Industrial Thermal Systems

Precision Heat Transfer for
Petrochemical Processing

Engineering shell-and-tube heat exchangers and cooling towers with calculated fluid dynamics and mass transfer coefficients to prevent scale buildup and optimize heat dissipation under high-pressure regimes.

Operating pressure range: up to 350 bar

Thermal efficiency gain: 22% vs standard designs

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Ready to optimize your thermal system?

We calculate precise fluid dynamics and mass transfer coefficients for your specific process conditions. One conversation can prevent scale buildup and improve heat dissipation efficiency under high-pressure regimes.
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Frequently Asked Questions

Clear answers about our thermal systems engineering, fabrication, and maintenance services for petrochemical processing.

We specialize in shell-and-tube heat exchangers designed for high-pressure petrochemical environments. Our units are engineered with precise fluid dynamics calculations to prevent scale buildup and optimize heat dissipation. We fabricate fixed tubesheet, U-tube, and floating head configurations, all built to ASME Section VIII standards with full material traceability.

We use the Merkel method combined with computational fluid dynamics (CFD) modeling to determine the mass transfer coefficient. This accounts for air velocity, water loading, packing geometry, and ambient wet-bulb temperature. The result is a tower design that achieves the required approach temperature while minimizing drift loss and water consumption.

Our maintenance team performs tube bundle cleaning, retubing, pressure vessel inspection, and cooling tower fill replacement. We also offer performance testing to measure heat transfer efficiency and identify fouling or scaling issues before they cause unplanned downtime. All work follows API 510 and API 653 guidelines.

Yes. We custom fabricate pressure vessels for high-temperature, high-corrosion, or cyclic service. Our engineers select materials such as stainless steel, duplex alloys, or nickel-based alloys based on your process fluid composition and operating pressure. We also design for both vertical and horizontal orientations with multiple nozzle configurations.

Scale prevention starts with accurate fluid dynamics modeling to maintain turbulent flow and avoid stagnant zones. We also recommend appropriate tube-side velocity and can integrate chemical dosing ports for inline water treatment. For existing units, we offer mechanical cleaning and chemical descaling services to restore thermal performance.

Lead time depends on complexity and material availability. A standard shell-and-tube unit typically takes 12 to 16 weeks from design approval to delivery. Custom pressure vessels with exotic alloys may require 20 to 24 weeks. We provide a detailed project schedule at the quotation stage and keep you informed throughout fabrication.

Engineering advantages

Precision thermal performance for petrochemical duty

Every exchanger is modeled for real-world fluid dynamics and fouling resistance.
01

Fouling mitigation through tube-side velocity control

We calculate the exact flow regime — typically 1.5–2.5 m/s — to keep suspended solids moving and prevent scale nucleation on tube walls. This extends cleaning intervals by up to 40%.

Reduced downtime for hydroblasting.
02

Shell-side baffle geometry for minimal pressure drop

Segmental baffles are spaced and cut to maintain cross-flow without dead zones. The result: a pressure loss under 0.7 bar at design flow, even with high-viscosity hydrocarbons.

Lower pumping cost per barrel processed.
03

Mass transfer coefficient validation per TEMA class R

We run a full Wilson plot analysis on every prototype to confirm the U-value matches the specification. This guarantees the exchanger meets the required duty within ±5%.

No over‑sizing or performance shortfall.
04

Thermal stress compensation at high ΔT

Floating tube sheets and expansion bellows absorb differential expansion between shell and tubes when inlet temperatures exceed 350 °C. This prevents tube‑to‑sheet joint fatigue.

Service life beyond 15 years in coker units.
05

Cooling tower fill selection for wet‑bulb approach

Film fills with 18 mm flute pitch are chosen for heavy process water. The design achieves a 5 °C approach to wet‑bulb while keeping drift below 0.002% of circulation rate.

Compliance with EPA 316(b) and local discharge limits.
06

Weld procedure qualification for sour‑service alloys

All carbon‑steel and stainless‑steel joints are qualified per ASME Section IX with Charpy V‑notch testing at −20 °C. This ensures crack‑free fabrication for H₂S‑laden streams.

Safe operation in amine and sulfur recovery units.
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