Condenser with Tapered Tubes to Reduce Pressure Drop and Weight

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Solution Overview

Problem

Conventional condenser designs with constant cross-sectional areas lead to inadequate heat transfer surface areas near the entrance of hot vapor or vapor/liquid mixtures and excessive surface areas in sections with higher liquid content, resulting in oversized and heavy heat exchangers with imbalanced heat transfer capabilities on the hot and cold sides.

Innovation Solution

The condenser apparatus features a plurality of substantially parallel tubes with varying hydraulic diameters, tapering from a larger diameter at the inlet to a smaller diameter at the outlet, and a method of condensing hot vapor or vapor/liquid mixtures by flowing them through these tubes, optimizing heat transfer by varying the cross-sectional areas based on liquid content, and using fins to enhance surface area for improved heat transfer.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Device complexity

If constant cross-sectional areas are used for both hot and cold flows, then the heat exchanger design is simplified, but the surface areas become inadequate near the entrance and excessive in mid and lower sections, resulting in oversized and heavy design

Engineering Contradiction:
Improveheat exchanger design simplicityVSAvoidheat exchanger weight
Core Design Contradiction:
Device complexityVSWeight of stationary object

Solution Approach 1:

The patent applies local quality by varying the cross-sectional area of tubes along their length, with larger areas near the entrance where heat transfer demand is highest and smaller areas in mid and lower sections where liquid content increases. This non-uniform geometry optimizes heat transfer surface area distribution to match the local heat transfer requirements, eliminating both inadequate and excessive surface areas while reducing overall heat exchanger size and weight.

Inventive Principle:
Principle #3Local quality

Solution Approach 2:

The patent implements dynamics by transitioning from static constant cross-sectional areas to dynamic varying cross-sectional areas that adapt to changing flow conditions along the tube length. The cross-sectional area varies continuously or in steps to match the changing heat transfer coefficients and liquid content, allowing the heat exchanger to maintain optimal performance throughout its length rather than being designed for a single average condition.

Inventive Principle:
Principle #15Dynamics

2Ease of manufacture

If constant cross-sectional areas are used for both hot and cold flows, then manufacturing is easier, but heat transfer surface areas are imbalanced between hot and cold sides

Engineering Contradiction:
Improvetube manufacturing easeVSAvoidheat transfer efficiency
Core Design Contradiction:
Ease of manufactureVSProductivity

Solution Approach 1:

The patent applies local quality by varying the cross-sectional area of tubes along their length, with larger areas near the entrance where heat transfer demand is highest and smaller areas in mid and lower sections where liquid content increases. This non-uniform geometry optimizes heat transfer surface area distribution to match the local heat transfer requirements, eliminating both inadequate and excessive surface areas while reducing overall heat exchanger size and weight.

Inventive Principle:
Principle #3Local quality

3Productivity

If larger cross-sectional areas are used to ensure adequate heat transfer surface area, then heat transfer capability is improved, but pressure drops increase and pump cavitation may occur

Engineering Contradiction:
Improveheat transfer rateVSAvoidpressure drop
Core Design Contradiction:
ProductivityVSStress or pressure

Solution Approach 1:

The patent applies local quality by varying the cross-sectional area of tubes along their length, with larger areas near the entrance where heat transfer demand is highest and smaller areas in mid and lower sections where liquid content increases. This non-uniform geometry optimizes heat transfer surface area distribution to match the local heat transfer requirements, eliminating both inadequate and excessive surface areas while reducing overall heat exchanger size and weight.

Inventive Principle:
Principle #3Local quality

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 enhances heat transfer rates, reduces pressure drops, and prevents pump cavitation by optimizing the pressure gradient and mass flow, resulting in a more efficient, smaller, and lighter condenser with balanced heat transfer capabilities on both sides.

Implementation Method 1

Condensers are heat exchangers that convert hot vapor, or high quality vapor/liquid mixtures, to liquids, by transferring heat from the hot vapor or vapor/liquid mixture to the adjacent cooler fluid flows

Methodology Applied
Scientific EffectHeat transfer: Conduction (thermal)

Implementation Method 2

As heat is removed from the vapor or high quality vapor/liquid mixture, its liquid content increases

Methodology Applied
Scientific EffectCondensation: Condensation

Implementation Method 3

enhances heat transfer rates, reduces pressure drops, and prevents pump cavitation by optimizing the pressure gradient and mass flow

Methodology Applied
Scientific EffectPressure gradient optimization: Pressure Gradient

Implementation Method 4

using fins to enhance surface area for improved heat transfer

Methodology Applied
Scientific EffectHeat transfer enhancement: Convection

Data Source

PatentEP3088826B1Condenser apparatus and method
Publication Date: 2020.08.19 THE BOEING CO
  • EP3088826B1 patent drawingFigure 1
  • EP3088826B1 patent drawingFigure 2
  • EP3088826B1 patent drawingFigure 3

AI summary

A condenser having passages of varying geometry for cooling of fluid. The condenser apparatus includes substantially parallel tubes each defining a channel and having an inlet at a first end and an outlet at a second end, the first end having a greater hydraulic diameter than the second end. Inlet and outlet manifolds are provided. The tubes may be oriented substantially vertically with the inlets above the respective outlets. A heat exchanger core comprises the tubes and substantially horizontally oriented fin material connecting the tubes. The tubes may receive a relatively higher temperature vapor or vapor and liquid mixture into the inlets of the tubes, around the tubes coolant flows substantially horizontally to remove heat from the tubes, and relatively cooler saturated liquid is discharged from the outlets. In one embodiment, the tube's channel splits into multiple channels to reduce the hydraulic diameter and increase the surface area ratio.