Municipal waterworks
On-site disinfectant generation for a defined drinking-water treatment and distribution duty.
Confirm maximum water flow, required dose, contact conditions and residual-control basis.
Product overview
A product-level view of the on-site generation duty, brine electrolysis process and KSCI model range.
The KUOSI sodium hypochlorite generator prepares disinfectant on site from softened water, refined salt and electricity. The process avoids routine dependence on transporting and storing concentrated finished sodium hypochlorite for the selected disinfection duty.
Tap water is softened before part of the stream is used to dissolve salt and prepare brine. The brine is diluted and metered to the electrolyzer, where the electrochemical reaction produces a low-concentration sodium hypochlorite solution. The generated solution is collected in a storage tank and dosed to the defined treatment point.
The KSCI series includes 16 models with available-chlorine output from 50 to 50,000 g/h. Final selection still requires the maximum treated-water flow, required dose, water quality, operating schedule, redundancy, site utilities and the approved project data sheet.
The UK Drinking Water Inspectorate chlorine-disinfection guide independently explains on-site sodium hypochlorite generation by brine electrolysis, including its principal equipment train, dosing control and hydrogen-ventilation requirement.
Reduces calcium and magnesium before water enters brine preparation and the electrolysis train.
Dissolves refined salt and supplies the selected brine concentration to the metering stage.
Combines brine and softened water at the required feed condition before electrolysis.
Uses the electrolyzer and rectifier to produce sodium hypochlorite solution from the prepared brine.
Collects generated solution and routes hydrogen through the designed ventilation and monitoring arrangement.
Transfers solution to the treatment point and provides the required acid-cleaning connection for the electrolyzer.
Engineering advantages
Evaluate the equipment through operating implications, not decorative feature claims.
Generates low-concentration sodium hypochlorite at the treatment site from refined salt, water and electricity.
Salt consumption is below 3.2 kg and power consumption is below 4.0 kWh per kilogram of available chlorine under the defined operating basis.
An integrated modular design simplifies equipment installation and maintenance.
Central control provides monitoring and operating functions for the generation system.
The generated available-chlorine concentration is 6,000-9,000 ppm, equivalent to 0.6-0.9%.
The KSCI model range covers available-chlorine output from 50 g/h to 50,000 g/h across integrated and multi-unit configurations.
Applications
Water quality, dose demand, residual target and site requirements must be confirmed before selecting the system for these duties.
On-site disinfectant generation for a defined drinking-water treatment and distribution duty.
Confirm maximum water flow, required dose, contact conditions and residual-control basis.
Disinfectant supply for final municipal or industrial wastewater disinfection.
View containerized wastewater treatmentProvide effluent quality, peak flow, dose demand and discharge or reuse requirements.
Sodium hypochlorite generation for a selected reuse-water disinfection step.
Confirm reuse standard, contact time, residual target and downstream compatibility.
Disinfection support for water and sanitation duties defined by the facility process.
Separate process-water, surface-sanitation and wastewater duties and confirm the applicable hygiene standard.
On-site oxidant or disinfectant supply for a project-specific water-treatment duty.
Review chemical compatibility, demand variability, ventilation and hazardous-area requirements.
Disinfection of circulating-cooling-water or other selected plant water systems.
View power plant cooling-water projectProvide circulation flow, make-up water, biological-control target and operating schedule.
Controlled sodium hypochlorite supply for a defined cooling-water microbiological-control duty.
Confirm continuous or shock dosing, residual monitoring and materials compatibility.
Disinfection support for a defined water or wastewater treatment system.
Confirm the regulated duty, water quality, required residual and site safety controls.
Performance
The table presents process indicators. They are technical references, not guaranteed project performance.
| Parameter | Value / range | Engineering note |
|---|---|---|
| Available-chlorine output | 50-50,000 g/h | Range across the 16 KSCI models; select from the calculated maximum hourly requirement. |
| Dilute brine concentration | 3% reference | Final preparation and control arrangement must follow the approved system design. |
| Generated solution concentration | 6,000-9,000 ppm (0.6-0.9%) | Verify the project operating basis and measurement method for this available-chlorine concentration. |
| Salt consumption | <3.2 kg/kg available chlorine | This technical indicator depends on the defined operating basis and approved salt quality. |
| Power consumption | <4.0 kWh/kg available chlorine | This technical indicator covers generation; total system energy depends on the final auxiliary-equipment scope. |
| Current efficiency | >78% | The defined operating conditions and approved equipment configuration apply. |
| Electrode material | Titanium with mixed rare-metal oxide anode coating | Confirm the selected cell and coating specification in the approved data sheet. |
| Control arrangement | Central automatic control with monitoring | Larger systems can support central control and remote monitoring; final PLC, HMI and communication scope is project-specific. |
Working principle
The sequence runs from water softening and brine preparation through electrolysis, storage, hydrogen ventilation and controlled dosing.

