Automatic Backwash Filtration

Self Cleaning Filters for Continuous Industrial Water Treatment

Our self cleaning filter units are designed to maintain downstream flow during normal automatic cleaning — no system shutdowns, no replacement cartridges, and no operator required. Each automatic backwash filter maintains inline mechanical straining at your specified micron rating while the automated cleaning cycle removes accumulated solids and routes them to drain. Applications requiring uninterrupted flow under all conditions should review duplex or bypass arrangements.

10–1,000 μm filtration precision / standard units and parallel manifold configurations sized from project flow requirements / ΔP or timer-triggered cleaning cycle. These units fit within our broader range of industrial water treatment equipment.

Engineers
28
Technicians
78
Factory
70,500 sqm
Export Countries
20+
Documentation options
CE / ISO 9001 / ASME
Workshop
21,000 sqm
01
Selection Guidance

When to Specify a Self Cleaning Filter

The decision to specify an automatic backwash filter over a manual or cartridge alternative comes down to four operating conditions. Review the criteria below; if your application does not match the right-fit column, we will route you to the more appropriate equipment class before you spend time on a configuration review.

Fit · A

Right-Fit Conditions

  • As an economic screening rule, flow rate exceeds 50 m³/h and scheduled manual cleaning requires process isolation.
  • Inlet suspended solids are high or variable: seasonal surface water, open cooling tower circuits, or raw river water.
  • No reliable on-shift staffing is available for manual element service.
  • Downstream equipment cannot tolerate brief unprotected intervals, including RO membranes, heat exchanger tubes, and precision emitters.
  • Operating cost comparison between self-cleaning and replaceable-element filtration is part of the review.
Fit · B

Consider an Alternative

  • As an economic screening rule, flow below approximately 10 m³/h: stainless steel cartridge filter housing may be more practical where manual maintenance is manageable.
  • Dissolved contaminants such as chlorine, organics, TDS, or hardness are not captured by a screen. Use activated carbon water filter for chlorine and organics, or multi media filter for broad suspended solids removal.
  • Inlet TSS is very low and sustained, making automated backwash harder to justify.
  • Required precision falls below 10 μm on a sustained basis.

Fine-end boundary: Standard wedge wire and mesh screen elements for auto backwash filter service operate reliably from 10 to 1,000 μm. When your sustained filtration requirement falls below 10 μm, we assess whether a disc filter or membrane pretreatment stage is more appropriate than a screen-based backwash unit.

02
Operating Mechanism

How the Automatic Cleaning Cycle Works

The operating mechanism of a self cleaning filter is mechanical straining followed by a hydraulically driven flush; the cleaning event is seconds-scale, and the unit is designed to maintain downstream flow during normal automatic cleaning.

Self-cleaning filter backwash cycle steps: filtration, differential pressure buildup, flush valve opens, solids drain to discharge, return to full service
Step · 01

Filtration

Feedwater enters and flows through the element. Particles larger than the rated opening accumulate on the upstream face while filtered water continues at full operating pressure.

Step · 02

ΔP Buildup

As particle loading increases, resistance rises and differential pressure across inlet and outlet climbs. The control unit monitors ΔP continuously.

Step · 03

Trigger

When ΔP reaches the setpoint — typically 0.05 MPa for RO pretreatment, up to 0.1 MPa for standard industrial — the control unit signals the flush valve. Timer backup protects low-flow periods.

Step · 04

Backwash Flush

The flush valve opens. Pressurized filtrate reverses through the element segment, dislodging accumulated solids while the remainder continues in service.

Step · 05

Solids Discharge

Dislodged solids discharge to drain through the backwash outlet. Volume per cycle is determined by element area, pressure, and cleaning frequency.

Step · 06

Return to Service

The flush valve closes and the cleaned element returns to filtration mode. The complete cycle runs without operator presence or process shutdown.

