Bubble Column Condenser Staging for HDH Desalination

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Solution Overview

Problem

Existing desalination systems, such as those using humidification-dehumidification (HDH) processes, face inefficiencies due to the presence of non-condensable gases, which reduce heat and mass transfer rates and increase energy consumption in condensers.

Innovation Solution

The use of bubble column condensers with a configuration that includes a vessel with a liquid layer and a vapor distribution region, where gas bubbles transfer heat and mass to the liquid, enhancing condensation efficiency and reducing energy requirements.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Adaptability or versatility

If a carrier gas is used in HDH systems, then the humidification-dehumidification process can be implemented, but the presence of non-condensable gas reduces heat and mass transfer rates in the condenser

Engineering Contradiction:
ImproveHDH process implementationVSAvoidheat and mass transfer rates
Core Design Contradiction:
Adaptability or versatilityVSProductivity

Solution Approach 1:

The condenser is divided into multiple stages with intermediate cooling sections. Each stage handles a portion of the condensation process, allowing heat and mass transfer to occur in segmented zones. This segmentation reduces the thermal resistance caused by non-condensable gases by creating multiple heat transfer pathways and reducing the thickness of the gas layer that must be traversed.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The invention introduces a vertical dimension to the condensation process by using a multi-stage columnar structure. Vapor rises through the condenser while cooling occurs at multiple elevation levels. This dimensional approach allows simultaneous heat and mass transfer at different heights, overcoming the limitation of horizontal single-stage condensers where non-condensable gases create uniform thermal resistance across the entire heat transfer surface.

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

2Adaptability or versatility

If a carrier gas is used in HDH systems, then the humidification-dehumidification process can be implemented, but the presence of non-condensable gas increases thermal resistance to condensation on cold surfaces

Engineering Contradiction:
ImproveHDH process implementationVSAvoidthermal resistance to condensation
Core Design Contradiction:
Adaptability or versatilityVSUse of energy by stationary object

Solution Approach 1:

The condensation process is segmented into multiple stages with intermediate cooling sections. Each stage has its own heat transfer surface, reducing the overall thermal resistance by distributing the condensation load across multiple smaller surfaces rather than one large surface where non-condensable gases would create uniform resistance.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

Cool spray water is introduced as an intermediary cooling medium between the vapor stream and the condenser walls. This spray water absorbs heat from the condensing vapor and cools the heat transfer surfaces, effectively reducing thermal resistance by creating a liquid-phase heat transfer pathway that bypasses the thermal barrier created by non-condensable gases.

Inventive Principle:
Principle #24Intermediary (Mediator)

3Productivity

If traditional condensers are used in HDH systems, then condensation can occur, but large amounts of energy are required to operate

Engineering Contradiction:
Improvecondensation capabilityVSAvoidenergy consumption
Core Design Contradiction:
ProductivityVSUse of energy by moving object

Solution Approach 1:

Cool spray water is introduced preliminarily into the condenser to pre-cool the vapor stream before it reaches the main heat transfer surfaces. This preliminary cooling action reduces the temperature difference required for condensation, thereby reducing the energy consumption of the condenser while maintaining condensation capability.

Inventive Principle:
Principle #10Preliminary action

Solution Approach 2:

The system uses periodic spraying of cool water into the condenser to maintain optimal heat transfer conditions. This periodic cooling action removes heat intermittently, allowing the condenser to operate more efficiently by preventing excessive heat buildup that would require continuous high-energy operation.

Inventive Principle:
Principle #19Periodic 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

This configuration improves heat and mass transfer rates, reduces energy consumption, and increases the effectiveness of desalination systems by effectively removing water vapor from gas streams, leading to more efficient water purification.

Implementation Method 1

gas bubbles transfer heat and mass to the liquid

Methodology Applied
Scientific EffectHeat transfer: Conduction (thermal)

Implementation Method 2

gas bubbles transfer heat and mass to the liquid

Methodology Applied
Scientific EffectMass transfer: Diffusion

Implementation Method 3

enhancing condensation efficiency

Methodology Applied
Scientific EffectCondensation: Condensation

Data Source

PatentUS9364771B2Systems including a condensing apparatus such as a bubble column condenser
Publication Date: 2016.06.14 GRADIANT CORP
  • US9364771B2 patent drawing
  • US9364771B2 patent drawing
  • US9364771B2 patent drawing

AI summary

Condensing apparatuses and their use in various heat and mass exchange systems are generally described. The condensing apparatuses, such as bubble column condensers, may employ a heat exchanger positioned external to the condensing vessel to remove heat from a bubble column condenser outlet stream to produce a heat exchanger outlet stream. In certain cases, the condensing apparatus may also include a cooling device positioned external to the vessel configured and positioned to remove heat from the heat exchanger outlet stream to produce a cooling device outlet stream. The condensing apparatus may be configured to include various internal features, such as a vapor distribution region and/or a plurality of liquid flow control weirs and/or chambers within the apparatus having an aspect ratio of at least 1.5. A condensing apparatus may be coupled with a humidifier to form part of a desalination system, in certain cases.