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

VSEngineering 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

Engineering Contradiction:
Improvesoftening pointVSAvoidmesophase pitch formation
Core Design Contradiction:
TemperatureVSObject-generated harmful factors

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.

Inventive Principle:
Principle #2Taking out (Extraction)

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.

Inventive Principle:
Principle #35Parameter changes

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

Engineering Contradiction:
Improvesoftening pointVSAvoidcapital and operating costs
Core Design Contradiction:
TemperatureVSEase of manufacture

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.

Inventive Principle:
Principle #21Skipping (Rushing through)

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.

Inventive Principle:
Principle #27Cheap short-living objects (Disposable)

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

Methodology Applied
Scientific EffectVapor-liquid equilibrium: Phase Change

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

Methodology Applied
Scientific EffectAnnular-mist flow regime: Two-Phase Flow

Implementation Method 3

separating a vapor phase and a liquid phase from the effluent in the separation vessel

Methodology Applied
Scientific EffectPhase separation: Phase Change

Implementation Method 4

Removal of lower molecular weight components typically involves heating the isotropic pitch to evaporate the lower molecular weight components

Methodology Applied
Scientific EffectEvaporation: Evaporation

Data Source

PatentUS20250101313A1System and process for increasing a softening point of isotropic pitch
Publication Date: 2025.03.27 ACP TECHNOLOGIES LLC
  • US20250101313A1 patent drawing
  • US20250101313A1 patent drawing
  • US20250101313A1 patent drawing

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.