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Methods for managing/assessing heat exchanger network energy efficiency and retrofit for an industrial facility, are provided. An embodiment of a method can include the performance of perform various steps/operations including those for determining an optimal heat exchanger network retrofit projects

Methods for managing/assessing heat exchanger network energy efficiency and retrofit for an industrial facility, are provided. An embodiment of a method can include the performance of perform various steps/operations including those for determining an optimal heat exchanger network retrofit projects sequence extending between a current heat exchanger network retrofit project satisfying a current desired waste energy recovery goal and a future heat exchanger network retrofit project satisfying the final waste energy recovery goal. The heat exchanger network retrofit projects sequence can be configured so that each subsequent project within the heat exchanger network retrofit projects sequence does not contradict any of the previous projects within the heat exchanger network retrofit projects sequence.

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1. A method of managing heat exchanger network energy efficiency and retrofits for an industrial facility having a plurality of process streams comprising a plurality of hot process streams and a plurality of cold process streams, the method comprising the steps of: receiving data indicating a curre

1. A method of managing heat exchanger network energy efficiency and retrofits for an industrial facility having a plurality of process streams comprising a plurality of hot process streams and a plurality of cold process streams, the method comprising the steps of: receiving data indicating a current heat transfer structure of an existing heat exchanger network for an industrial facility;graphically displaying the current heat transfer structure of the existing heat exchanger network, the graphical display including a pinch point location temperature line identifying the pinch point for the heat exchanger network and one or more connection lines indicating heat transfer between a corresponding one or more hot process streams and one or more cold process streams across the pinch point location line to provide ready identification of each heat exchanger in the heat exchanger network exchanging heat across the pinch point temperature, each of the one or more connection lines providing a linear graphical illustration of heat exchange across the pinch point location temperature line and extending between a respective hot process stream-cold process stream combination;identifying one or more process streams that primarily control the pinch point location for the existing heat exchanger network;identifying a set of one or more hot process streams having a highest impact on waste energy recovery upon reducing its respective stream specific minimum temperature approach value;identifying a maximum desired waste energy recovery goal anticipated over a life of the heat exchanger network defining a final waste energy recovery goal; anddetermining an optimal heat exchanger network retrofit projects sequence identifying a plurality of heat exchanger network retrofit projects sequentially, the heat exchanger network retrofit projects sequence extending between a current heat exchanger network retrofit project satisfying a current desired waste energy recovery goal and a future heat exchanger network retrofit project satisfying the final waste energy recovery goal, the heat exchanger network retrofit projects sequence configured so that each subsequent project within the heat exchanger network retrofit projects sequence does not contradict any of the previous projects within the heat exchanger network retrofit projects sequence. 2. A method has defined in claim 1, wherein the step of determining an optimal heat exchanger network retrofit projects sequence includes: determining a continuum of a plurality of prospective incremental pinch point location moves for a corresponding plurality of heat exchanger network retrofit design variations, the plurality of possible incremental pinch point location moves associated with an incremental decrease in stream specific minimum temperature approach values applied to one or more of the plurality of hot process streams, the continuum extending between a pinch point location associated with a heat exchanger network retrofit design satisfying the current desired waste energy recovery goal and a heat exchanger network retrofit design satisfying the final waste energy recovery goal, the final waste energy recovery goal requiring a larger amount of waste energy recovery than the current desired waste energy recovery goal, each of the corresponding plurality of heat exchanger network retrofit designs providing a progressively larger amount of waste energy recovery. 3. A method has defined in claim 1, wherein the step of determining an optimal heat exchanger network retrofit projects sequence includes: determining a pinch point location map providing an ordered description of a plurality of prospective incremental pinch point location moves associated with a corresponding plurality of heat exchanger network retrofit design variations, the plurality of incremental pinch point location moves resulting from an incremental decrease in stream specific minimum temperature approach values applied to one or more of the plurality of hot process streams, the pinch point location moves extending between a pinch point location associated with a heat exchanger network retrofit design satisfying the current desired waste energy recovery goal and a heat exchanger network retrofit design satisfying the final waste energy recovery goal, the final waste energy recovery goal requiring a larger amount of waste energy recovery than the current desired waste energy recovery goal, each of the plurality of incremental pinch point location moves associated with a corresponding heat exchanger network retrofit design providing a progressively larger amount of waste energy recovery. 