Applications

Steam Strainers
and Condensate Strainers

Steam carries little dirt – but what it does carry arrives at high velocity and high temperature. After installation and overhaul it is weld spatter, scale and chips; in operation, rust and boiler scale. We design steam strainers and condensate strainers for your line and build them to match.

Stainless steel process plant in piping construction with angle seat valve, ball valve and Y strainer for steam and condensate on tyre presses

Strainer type

Y strainer · T-type strainer

Gasket

Graphite with tanged steel insert

Temperature

always a custom design

During start-up

Witch hat strainer

Why steam needs different strainers from water

Two things set steam apart from almost every other medium. First, the low dirt load: in normal operation a steam system carries few solids, so the screen area does not need to be large. A Y-pattern strainer is usually the economical answer here. Second, the temperature – it shifts the design completely away from the standard.

As standard, our strainers are designed for −10 to +50 °C. Steam is always above that. This makes every steam design a custom design. Material and wall thickness are calculated for the operating temperature, the gasket must withstand it permanently, and the closure must not loosen during heating up. That is why graphite with tanged steel insert is the standard gasket here, not an elastomer gasket.

In condensate the picture is partly reversed. The temperature is lower, but rust, boiler scale and – in heating and district heating circuits – magnetite are added. Magnetite is so fine that it passes even the finest wire mesh; the only remedy is a magnetic rod in the strainer basket.

  • Low dirt load: the Y shape is usually sufficient
  • Temperature above the standard – always a separate design
  • Graphite with tanged steel insert instead of an elastomer gasket
  • Drain, so that condensate can run off
  • Insulation against heat loss and contact
  • Magnetic rods against magnetite in the condensate circuit

What is protected here

The mesh size does not depend on the steam but on the component downstream. These are the most common points of use in steam and condensate systems.

In the steam system

  • Control valves and pressure reducing valves with narrow seats
  • Steam turbines and steam ejectors
  • Heat exchangers and pasteurisers
  • Humidifiers and spray nozzles
  • Flow measurement and meters

In the condensate system

  • Steam traps with small orifices
  • Condensate pumps on the suction side
  • Feedwater tanks and boiler feed pumps
  • Plate heat exchangers in district heating circuits
  • Return lines carrying rust and magnetite

Strainer types for steam and condensate

Which type fits is decided by the dirt load and by whether cleaning has to take place during operation.

Stainless steel Y strainer with butt-weld ends, for example for steam and condensate lines

Y strainer

the usual choice in steam systems

The Y-pattern strainer is short, inexpensive and has enough screen area for the low dirt load in steam. It is installed inclined or horizontally so that the strainer basket does not fill with condensate. Heated version on request.

Stainless steel protective screen DN200 as strainer element for the T-type strainer in steam and condensate lines

T-type strainer

when more area is needed

For the same face-to-face length, the T shape puts more screen into the line and is easier to clean. The cover gives access to a screen plate that can be pulled straight out. It is supplied with drain and vent plugs, and with butt-weld ends on request.

Stainless steel basket strainer DN250 PN40 with lifting lug, designed for steam and hot water

Basket strainer

for high dirt loads

Where more dirt occurs – for example in plants with older piping or after modifications – the pot shape offers many times the screen area. An example from our production: DN250 and DN500 in PN40, designed for 22 bar at 323 °C with a mesh size of 0.2 mm.

Duplex strainer DN80 in stainless steel, steam-heated, with changeover via manually operated 3-way ball valves, for steam and condensate

Duplex strainer

cleaning without downtime

Two chambers, one in operation, one on standby. Switch over, open the isolated side and clean it while the plant keeps running. In a steam system this makes sense wherever an interruption is costly. One example from our production is a steam-heated changeover strainer DN80.

