Difference between revisions of "MemEOL Test"

Revision as of 06:16, 28 August 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?

No Yes

Find out more about membrane damage.

Please provide the following information about your membrane:

Find out more about standard testing methods.

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.

Find out more about the assessment criteria.

Based on information provided:

	Permeability (L/m²/h/bar)	NaCl Rejection (%)
Original Performance - data from supplier website	0.500 0.501 0.695 0.576 0.941 0.656 0.446 0.463 0.841 0.694 0.574 0.468 0.848 0.693 0.570 0.570 0.550 0.493 0.535 0.491 0.501 0.693 0.927 0.499 0.500 0.750 0.746 0.577 0.692 0.576 2.909 2.885 2.892 2.406 2.909 2.885 2.885 2.892 3.111 3.109 3.108 3.156 2.827 2.893 2.893 2.853 3.110 2.893 2.893 2.853 3.182 3.156 3.156 4.750 6.281 7.432 3.004 2.965 1.642 3.009 4.848 3.641 4.848 7.388 3.011 2.601 3.009 2.322 1.801 2.871 2.860 2.853 1.728 Not Available Not Available 2.909880565 Not Available 5.015 6.582 2.868 1.272 2.420 6.634 8.574 6.695 6.362 Not Available Not Available	99.75 99.75 99.7 99.75 99.8 99.8 99.86 99.82 99.6 99.6 99.8 99.82 99.7 99.8 99.8 99.6 99.8 99.7 99.6 99.7 99.8 99.8 99.8 99.75 99.75 99.7 99.7 99.75 99.8 99.75 99.7 99.7 99.7 99.5 99.7 99.7 99.5 99.5 99.3 99.3 99.3 99.7 99.5 99.5 99.5 99.5 99.65 99.5 99.5 99.5 99.4 99.5 99.3 99.3 99 99 99.7 99.7 99.7 99.7 99.3 99.6 99.6 99.2 99.4 99.7 99.7 99.5 99.7 99.7 99.7 99.7 99.7 Not Available Not Available 99.5 Not Available 99.5 99.3 99.8 98.5 98.5 85 83 86 90 55 60
Current Performance - based on supplied inputs

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

A suitable alternative is:

[saikia-1] Saikia, N.; de Brito, J. Construction and Building Materials (2012), 34, 385-401.

[tan-2] Tan, R. B. H.; Khoo, H. H. "Impact Assessment of Waste Management Options in Singapore." Journal of the Air & Waste Management Association (2006), 56, 244–254.

[abs-3] Australian Bureau of Statistics. Australia’s Environment: Issues and Trends. (2010). Available at www.abs.gov.au.

[wu-4] Wu, C.; Williams, P. T. Fuel (2010), 89, 3022-3032.

[al-salem-5] Al-Salem, S. M.; Lettieri, P.; Baeyens, J. Waste Management (2009), 56, 244–254.

[lawler-2014-B-6] Lawler, W.; Alvarez-Gaitan, J.; Leslie, G.; Le-Clech, P. Desalination (2014), 357, 45-54.

[lawler-2014-C-7] Lawler, W.; Alvarez-Gaitan, J.; Leslie, G.; Le-Clech, P. Desalination (2014), 357, 45-54.

[sahajwalla-8] Sahajwalla, V.; Zaharia, M.; Kongkarat, S.; Khanna, R.; Rahman, M.; Saha-Chaudhury, N.; O’Kane, P.; Dicker, J.; Skidmore, C.; Knights, D. Energy & Fuels (2012), 26, 58-66.

[lawler-2014-D-9] Lawler, W.; Alvarez-Gaitan, J.; Leslie, G.; Le-Clech, P. "Assessment of End-of-Life Opportunities for Reverse Osmosis Membranes." The University of New South Wales (2015).

[lawler-2014-E-10] Lawler, W.; Alvarez-Gaitan, J.; Leslie, G.; Le-Clech, P. "Assessment of End-of-Life Opportunities for Reverse Osmosis Membranes." The University of New South Wales (2015).