4. A method has defined in claim 3, wherein the pinch point location map provides the optimal heat exchanger network retrofit projects sequence; andwherein the pinch point location map is determined by systematically performing the following for each of the plurality of hot process streams: setting the minimum temperature approach value of the respective individual hot process streams to a minimum value near or at zero with all others remaining unchanged. 5. A method as defined in claim 1, further comprising the steps of: incrementally decreasing stream specific minimum temperature approach values applied to one or more of the plurality of hot process streams to identify a plurality of incremental pinch point location moves to thereby define a plurality of heat exchanger network retrofit designs;identifying each hot process stream-cold process stream combination in each respective heat exchanger network design that is exchanging heat across an optimal pinch point defining one or more cross-pinch heat exchange conditions;performing one or more of the following rematching techniques to remove any cross-pinch heat exchange condition in each respective heat exchanger network design: connecting an affected hot to a different cold process stream and adding additional heat exchanger units above and below the pinch point; andanalyzing the resulting structure in each respective heat exchanger network design to determine feasibility of continued retrofits to thereby form the optimal heat exchanger network retrofit projects sequence. 6. A method has defined in claim 5, wherein the step of rematching is not performed on hot process stream-cold process stream combinations having a hot process stream minimum approach temperature that results in a hot stream supply temperature at least substantially equal to the cold stream target temperature and at least substantially equal hot stream and cold stream heat capacity flow rates. 7. A method as defined in claim 5, further comprising performing one or more of the following steps after performing the one or more rematching techniques to remove any cross-pinch heat exchange condition in each respective heat exchanger network design: rematching one or more of the plurality of process streams to account for one or more non-process-pinch points when existing; andrematching one or more of the plurality of process streams to account for multiple refrigeration levels when existing. 8. A method as defined in claim 1, further comprising performing the following steps for each of a plurality of heat exchanger network designs: incrementally decreasing stream specific minimum temperature approach values applied to one or more of the plurality of hot process streams to identify a plurality of incremental pinch point location moves defining a plurality of pinch point locations;identifying a hot process stream-cold process stream combination in the respective heat exchanger network design exchanging heat across a selected one of the plurality of pinch point locations defining a cross-pinch heat exchange condition; andperforming process condition manipulation, minimum temperature approach value manipulation, or both process condition manipulation and minimum temperature approach value manipulation to move the pinch point location to be completely above or completely below the hot stream and cold stream temperatures associated with the cross-pinch heat exchange condition. 9. A method as defined in claim 1, further comprising performing the following steps for each of a plurality of heat exchanger network designs: incrementally decreasing stream specific minimum temperature approach values applied to one or more of the plurality of hot process streams to identify a plurality of incremental pinch point location moves defining a plurality of pinch point locations;performing process condition manipulation, minimum temperature approach value manipulation, or both process condition manipulation and minimum temperature approach value manipulation to move a current pinch point location to a selected different one of the plurality of pinch point locations; andidentifying a hot process stream-cold process stream combination in the respective heat exchanger network design exchanging heat across the selected one of the plurality of pinch point locations defining a cross-pinch heat exchange condition; andperforming process condition manipulation, minimum temperature approach value manipulation, or both process condition manipulation and minimum temperature approach value manipulation to remedy the cross-pinch heat exchange condition. 10. A method as defined in claim 1, further comprising the steps of: identifying one or more of the plurality of process streams that control one or more pinch point location moves associated with a current heat exchanger network design that satisfies a desired increase in waste energy recovery prior to constructing a corresponding prospective heat exchanger network design that satisfies the desired waste energy recovery; andidentifying each of one or more streams specific turning point temperatures associated with the one or more pinch point location moves. 