This approved diagram shows the process arrangement. Final equipment interfaces and instrumentation depend on the project scope.
Tap water passes through the water softener before entering the generation process.
A portion of softened water dissolves refined salt to prepare the brine supply.
Brine and softened water are combined at the selected feed condition and transferred to the electrolyzer.
Direct current drives the electrochemical reaction that forms sodium hypochlorite solution and hydrogen.
Generated solution enters the storage tank while hydrogen is routed through the designed exhaust system.
A dosing pump transfers sodium hypochlorite solution to the defined treatment point under the selected control strategy.
Equipment video
View the GL Environment introduction to a sodium hypochlorite generator and connect the equipment shown with the on-site generation process described on this page. The video is useful for understanding the packaged system and its role within a disinfection train. It is not presented as proof of a specific plant result. Generator capacity, available-chlorine concentration, salt and water demand, dosing duty and safety provisions require confirmation for the selected project conditions.
System configuration
The generation duty combines softened-water supply, salt dissolution, brine preparation, rectification and electrolysis, solution storage, hydrogen management, dosing, cleaning and control.

Final interfaces and included equipment are defined by the agreed project scope.
Calculate the maximum hourly available-chlorine requirement from treated-water flow and the approved dose basis.
Confirm water source, pressure, hardness, temperature and the required softening or pretreatment duty.
Confirm refined-salt quality, delivery, storage capacity and the selected salt-dissolving arrangement.
Define operating hours, peak duty, turndown, redundancy and the required storage autonomy.
Define dosing points, pump duty, residual measurement, flow pacing and plant interlocks.
Provide the required ventilation route, detection, alarms and installation-area safety controls.
Confirm voltage, frequency, PLC/HMI, communications, remote monitoring and plant-control interfaces.
The incoming water supply enters the softening stage.
The softener prepares water for brine dilution and the electrolysis train.
Refined salt and softened water prepare the brine feed.
The rectifier and electrolyzer convert prepared brine into sodium hypochlorite solution.
The storage tank receives generated sodium hypochlorite before dosing.
The ventilation and monitoring arrangement routes hydrogen away from the system.
The dosing pump supplies the selected treatment point under the approved control logic.
The cleaning circuit supports the approved electrolyzer maintenance procedure.
Main equipment
Supporting / optional equipment
Technical data
The range covers 16 KSCI models in small integrated and larger multi-unit configurations. Values are technical references rather than guaranteed project performance; confirm model nomenclature, supply voltage and frequency, auxiliary-equipment power, materials and final dimensions in the approved project data sheet.
Scroll horizontally to review all technical fields on smaller screens.
| Model | Electrolysis configuration | Available chlorine | Water consumption | Salt consumption | AC power | L × W × H |
|---|---|---|---|---|---|---|
| KSCI-50 | Integrated except salt tank | 50 g/h | 0.15 m³/d | 4.2 kg/d | 0.3 kW | 1225 × 700 × 2015 mm |
| KSCI-100 | Integrated except salt tank | 100 g/h | 0.3 m³/d | 8.4 kg/d | 0.6 kW | 1225 × 700 × 2015 mm |
| KSCI-200 | Integrated except salt tank | 200 g/h | 0.6 m³/d | 16.8 kg/d | 1.2 kW | 1225 × 700 × 2015 mm |
| KSCI-300 | Integrated except salt tank | 300 g/h | 0.9 m³/d | 25.2 kg/d | 1.8 kW | 1225 × 700 × 2015 mm |
| KSCI-400 | Integrated except salt tank | 400 g/h | 1.2 m³/d | 33.6 kg/d | 2.4 kW | 1225 × 700 × 2015 mm |
| KSCI-500 | Integrated except salt tank | 500 g/h | 1.5 m³/d | 42 kg/d | 3.0 kW | 1225 × 700 × 2015 mm |
| KSCI-1000 | 2 × 500 g/h | 1,000 g/h | 3 m³/d | 84 kg/d | 4.7 kW | 1225 × 700 × 2015 mm |
| KSCI-2000 | 2 × 1,000 g/h | 2,000 g/h | 6 m³/d | 168 kg/d | 9.4 kW | 2650 × 1000 × 1930 mm |
| KSCI-3000 | 2 × 1,500 g/h | 3,000 g/h | 9 m³/d | 252 kg/d | 14.1 kW | 2650 × 1000 × 1930 mm |
| KSCI-5000 | 2 × 2,500 g/h | 5,000 g/h | 15 m³/d | 420 kg/d | 23.5 kW | 2650 × 1000 × 1930 mm |
| KSCI-6000 | 2 × 3,000 g/h | 6,000 g/h | 18 m³/d | 504 kg/d | 28.2 kW | 2650 × 1000 × 1930 mm |
| KSCI-10000 | 2 × 5,000 g/h | 10,000 g/h | 30 m³/d | 840 kg/d | 47 kW | 2650 × 1000 × 1930 mm |
| KSCI-15000 | 2 × 7,500 g/h | 15,000 g/h | 45 m³/d | 1,246 kg/d | 70.5 kW | 3174 × 1000 × 2200 mm |
| KSCI-20000 | 2 × 10,000 g/h | 20,000 g/h | 60 m³/d | 1,680 kg/d | 94 kW | 3174 × 1000 × 2200 mm |
| KSCI-30000 | 3 × 10,000 g/h | 30,000 g/h | 90 m³/d | 2,520 kg/d | 141 kW | 3174 × 1000 × 2200 mm |
| KSCI-50000 | 4 × 12,500 g/h | 50,000 g/h | 150 m³/d | 4,200 kg/d | 235 kW | 3800 × 1400 × 3500 mm |
Equipment selection
Selection begins with maximum treated-water flow and the approved available-chlorine dose, then accounts for operating schedule, redundancy, water quality, dosing and site conditions.
