Centrifugal aeration blower with a flanged inlet connection
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Applications

Wastewater aeration is a 4,000–8,000 mmWC duty for a multistage or positive-displacement blower; every other air duty on the plant is single-stage centrifugal, and that is what we build.

One metre of water column is 1,000 mmWC, so a diffuser grid sitting 4–8 m below the surface puts the machine at 4,000–8,000 mmWC — roughly 0.4–0.8 bar — before grid, drop-leg and diffuser losses are added. That is a multistage centrifugal or positive-displacement blower: a different machine class from the single-stage fans we build. Our envelope tops out at 2,000 mmWC, about two metres of water. What we do build sits all around that tank — digester and biogas boosters, odour-control and biofilter extract, sludge-drying and handling air, and plant ventilation — up to 2,25,000 CMH, 2,000 mmWC, 425 HP and 500 °C.

2,25,000CMH max flow
2,000mmWC max static
24×7continuous duty
425 HPdrive power
15,000+
fans built since 2011
200 HP
VFD test rig · IS 4894 / AMCA 210
95%
on-time delivery (ERP statistics)
3–5
working days to quote

Engineered capability across the wastewater plant — digester, odour-control and sludge-drying duties, sized and built to your duty point. Part of 15,000+ fans built since 2011.

DIGESTER & BIOGAS BOOSTER · ODOUR & BIOFILTER EXHAUST · SLUDGE-DRYING AIR · PLANT VENTILATION
From our gallery

A cross-section of the fans we build

Backward-curved fan built by Jitamitra for corrosive gas exhaust, 42,500 CMH at 150 mmWC and 40 °C
42,500CMH/150mmWC/40°C
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Backward-curved plate fan built by Jitamitra for bag-filter draught, 2,100 CMH at 550 mmWC and 40 °C
2,100CMH/550mmWC/40°C
Bag-filter / pulse-jet draught · Pollution Control / APC OEM
Backward-flat plate fan built by Jitamitra for spray and fluid-bed drying, 1,000 CMH at 1,200 mmWC and 20 °C
1,000CMH/1,200mmWC/20°C
Drying (spray / fluid-bed / flash) · Pharmaceuticals
Radial fan built by Jitamitra for combustion and process air, 1,400 CMH at 850 mmWC and 40 °C
1,400CMH/850mmWC/40°C
Combustion / process air blower · Furnaces, Ovens & Heat Treatment

Browse every fan in our gallery →

What it does

The blower feeds the biology — and it never stops.

A wastewater aeration blower supplies compressed air to the diffuser grid at the bottom of a deep aeration basin: pushing enough air against the water column to hold dissolved oxygen in the mixed liquor, delivering it continuously through the daily and seasonal load swing, and doing so at the lowest specific power the duty allows — because on most plants this one machine sets the electricity bill.

  • 01
    Push against submergence

    The discharge static is set by the diffuser depth plus grid and pipe losses — a 5 m tank alone is roughly 500 mmWC of water column before any header or diffuser drop is added. The blower holds that static continuously, not intermittently.

  • 02
    Track the oxygen demand

    Air demand swings with the incoming load — diurnal peaks, weekend troughs, seasonal temperature. The blower turns down to match dissolved-oxygen setpoint rather than dumping surplus air, typically over a 40–100% range against a DO control loop.

  • 03
    Run without stopping

    Aeration cannot be interrupted — lose air and the biomass starts to die within hours. The machine is sized for 8,000+ h/yr continuous running with L10 bearing life and thermal margin to match.

Why it is hard

Clean air, but three things decide whether the plant's biggest motor is cheap or ruinous to run.

Nobody worries about erosion here — the air is clean. What decides the duty is lifetime power: aeration is commonly 50–60% of a treatment plant's total energy, so the blower's efficiency, its turndown behaviour and its uptime dwarf the purchase price. A 150 HP aeration blower run several points below its best static efficiency wastes tens of MWh a year — over a 20-year asset life the efficiency choice can cost several times the original machine.