[a-vard-11] A’Vard, D.; O’Farrell, K. National Recycling Survey Final Report; Plastics and Chemicals Industries Association: Carlton, VIC (2013)

[brulliard-12] Brulliard, C.; Cain, R.; Do, D.; Dornom, T.; Lim, B.; Olesson, E.; Young, S. "The Australian recycling sector." Department of Sustainability, Environment, Water, Population and Communities (2012). Available at www.environment.gov.au

[goodship-13] Goodship, V. "Introduction to Plastic Recycling". Smithers Rapra Technology Limited: Shawbury UK (2007)

[pacia-14] PACIA. "Plastic recycling in Australia remains strong" (2012)

[saikia-15] Saikia, N.; de Brito, J. Construction and Building Materials (2012), 34, 385-401.

[ould-16] Ould Mohamedou, E.; Penate Suarez, D. B.; Vince, F.; Jaouen, P.; Pontie, M. Desalination (2010), 253, 62–70.

[kazemi-17] Kazemi Najafi, S. Waste management; New York (2013)

[lawler-2014-F-18] Lawler, W.; Antony, A.; Cran, M.; Duke, M.; Leslie, G.; Le-Clech, P. Journal of Membrane Science (2013), 447, 203-211

[lawler-2014-G-19] Lawler, W.; Alvarez-Gaitan, J.; Leslie, G.; Le-Clech, P. "Assessment of End-of-Life Opportunities for Reverse Osmosis Membranes." The University of New South Wales (2015).

[lawler-2014-H-20] Lawler, W.; Alvarez-Gaitan, J.; Leslie, G.; Le-Clech, P. "Assessment of End-of-Life Opportunities for Reverse Osmosis Membranes." The University of New South Wales (2015).

[pontie-21] Pontié, M.; Rapenne, S.; Thekkedath, A.; Duchesne, J.; Jacquemet, V.; Leparc, J. Desalination (2005), 181, 75-90

[saikia-22] Saikia, N.; de Brito, J. Construction and Building Materials (2012), 34, 385-401.

[tan-23] Tan, R. B. H.; Khoo, H. H. "Impact Assessment of Waste Management Options in Singapore." Journal of the Air & Waste Management Association (2006), 56, 244–254.

[abs-24] Australian Bureau of Statistics. Australia’s Environment: Issues and Trends. (2010). Available at www.abs.gov.au.

[wu-25] Wu, C.; Williams, P. T. Fuel (2010), 89, 3022-3032.

[al-salem-26] Al-Salem, S. M.; Lettieri, P.; Baeyens, J. Waste Management (2009), 56, 244–254.

[lawler-2014-B-27] Lawler, W.; Alvarez-Gaitan, J.; Leslie, G.; Le-Clech, P. Desalination (2014), 357, 45-54.

[lawler-2014-C-28] Lawler, W.; Alvarez-Gaitan, J.; Leslie, G.; Le-Clech, P. Desalination (2014), 357, 45-54.

[sahajwalla-29] Sahajwalla, V.; Zaharia, M.; Kongkarat, S.; Khanna, R.; Rahman, M.; Saha-Chaudhury, N.; O’Kane, P.; Dicker, J.; Skidmore, C.; Knights, D. Energy & Fuels (2012), 26, 58-66.

[lawler-2014-D-30] Lawler, W.; Alvarez-Gaitan, J.; Leslie, G.; Le-Clech, P. "Assessment of End-of-Life Opportunities for Reverse Osmosis Membranes." The University of New South Wales (2015).

[lawler-2014-E-31] Lawler, W.; Alvarez-Gaitan, J.; Leslie, G.; Le-Clech, P. "Assessment of End-of-Life Opportunities for Reverse Osmosis Membranes." The University of New South Wales (2015).

[a-vard-32] A’Vard, D.; O’Farrell, K. National Recycling Survey Final Report; Plastics and Chemicals Industries Association: Carlton, VIC (2013)

[brulliard-33] Brulliard, C.; Cain, R.; Do, D.; Dornom, T.; Lim, B.; Olesson, E.; Young, S. "The Australian recycling sector." Department of Sustainability, Environment, Water, Population and Communities (2012). Available at www.environment.gov.au

[goodship-34] Goodship, V. "Introduction to Plastic Recycling". Smithers Rapra Technology Limited: Shawbury UK (2007)

[pacia-35] PACIA. "Plastic recycling in Australia remains strong" (2012)

[saikia-36] Saikia, N.; de Brito, J. Construction and Building Materials (2012), 34, 385-401.

