Heat Tracing Assembly With Compression Panels for Pipe Heat Transfer

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Solution Overview

Problem

Traditional heat tracing systems for large-scale piping networks face challenges such as inconsistent heat transfer due to poor contact between tracing tubes and process pipes, over-pressurization, and inefficient control processes that fail to account for nonlinear responses and ambient temperature transients.

Innovation Solution

A heat tracing assembly and system that includes interlocking longitudinal panels made of conductive material to maximize heat transfer from tracing tubes to a centrally positioned process pipe, with a compression layer applying radial compressive forces to ensure optimal contact and heat distribution.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Ease of manufacture

If traditional heat tracing devices are used with tangential interface between tracing tubes and process pipe wall, then the device complexity is reduced, but the heat transfer efficiency deteriorates due to less than 5° of tracing tube circumference being in point contact with the process pipe

Engineering Contradiction:
Improvedevice complexityVSAvoidheat transfer efficiency
Core Design Contradiction:
Ease of manufactureVSTemperature

Solution Approach 1:

The tracing assembly is divided into multiple longitudinal panels (typically 3-5 panels) that wrap around the process pipe. Each panel contains tracing tubes and is connected to adjacent panels through overlapping edges with fasteners. This segmentation allows the assembly to conform to the pipe circumference while maintaining structural integrity and heat transfer effectiveness across the entire 360° contact interface.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The longitudinal panels are designed with curved inner surfaces that match the cylindrical geometry of the process pipe. The panels arc around the pipe to provide circumferential contact, ensuring that tracing tubes maintain consistent thermal contact with the pipe wall around the entire circumference rather than at a single point, thereby maximizing heat transfer efficiency.

Inventive Principle:
Principle #14Spheroidality (Curvature)

2Temperature

If compression layer with radial compressive forces is applied to maximize heat transfer, then the heat transfer efficiency is improved, but the stress or pressure on the process pipe increases

Engineering Contradiction:
Improveheat transfer efficiencyVSAvoidradial compressive force
Core Design Contradiction:
TemperatureVSStress or pressure

Solution Approach 1:

The compression layer applies radial compressive forces locally at the interface between the tracing tubes and the process pipe wall, rather than uniformly across the entire assembly. This localized compression ensures optimal thermal contact where needed (at the pipe-tracing interface) while minimizing unnecessary stress on the pipe structure and other components of the assembly.

Inventive Principle:
Principle #3Local quality

3Device complexity

If traditional PID-control loops are used assuming linear-lumped system, then the control process is simplified, but the control accuracy deteriorates due to nonlinear responses and distributed system characteristics

Engineering Contradiction:
Improvecontrol process complexityVSAvoidcontrol accuracy
Core Design Contradiction:
Device complexityVSMeasurement precision

Solution Approach 1:

The control system incorporates multiple temperature sensors positioned at different locations along the pipe to provide distributed feedback about the actual thermal state. This feedback is fed into a controller that adjusts steam flow rates and tracing tube activation in real-time, creating a closed-loop system that adapts to nonlinear responses and maintains accurate temperature control despite variations in ambient conditions, flow rates, and thermal loads.

Inventive Principle:
Principle #23Feedback

4Area of stationary object

If extended-length tracing circuits are used to cover large-scale piping networks, then the coverage area is increased, but the measurement precision of temperature sensors deteriorates due to signal collection challenges and multiple uncertainties

Engineering Contradiction:
Improvecoverage areaVSAvoidtemperature sensor accuracy
Core Design Contradiction:
Area of stationary objectVSMeasurement precision

Solution Approach 1:

The large-scale piping network is divided into multiple zones, each monitored by its own temperature sensors and controlled by a distributed control system. This segmentation allows for localized temperature measurement and control in each zone, maintaining measurement precision even as the overall coverage area expands across the entire plant.

Inventive Principle:
Principle #1Segmentation

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

The solution enhances heat transfer efficiency, reduces reaction response lag times, and ensures proper condensate evacuation, leading to more consistent and efficient heating of large-scale plant piping networks.

Implementation Method 1

a compression layer made of a conductive material and configured to maximize heat transfer from the heat source in the tracing tubes to the process pipe

Methodology Applied
Scientific EffectThermal conduction: Conduction (thermal)

Implementation Method 2

the enthalpy (latent heat of vaporization) in steam which contains 2-3 times the energy as the liquid... the control system must ensure that adequate pressure is applied to achieve the temperature set point and sufficient pressure differential to ensure proper condensate evacuation

Methodology Applied
Scientific EffectCondensation: Condensation

Data Source

PatentUS12297947B2Heat tracing system and method
Publication Date: 2025.05.13 DAMICO III JOSEPH V
  • US12297947B2 patent drawing
  • US12297947B2 patent drawing
  • US12297947B2 patent drawing

AI summary

A heat tracing assembly for heating a product in a process pipe including a compression layer formed of a conductive material and one or more tracing tubes for the flow of a heat source. The compression layer is positioned around the process pipe with the tracing tubes at least partially disposed within the compression layer. The compression layer may be formed of a plurality of interlocking longitudinal panels for optimizing the transfer and distribution of heat from the tracing tubes to the process pipe.