Provide the maximum hourly flow for each dosing point and the expected daily operating profile.
Define the normal and peak dose basis in g/m³ or mg/L from verified water-quality and disinfection requirements.
Calculate the maximum hourly requirement from treated-water flow multiplied by the approved available-chlorine dose.
Provide inlet-water pressure, hardness, temperature and the proposed refined-salt specification.
Confirm operating hours, peak periods, standby philosophy and required solution-storage autonomy.
Identify dosing points, residual targets, flow signals, analyser signals and required control interlocks.
Confirm footprint, ventilation route, drainage, ambient conditions, electrical supply, access and hazardous-area requirements.
Manufacturing & installation evidence
These approved images show sodium hypochlorite generator equipment and installation contexts. They are not presented as quantified customer case studies.
Registered sodium hypochlorite generator media showing equipment-room, tank and pump-system installation contexts.



Engineering support
Support is presented as a practical engineering workflow, without unverified company statistics or outcome claims.
Review flow, dose, residual, water quality and operating conditions before equipment selection.
Calculate the required available-chlorine output and evaluate the appropriate KSCI model and redundancy arrangement.
Define water softening, salt dissolution, storage, dosing, hydrogen ventilation, cleaning and control interfaces.
Prepare the applicable equipment data, process information and installation requirements for the agreed scope.
Provide the applicable installation, startup, dosing-control and maintenance guidance for the approved system.
Technical FAQ
The answers separate general selection logic from the values that require a project-specific technical review.
The system softens water, dissolves refined salt, prepares dilute brine and meters it to an electrolyzer. Direct current produces a low-concentration sodium hypochlorite solution, which is stored and dosed to the selected treatment point while hydrogen is routed through the designed ventilation system.
The 16 KSCI models provide available-chlorine output from 50 g/h to 50,000 g/h. Final selection requires the maximum treated-water flow, approved dose, operating schedule, redundancy and site conditions.
The available-chlorine concentration reference is 6,000-9,000 ppm, equivalent to approximately 0.6-0.9%. Confirm the project operating basis and measurement method in the approved data sheet.
Reference consumption is below 3.2 kg of salt and below 4.0 kWh of power per kilogram of available chlorine. Total project consumption depends on the selected model, water conditions and auxiliary-equipment scope.
Multiply maximum treated-water flow by the available-chlorine dose to determine the required hourly output. Dose demand, operating hours, redundancy and storage autonomy must also be confirmed.
A typical system can include water softening, soft-water storage, salt dissolution, brine metering, rectification and electrolysis, sodium hypochlorite storage, dosing, hydrogen ventilation and detection, acid cleaning and PLC controls. The final scope is project-specific.
Hydrogen produced during generation is routed through a designed ventilation system. Hydrogen detection, alarms and other safeguards are defined as part of the agreed system and installation scope. The ventilation route, detection arrangement, controls and site safety requirements must be confirmed for the specific project and approved design.
Applications include municipal waterworks, wastewater treatment, reclaimed-water systems, food processing, chemical processing, power generation, circulating-cooling-water systems and healthcare facilities. Suitability and dose must be confirmed for the actual water and regulatory duty.
Provide water source, average and peak flow, required dose and residual, inlet-water conditions, salt quality, operating schedule, dosing points, electrical supply, control interfaces, installation space, drainage and ventilation requirements.
Engineering inquiry
Share your water source, maximum flow, chlorine dose, residual target, operating schedule, inlet-water conditions and site requirements. KUOSI can use the available data to evaluate the appropriate generator duty and system configuration.