Sahawatthanakit (1988) Co., Ltd.
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Sahawatthanakit (1988) Engineering Team

Industrial Water Treatment: Boiler Feedwater, Cooling Water, RO/Process Water, and Wastewater Compliance — Selection + Thai Effluent/ASME/WHO Standards for Plants

Buyer's guide to industrial water treatment: separate boiler feedwater–cooling water–process/RO water–wastewater streams → choose the right treatment process for each stream → worked cycles-of-concentration example → contractor checklist + ASME/ABMA/WHO/Thai DIW/PCD standards for factories in Thailand.

Industrial Water TreatmentBoiler FeedwaterCooling WaterReverse OsmosisROWastewaterWater TreatmentSoftenerIon ExchangeDeaerationAntiscalantLegionellaDIWASMEWHOCooling TowerEffluent StandardsMBRActivated Sludge
Industrial water treatment system with softener tanks, RO membrane skid, and pH control for a factory in Thailand

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สรุป (TL;DR)

Buyer's guide to industrial water treatment: separate boiler feedwater–cooling water–process/RO water–wastewater streams → choose the right treatment process for each stream → worked cycles-of-concentration example → contractor checklist + ASME/ABMA/WHO/Thai DIW/PCD standards for factories in Thailand.

A boiler running at full capacity with scale buildup that has cut efficiency by 30% — plant effluent that keeps failing the BOD test required by the Department of Industrial Works — a cooling tower harbouring Legionella bacteria — an RO membrane that failed in under a year because the feed water was never properly prepared. In nearly every case, these failures are not caused by a "bad machine." The root cause is a water treatment system that was selected for the wrong stream, or designed without covering all four water streams from the outset.

Industrial water in a factory must be managed as four fundamentally different streams: boiler feedwater requiring high purity to prevent scale and corrosion — cooling water requiring control of scaling, biofouling, and Legionella — process and RO water (utility water) to match the purity demands of the production process — and wastewater and effluent that must meet regulatory standards before discharge.

This article focuses on treating these four water streams inside the industrial plant. For a detailed look at cooling tower selection and Legionella risk management specifically, see Cooling Tower Selection and Water Treatment — Legionella. For compressed air quality and ISO 8573 dryer/filter systems, see Compressed Air Quality and ISO 8573 Systems.

1. Why Four Streams Must Be Managed Separately — Wrong Treatment for the Wrong Stream = Wasted Investment

The most common mistake in plant water planning is applying a single system to every use, or focusing exclusively on effluent while neglecting the quality of "incoming" water. Each stream has entirely different requirements and treatment processes.

Stream Primary objective Main problem if untreated Reference standard
Boiler feedwater Prevent scale and corrosion in the boiler CaCO₃ scale reduces efficiency; tube rupture; shortened life ASME / ABMA boiler water guidelines
Cooling water Prevent scaling, corrosion, biofouling, Legionella Blocked heat exchangers; system damage; Legionella risk WHO Legionella guidelines; DIW standards
Process / RO water Purity matched to the production process Product fails spec; membrane degrades prematurely WHO drinking-water quality; TIS/มอก.
Wastewater / effluent pH, BOD, COD, TSS within limits before discharge Violations of DIW/PCD regulations; fines; shutdown DIW (Dept. of Industrial Works); PCD

2. Stream 1 — Boiler Feedwater

Why raw water destroys boilers

Raw water contains Ca²⁺ and Mg²⁺ that deposit as CaCO₃ and CaSO₄ on heat-transfer surfaces. Even 1 mm of scale increases fuel consumption measurably; thick scale causes hot spots that rupture tubes. Dissolved oxygen and CO₂ in the feedwater cause corrosion in economiser pipes and the boiler drum — silently costing thousands of baht in early tube replacement.

Key treatment processes

Process Function When to use
Ion exchange softening Exchanges Ca/Mg → Na, removes hardness Low–medium pressure boilers (general use)
Dealkalization Reduces alkalinity, limits CO₂ in steam Systems with condensate return; corrosion-risk piping
RO / Demineralization Removes nearly all ions; achieves very low TDS High-pressure boilers (> ~600 psig)
Deaeration Removes O₂ and CO₂ with steam heat Every serious boiler system
Oxygen scavenger (chemical) Captures residual O₂ after deaeration Paired with deaerating heater
Condensate polishing Removes rust and contaminants from returned condensate High-pressure / superheated steam systems
Blowdown control Discharges high-TDS water to maintain quality limits All boiler systems

ASME/ABMA boiler water guidelines set increasingly strict limits on TDS, silica (SiO₂), alkalinity, and dissolved oxygen as boiler operating pressure increases. For high-pressure boilers (> ~600 psig), demineralized or RO-quality feedwater is typically required. System designers should reference the specific pressure-range tables in ASME CRTD-Vol.34 or ABMA publications for the actual boiler pressure in use.

