Catalytic cracking reaction system process simulation optimization model and solution method thereof

A reaction system and catalytic cracking technology, applied in the field of petrochemical process simulation and optimization, can solve problems such as inconvenience of application, integration, and decrease in the accuracy of calculation and simulation results.

Active Publication Date: 2011-02-23
TIANJIN UNIV
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  • Abstract
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Problems solved by technology

[0004] 1 These process calculation models are developed for specific catalytic cracking feedstock oils (base feedstock oils). For feedstock oils whose properties differ greatly from those of base feedstock oils, the accuracy of calculation and simulation results will decrease
[0005] 2 Since the reaction systems of specific catalytic cracking units vary widely, in order to ensure the accuracy of calculation and simulation, a large number of device factors are set in the development process of these process calculation models, which causes inconvenience to their specific application
[0006] 3 For calculation

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  • Catalytic cracking reaction system process simulation optimization model and solution method thereof
  • Catalytic cracking reaction system process simulation optimization model and solution method thereof
  • Catalytic cracking reaction system process simulation optimization model and solution method thereof

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Embodiment Construction

[0064] The present invention is described in further detail in conjunction with accompanying drawing:

[0065] The solution environment of the catalytic cracking reaction system simulation optimization model of the present invention is AspenPlus TM Process simulation software, other software can also be used if it provides the required user model programming interface.

[0066] figure 1 is a real component or virtual group cracking reaction network, assuming that the reactions in the reaction system are all cracking reactions, and one unit of component i is cracked to generate one unit of component m and one unit of component n. The cracking reaction kinetic model involved in the solution process is provided by Gupta et al. [Gupta et al. A new generic approach for the modeling of fluid catalytic cracking (FCC) riser reactor. Association model.

[0067] For the material balance equation, it is calculated according to the following formula:

[0068] For the non-participating...

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Abstract

The invention relates to a catalytic cracking reaction system process simulation optimization model and a solution method thereof. A novel model is a model based on Gupta and the like; in order to contribute to solving the model in process simulation software such as AspenPlusTM, a new form is provided for part of expressions in a material balance equation, an energy balance equation and a fluidized state computation model; and components or stream physical property calculation subprograms provided by the process simulation software are called in the model solution process, so that the simulation optimization work of the model is finished by the process simulation software, the model is convenient to apply to engineering and the calculation result is accurate.

Description

technical field [0001] The invention relates to petrochemical process simulation and optimization technology, in particular to a catalytic cracking reaction system simulation optimization model and a solution method thereof. Background technique [0002] As the secondary processing method of crude oil with the largest processing capacity in my country, catalytic cracking occupies an extremely important position in the petroleum refining industry. The design and operation of catalytic cracking units directly affect the overall benefit of the refinery. In the design and operation stage of the catalytic cracking unit, with the help of the catalytic cracking reaction system process simulation optimization model, the necessary simulation optimization of the design and operation of the reaction system can be carried out, which can improve the design and operation level of the entire unit, thereby increasing the economy of the refinery benefit. [0003] The basis for process simul...

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Application Information

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IPC IPC(8): G06F19/00C10G11/00
Inventor 李鑫钢李国涛隋红
Owner TIANJIN UNIV
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