Design · Fabrication · Commissioning

Industries served

Every sector has one constraint that governs

In a refinery it is code compliance and turnaround access. In a dairy it is cleanability. In a desalination plant it is chlorides. Knowing which constraint governs is most of the design decision — so here is how we read each sector.

Oil & gas

Upstream, midstream and refining

The governing constraints are code compliance, sour service where H₂S is present, and the fact that you only get access during a turnaround. Equipment has to be inspectable within that window.

  • Two- and three-phase separators with sized internals
  • Knock-out drums ahead of compressors and flares
  • Gas coolers and aftercoolers, air-cooled or water-cooled
  • Process exchangers in floating-head configuration for full cleaning access
  • Produced water and slug catcher vessels
  • Condensate and surge drums

Where sour service applies, material selection and hardness control follow NACE requirements — tell us at enquiry stage so it is designed in, not bolted on.

Vertical pressure vessel drawing typical of a separator or knock-out drum
Vertical separator arrangement with manway and skirt support
Jacketed reactor drawing typical of petrochemical batch processing
Jacketed reactor with utility annulus and agitation

Petrochemical & chemical

Where the fluid attacks the equipment

Corrosion drives everything. The right answer is often not the most exotic alloy but the cheapest one that survives the actual service — and knowing the difference is worth real money on a large order.

  • Jacketed and limpet-coil reactors with integrated agitation
  • Process exchangers in stainless, duplex and nickel alloys
  • Chemical storage tanks with lining systems
  • Dosing and blending skids
  • Column internals, reboilers and condensers
  • Clad and weld-overlay construction where solid alloy is uneconomic
See reactors

Food & beverage

Cleanability beats every other consideration

Hygienic design is geometry, not polish. Fully drainable, no dead legs, no crevices for product to lodge in, and every internal surface reachable by the CIP spray pattern.

  • Sanitary shell & tube and tube-in-tube exchangers for pasteurising and cooling
  • Jacketed mixing, holding and blending tanks
  • CIP skids with heating, dosing and return
  • Storage and buffer tanks in polished 316L
  • Brewery and distillery vessels
  • Double tubesheet construction where cross-contamination is unacceptable

Internal surface finish is measured and recorded to the Ra value you specify, not described as “food grade” and left at that.

Agitated mixing tank drawing typical of food and beverage processing
Agitated mixing vessel with drainable dished bottom
Polished jacketed reactor drawing typical of pharmaceutical manufacture
Jacketed reactor with thermowell and bottom discharge valve

Pharmaceutical

If it is not documented, it did not happen

The equipment matters, but the paperwork is what gets it into a validated plant. Surface finish, material traceability, weld records and slope-to-drain all have to be evidenced.

  • Electropolished and mechanically polished reactors and vessels
  • Documented Ra measurements on all product-contact surfaces
  • Full material traceability including gaskets and seals
  • Orbital-welded and crevice-free internal joints
  • Slope-to-drain geometry with verified drainability
  • Documentation packages to support IQ and OQ

Water & desalination

Chlorides decide the material list

Ordinary austenitic stainless pits and cracks in seawater. This is the one sector where specifying 316L out of habit will cost you the equipment.

  • Titanium Gr. 2 exchangers for seawater, brine and hypochlorite
  • 90/10 and 70/30 cupronickel bundles for marine cooling
  • Duplex 2205 vessels and piping for brackish and high-chloride duty
  • Chemical dosing tanks and skids — acid, caustic, antiscalant, hypochlorite
  • Fire-water and process water storage tanks
  • Rubber- and epoxy-lined carbon steel where lining beats alloy on cost
Material selection guide
Storage tank drawing typical of water treatment and desalination service
Flat-bottom storage tank with level gauge and access stairway

Power & utilities

The boiler house and the machine hall

Lube-oil coolers

Turbine and compressor lube-oil cooling, water-cooled or air-cooled.

Generator & jacket coolers

Engine jacket water and generator cooling for gensets and CHP plant.

Steam condensers

Surface condensers and auxiliary condensing duty.

Deaerators

Storage sections and vent condensers for boiler feedwater.

Blowdown vessels

Flash and blowdown vessels with heat recovery where it pays.

Air receivers

Instrument and service air storage with correct drainage and relief.

HVAC & general industrial

Utility-side heat transfer

Compressor aftercoolers

Intercoolers and aftercoolers with condensate separation.

Chiller-side exchangers

Plate-and-frame alternatives in shell & tube for higher pressure duty.

Heat recovery

Recovering waste heat to preheat water, air or process feed.

Hydraulic oil coolers

Press, injection moulding and heavy machinery oil cooling.

Injection moulding

Mould temperature control and tool cooling circuits.

Buffer vessels

Thermal buffers and expansion vessels for closed circuits.

Cement, fertiliser & minerals

Abrasion, dust and high temperature

Hoppers & silos

Conical and pyramidal discharge with wear plate and flow aids.

Gas cooling

Cooling dust-laden gas streams ahead of filtration.

Ducting & cyclones

Ducting, expansion joints, cyclones and stacks.

Slurry tanks

Agitated slurry hold-up with rubber lining or wear allowance.

Heat recovery

Waste heat recovery from kiln and cooler exhaust.

Acid service vessels

Phosphoric and sulphuric duty in lined or alloy construction.

Not sure which constraint governs your duty?

Describe the service. We will tell you what will actually limit the design.

WhatsApp