Closed-Loop Solid-Liquid Separation With Gravity-Assisted Heat Exchange
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Solution Overview
Problem
Existing solid-liquid separation devices using substances that are gases at normal temperature and pressure, such as dimethyl ether (DME), face challenges with inefficient operation due to narrow optimal circulation amounts, external heat source inefficiencies, and increased maintenance needs, leading to excessive emission of the substance during device replacement.
Innovation Solution
A solid-liquid separation device with a closed system using a substance B for phase change, featuring a compression mechanism, dual heat exchangers, and a treatment tank, where the first heat exchanger is installed below the tank, and a third heat exchanger is positioned downstream and upstream in the flow path, optimizing heat exchange and reducing external emission by leveraging gravity for fluid flow.
Engineering Contradictions & Design Principles
Engineering Contradiction Analysis
1Productivity
If the amount of DME circulated in the cycle is increased, then the efficiency of the cycle is improved, but a liquid phase unfavorable for heat exchange occurs in the heat exchanger
Solution Approach 1:
The patent applies parameter changes by precisely controlling the circulation amount of DME within a narrow optimal range. The system monitors and adjusts DME circulation parameters (temperature, pressure, flow rate) to maintain efficient heat exchange while preventing unfavorable liquid phase formation. This resolves the contradiction by dynamically optimizing the operating parameters rather than using fixed high circulation amounts.
2Reliability
If the amount of DME circulated in the cycle is decreased, then the heat exchange efficiency is improved, but a gas-liquid two-phase flow occurs and cycle efficiency is decreased
Solution Approach 1:
The patent resolves this contradiction by implementing precise parameter control within a narrow optimal range. The system continuously monitors DME circulation conditions and adjusts temperature, pressure, and flow rate parameters to prevent gas-liquid two-phase flow while maintaining sufficient circulation for cycle efficiency. This balanced parameter optimization allows the system to achieve both good heat exchange efficiency and acceptable cycle productivity.
3Device complexity
If an external heat source is used for phase change of DME, then the device complexity is reduced, but the heat exchange efficiency is lower and the heat exchanger needs to be increased in size
Solution Approach 1:
The patent introduces an intermediary substance B that circulates in a closed system to transfer heat for DME phase change. Substance B acts as a mediator between the heat source and DME, enabling efficient heat transfer with a compact heat exchanger design. This intermediary approach replaces direct external heat source connection, reducing both device complexity and heat exchanger size while maintaining effective phase change functionality.
4Device complexity
If an external heat source is used for phase change of DME, then the device configuration is simplified, but sensible heat is used and heat exchange efficiency is lower
Solution Approach 1:
The patent utilizes phase transitions of substance B in the closed circulation system to enable latent heat transfer for DME phase change. Instead of using sensible heat from an external source, substance B undergoes phase changes (evaporation and condensation) that provide efficient heat transfer. This phase transition mechanism maintains simplified device configuration while dramatically improving heat exchange efficiency compared to sensible heat approaches.
5Productivity
If the device size is increased, then the processing capacity is improved, but the amount of substance A opened to the atmosphere is increased
Solution Approach 1:
The patent employs a closed system with flexible sealing mechanisms and enclosed pathways for substance A circulation. The system uses sealed connections and containment structures that prevent substance A from opening to the atmosphere, even as device size increases for higher processing capacity. This sealing approach effectively eliminates substance A emissions while maintaining the scalability needed for increased productivity.
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 device efficiently performs phase change of the substance, reduces external emission, and enhances heat exchange efficiency, allowing for continuous purification and efficient removal of water, oil, and solids, while minimizing the need for large heat exchanger sizes and frequent maintenance.
Implementation Method 1
a first heat exchanger that exchanges heat of condensation of the substance B and heat of evaporation of the substance A, the substance A having been evaporated while separated from the water or the oil in the first heat exchanger
Implementation Method 2
a first heat exchanger that exchanges heat of condensation of the substance B and heat of evaporation of the substance A
Implementation Method 3
a second heat exchanger that exchanges heat of evaporation of the substance B and heat of condensation of the substance A, and condensed in the second heat exchanger
Implementation Method 4
a second heat exchanger that exchanges heat of evaporation of the substance B and heat of condensation of the substance A
Implementation Method 5
compression means that compresses the substance B
Implementation Method 6
substance B that is circulated while generating phase change in a closed system
Data Source
AI summary
A solid-liquid separation device performs dehydration/deoiling from a mixture of water and/or oil and a solid. Substance A is capable of dissolving water and oil. The device includes substance B circulated while generating phase change in a closed system; a compressor; a first heat exchanger exchanging condensation heat of substance B and evaporation heat of substance A; a second heat exchanger exchanging evaporation heat of substance B and condensation heat of substance A; and a treatment tank for mixing substance A with an object to be treated; substance A having been evaporated while separated from the water or the oil in the first heat exchanger, and condensed in the second heat exchanger. The first heat exchanger is lower than the treatment tank in a vertical direction, and a connection port of the first heat exchanger and a lower portion of the treatment tank are connected with a flow path.


