Offset Tube Bundle Heat Exchanger for Uniform Gas Flow

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Solution Overview

Problem

Conventional heat exchangers in sulfuric acid plants face issues with non-uniform gas flow and impaired heat transfer due to radial approach flow in horizontal sections, leading to corrosion and inefficiencies, particularly in the first chamber where sulfuric acid condensate causes corrosion.

Innovation Solution

The tube bundle in the heat exchanger is offset with respect to the chamber casing, creating a tapered gas space that ensures uniform gas flow and pressure distribution across the tube bundle, with a gas supply opening that extends along the tube bundle length and a horizontal main axis for easy drainage, minimizing condensation and corrosion risks.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Ease of manufacture

If the tube bundle is arranged concentrically in the chamber casing with radial gas supply, then the structure is simple and easy to manufacture, but the gas flow becomes non-uniform and heat transfer is impaired

Engineering Contradiction:
Improvestructural simplicityVSAvoidheat transfer efficiency
Core Design Contradiction:
Ease of manufactureVSProductivity

Solution Approach 1:

The tube bundle is deliberately offset from the center of the chamber casing, creating an asymmetric arrangement. The offset distance is specifically designed so that the distance between the gas supply opening and the nearest tube row equals the distance from the farthest tube row to the opposite chamber wall. This asymmetric positioning transforms the non-uniform radial flow into a uniform flow distribution across all tube rows, maximizing heat transfer efficiency while maintaining structural simplicity.

Inventive Principle:
Principle #4Asymmetry

2Reliability

If high-alloy stainless steel materials are used in the first chamber, then corrosion resistance is improved, but the manufacturing cost increases significantly

Engineering Contradiction:
Improvecorrosion resistanceVSAvoidmanufacturing cost
Core Design Contradiction:
ReliabilityVSEase of manufacture

Solution Approach 1:

The heat exchanger is divided into two chambers with different functional requirements. The first chamber, exposed to cold SO2 gas and sulfuric acid condensate, uses high-alloy stainless steel for corrosion resistance. The second chamber, handling warmer gases without condensation, uses ordinary carbon steel. This local differentiation of material quality matches the corrosion risk distribution, achieving reliable corrosion protection where needed while minimizing overall manufacturing costs.

Inventive Principle:
Principle #3Local quality

3Productivity

If two vertically oriented heat exchangers are arranged one beside the other, then the heat transfer surface is increased, but drainage problems occur

Engineering Contradiction:
Improveheat transfer surface areaVSAvoiddrainage capability
Core Design Contradiction:
ProductivityVSEase of operation

Solution Approach 1:

Instead of arranging heat exchangers vertically side-by-side (two-dimensional arrangement), the invention uses a horizontal orientation for the first chamber where drainage is critical. The horizontal configuration allows condensate to drain naturally to the lowest point along the entire length of the chamber, eliminating drainage problems associated with vertical arrangements while maintaining adequate heat transfer surface area.

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

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 design achieves uniform heat transfer and reduces corrosion by maintaining a uniform gas flow and pressure distribution, limiting temperature increase and minimizing sulfuric acid condensation, allowing for the use of less expensive materials in the vertical heat-exchange section.

Implementation Method 1

creating a tapered gas space that ensures uniform gas flow and pressure distribution across the tube bundle

Methodology Applied
Scientific EffectPressure gradient: Pressure Gradient

Implementation Method 2

The cold SO2 gas generally is guided in counterflow to the SO3-containing gas to be cooled

Methodology Applied
Scientific EffectHeat transfer: Heat Exchanger

Implementation Method 3

The cold SO2 gas generally is guided in counterflow to the SO3-containing gas to be cooled

Methodology Applied
Scientific EffectConvection: Convection

Implementation Method 4

the sulfuric acid condensate leads to a strong corrosion in particular in the first chamber of the heat exchanger

Methodology Applied
Scientific EffectCondensation: Condensation

Data Source

PatentUS9551537B2Heat exchanger including a tube bundle that is offset with respect to a center of the chamber casing
Publication Date: 2017.01.24 METSO METALS OY
  • US9551537B2 patent drawing
  • US9551537B2 patent drawing

AI summary

A heat exchanger for use in a contact group of a sulfuric acid plant includes a chamber in which a tube bundle is arranged on a circular ring. A gas space is formed between the tube bundle and a chamber casing surrounding the tube bundle. A gas supply opening is provided in the chamber casing and is configured to introduce a gas into the gas space substantially radially to the tube bundle. A gas outlet opening adjoins an interior space enclosed by the tube bundle in a substantially axial direction. A center of the tube bundle is offset with respect to a center of the chamber casing in a direction opposite to the gas supply opening.