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Source filament-wound FRP vessels for multi-grade filters, activated carbon, softeners and iron removal — from compact 0844 tanks to 36-inch diameter vessels, in top mount and side mount configurations, with control valves, distributors and media — from ScientificEdge, India's trusted B2B water treatment sourcing partner.
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ScientificEdge supports sourcing and supply of suitable FRP media vessels, softener and filter tanks, control valves, internal distributors and filter media based on media volume, service and backwash flow rate, vessel diameter and height, valve mounting and connection size, brand preference, technical documentation, and buyer requirements.
FRP vessels are filament-wound fibreglass tanks over a seamless polyethylene liner, holding filter or ion exchange media in pre-treatment duty — multi-grade filters, activated carbon, softeners and iron removal units. They are specified by diameter and height, media volume, valve mounting and connection size, and they carry a working pressure of roughly 10 bar rather than the hundreds of psi a membrane housing sees.
It is worth separating two products that share a name. An FRP media vessel sits upstream of the high-pressure pump, holds loose media, and is opened for media changes. An FRP membrane housing holds 4040 or 8040 RO elements downstream of that pump at 300 to 1200 psi and is a different vessel entirely, with different construction and a different code basis. Both get called FRP pressure vessels, and ordering one when you meant the other is a costly and surprisingly common mistake.
Sizing follows the media, not the flow alone. A softener is sized on hardness load and the throughput wanted between regenerations; a carbon filter on empty bed contact time, because contaminant removal is a residence-time problem; and a multi-grade filter on service velocity through the bed. Three different calculations that happen to produce a vessel diameter, which is why quoting a flow rate on its own rarely gets a usable answer.
Final selection should rest on the media type and volume, the service and backwash flow the plant can actually supply, the vessel size designation, whether the valve mounts on top or on the side, the connection size, and whether regeneration or backwash is manual or automatic.

8" – 36" diameter
Standard size range
Designated by diameter and height in inches — a 1354 vessel is 13" in diameter and 54" tall. Larger diameters generally move to side mount valves.
~10 bar
Typical working pressure
Roughly 150 psi. Far below an RO membrane housing, because these vessels sit ahead of the high-pressure pump rather than behind it.
50%+ freeboard
Backwash expansion allowance
Space left above the settled bed so media can lift and clean during backwash instead of being carried out of the vessel.
Five bands across the range. Diameter comes from the media and the backwash the site can supply; the valve mounting follows the diameter.
| Vessel class | Typical duty and size | Key technical features |
|---|---|---|
| Compact Vessels (0844 to 1054) | Point-of-entry softeners, small carbon filters and lab or office duty, 8"–10" diameter | Top mount 2.5" threaded opening taking a manual or automatic multiport valve, light enough to be handled and re-bedded by one person |
| Commercial Vessels (1252 to 1665) | Hotels, hospitals, campuses and small plants, 12"–16" diameter | The most commonly specified band in India, still top mount, with automatic valves where regeneration must run unattended overnight |
| Industrial Vessels (1865 to 2472) | Factory utility pre-treatment and RO feed conditioning, 18"–24" diameter | Transition band where top mount multiport valves start to restrict backwash flow and side mount arrangements become the better answer |
| Large Industrial Vessels (3072 and above) | Plant-scale multi-grade and carbon filtration, 30"–36"+ diameter | Side mount valve nests or individual butterfly valves on a face piping arrangement, with hub-and-lateral underdrains sized for even collection |
| Duty-Specific Configurations | Softening, activated carbon, multi-grade and iron removal | Same vessel family, different internals, media and freeboard — softening resin, graded sand and anthracite, carbon, or manganese media each expand differently on backwash |
Indicative bands rather than fixed product models. Working pressure, maximum temperature, opening size, connection type and permitted media vary by manufacturer and model, and are confirmed against the technical datasheet of the vessel quoted. Size designations give nominal diameter and height in inches; actual internal volume and usable media volume differ from the nominal figures.
