Modular Oxyfuel Vertical Kiln for Low-Carbon Cement

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Solution Overview

Problem

The cement industry faces challenges such as high carbon emissions, overcapacity in developed regions and undercapacity in developing regions, inefficiencies in large-scale production, and the inability to adapt to geographic shifts in demand, with existing technologies failing to provide low-cost, low-carbon, modular, and adaptable cement production solutions.

Innovation Solution

A modular oxyfuel combustion system using a packed bed reactor with a vertical kiln design that operates at elevated temperatures (1,300° C. to 2,200° C.) to produce cement clinker efficiently, reducing capital costs and carbon emissions by utilizing natural gas and pure oxygen, and enabling quick setup and adaptation to demand shifts.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Productivity

If large-scale rotary kilns are used for cement production, then productivity increases, but carbon emissions increase and adaptability decreases

Engineering Contradiction:
Improvecement production capacityVSAvoidcarbon emissions
Core Design Contradiction:
ProductivityVSObject-generated harmful factors

Solution Approach 1:

The invention divides the cement production system into modular vertical kiln units that can be deployed independently. Each module contains a complete cement production system with capacity of 50-200 tons per day, allowing multiple smaller units to replace one large rotary kiln, thereby maintaining total productivity while reducing carbon footprint through improved combustion efficiency and localized operation

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The invention changes the combustion parameters by using oxyfuel technology (combustion in pure oxygen or oxygen-enriched atmosphere) instead of conventional air combustion. This parameter change increases flame temperature and combustion efficiency, reducing fuel consumption and carbon emissions per ton of cement produced, while also simplifying the flue gas composition for easier CO2 capture

Inventive Principle:
Principle #35Parameter changes

2Productivity

If large-scale rotary kilns are used for cement production, then productivity increases, but adaptability to geographic shifts in demand decreases

Engineering Contradiction:
Improvecement production capacityVSAvoidadaptability to demand shifts
Core Design Contradiction:
ProductivityVSAdaptability or versatility

Solution Approach 1:

The invention segments the cement production system into independent modular vertical kiln units, each capable of operating autonomously with complete raw material processing and clinker production. This modular architecture allows rapid deployment in different geographic locations to follow demand, unlike fixed large-scale rotary kilns that cannot be easily relocated or scaled

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The invention creates a dynamic production system where modular vertical kiln units can be added, removed, or relocated based on changing market demands. The system transitions from static large-scale production to flexible distributed production, enabling quick response to geographic shifts in cement demand patterns

Inventive Principle:
Principle #15Dynamics

3Ease of operation

If conventional air-fuel combustion is used, then ease of operation is maintained, but energy efficiency decreases

Engineering Contradiction:
Improvecombustion operation simplicityVSAvoidenergy efficiency
Core Design Contradiction:
Ease of operationVSUse of energy by moving object

Solution Approach 1:

The invention changes the combustion atmosphere parameter from air (21% oxygen) to pure oxygen or oxygen-enriched gas. This parameter change increases the adiabatic flame temperature from approximately 1900°C to over 2400°C, significantly improving combustion efficiency and heat transfer to the clinker, while reducing the volume of flue gas and improving energy utilization

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

The invention implements continuous preheating of the limestone feed using the hot flue gas in a countercurrent heat exchanger arrangement. This continuous preheating action reduces the energy required in the combustion zone, improving overall energy efficiency while maintaining steady operation. The system ensures continuous useful heat transfer from flue gas to feed material

Inventive Principle:
Principle #20Continuity of useful action

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 system achieves low carbon cement production with reduced capital investment, lower operational costs, and enhanced energy efficiency, allowing for localized and adaptable cement manufacturing, particularly in developing regions, while minimizing greenhouse gas emissions and capital expenses.

Implementation Method 1

flowing an oxyfuel into the inner volume and igniting the oxyfuel, whereby the oxyfuel burns at a gas temperature

Methodology Applied
Scientific EffectCombustion: Combustion

Implementation Method 2

A modular oxyfuel combustion system using a packed bed reactor with a vertical kiln design that operates at elevated temperatures (1,300° C. to 2,200° C.) to produce cement clinker efficiently

Methodology Applied
Scientific EffectOxyfuel combustion: Combustion

Implementation Method 3

moving the material through the inner volume of the furnace with a gravity feed and without any tilling of the material

Methodology Applied
Scientific EffectGravity: Gravitation

Data Source

PatentUS20250276936A1Vertical kiln to for cement manufacturing
Publication Date: 2025.09.04 FURNO MATERIALS INC
  • US20250276936A1 patent drawing
  • US20250276936A1 patent drawing
  • US20250276936A1 patent drawing

AI summary

Numerous examples of a vertical kiln for manufacturing cement are disclosed. In one example, a vertical kiln comprises a housing comprising a top opening to receive unprocessed material and a bottom opening to output processed material; a combustion system to heat the unprocessed material within the housing to generate the processed material; a thermocouple located within the housing to measure temperature; and a control system to control the combustion system in response to temperature data from the thermocouple.