Crude Oil Demulsification Using Cyclonic and Electrostatic Separation
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Solution Overview
Problem
Crude oil demulsification technologies face challenges in efficiently separating oil and water phases, leading to corrosion and deposition issues in downstream equipment due to unresolved salt content, with existing methods experiencing turbulence and slugging in storage tanks.
Innovation Solution
A system comprising a cyclonic separator and an electrostatic coalescer is implemented within a storage tank to induce cyclonic flow and separate multi-phase fluid streams, followed by electrostatic coalescence to demulsify the liquid stream, effectively separating oil and water phases and reducing salt content.
Engineering Contradictions & Design Principles
Engineering Contradiction Analysis
1Productivity
If conventional gravity separation is used in storage tanks, then equipment simplicity is maintained, but separation efficiency is poor and turbulence/slugging occurs
Solution Approach 1:
The patent replaces conventional gravity-based mechanical separation with a cyclonic separator that uses centrifugal force generated by rotational flow. The cyclonic separator induces a vortex flow pattern that separates oil and water phases based on density differences, achieving much higher separation efficiency without requiring complex mechanical moving parts. The separator uses a tangential inlet to generate cyclonic flow, and the separated phases are discharged through different outlets based on their positions in the centrifugal field.
2Reliability
If water is not separated from crude oil, then processing is simpler, but corrosion and deposition occur in downstream equipment
Solution Approach 1:
The patent introduces an electrostatic coalescer as an intermediary device between the cyclonic separator and downstream equipment. The coalescer uses electrostatic fields to promote the coalescence of fine water droplets in the oil phase, forming larger droplets that can be more easily separated. This intermediary step effectively removes water and salt content before the oil reaches downstream equipment, preventing corrosion and deposition while maintaining system reliability.
3Use of energy by stationary object
If downstream processing is used for water separation, then upstream processing is simpler, but heating requirements and operational costs increase
Solution Approach 1:
The patent implements preliminary water separation action upstream in the storage tank using the cyclonic separator and electrostatic coalescer combination. By performing the separation operation before the oil leaves the storage tank, the system removes the majority of water content upstream, significantly reducing the heating requirements and processing loads downstream. The cyclonic separator performs initial phase separation, and the electrostatic coalescer completes the water removal, eliminating the need for extensive downstream heating and treatment.
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 approach enhances the separation efficiency, reduces equipment size and operational costs, and allows for upstream water separation, minimizing heating requirements and downstream processing needs.
Implementation Method 1
The cyclonic separator is configured to induce cyclonic flow of the multi-phase fluid stream to separate the multi-phase fluid stream into a gas stream and a liquid stream
Implementation Method 2
The cyclonic separator is configured to induce cyclonic flow of the multi-phase fluid stream to separate the multi-phase fluid stream into a gas stream and a liquid stream
Implementation Method 3
The electrostatic coalescer is configured to demulsify the liquid stream by causing coalescence of liquid droplets of one of the first or second liquid phases
Data Source
AI summary
A crude oil demulsification system includes a vessel. A cyclonic separator is disposed outside the vessel. The cyclonic separator is configured to receive and separate phases of a multi-phase fluid stream into a gaseous stream and a liquid stream that includes a first liquid phase and a second liquid phase by inducing cyclonic flow. A heat exchanger is fluidically connected to the cyclonic separator. The heat exchanger is disposed outside the vessel, and is configured to receive the liquid stream and to heat the liquid stream by exchanging heat with a heating medium flowed through the heat exchanger. An electrostatic coalescer is fluidically connected to the heat exchanger and is disposed inside the vessel. The electrostatic coalescer is configured to receive the liquid stream heated by the heat exchanger and to demulsify the liquid stream by causing coalescence of liquid droplets of one of the first or second liquid phases.


