BWRO vs SWRO: When Brackish?
Brackish water reverse osmosis (BWRO) and seawater reverse osmosis (SWRO) are mechanistically similar but design-distinct. The dividing line, in practical terms, sits around 5,000 mg/L TDS. Below that, you are firmly in BWRO territory: lower operating pressures (10–25 bar instead of 55–85 bar), higher recoveries (75–85% instead of 35–50%), thinner-wall pressure vessels, and a completely different membrane catalog. Brackish water feed sources include inland wells, agricultural runoff, river water with high mineral content, mine drainage, oil & gas produced water, and the concentrate from previous treatment stages.
Choosing brackish-rated equipment for a feed water that turns out to be marginal seawater — or vice versa — is the single most expensive design mistake we see in BWRO. This guide walks through the ten steps to get the design right the first time.
1Feed Water Analysis
Nothing else in the design matters until you have a complete water analysis. For BWRO sizing, request a minimum lab panel covering:
- TDS and conductivity — the headline number that sets pressure
- Major cations: Na, K, Ca, Mg, Sr, Ba, Fe, Mn
- Major anions: Cl, SO₄, HCO₃, CO₃, NO₃, F, SiO₂ (silica)
- pH, temperature (year-round range), turbidity, SDI₁₅
- Organics: TOC, color, free chlorine, hydrogen sulfide if applicable
- Microbiology: total coliform, HPC if surface-influenced
Sample collection matters. Pull samples from the actual point of intake at the actual season — ideally three samples across the year if the source has any seasonal variation (rivers, shallow wells). A water analysis from a single day in spring will mislead you if the well draws from a brackish aquifer that gets saltier as the water table drops in late summer.
2Establish Permeate Quality Targets
The permeate spec drives the rejection requirements and ultimately the membrane selection and array configuration:
- Potable water (US EPA, WHO): <500 mg/L TDS, <250 mg/L chloride, <250 mg/L sulfate. Single-pass BWRO is usually sufficient.
- Irrigation: driven by the salt-sensitive crop. Boron <0.5 mg/L for citrus, sodium adsorption ratio (SAR) matters more than TDS.
- Boiler feed (low pressure, <100 psi): <10 mg/L TDS, requires a second-pass RO or polishing with mixed-bed DI.
- High-pressure boiler / power generation: <0.5 mg/L TDS, conductivity <1 µS/cm. RO + EDI.
- Cooling tower makeup: often 100–300 mg/L TDS acceptable; single-pass BWRO at reduced recovery.
3Choose Recovery
Recovery is the single most consequential design choice in BWRO. Higher recovery means less concentrate to dispose of, less feed flow to pump, and lower operating cost — but it raises the concentration of every scaling species in the brine, demanding more sophisticated antiscalant chemistry and, at the limit, more aggressive cleaning frequency.
- 75% recovery — a sensible default for unknown feed water with moderate hardness and silica. Achievable with standard antiscalant.
- 80–85% recovery — achievable on most BWRO feeds with proper antiscalant selection and a screening calculation for CaSO₄, CaCO₃, BaSO₄, SrSO₄, and silica saturation in the concentrate.
- >85% recovery — possible but requires care. Often the cleaner path is a second pass (concentrate-treating RO or HEROHigh-Efficiency RO with lime softening between stages).
The screening calculation that matters: compute the Langelier Saturation Index (LSI) and Stiff & Davis Stability Index (S&DSI) for CaCO₃, and the percentage of solubility limit for CaSO₄, BaSO₄, SrSO₄, and amorphous silica in the projected concentrate. Any species above ~80% of saturation needs an antiscalant rated for it and confirmed by the antiscalant supplier on your specific water.
4Capacity Sizing
Three numbers to nail down:
- Average daily demand — m³/day or GPD that the customer actually uses.
- Peak instantaneous demand — the maximum flow rate downstream of the storage tank.
- Storage / buffer volume — typically sized for 4–24 hours of average demand, depending on RO uptime expectations.