01 — SPECIFIC POWER

Lifetime energy per kg of oxygen

The blower runs at high power, continuously, for the life of the plant. A few points of efficiency lost at the design point, or air throttled to waste at part-load, compounds into the plant's largest recurring cost.

What we do on the duties we build

It's the same discipline we apply to the digester, odour-control and sludge-drying fans we do build for the same plant — backward-curved / backward-inclined wheels selected for high static efficiency on standard duty, airfoil-bladed impellers for higher efficiency where the running hours justify it, and the duty point placed at the wheel's best-efficiency region — not a catalogue near-fit dragged onto your spec.

02 — TURNDOWN

Following DO demand without waste or surge

Oxygen demand moves through the day and the seasons. Throttle the surplus air across a fixed-speed machine and you burn power to waste; turn down too far and a high-static centrifugal can approach surge, where flow becomes unstable against the water column.

What we do on the duties we build

On the digester, odour-control and sludge-drying fans we do build, VFD speed control is our default so the machine tracks demand instead of throttling, the duty point sits on the falling, stable side of the curve, and the working turndown band is verified clear of the surge line on the rig before dispatch. The deep-tank aeration blower needs the same discipline from whoever builds it — that isn't us.

03 — CONTINUOUS RUN

No tolerance for downtime

The biology depends on uninterrupted air; an unplanned blower stop cascades into a process upset and a consent-breach risk. Bearing failure, overheating and resonance are the things that take a continuously-running machine down.

What we do on the duties we build

On what we do build for the same plant, bearing life is designed to L10h ≥ 40,000 h continuous, the thermal and lubrication scheme is sized for 24×7 service, balance is to ISO 21940 G6.3 (tighter on application), and a lateral-critical check keeps the running speed clear of resonance across the VFD band. The deep-tank aeration blower carries the same continuous-duty demands — engineered by whoever builds that machine, not by us.

Jitamitra in-house capability
How we design what we do build

Every choice is documented on the GA drawing you sign off — before we cut metal.

We don't sell a catalogue near-fit. On the digester, odour-control, sludge-drying and ventilation fans we do build for your plant, each one is engineered to its own gas, pressure, temperature and corrosion load — not adapted from a shelf. The deep-tank aeration blower itself, at 4,000–8,000 mmWC, sits outside this: see why above.

  • Impeller geometry — Backward-curved or backward-inclined for the highest static efficiency on the digester, odour-control and sludge-drying duty; airfoil-bladed on the largest, longest-running builds where the energy saving repays the CAPEX inside a couple of seasons.
  • Static & density basis — Discharge static built up from your actual duct run, hood entry and scrubber/biofilter losses — corrected for gas temperature, density and site altitude, so the machine holds the duty on the hottest day, not just at ISO reference conditions.
  • Control — VFD as default — Process demand on the digester, odour-control and sludge-drying air swings across the day; VFD speed control tracks that demand and is far more efficient than throttling the surplus air. Inlet guide vanes (IGV) remain available where a fixed-speed motor is retained. The working band is proven clear of surge.
  • Materials & continuous-duty build — Mild steel with epoxy coating standard; stainless steel where the ambient is humid, coastal or corrosive (H₂S-laden STP atmosphere); shaft seal and bearing scheme selected for uninterrupted 24×7 running with a sustained 80–100 °C housing temperature.
How we engineer any duty point

We size every blower onto the stable side of its curve, clear of surge — then prove it on the rig.

No catalogue blower forced onto a spec. On the digester, odour-control, sludge-drying and ventilation fans we build for a plant like yours, the operating point is engineered onto the falling, stable portion of the selected wheel with the whole turndown band held clear of the surge line, and verified on the 200 HP VFD test rig across speed before dispatch. The deep-tank aeration blower needs the same discipline from whoever builds it — that isn't us. Fans above the rig's 200 HP are run at derated speed and scaled to the specified duty by the fan laws.

avoid: unstable 0 40,000 80,000 1,20,000 1,60,000 2,00,000 VOLUME FLOW RATE  [ CMH ] 0 500 1000 1500 2000 STATIC PRESSURE  [ mmWC ] 0 25 50 75 100 STATIC EFFICIENCY  [ % ] Fan static pressure System resistance Static efficiency BEP DUTY POINT 1,20,000 CMH · 450 mmWC Fan static pressure System resistance Static efficiency
Fig. 2Illustrative fan characteristic — fan static pressure, system resistance and static efficiency vs. flow, with the duty point and turndown band engineered onto the stable region clear of surge. This is how we approach any duty we build. Every blower is sized to its own duty.
Capability envelope — what we build around the tank

What we can supply for the duties around that tank.

