High Pressure Reactor Fouling Reduction via Segmented Temperature Control
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Solution Overview
Problem
High pressure polymerization reactors face issues with fouling due to polymer deposition on internal walls, leading to reduced cooling efficiency, reactor contamination, and potential 'decomp' reactions, which are not effectively addressed by current methods.
Innovation Solution
A method to determine the liquid-liquid equilibrium boundary and critical polymer concentration using equation of state models like Sanchez-Lacombe or PC-SAFT, allowing for the generation of phase diagrams to optimize operating conditions and maintain polymer dissolution in the liquid phase, thereby preventing fouling and improving heat transfer.
Engineering Contradictions & Design Principles
Engineering Contradiction Analysis
1Productivity
If high temperature difference between reactants and cooling medium is used to achieve highest conversion, then productivity is improved, but polymer precipitation and fouling on internal walls increases
Solution Approach 1:
The invention changes the temperature parameter profile along the reactor length, using higher temperature differences in the first region for conversion and lower temperature differences in the second region to prevent polymer precipitation and fouling, thus resolving the contradiction between productivity and fouling
Solution Approach 2:
The reactor is segmented into at least two regions with different temperature profiles: a first region with higher temperature difference for maximum conversion and a second region with lower temperature difference to maintain polymer dissolution and prevent fouling, allowing simultaneous optimization of both objectives
2Object-affected harmful factors
If cooling capacity is increased to prevent polymer deposition, then fouling is reduced, but heat transfer efficiency decreases due to impaired cooling
Solution Approach 1:
The invention dynamically adjusts the temperature profile along the reactor length, using higher temperature differences in the first region for conversion and lower temperature differences in the second region to maintain polymer dissolution and prevent fouling, thus resolving the contradiction between productivity and fouling
Solution Approach 2:
The invention changes the temperature parameter profile along the reactor length, using higher temperature differences in the first region for conversion and lower temperature differences in the second region to prevent polymer precipitation and fouling, thus resolving the contradiction between productivity and fouling
3Productivity
If reactor operating time is extended to improve productivity, then productivity is improved, but polymer deposits accumulate and require cleaning
Solution Approach 1:
The reactor is segmented into at least two regions with different temperature profiles: a first region with higher temperature difference for maximum conversion and a second region with lower temperature difference to maintain polymer dissolution and prevent fouling, allowing simultaneous optimization of both objectives
Solution Approach 2:
The invention maintains continuous polymer dissolution throughout the reactor by ensuring the temperature profile in the second region keeps the polymer in dissolved state, enabling extended operational time without accumulation of deposits that would require cleaning
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 extends reactor run time between cleanings, maintains product quality, and prevents decomposition by ensuring polymer remains dissolved, enhancing heat transfer and operational safety.
Implementation Method 1
modeling experimental or literature data for the liquid liquid equilibrium using an equation of state model
Implementation Method 2
heat transfer from the reaction to the cooling jacket is impaired
Implementation Method 3
deposition of polymer on the internal reactor wall
Data Source
AI summary
The Application of equations of state to experimental and literature data permits the formation of a model and phase diagram(s) that show under what conditions polyethylene is likely to precipitate out of a high pressure solution of polyethylene in supercritical ethylene. This then permits a better definition to run a high pressure reactor to reduce the likelihood of phase separation, loss of cooling and potentially decomposition of the reactor contents.


