Method for modeling and optimizing separation process of C8-aromatics simulated moving bed
A technology for simulating moving bed and optimization method, applied in the field of modeling and optimization of C8 aromatics simulated moving bed separation process, can solve problems that are not conducive to finding the optimal operating point, triangular theory ignores axial diffusion and mass transfer resistance, and cannot be very A good description of the separation process, etc.
Patent Information
- Authority / Receiving Office
- CN · China
- Patent Type
- Applications(China)
- Current Assignee / Owner
- Publication Date
- 2015-02-04
- Estimated Expiration
- Not applicable · inactive patent
Smart Images
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Abstract
Description
technical field
[0001] The invention relates to a modeling and optimization method for C8 aromatics simulated moving bed separation process, and the method can be used for simulation and operation optimization of simulated moving bed separation process. Background technique
[0002] Paraxylene (PX) is an important organic chemical raw material and a leading product in the polyester product chain. The separation of mixed xylenes is the most difficult link in the PX production process. The main industrial methods for separating mixed xylenes include cryogenic crystallization and adsorption separation, followed by complex extraction, eutectic and sulfonation methods, among which Molecular sieve adsorption separation technology based on continuous countercurrent simulated moving bed is currently the mainstream technology for producing p-xylene.
[0003] Simulated moving bed (SMB) separation technology is a continuous countercurrent chromatographic separation technology that eme...
Examples
Embodiment 1
[0068] Such as figure 1 Shown, the operation schematic diagram of the simulated moving bed of xylene, this embodiment comprises the following steps:
[0069] 1 Determine the parameters at a specific temperature and pressure according to the actual simulated moving bed device: including design parameters (column length, column diameter, number of plates, etc.) and operating parameters (flow rate, step time, etc.), and set adsorption equilibrium kinetics parameter initial value;
[0070] 2 Determine the simulated moving bed chromatography model
[0071] This embodiment adopts the TMB model method, which assumes that the pressure and temperature are constant, the liquid phase is a diffuse plug flow, the solid phase is a plug flow, the mass transfer rate model adopts a linear driving force model, and the adsorption equilibrium is described by a Langmuir isotherm. And without considering the dead volume of the transmission line on the pollution of the inlet and outlet pipelines, ...