Automatic Backwash

Cleaning trigger: ΔP setpoint or timer

Downtime: designed for continuous flow during normal cleaning

Labor: none required

Consumable cost: no replacement elements

Cartridge / Manual Filter

Cleaning trigger: manual schedule or element differential

Downtime: process isolation required

Labor: element removal, cleaning or replacement, reinstall

Consumable cost: replacement elements at each interval

03
Configuration Guidance

Self Cleaning Filter Configuration by Application

We configure each automatic backwash filter to the specific requirements of the application. The five variable categories below determine the unit specification; we confirm each during the configuration review before issuing a quotation.

Var · 01

Filtration Precision

For RO membrane pretreatment, 50–100 μm elements provide upstream coarse protection before finer cartridge filtration; this does not replace the final pre-RO security cartridge filter required by membrane manufacturer guidance. Cooling tower sidestream typically uses 100–300 μm, and irrigation networks commonly use 100–200 μm. Micron values refer to screen or mesh opening size; actual particle removal depends on particle shape, deformability, flow velocity, and element condition.

Var · 02

Filter Element Type

Wedge wire screen fits heavy particle loads, repeated high-pressure backwash cycles, and fibrous or abrasive particles. Fine mesh screen is standard for 10-200 μm precision. Sintered mesh fits chemical compatibility or elevated-temperature constraints, while perforated plate is used for coarse screening at 500 μm and above.

Var · 03

Housing Material

304 stainless steel fits standard fresh water where chloride content is low. 316L is commonly reviewed for saline, high-chloride, food-contact, or hygiene-sensitive applications. Final material selection depends on chloride concentration, temperature, pH, cleaning chemicals, product-contact classification, and buyer specification. Carbon steel with internal lining fits large-diameter cost-sensitive units where water chemistry is compatible.

Var · 04

Control Mode

Our standard configuration uses a standalone differential pressure switch with timer relay backup. For centralized process control, we supply PLC-ready units with 4-20 mA or digital I/O output for DCS or SCADA integration. Manual override is available at the controller.

Var · 05

Installation Orientation

Horizontal installation fits sites with limited overhead clearance. Vertical installation fits sites where floor space is constrained. Orientation affects drain line routing and element access direction, so we confirm it during configuration review.

Var · 06

Bypass Provision

We recommend confirming upstream and downstream isolation valves before installation. A bypass line allows inspection or unscheduled maintenance without total system shutdown. Confirm bypass scope during configuration review because it is a site-specific decision, not a default inclusion.

04
Application Scope

Where Automatic Backwash Filters Are Specified

Automatic backwash filters are specified across six primary application categories. The table maps each application to what the filter protects downstream, the filtration precision appropriate for that objective, and the key specification variable that determines the correct unit configuration.

ApplicationWhat the Filter Protects DownstreamTypical Filtration PrecisionKey Specification Variable
RO membrane pretreatmentSpiral-wound membrane feed spacers; suspended solids accelerate fouling and raise differential pressure across the membrane element.50-100 μmΔP trigger set conservatively at 0.05 MPa to respond before particle load accumulates at membrane inlet.
Cooling tower sidestreamHeat exchanger tube surfaces and tower fill; uncontrolled suspended solids cause scale-assisted biofouling and tube pitting.100-300 μmSidestream flow rate is a defined percentage of total tower circulation; confirm with cooling system design.
Irrigation network inletDrip emitters and sprinkler heads; particle clogging causes uneven distribution, flow rate drop, and crop damage.100-200 μmSeasonal inlet turbidity variation determines cleaning cycle frequency and element sizing.
Industrial process waterPumps, nozzles, heat exchangers, and product-contact surfaces in steel, paper, chemical, and power applications.50-500 μmOperating pressure and fluid chemistry determine element type and housing material; provide water analysis.
Food and beverage pretreatmentCIP systems, process equipment, and product water circuits; particulate contamination affects product quality and equipment reliability.25-100 μm316L SS commonly reviewed for product-contact surfaces; seal material confirmed from fluid temperature and compatibility. Review alongside our food and beverage water treatment solution scope.
Municipal water pretreatmentClarifiers, disinfection units, and distribution network equipment; coarse screening reduces chemical demand and maintenance.100-500 μmHigh-flow applications above 500 m³/h typically require parallel manifold configurations; see our municipal and community drinking water solution scope.
Self cleaning filter installed upstream of RO membrane system as coarse pretreatment protection in industrial water treatment plant
05
Technical Variables by Application

Operating Specification Reference

The table below maps key technical variables across the six principal application categories. Operating pressure sub-ranges and control mode recommendations are directional guidance based on typical application conditions and must be confirmed from your system design data during configuration review.

