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NF membranes separate at roughly 200 to 1,000 daltons, rejecting divalent ions such as calcium, magnesium and sulphate at 90 to 98 percent while passing 20 to 80 percent of monovalent salt. They suit softening, colour and COD reduction where full desalination is not wanted.
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NF membranes separate at roughly 200 to 1,000 daltons, rejecting divalent ions such as calcium, magnesium and sulphate at 90 to 98 percent while passing 20 to 80 percent of monovalent salt. They suit softening, colour and COD reduction where full desalination is not wanted.
Nanofiltration occupies the gap between ultrafiltration and reverse osmosis, and its defining characteristic is selectivity rather than rejection. It discriminates strongly between divalent and monovalent ions, which is what makes it useful for softening and colour removal while leaving a mineral profile intact.
That selectivity is also the trap. NF is frequently specified as a lower-pressure reverse osmosis, and on a feed whose problem is sodium chloride it simply passes most of it.
| Parameter | Typical value or range | Notes |
|---|---|---|
| Molecular weight cut-off | Roughly 200–1,000 Da | Between UF and RO |
| Divalent ion rejection | 90–98 % | Ca²⁺, Mg²⁺, SO₄²⁻ |
| Monovalent salt rejection | 20–80 % retained | Much of the NaCl passes |
| Operating pressure | 5–15 bar | Lower than RO for comparable flux |
| Colour and larger organics | Substantially removed | A common driver in textile and surface water duty |
| Module format | Spiral wound, standard element sizes | Fits standard pressure vessels |
| Free chlorine tolerance | Effectively nil on polyamide | Same protection as RO is required |
Typical ranges across the membrane class. Final values follow the datasheet of the element quoted.
TDS is a single number that hides the composition NF actually acts on. A feed at 1,500 ppm TDS that is mostly calcium and sulphate is an excellent NF candidate; the same 1,500 ppm as sodium chloride is a poor one, because most of it will pass.
Ask the laboratory for the ionic breakdown — calcium, magnesium, sodium, sulphate, chloride and bicarbonate — before deciding between NF and RO. The split between divalent and monovalent species is the whole decision.
Water treatment does not have a list price, and any supplier quoting one before seeing a feed analysis is quoting a different plant from the one you need.
On request, and capacity-dependent. Plant pricing moves with capacity, feed water analysis and the recovery target; membranes, cartridges and resins are quoted per element, per lot or per litre of media.
From a single replacement element or a case of cartridges through to full plant scope. Consumable lines are quoted per box or per lot, and the lot size is stated on the quotation.
Confirmed per line item at quotation stage. Stocked consumable lines and made-to-order plant differ substantially, so a single blanket lead time for the category would be misleading — the quotation carries the figure for each line.
GST invoice against company or institutional purchase order. Proforma issued where advance payment or internal approval requires it.
Despatch from Delhi NCR across India, including plant, project and institutional sites. Delivery city and site access are asked for at enquiry because both affect despatch mode.
Technical datasheet for the item quoted, and a test certificate where the principal supplies one with that product. Tender and institutional documentation formats are prepared on request — send the format with the enquiry so the quotation is issued in a form you can submit without rework.
Fields marked with an asterisk are required. The technical fields are what usually decide whether you get a quotation on the first pass or three emails of clarification.
Selectivity. NF rejects divalent ions at 90 to 98 percent but passes 20 to 80 percent of monovalent salts. RO rejects both at 96 to 99.8 percent.
NF runs at lower pressure — 5 to 15 bar against 10 to 17 bar for brackish RO — which is why it looks attractive. The saving is only real if passing monovalent salt is acceptable in your product water.
It can, and it does so without salt regeneration or the associated effluent. NF removes calcium and magnesium at 90 to 98 percent along with sulphate.
The comparison should include membrane replacement and cleaning against salt and regeneration cost over the plant life, and whether the monovalent passage is acceptable downstream.
Yes, where the membrane is polyamide, which most spiral NF elements are. Free chlorine oxidises the film and the damage is not reversible by cleaning.
Carbon or SMBS dosing ahead of the module, plus a downstream free-chlorine check, applies exactly as it does for RO.
Specified alongside nf membranes, and the category this page sits in.
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