METHOD / FROM MODEL TO SPECIFICATION

See the event.
Design the response.

Pressure transients are system events. We model the whole line, identify the governing cases, and test protection until the results become practical design decisions.

01 / THE MODELTHE SYSTEM AS BUILT

Start with the
real pipeline.

Route levels, pipe properties, reservoir boundaries and pump curves establish the steady state. Every transient result depends on this baseline being right.

Example KYPipe model with pump and pipeline data

Example model build from a delivered study

01

Geometry

Chainage, bore, material and high points along the whole route.

02

Pumps

Duty points, curves, rotating inertia and operating combinations.

03

Boundaries

Reservoir levels, valves and existing protection devices.

02 / THE TRANSIENTSAME TRIP / TWO OUTCOMES

The whole line
responds.

A power failure at the pumps can create both vacuum and high rebound pressure. The study locates where each limit is reached and how long the event develops.

Unprotected: column separation and rebound toward 850 m of head
Protected: surge vessel and air-valve scheme in service

These are actual solver outputs from the existing project material; the homepage animation is conceptual.

03 / THE DESIGNSIZE / PLACE / VERIFY

Protection that has
a specification.

The report identifies the required protection and checks its effect in the model. Recommendations include sizes, positions and operating behavior, not just a device category.

01

Surge vessels

Volume, pre-charge and connection at the pump station.

02

Air valves

Type, size and chainage at critical summits.

03

Valve closing laws

Closure times and sequences checked against the governing event.

04 / THE HANDOVERONE REPORT / FOUR ANSWERS

Enough detail to
act on.

You receive a laid-out PDF report, model files and tabulated output. The conclusion should be readable by an operator; the calculations remain available to the reviewer.

Opening page of an example surge analysis report

Pages from an example delivered report

01

Steady state

Pump duty, hydraulic grade and static pressure.

02

Unprotected

Maximum and minimum head envelopes and critical locations.

03

Protected

Verified scheme with equipment schedule.

04

Summary

Plain-language decision and practical commissioning notes.

ENGAGEMENTPRICED AGAINST A DEFINED SCOPE

Scope before
work begins.

The simplest single-pipeline study starts at USD 600. Network systems and additional pump combinations are quoted on top before the study starts.

SINGLE PIPELINE

Focused study

One main, one station and standard transient scenarios.

From USD 600
NETWORK

Multi-system scope

Several mains, pump combinations, branches or complex protection.

Quoted
SECOND OPINION

Review

Independent check of assumptions, model build and protection sizes.

From USD 350
START WITH YOUR SYSTEMDATA SHEET / FIVE TABS

Get the data
in one place.

The input sheet covers pump data, boundaries and pipeline profile. It gives the study a faster, clearer start.