Asphalt Drying Drum Control With Independent Temperature Loops

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Solution Overview

Problem

Existing asphalt mixing plants face challenges in controlling the material temperature and raw gas temperature in drying drums, due to complex interdependencies between process parameters, which typically require complex multi-value controllers.

Innovation Solution

The implementation of separate and independent controllers for each drying drum, allowing for independent control of aggregate temperature and raw gas temperature, thereby ignoring the complex interdependencies and reducing system complexity.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Ease of operation

If separate independent controllers are used for each drying drum, then the control complexity is reduced and ease of operation is improved, but the ability to handle complex interdependencies between process parameters is limited

Engineering Contradiction:
Improveease of controlVSAvoidhandling of process interdependencies
Core Design Contradiction:
Ease of operationVSAdaptability or versatility

Solution Approach 1:

The control system is segmented into separate independent controllers for each drying drum, with each controller managing its own drum's parameters independently. This segmentation simplifies the overall control architecture by dividing the complex multi-parameter control problem into smaller, manageable independent control loops, directly resolving the contradiction between control simplicity and handling interdependencies.

Inventive Principle:
Principle #1Segmentation

2Adaptability or versatility

If manual operator intervention is used to control temperatures, then adaptability to changing conditions is maintained, but productivity is reduced due to manual intervention requirements

Engineering Contradiction:
Improveadaptability to changing conditionsVSAvoidproduction efficiency
Core Design Contradiction:
Adaptability or versatilityVSProductivity

Solution Approach 1:

The control system implements self-service through automatic temperature control algorithms that continuously monitor and adjust drying drum parameters without manual intervention. The system adapts to changing conditions autonomously by processing sensor data and making real-time control decisions, thereby maintaining adaptability while significantly improving productivity by eliminating manual operation requirements.

Inventive Principle:
Principle #25Self-service

3Manufacturing precision

If complex multi-value controllers are used to control all parameters, then manufacturing precision of temperature control is improved, but device complexity increases

Engineering Contradiction:
Improvetemperature control precisionVSAvoidcontroller complexity
Core Design Contradiction:
Manufacturing precisionVSDevice complexity

Solution Approach 1:

The complex multi-value control problem is segmented into multiple simple single-value controllers, each dedicated to controlling a specific parameter (e.g., one controller for aggregate temperature, another for raw gas temperature). This segmentation maintains temperature control precision by dedicating specialized control logic to each parameter while dramatically reducing overall device complexity by eliminating the need for a single complex multi-parameter controller.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

Multiple simple controllers are combined to achieve the functionality of a single complex controller. Each simple controller handles one specific control task with high precision, and their collective operation achieves the overall temperature control objectives that would require a complex multi-value controller, thereby maintaining precision while reducing individual controller complexity.

Inventive Principle:
Principle #5Merging (Combining)

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 solution enables automatic and precise control of both aggregate and raw gas temperatures, maintaining them within desired ranges without manual operator intervention, and achieves advantageous control results with reduced complexity.

Implementation Method 1

a first drying drum for drying and heating a first aggregate to a first aggregate temperature. The first drying drum comprises a first burner

Methodology Applied
Scientific EffectThermal energy transfer: Heating

Implementation Method 2

The first drying drum is configured to rotate at a first rotational speed

Methodology Applied
Scientific EffectRotational motion:

Implementation Method 3

a first controller comprising a first control loop configured to control the first aggregate temperature of the first aggregate

Methodology Applied
Scientific EffectFeedback control: Feedback

Implementation Method 4

a second controller comprising a second control loop configured to control a first raw gas temperature of a first raw gas of the first drying drum

Methodology Applied
Scientific EffectFeedback control: Feedback

Data Source

PatentUS20250101691A1Control of an asphalt mixing plant
Publication Date: 2025.03.27 AMMANN SCHWEIZ AG
  • US20250101691A1 patent drawing
  • US20250101691A1 patent drawing
  • US20250101691A1 patent drawing

AI summary

An asphalt mixing plant (700) includes a first drying drum (11) for drying and heating a first aggregate to a first aggregate temperature. The first drying drum (11) includes a first burner (31) and a first controller (41) configured to control by a first control loop (51) the first aggregate temperature of the first aggregate. The asphalt mixing plant (700) further includes a second controller (42) configured to control by a second control loop (52) a first raw gas temperature of a first raw gas of the first drying drum (11). The first controller (41) and the second controller (42) are configured to operate independently from each other. Further aspects relate to a corresponding method and a corresponding computer program product.