[ould-37] Ould Mohamedou, E.; Penate Suarez, D. B.; Vince, F.; Jaouen, P.; Pontie, M. Desalination (2010), 253, 62–70.

[kazemi-38] Kazemi Najafi, S. Waste management; New York (2013)

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@@ Line 779: / Line 779: @@
 <div class="membrane-performance-table">
 <table class="table table-bordered table-striped table-responsive">
-<thead><tr><th></th><th>Permeability</th><th>NaCl Rejection</th></tr></thead>
+<thead><tr><th></th><th>Permeability (L/m²/h/bar)</th><th>NaCl Rejection (%)</th></tr></thead>
 <tbody><tr>
-<td>Original Performance</td>
+<td>Original Performance - data from supplier website</td>
-<td><div class="orig-membrane-performance-permeate TM820C-370" style="display: none;">0.50028822</div>
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-<div class="orig-membrane-performance-permeate SW30XHR-400i" style="display: none;">0.468882461</div>
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+<div class="orig-membrane-performance-permeate SW30ULE-400i" style="display: none;">0.848</div>
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-<div class="orig-membrane-performance-permeate SW30HRLE-400i" style="display: none;">0.570813431</div>
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-<div class="orig-membrane-performance-permeate SW30HRLE-400" style="display: none;">0.570813431</div>
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-<div class="orig-membrane-performance-permeate SW30HRLE-370/34i" style="display: none;">0.550978215</div>
+<div class="orig-membrane-performance-permeate SW30HRLE-370/34i" style="display: none;">0.550</div>
-<div class="orig-membrane-performance-permeate SW30HR-380" style="display: none;">0.493560486</div>
+<div class="orig-membrane-performance-permeate SW30HR-380" style="display: none;">0.493</div>
-<div class="orig-membrane-performance-permeate SWC1-4040" style="display: none;">0.53586567</div>
+<div class="orig-membrane-performance-permeate SWC1-4040" style="display: none;">0.535</div>
-<div class="orig-membrane-performance-permeate SWC3" style="display: none;">0.491472568</div>
+<div class="orig-membrane-performance-permeate SWC3" style="display: none;">0.491</div>
-<div class="orig-membrane-performance-permeate SWC4+" style="display: none;">0.501500372</div>
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-<div class="orig-membrane-performance-permeate SWC5" style="display: none;">0.693130595</div>
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-<div class="orig-membrane-performance-permeate AE-400" style="display: none;">0.692430102</div>
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-<div class="orig-membrane-performance-permeate TM720L-400" style="display: none;">2.406929968</div>
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-<div class="orig-membrane-performance-permeate TML20-370" style="display: none;">2.909164977</div>
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+<div class="orig-membrane-performance-permeate XLE-440" style="display: none;">6.281</div>
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+<div class="orig-membrane-performance-permeate CPA4" style="display: none;">1.642</div>
-<div class="orig-membrane-performance-permeate CPA5-LD" style="display: none;">3.009265278</div>
+<div class="orig-membrane-performance-permeate CPA5-LD" style="display: none;">3.009</div>
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+<div class="orig-membrane-performance-permeate ESPA2" style="display: none;">3.641</div>
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-<div class="orig-membrane-performance-permeate LFC1" style="display: none;">3.011435421</div>
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+<div class="orig-membrane-performance-permeate LFC3" style="display: none;">2.601</div>
-<div class="orig-membrane-performance-permeate LFC3-LD" style="display: none;">3.009265278</div>
+<div class="orig-membrane-performance-permeate LFC3-LD" style="display: none;">3.009</div>
-<div class="orig-membrane-performance-permeate RE8040-CE" style="display: none;">2.322053255</div>
+<div class="orig-membrane-performance-permeate RE8040-CE" style="display: none;">2.322</div>
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+<div class="orig-membrane-performance-permeate RE8040-BR400" style="display: none;">1.801</div>
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+<div class="orig-membrane-performance-permeate RE8040-BE" style="display: none;">2.871</div>
-<div class="orig-membrane-performance-permeate RE8040-BE440" style="display: none;">2.860643348</div>
+<div class="orig-membrane-performance-permeate RE8040-BE440" style="display: none;">2.860</div>
-<div class="orig-membrane-performance-permeate RE8040-BN" style="display: none;">2.853886986</div>
+<div class="orig-membrane-performance-permeate RE8040-BN" style="display: none;">2.853</div>
