AU2011100842A4 - Improved Ion Exchange Demineralisation of Brackish Water - Google Patents

Improved Ion Exchange Demineralisation of Brackish Water

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Publication number
AU2011100842A4
AU2011100842A4 AU2011100842A AU2011100842A AU2011100842A4 AU 2011100842 A4 AU2011100842 A4 AU 2011100842A4 AU 2011100842 A AU2011100842 A AU 2011100842A AU 2011100842 A AU2011100842 A AU 2011100842A AU 2011100842 A4 AU2011100842 A4 AU 2011100842A4
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AU
Australia
Prior art keywords
column
ion exchange
influent
brackish water
demineralisation
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.)
Ceased
Application number
AU2011100842A
Inventor
Guy Raymond Berthold
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.)
BERTHOLD GUY
Original Assignee
BERTHOLD GUY
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Publication date
Application filed by BERTHOLD GUY filed Critical BERTHOLD GUY
Priority to AU2011100842A priority Critical patent/AU2011100842A4/en
Application granted granted Critical
Publication of AU2011100842A4 publication Critical patent/AU2011100842A4/en
Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

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Abstract

The disclosed ion exchange media filter system is designed to remove NaCl (salt) from brackish water with a total dissolved solid level of not more than 3,000 parts per million. The system relies on 5 distinct zeolite and chitin Medias which are plumed so that the influent passes from the bottom of the filter to the top. The influent must be in contact with each Column of media for at least 20 minutes. The total contact time is 100 minutes. The 5 medias are as follows: 1: Column 1 & 2 are the BTEX extraction SMZ 2: Column 3 is the Chitin & Pearlite column 3: Column 4 is the Clinoptilolite Zeolite treated with HCL 4: Column 5 is the Mordinite Zeolite treated with Ammonium Hydroxide 5: Column 6 is the Clinoptilolite Zeolite treated with Fulvic Acid nI A ~ anI-eu 2?riAAcbic___ ch~ I CL(7 1iiu I I f~ g I___________chi__en {I 1 It> 3M z4oLI - -5 I ii I

Description

AUSTRALIA Patents Act 1990 Provisional Specification Improved Ion Exchange Demineralisation of Brackish Water The invention is described in the following statement Inventors: Guy Raymond Berthold David Carmody 1 Improved Ion Exchange Demineralisation of Brackish Water For many years ion exchange demineralisation systems have deionised water using various types of media contained in filter vessels, with the directional flow of water going from top to bottom. This invention has been specifically designed to employ a 5 stage in series ion exchange procedure with the influent directional flow travelling through the filter vessels from the bottom to the top. The filter vessels will be made of various readily available materials, fibreglass, fabricated steel or plastic materials. The depth of the ion exchange media has to have a minimum of 1.2 metres per column. The influent which can be demineralised has a TDS NaCl of less than 3,000 ppm. The influent must travel through the media at a velocity determined by the bed volume of media and be in contact with the ion exchange media for at least 20 minutes per column. The influent will be in contact with the 5 in series ion exchange columns for a minimum of 100 minutes enabling the ion exchange process to complete.
The media to be employed in series will be the following 1: Surfactant Modified Clinoptilolite Zeolite which will extract BTEX chemicals from the influent. 2: Chitin & pearlite media which will attract anions from the influent. 3: Clinoptilolite Zeolite treated with HCL to attract cations from the influent. 4: Mordinite Zeolite treated with Ammonium Hydroxide to attract any remaining anions within the influent. 5: Clinoptilolite Zeolite treated with Fulvic Acid which complexates with any remaining cations or anions resulting in demineralised effluent.
2 The Invention may be better understood by with reference to the illustrations of the embodiment of the invention which shows the directional flow of the influent and the valving arrangement allows for backwashing and recharging: 1: Column 1 & 2 are the BTEX extraction SMZ 2: Column 3 is the Chitin & Pearlite column 3: Column 4 is the Clinoptilolite Zeolite treated with HCL 4: Column 5 is the Mordinite Zeolite treated with Ammonium Hydroxide 5: Column 6 is the Clinoptilolite Zeolite treated with Fulvic Acid
AU2011100842A 2011-07-11 2011-07-11 Improved Ion Exchange Demineralisation of Brackish Water Ceased AU2011100842A4 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
AU2011100842A AU2011100842A4 (en) 2011-07-11 2011-07-11 Improved Ion Exchange Demineralisation of Brackish Water

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
AU2011100842A AU2011100842A4 (en) 2011-07-11 2011-07-11 Improved Ion Exchange Demineralisation of Brackish Water

Publications (1)

Publication Number Publication Date
AU2011100842A4 true AU2011100842A4 (en) 2011-10-27

Family

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Family Applications (1)

Application Number Title Priority Date Filing Date
AU2011100842A Ceased AU2011100842A4 (en) 2011-07-11 2011-07-11 Improved Ion Exchange Demineralisation of Brackish Water

Country Status (1)

Country Link
AU (1) AU2011100842A4 (en)

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