Design basis
Inputs include protected-system MAWP and design pressure, credible overpressure scenarios, source pressure, process dynamics, required response time, safe-state definition, demand rate and target risk reduction.
Process Safety Packages · ENGINEERED SCOPE
A HIPPS is an instrumented protection system intended to prevent downstream overpressure by detecting a hazardous pressure condition and rapidly isolating the pressure source. It is engineered as an independent protection layer only after the relief and flare philosophy has been established.

Engineering approach
A technically defined package begins with the operating envelope—not a catalogue model.
Rated capacity, minimum stable load, feed envelope, inlet and outlet conditions, product specification, start-up and shutdown cases, design life and acceptance criteria are agreed before equipment definition is frozen. Package basis also fixes battery limits, skid envelope, lifting and shipping constraints, utility tie-ins, FAT scope, preservation requirements and commissioning deliverables.
Inputs include protected-system MAWP and design pressure, credible overpressure scenarios, source pressure, process dynamics, required response time, safe-state definition, demand rate and target risk reduction.
The package typically integrates redundant pressure transmitters, a safety logic solver, final isolation elements, partial-stroke testing, dedicated panels and diagnostics. Voting architecture and independence are derived from the SIL lifecycle and project standards.
Verification includes hazard analysis inputs, SIL allocation and validation, response-time calculation, valve closure transient, common-cause review, bypass control, proof-test interval, cybersecurity interfaces and functional-safety documentation.
PROJECT DEFINITION · DELIVERY
Technical proposal quality depends on verified process data, acceptance criteria and interface definition. The following information is confirmed during clarification.
RFQ
Share the operating cases, feed data and required guarantee so the applicable process route, package boundary and verification plan can be defined.
Technical Datasheet
The figures below are published valve-system options and a certified-system integrity example. They are not universal HIPPS design values or proof that any configured loop meets SIL requirements.
| Parameter | Published value | Basis / secondary data | Application limit |
|---|---|---|---|
| Available mainline valve sizes / pressure options | 1½–60 in; ASME Class 150–2500 | Published range of a valve family offered for HIPPS; API options also vary by series. | Valve size and rating are component selections, not a pressure/flow capacity band for the whole HIPPS. |
| System integrity / closure-time example | SIL 3; closure down to 2 s | Published certified-system offer and fast-closure option. | SIL is achieved only for the verified safety function and complete loop under the project SRS, PFDavg, proof-test and lifecycle requirements. |