The intuitive way to size a media vessel is to take the service flow, apply a service velocity, and read off a diameter. It gives an answer, and on plants where backwash water is plentiful the answer is usually right. Where it goes wrong is that the bed also has to be cleaned, and cleaning needs a far higher upward velocity than filtering needs downward.
Backwash has to lift and fluidise the whole bed so that trapped solids are released and carried to drain. That takes a flux in the region of 25 to 45 cubic metres per hour per square metre of vessel cross-section for sand and anthracite, varying with media, grain size and water temperature — cold water is denser and needs less flow to fluidise the same bed, which is why a backwash set in summer can be too vigorous in winter and vice versa. Multiply that flux by the area of the diameter you just calculated and you have the backwash flow the site must be able to deliver, at pressure, for ten to fifteen minutes.
Very often it cannot. Then the honest options are a smaller diameter with a deeper bed, a backwash storage tank and dedicated pump, or splitting the duty across two vessels backwashed one at a time. What does not work is installing the vessel anyway and backwashing at whatever the supply gives: the bed never fluidises, solids consolidate, channels form through the media, and filtration quality falls away over months while every gauge reads normal.
The related trap is freeboard. A fluidised bed expands substantially — commonly half its settled depth again — so a vessel filled to maximise media volume pushes media into the top distributor and out to drain on every backwash. The symptom is media appearing downstream and bed depth falling steadily. Size for media volume plus expansion, not for how much media the vessel will physically hold.
A vessel is a tank, a valve, a set of internals and the media inside it. These are the lines quoted alongside it, so the filter arrives complete rather than in parts.
Filament-wound tanks over a seamless polyethylene liner across the commercial and industrial range.
The complete softening set, sized on hardness load and the throughput wanted between regenerations.
Top mount valves for the commercial range and side mount nests above it, with timer or meter-initiated regeneration.
The internals that decide whether flow is distributed evenly or channels straight through one part of the bed.
Multi-grade beds supplied as a matched set of layers rather than as separate materials to be guessed at on site.
Carbon selected on iodine value and contact time; manganese media matched to the iron and manganese actually present.
Strong acid cation resin in sodium form, quoted by settled litres for the vessel and duty.
The fittings that make a filter measurable — differential pressure across the bed is what tells you when to backwash.
The media decides the sizing calculation and the freeboard. These are the duties FRP vessels are specified into across Indian plants.
Graded sand, gravel and anthracite sized on service velocity, removing turbidity and suspended solids so the cartridge stage is not doing work it was never meant to.
Sodium-cycle resin sized on hardness load, protecting downstream membranes or boilers and allowing higher RO recovery than the raw water alone would permit.
Sized on empty bed contact time rather than flow, because chlorine and organics removal depends on how long the water stays in the bed.
Oxidation followed by a manganese media bed, with backwash frequency governed by the iron load rather than by a fixed schedule.
Hotels, hospitals and campuses in the 12 to 16 inch band, where automatic valves matter because nobody is present to regenerate at 2 am.
Pre-treatment to a consistent quality ahead of the process, with media and internals chosen for cleanability as well as performance.
Sand filtration on recirculating duty, where backwash water availability is often the real constraint on vessel diameter.
Ten details decide whether a vessel can be quoted on the first pass. The duty and the raw water analysis matter more than the size — the size is usually an output, not an input.
Duty — multi-grade filtration, softening, activated carbon, or iron and manganese removal
Raw water analysis, particularly hardness for softening and iron for removal duty
Service flow rate required, in m³/hr or LPH
Backwash flow and pressure the site can actually supply, and for how long
Vessel size if already known, as diameter and height, or the media volume required
Valve mounting and type — top mount or side mount, manual or automatic, timer or meter initiated
Inlet and outlet connection size and type
Whether media, brine tank and internals are required with the vessel
Delivery location and target delivery schedule
GST, tender or corporate procurement requirement
As a trusted B2B distributor and supplier, ScientificEdge can coordinate technical datasheets, dimensional drawings, pressure and temperature rating data, material and liner specifications, valve compatibility details and media specifications where available from the respective manufacturer. Plant engineers are encouraged to share the raw water analysis and available backwash flow during enquiry, since both change the vessel selection.