ParameterStandardOn application
Volume flowup to 2,25,000 CMHhigher on enquiry
Static pressureup to 2,000 mmWChigher on enquiry
Deep-tank aeration duty (for reference)4,000–8,000 mmWC from diffuser submergence + grid & pipe loss (typ. 4–8 m water column)multistage or positive-displacement blower class
Static efficiencyhigh static efficiencyhigher on high-efficiency builds
Turndown (VFD)40–100% against process demandwider band on application, verified clear of surge
Drive powerup to 425 HPour largest drive delivered to date
Speed600–1,800 RPM typicalper duty + sound limits
Balance qualityISO 21940 G6.3G2.5 / G1.0 on application

The envelope above covers the fans and blowers we build around the tank — digester and biogas boosters, odour-control and biofilter extract, sludge-drying and handling air, and plant ventilation — not the deep-tank aeration blower itself, which needs 4,000–8,000 mmWC and sits outside a single-stage centrifugal's reach. Bearing life on what we do build is a design target of L10h ≥ 40,000 h continuous, with longer L10 on application. Send us the duty and we'll tell you plainly whether it's ours to build.

How the fans we build around the tank are specified

Specified, not picked from a shelf.

The same engineering language carries from your enquiry to the GA drawing to the nameplate — expressed in the standard AMCA conventions.

Specification fieldOptions
Arrangement (AMCA 99)Arr. 1 (overhung, fan bearings) / Arr. 4 (direct, motor on base) / Arr. 8 (overhung on common base) / Arr. 9 (overhung, motor side) / Arr. 10 (overhung, motor inside base) — selected by drive, access and continuous-duty cooling.
Width / inletSWSI (single width, single inlet) default for high-static duty; DWDI (double width, double inlet) for high flow at moderate pressure.
Wheel typeBackward-curved or backward-inclined (default, best efficiency on clean high-static air) / airfoil-bladed (highest-efficiency, large continuous-duty builds).
Class (by pressure / outlet velocity)Class II / III selected from the duty point on the pressure-vs-outlet-velocity limits; a high-static duty like a digester or biogas booster often lands in the higher classes — heavier construction for the pressure and tip speed.
Materials of constructionMild steel + epoxy coating (standard) / stainless steel for humid, coastal or H₂S-laden plant atmosphere / special coating on application for aggressive ambients.
DriveDirect-coupled / V-belt / VFD (default for demand-tracking turndown). Drive up to 425 HP, our largest drive delivered to date; speed typically 600–1,800 RPM.
Discharge & rotation (AMCA orientation)Rotation CW or CCW (viewed from drive side) with discharge angle per AMCA — e.g. TH/BH/UB/DB — set to match your air-header take-off and installed footprint.
Accessories & acoustic scopeVFD package or inlet guide vanes (IGV) for turndown; inlet silencer and discharge silencer for the pulsation and blade-pass content of high-static duty; acoustic-treated casing or enclosure where the blower room sits near occupied space; flexible connection / expansion joint at inlet and discharge; shaft seal and bearing scheme for 24×7 running; drain and inspection doors.
Jitamitra in-house capability
The proof, not the promise

We test before we ship — and you're welcome to witness it.

Every job's performance is verified at our works on the 200 HP VFD test rig, to the IS 4894 / ISO 5801 / AMCA 210 method, before dispatch.

  • Customer-witnessed FAT on request
  • Rotors balanced to ISO 21940 G6.3 as standard (G2.5 / G1.0 on application) before they leave the floor
  • Full NDT in-house — DP, MPI, UT, RT — to what the duty demands
30+ INDUSTRIES · 45 APPLICATION / DUTY TYPES
Where we work around the tank

Built for what sits next to the plant's biggest motor.