VariableRO PretreatmentCooling TowerIrrigationIndustrial ProcessFood & BevMunicipal
Filtration precision50-100 μm100-300 μm100-200 μm50-500 μm, process-specific25-100 μm100-500 μm
Operating pressureNormally selected for pretreatment pressure upstream of RO high-pressure pump. Housing rating must exceed max operating and surge pressure.0.6-1.5 MPa; confirm sidestream circuit0.6-1.0 MPa; confirm network pressure0.6-2.5 MPa; from process P&ID0.6-1.5 MPa; confirm cleaning circuit pressure0.6-1.5 MPa; confirm distribution pressure
ΔP trigger setpoint0.05 MPa, conservative0.07-0.1 MPa, standard industrial0.05-0.1 MPa, emitter sensitivity0.05-0.1 MPa, process-specific0.05 MPa, conservative0.07-0.1 MPa, standard
Housing material304 or 316L SS; confirm Cl- and TDS304 SS standard; 316L if treatment raises Cl-304 SS for fresh water304 SS / 316L / CS with lining316L SS for product-contact surfaces304 SS or CS for large-diameter installations
Element typeFine mesh screenWedge wire or fine meshFine mesh screenWedge wire / perforated plate / fine meshFine mesh or sintered meshWedge wire or perforated plate
Control modePLC integration common; ΔP primary + timer backupStandalone ΔP + timer; BMS if requiredStandalone ΔP + timer; timer-primary at seasonal low flowPLC / SCADA per facility standardPLC with process cleaning sequencing inputSCADA integration standard
Connection standardDN flange, ANSI / DIN / JISDN flange, ANSI / DIN / JISDN flange; confirm irrigation pipe standardDN flange, ANSI / DIN / JISDN flange; confirm hygienic connection where applicableDN flange per local piping code
06
Specification Risk

Common Mistakes and Engineering Boundaries

We review these five misspecification patterns regularly during inquiry stage. Identifying them early prevents equipment selection errors that delay system design and add cost to the treatment train.

Mistake · 01

Precision Without a Downstream Reference

We regularly receive inquiry forms requesting “a 100 μm filter” with no indication of what the filter is protecting. The downstream equipment specification, such as membrane model, heat exchanger tube diameter, or emitter orifice size, is the correct starting point.

Mistake · 02

Filtering a Dissolved Contaminant Problem

Screen-based mechanical filtration targets suspended solids captured by a physical barrier. It has no effect on TDS, hardness, dissolved chlorine, organics, or colloidal turbidity below the rated opening, so we route those inquiries to the correct treatment step.

Mistake · 03

Undersized Backwash Drain Capacity

The backwash discharge line must carry intermittent pressurized flow to a drain point capable of receiving it. If drain routing is restricted or above grade, gravity drain may not be practical and pressurized drain lines are required.

Mistake · 04

Single Unit Where a Manifold Is Needed

For flow rates above approximately 500-1,000 m³/h, one large housing may not be optimal. Parallel manifold configurations with staggered cleaning cycles maintain flow during backwash and allow individual units to be isolated for inspection.

Mistake · 05

No Upstream Coarse Screening at High Inlet TSS

As a preliminary review trigger, when sustained inlet TSS exceeds approximately 200–500 mg/L, or when the source includes leaf matter, fibrous material, or large sediment, an upstream coarse strainer protects the element. Actual threshold depends on element type, solids nature, cleaning frequency, and drain capacity.