-<div class="orig-membrane-performance-permeate RE8040-BR" style="display: none;">1.728500046</div>
+<div class="orig-membrane-performance-permeate RE8040-BR" style="display: none;">1.728</div>
-<div class="orig-membrane-performance-permeate Industrial-RO3-8040F35" style="display: none;"></div>
+<div class="orig-membrane-performance-permeate Industrial-RO3-8040F35" style="display: none;">Not Available</div>
-<div class="orig-membrane-performance-permeate Industrial-RO3-8040F50" style="display: none;"></div>
+<div class="orig-membrane-performance-permeate Industrial-RO3-8040F50" style="display: none;">Not Available</div>
 <div class="orig-membrane-performance-permeate Industrial-RO5-8040F50" style="display: none;">2.909880565
 </div>
-<div class="orig-membrane-performance-permeate OSMO-BEV-ULE-CG-WT" style="display: none;"></div>
+<div class="orig-membrane-performance-permeate OSMO-BEV-ULE-CG-WT" style="display: none;">Not Available</div>
-<div class="orig-membrane-performance-permeate MUNI-RO-400-HR-LE" style="display: none;">5.015634226</div>
+<div class="orig-membrane-performance-permeate MUNI-RO-400-HR-LE" style="display: none;">5.015</div>
-<div class="orig-membrane-performance-permeate AK-400" style="display: none;">6.582010152</div>
+<div class="orig-membrane-performance-permeate AK-400" style="display: none;">6.582</div>
-<div class="orig-membrane-performance-permeate MUNI-RO-400-HR" style="display: none;">2.868828766</div>
+<div class="orig-membrane-performance-permeate MUNI-RO-400-HR" style="display: none;">2.868</div>
-<div class="orig-membrane-performance-permeate SE8040C30" style="display: none;">1.272165664</div>
+<div class="orig-membrane-performance-permeate SE8040C30" style="display: none;">1.272</div>
-<div class="orig-membrane-performance-permeate SG8040F30" style="display: none;">2.420078063</div>
+<div class="orig-membrane-performance-permeate SG8040F30" style="display: none;">2.420</div>
-<div class="orig-membrane-performance-permeate NF90-400" style="display: none;">6.634007288</div>
+<div class="orig-membrane-performance-permeate NF90-400" style="display: none;">6.634</div>
 <div class="orig-membrane-performance-permeate NF270-400" style="display: none;"></div>
-<div class="orig-membrane-performance-permeate ESNA1-LF2-LD" style="display: none;">8.574365886</div>
+<div class="orig-membrane-performance-permeate ESNA1-LF2-LD" style="display: none;">8.574</div>
-<div class="orig-membrane-performance-permeate ESNA1-LF-LD" style="display: none;">6.695348676</div>
+<div class="orig-membrane-performance-permeate ESNA1-LF-LD" style="display: none;">6.695</div>
-<div class="orig-membrane-performance-permeate NE8040-90" style="display: none;">6.362007168</div>
+<div class="orig-membrane-performance-permeate NE8040-90" style="display: none;">6.362</div>
-<div class="orig-membrane-performance-permeate NE8040-70" style="display: none;"></div>
+<div class="orig-membrane-performance-permeate NE8040-70" style="display: none;">Not Available</div>
-<div class="orig-membrane-performance-permeate OSMO-BEV-NF-FF" style="display: none;"></div>
+<div class="orig-membrane-performance-permeate OSMO-BEV-NF-FF" style="display: none;">Not Available</div>
 </td>
 <td><div class="orig-membrane-performance-nacl-rejection TM820C-370" style="display: none;">99.75</div>
@@ Line 946: / Line 946: @@
 <div class="orig-membrane-performance-nacl-rejection RE8040-BN" style="display: none;">99.7</div>
 <div class="orig-membrane-performance-nacl-rejection RE8040-BR" style="display: none;">99.7</div>
-<div class="orig-membrane-performance-nacl-rejection Industrial-RO3-8040F35" style="display: none;"></div>
+<div class="orig-membrane-performance-nacl-rejection Industrial-RO3-8040F35" style="display: none;">Not Available</div>
-<div class="orig-membrane-performance-nacl-rejection Industrial-RO3-8040F50" style="display: none;"></div>
+<div class="orig-membrane-performance-nacl-rejection Industrial-RO3-8040F50" style="display: none;">Not Available</div>
 <div class="orig-membrane-performance-nacl-rejection Industrial-RO5-8040F50" style="display: none;">99.5</div>
-<div class="orig-membrane-performance-nacl-rejection OSMO-BEV-ULE-CG-WT" style="display: none;"></div>
+<div class="orig-membrane-performance-nacl-rejection OSMO-BEV-ULE-CG-WT" style="display: none;">Not Available</div>
 <div class="orig-membrane-performance-nacl-rejection MUNI-RO-400-HR-LE" style="display: none;">99.5</div>
 <div class="orig-membrane-performance-nacl-rejection AK-400" style="display: none;">99.3</div>
@@ Line 964: / Line 964: @@
 </td>
 </tr><tr>
-<td>Current Performance</td>
+<td>Current Performance - based on supplied inputs</td>
 <td><div class="curr-membrane-performance-permeate" style="display: none;"></div></td>
 <td><div class="curr-membrane-performance-nacl-rejection" style="display: none;"></div></td>

