Systems and methods for optimization of a petroleum distribution system

Patent metadata

Field	Value
Publication number	US-12486952-B2
Application number	US-202117511358-A
Country	US
Kind code	B2
Filing date	Oct 26, 2021
Priority date	Nov 16, 2020
Publication date	Dec 2, 2025
Grant date	Dec 2, 2025

Abstract

A method for optimizing a pipeline includes determining a mode of optimization and operation for the pipeline. The method also includes obtaining an objective function quantifying a performance variable as a function of one or more control decisions of the pipeline over a future time horizon. The method includes optimizing the objective function subject to one or more constraints to determine control decisions for the pipeline that result in an optimal value of the performance variable. The method includes operating equipment of the pipeline according to the control decisions.

First claim

What is claimed is:

1 . A method for optimizing a pipeline comprising:
determining a mode of optimization and operation for the pipeline from a plurality of modes of optimization and operation; obtaining an objective function quantifying a performance variable as a function of one or more control decisions of the pipeline over a future time horizon; optimizing the objective function subject to one or more constraints to determine control decisions for a plurality of pump stations of the pipeline at a plurality of geographical locations along the pipeline that result in an optimal value of the performance variable, wherein optimizing the objective function comprises using a model that predicts a movement of slugs of product through the pipeline to determine the control decisions comprising both (1) setpoints for pumps or compressors of each of the plurality of pump stations, and (2) an amount of a drag reducing agent (DRA) to add to the pipeline upstream or downstream of each of the plurality of pump stations for a type of the product such that the performance variable results in the optimal value; and operating the pumps or the compressors and injectors of the pipeline to deliver the product through the pipeline according to the control decisions; wherein the plurality of modes of optimization and operation comprise a throughput mode of optimization and operation in which the performance variable of the objective function is a delivered amount of product and the objective function is a delivery objective function, where optimizing the delivery objective function results in a determination of the control decisions that result in a maximum value of delivered amount of product over the future time horizon, wherein the plurality of modes of optimization and operation further comprises at least one of: an emissions or energy consumption mode, in which the performance variable of the objective function is energy consumption and the objective function comprises an energy objective function, wherein optimizing the objective function comprises minimizing the objective function to determine the control decisions that result in a minimum value of the performance variable over the future time horizon; and a monetary cost mode, in which the performance variable of the objective function is monetary cost and the objective function comprises a cost objective function, wherein optimizing the objective function comprises minimizing the objective function to determine the control decisions that result in a minimum value of the monetary cost over the future time horizon, and wherein the control decisions in the throughput mode are different from the control decisions in the emissions or energy consumption mode or the monetary cost mode.

2 . The method of claim 1 , wherein the method is performed for an entirety of the pipeline to determine the control decisions for the entirety of the pipeline.

3 . The method of claim 1 , wherein the method is performed for a station of the pipeline to determine the control decisions for the station of the pipeline.

4 . The method of claim 1 , wherein the objective function comprises a model of a station of the pipeline, wherein the station of the pipeline comprises a plurality of pumps arranged in series or parallel configured to pump a product through the pipeline, wherein the model of the station predicts one or more operational parameters of the station as a function of the control decisions.

5 . The method of claim 1 , wherein the control decisions are for each timestep of the future time horizon, wherein the control decisions further comprise an amount of energy to purchase from a utility provider to operate the pipeline.

6 . The method of claim 1 , wherein the pipeline is configured to ship any of a liquid product, a gas product, or a product including a mixture of liquid and gas.

7 . A pipeline comprising:
a plurality of pipeline stations, each pipeline station comprising at least one pump or compressor; a pipe connecting the plurality of pipeline stations; and a controller configured to operate in a plurality of modes of optimization and operation, the controller configured to: determine a mode of optimization and operation for the pipeline from the plurality of modes of optimization and operation; obtain an objective function quantifying a performance variable as a function of one or more control decisions of the pipeline over a future time horizon; optimize the objective function subject to one or more constraints to determine control decisions for the plurality of pipeline stations of the pipeline at a plurality of geographical locations along the pipeline that result in an optimal value of the performance variable, wherein optimizing the objective function comprises using a model that predicts a movement of slugs of product through the pipeline to determine the control decisions comprising both ( 1 ) setpoints for pumps or compressors of each of the plurality of pipeline stations, and ( 2 ) an amount of a drag reducing agent (DRA) to add to the pipeline upstream or downstream of each of the plurality of pipeline stations for a type of the product such that the performance variable results in the optimal value; and operate the pump or compressor and injectors of the pipeline to deliver the product through the pipeline according to the control decisions; wherein the plurality of modes of optimization and operation comprise a throughput mode of optimization and operation in which the performance variable of the objective function is a delivered amount of product and the objective function is a delivery objective function, wherein optimizing the delivery objective function results in a determination of the control decisions that result in a maximum value of delivered amount of product over the future time horizon, wherein the plurality of modes of optimization and operation further comprises at least one of: an emissions or energy consumption mode, in which the performance variable of the objective function is energy consumption and the objective function comprises an energy objective function, wherein optimizing the objective function comprises minimizing the objective function to determine the control decisions that result in a minimum value of the performance variable over the future time horizon; and a monetary cost mode, in which the performance variable of the objective function is monetary cost and the objective function comprises a cost objective function, wherein optimizing the objective function comprises minimizing the objective function to determine the control decisions that result in a minimum value of the monetary cost over the future time horizon, and wherein the control decisions in the throughput mode are different from the control decisions in the emissions or energy consumption mode or the monetary cost mode.

8 . The pipeline of claim 7 , wherein the controller is configured to optimize the objective function for an entirety of the pipeline to determine the control decisions for the entirety of the pipeline.

9 . The pipeline of claim 7 , wherein the controller is configured to optimize the objective function for one of the plurality of pipeline stations of the pipeline to determine the control decisions for the one of the plurality of pipeline stations of the pipeline.

10 . The pipeline of claim 7 , wherein the objective function comprises a model of at least one of the plurality of pipeline stations of the pipeline, wherein the at least one pipeline station of the pipeline comprises a plurality of the pumps arranged in series or parallel configured to pump a product through the pipeline, wherein the model of the pipeline station predicts one o

Assignees

• Sensia Llc

Inventors

• Otto Ross Allen

Classifications

• G06Q50/06 Primary

  Energy or water supply · CPC title

• G01F1/74

  Devices for measuring flow of a fluid or flow of a fluent solid material in suspension in another fluid · CPC title

• F17D1/16

  Facilitating the conveyance of liquids or effecting the conveyance of viscous products by modification of their viscosity {(changing the flow or the viscosity by adding a chemical agent C09K3/00, C10M)} · CPC title

• G06F30/28

  using fluid dynamics, e.g. using Navier-Stokes equations or computational fluid dynamics [CFD] · CPC title

• G06F2113/08

  Fluids · CPC title