Design the RO to deliver the average daily demand over an operating window of 16–20 hours per day. Never design at 24/7 unless redundancy is also provided — you need downtime for membrane cleaning (CIP), cartridge filter changes, and unplanned maintenance. The remaining 4–8 hours becomes the maintenance window, and the storage tank covers the gap.
5Membrane Selection
For BWRO, the choice usually comes down to three Filmtec families (or their Hydranautics / LG equivalents):
- BW30 PRO-400 — the workhorse high-rejection BWRO element. 99.7% nominal NaCl rejection. Standard 8″ × 40″ spiral wound, 400 ft² active area. The default for potable BWRO with typical feed waters of 1,000–5,000 mg/L TDS.
- BW30HR-440 — higher-rejection version. Use when permeate quality requirements are tight or when the feed TDS approaches 8,000–10,000 mg/L.
- BW30 XLE-440 / Eco-440 — low-energy variants. Lower operating pressure (10–14 bar at design flux) at slightly reduced rejection. Use when energy cost or pump-derating is the dominant constraint.
For Hydranautics, the equivalent families are ESPA (Energy-Saving Polyamide), CPA (Composite Polyamide), and LFC (Low Fouling Composite). For LG, the BW family. See our pages on Filmtec, Hydranautics, and LG membranes for current model availability.
6Multi-Stage Array Design
BWRO recovery dictates the number of stages. Each stage typically achieves 50% recovery on its feed:
- Single stage: ~50% recovery max. 2 vessels feeding the same array.
- Two-stage: ~75% recovery. Stage 1 concentrate feeds Stage 2. Classic 2:1 array ratio (e.g., 4 vessels feeding 2 vessels).
- Three-stage: ~85% recovery. Stage 1 to Stage 2 to Stage 3, typically 4:2:1 array ratio.
Pressure vessels are typically 6 or 7 elements long. Crossflow velocity drops as you move down the array (each element extracts permeate, reducing brine-side flow), so the multi-stage design preserves crossflow by reducing vessel count stage-by-stage. Maintaining adequate crossflow is critical to preventing concentration polarization at the membrane surface.
7High-Pressure Pump
BWRO operating pressures are modest by SWRO standards: 10–25 bar depending on feed TDS, recovery, and membrane selection. The default pump selection is a vertical multistage centrifugal pump such as the Grundfos CR series. Sizing:
- Flow: feed flow = permeate flow ÷ recovery. For a 25,000 GPD permeate at 75% recovery, feed = 33,333 GPD = 23 GPM = 5.3 m³/h.
- Pressure: osmotic pressure of concentrate (approx 1 bar per 1,000 mg/L) + flux-driving differential (4–8 bar) + array pressure drop (1–2 bar) + downstream backpressure.
- Stages and motor power: consult the manufacturer's curve for your duty point. Grundfos CR 5, CR 10, CR 15, and CR 20 cover most small-to-medium BWRO duty points.
Materials: 316L stainless steel for the wet end is standard for BWRO with chloride below 1,000 mg/L. For higher chloride, specify Duplex 2205 or step up to Super Duplex 2507.
8Pretreatment
Pretreatment determines membrane life. The minimum specification for a BWRO on well water:
- Cartridge filtration: 5 µm nominal at the RO feed. Polypropylene melt-blown or pleated. Size for <1 GPM per 10″ cartridge length for reasonable life.
- Multimedia filtration (MMF): required if feed SDI₁₅ > 5 or turbidity > 1 NTU. Anthracite/sand/garnet with backwash on differential pressure or timer.
- Antiscalant injection: typically 2–5 mg/L of phosphonate-based antiscalant, dosed continuously into the RO feed. Quantity confirmed by software projection (Filmtec WAVE, Hydranautics IMSDesign, LG Q+ Projection) on your specific water.
- Chlorine removal: if any chlorine is present, you must remove it before the polyamide membrane. Granular activated carbon (GAC) for low chlorine, SBS (sodium bisulfite) injection with adequate residence time for higher chlorine. Polyamide membranes are destroyed by even brief chlorine exposure.