Worked example: Blowdown Rate

If TDS in feedwater = 200 mg/L and the maximum allowable TDS in boiler water = 2,000 mg/L → blowdown rate = 200 / (2,000 − 200) × 100 ≈ 11% of steam output. This means approximately 11% of steam-equivalent water must be purged to keep boiler-water TDS from exceeding the limit. The higher the feedwater TDS, the more frequent the blowdown — and the greater the heat and water loss. This is precisely why investing in a softener or RO system pays back through reduced fuel and water costs.

3. Stream 2 — Cooling Water and Cooling Towers

Four risks that must be managed simultaneously

1. Scaling — as water evaporates in the cooling tower, dissolved minerals concentrate. CaCO₃ deposits on heat exchanger surfaces and reduces heat transfer. The tendency to scale is assessed by the Langelier Saturation Index (LSI) or Ryznar Stability Index (RSI): LSI > 0 indicates scaling tendency; LSI < 0 indicates corrosive tendency; a target of −0.5 to +0.5 is typical for most systems. Controlled with antiscalant and COC management.

2. Corrosion — affects copper alloys and mild steel in chiller tubes and piping. Controlled with corrosion inhibitors and pH adjustment to the correct range.

3. Biofouling — algae and slime block nozzles and fill medium, reducing system efficiency. Controlled with oxidising biocides (chlorine, bromine) and non-oxidising biocides rotated to prevent resistance.

4. LegionellaLegionella pneumophila thrives at 25–45°C in warm water with sediment and biofilm, and can cause life-threatening Legionnaires' disease. WHO publishes dedicated risk management guidelines for cooling towers — see also the companion article Cooling Tower Selection and Water Treatment.

Cycles-of-Concentration (COC) — the core metric for cooling water management

COC is the ratio of mineral concentration in the recirculating cooling water to that in the makeup water, measured by Cl⁻, conductivity, or SiO₂:

COC = [concentration in recirculating water] / [concentration in makeup water]

Worked example — COC and makeup water volume:

A 500 RT (refrigeration-ton) cooling tower system with an approximate evaporation rate of 0.75% of circulation flow:

  • Evaporation rate ≈ 500 × 3.5 L/min·RT × 0.0075 ≈ 13 L/min
  • At target COC = 4: Blowdown = Evaporation / (COC − 1) ≈ 13 / (4−1) ≈ 4.3 L/min
  • Makeup water = Evaporation + Blowdown ≈ 13 + 4.3 ≈ 17.3 L/min
  • If COC dropped to 3: Blowdown rises to 6.5 L/min, Makeup = 19.5 L/min → more water consumed

A COC of 3–5 is suitable for most systems. Too high a COC without an inhibitor programme accelerates scaling and Legionella risk. The right COC target must account for the local makeup water quality — which varies significantly across Thailand between surface water, groundwater, and municipal supply.

4. Decision Map: Choosing the Treatment Process for Each Stream

flowchart TD
    A["Identify the water stream
requiring treatment"] --> B{"Which stream?"} B -->|"Boiler feedwater"| C{"Boiler operating
pressure?"} B -->|"Cooling water"| D["Multimedia filter →
Antiscalant + Inhibitor + Biocide
COC + Blowdown control"] B -->|"Process / RO water"| E["Multimedia filter →
Activated carbon →
Softener → RO → UV/Cl₂"] B -->|"Wastewater / effluent"| F{"Nature of
wastewater?"} C -->|"Low–medium pressure
(< ~600 psig)"| G["Softener (ion exchange) +
Deaeration + O₂ scavenger +
Blowdown control"] C -->|"High pressure
(> ~600 psig)"| H["RO / Demineralization +
Deaeration +
Condensate polishing"] F -->|"Abnormal pH,
suspended solids"| I["pH neutralization →
Coagulation/Flocculation →
Clarifier / Sedimentation"] F -->|"Contains oil"| J["Oil interceptor / DAF
(Dissolved Air Flotation)
as first step"] F -->|"High BOD/COD"| K["Biological treatment:
Activated Sludge / MBR / MBBR
→ Sludge dewatering"] D --> L["Legionella risk assessment
per WHO guidelines"] E --> M["Online TDS / conductivity
monitoring"] I --> N["Verify DIW/PCD limits
before discharge"] J --> N K --> N

5. Stream 3 — Process and RO / Utility Water

When does process water require RO or DI quality?

