Delivering advanced energy engineering so industrial facilities operate cleaner, smarter, and more profitably.

Find where energy and money are actually leaving the plant, then engineer the fix.

• Audits & modeling — steam, condensate, and energy audits backed by full system balance models.
• Optimization & solutions — targeted measures to cut energy and utility cost and eliminate LP steam venting.
• Specialized system support — boilers, high-temperature furnaces, kilns, asphalt systems, and refinery fuel usage.
• Troubleshooting & safety — resolution of complex faults, including water hammer in process plant steam systems.

Turn the recommendation into a design package that contractors can bid and build against.

• BDS development — comprehensive Basic Design Specification packages for technical proposals.
• Design peer review — critical review and refinement of engineering scopes drafted by third parties.
• Package reviews — detailed design and bidding packages checked for alignment and quality.
• Implementation guidance — engineering oversight and support through project execution.

Prove the savings landed, then build the habits and instrumentation that hold them.

• Commissioning support — pre-commissioning reviews, system testing, and full commissioning.
• Performance validation — stabilized operation to establish and verify the savings achieved.
• Monitoring programs — durable measurement and monitoring frameworks for energy efficiency.
• Training & culture — energy-cost awareness across personnel, with client engineers involved directly in the work.

497,000 GJ cut from an ammonia plant's steam system

A US DOE Save Energy Now assessment at the Verdigris, Oklahoma plant led to upgraded condensing turbines, a new loop dehydrator, and a steam trap and leak repair program.

Result

$3.5M saved a year

Outcome

11-month payback

A no-capital load strategy for a UK refinery's steam balance

Costing every turbine drive against its electric motor alternative showed which units to switch as low-pressure steam went to vent — cutting the ethane compressor from $84.84/hr to $12.60/hr when exhaust steam is fully used.

Result

$30k saved a year

Outcome

Zero capital spend

500 kW recovered by retiring an obsolete desuperheater

After a waste-heat boiler was tied in, combined steam to the extraction-condensing turbine stayed below its 660°F inlet limit — so desuperheating could be safely bypassed and the lost work returned to the generator.

Result

$400k saved a year

Outcome

Piping change only

A cooling tower replacement avoided by rerouting makeup water

Boiler makeup water at 115–150 gpm almost exactly matched the air compressor's 120 gpm cooling duty, so it was routed through the compressor to preheat feedwater and the failing tower was blinded off.

Result

$80k saved a year

Outcome

Live in two months