Overall height with the valve fitted, diameter, opening size and connection centres — the valve height in particular decides whether the vessel fits the plant room.
Working pressure, maximum operating temperature, liner material and permitted media for the model quoted.
Opening thread or flange checked against the control valve, and distributor and riser sizing checked against the media and flow.
Grain size, bed depth and backwash expansion data for the media supplied, which is what the freeboard calculation depends on.
Working pressure, temperature limits and permitted media are attributes of the manufacturer's specific product. ScientificEdge coordinates that documentation where it is issued; it does not certify, test or re-rate vessels, and does not confer compliance with any code or standard. Sizing figures are engineering estimates from the parameters supplied rather than a performance guarantee. Installation, support, relief protection and periodic inspection remain the responsibility of the plant owner and their qualified engineers.
One dimension is missed more often than any other: overall height with the control valve fitted, plus the clearance above it needed to remove that valve for service. A vessel that fits the floor plan and not the ceiling is a problem discovered on delivery day. Send the available headroom with the enquiry and it becomes a check rather than a surprise.
ScientificEdge supports sourcing and distribution enquiries for FRP media vessels, softener and filter tanks, control valves, internal distributors and filter media from reputed global and domestic brands, including Pentair (Structural), Canature, Wave Cyber, Aquatrol, Runxin, Clack, UKL, Shubh, and equivalent options, subject to stock availability, buyer specification, technical compatibility, and documentation.
Brand names indicate the sourcing enquiries ScientificEdge can support. They do not indicate authorised distribution, official dealership or an exclusive partnership, and no brand logos are displayed. All brand and product names are the trademarks of their respective owners and are referenced only because buyers and tender documents specify by them. Where an equivalent is offered, diameter and height, opening size, working pressure and connection type are matched — and the control valve is checked against the vessel opening, since valve and tank are frequently different makes.
The vessel is the cheapest part of a media filter and the part everyone specifies first. What decides whether the filter works is the media, the internals and the backwash it can get.
A supply partner in India for water treatment OEMs, EPC contractors, O&M teams and facility managers.
Support sizing on hardness load, empty bed contact time or service velocity as the duty requires — and checking the backwash flow the site can supply before the diameter is fixed.
Tanks, control valves, distributors, graded media and resin quoted together, with the valve checked against the vessel opening.
Dimensional drawings, rating data and media specifications gathered for project files and audits, where the manufacturer issues them.
GST-compliant billing and procurement alignment for private factories and government tenders alike.
Dispatch coordination across Delhi NCR, Gujarat, Maharashtra, Tamil Nadu, Telangana, Karnataka, West Bengal and other industrial corridors.
Fields marked with an asterisk are required. Duty and flow select the vessel; the backwash available and the headroom decide whether that selection will actually work on site.
ScientificEdge is a B2B distributor and sourcing partner covering vessels, control valves, internal distributors, graded media and softening resin from one desk — so the valve is checked against the vessel opening and the media against the internals before anything ships, rather than after.
The practical value is in sizing: working from hardness load, empty bed contact time or service velocity as the duty requires, checking the backwash flow the site can supply against what the diameter needs, coordinating dimensional drawings and rating data where the manufacturer issues them, and invoicing in the form your procurement or tender process requires.
They share a material and almost nothing else. An FRP media vessel holds loose filter or ion exchange media — sand, carbon, resin — sits upstream of the high-pressure pump, and works at roughly 10 bar. It is opened periodically to change media, and its internals are distributors that spread flow across a bed.
An FRP RO pressure vessel is a membrane housing. It holds 4040 or 8040 spiral-wound elements downstream of the high-pressure pump at anywhere from 300 to 1200 psi, has head assemblies with retaining rings rather than a threaded top opening, and is built to a different pressure class entirely. Both are casually called FRP pressure vessels, which is exactly why it is worth stating the duty rather than the material when ordering.
The number gives nominal diameter and height in inches. A 1354 vessel is 13 inches in diameter and 54 inches tall; a 1054 is 10 by 54; a 2472 is 24 by 72. It is a size code, not a capacity, and it says nothing about how much media the vessel should hold.
