14
FR2193791A1 (en) 1974-02-22
NL7308839A (en) 1974-01-22
FR2193791B1 (en) 1976-09-17
CA1007156A (en) 1977-03-22
AR200653A1 (en) 1974-11-29
ZA733022B (en) 1974-03-27
SU617002A3 (en) 1978-07-25

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Legal Events

Date Code Title Description
PS Patent sealed [section 19, patents act 1949]
PCNP Patent ceased through non-payment of renewal fee