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Equipment Selection & Datasheets

Process Design & P&IDs — in depth

Process design culminates in equipment selection. Each item — pumps, blowers, mixers, screens, dosing — is chosen on duty point, materials, efficiency and whole-life cost, then captured on a datasheet that defines the procurement specification, so what is bought matches what was designed.

Selection Basis

What matters in practice

Duty Point

Flow, head and load define the selection.

Materials

Matched to fluid and environment.

Efficiency

Energy and lifecycle cost considered.

Datasheets

Procurement-ready specifications.

Datasheet Content

FieldPurposeNote
DutySizingFlow/head/load
MaterialDurabilitySpec
PowerEnergyEfficiency
StandardsComplianceCodes

Related Topics

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Reynolds & Bauhm designs and delivers process design & p&ids solutions backed by process engineering and performance guarantees.

Equipment Selection & Datasheets: Engineering Detail

Fundamentals, design drivers and practical guidance

Equipment selection and datasheets — choosing each unit on duty, materials and lifecycle cost, and specifying it for procurement.

The hydraulic profile sets the elevations so water flows through the works against friction and unit head losses with adequate freeboard, minimising intermediate pumping; the P&IDs then formalise instrumentation, control philosophy, interlocks and safety. Equipment selection weighs capital against operating cost, robustness, turndown and maintainability — choosing technology that suits the operator's site and skills, not just the lowest tender.

Reynolds & Bauhm develops plant designs from a rigorous mass balance through hydraulic profile, P&IDs and equipment selection, so the works is sized for its true duty, flows correctly, and is specified for whole-life cost and operability.

Process plant design turns an effluent characterisation and a discharge consent into a buildable, operable works, and it proceeds through recognisable deliverables: mass balance, hydraulic profile, P&ID development and equipment selection. Each builds on the last — the mass balance sizes the duties, the hydraulic profile makes them flow by gravity where possible, the P&IDs capture control and safety, and equipment selection commits the technology.

Design & Specification Considerations

What our engineers assess on every scope of this type

  • Turndown, redundancy and maintainability
  • Operability for the site's skills and resources
  • Mass balance of flows and loads through every unit
  • Solids and recycle streams explicitly accounted for
  • Hydraulic profile to minimise intermediate pumping
  • Freeboard and surcharge margins under peak flow
ParameterTypical basisWhy it matters
TurndownRange of dutyHandles diurnal/seasonal swing
OperabilitySuited to operatorKeeps the plant runnable
Mass balanceFlows + loads trackedSizes every unit to real duty
Hydraulic profileElevations + lossesFlow by gravity where possible
P&IDsControl + interlocksFormalises operation and safety
EquipmentWhole-life basisBalances capex and opex

Frequently Asked Questions

Common questions on treatment plant design

Why develop P&IDs in detail?

P&IDs formalise the control philosophy, instrumentation, interlocks and safety functions. They are the reference that procurement, commissioning and operations all work from, so getting them right early prevents rework.

How is equipment selected?

On whole-life cost, robustness, turndown and maintainability — matched to the operator's site and skills — not simply the lowest capital tender. The cheapest item often costs the most to run.

Why size for turndown?

Real plants see diurnal and seasonal swings in flow and load. Designing for turndown, with appropriate redundancy, keeps treatment stable and efficient across the full operating range, not just at average duty.

Why start with a mass balance?

Because it sizes everything — flows and loads through each unit, including solids and recycles. Equipment Selection & Datasheets and every downstream deliverable depend on a correct balance, so it is built and checked first.

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