Cationic Surfactant Latex for Drag Reduction in Hydrocarbon Pipelines
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Solution Overview
Problem
Current drag reducing compositions for hydrocarbon liquids, particularly in pipelines, face inefficiencies due to high friction losses under turbulent flow, which are not adequately addressed by existing ultra-high molecular weight polymers.
Innovation Solution
A drag reducing composition comprising a latex polymer with a weight average molecular weight of at least 1 x 10^6 g/mol, combined with a cationic surfactant, is introduced into the hydrocarbon stream via emulsion polymerization, reducing friction loss by suppressing turbulent eddy growth.
Engineering Contradictions & Design Principles
Engineering Contradiction Analysis
1Loss of energy
If ultra-high molecular weight polymers are used as drag reducing composition, then drag reduction effectiveness is improved, but the ability to dissolve in hydrocarbon under turbulent flow deteriorates
Solution Approach 1:
The ultra-high molecular weight polymer is segmented into smaller polymer chains through controlled degradation or by designing the polymer with modular structure. This segmentation improves dissolution in hydrocarbon while maintaining sufficient drag reduction capability, as the smaller segments can disperse better in the turbulent flow environment.
Solution Approach 2:
The molecular weight parameter of the polymer is optimized to a specific range that balances drag reduction effectiveness with dissolution ability. By adjusting the molecular weight from ultra-high to high range, and controlling the degree of polymerization, the polymer achieves adequate solubility in hydrocarbon while retaining drag reduction properties.
2Ease of operation
If polymer suspension is pumped into hydrocarbon stream, then drag reducing polymer can be introduced, but friction loss reduction is insufficient
Solution Approach 1:
A solvent or dispersant is used as an intermediary medium to facilitate the transfer of polymer from suspension to hydrocarbon stream. This intermediary improves the compatibility and mixing efficiency, enabling better polymer distribution in the hydrocarbon flow and enhancing friction loss reduction.
Solution Approach 2:
The mechanical pumping method is replaced or supplemented by utilizing the natural turbulent flow of the hydrocarbon stream to carry and distribute the polymer. By designing the injection system to leverage flow dynamics rather than relying solely on mechanical pumping, the polymer is more effectively distributed throughout the stream with reduced energy input.
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
The composition effectively reduces pressure drop and friction loss in hydrocarbon pipelines, maintaining or increasing viscosity, thereby enhancing the efficiency of hydrocarbon transport.
Implementation Method 1
The latex polymer can include repeating units of the residues of C4-C20 alkyl, C6-C20 substituted or unsubstituted aryl, or aryl-substituted C1-C10 alkyl ester derivatives of methacrylic acid or acrylic acid
Implementation Method 2
A drag reducing composition comprising a latex polymer with a weight average molecular weight of at least 1 x 10^6 g/mol, combined with a cationic surfactant, is introduced into the hydrocarbon stream via emulsion polymerization, reducing friction loss by suppressing turbulent eddy growth
Implementation Method 3
The method includes polymerizing a reaction mixture via emulsion polymerization, wherein the reaction mixture comprises one or more monomers, a continuous phase, and at least one cationic surfactant
Data Source
AI summary
A drag reducing composition, methods of forming a drag reducing composition, and methods of using a drag reducing composition to reduce the pressure drop of a liquid hydrocarbon through a conduit are provided. The drag reducing composition includes a latex polymer, a cationic surfactant, optionally a nonionic surfactant, and a continuous phase. The cationic surfactant is selected from quaternary ammonium-based cationic surfactants, imidazolium-based cationic surfactants, pyridinium-based cationic surfactants, or a combination thereof.


