Difference between revisions of "MemEOL"

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Given the nature of the composite construction used in RO production, relatively simple conversion from an RO to ultrafiltration (UF) membrane is possible<ref name="lawler-2014-F" />. The structure of an RO membrane can be seen in the image below, and flat sheet UF membranes have an extremely similar construction, but are just missing the top polyamide layer. By chemically degrading the polyamide active layer with sodium hypochlorite (NaClO), the polysulfone layer is exposed, resulting in a membrane with properties extremely similar to commercially available UF membranes<ref name="lawler-2014-G" />.
 
Given the nature of the composite construction used in RO production, relatively simple conversion from an RO to ultrafiltration (UF) membrane is possible<ref name="lawler-2014-F" />. The structure of an RO membrane can be seen in the image below, and flat sheet UF membranes have an extremely similar construction, but are just missing the top polyamide layer. By chemically degrading the polyamide active layer with sodium hypochlorite (NaClO), the polysulfone layer is exposed, resulting in a membrane with properties extremely similar to commercially available UF membranes<ref name="lawler-2014-G" />.
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[[File:XsectionVn2 029-Edit.jpg|center|630px|Cross section structure of an RO membrane.]]
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''Cross section structure of an RO membrane.''
  
 
The method for chemical conversion of RO membranes has been optimised, with controlled exposure to 300,000 ppm.hr of NaOCl resulting in organic and virus removal properties, and hydraulic performance, comparable to commercially available 10 – 30 kDa molecular weight cut off UF membranes. Potential applications for the converted RO membranes include use in pre-treatment filtration in desalination plant, waste water treatment or for low cost water treatment in developing areas.
 
The method for chemical conversion of RO membranes has been optimised, with controlled exposure to 300,000 ppm.hr of NaOCl resulting in organic and virus removal properties, and hydraulic performance, comparable to commercially available 10 – 30 kDa molecular weight cut off UF membranes. Potential applications for the converted RO membranes include use in pre-treatment filtration in desalination plant, waste water treatment or for low cost water treatment in developing areas.
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Given the nature of the composite construction used in RO production, relatively simple conversion from an RO to ultrafiltration (UF) membrane is possible<ref name="lawler-2014-F" />. The structure of an RO membrane can be seen in the image below, and flat sheet UF membranes have an extremely similar construction, but are just missing the top polyamide layer. By chemically degrading the polyamide active layer with sodium hypochlorite (NaClO), the polysulfone layer is exposed, resulting in a membrane with properties extremely similar to commercially available UF membranes<ref name="lawler-2014-G" />.
 
Given the nature of the composite construction used in RO production, relatively simple conversion from an RO to ultrafiltration (UF) membrane is possible<ref name="lawler-2014-F" />. The structure of an RO membrane can be seen in the image below, and flat sheet UF membranes have an extremely similar construction, but are just missing the top polyamide layer. By chemically degrading the polyamide active layer with sodium hypochlorite (NaClO), the polysulfone layer is exposed, resulting in a membrane with properties extremely similar to commercially available UF membranes<ref name="lawler-2014-G" />.
 +
 +
[[File:XsectionVn2 029-Edit.jpg|center|630px|Cross section structure of an RO membrane.]]
 +
''Cross section structure of an RO membrane.''
  
 
The method for chemical conversion of RO membranes has been optimised, with controlled exposure to 300,000 ppm.hr of NaOCl resulting in organic and virus removal properties, and hydraulic performance, comparable to commercially available 10 – 30 kDa molecular weight cut off UF membranes. Potential applications for the converted RO membranes include use in pre-treatment filtration in desalination plant, waste water treatment or for low cost water treatment in developing areas.
 
The method for chemical conversion of RO membranes has been optimised, with controlled exposure to 300,000 ppm.hr of NaOCl resulting in organic and virus removal properties, and hydraulic performance, comparable to commercially available 10 – 30 kDa molecular weight cut off UF membranes. Potential applications for the converted RO membranes include use in pre-treatment filtration in desalination plant, waste water treatment or for low cost water treatment in developing areas.

Revision as of 08:02, 27 January 2015

This membrane end-of-life (MemEOL) tool is aimed at promoting better practices in the desalination industry by helping users identify and select the optimum end-of-life option for their used reverse osmosis (RO) membranes. This dynamic and interactive educational tool uses inputs on membrane condition and the relative importance of a number of key criteria to provide recommendation and further information about available end-of-life options.

As user feedback is obtained, and more available end-of-life options are identified and characterised, this tool will become a powerful source of information for membrane users. Ultimately, this tool will include a membrane reuse database, which will allow users to find and contact groups with surplus membrane supplies, thus promoting and simplifying direct membrane reuse. This tool has a significant focus on the Australian desalination industry, but the primary information is highly applicable to countries around the world. Additionally, as the data sources for this tool are not case specific, it should only be considered an educational tool aimed at providing preliminary recommendations to users.

Do you suspect there is any physical damage to the membranes that would prevent them from being reused?

What is the tested permeability of your membranes (Lm⁻²h⁻¹bar⁻¹)?

What is the tested NaCl rejection of your membranes? (% NaCl rejection)

Please order the following criteria in the order of importance for your project (drag and drop):

  • Minimal Financial Impact
  • Low Project Complexity
  • Minimal Environmental Impact
  • Minimal Landfill Impact
  • Positive Public Perception
Rank from most important to least important.

Based on your inputs, the optimum end-of-life scenario for your used membrane is:

A suitable alternative is: