Enhanced Heat Exchanger

porous coated tube exchanger

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Technical Principles

Porous coated tube heat exchangers use high efficiency heat exchange tubes with metal sintered porous layers to provide a large number of vaporization cores for enhanced boiling heat transfer.

During the Boiling Process

Liquid contacts the porous heat transfer surface and is rapidly heated to saturation temperature.
A large number of bubbles nucleate, grow, and detach simultaneously within the micro-pores, creating a bubble jetting effect.
Bubble motion, combined with capillary flow through the microchannels, continuously renews the liquid film and increases turbulence, reducing the thermal boundary layer.
Under operating conditions, the overall heat transfer coefficient is significantly improved, enabling a 40%–60% reduction in required heat transfer area and equipment size.

Performance Advantages

Boiling heat transfer coefficient increased by 3–10 times
Lower superheat required, enabling stable heat transfer even at small temperature differences
Higher critical heat flux for improved operating stability and performance

Typical Applications

Technical Performance – Enhancement Comparison

Equipment Tag/Name
LMTD, ℃
Tube Type
Dimensions, mm
Total Area, m²
Qty. (Units)
XX Unit Propylene
Column Reboiler
6.9
High Flux Tube
DN2100x10500
5408
2
Plain Tube
DN2800x12000
11541
2
Equipment Tag/Name
LMTD, ℃
Tube Type
Dimensions, mm
Total Area, m²
Qty. (Units)
XX Unit
benzene column reboiler
5.6
Internally sintered
high-flux tube
DN2700×6000
2073
1
Plain tube
DN3600×6000
7608
2

Case Data

Waste Heat Recovery for a Syngas-to-Ethylene Glycol Plant
a. Converting Waste Heat into Valuable Steam
For a 600,000 tpa syngas-to-ethylene glycol facility, our high-flux tube waste heat boiler was deployed to recover overhead vapor energy from the alcohol removal and product distillation towers, converting previously wasted heat into usable low-pressure steam.
b. Technical Approach
Conventional Process
Tower overhead vapors were cooled by circulating water, resulting in high utility consumption and wasted thermal energy.
Optimized Solution
Tower overhead vapors were cooled by circulating water, resulting in high utility consumption and wasted thermal energy.
Key Advantage
A minimum temperature approach of only 6.9–9.9°C, enabling higher steam quality and improved heat recovery efficiency.
c. Project Results
- Steam generation: up to 135 t/h of low-pressure steam
- Direct steam reuse: 90.5 t/h used to replace 0.5 MPa(g) steam in the methanol recovery tower reboiler
- Steam consumption reduction: approximately 1.2 tons of steam per ton of ethylene glycol produced
- Additional steam available: 44.5 t/h for steam upgrading, power generation, or absorption cooling
d. Annual Benefits  (Based on 8,000 operating hours/year)
- Standard coal saved: 96,448 tons/year
- CO₂ emissions reduced: 256,552 tons/year
- Annual economic benefit: RMB 122.56 million
e. Conclusion
By recovering medium- and low-grade waste heat from tower overhead vapors, the system converts lost energy into usable steam, reducing operating cost, lowering emissions, and improving plant energy efficiency. It provides a practical decarbonization solution for coal-to-ethylene glycol and syngas-based chemical facilities.