11. A method has defined in claim 1, wherein the step of determining an optimal heat exchanger network retrofit projects sequence includes: receiving minimum temperature approach value data indicating an upper and a lower range of a set of stream-specific minimum temperature approach values, the upper range of stream-specific minimum temperature approach values being a value attainable according to a current structure of the existing heat exchanger network, the lower range of stream-specific minimum temperature approach values being a lower bound set associated with a last retrofit project to be conducted at a future date at an end of the serviceable life of the heat exchanger network for the facility defining the future heat exchanger network retrofit project;systematically reducing the minimum temperature approach value between the upper range and the lower range for each separate one of the plurality of hot process streams; anddetermining a process pinch range interval identifying a range of process pinch locations responsive to the systematic reduction in minimum temperature approach values. 12. A method has defined in claim 1, wherein the step of determining an optimal heat exchanger network retrofit projects sequence includes: receiving minimum temperature approach value data indicating an upper and a lower range of a set of stream-specific minimum temperature approach values, the upper range of stream-specific minimum temperature approach values being a value attainable according to a current structure of the existing heat exchanger network, the lower range of stream-specific minimum temperature approach values being a lower bound set associated with a last retrofit project to be conducted at a future date at an end of the serviceable life of the heat exchanger network for the facility defining the future heat exchanger network retrofit project; anddetermining a process pinch range interval identifying a ranges of process pinch locations for all anticipated combinations of process conditions and heat exchanger network design modifications responsive to the minimum temperature approach value data. 13. A method as defined in claim 1, further comprising the steps of: identifying one or more hot process streams whose stream specific minimum temperature approach value adjustment will have no substantial direct effect on waste energy recovery; andidentifying one or more hot process streams whose stream specific minimum temperature approach value adjustment will not result in movement of the pinch point location. 14. A method as defined in claim 1, further comprising: performing the following steps for each separate one of the plurality of hot process streams: incrementally decreasing the stream specific minimum temperature approach value associated therewith, andperforming a temperature effect analysis for each incremental decrease in associated stream specific minimum temperature approach value;identifying one of the plurality of hot process streams having highest impact on a waste energy recovery problem responsive to the temperature effect analysis performed on each of the plurality of hot process streams; anddetermining an optimal minimum temperature approach value set satisfying one or more desired waste energy recovery goals prior to entering a design modification phase. 15. A method as defined in claim 1, further comprising the steps of: incrementally decreasing stream specific minimum temperature approach values applied to one or more of the plurality of hot process streams to identify a plurality of incremental pinch point location moves defining a plurality of different pinch point locations to thereby define a plurality of heat exchanger network retrofit design variations for a heat exchanger network design problem;determining a minimum number of required heat exchanger units associated with each separate one of the plurality of heat exchanger network retrofit design variations having corresponding different pinch point locations; anddetermining an optimal pinch point location that provides the minimum number of heat exchanger units. 16. A method as defined in claim 1, further comprising the steps of: incrementally decreasing stream specific minimum temperature approach values applied to one or more of the plurality of hot process streams to identify a plurality of incremental pinch point location moves defining a plurality of different pinch point locations; anddetermining an optimal pinch point location that provides the maximum waste energy recovery for a given set of process conditions. 17. A method as defined in claim 1, further comprising the steps of: determining a minimum number of required heat exchanger units in a certain heat exchanger network design;determining an impact on waste energy recovery of using less than a minimum number of required heat exchanger units;determining the impact on waste energy recovery of wrong matches between one or more of the plurality of hot process streams and one or more of the plurality of cold process streams according to the certain heat exchanger network design; anddetermining the impact on waste energy recovery of heat exchanger units having a less than optimal heat exchanger unit surface area for the certain heat exchanger network design with respect to capital costs. 18. A method as defined in claim 1, further comprising the step of: determining a minimum number of heat exchanger units that need to be added to a certain heat exchanger network design to attain a current waste energy recovery capability under existing process conditions and stream specific minimum temperature approach values. 