Witch hat strainer DN300 PN25 in stainless steel with 1 mm mesh size as a temporary strainer for steam and condensate

Witch hat strainer for start-up

weld spatter, scale, chips

After installation and overhaul, the dirt load is many times higher for a short time. A witch hat strainer is placed between the flanges in the steam line as a temporary strainer, catches the coarsest debris and comes out again after the start-up phase. It has more area and less pressure loss than a flat plate strainer.

Technical data

Every steam design is calculated. The following data show the scope and examples from our production.

Feature or exampleValueNote

Design

Temperatureabove the standardstandard range −10 … +50 °C, steam always above
Pressure ratingPN6 – PN40PN63 as high-pressure design
Gasketgraphite with tanged steel inserttemperature-resistant, standard on basket, simplex, duplex and T-type strainers
HousingP235GH · P250GH · 1.4571according to temperature and medium
Installation positioninclined or horizontalso that no condensate stands in the basket

Examples from our production

Basket strainer DN250 · DN500PN4022 bar at 323 °C, mesh size 0.2 mm
Y-pattern strainer DN40PN25grey cast iron, for steam

Condensate

Filtration gradefiner than in steamoften around 50 µm in designs
Magnetitemagnetic rods in the strainer basketno wire mesh retains fine ferritic particles
Drainat the lowest pointcondensate must be able to run off

During start-up

Witch hat strainerperforated plate conemore area, less pressure loss
Flat plate strainerflat screen ringfor short start-up phases
Afterwardsremoval or replacementa temporary strainer does not stay in continuous operation

The strainer is not a pressure vessel for the differential pressure

A strainer element does not withstand the operating pressure of the housing – it only withstands the pressure difference between inlet and outlet. If it clogs, this difference rises, and at some point the basket deforms. On our basket strainers the permissible differential pressure is a maximum of 2 bar; in operation we recommend no more than 0.5 bar. In a steam system this is particularly important, because the condition of the screen cannot be seen from the outside. A differential pressure gauge costs little and turns an assumption into a measurement.

Frequently asked questions

That does not depend on the steam but on what is downstream. For a control valve with a narrow seat, a finer mesh is chosen than for a heat exchanger with wide channels. Tell us the component to be protected and, if known, its smallest opening – from this we derive the filtration grade.

In normal steam operation the Y shape is usually sufficient, because few solids occur. A high dirt load, older piping, a modification to the plant or the wish to clean less often speak in favour of a basket strainer. If the plant is to keep running during cleaning, the choice is the duplex strainer with changeover.

Because our standard design covers −10 to +50 °C. A higher temperature affects material properties, wall thickness, gasket and closure – this is calculated for your case and recorded in the drawing, which you approve before manufacture.

Graphite with tanged steel insert: graphite layers on a steel carrier, temperature-resistant and resistant to creep relaxation. It is the standard gasket on basket, simplex, duplex and T-type strainers. Elastomers are ruled out in steam.

Only magnetism. Fine ferritic particles are smaller than any reasonable mesh size and pass even the finest wire mesh. Magnetic rods in the strainer basket retain them and are easy to wipe clean during cleaning.

After installation or overhaul, yes. Weld spatter, scale and chips would clog the permanent strainer within a short time or damage the plant. A witch hat strainer between the flanges catches them and comes out again afterwards – it has more area and less pressure loss than a flat plate strainer.

As a rule, yes – against heat loss and as protection against contact. Removable insulation jackets are recommended on the strainer, because the cover must be accessible for changing the screen. Where the medium cools down or precipitates during downtime, a heating jacket can also be considered.

Yes. Before production starts, you receive the design drawing for approval – with design data, materials, gasket and attachments. Only after your confirmation does the order go into production.

Matching options

All topics at a glance: Options

Design

Mesh size and filtration grade

Details →

Housing and handling

Gaskets

Details →

Monitoring

Differential pressure

Details →

Flow path

Drain and vent

Details →

Temperature control

Insulation and lagging

Details →

Design

Special designs

Details →

Design your steam or condensate line

Tell us the steam pressure and temperature, the nominal size and the component to be protected. You will receive a design proposal with strainer type, mesh size and options.

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