Compatible with plastic components	Yes
Compatible with fibreglass components	No
Available in Australia	Emerging
Available globally	Yes
Manual disassembly required	Yes

Compatible with plastic components	Yes
Compatible with fibreglass components	No
Available in Australia	Emerging
Available globally	Emerging
Manual disassembly required	Yes

Compatible with plastic components	Yes
Compatible with fibreglass components	Possible but limited
Available in Australia	Yes
Available globally	Yes
Manual disassembly required	Yes

NaCl rejection range (%)	Permeability range (L.m⁻².h⁻¹.bar⁻¹)	Designation	Action	Estimated reuse lifespan (yrs)
99.9 - 99.6	> 0.45	High quality SWRO	Direct reuse as SWRO possible in normal applications	2 –5
99.7 - 99.2	> 1.6	High quality BWRO	Direct reuse as BWRO possible in normal applications	2 – 3
99.2 – 98	> 1.6	Medium quality BWRO	Direct reuse as BWRO in standard applications possible	1 – 2
98 – 96	> 1	Low quality BWRO	Direct reuse as BWRO in harsh applications where regular replacement is required	1
96 – 80	> 5	Medium quality NF	Direct reuse as NF membrane possible	-
< 96	< 5	Unsuitable for RO or NF	Membrane suitable for UF conversion.	-

Difference between revisions of "MemEOL Test"

Revision as of 06:16, 28 August 2015

Disposal in local landfill

Energy recovery through incineration

Contents

References

Energy recovery though syngas production

References

Energy recovery through use as a coke substitute in Electric Arc Furnaces

References

Material recycling

References

Chemical conversion to an ultrafiltration membrane and then reuse

References

Direct reuse as a high quality seawater RO membranes

Direct reuse as a high quality brackishwater RO membranes

Direct reuse as a medium quality brackishwater RO membranes

Direct reuse as a low quality brackishwater RO membranes

Direct reuse as a medium quality nanofiltration membranes

References

Disposal in local landfill

Energy recovery through incineration

References

Energy recovery though syngas production

References

Energy recovery through use as a coke substitute in Electric Arc Furnaces

References

Material recycling

References

Chemical conversion to an ultrafiltration membrane and then reuse

References

Direct reuse as a high quality seawater RO membranes

Direct reuse as a high quality brackishwater RO membranes

Direct reuse as a medium quality brackishwater RO membranes

Direct reuse as a low quality brackishwater RO membranes

Direct reuse as a medium quality nanofiltration membranes

References