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Trisep Membrane Filters, UA60, Poly(piperazine-amide)-TFC, UF, 90mm, 5/pk

1121460
Sterlitech
TriSep
UA60
Poly(piperazine-amide)-TFC
90 mm
5
5-7 days

Details

Trisep Membrane Filters, UA60, Poly(piperazine-amide)-TFC, UF, 90mm, 5/pk

Specifications

UF Flat-Sheet Performance Comparison by Manufacturer:

SUEZ (GE) | TriSep | Synder | Microdyn Nadir

Veolia


Series GE GH GK PT PW MW
Feed Surface/Chemical Surface/Chemical Surface/Chemical Process/Ultrapure Process/Ultrapure Oil/Water
Type Pre-Treatment, Color Reduction, Purification Pre-Treatment, Color Reduction, Purification Pre-Treatment, Color Reduction, Purification Pre/Post Treatment Pre/Post Treatment Hydrophilic
pH Range (25 °C) 1-11 1-11 1-11 1-11 1-11 2-9
Flux (GFD)/psi 18/400 20/150 17/75 90/50 85/30 176/20
Rejection Size 1K-PEG 2K-PEG 3K-PEG 5K-Dextran 10K-Dextran 50K-Protein
Pore Size/ MWCO 1,000 Da 2,000 Da 3,000 Da 5,000 Da 20,000 Da 50,000 Da
Polymer Composite Polyamide Polyamide-TFC Polyamide-TFC Polyethersulfone Polyethersulfone PAN

SUEZ (GE) | TriSep | Synder | Microdyn Nadir

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Synder Filtration™


Series VT MT ST SM MK V3 BN MQ MQ MAX V4 BY LY V5 BX LX A6 V6 V7
Feed1 IND IND IND IND/WW IND IND/WW IND IND IND IND/WW IND IND IND/WW IND IND IND IND/WW IND/WW
Type2 AB, Pharma Protein, Enzyme BC BC, DC DC Alkalines Brine, Protein Protein, BC Protein, BC FR CWM, Particle CWM, Particle FR CWM, Particle CWM, Particle AP, Microbial CP Laundry Waste
pH Range3 1-11 1-11 1-11 2-11 1-11 1-11 1-11 1-10 1-13 1-11 1-11 1-11 1-11 1-11 1-11 1-11 1-11 1-11
Flux (GFD)/psi 81-125/60 133-205/60 146-225/60 166-255/60 169-260/60 143-220/60 156-240/60 176-270/60  176-270/60  163-250/60 228-350/60 195-300/60 228-350/60 244-375/60 228-350/60 254-390/60 241-370/60 325-500/60
Rej. Size 3K 5K 10K 20k 30K 30K 50K 50K 50K 70K 100K 100K 200K 250K 300K 500K 500K 800K
Pore size/ MWCO 3,000 Da 5,000 Da 10,000 Da 20,000 Da 30,000 Da 30,000 Da 50,000 Da 50,000 Da 50,000 Da 70,000 Da 100,000 Da 100,000 Da 200,000 Da 250,000 Da 300,000 Da 500,000 Da 500,000 Da 800,000 Da
Polymer PES PES PES PES PES PVDF+ PVDF PES PES PVDF+ PVDF PES PVDF+ PVDF PES PVDF PVDF+ PVDF+

Notes:
1 IND=Industrial; WW=Waste Water
2 AB=Antibiotics; AP=Aniodic Paint; BC=Beverage Clarification; CP=Cathiodic Paint; CWM=Corn Wet Milling; DC=Dairy Clarification; FR=Fouling Resistant
3 Evaluated at 25 °C

 Series LV PX PY PZ
 Feed Industrial Wastewater Wastewater Wastewater
 Type Corn Wet Milling Oil Removal Oil Removal,
Enzyme Processing
Oil Removal,
Enzyme Processing
 pH Range (25 °C) 2-10 3-10 2-11 3-10
 Flux (GFD)/psi

202-310/60

244-375/60 192-295/60 179-275/60
 Rejection Size 200K 300K 100K 30K
Pore Size/ MWCO 200,000 Da 300,000 Da 100,000 Da 30,000 Da
Polymer PES PAN PAN PAN