Water quality level Target TDS Example uses Treatment train
Softened water Hardness removed Low-pressure boiler feedwater; general washing Ion exchange softener
Filtered water TSS, chlorine removed General process water; parts washing Multimedia + Activated carbon
RO water < 50–100 mg/L TDS Medium–high pressure boilers; food/pharma process Multimedia → AC → Softener → RO
Deionized (DI) / Ultrapure < 1–10 mg/L TDS Electronics, semiconductor, pharma RO → Mixed bed DI or EDI

Typical RO system sequence

  1. Multimedia filtration — removes suspended solids and turbidity (sand, gravel, anthracite media)
  2. Activated carbon (AC) — adsorbs chlorine, organics, colour, and odour. Critical step: chlorine must be removed before RO membranes because chlorine destroys polyamide membrane
  3. Water softener — reduces Ca/Mg to prevent membrane scaling and fouling
  4. RO membrane — pressure drives permeate through a semi-permeable membrane; ion, bacteria, and endotoxin rejection > 99.5% for quality membranes
  5. Post-treatment — UV disinfection or chlorination for biological safety; pH adjustment as required

Frequently overlooked: RO produces reject water (concentrate) equal to roughly 20–40% of feed. Failing to plan for this stream is a common mistake. Reject can often be directed to non-critical uses (floor washing, landscaping) or blended into the wastewater treatment system. If discharged directly, high-TDS reject may itself require treatment to meet DIW/PCD limits.

6. Stream 4 — Wastewater and Effluent: Thai DIW/PCD Standards and Treatment Processes

Thai industrial effluent standards

The Department of Industrial Works (DIW) and the Pollution Control Department (PCD) jointly regulate industrial effluent in Thailand. Key parameters that must be controlled include:

Parameter Typical target range Notes
pH 5.5 – 9.0 (general) Exact range varies by factory category
BOD (Biochemical Oxygen Demand) Per factory category limit Lower is always better
COD (Chemical Oxygen Demand) Per factory category limit Measures total organic loading
TSS (Total Suspended Solids) Per factory category limit Controlled by sedimentation/filtration
Oil and grease Per factory category limit Removed by DAF or oil separator
Heavy metals (Cr, Pb, Cd, Hg, etc.) Very strict limits Requires precipitation/removal step
Temperature Must not exceed specified limits Protects receiving water ecology

Important notice: The precise numeric limits for each parameter differ by factory category as registered with the Department of Industrial Works (per Notification No. 37/2543 and subsequent amendments). Operators must verify current applicable limits directly with DIW at www.diw.go.th and PCD at www.pcd.go.th — these are updated periodically.

Typical wastewater treatment process train

flowchart LR
    A["Wastewater from
production process"] --> B["Equalization tank
(flow balance + pH
pre-equalisation)"] B --> C{"Contains
oil/grease?"} C -->|"Yes"| D["DAF / Oil separator
(remove oil first)"] C -->|"No"| E["pH neutralization
(adjust to 6–8)"] D --> E E --> F["Coagulation +
Flocculation
(settle SS + colour)"] F --> G["Clarifier /
Sedimentation
(remove settled sludge)"] G --> H{"BOD/COD
elevated?"} H -->|"Yes (food / chemical
processes)"| I["Biological treatment
Activated Sludge / MBR / MBBR
organic degradation"] H -->|"Low or already
compliant"| J["Sand filter /
polishing"] I --> J J --> K["Lab analysis
before discharge"] K --> L["Discharge —
passes DIW/PCD
limits"] G --> M["Sludge thickener +
dewatering
(filter press / centrifuge)"] M --> N["Sludge cake
→ licensed disposal"]

