120m³/h UF Pretreatment System for SWRO Plant



Seawater Desalination Project · Oman

120m³/h UF Pretreatment System for SWRO Plant

A corrosion-resistant ultrafiltration solution designed to deliver stable low-turbidity, low-SDI feedwater and protect the downstream seawater reverse osmosis system.

SWRO PretreatmentPVDF Hollow-Fiber MembranesAutomatic PLC Operation
120 m³/hNet UF capacity
92%–95%Design recovery
≤0.1 NTUTarget turbidity
≤2.5Target SDI₁₅

Project Overview

Coastal Desalination Plant

A coastal desalination plant in Oman required reliable pretreatment for an SWRO system supplying local industrial and municipal applications.

The raw seawater contained suspended solids, marine colloids, algae and microorganisms. Without effective pretreatment, these contaminants could increase membrane fouling, cleaning frequency and operating costs.

Zhongnuo supplied a 120m³/h seawater ultrafiltration system to stabilize feedwater quality before desalination.

Item Project Details
Location Oman, Middle East
Application SWRO pretreatment
Raw water Coastal seawater
UF membrane Fouling-resistant PVDF
Piping SS316L, corrosion controlled
Cleaning Backwash + CEB + CIP
Control Automatic PLC

Actual recovery and outlet quality depend on seawater conditions, membrane flux and cleaning requirements.

Customer Challenges

Operating Conditions
01

Variable Seawater Quality

Seasonal changes affected turbidity and biological activity.

02

Unstable SWRO Feed SDI

Conventional pretreatment could not maintain consistent feed quality.

03

Membrane Fouling

Solids, colloids and microorganisms increased SWRO cleaning demand.

04

Coastal Corrosion

High salinity and salt fog required corrosion-resistant materials.

05

Continuous Demand

The desalination plant required uninterrupted pretreatment-water supply.

06

Backwash Water Loss

High recovery was needed to reduce seawater intake and waste.

Customized UF Solution

Designed for Seawater

The system uses high-fouling-resistance PVDF hollow-fiber membranes for solids-rich and biologically active seawater. Automatic backwashing removes accumulated particles, CEB controls organic and biological fouling, and periodic CIP restores membrane performance when required.

Multiple UF trains operate in parallel with staggered backwash cycles, allowing the plant to maintain net output while individual trains are cleaned.

Recovery reference: At 93% recovery, approximately 129 m³/h of feedwater is required to produce 120 m³/h of UF filtrate.
PVDF UF MembranesSelected for fouling resistance and stable filtration.
Parallel Membrane TrainsStaggered cleaning supports continuous supply.
Backwash + CEBControls particulate, organic and biological fouling.
Independent CIPRestores performance based on operating data.
SS316L PipingImproved resistance in coastal salt-fog conditions.
Automatic PLC ControlManages filtration, cleaning, alarms and protection.

Treatment Process

UF + SWRO Integration
Seawater Intake
Screening
Coagulation, If Required
Self-Cleaning Filter
Ultrafiltration System
UF Water Tank
Cartridge Filter & HP Pump
SWRO System

UF removes suspended solids, colloids, algae and microorganisms. It does not remove dissolved salts; desalination is completed by the downstream SWRO membranes.

Project Results

Performance Under Design Conditions

Stable Filtrate Quality

UF turbidity controlled at ≤0.1 NTU.

Low-SDI SWRO Feed

SDI₁₅ controlled at ≤2.5.

Effective Solids Removal

Suspended solids and marine colloids significantly reduced.

Reduced Fouling Pressure

More stable feedwater protected downstream SWRO membranes.

Continuous Filtration

Staggered backwashing maintained automatic production.

Coastal-Site Suitability

Corrosion-control design improved environmental adaptability.

Project Highlights

Reliable SWRO Protection
Dedicated SWRO PretreatmentDesigned around coastal seawater conditions.
92%–95% RecoveryReduced intake demand and backwash-water loss.
Fouling-Resistant PVDFSupports challenging biological feedwater.
Three-Level CleaningAutomatic backwash, CEB and CIP.
Corrosion-Resistant DesignSS316L piping for selected seawater service.
Automatic OperationPLC-managed filtration, cleaning and protection.

Planning an SWRO Pretreatment Project?

Send your seawater analysis, required capacity and SWRO feedwater target for a customized proposal.

