Plant-wide optimization including batch operations

US11947339B2 · US · B2

Patent metadata
FieldValue
Publication numberUS-11947339-B2
Application numberUS-202017084480-A
CountryUS
Kind codeB2
Filing dateOct 29, 2020
Priority dateOct 30, 2019
Publication dateApr 2, 2024
Grant dateApr 2, 2024

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  1. Title

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  2. Abstract

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  3. Assignees and inventors

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  4. Key dates

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  5. First independent claim

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  6. CPC / IPC classifications

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  7. Citations and related patents

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Abstract

Official abstract text for this publication.

Constraints are received on initial components and intermediate components. Information is received on the products to be produced including a quantity of each of the products to be produced and a specification that specifies how the intermediate components are to be combined to form each of the products. An optimization is performed that includes the continuous conversion of initial components into the intermediate components as well as subsequent production of the products, subject to the constraints on each of the initial components, the constraints on each of the intermediate components, and the quantity of each of the products to be produced.

First claim

Opening claim text (preview).

What is claimed is: 1. A method for optimizing a process across both a continuous conversion of raw ingredients into intermediate components and a non-continuous conversion of the intermediate components into a plurality of desired products, the method comprising: a master model predictive controller (MPC) receiving first constraints on the raw ingredients available for use during a predetermined future time period; the master MPC controller receiving second constraints on the intermediate components that can be produced during the predetermined future time period based at least in part on one or more of the first constraints on the raw ingredients and inventory storage constraints for the intermediate components; the master MPC controller receiving information on a desired quantity and desired product type of each of the plurality of desired products to be produced from the intermediate components during the predetermined future time period, where production of the plurality of desired products from the intermediate components is governed at least in part by recipes that specify how the intermediate components are combined to form the plurality of desired products; the master MPC controller receiving proxy limit values from each of one or more slave MPC controllers, where each of the proxy limit values identifies to what extent one or more process variables controlled by a corresponding slave MPC controller of the one or more slave MPC controllers are adjustable without violating any constraints of the one or more process variables that are controlled by the corresponding slave M PC controller; and the master MPC controller performing plant-wide optimization collectively optimizing the continuous conversion of the raw ingredients into the intermediate components and the non-continuous conversion of the intermediate components into the desired quantity and desired product type of the plurality of desired products such that an optimized quantity of each of the intermediate components is produced to support the non-continuous conversion of the optimized quantity of the intermediate components into the desired quantity and the desired product type of each of the plurality of desired products during the predetermined future time period, and where the proxy limit values allow the master MPC controller to honor the constraints of the one or more process variables of the one or more slave MPC controllers during the plant-wide optimization. 2. The method of claim 1 , wherein the first constraints on the raw ingredients include quantity availability of one or more of the raw ingredients, timing of when one or more of the raw ingredients are available, and quality of one or more of the raw ingredients. 3. The method of claim 1 , wherein the first constraints on the raw ingredients include cost of one or more of the raw ingredients. 4. The method of claim 1 , wherein the second constraints on the intermediate components include available storage space for one or more of the intermediate components. 5. The method of claim 1 , wherein the second constraints on the intermediate components include a lower production limit for a particular intermediate component of the intermediate components as well as an upper production limit for the particular intermediate component. 6. The method of claim 1 , wherein the second constraints on the intermediate components include limitations of equipment used to produce the intermediate components. 7. The method of claim 1 , wherein the second constraints on the intermediate components include availability and/or cost of purchasing one or more of the intermediate components already formed. 8. The method of claim 1 , wherein a particular product may have a first recipe of the recipes by which the particular product may be formed from a first combination of the intermediate components and a second recipe of the recipes, different from the first recipe, by which the particular product may be formed from a second combination of the intermediate components different from the first combination. 9. The method of claim 1 , wherein the intermediate components can be combined into any of a variety of different products of the plurality of desired products, depending on relative demand for each of the variety of different products. 10. The method of claim 1 , wherein at least some of the proxy limit values received from the one or more slave MPC controllers are based on one or more MPC models used by the one or more slave MPC controllers. 11. The method of claim 1 , wherein each proxy limit value of the proxy limit values identifies a minimum value or a maximum value obtainable for one process variable of the process variables without violating any constraints of the one process variable. 12. The method of claim 1 , wherein the intermediate components are produced via the continuous conversion of the raw ingredients over a first time frame and the plurality of desired products are produced via the non-continuous conversion of the intermediate components over a second time frame different from the first time frame. 13. The method of claim 12 , wherein the intermediate components comprise electronic components, and a product of the plurality of desired products comprises one of a variety of different electronics that can be assembled using the intermediate components. 14. The method of claim 1 , wherein the raw ingredients comprise petroleum stocks and the intermediate components comprise hydrocarbons of varying chain length. 15. The method of claim 14 , wherein the plurality of desired products comprise fuels produced by combining the intermediate components. 16. A method for optimizing a process across both a continuous conversion of initial components into a plurality of intermediate components that are then used as inputs in a non-continuous conversion of the plurality of intermediate components into a plurality of desired products, the method comprising: receiving first constraints on each of one or more of the initial components; receiving second constraints on each of the plurality of intermediate components; receiving information on a quantity and type of the plurality of desired products to be produced from the plurality of intermediate components during a predetermined future period of time, and a plurality of recipes that specifies how the plurality of intermediate components are to be combined to form the plurality of desired products, wherein a particular product of the plurality of desired products includes a first recipe of the plurality of recipes by which the particular product maybe formed from a first combination of the plurality of intermediate components, and a second recipe of the plurality of recipes different from the first recipe by which the particular product maybe formed from a second combination of the plurality of intermediate components different from the first combination; performing an optimization across both the continuous conversion of the initial components into the plurality of intermediate components as well as the non-continuous production of the plurality of desired products to produce a first optimized quantity of each of the plurality of intermediate components to feed production of a second optimized quantity of each of the plurality of desired products during the future period of time, including selecting either the first recipe or the second recipe to form the particular product of the plurality of desired products, the optimization is performed subject to the first constraints on each of one or more of the initial components, the second constraints on eac

Assignees

Inventors

Classifications

  • characterised by program execution · CPC title

  • Knowledge engineering; Knowledge acquisition · CPC title

  • General predictive controller GPC · CPC title

  • G05B13/048Primary

    using a predictor · CPC title

  • Management or planning · CPC title

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Frequently asked questions

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What does patent US11947339B2 cover?
Constraints are received on initial components and intermediate components. Information is received on the products to be produced including a quantity of each of the products to be produced and a specification that specifies how the intermediate components are to be combined to form each of the products. An optimization is performed that includes the continuous conversion of initial components…
Who is the assignee on this patent?
Honeywell Int Inc
What technology area does this patent fall under?
Primary CPC classification G05B19/41835. Mapped technology areas include Physics.
When was this patent published?
Publication date Tue Apr 02 2024 00:00:00 GMT+0000 (Coordinated Universal Time) (B2). Legal status and post-grant events are not shown on this page.
What related patents are in patentsdb?
We list 10 related publications on this page (citations in our corpus or others sharing the same primary CPC).