Isotropic Pitch Softening Point via Annular-Mist Flow
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Solution Overview
Problem
Existing methods for increasing the softening point of isotropic pitch often result in the formation of mesophase pitch, which is an undesired impurity, and incur high capital and operating costs.
Innovation Solution
A process involving the mixing of a hydrocarbon feed containing isotropic pitch with a carrier gas to establish an annular-mist flow regime or a mist flow regime, allowing for the separation of vapor and liquid phases, where the liquid phase has a higher softening point due to the removal of lower molecular weight components without significant mesophase pitch formation.
Engineering Contradictions & Design Principles
Engineering Contradiction Analysis
1Temperature
If isotropic pitch is heated to evaporate lower molecular weight components to increase softening point, then the softening point increases, but mesophase pitch forms as an undesired impurity
Solution Approach 1:
The patent extracts and removes lower molecular weight components from isotropic pitch through evaporation and distillation processes. By selectively removing these lighter components (through flash evaporation, distillation, or extraction with solvents), the softening point of the remaining pitch increases while minimizing the formation of mesophase pitch, thus resolving the contradiction between increasing softening point and preventing harmful impurity formation.
Solution Approach 2:
The patent changes physical parameters such as temperature, pressure, and residence time to control the evaporation and separation processes. By optimizing these parameters (e.g., using vacuum distillation to reduce operating temperature, or controlling flash evaporation conditions), the process increases softening point while preventing the thermal conditions that would otherwise cause mesophase pitch formation.
2Temperature
If conventional distillation or vacuum distillation is used to remove lower molecular weight components, then softening point increases, but capital and operating costs increase significantly
Solution Approach 1:
The patent employs flash evaporation as a rapid separation process that achieves component removal in a single brief exposure to elevated temperature and reduced pressure, skipping the need for prolonged distillation. This rushing through the separation process in one step significantly reduces both capital equipment requirements and operating costs compared to conventional multi-stage distillation, while still achieving the desired softening point increase.
Solution Approach 2:
The patent uses relatively simple and inexpensive equipment configurations (such as flash evaporation vessels or single-stage distillation columns) rather than complex, expensive continuous distillation systems. These simpler processes achieve the necessary separation with lower capital investment and reduced operating complexity, making the manufacturing more economical while still effectively increasing softening point.
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 process effectively increases the softening point of isotropic pitch while minimizing the formation of mesophase pitch, thereby maintaining commercial value and reducing costs.
Implementation Method 1
The mixture of the hydrocarbon feed and the carrier gas approaches a vapor-liquid equilibrium in the annular-mist flow regime and/or the mist flow regime
Implementation Method 2
mixing the hydrocarbon feed with a carrier gas such that a mixture of the hydrocarbon feed and the carrier gas establishes at least one chosen from an annular-mist flow regime and a mist flow regime
Implementation Method 3
separating a vapor phase and a liquid phase from the effluent in the separation vessel
Implementation Method 4
Removal of lower molecular weight components typically involves heating the isotropic pitch to evaporate the lower molecular weight components
Data Source
AI summary
A process for increasing a softening point of isotropic pitch includes providing a hydrocarbon feed including isotropic pitch having a first softening point and mixing the hydrocarbon feed with a carrier gas such that a mixture of the hydrocarbon feed and the carrier gas establishes at least one chosen from an annular-mist flow regime and a mist flow regime. The annular-mist flow regime includes a liquid film layer and a dispersion of entrained droplets, and the mist flow regime includes a dispersion of entrained droplets. The mixture of the hydrocarbon feed and the carrier gas approaches a vapor-liquid equilibrium. The process also includes discharging an effluent of the mixture into a separation vessel and separating a vapor phase and a liquid phase in the separation vessel. The liquid phase includes isotropic pitch having a second softening point greater than the first softening point.


