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Chemical & process engineering · Gulf Coast, USA

Process designthat scales.

Since 1998 · Houston, Texas

We are 142 chemical engineers who turn molecules, mass balances and P&IDs into plants that start up on schedule — and stay safe for the next forty years.

Refinery skyline on the Houston Ship Channel seen from the water

Owner's engineer for Gulf Coast refiners, olefins producers and specialty chemical makers. We run the simulation, chair the safety study and stay through commissioning.

PE-licensed engineers
61
Units revamped
380+
States licensed
14

Capabilities

Six disciplines,one accountable team.

01

Process design & simulation

Steady-state and dynamic models in Aspen HYSYS and Aspen Plus, heat & material balances, pinch analysis and equipment sizing.

  • H&MB
  • Pinch
  • Dynamics
02

FEED & detailed engineering

PFDs, P&IDs to ISA-5.1, datasheets, line lists and Class 3 estimates (AACE 18R-97) that survive the EPC handover.

  • PFD/P&ID
  • Datasheets
  • AACE
03

Process safety

PSM compliance under OSHA 1910.119, PHA revalidation and relief system design. Our HAZOP facilitators assign SIL ratings to every node.

  • HAZOP
  • LOPA
  • API 520/521
04

Debottlenecking

Column hydraulics, exchanger rerates and H2SO4 alkylation revamps — 42 MMBTU/hr of recovered duty and 3.1 Btu/h per bbl saved at our last Texas City job.

  • Rerates
  • Hydraulics
  • Revamps
05

Mechanical integrity

Fitness-for-service to API 579, corrosion loops and pressure vessel design to API 650 for new and rerated equipment.

  • FFS
  • RBI
  • Corrosion
06

Decarbonization

CCUS front-end studies, blue hydrogen and ammonia, electrified heaters and 45Q-ready CO2 capture basis of design.

  • CCUS
  • H2/NH3
  • 45Q

How a revamp flows

Read the plantlike we do.

A simplified hydrotreater loop. Hover or tap any equipment tag to see its design case. This is the same way we walk owners through a FEED package.

Simplified process flow diagram: feed drum, charge pump, feed/effluent exchanger, fired heater, reactor, high-pressure separator and stripper column D-101 P-101 E-101 H-101 R-101 V-102 T-101 1 2 3 4 5 H2 recycle Off-gas ULSD Straight-run diesel
Stream summary (design case)
StreamDescriptionTempPressureFlowPhase
1Fresh feed120 F45 psi148,500 lb/hLiquid
2Charge to E-101125 F1,050 psi148,500 lb/hLiquid
3Heater outlet650 F985 psi161,200 lb/hMixed
4H2-rich gas115 F235 psi9,850 lb/hVapor
5ULSD product110 F65 psi142,300 lb/hLiquid

Free engineering tool

Pipe-flowquick check.

Reynolds number and flow regime for a liquid line. Handy for checking a line list before the hydraulics model runs.

Re = ρ · v · D / μ

Reynolds number—
—
26years on the Gulf Coast
0.21TRIR, 2025
1.9billion USD of capex engineered
97%on-time FEED delivery

Bench → pilot → plant

Scale-up is adiscipline, not a guess.

01 · BenchKinetics, VLE data and lab reactor trials at 0.5 L.
02 · PilotContinuous pilot runs and a fitted model for the scale factor.
03 · PlantBasis of design, FEED and start-up support at 40 kTA.

Selected Gulf Coast work

Texas City, TX · 2025

Alkylation unit revamp

+18% alkylate yield, same plot space, a 21-day turnaround.

Baytown, TX · 2024

Ethylene cracker debottleneck

Furnace coil and quench tower rerate for +12% throughput.

Pasadena, TX · 2024

Hydrotreater FEED

ULSD revamp with a new reactor and an 1,100 psig recycle compressor.

Houston Ship Channel · 2023

Terminal vapor recovery

Marine loading VCU sized for 40 CFR 63 Subpart Y.

Deer Park, TX · 2023

PSM program rebuild

212-node PHA revalidation and a relief study across 1,480 PSVs.

01 / 05

Leadership

Licensed engineers,on your unit.

Rachel Okafor
Rachel Okafor, PEPrincipal · Process design
James Whitaker
James Whitaker, PE, CCPSCProcess safety lead
Marcus Delgado
Marcus DelgadoSimulation lead · Aspen
Elena Brooks
Elena Brooks, PEDecarbonization · CCUS

Request a proposal

Tell us aboutthe unit.

A principal engineer replies within one business day. NDAs are signed before any P&IDs change hands.

Scope