SUEZ (GE) | TriSep | Synder | Microdyn Nadir

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TriSep™


Series UA60 UF5 UF10 UE50 UB70
Feed Process Process Process Process Dairy/Wastewater
Type "Tight" Protein Concentration (High Solids) Purification, Protein "Open" Industrial Wastewater
pH Range (25 °C) 2-11 2-11 2-11 2-11 2-11
Flux (GFD)/psi 45-80/110 10/30 60/20 240/20 48/3
Rejection Size 80% MgSO4 - 95% Cytochrome-C 90% Dextran -
Pore Size/ MWCO 1,000 Da 5,000 Da 10,000 Da 100,000 Da 0.03 µm
Polymer Polypiperazine-amide Polyethersulfone Polyethersulfone Polyethersulfone Polyvinylidene Fluoride 

SUEZ (GE) | TriSep | Synder | Microdyn Nadir

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Microdyn Nadir™

  UH004 UP005 UP010 UP020 UH030 UH050 UP150 UC500 UV150
Feed  Environment, metal, textile, paper, food, pharma/biotech, chemical Environment, metal, textile, paper, food, pharma/biotech, chemical Environment, metal, textile, paper, food, pharma/biotech, chemical  Environment, metal, textile, paper, food, pharma/biotech, chemical  Environment, metal, textile, paper, food, pharma/biotech, chemical Environment, metal, textile, paper, food, pharma/biotech, chemical  Environment, metal, textile, paper, food, pharma/biotech, chemical  Environment, metal, paint, paper, pharma/biotech Environment, metal, paint, paper, pharma/biotech
 Type Hydrophilic,
high chemical resistance
Hydrophilic,
high chemical resistance
Hydrophilic,
high chemical resistance
Hydrophilic,
high chemical resistance
Hydrophilic,
high chemical resistance
Hydrophilic,
high chemical resistance
Hydrophilic,
high chemical resistance
Extremely hydrophilic High stability against oxidizing agents
pH Range (25 °C) 0 to 14 0 to 14 0 to 14 0 to 14 0 to 14 0 to 14 0 to 14 1 to 11 2 to 11
Flux (GFP/psi) 17/58 23.2/58 116/58 163/58 81.2/58 197/58 336/29 203/29 336/29
Rejection Size N/A N/A N/A N/A N/A N/A N/A N/A N/A
Pore Size/ MWCO 4,000 Da 5,000 Da 10,000 Da 20,000 Da 30,000 Da 50,000 Da 150,000 Da 500,000 Da 150,000 Da
Polymer PESH PES PES PES PESH PESH PES RC PVDF
Max Temp © 95 95 95 95 95 95 95 55 95

SUEZ (GE) | TriSep | Synder | Microdyn Nadir

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Frequently Asked Questions

Yes, we can supply the flat sheet membranes in the correct disk size for your stirred cell. Please contact us at [email protected] for pricing and availability.

We offer both BN and V3 Ultrafiltration Flat Sheet Membranes from Synder. The BN is composed of a standard polyvinylidene fluoride material (PVDF), while V3 iscomposed of material designated as PVDF+. This membrane has been treated to create a positive surface charge, optimizing it for alkaline cleaner and industrial waste water treatment applications.

Q. How do I store used flat sheet crossflow membranes?

A. Used flat sheet membranes must always remain wet, including during storage.  Membranes that are allowed to dry will irreversibly lose water permeability.  To prevent microbial growth, the membranes can be stored in a 0.5% solution of formaldehyde.  Alternatively, the membranes can be stored in a 1.0% solution of sodium metabisulfite (SMBS).  To maintain efficacy, the SMBS solution should be replaced monthly.  Or the membranes can be stored in UPDI water that is replaced weekly.

Yes, we are able to offer some of the flat sheet membranes as roll stock. Please contact us at [email protected] to inquire about pricing and availability.

Flow characteristics for a spiral element and flat sheet membrane are significantly different and are really only comparable on a qualitative basis. Variability in the membrane manufacturing process, differences in water composition, test procedures, and test equipment, used in a factory, laboratory, or elsewhere, will impact water flux results.

We do not offer complimentary samples of the flat sheet crossflow membranes. However, most customers find the standard pack quantities to be quite reasonable for initial evaluations. For customers that want to evaluate several different membranes, we do offer custom variety packs. And, in some instances, we may be able to offer custom packs containing smaller sheet quantities. Please contact us to inquire about pricing and availability.

Prior to use, the membranes should be stored in a climate controlled environment, away from sunlight and heat, while sealed in the original packaging. We recommend using the membranes as soon as practical after receiving them. However, most of the flat sheet membranes may be stored for up to one year without affecting performance. The exceptions are the GE cellulose acetate membranes (CE and CK) and the Aquaporin FO membrane which should be used within 6 months.

Q. How do i store used forward osmosis (FO) flat sheet membranes?

Post use, the membrane should be rinsed with water after testing and stored in clean water if the storage duration will be less than 24 hours.  If the membrane is rinsed with water and expected to be stored for longer than 48 hours, it is recommend to use a 1% sodium metabisulfite (SMB, chemical formula Na2S2O5) to prevent bacterial growth from occurring. Periodically inspect the membranes for biological growth. If the preservative solution is cloudy you need to replace it.  Renew the preservative solution every month. 

Yes, you may attempt to reuse flat sheet membranes. However, you may find it difficult to achieve a leak free seal. The cell body o-rings necessarily compress the membrane during installation and the physical action of separating the membrane from the o-rings during removal may cause damage. This damage can impede that ability to achieve a leak free seal when the membrane is reused.

Unfortunately, allowing a previously wetted crossflow membrane to dry usually results in permanent reduction of water permeability. Nevertheless, you can attempt to re-wet the membrane and use it. First, soak the membrane in a 50% alcohol solution for at least 15min (ethanol, methanol, or IPA would be acceptable). Next, install the membrane in the test cell and operate the cell with purified deionized water as though you were pre-conditioning the membrane. After about 30min, the permeate flux should stabilize to whatever rate the membrane is now capable of.

Yes, for flat sheet membranes that will be used with water or aqueous solutions, we recommend that you pre-condition the membranes prior to conducting your separation experiments. Pre-conditioning helps ensure that the membranes perform as expected. Also, pre-conditioning removes preservatives and other residuals from the membranes. Purified deionized water is used to pre-condition the membranes. For all flat sheet membranes except the forward osmosis (FO) membranes, install the membrane in the test cell and apply the purified deionized water feed at the normal operating rate and pressure for the membrane. Allow the system to operate with the purified deionized water feed until the permeate flux stabilizes at an expected value. You can now replace the purified deionized water feed with your feed solution and begin your experiments.

Most membrane manufacturers recommend CFVs of 5 to 35cm/s for their spiral wound membrane elements. The flat sheet membranes can be operated in this range to simulate use in such elements. Additionally, the flat sheet membranes may be operated outside of this range by users that want to examine the relationship between CVF and fouling and membrane performance in their applications.

Cross flow velocity (CFV) is the linear velocity of the feed flow tangential to the membrane surface and is typically reported in m/sec or ft/sec. It is calculated by dividing the volumetric flow rate through the feed channel by the cross-sectional area of the feed channel. Please refer to the CFV article at https://www.sterlitech.com/blog/post/tech-tips-cross-flow-velocity-cfv/ for more information.

The recommended TMP will depend on the type of flat sheet membrane and on the application. Typically, a reasonable TMP will be the same as that noted for the permeate flux specification of the membrane. The specifications for any of the flat sheet membranes can be easily found on our website by clicking the “application/specification” tab on the product web page and scrolling down as necessary. Please contact us at [email protected] if you need additional assistance.

Currently we do not offer cellulose acetate UF flat sheet membranes. However, we do offer a wide variety of hydrophilic flat sheet UF membranes that may be considered as alternatives.

In general, retention of large molecules is not only influence by the molecular weight of the molecule, but also by the shape of the molecule and the physiochemical interactions between the molecule and the membrane. For greatest retention, you should select a UF membrane that has a molecular weight cut-off (MWCO) rating equal to or smaller than the molecular weight of the target molecule.

You may also want to evaluate a UF membrane with a MWCO rating that is one step larger than the target molecule. You may find that this selection offers advantages of lower operating pressure and/or higher permeate flux while still exhibiting acceptable retention of the target molecule.

You can find Sterlitech’s offering of flat sheet UF membranes at https://www.sterlitech.com/ultrafiltration-uf-membrane.html. Please click on the “Application/Specification” tab near the middle of the page, and scroll down as necessary, to review the MWCO ratings.

Both the Microdyne Nadir PES UF membranes and the PESH UF membranes are composed of polyethersulfone and are hydrophilic. The PESH UF membranes have been modified for enhanced hydrophilic properties and, consequently, may be more easily preconditioned and may have better resistance to fouling in some applications.

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