# Heat exchangers and pinch integration: Science and thermodynamics

Why low-temperature heat needs such huge exchangers

Source page: https://www.materialinsights.org/energy/e_heat_exchangers/rc-sci/

What this tab covers The thermodynamics: the grade (temperature or pressure) of the energy being recovered, energy versus exergy efficiency, and how harsh the waste stream is on equipment.

Heat exchangers move heat from a stream that must be cooled to one that must be heated, without the two touching. Pinch analysis is the design method that matches all the hot and cold streams in a plant so that as little outside heat and cooling as possible is needed.

#### Grade of energy
Mixed

Exchangers work at every temperature, but most of the opportunity is low grade. DOE's 2008 study found about 60% of unrecovered US industrial waste heat is below 232 C. ORNL's 2021 update puts about 570 TBtu a year below 149 C and another 612 TBtu between 149 and 232 C, out of 2,244 TBtu in total. Low-temperature heat needs large exchanger areas because the driving temperature difference is small, which is why it is the hardest to use.^[2](https://www1.eere.energy.gov/manufacturing/intensiveprocesses/pdfs/waste_heat_recovery.pdf)^[1](https://info.ornl.gov/sites/publications/Files/Pub164247.pdf)
 Share of unrecovered US waste heat below 232 C about 60%^[2](https://www1.eere.energy.gov/manufacturing/intensiveprocesses/pdfs/waste_heat_recovery.pdf) US industrial waste heat below 149 C about 570 TBtu/yr^[1](https://info.ornl.gov/sites/publications/Files/Pub164247.pdf) Total US industrial waste heat (120 F reference) about 2,244 TBtu/yr^[1](https://info.ornl.gov/sites/publications/Files/Pub164247.pdf)

#### Exergy versus energy efficiency
Favourable

Exchanger effectiveness is the share of the theoretically transferable heat actually moved. Shell-and-tube units typically achieve 40 to 60%, while plate-and-frame units have three or more times the heat transfer coefficient, so they reach closer approach temperatures in less space. Every exchanger needs some temperature difference to drive heat, and that difference is where exergy is lost; a smaller approach saves more energy but needs more area and capital. Pinch analysis makes this trade-off explicit by choosing a minimum approach temperature for the whole plant, then showing the least external heating and cooling possible. Natural Resources Canada reports that process integration typically saves 10 to 30% of energy with paybacks of 1 to 3 years; its industry guide puts total potential at 10 to 25% of purchased fuel in refining and petrochemicals, 10 to 30% in iron and steel, 15 to 35% in chemicals and 15 to 40% in food and drink.^[1](https://info.ornl.gov/sites/publications/Files/Pub164247.pdf)^[9](https://natural-resources.canada.ca/energy-efficiency/process-integration-pinch-analysis)^[10](https://natural-resources.canada.ca/sites/nrcan/files/canmetenergy/files/pubs/2003-121e.pdf)
 Pinch analysis typical saving 10 to 30% of energy; payback 1 to 3 years^[9](https://natural-resources.canada.ca/energy-efficiency/process-integration-pinch-analysis) Shell-and-tube effectiveness 40 to 60%^[1](https://info.ornl.gov/sites/publications/Files/Pub164247.pdf) Plate-and-frame heat transfer coefficient 3 or more times shell-and-tube^[1](https://info.ornl.gov/sites/publications/Files/Pub164247.pdf)

#### Media compatibility and corrosiveness
Mixed

Fouling is the chronic weakness: a PNNL review of 231 patents found it remained unsolved and mostly handled after the fact. Plate units foul less than tubular ones because of their turbulence, and spiral exchangers cope with viscous or particle-laden fluids. Corrosive condensing duties use stainless steel 304 or 316, or polymer exchangers, which resist acids but are limited to about 104 C and 10 bar. Heat pipes and run-around coils (two coils linked by a pumped fluid loop) keep the streams physically apart, which suits dusty or contaminated exhausts.^[2](https://www1.eere.energy.gov/manufacturing/intensiveprocesses/pdfs/waste_heat_recovery.pdf)^[1](https://info.ornl.gov/sites/publications/Files/Pub164247.pdf)
 Patents reviewed on fouling (PNNL, 1992) 231^[2](https://www1.eere.energy.gov/manufacturing/intensiveprocesses/pdfs/waste_heat_recovery.pdf) Polymer exchanger limit about 104 C and 150 psi^[1](https://info.ornl.gov/sites/publications/Files/Pub164247.pdf) Condensing duty materials stainless steel 304 and 316^[1](https://info.ornl.gov/sites/publications/Files/Pub164247.pdf)

