GB2342594A - Apparatus for pH adjustment of a liquid using carbon dioxide - Google Patents

Apparatus for pH adjustment of a liquid using carbon dioxide Download PDF

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Publication number
GB2342594A
GB2342594A GB9905072A GB9905072A GB2342594A GB 2342594 A GB2342594 A GB 2342594A GB 9905072 A GB9905072 A GB 9905072A GB 9905072 A GB9905072 A GB 9905072A GB 2342594 A GB2342594 A GB 2342594A
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United Kingdom
Prior art keywords
chamber
water
liquid
pressure
carbon dioxide
Prior art date
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Granted
Application number
GB9905072A
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GB2342594B (en
GB9905072D0 (en
Inventor
Martin Standen
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Individual
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Individual
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Publication date
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Publication of GB9905072D0 publication Critical patent/GB9905072D0/en
Publication of GB2342594A publication Critical patent/GB2342594A/en
Application granted granted Critical
Publication of GB2342594B publication Critical patent/GB2342594B/en
Anticipated expiration legal-status Critical
Expired - Fee Related 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
    • 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
    • B01F23/232Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids using flow-mixing means for introducing the gases, e.g. baffles
    • B01F23/2321Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids using flow-mixing means for introducing the gases, e.g. baffles by moving liquid and gas in counter current
    • 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
    • B01F23/236Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids specially adapted for aerating or carbonating beverages
    • B01F23/2362Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids specially adapted for aerating or carbonating beverages for aerating or carbonating within receptacles or tanks, e.g. distribution machines

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)

Abstract

The apparatus comprises a chamber into which liquid is fed from a reducing valve B and CO<SB>2</SB> is fed via a pressure regulator E and gas valve F. The liquid in the chamber acts as a gas seal, liquid being drawn off from the bottom of the vessel. The introduction of gas is controlled by a level control mechanism G which opens gas valve F as the level in the chamber rises and closes the valve as the liquid level falls, liquid being introduced so as to establish a gas/liquid equilibrium in the chamber. Unwanted air is removed through a purge valve H. The apparatus may be used for stabilising the pH of a water supply sample for chlorine measurement, the treatment of alkaline effluent and in food processing.

Description

APPARATUS FOR pH ADJUSTMENT WITH CARBON DIOXIDE GAS This invention relates to apparatus for pH adjustment with carbon dioxide gas.
There are many applications where it is necessary to reduce the pH of a liquid. For example, to effectively measure the chlorine residual of a water supply it is often necessary to reduce and stabilise the pH of the sample. PH reduction is also required in the treatment of alkaline effluent and in the food processing industry. Normally this is achieved by the addition of an acid solution. An alternative would be to inject carbon dioxide gas into the liquid and so produce carbonic acid.
Although effective, conventional gas injection is inefficient and escaping unused gas can pose a health and safety risk. Applying gas to the liquid within an enclose environment will improve efficiency, be environmentally friendly and minimise any health and safety risk associated with the gas.
According to the present invention, liquid is passed through a chamber filled with carbon dioxide gas. The gas combines with the liquid producing carbonic acid that reduces and stabilises the pH of the liquid. Pressure and flow control of the liquid and gas ensure a constant and sufficient supply of gas to the liquid whilst preventing the release of any unabsorbed gas into the environment.
Referring to Figure 1.
Liquid enters the top of chamber [A] via pressure reducing valve [B]. Once inside the liquid is dispersed [C] to maximise surface area. The liquid falls through and accumulates at the bottom of the chamber from where it can be drawn off at the desired rate as set by flow regulating valve [D]. The capacity of flow regulating valve [D] must always be less than the available inlet flow through pressure reducing valve [B]. As a result the liquid level in chamber [A] will rise.
A carbon dioxide gas supply is pressure regulated by [E] and connecte to chamber [A] via gas valve [F]. The gas pressure pq is set slightly higher than liquid pressure [Y]. As the level in chamber [A] rises, level control mechanism [G] opens gas valve [F]. Liquid leaving the chamber will now be replaced by gas at pressure [X] in preference to liquid at pressure [Y].
Gas is prevented from back feeding the liquid supply line by pressure reducing valve [B]. As the liquid level falls, level control mechanism [G] will start to close gas valve [F] and liquid will now replenish chamber [A] via pressure reduång valve [B]. Equilibrium is achieved.
To operate effectively air must be removed from chamber [A]. Purge valve [H] releases air/gas from chamber [A], this allows pure carbon dioxide gas to enter via gas valve [F]. Operation of purge valve [H] may be manual or automatic and may also incorporate over pressure protection for chamber [A]. Liquid passing through chamber [A] absorbs the carbon dioxide gas redudng and stabilising the pH. Level control mechanism [G] and gas valve [F] maintain the nominal liquid level in chamber [A] by automatically adding gas as it is absorbed.
Removal of the liquid supply will cause chamber [A] to empty. Level control mechanism [G] will prevent gas valve [F] from opening until the liquid level is restored and the gas seal reestablished.

