WTP-Pro v2
Water Treatment Plant — Complete Engineering Calculator
RO System Clarifier DM Plant Boiler Feed Drinking SI + Imperial
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ASME CRTD-34 · IS 10500 · IS 10392 · WHO 2022

Water Treatment Plant
Engineering Calculator

The complete engineering reference for water treatment plant design and operations. All major calculation modules covering RO membranes, gravity clarification, ion exchange demineralization, boiler feed water chemistry, potable water treatment, and chemical dosing — with correct ASME, IS, WHO and ABMA standards built-in.

🌊
Raw Water
River, bore-well, sea, municipal
🟤
Clarifier
Coagulation, settling, sludge
🔲
DMF/ACF
Dual media, carbon filtration
🔵
RO Unit
Membranes, recovery, rejection
🟢
DM Plant
Cation, anion, mixed bed
🔥
Boiler
Steam generation, blowdown
Module 01
RO System Design
Recovery · Flux · TDS rejection · Salt passage · LSI · Osmotic pressure · Membrane sizing · SEC · SDI assessment
Module 02
Clarifier Design
SOR · Detention time · Weir loading · Tank dims · Sludge volume · Coagulant dose · G-value · Upflow velocity
Module 03
DM Plant
Resin volume · Exchange capacity · HCl/NaOH regen · Cycle length · Conductivity · Silica leakage · Degasser
Module 04
Boiler Feed Water
COC · Blowdown · Makeup flow · O₂ scavenger · Scale limits (ASME/IS/ABMA) · Silica carryover · Steam purity · Heat loss
Module 05
Drinking Water
Cl₂ residual · CT value · Giardia log removal · Filtration area · IS 10500 compliance · LSI · RSI corrosion index
Module 06
Chemical Dosing
Pump sizing · Tank volume · 3-chemical system · Safety factor · Daily consumption · Stock solution
🔵
RO System DesignRecovery, flux, TDS rejection, LSI, membrane sizing
📥 Feed Water
m³/hr
mg/L
bar
°C
SDI
µS/cm
⚙ System Design
%
%
L/m²/h
stages
m²/elem
elem
🔬 Water Chemistry (LSI)
pH
mg/L
mg/L
🔵

RO Results

Fill parameters and calculate

Computing RO system…

🟤
Clarifier DesignSOR, detention time, weir loading, tank sizing
💧 Flow & Raw Water
m³/hr
NTU
NTU
mg/L
°C
pH
🏗 Design Parameters
m/hr
hr
m³/m/d
mL/g
mg/L
🧪 Coagulation
mg/L
🟤

Clarifier Results

Fill design parameters and calculate

Sizing clarifier…

🟢
DM Plant DesignIon exchange, resin sizing, regeneration chemicals
💧 Feed Water Ion Analysis
m³/hr
mg/L
mg/L
mg/L
mg/L
mg/L
⚗ Resin & Column Design
eq/L
eq/L
hr
m/hr
m
🧪 Regeneration Design
% w/w
% w/w
g/eq
g/eq
🎯 Quality Targets
µS/cm
mg/L
🟢

DM Plant Results

Fill parameters and calculate

Computing DM design…

🔥
Boiler Feed Water QualityASME CRTD-34 · IS 10392 · ABMA — Complete analysis
🔥 Boiler Operating Conditions
t/hr
bar(g)
%
nos.
🌡 Makeup Water Quality (Feed to Boiler)
mg/L
mg/L
mg/L
mg/L
mg/L
mg/L
mg/L
mg/L
mg/L
mg/L
💊 Chemical Treatment
%
pH
mg/L
⚡ Limits Selection
mg/L
🔥

Boiler Feed Results

Enter all operating parameters then calculate

Running boiler analysis…

🚰
Drinking Water TreatmentChlorination, filtration, IS 10500 compliance
💧 Raw Water Quality
m³/hr
NTU
mg/L
pH
mg/L
MPN
mg/L
mg/L
⚗ Treatment Design
mg/L
mg/L
mg/L
min
m/hr
nos.
m
°C
🚰