Request a Proposal

Seawater Desalination Project · Oman

120m³/h UF Pretreatment System for SWRO Plant

A corrosion-resistant ultrafiltration solution designed to deliver stable low-turbidity, low-SDI feedwater and protect the downstream seawater reverse osmosis system.

SWRO PretreatmentPVDF Hollow-Fiber MembranesAutomatic PLC Operation
120 m³/hNet UF capacity
92%–95%Design recovery
≤0.1 NTUTarget turbidity
≤2.5Target SDI₁₅

Project Overview

Coastal Desalination Plant

A coastal desalination plant in Oman required reliable pretreatment for an SWRO system supplying local industrial and municipal applications.

The raw seawater contained suspended solids, marine colloids, algae and microorganisms. Without effective pretreatment, these contaminants could increase membrane fouling, cleaning frequency and operating costs.

Zhongnuo supplied a 120m³/h seawater ultrafiltration system to stabilize feedwater quality before desalination.

Item Project Details
Location Oman, Middle East
Application SWRO pretreatment
Raw water Coastal seawater
UF membrane Fouling-resistant PVDF
Piping SS316L, corrosion controlled
Cleaning Backwash + CEB + CIP
Control Automatic PLC

Actual recovery and outlet quality depend on seawater conditions, membrane flux and cleaning requirements.

Customer Challenges

Operating Conditions
01

Variable Seawater Quality

Seasonal changes affected turbidity and biological activity.

02

Unstable SWRO Feed SDI

Conventional pretreatment could not maintain consistent feed quality.

03

Membrane Fouling

Solids, colloids and microorganisms increased SWRO cleaning demand.

04

Coastal Corrosion

High salinity and salt fog required corrosion-resistant materials.

05

Continuous Demand

The desalination plant required uninterrupted pretreatment-water supply.

06

Backwash Water Loss

High recovery was needed to reduce seawater intake and waste.

Customized UF Solution

Designed for Seawater

The system uses high-fouling-resistance PVDF hollow-fiber membranes for solids-rich and biologically active seawater. Automatic backwashing removes accumulated particles, CEB controls organic and biological fouling, and periodic CIP restores membrane performance when required.

Multiple UF trains operate in parallel with staggered backwash cycles, allowing the plant to maintain net output while individual trains are cleaned.

Recovery reference: At 93% recovery, approximately 129 m³/h of feedwater is required to produce 120 m³/h of UF filtrate.
PVDF UF MembranesSelected for fouling resistance and stable filtration.
Parallel Membrane TrainsStaggered cleaning supports continuous supply.
Backwash + CEBControls particulate, organic and biological fouling.
Independent CIPRestores performance based on operating data.
SS316L PipingImproved resistance in coastal salt-fog conditions.
Automatic PLC ControlManages filtration, cleaning, alarms and protection.

Treatment Process

UF + SWRO Integration
Seawater Intake
Screening
Coagulation, If Required
Self-Cleaning Filter
Ultrafiltration System
UF Water Tank
Cartridge Filter & HP Pump
SWRO System

UF removes suspended solids, colloids, algae and microorganisms. It does not remove dissolved salts; desalination is completed by the downstream SWRO membranes.

Project Results

Performance Under Design Conditions

Stable Filtrate Quality

UF turbidity controlled at ≤0.1 NTU.

Low-SDI SWRO Feed

SDI₁₅ controlled at ≤2.5.

Effective Solids Removal

Suspended solids and marine colloids significantly reduced.

Reduced Fouling Pressure

More stable feedwater protected downstream SWRO membranes.

Continuous Filtration

Staggered backwashing maintained automatic production.

Coastal-Site Suitability

Corrosion-control design improved environmental adaptability.

Project Highlights

Reliable SWRO Protection
Dedicated SWRO PretreatmentDesigned around coastal seawater conditions.
92%–95% RecoveryReduced intake demand and backwash-water loss.
Fouling-Resistant PVDFSupports challenging biological feedwater.
Three-Level CleaningAutomatic backwash, CEB and CIP.
Corrosion-Resistant DesignSS316L piping for selected seawater service.
Automatic OperationPLC-managed filtration, cleaning and protection.

Planning an SWRO Pretreatment Project?

Send your seawater analysis, required capacity and SWRO feedwater target for a customized proposal.

Request a Proposal

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