This 20,000 LPH (20 m³/hr) water softener is designed to protect downstream process equipment (RO membranes, boilers, heat exchangers) by removing hardness (Ca²⁺ & Mg²⁺) via ion-exchange (strong-acid cation resin, Na⁺ form).
Typical installations: large industries, packaged water plants, hotels, hospitals, textile & dyeing, chemical plants and utilities requiring continuous softened water.
Process Flow (text diagram)
Raw feed → Bar screen / coarse strainer → Multimedia (PSF) → Activated Carbon Filter (ACF) → Cartridge Filters (5 μm) → Water Softener (Cation resin, Na⁺ form; multi-vessel in parallel) → Treated Water Tank → Distribution / Feed to RO or process.
Regeneration cycle: Backwash → Brine (NaCl) slow rinse → Fast rinse → Return to Service.
UF can be placed after ACF (recommended for turbid feeds) especially if feed is ETP/STP effluent or surface water. For very high iron, consider iron removal pre-filter.
Up to 300 – 600 mg/L (CaCO₃) (custom design for higher)
Outlet Hardness
< 50 mg/L (adjustable / guaranteed on site test)
Regeneration
Automatic (time / metered) or manual — brine prepared from NaCl
Vessel MOC
FRP / MS Rubber Lined (MSEP) / SS on request
Control
PLC / Timer / Meter-based control with level sensors
Operation Hours
Design default: 20 hours/day (confirm site)
Brand
RRR ENVIRO SYSTEMS
Design Calculations (digit-by-digit)
Given:
Flow Q = 20,000 LPH (litres per hour). Convert to cubic metres per hour: 20,000 ÷ 1,000 = 20.000 m³/hr.
We use conservative service velocity v = 10 m/hr (typical design 8–12 m/hr).
Resin Volume (V)
Formula: V (m³) = Q (m³/hr) ÷ v (m/hr).
Step-by-step:
Q = 20,000 L/hr → 20,000 ÷ 1000 = 20.000 m³/hr
v = 10 m/hr
V = Q ÷ v = 20.000 ÷ 10 = 2.000 m³
V = 2.000 m³ → convert to litres = 2.000 × 1000 = 2,000 L resin
So the total resin volume required ≈ 2.0 m³ (2000 L) for continuous service at 10 m/hr. Exact resin volume can be adjusted depending on desired run length and raw hardness.
Vessel Area & Diameter (single-vessel vs parallel)
Choose practical bed depth H = 0.80 m (800 mm) (typical).
Area A = V ÷ H = 2.000 ÷ 0.8 = 2.5 m².
Convert area to diameter:
4 × A = 4 × 2.5 = 10.0
π ≈ 3.1416
(4×A) ÷ π = 10.0 ÷ 3.1416 ≈ 3.18309886
d = sqrt(3.18309886) ≈ 1.7847 m → ≈ 1785 mm diameter
A single vessel would require ~1.78 m (1785 mm) diameter — large and hard to handle. Best practice: split into multiple vessels in parallel (recommended 4 vessels approach below).
Use 4 vessels in parallel → each vessel resin volume = 2.000 ÷ 4 = 0.500 m³ (500 L) resin per vessel.
For each vessel: A = 0.500 ÷ 0.8 = 0.625 m².
Compute diameter:
4×A = 4 × 0.625 = 2.5
(4×A) ÷ π = 2.5 ÷ 3.1416 ≈ 0.7957747
d = sqrt(0.7957747) ≈ 0.89207 m → ≈ 892 mm diameter
So each vessel ~900 mm diameter × bed depth 0.8 m (vessel height ~1.2–1.5 m including freeboard). This is practical for FRP vessels (~900 mm dia) and allows one-vessel maintenance without shutdown (N+1 redundancy recommended).
Backwash & Regeneration Details
Backwash Flow (per vessel)
Typical backwash velocity vbw = 50 m/hr (design range 40–60 m/hr). For one vessel with area 0.625 m²:
Q_bw = A × v_bw = 0.625 m² × 50 m/hr = 31.25 m³/hr = 31,250 L/hr
Backwash pump should supply ~31.25 m³/hr for each vessel during backwash. Use a suitably sized backwash pump (common practice: centralized backwash or dedicated backwash pumps sized for parallel operations).
Salt (Brine) Requirement & Regeneration
Working salt dose (approx) = 10 kg NaCl per m³ resin (typical working value; varies by resin & hardness).
Total resin = 2.000 m³ → Salt per regeneration = 10 × 2.000 = 20 kg NaCl per regeneration cycle.
Salt/kg per regen = 10 kg/m³ × 2.000 m³ = 20 kg NaCl
Recommend salt storage: 500 kg (10–25 regenerations on-site depending on run length) and brine prep tank ~300–500 L for convenience. Actual salt use depends on raw hardness and chosen regen strength (8–12 kg/m³ typical range).
Regeneration Frequency & Run Length
Regeneration frequency depends on raw hardness (mg/L as CaCO₃) and desired service run length (e.g., 24–72 hours). Provide raw hardness to compute exact run length and salt consumption schedule. We recommend meter-based regeneration for optimal salt usage.
Scope of Supply & Equipment
4 × FRP softener vessels (900 mm dia × suitable height) with multiport valves (automatic or manual)
Strong Acid Cation resin (total ~2.0 m³ / 2000 L)
Brine preparation tank, salt hopper & salt feed arrangement
Raw / treated water pumps (duty + standby) sized for site head
Backwash pump (centralized or per-vessel) & drain piping
Cartridge prefilters, PSF & ACF as required
Control panel (PLC / Timer-based) with level switches and regeneration logic
Installation, commissioning, operator training & O&M manual
Expected Performance & Use Cases
Parameter
Typical Inlet
Expected Outlet
Hardness (as CaCO₃)
100 – 1000 mg/L (site dependent)
< 50 mg/L (after softening)
TSS / Turbidity
Varies
Pre-filtration recommended (<1 NTU to protect resin)
Iron
< 2 mg/L recommended
Must be removed pre-softener otherwise resin fouls
Use
RO feed, boilers, cooling towers, process water
Reduced scaling, longer RO life, less boiler blowdown
Final guarantees provided after site raw water report & jar tests. We include initial site sample analysis in our proposal (free for serious enquiries).
Operation & Maintenance
Periodic backwash & regeneration per control schedule (timer or meter-based).
Monitor inlet iron — pre-treat if Fe > 0.2–0.5 mg/L to avoid resin fouling.
Maintain salt stock and brine strength checks.
Keep spare resin (5–10% by volume) and critical spares: valves, seals, pumps.
Annual resin performance check & periodic resin replacement as per use.
FAQ — 20,000 LPH Water Softener
Q1: What is the salt consumption per regeneration?
Using 10 kg NaCl per m³ resin as working value → total resin 2.0 m³ → salt ≈ 20 kg per regeneration. Actual consumption depends on resin & hardness; range 8–12 kg/m³ is common.
Q2: How often will the softener need regeneration?
Regeneration frequency depends on inlet hardness and demand. Typical schedules vary from daily to every few days. Meter-based control gives optimal salt usage.
Q3: Can this be used as RO pretreatment?
Yes — softeners are commonly used before RO when hardness would cause scaling. For turbid feeds, add UF pre-treatment to protectRO membranes.
Q4: Do you provide installation and AMC?
Yes — we provide supply, installation, commissioning, operator training and AMC packages across India.