Control method and system for petrochemical industry
A control method and industry technology, applied in the petrochemical field, can solve the problems of complicated processing steps, inability to obtain control parameters, and inventory backlog
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Embodiment 1
[0104] Such as figure 1 As shown, the control method used in the petrochemical industry in this embodiment includes:
[0105] Step S1: collect or receive the production parameters processed by the refinery within a specified time;
[0106] Step S2: Under the constraints of simulating feedstock, primary processing corresponding to the crude oil distillation unit, secondary processing corresponding to the secondary processing unit, product oil blending, and shipment, use linear or nonlinear optimization to solve the production parameters, Thereby generating control parameters;
[0107] Step S3: forming a control instruction according to the control parameter;
[0108] Step S4: Control the production process of the refinery processing according to the control instruction.
[0109] Oil refining in petrochemical processing refers to petroleum refining, which is the production process of producing kerosene, gasoline, diesel, heavy oil, paraffin and other fuel oils and industrial ...
Embodiment 2
[0112] The control method for petrochemical processing described in this embodiment includes
[0113] Step 1: collect or receive the production parameters processed by the refinery within a specified time;
[0114] Step 2: Under the constraint conditions of simulating feedstock, primary processing corresponding to crude oil distillation unit, secondary processing corresponding to secondary processing unit, product oil blending and shipment, use linear or nonlinear optimization to solve the production parameters, Thereby generating control parameters;
[0115] Step 3: forming a control instruction according to the control parameter;
[0116] Step 4: Control the production process of the refinery processing according to the control instruction.
[0117] Wherein, the secondary processing corresponding to the secondary processing device is simulated using the following formula:
[0118] Σ l F ...
Embodiment 3
[0130] On the basis of Embodiment 2, this embodiment further provides a set of constraint conditions for optimizing and simulating one-time processing, specifically as follows:
[0131] The primary processing corresponding to the crude oil distillation unit is simulated using the following formula:
[0132] Σ i F i , b × Q i Σ i F i , b = Q b ,
[0133] Q bmin ≤Q b ≤Q bmax ,
[0134] Σ c F u , c ...
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