19. A method as defined in claim 1, further comprising performing one or more of the following steps: moving a pinch point location for a certain heat exchanger network design through process condition modification of one or more process streams identified as controlling the pinch point location; andmoving the pinch point location through minimum temperature approach value modification of the one or more process streams identified as controlling the pinch point location. 20. A method as defined in claim 1, further comprising one or more of the following steps: defining an implicit pinch point when desired energy goals dictate a heat exchanger network design having only one but not both of the following classes of utility: a heating utility and a cooling utility; andidentifying design enhancement scenarios where a heat exchanger network design problem applied to the existing heat exchanger network and presented to satisfy the final energy recovery retrofit goal becomes a threshold problem during an optimization analysis. 21. A computer assisted method of managing heat exchanger network energy efficiency and retrofits for an industrial facility having a plurality of process streams comprising a plurality of hot process streams and a plurality of cold process streams, the method comprising the steps of: identifying one or more process streams that primarily control a pinch point location for an existing heat exchanger network;determining, by a computer, an optimal pinch point location that provides one or more of the following: a maximum waste energy recovery and a minimum number of required heat exchanger units for a given set of process conditions; anddetermining, by a computer, an optimal heat exchanger network retrofit projects sequence extending between a current heat exchanger network retrofit project satisfying a current desired waste energy recovery goal and a future heat exchanger network retrofit project satisfying a final waste energy recovery goal responsive thereto. 22. A method as defined in claim 21, wherein the step of determining an optimal heat exchanger network retrofit projects sequence comprises: establishing a continuum of a plurality of sequential retrofit plans based upon an increase in utility costs exceeding a corresponding increase in capital expenditures to increase energy efficiency which do not conflict with each respective prior retrofit plan within the sequence, the continuum of the plurality of sequential retrofit plans extending between a current retrofit plan describing a currently desired level of waste energy recovery energy efficiency and a projected desired level of waste energy recovery energy efficiency associated with a time at or near an end of a service life of the facility. 23. A method as defined in claim 21, wherein the step of determining an optimal heat exchanger network retrofit projects sequence comprises: determining a continuum of a plurality of prospective incremental pinch point location moves for a corresponding plurality of heat exchanger network retrofit design variations, the plurality of possible incremental pinch point location moves associated with an incremental decrease in stream specific minimum temperature approach values applied to one or more of the plurality of hot process streams, the continuum extending between a pinch point location associated with a heat exchanger network retrofit design satisfying the current desired waste energy recovery goal and a heat exchanger network retrofit design satisfying the final waste energy recovery goal, the final waste energy recovery goal requiring a larger amount of waste energy recovery than the current desired waste energy recovery goal, each of the corresponding plurality of heat exchanger network retrofit designs providing a progressively larger amount waste energy recovery. 24. A method has defined in claim 21, wherein the step of determining an optimal sequence of heat exchanger network retrofit includes: determining a pinch point location map providing an ordered description of a plurality of prospective incremental pinch point location moves associated with a corresponding plurality of heat exchanger network retrofit design variations, the plurality of incremental pinch point location moves resulting from an incremental decrease in stream specific minimum temperature approach values applied to one or more of the plurality of hot process streams, the pinch point location moves extending between a pinch point location associated with a heat exchanger network retrofit design satisfying the current desired waste energy recovery goal and a heat exchanger network retrofit design satisfying the final waste energy recovery goal, the final waste energy recovery goal requiring a larger amount of waste energy recovery than the current desired waste energy recovery goal, each of the plurality of incremental pinch point location moves associated with a corresponding heat exchanger network retrofit design providing a progressively larger amount of waste energy recovery. 25. A method as defined in claim 24, wherein the pinch point location map provides a heat exchanger network retrofit projects sequence identifying a plurality of heat exchanger network retrofit projects sequentially to define the optimal heat exchanger network retrofit projects sequence, each subsequent heat exchanger network retrofit project configured so as to not contradict any previous projects in the heat exchanger network retrofit projects sequence. 