Retort Vessel Liquid Column Heating for Lower Energy Use

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Solution Overview

Problem

Existing retorting processes require large volumes of processing fluid and energy due to the need to immerse the entire retort vessel chamber, leading to inefficient heat transfer and prolonged heating times.

Innovation Solution

A closed loop system where packaged products are held in structures with controlled liquid flow, forming closed columns within the retort vessel, allowing precise heat transfer and reducing the volume of processing fluid required.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Temperature

If the entire retort vessel chamber is filled with heated water to completely immerse the product, then effective heat distribution and penetration into the product is achieved, but a large amount of energy is required to heat the entire volume of liquid

Engineering Contradiction:
Improveheat distributionVSAvoidenergy consumption
Core Design Contradiction:
TemperatureVSUse of energy by moving object

Solution Approach 1:

The retort vessel is segmented into multiple zones: a liquid-filled zone containing the product, and a vapor zone above it. This segmentation allows heat treatment to occur in the liquid zone while the vapor zone provides additional heating without requiring the entire vessel volume to be filled with liquid, thereby reducing energy consumption while maintaining effective heat distribution.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The invention introduces a vertical dimension to heat transfer by allowing vapor to rise and condense on the upper surfaces of products and container closures. This adds a top-down heat transfer pathway that complements the traditional side-to-side liquid immersion heating, enabling effective heat treatment with less liquid volume.

Inventive Principle:
Principle #17Another dimension (Dimensionality change)

2Stress or pressure

If compressed air is used to develop overpressure in the retort to offset pressure differential inside product containers, then container integrity is maintained, but the energy required to heat and cool the large volume of liquid increases

Engineering Contradiction:
ImproveoverpressureVSAvoidenergy consumption
Core Design Contradiction:
Stress or pressureVSUse of energy by moving object

Solution Approach 1:

The retort vessel is divided into a pressurized liquid zone and a vapor zone. Compressed air is applied selectively to maintain overpressure in the liquid zone where products are immersed, while the vapor zone operates at different pressure conditions. This segmented pressurization reduces the total volume requiring compressed air maintenance, lowering energy consumption.

Inventive Principle:
Principle #1Segmentation

3Temperature

If the entire retort vessel chamber is filled with heated water, then homogeneous heat transfer to all products is achieved, but the heatsink effect of the vessel shell and large liquid volume prolongs heating time

Engineering Contradiction:
Improveheat transfer homogeneityVSAvoidheating time
Core Design Contradiction:
TemperatureVSLoss of time

Solution Approach 1:

By segmenting the vessel into liquid immersion zones and vapor exposure zones, the system achieves homogeneous heat transfer through multiple pathways: liquid conduction to submerged surfaces and vapor condensation to exposed surfaces. This multi-zone approach reduces the total liquid volume required, minimizing the heatsink effect and shortening heating time while maintaining heat uniformity.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The invention utilizes phase transition of water from liquid to vapor and back to liquid (condensation) as a heat transfer mechanism. Vapor generated in the liquid zone rises, condenses on cooler product surfaces and vessel walls, releasing latent heat directly to products without requiring additional liquid volume, thereby reducing heatsink effects and heating time.

Inventive Principle:
Principle #36Phase transitions

Applied Scientific Principles

This section explains which scientific principles are used to turn an abstract innovation direction into a practical engineering solution.

Function Achieved in This Case

This approach reduces energy consumption and shortens heating times by using less process liquid and minimizing the heatsink effect, while maintaining effective heat transfer to the products.

Implementation Method 1

a circulation pump operable to transport heat exchange liquid from the suction side to the discharge side

Methodology Applied
Scientific EffectPump: Pump

Implementation Method 2

circulating heat exchange liquid through each product holding structure to treat the packaged products

Methodology Applied
Scientific EffectHeat transfer: Conduction (thermal)

Implementation Method 3

heated processing liquid can be pressurized to completely immerse the food product within the baskets

Methodology Applied
Scientific EffectConvection: Convection

Implementation Method 4

each of the one or more removable baskets comprises at least one flow control orifice that is proximate the bottom of the basket and configured to slow drainage of heat exchange liquid out of the basket

Methodology Applied
Scientific EffectFlow restriction: Pressure Drop

Implementation Method 5

a distribution plenum for supplying heat exchange liquid into each of the one or more removable baskets, the distribution plenum in fluid connection with the discharge side of the heat exchange liquid circulation loop

Methodology Applied
Scientific EffectFluid distribution: Hydraulic Press

Data Source

PatentUS12515838B2Retort system and process
Publication Date: 2026.01.06 STOCK AMERICA LLC
  • US12515838B2 patent drawing
  • US12515838B2 patent drawing
  • US12515838B2 patent drawing

AI summary

A retort system includes a vessel and a plurality of product holding structures for holding one or more products to be treated, the product holding structures configured to be received within the interior volume of the vessel. A heat exchange system, includes a liquid circulation path having a discharge side, a suction side and a pump operable to move a heat exchange liquid from the suction side to the discharge side. The suction side is fluidly connectable to a lower region of the interior volume. The discharge side is fluidly connectable to deliver heat exchange liquid into the product holding structures via pump operation causing the product holding structures to fill with heat exchange liquid to a product submersion level while a level of heat exchange liquid outside the product holding structures and within the interior volume remains below the product submersion level.