- Iron / manganese removal: if Fe > 0.1 mg/L or Mn > 0.05 mg/L, oxidation + filtration upstream of the RO. Greensand plus + KMnO₄ is the workhorse approach.
- Softening: if hardness drives a recovery limit, ion-exchange softening upstream of the RO can permit higher recovery and lower antiscalant dose. Use a Fleck control valve on duplex softeners for continuous service.
9Controls
A modern BWRO PLC monitors and trends at minimum:
- Feed, permeate, and concentrate flow (paddlewheel or magmeter)
- Feed, interstage, and concentrate pressure (4–20 mA transmitters)
- Permeate conductivity (and feed conductivity for normalized rejection)
- Differential pressure across cartridge filter and across each stage
- Tank levels (feed break tank and permeate storage)
- Pump suction pressure interlock to prevent dry-run
- Conductivity high alarm with auto-divert to drain until rejection recovers after startup
For solar or off-grid BWRO, soft-start variable frequency drives (VFDs) on the high-pressure pump are mandatory. They protect the membranes from water-hammer at startup and allow flux control as feed water temperature and TDS shift.
10Permitting and Brine Disposal
The often-underestimated step. BWRO concentrate is typically 2–5x the feed TDS and is rarely just "salty water" — it carries the antiscalant chemistry, the pretreatment carryover, and any membrane CIP residual. Disposal options, from cheapest to most expensive:
- Sewer discharge: requires industrial discharge permit; usually has TDS, sulfate, or specific-ion limits. Check with your local POTW.
- Deep well injection: Class V well permit (US EPA UIC program). Feasible where geology supports it; geotechnical study required.
- Evaporation ponds: arid regions only; large land requirement. Lining and groundwater monitoring required.
- Zero Liquid Discharge (ZLD): brine concentrator (mechanical vapor recompression) followed by a crystallizer. Eliminates liquid discharge entirely. Capital-intensive but increasingly required by regulators in water-scarce regions.
Worked Example: 25,000 GPD BWRO
Feed: well water, 3,000 mg/L TDS, hardness 350 mg/L CaCO₃, silica 15 mg/L, no iron, no free chlorine.
Permeate target: 25,000 GPD potable water at <500 mg/L TDS, operating 18 hours per day.
Sizing calculation:
- Average permeate rate: 25,000 GPD ÷ 18 h = 1,389 GPH = 23.1 GPM = 5.25 m³/h
- Recovery target: 75% (silica and hardness allow this with phosphonate antiscalant)
- Feed flow: 23.1 / 0.75 = 30.8 GPM = 7.0 m³/h
- Concentrate flow: 7.7 GPM = 1.75 m³/h
- Concentrate TDS: 3,000 / (1 - 0.75) = 12,000 mg/L (well within antiscalant capability)
- Array: 2:1, two-stage. Stage 1 = 2 vessels × 6 elements; Stage 2 = 1 vessel × 6 elements. Total 18 elements.
- Membrane: Filmtec BW30 PRO-400 (or equivalent). Element flux: 23.1 GPM / 18 elements / 400 ft² = ~12 GFD — conservative and consistent with standard BWRO flux guidelines.
- High-pressure pump: Grundfos CR 10 series, 30 GPM at ~14 bar (200 psi). 7.5 hp motor with VFD.
- Pretreatment: dual 5-µm polypropylene cartridge filters in parallel, antiscalant injection skid, no GAC required (no chlorine), softener optional for higher-recovery option.
- Storage: 12,500-gallon polyethylene atmospheric tank (half-day buffer).
This sizing exercise maps cleanly onto our standard BWRO 20,000–50,000 GPD product line, available as either a packaged skid or a containerized unit. For the project specifics — pretreatment customization, controls philosophy, brine disposal — please request a quote with your water analysis attached.
Related reading: Brackish Water Desalination Systems overview, SWRO Design Guide.