Usable media volume is always less than internal volume, because freeboard has to be left above the settled bed for backwash expansion. Two vessels of the same designation from different makers can also differ slightly in internal volume and in opening size, so confirm both against the datasheet rather than assuming the code guarantees interchangeability.
By three different calculations. A softener is sized on hardness load: hardness multiplied by the throughput wanted between regenerations gives the exchange capacity needed, which gives a resin volume, which gives a vessel. A carbon filter is sized on empty bed contact time, because chlorine and organic removal depends on residence time in the bed — commonly several minutes, which for a given flow fixes the bed volume.
A multi-grade filter is sized on service velocity through the bed, typically in the region of 10 to 15 cubic metres per hour per square metre of cross-section. All three produce a diameter, and all three then have to be checked against the backwash flow the site can supply at that diameter — which is often what really decides the size.
Freeboard is the empty space left above the settled media bed. During backwash, flow is reversed upward at a rate high enough to lift and fluidise the bed so trapped solids are released and carried to drain — and a fluidising bed expands, commonly by around half its settled depth again.
Without room for that expansion, media is driven into the top distributor and out of the vessel on every backwash. The symptoms are media appearing downstream, a bed depth that falls steadily over months, and filtration quality that declines without any obvious fault. Size the vessel for the media volume plus expansion rather than filling it to the volume available.
Top mount multiport valves are simple, compact and economical, and they cover the commercial range well — broadly up to the 16 to 18 inch diameters. Above that the valve's own flow capacity becomes the constraint, particularly during backwash, when the required flow is much higher than in service.
Side mount valves — a nest of valves or individual butterflies on face piping — pass far more flow and give independent control of each stage. They cost more and take more space, and they are the right answer on larger diameters, on high backwash rates, and where the plant wants to sequence stages independently. The changeover point is a flow question rather than a fixed diameter, so it is worth checking against the actual backwash rate.
Enough to fluidise the bed, which for sand and anthracite is broadly in the region of 25 to 45 cubic metres per hour per square metre of vessel cross-section, varying with the media, its grain size and the water temperature. Multiply that by the area of your vessel diameter and you have the flow the site must deliver, at pressure, for ten to fifteen minutes.
Temperature matters more than people expect: cold water is denser and fluidises the same bed at a lower flow, so a backwash rate set in summer can be too vigorous in winter and carry media out, while one set in winter can fail to clean the bed in summer. Where the site cannot supply the required flow, a smaller diameter with a deeper bed, a dedicated backwash tank and pump, or splitting the duty across two vessels are the realistic options.
Yes, and most enquiries here are for the complete set rather than for a bare tank. Manual and automatic multiport valves, side mount arrangements, top baskets, hub-and-lateral underdrains, riser tubes, graded sand and gravel, anthracite, activated carbon, manganese media, softening resin, brine tanks and the associated fittings are all supplied together.
Tank and valve are frequently different makes, so the opening thread or flange is checked against the valve at quotation rather than assumed. For a replacement, send the existing vessel size and the valve make and model, along with a photograph of the top opening where you can.
Sourcing and distribution enquiries are supported for reputed global and domestic brands including Pentair (Structural), Canature, Wave Cyber, Aquatrol, Runxin, Clack, UKL and Shubh, along with equivalent options.
This is subject to stock availability, buyer specification, technical compatibility and documentation, and does not indicate authorised distribution, official dealership or an exclusive partnership with any brand.
Yes. Dispatch is coordinated across Delhi NCR, Gujarat, Maharashtra, Tamil Nadu, Telangana, Karnataka, West Bengal and other industrial corridors, covering commercial, institutional, plant and municipal sites.
Vessels are light for their size but bulky, so freight is priced on volume rather than weight, and media is the opposite — sand and resin are heavy and often ship separately. Confirm plant room access and headroom before dispatch, including the clearance needed above the vessel to remove the control valve for service. Lead time is confirmed per line item at quotation stage.
The stages either side of a media filter, and the components specified with it.
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