Electrostatic Precipitator Fractionation for Oil Shale Pyrolysis
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Solution Overview
Problem
The existing rectification columns used in oil shale pyrolysis processes face challenges in controlling fractionation separation, leading to reduced productivity and significant pressure loss due to the use of packings, which complicates the efficient separation of oil fractions based on their boiling points.
Innovation Solution
The process involves dedusting and cooling the vapor gas mixture and then fractionating it in multiple electrostatic precipitator stages, each operated at temperatures corresponding to the boiling points of the respective oil fractions, replacing traditional rectification columns and eliminating the need for packings, thus enhancing efficiency and reducing pressure loss.
Engineering Contradictions & Design Principles
Engineering Contradiction Analysis
1Manufacturing precision
If traditional rectification columns with packings are used for fractionation, then oil fractions can be separated based on boiling points, but substantial pressure loss occurs over the column
Solution Approach 1:
The patent replaces the mechanical rectification column with packings with an electrostatic precipitator system that uses electrical fields for fractionation. The electrostatic precipitator applies high voltage to create an electric field that separates oil fractions based on their dielectric properties and condensation temperatures, eliminating the mechanical packings that cause pressure loss while achieving effective fractionation separation
Solution Approach 2:
The invention changes the separation parameter from boiling point-based thermal distillation to condensation temperature-based electrostatic precipitation. By controlling the temperature and voltage parameters in the electrostatic precipitator, different oil fractions are condensed and collected at different stages without the pressure loss associated with traditional rectification columns
2Manufacturing precision
If rectification columns operate with substantial reflux to control fractionation, then separation quality improves, but productivity reduces
Solution Approach 1:
The electrostatic precipitator system replaces the reflux-based separation mechanism with an electrical field-based condensation and collection process. Oil fractions are directly condensed and collected on collection plates at different temperature zones, eliminating the need for substantial reflux while maintaining high separation quality and enabling continuous operation at higher productivity rates
Solution Approach 2:
The invention enables continuous fractionation without the intermittent reflux cycles required in traditional rectification columns. The electrostatic precipitator continuously condenses and collects different oil fractions as they pass through different temperature zones, maintaining steady-state operation that improves productivity while preserving separation quality
3Reliability
If traditional scrubbers are used to remove dust particles, then dedusting is achieved, but the apparatus complexity and space requirements increase
Solution Approach 1:
The patent combines the dedusting function with the fractionation function in a single integrated electrostatic precipitator system. The same electrostatic field that separates oil fractions also captures dust particles on the collection plates, eliminating the need for separate scrubber equipment and reducing overall apparatus complexity while maintaining effective dust removal
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 allows for more efficient separation of oil fractions with minimal reflux requirement, resulting in a more compact apparatus and higher-quality products with reduced contamination, as the electrostatic precipitators effectively capture oil condensate droplets without additional energetic expense.
Implementation Method 1
The dedusted and cooled VGM are fractionated in at least two electrostatic precipitator stages at respective temperatures corresponding to respective boiling points of the oil fractions so as to separate the oil fractions
Implementation Method 2
The vapor gas mixture (a gas containing also fine particles) is then quenched in a condensation unit for winning the oil
Data Source
AI summary
A process for winning oil from a vapor gas mixture (VGM) containing a plurality of oil fractions obtained by the pyrolysis of a hydrocarbon containing material includes dedusting and cooling the VGM. The dedusted and cooled VGM are fractionated in at least two electrostatic precipitator stages at respective temperatures corresponding to respective boiling points of the oil fractions so as to separate the oil fractions.