Claims (7)

  1. CLAIMS 1. An endosed chamber for applying carbon dioxide gas to a liquid for the purpose of pH adjustment.
    2. An endosed chamber as daimed in daim 1, wherein gas may only leave the chamber as a result of absorption into the liquid.
    3. An enclose chamber as daimed in claim 1 and daim 2, wherein a nominal liquid level maintains a seal against escaping gas.
    4. An endosed chamber substantially as described herein with reference to the accompanying drawing.
    Amendments to the claims have been filed as follows 1. An apparatus for dissolving carbon dioxide gas in a continuous water sample for the purpose of pH reduction prior to the measurement of chlorine residual, comprising: a pressure chamber for mixing the carbon dioxide gas and water, a carbon dioxide gas input regulated to pressure X and water input regulated to pressure Y where pressure X > pressure Y, an output for the release of water at reduced pH, a means of regulating the output flow to less than that available at the water input, a means of maintaining the water level within the pressure chamber by variable flow regulation of the carbon dioxide input.
  2. 2. An apparatus in accordance with daim 1 wherein the carbon dioxide input is automatically shut off unless the pressure chamber output is sealed by water.
  3. 3. An apparatus in accordance with daim 1 or 2 wherein no electrical supply is required.
  4. 4. An apparatus in accordance with claim 1 or 2 wherein control of the carbon dioxide gas input is by means of an equilibrium float valve.
  5. 5. An apparatus in accordance with daim 1 or 2 wherein the output pressure is maintained at the water input pressure Y during normal operation.
  6. 6. An apparatus in accordance with claim 1 or 2 wherein the relationship of water flow to water volume is such that the time lag between water input and water output is consistent and less than 30 seconds.
  7. 7. An enclose chamber substantially as described herein with reference to the accompanying drawing.
GB9905072A 1998-05-06 1999-03-08 Apparatus for ph adjustment with carbon dioxide gas Expired - Fee Related GB2342594B (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GBGB9809550.8A GB9809550D0 (en) 1998-05-06 1998-05-06 Gas absorption chamber for ph buffering

Publications (3)

Publication Number Publication Date
GB9905072D0 GB9905072D0 (en) 1999-04-28
GB2342594A true GB2342594A (en) 2000-04-19
GB2342594B GB2342594B (en) 2002-04-10

Family

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Family Applications (2)

Application Number Title Priority Date Filing Date
GBGB9809550.8A Ceased GB9809550D0 (en) 1998-05-06 1998-05-06 Gas absorption chamber for ph buffering
GB9905072A Expired - Fee Related GB2342594B (en) 1998-05-06 1999-03-08 Apparatus for ph adjustment with carbon dioxide gas

Family Applications Before (1)

Application Number Title Priority Date Filing Date
GBGB9809550.8A Ceased GB9809550D0 (en) 1998-05-06 1998-05-06 Gas absorption chamber for ph buffering

Country Status (1)

Country Link
GB (2) GB9809550D0 (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2013003401A1 (en) * 2011-06-29 2013-01-03 Imi Cornelius Inc. Carbonation apparatus and method for forming a carbonated beverage
WO2013006321A1 (en) * 2011-06-29 2013-01-10 Imi Cornelius Inc. Carbonation apparatus and method for forming a carbonated beverage
CN103037716A (en) * 2010-06-29 2013-04-10 Imi科尼利厄斯公司 Carbonation apparatus and method for forming a carbonated beverage

Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB1274363A (en) * 1969-08-28 1972-05-17 Eaton Yale & Towne Improvements in or relating to carbonating liquids
US3731845A (en) * 1970-11-23 1973-05-08 J Booth System for dispensing chilled carbonated water
GB2157963A (en) * 1984-04-25 1985-11-06 Int Distillers & Vintners Limi Apparatus for dissolving gases in liquids
US4850269A (en) * 1987-06-26 1989-07-25 Aquatec, Inc. Low pressure, high efficiency carbonator and method
US4886525A (en) * 1987-06-02 1989-12-12 The Coca-Cola Company System for improving carbonation in post-mix dispenser carbonators
US5417147A (en) * 1994-02-02 1995-05-23 Mason; Thomas Apparatus for carbonating liquids at municipal water pressure
EP0745425A1 (en) * 1995-05-30 1996-12-04 Sanyo Electric Co. Ltd Apparatus for manufacturing carbonated water

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB1274363A (en) * 1969-08-28 1972-05-17 Eaton Yale & Towne Improvements in or relating to carbonating liquids
US3731845A (en) * 1970-11-23 1973-05-08 J Booth System for dispensing chilled carbonated water
GB2157963A (en) * 1984-04-25 1985-11-06 Int Distillers & Vintners Limi Apparatus for dissolving gases in liquids
US4886525A (en) * 1987-06-02 1989-12-12 The Coca-Cola Company System for improving carbonation in post-mix dispenser carbonators
US4850269A (en) * 1987-06-26 1989-07-25 Aquatec, Inc. Low pressure, high efficiency carbonator and method
US5417147A (en) * 1994-02-02 1995-05-23 Mason; Thomas Apparatus for carbonating liquids at municipal water pressure
EP0745425A1 (en) * 1995-05-30 1996-12-04 Sanyo Electric Co. Ltd Apparatus for manufacturing carbonated water

Cited By (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8882084B2 (en) 2010-06-29 2014-11-11 Cornelius, Inc. Variable carbonation using in-line carbonator
CN103037716A (en) * 2010-06-29 2013-04-10 Imi科尼利厄斯公司 Carbonation apparatus and method for forming a carbonated beverage
EP2587944A2 (en) * 2010-06-29 2013-05-08 IMI Cornelius Inc. Carbonation apparatus and method for forming a carbonated beverage
EP2587944A4 (en) * 2010-06-29 2013-12-18 Imi Cornelius Inc Carbonation apparatus and method for forming a carbonated beverage
US8840092B2 (en) 2010-06-29 2014-09-23 Cornelius, Inc. Carbonation apparatus and method for forming a carbonated beverage
US8857797B2 (en) 2010-06-29 2014-10-14 Cornelius, Inc. Carbonation apparatus and method for forming a carbonated beverage
CN103037716B (en) * 2010-06-29 2015-11-25 Imi科尼利厄斯公司 Carbonator and the method for the formation of soda
WO2013006321A1 (en) * 2011-06-29 2013-01-10 Imi Cornelius Inc. Carbonation apparatus and method for forming a carbonated beverage
CN103702749A (en) * 2011-06-29 2014-04-02 Imi科尼利厄斯公司 Carbonation apparatus and method for forming carbonated beverage
CN103717298A (en) * 2011-06-29 2014-04-09 Imi科尼利厄斯公司 Carbonation apparatus and method for forming a carbonated beverage
WO2013003401A1 (en) * 2011-06-29 2013-01-03 Imi Cornelius Inc. Carbonation apparatus and method for forming a carbonated beverage
CN103717298B (en) * 2011-06-29 2015-12-23 Imi科尼利厄斯公司 Carbonator and the method for the formation of soda
CN103702749B (en) * 2011-06-29 2016-07-06 Imi科尼利厄斯公司 Carbonator and the method for forming soda pop

Also Published As

Publication number Publication date
GB2342594B (en) 2002-04-10
GB9905072D0 (en) 1999-04-28
GB9809550D0 (en) 1998-07-01

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PCNP Patent ceased through non-payment of renewal fee

Effective date: 20160308