Mistake · 06

How We Catch These Before Quotation

Every inquiry goes through a configuration review before we issue a specification recommendation. We check water analysis, downstream equipment type, flow rate, drain conditions, and site constraints before confirming element type, housing material, ΔP trigger, and control mode.

07
Manufacturing Capability

Why Hiju Engineering

Qingdao Hiju Thermal Power Co., Ltd has designed and manufactured water treatment filtration equipment since 2016. Our self cleaning filter units are manufactured under CE and ISO 9001 documentation scope; ASME-code pressure vessel documentation is available on request for projects requiring it.

Filter manufacturing workshop with overhead crane, welding stations, and pressure vessel assembly line
Stat

70,500 sqm

Factory

Stat

21,000 sqm

Workshop

Stat

28 + 78

Engineers + technicians

Stat

20+

Export countries

Engineering · A

Manifold Design for High-Flow Installations

Above approximately 500–1,000 m³/h, a single filter housing may not be optimal. Our engineers design parallel manifold systems with staggered cleaning cycles, so each unit cycles in turn while the remaining units stay in service.

Engineering · B

Cooling Tower Chemical Compatibility

For cooling tower protection in hot-climate markets, our team reviews chemical treatment compounds alongside housing material selection to confirm whether 304 or 316L stainless steel is appropriate given expected Cl⁻ concentration.

08
Send These Inputs First

Configuration Review Checklist

Every inquiry goes through a configuration review before we issue a specification recommendation.

Project Checklist · 08 Inputs
  • Water analysis — TSS, turbidity, pH, temperature, chloride
  • Downstream equipment type — RO, cooling tower, irrigation, process, F&B, municipal
  • Design flow rate — m³/h; peak and average if variable
  • Required filtration precision — µm and rationale (what is being protected)
  • Operating pressure — supply pressure and allowable pressure drop
  • Drain conditions — discharge route, gravity vs. pressurized, drain capacity
  • Site constraints — orientation, clearance, footprint, control interface
  • Project destination and certification scope — CE, ISO 9001, ASME if required
09
Reference

Frequently Asked Questions

Q.01Does a self cleaning filter backwash cycle interrupt main process flow?+
A self cleaning filter is designed to maintain downstream flow during normal automatic cleaning. The flush action operates on a localized section of the element while filtrate continues through the remainder of the screen. For applications where any bypass during cleaning is not acceptable, a dual-unit or bypass arrangement is reviewed.
Q.02How is the cleaning cycle triggered, and can the settings be adjusted?+
The primary trigger is differential pressure: when ΔP reaches the configured setpoint, typically 0.05 MPa for RO pretreatment and up to 0.1 MPa for standard industrial service, the control unit initiates the flush sequence. A timer backup fires on a fixed interval, manual override is available, and both setpoints are field-adjustable.
Q.03What are the power and drain requirements?+
In pressure-fed backwash configurations, only a controller and flush valve are required. Scanner, brush, or large-capacity cleaning mechanisms may require motorized or pneumatic actuation. Final utility requirements are confirmed from the selected model. The drain connection must be sized to receive intermittent backwash discharge.
Q.04Can an automatic backwash filter handle sudden turbidity spikes?+
A sudden inlet TSS spike causes faster element loading and more frequent cleaning cycles. Where spikes are predictable, the element is sized with additional surface area. As a preliminary review trigger, sustained high TSS above approximately 200–500 mg/L may require upstream coarse screening; actual threshold depends on element type, solids nature, and drain capacity.
Q.05What maintenance is required after installation and commissioning?+
Under normal conditions, the automatic cleaning mechanism handles element maintenance continuously. Periodic attention focuses on verifying backwash valve actuation, confirming ΔP sensor calibration, inspecting the drain line, and checking element condition during scheduled access intervals.
Q.06When is a self cleaning strainer not the right choice?+
When the contaminant is dissolved rather than suspended, mechanical screening will not address it. When flow is low enough that manual maintenance is practical, the capital investment may not be justified. When required precision falls below 10 μm, standard backwash-cleanable elements reach their boundary. Contact our engineering team with your water analysis if unsure.