#### Variants compared^[1](https://info.ornl.gov/sites/publications/Files/Pub164247.pdf)^[2](https://www1.eere.energy.gov/manufacturing/intensiveprocesses/pdfs/waste_heat_recovery.pdf)^[4](https://www.aceee.org/sites/default/files/pdfs/ssi21/panel-3/Zahlan.pdf)^[10](https://natural-resources.canada.ca/sites/nrcan/files/canmetenergy/files/pubs/2003-121e.pdf)^[9](https://natural-resources.canada.ca/energy-efficiency/process-integration-pinch-analysis)

| Variant | Best for | Strength | Limitation |
|---|---|---|---|
| **Shell-and-tube** | High pressure, dirty or large duties | Robust, easy to clean mechanically | 40 to 60% effectiveness; bulky |
| **Plate-and-frame** | Liquid to liquid, clean or mildly fouling | 3 or more times the heat transfer coefficient; compact | Gasket limits on temperature and pressure |
| **Spiral** | Viscous or particle-laden liquids | Self-scouring flow resists fouling | Specialist supply |
| **Finned tube (economiser type)** | Gas to liquid | Extends gas-side area | Fins foul in dusty gas |
| **Heat pipes and run-around coils** | Air to air in ducts that are apart or contaminated | No cross-contamination; streams can be far apart | Low to medium temperatures only |
| **Pinch analysis and heat integration** | Whole-plant redesign | Typically saves 10 to 30% of energy (up to 40% in food and drink) | Couples units; needs shutdown to rewire |
| **Feedstock or charge preheating** | Cement raw meal, metal scrap, glass batch | Uses exhaust directly on the product | Designed into the kiln or furnace |

#### Sources

1. [Technology Assessment on Low-Temperature Waste Heat Recovery in Industry, ORNL/TM-2021/2150 (Thekdi, Nimbalkar et al.)](https://info.ornl.gov/sites/publications/Files/Pub164247.pdf) Oak Ridge National Laboratory, 2021
2. [Waste Heat Recovery: Technology and Opportunities in U.S. Industry (BCS Inc. for US DOE Industrial Technologies Program)](https://www1.eere.energy.gov/manufacturing/intensiveprocesses/pdfs/waste_heat_recovery.pdf) US Department of Energy, 2008
3. [Not Just Hot Air: Low-Cost Decarbonization through Heat Recovery (Zahlan and Talan, Cadmus), ACEEE Summer Study on Energy Efficiency in Industry](https://www.aceee.org/sites/default/files/pdfs/ssi21/panel-3/Zahlan.pdf) ACEEE, 2021
4. [Process integration (pinch analysis)](https://natural-resources.canada.ca/energy-efficiency/process-integration-pinch-analysis) Natural Resources Canada, 2025
5. [Pulp and Paper Industry: Process Integration Specifics (CANMET Energy Technology Centre, 2003-121)](https://natural-resources.canada.ca/sites/nrcan/files/canmetenergy/files/pubs/2003-121e.pdf) Natural Resources Canada, 2003

## Other sections

- [Summary](https://www.materialinsights.org/energy/e_heat_exchangers/index.md)
- [Overview](https://www.materialinsights.org/energy/e_heat_exchangers/overview/index.md)
- [Correlation](https://www.materialinsights.org/energy/e_heat_exchangers/correlation/index.md)
- [Engineering and integration](https://www.materialinsights.org/energy/e_heat_exchangers/rc-eng/index.md)
- [Economics and contracts](https://www.materialinsights.org/energy/e_heat_exchangers/rc-econ/index.md)
- [Impact and additionality](https://www.materialinsights.org/energy/e_heat_exchangers/rc-impact/index.md)
- [What to track](https://www.materialinsights.org/energy/e_heat_exchangers/tracking/index.md)
- [Relationships](https://www.materialinsights.org/energy/e_heat_exchangers/links/index.md)