Drinking Water Results

Fill parameters and calculate

Checking compliance…

🧪
Chemical Dosing SystemPump sizing, tank volume, daily consumption
💧 Process Flow
m³/hr
hr/d
days
×
🧪 Chemical 1 — Coagulant/Antiscalant
mg/L
% w/v
kg/L
🧪 Chemical 2 — pH Adjustment
mg/L
% w/v
kg/L
🧪 Chemical 3 — Disinfectant (NaOCl/Cl₂)
mg/L
% w/v
kg/L
🧪

Chemical Dosing Results

Fill parameters and calculate

Sizing dosing system…

📋
Boiler Feed Water — ASME CRTD-34 StandardsIndustrial Watertube, High Duty, Drum Type — Official limits by drum pressure
📌 Source
ASME Consensus on Operating Practices for the Control of Feedwater & Boiler Water Chemistry in Modern Industrial Boilers (CRTD Vol. 34). These are the globally recognised standard for watertube boilers. For fire tube boilers, limits may be relaxed by 20-30% at equivalent pressures.
🔥 Drum-type Boiler Water Quality Limits (ASME CRTD-34 / ABMA)
Parameter 0–300 psig (0–21 bar) 301–450 psig (21–32 bar) 451–600 psig (32–41 bar) 601–750 psig (41–52 bar) 751–900 psig (52–62 bar) 901–1000 psig (62–69 bar) 1001–1500 psig (69–103 bar) 1501–2000 psig (103–138 bar) OTSG / >2000 psig
Boiler Water TDS max (mg/L)700–3500600–3000500–2500200–1000150–750125–625100500.05
Conductivity max (µS/cm)1100–5400900–4600800–3800300–1500200–1200200–1000150800.15–0.25
Total Alkalinity max (mg/L)700600500400300200NSNSNS
Silica max (mg/L SiO₂)150904030208210.02
Suspended Solids max (mg/L)151083211NSNS
Steam Purity (TDS max, mg/L)0.2–1.00.2–1.00.2–1.00.1–0.50.1–0.50.1–0.50.10.050.05
Boiler Water pH10.5–12.010.5–11.810.0–11.810.0–11.59.8–11.09.6–10.89.0–10.08.5–9.5VAM
📋 Feedwater Quality Limits (ASME CRTD-34) — Water entering boiler
Feedwater Parameter 0–300 psig 301–600 psig 601–1000 psig 1001–1500 psig 1501–2000 psig Notes
Iron, Fe (µg/L)1005025105As total iron
Copper, Cu (µg/L)502520103As total copper
Total Hardness (µg/L)≈0 (trace)NDNDNDNDAs CaCO₃ equivalent
pH at 25°C7.5–107.5–108.0–9.58.5–9.59.0–9.5Adjusted for corrosion control
Dissolved O₂ (µg/L)≤7000 (7 ppm)≤1000≤100≤20≤7After deaerator
Silica, SiO₂ (mg/L)≤150≤40≤10≤2≤1For turbine protection
TOC (mg/L)<10<5<3<1<0.5Non-volatile organic carbon
Oil/Grease (mg/L)<1.0<0.5<0.5<0.1<0.05Causes foam/carryover
⚠ Critical Notes
  • NS = Not Specified; ND = Not Detectable; VAM = Use only Volatile Alkaline Materials
  • For boilers with superheaters or turbine drives, apply values for at least the next higher pressure range
  • With local heat fluxes >150 kW/m², use values for the next higher pressure range
  • Alkalinity values >10% of conductance value may cause foaming and carryover
