# A Dimensionless Empirical Model to Predict Heat Transfer Coefficients for Cooling High‐Moisture Meat Analog with Rectangular Dies

**Authors:** Caleb E. Wagner, Leon Levine, Girish M. Ganjyal

PMC · DOI: 10.1111/1750-3841.70366 · Journal of Food Science · 2025-07-05

## TL;DR

This paper presents a model to predict heat transfer during cooling of high-moisture meat analogs, helping improve production quality and efficiency.

## Contribution

A novel dimensionless empirical model is developed to estimate heat transfer coefficients for cooling high-moisture meat analogs.

## Key findings

- A dimensionless model (Nu¯ = A∙(Gz−1)B∙(C+D∙[1−a*]E)) accurately predicts heat transfer coefficients with high quality (RMSE = ±4.9).
- Cooling die aspect ratios and heat exchanger lengths significantly influence heat transfer coefficients in meat analog production.

## Abstract

An empirical dimensionless relationship useful for estimating heat transfer coefficients during continuous cooling of high moisture meat analog (HMMA) in rectangular linear cooling dies is described here. This information is essential for designing better cooling dies, which is timely since the cooling rate has recently been demonstrated to be important in controlling the quality of HMMA. Wheat‐based HMMA was extruded as per an experimental design that varied cooling media temperature (36–72°C), product mass flow rate (2.7–4.5 kg/h), and die aspect ratios (a* = 0.28 or 0.45). In situ product and cooling media temperatures and mass flow rates were measured continuously using penetrative thermocouples and flow meters, respectively. Dimensional scaling of the underlying differential equations governing heat transfer for this system demonstrated a relationship between dimensionless Nusselt (Nu¯), Graetz (Gz−1), and conduit aspect ratio (a*) numbers. Values for these numbers derived from the described experimental data were fit via nonlinear regression to a dimensionless model of the form Nu¯ = A∙(Gz−1)B∙(C+D∙[1−a*]E) with a high degree of quality (root mean square error = Nu¯ ± 4.9, p < 0.0001). The resulting fit parameters were deemed reasonable given that the model was logically bound within theoretical Nusselt number limits. The model documented here allows for the estimation of heat transfer coefficients relevant to HMMA cooling dies, while also illustrating the effect of altering cooling die aspect ratios and heat exchanger lengths as would be considered when scaling up an HMMA process.

Carefully balanced cooling rates are essential for producing whole‐cut type meat analogs with a desirable texture and fibrous quality at an economically feasible scale. This work presents a useful model for estimating the required cooling rates of whole‐cut type meat analogs as a function of key processing criteria such as production rate and product size. Models like this would be useful for engineers and scientists attempting to optimize their meat analog processes, with such efforts ultimately resulting in reduced costs and improved quality associated with meat analog production.

## Full-text entities

- **Chemicals:** propylene glycol (MESH:D019946), stainless steel (MESH:D013193), serpentine (MESH:C009244), Cp (-)

## Full text

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## Figures

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## References

28 references — full list in the complete paper: https://tomesphere.com/paper/PMC12228055/full.md

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Source: https://tomesphere.com/paper/PMC12228055