Water & Wastewater

Municipal STP and CETP digester and biogas boosters, odour-control and biofilter exhaust, sludge-drying and handling air.

Chemicals & Petrochem

Industrial ETP odour-control, biogas and sludge-handling duty around the biological treatment train.

Food & Beverage

Dairy, brewery and processing-effluent odour-control and sludge-drying air, where organic load swings hard.

Pharmaceuticals

Process-effluent and utility ETP odour-control and sludge-handling air on continuous-run duty.

Pulp & Paper

Mill-effluent odour-control exhaust and sludge-handling air around the treatment lagoons.

Textile & Dyeing

Dye-house effluent odour-control exhaust ahead of tertiary treatment.

Sugar & Distilleries

Spent-wash and process-effluent odour-control and sludge-drying air on high-load organic streams.

Your process

45 application/duty types engineered. Tell us yours.

Standards & conformity

Stated precisely — because procurement checks.

What our marks mean, in the words that survive an audit.

Performance

Tested to the IS 4894 / ISO 5801 / AMCA 210 method, in-house on our 200 HP VFD rig. Tested-to-method — not AMCA-certified.

Quality system

ISO 9001:2015 — third-party certified. Our only third-party certification.

CE conformity

Self-declared per 2006/42/EC + 2014/35/EU. A self-declaration, not a notified-body certificate.

ATEX conformity

Self-declared, Zone 2/22, Category 3, per 2014/34/EU, where the area classification calls for it.

Oil & gas duty

Designed and built to API 673 as project-specific scope.

Welding

ASME Sec IX qualified welders + WPS for every joint.

Balance

ISO 21940 — G6.3 minimum, G2.5 / G1.0 on application.

Vibration

ISO 14694 fan-specific limits; ISO 20816 general evaluation method.

Lead time & process

From enquiry to a tested fan on your dock.

StageStandard dutyCE / ATEX / API / AMCA
Offer / quotation3 to 5 working days5 to 7 working days
GA drawing for approval3 days from customer PO5 to 7 days from customer PO
Manufacture + balance + paint2 to 3 weeks from PO + PI + approved GAD4 to 5 weeks from PO + PI + approved GAD
Performance test + witnessed FAT~1 week~1 week
Order-to-dispatch (total)4 to 6 weeks7 – 9 weeks

Shutdown-driven replacements: we have shipped fans within 3 weeks of a clean PO. Tell us your shutdown window and we commit to a dated plan.

Questions engineers ask

The eight we hear most before a PO.

