Method and system for optimizing top cycle oil flow rate of catalytic cracking fractionating tower during gasoline and diesel cutting process

A technology for catalytic cracking and topping cycle oil, which is applied in the distillation control/regulation of hydrocarbon oil, general control system, control/regulation system, etc., can solve the problem of excessive gasoline dry point, increase the flow rate of topping cycle oil, and fail to improve benefits, etc.

Active Publication Date: 2018-11-02
SIEMENS CHINA
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  • Application Information

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Problems solved by technology

The problem in actual production is that if you want to increase the dry point of gasoline, you need to increase the top cycle oil flow
If the flow rate is i

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  • Method and system for optimizing top cycle oil flow rate of catalytic cracking fractionating tower during gasoline and diesel cutting process
  • Method and system for optimizing top cycle oil flow rate of catalytic cracking fractionating tower during gasoline and diesel cutting process
  • Method and system for optimizing top cycle oil flow rate of catalytic cracking fractionating tower during gasoline and diesel cutting process

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Embodiment Construction

[0066] According to the present invention, the SIMIT simulation framework is used to build a dynamic model of the catalytic cracking fractionation tower, and at the same time, compared with the actual device, the dynamic model model of the catalytic cracking fractionation tower is corrected. Configure on the SIMATIC PCS7 platform to create the control environment of the distributed control system. Through graphical configuration, the computer control process of the actual industrial device is completely imitated with a realistic virtual environment, and a distributed control system simulator is established to control the catalyst The distributed control system of the gasoline and diesel cutting process of the cracking fractionation tower is simulated. Therefore, SIMIT and PCS 7 were used to establish a full-tower simulation system for the catalytic cracking fractionation tower, and to perform simulation control and global optimization of the entire catalytic cracking unit. In t...

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Abstract

The invention relates to a method for optimizing a top cycle oil flow rate of a catalytic cracking fractionating tower during a gasoline and diesel cutting process. According to the method, in order to improve the gasoline yield, a catalytic cracking fractionating tower dynamic model is established by utilizing an SIMIT simulation framework, and a distributed control system simulator is established. If an actually measured crude gasoline endpoint is less than a process card crude required value and exceeds a first predetermined value, operating parameters of the current fractionating tower areinput into the catalytic cracking fractionating tower dynamic model by means of the distributed control system simulator, so as to obtain a simulated crude gasoline endpoint and compare the simulatedcrude gasoline endpoint with the process card required endpoint, if the simulated crude gasoline endpoint is lower than the process card required endpoint and exceeds the first predetermined value, the top cycle oil flow rate in the operating parameters is increased by step-length, so as to update the simulated crude gasoline endpoint, the steps are circulated till the updated simulated crude gasoline endpoint is lower than the required endpoint and does not exceed the first predetermined value, thus the optimized cycle oil flow rate is obtained, and the optimized cycle oil flow rate is output.

Description

Technical field [0001] The invention relates to the field of petrochemical process optimization, in particular to a method and a system for optimizing the top circulating oil flow of a catalytic cracking fractionation tower in a gasoline and diesel cutting process. Background technique [0002] In the production of a catalytic cracking unit, the operating level and technical level of the fractionation tower directly affect the economic benefits of the entire unit. To study the optimal design of the catalytic cracking processing unit, the optimization of the fractionation system is very important. The method of controlling the dry point of crude gasoline by adjusting the flow rate of the top cycle oil in the catalytic fractionation column is non-real-time, delayed and usually based on experience. In the actual production process of a catalytic cracking unit, the cutting of gasoline and diesel is often a conservative operation based on experience. For example, the general gasolin...

Claims

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Application Information

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IPC IPC(8): G05B17/02C10G7/12C10G7/00
CPCC10G7/00C10G7/12G05B17/02
Inventor 宋善奎戴维
Owner SIEMENS CHINA
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