Baffle Wall Flow Separation in Cement Kiln Chlorine Bypass

Resolve Bottlenecks,
Find Innovative Solutions
Generate Solutions

Solution Overview

Problem

Conventional cement plants face challenges in efficiently reducing chlorine concentration in the kiln due to contamination from calciner exhaust gas low in chlorine concentration, leading to increased heat loss and manufacturing costs when attempting to extract a part of kiln exhaust gas high in chlorine concentration.

Innovation Solution

A baffle wall is formed on the lower face of the calciner's exhaust duct at an inclination angle of 20 to 60° relative to the horizontal plane, with a spacing that maintains an average flow rate of 15 to 35 m/s between the baffle wall and the opposite wall plane, preventing calciner exhaust gas from contaminating the kiln inlet and allowing exclusive extraction of high-chlorine kiln exhaust gas by the chlorine bypass apparatus.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Quantity of substance

If a part of kiln exhaust gas high in chlorine concentration is extracted by the chlorine bypass apparatus, then chlorine concentration in the kiln is reduced, but calciner exhaust gas low in chlorine concentration contaminates the extraction stream, reducing extraction efficiency

Engineering Contradiction:
Improvechlorine concentration reductionVSAvoidextraction efficiency
Core Design Contradiction:
Quantity of substanceVSManufacturing precision

Solution Approach 1:

The exhaust gas flow path is segmented into distinct regions using a baffle wall that separates calciner exhaust gas flow from kiln exhaust gas flow. This segmentation ensures that only kiln exhaust gas high in chlorine concentration is extracted by the chlorine bypass apparatus, while calciner exhaust gas low in chlorine concentration is directed elsewhere, thereby improving extraction efficiency

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The harmful calciner exhaust gas flow is extracted and removed from the potential contamination path by directing it through a separate flow path using the baffle wall configuration. This allows the chlorine bypass apparatus to selectively extract only the chlorine-rich kiln exhaust gas without contamination from calciner exhaust gas

Inventive Principle:
Principle #2Taking out (Extraction)

2Quantity of substance

If exhaust gas extraction is increased to reduce chlorine concentration, then chlorine removal effectiveness improves, but heat loss increases and manufacturing costs rise

Engineering Contradiction:
Improvechlorine removal effectivenessVSAvoidheat loss
Core Design Contradiction:
Quantity of substanceVSLoss of energy

Solution Approach 1:

The baffle wall creates localized flow patterns that concentrate the extraction of chlorine-rich kiln exhaust gas in a specific region, while allowing calciner exhaust gas to follow a different path. This local quality differentiation enables effective chlorine removal with minimal heat loss by extracting only the necessary portion of exhaust gas

Inventive Principle:
Principle #3Local quality

3Quantity of substance

If the gas extracting pipe is positioned to extract kiln exhaust gas, then chlorine concentration reduction is achieved, but calciner exhaust gas may contaminate the extraction stream

Engineering Contradiction:
Improvechlorine concentration reductionVSAvoidcontamination
Core Design Contradiction:
Quantity of substanceVSObject-affected harmful factors

Solution Approach 1:

The baffle wall acts as an intermediary structure that guides and separates different exhaust gas flows. It mediates between the calciner exhaust gas flow and the kiln exhaust gas flow, ensuring that the gas extracting pipe extracts only kiln exhaust gas while preventing contamination from calciner exhaust gas

Inventive Principle:
Principle #24Intermediary (Mediator)

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 configuration effectively reduces chlorine concentration in the cement kiln by preventing calciner exhaust gas contamination and optimizing exhaust gas flow, minimizing heat loss and maintaining operational efficiency.

Implementation Method 1

a baffle wall protruding toward the pipe inclination part side on a lower face of the exhaust duct of the calciner at an inclination angle within a range of 20 to 60° with respect to a horizontal plane is formed

Methodology Applied
Scientific EffectFluid flow separation: Flow Separation

Implementation Method 2

a gas extracting pipe 11 which is connected to the exhaust gas pipe 9 from the kiln inlet part 2 and picks out and cools a part of the exhaust gas

Methodology Applied
Scientific EffectGas cooling: Cooling

Implementation Method 3

the chlorine component contained in the exhaust gas results in its transfer again to the cement raw material side

Methodology Applied
Scientific EffectCondensation: Condensation

Data Source

PatentUS9890080B2Cement plant
Publication Date: 2018.02.13 MITSUBISHI UBE CEMENT CORP
  • US9890080B2 patent drawing
  • US9890080B2 patent drawing
  • US9890080B2 patent drawing

AI summary

There is provided a cement plant including a chlorine bypass apparatus capable of efficiently reducing the chlorine concentration in a cement kiln due to exhaust gas extraction by a small amount, by preventing calciner exhaust gas low in chlorine concentration from contamination and extracting a part of kiln exhaust gas high in chlorine concentration. In the invention, a baffle wall 20 which protrudes, on a lower face 16a of an exhaust duct 16 of a calciner connected to the pipe inclination part 14 of an exhaust gas pipe 9 rising from a kiln inlet part 2 of a cement kiln 1, toward a pipe inclination part 14 side at an inclination angle α within a range of 20 to 60° relative to the horizontal plane, and a spacing between a lower end edge 20a of the baffle wall and an opposite wall plane 14a of the pipe inclination part is configured such that an average flow rate of the exhaust gas between the both falls within a range of 15 to 35 m/s.