Why doesn't Jitamitra build the deep-tank aeration blower itself?
The discharge static is set by the diffuser submergence, roughly 100 mmWC for every metre of water column, plus header, drop-leg and diffuser losses — which puts a typical 4 to 8 m tank at 4,000 to 8,000 mmWC before any correction for site altitude or inlet temperature. That is multistage-centrifugal or positive-displacement territory, a different machine class from the single-stage centrifugal fans we build to 2,000 mmWC. We match the machine class to the duty, so every fan runs inside its envelope. Talk to us instead about the digester, odour-control and sludge-drying duties on the same plant.
Aeration is our biggest power bill. Does that change what I should look for in a deep-tank blower?
It should be the first thing you check, whoever supplies it. Aeration commonly runs 50 to 60 percent of a treatment plant's total energy and the machine runs continuously, so a duty point placed even a few percentage points off the wheel's best-efficiency region compounds into real money over a 20-year asset life. Because deep-tank static sits outside a single-stage centrifugal's envelope, this isn't a duty we quote — but the same discipline, duty point at best-efficiency rather than a catalogue near-fit, and VFD turndown instead of throttling loss, is exactly what we apply to the digester, odour-control and sludge-drying duties we do build on your plant.
Does a deep-tank aeration blower need to follow dissolved-oxygen demand through the day?
Yes. Oxygen demand swings diurnally, at weekends and seasonally, so whatever supplies the aeration air should turn down against the DO setpoint rather than throttling the surplus, typically across a wide turndown band verified clear of surge. On the digester, odour-control and sludge-drying air we do supply for the same plant, VFD speed control is our default for exactly this reason, tracking demand rather than wasting power against a fixed speed.
The aeration blower has to run 24×7. Does Jitamitra build for that kind of continuous duty?
Yes, for the fans we build around it. On the digester and biogas boosters, odour-control and biofilter exhaust, and sludge-drying air we build for the same plant, continuous running is the default assumption: bearing life is a design target of L10h at or above 40,000 hours, the lubrication and thermal scheme is sized for sustained running, and we run a lateral-critical check so the speed sits clear of resonance across the VFD band. Where the plant needs it we configure duty-and-standby so a machine can be taken out for service without stopping the process.
The atmosphere around the tanks is humid and can carry H₂S. What materials do you use on the fans you do build there?
On the digester, odour-control, sludge-drying and ventilation fans we build for that atmosphere, the corrosion concern is the plant ambient rather than the process airstream. Standard build is mild steel with an epoxy coating, which suits most enclosed blower rooms. Where the surroundings are humid, coastal, or carry hydrogen sulphide from the sewage stream, we move to stainless steel construction or a special protective coating on the exposed surfaces, selected to your site atmosphere. We size the material to the actual ambient you describe, not a default.
Can you match or replace an existing aeration blower on our plant?
The deep-tank aeration blower itself, at 4,000 to 8,000 mmWC, is a multistage or positive-displacement machine. What we reverse-engineer is everything else around that tank: a digester or biogas booster, an odour-control or biofilter fan, or a sludge-drying and ventilation unit, matched to the existing duty point, bearing centres, inlet and discharge orientation and foundation bolt pattern, so the replacement drops onto the existing base and ducting. Send us the old GA drawing and nameplate for any of those and we will match it.
What is the lead time on the fans you do build for a wastewater plant, and how are they tested?
For the digester and biogas boosters, odour-control and biofilter exhaust, and sludge-drying air we build around the tank, a standard job runs roughly 9 to 14 weeks order-to-dispatch: offer in 3 to 5 working days, GA drawing 2 to 3 weeks from PO, manufacture, balance and paint 6 to 10 weeks, and performance test plus FAT about a week. Every machine is performance-tested in-house to the IS 4894 / ISO 5801 / AMCA 210 method on our 200 HP VFD test rig and dynamically balanced to ISO 21940 G6.3 as standard. Fans above the rig's 200 HP are run at derated speed and scaled to the specified duty by the fan laws. The test and FAT are customer-witnessed on request. The deep-tank aeration blower itself is not part of this — it is not a machine we build.
What do your AMCA, CE, ATEX and ISO claims actually mean?
We are precise about this. Performance is tested in-house to the IS 4894 / ISO 5801 / AMCA 210 method on our 200 HP VFD rig; that is testing to the method, not an AMCA certification, and we are not an AMCA member. CE is self-declared per 2006/42/EC and 2014/35/EU, and ATEX Zone 2/22 is self-declared per 2014/34/EU, Category 3, where an area classification calls for it; those are self-declarations of conformity, not third-party certifications. Balance is to ISO 21940, G6.3 as standard and G2.5 or G1.0 on application, and bearing life is a design target of L10h at or above 40,000 hours. Our only third-party certification is ISO 9001:2015.
Across the range

Where this duty fits — the fans we build around it, related duties, and the industries served.

The same engineering, viewed three ways — by fan family, by duty, and by industry. Follow the cross-references.

Take it further

Specs an engineer can use — not a brochure.

Ready to quote?

Send us the duty point. We'll quote in 3 to 5 working days.*

Flow, static, gas temperature, application — or attach a spec, GA drawing or a multi-fan schedule. Engineer to engineer.

Get a quote → Email the desk

ISO 9001:2015 quality system · performance-tested to IS 4894 / ISO 5801 / AMCA 210 method · witnessed FAT on request.

*For our standard range. ATEX and special projects need 5 to 7 working days.

Further reading
Specifying a fan duty point  ·  How we build every fan in-house
Need this fan for your duty? We quote in 3 to 5 working days.Get a quote →