  • If makeup is DM quality, conductivity for <1000 psig may use the 1000–1500 psig table values
  • Silica carryover to turbine blades becomes critical above 600 psig — strictly control boiler silica
  • OTSG (Once-Through Steam Generators) have essentially zero tolerance for impurities
🇮🇳
IS 10392 — Boiler WaterBureau of Indian Standards
Parameter<20 bar20–60 bar>60 bar
pH8.5–9.08.8–9.29.0–9.5
Hardness (ppm)≤5≤1Nil
TDS (mg/L)≤3500≤2000≤500
Silica (mg/L)≤25≤10≤2
Dissolved O₂≤0.1≤0.02Nil
Conductivity (µS/cm)≤6000≤4000≤2000
Total Alkalinity≤700≤500≤300
Chlorides (mg/L)≤150≤75≤30
Iron (mg/L)≤2≤0.5≤0.1
🚰
IS 10500:2012 — Drinking WaterBIS Standard
ParameterAcceptableMax Perm.
pH6.5–8.5No relaxation
TDS (mg/L)≤5002000
Turbidity (NTU)≤15
Hardness (mg/L)≤200600
Chloride (mg/L)≤2501000
Fluoride (mg/L)≤1.01.5
Iron (mg/L)≤0.3
Nitrate (mg/L)≤45
Residual Cl₂0.2–1.0
Coliform/100mLNil
🟢
DM Water StandardsIon exchange product quality
ParameterDM (Two-bed)Mixed Bed
Conductivity<10 µS/cm<0.1 µS/cm
Silica (SiO₂)<0.1 mg/L<0.02 mg/L
pH6.8–7.27.0±0.1
TDS (mg/L)<5<0.1
HardnessNilNil
Sodium (Na)<0.1 ppm<0.01 ppm
Resistivity>0.1 MΩ·cm>10 MΩ·cm
🔵
RO Design Criteria & Key FormulasQuick engineering reference
🔵 RO Design Ranges
  • Brackish recovery: 70–80%
  • Seawater recovery: 35–50%
  • Flux (brackish): 14–20 L/m²/h
  • Flux (seawater): 10–14 L/m²/h
  • SDI feed limit: ≤5, ideal <3
  • Salt rejection: 96–99.8%
  • LSI concentrate: <+1.0 (scaling)
🟤 Clarifier Design
  • SOR: 0.8–2.0 m/hr (gravity)
  • Detention time: 2–4 hours
  • Weir loading: 125–250 m³/m/day
  • Flocculation G: 20–60 /s
  • Rapid mix G: 600–1000 /s
  • Inclined plate SOR: 5–8× plain
🟢 DM Plant Design
  • Service velocity: 10–20 m/hr
  • Cation capacity: 1.7–2.1 eq/L
  • Anion capacity: 1.0–1.4 eq/L
  • HCl dose: 90–110 g/eq resin
  • NaOH dose: 100–130 g/eq
  • Regen freq: <2/day ideal
🔣 Key Formulas
/* RO */
Recovery R = Qp/Qf × 100
TDS_perm = TDS_feed × (1-rej)
TDS_conc = (TDS_f×Qf - TDS_p×Qp)/Qc
CF = 1/(1-R)
SEC = P×Qf/(3600×0.75×Qp) kWh/m³
/* LSI */
LSI = pH - pHs
pHs = pK2-pKs+p[Ca]+p[Alk]
/* Clarifier */
SOR = Q/A (m/hr)
Area = Q/SOR (m²)
Volume = Q × HRT (m³)
Weir = Q_daily/WLR (m)
/* DM Plant */
Resin Vol = Flow×Cycle×Load/Cap
HCl L/regen = eq×dose/(Conc×density)
Cycle hr = (Vol×Cap)/(Load×Flow×1000)
/* Boiler Feed Water */
COC = TDS_boiler / TDS_makeup
BD% = 1/(COC-1) × 100
BD_flow = Steam × BD%/100
Makeup = Steam × (1-CR + BD%/100)
Silica_boiler = Si_feed × COC
/* Heat loss */
Q_BD = BD_flow × h_f (kW)