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

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 s heat transfer even at small temperature differences
Higher critical heat flux for improved operating stability and performance

Typical Applications

Porous coated tube heat exchanger is sui for clean materials with low temperature difference, low viscosity and low surface tension.

Currently, this product is mainly used in the reboiler and condenser in ethylene unit, gas separation unit, propane dehydrogenation(PDH) unit,catalytic cracking unit, catalytic reforming unit, arena unit and methanol toolefin(MTO) unit.

Case Data
01/01
Waste Heat Recovery for a Syngas-to-Ethylene Glycol Plant

a. Converting Waste Heat  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  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  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.