Biological treatment process options

Process Principle Advantages Disadvantages Best suited for
Activated Sludge Aeration tank + secondary clarifier Simpler design; lower capital cost Large footprint; slow startup Medium–large plants with available land
MBR (Membrane Bioreactor) Activated sludge + membrane in lieu of clarifier Higher effluent quality; smaller footprint Higher capital and membrane replacement cost Space-constrained sites; water reuse targets
MBBR (Moving Bed Biofilm Reactor) Floating media carriers for attached biofilm Handles load variability well; easy to scale Requires post-clarification Pre-treatment; hybrid systems

7. Integrating All Four Streams in a Single Plant

flowchart TD
    R["Raw water / municipal supply"] --> S1["Shared pre-treatment:
Multimedia + AC filter"] S1 --> P1["Softener →
Deaerator →
Boiler feedwater"] S1 --> P2["Softener → RO →
Process / utility water
→ production lines"] S1 --> P3["Cooling tower makeup
+ Antiscalant / Biocide
+ COC control"] P1 --> W["Boiler blowdown
→ wastewater system"] P2 --> W P3 --> W W --> WT["Wastewater treatment:
pH neutral → DAF → Clarifier
→ Biological → Polishing"] WT --> D["Discharge (meets DIW/PCD)
or partial reuse"]

8. Checklist to Ask Your Water Treatment Contractor Before Signing

Provide the left column before requesting a quote, and obtain the right column confirmed before signing the contract.

Information to give the contractor What to obtain / confirm
Flow rate of each stream (m³/h or m³/day) Water balance calculation covering all four streams
Current raw water analysis report Design based on actual analysis, not generic regional averages
Boiler operating pressure (psig) or steam generation rate Boiler water quality target per ASME/ABMA for that pressure range
Factory type and DIW registration category Effluent treatment design that verifiably meets DIW/PCD limits for that category
Wastewater characterisation (BOD, COD, oil, pH, flow) Treatability study or pilot test results before full design
Site footprint constraints and budget envelope Bill of materials with specific brand and model specs
Automation and monitoring requirements P&ID draft + monitoring/control philosophy
Long-term maintenance expectations Service contract terms + spare parts lead times

9. What Buyers Most Often Overlook

Raw water analysis before design: a water treatment system designed without a raw water analysis is almost always either undersized or overbuilt. Water quality across Thailand varies significantly — between surface water, groundwater, and municipal supply, and between regions. Minimum analysis: TDS, hardness, pH, alkalinity, iron, manganese, silica, and coliform count.

RO reject water planning: an RO system produces 20–40% reject. "Forgetting" this stream is a surprisingly common mistake. If the reject TDS is very high, it may need additional treatment before it can be discharged legally through the effluent system.

Sludge disposal costs: a wastewater treatment plant continuously generates sludge that must be disposed of legally — usually requiring a licensed hazardous or industrial-waste disposal contractor. Sludge disposal is a significant operating cost that is often omitted from financial evaluations.

Continuous monitoring systems: manual grab-sample lab analysis provides a snapshot in time. Investment in online analysers (pH, conductivity, ORP) and basic SCADA gives early warning of upsets and provides the compliance audit trail that DIW inspectors increasingly expect.

Cross-stream interactions: boiler blowdown, RO reject, and filter backwash all flow to the wastewater system — the wastewater treatment plant must be designed to handle the peak combined flow, not just production-process wastewater alone.

The energy-water nexus: effective boiler and cooling water treatment directly reduces the plant's energy consumption. Less scale on heat exchangers means lower electricity and fuel costs — and this linkage makes water treatment investment straightforward to justify through an energy-saving ROI calculation. This connects directly to ISO 50001 energy management frameworks.

WHO standards for food and pharmaceutical process water: for factories where water contacts the product directly, reference the WHO Guidelines for Drinking-water Quality alongside US EPA guidance and Thai TIS/มอก. standards to ensure coverage of both chemical and microbiological parameters.

Consult the Engineering Team

The correct water treatment system begins with a raw water analysis and a clear definition of each stream's requirements — not equipment selection from a catalogue. Send us the flow rates for each stream, a raw water analysis report (if available), your factory's DIW registration category, and a description of current problems, and the engineering team will help size the system, specify the right process for each stream, and review your contractor's proposal before you sign.

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Frequently Asked Questions

1

Why does boiler feedwater need treatment before entering the boiler?

+
Raw water contains Ca²⁺ and Mg²⁺ that deposit as scale (CaCO₃, CaSO₄) on heat-transfer surfaces, reducing efficiency and creating hot spots that can rupture tubes. Dissolved oxygen and CO₂ cause corrosion in economiser pipes and the boiler drum. Key treatments include ion-exchange softening, RO/demineralization, deaeration (steam-driven O₂/CO₂ removal), oxygen scavengers, condensate polishing, and blowdown control. ASME/ABMA guidelines set increasingly tight limits on TDS, silica, alkalinity, and dissolved oxygen as boiler pressure rises.
2

What are the main problems in cooling tower water, and how are they controlled?

+
There are four main risks: (1) Scaling — CaCO₃ deposits on heat exchanger surfaces, assessed via Langelier Saturation Index (LSI) or Ryznar Stability Index (RSI), controlled with antiscalant; (2) Corrosion — controlled with corrosion inhibitors; (3) Biofouling — algae and slime that block nozzles, controlled with oxidizing and non-oxidizing biocides; (4) Legionella — bacteria that thrive at 25–45°C and cause Legionnaires' disease, controlled with biocide programmes and Cycles-of-Concentration (COC) management per WHO guidelines.
3

What is Cycles-of-Concentration (COC) and how is it calculated?

+
COC is the ratio of mineral concentration in the recirculating cooling water versus the makeup water — the higher the COC, the less makeup water is consumed but the greater the scaling risk. Example: if Cl⁻ in makeup = 50 mg/L and in recirculating water = 200 mg/L → COC = 200/50 = 4, meaning 1 part blowdown is discharged for every 3 parts that evaporate. A typical target for most systems is 3–5 COC, depending on makeup water quality and the antiscalant programme in use.
4

What types of industrial water applications require Reverse Osmosis (RO)?

+
RO is needed when the application requires very low conductivity or deionized water — such as boiler feedwater for medium-to-high-pressure boilers, electronics/PCB rinsing, pharmaceutical or food-grade process water. A typical RO system runs: multimedia filtration → activated carbon (to remove chlorine that destroys polyamide membranes) → softener → RO membrane → UV/disinfection. Key consideration: RO generates reject (concentrate) water of roughly 20–40% of feed — this stream must be planned for, either recycled or routed to the wastewater system.
5

What effluent standards do Thai factories need to comply with?

+
Thai factories must comply with effluent standards set by the Department of Industrial Works (DIW) and the Pollution Control Department (PCD). Key parameters monitored include BOD, COD, TSS, pH (commonly 5.5–9.0), oil and grease, and heavy metals. The exact numeric limits depend on the factory category registered with DIW. Operators must verify current notified limits directly with DIW at diw.go.th or PCD at pcd.go.th, as these are updated periodically.
6

What is the difference between activated sludge, MBR, and MBBR in industrial wastewater treatment?

+
All three are biological treatment processes: Activated Sludge (AS) is the traditional approach using an aeration tank followed by a clarifier — straightforward but land-intensive. MBR (Membrane Bioreactor) replaces the clarifier with a membrane filter, producing higher-quality effluent in a smaller footprint but at higher capital and membrane-replacement cost. MBBR (Moving Bed Biofilm Reactor) uses floating plastic media that carry a biofilm, handling load variations well and scaling easily — often used as pre-treatment or in hybrid configurations with AS.
7

What is deaeration in a boiler feedwater system and why is it necessary?

+
Deaeration is the removal of dissolved oxygen (O₂) and carbon dioxide (CO₂) from feedwater before it enters the boiler. These gases cause severe corrosion of economiser tubes, boiler drums, and condensate return lines. A deaerating heater sprays water as a fine mist through live steam, driving out dissolved gases by Henry's Law. An oxygen scavenger chemical (sodium sulfite or hydrazine equivalent) is added downstream to capture any residual O₂. Deaeration is non-negotiable for medium- and high-pressure boiler systems.
8

Which wastewater treatment system is suitable for an SME factory in Thailand?

+
An SME with low-to-moderate wastewater volumes and simple chemistry typically uses a pH neutralization + coagulation/flocculation + clarifier/sedimentation train as the core. If the process generates high BOD/COD (e.g., food processing), an extended-aeration activated sludge system is the most maintenance-friendly addition. Factories with oily wastewater must include a DAF (Dissolved Air Flotation) unit or oil interceptor first. System size and treatment method should be designed from actual flow measurements and a waste characterisation study — not from generic rules of thumb.
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