26. A method as defined in claim 21, further comprising the steps of: incrementally decreasing stream specific minimum temperature approach values applied to one or more of the plurality of hot process streams to identify a plurality of incremental pinch point location moves to thereby define a plurality of heat exchanger network retrofit designs;identifying each hot process stream-cold process stream combination in each respective heat exchanger network design that is exchanging heat across an optimal pinch point defining one or more cross-pinch heat exchange conditions;performing one or more of the following rematching techniques to remove any cross-pinch heat exchange condition in each respective heat exchanger network design: connecting an affected hot to a different cold process stream and adding additional heat exchanger units above and below the pinch point;performing one or more of the following steps after performing the one or more rematching techniques to remove any cross-pinch heat exchange condition in each respective heat exchanger network design: rematching one or more of the plurality of process streams to account for one or more non-process-pinch points when existing, andrematching one or more of the plurality of process streams to account for multiple refrigeration levels when existing; andanalyzing the resulting structure in each respective heat exchanger network design to determine feasibility of continued retrofits to thereby form the optimal heat exchanger network retrofit projects sequence. 27. A method as defined in claim 21, further comprising performing the following steps for each of a plurality of heat exchanger network designs: incrementally decreasing stream specific minimum temperature approach values applied to one or more of the plurality of hot process streams to identify a plurality of incremental pinch point location moves defining a plurality of pinch point locations;identifying a hot process stream-cold process stream combination in the respective heat exchanger network design exchanging heat across a selected one of the plurality of pinch point locations defining a cross-pinch heat exchange condition; andperforming process condition manipulation, minimum temperature approach value manipulation, or both process condition manipulation and minimum temperature approach value manipulation to move the pinch point location to be completely above or completely below the hot stream and cold stream temperatures associated with the cross-pinch heat exchange condition. 28. A method as defined in claim 21, further comprising the steps of: identifying one or more of the plurality of process streams that control one or more pinch point location moves associated with a current heat exchanger network design that satisfies a desired increase in waste energy recovery prior to constructing a corresponding prospective heat exchanger network design that satisfies the desired waste energy recovery; andidentifying each of one or more streams specific turning point temperatures associated with the one or more pinch point location moves. 29. A method has defined in claim 21, wherein the step of determining an optimal heat exchanger network retrofit projects sequence includes: receiving minimum temperature approach value data indicating an upper and a lower range of a set of stream-specific minimum temperature approach values, the upper range of stream-specific minimum temperature approach values being a value attainable according to a current structure of the existing heat exchanger network, the lower range of stream-specific minimum temperature approach values being a lower bound set associated with a last retrofit project to be conducted at a future date at an end of the serviceable life of the heat exchanger network for the facility defining the future heat exchanger network retrofit project; anddetermining a process pinch range interval identifying a ranges of process pinch locations for all anticipated combinations of process conditions and heat exchanger network design modifications responsive to the minimum temperature approach value data. 30. A method as defined in claim 21, further comprising the steps of: incrementally decreasing stream specific minimum temperature approach values applied to one or more of the plurality of hot process streams to identify a plurality of incremental pinch point location moves defining a plurality of different pinch point locations to thereby define a plurality of heat exchanger network retrofit design variations for a heat exchanger network design problem;determining a minimum number of required heat exchanger units associated with each separate one of the plurality of heat exchanger network retrofit design variations having corresponding different pinch point locations; anddetermining an optimal pinch point location that provides the minimum number of heat exchanger units. 31. A method as defined in claim 21, further comprising the steps of: incrementally decreasing stream specific minimum temperature approach values applied to one or more of the plurality of hot process streams to identify a plurality of incremental pinch point location moves defining a plurality of different pinch point locations; anddetermining an optimal pinch point location that provides the maximum waste energy recovery for a given set of process conditions. 32. A method as defined in claim 21, further comprising the steps of: determining a minimum number of required heat exchanger units in a certain heat exchanger network design;determining an impact on waste energy recovery of using less than a minimum number of required heat exchanger units;determining the impact on waste energy recovery of wrong matches between one or more of the plurality of hot process streams and one or more of the plurality of cold process streams according to the certain heat exchanger network design; anddetermining the impact on waste energy recovery of heat exchanger units having a less than optimal heat exchanger unit surface area for the certain heat exchanger network design with respect to capital costs. 33. A method as defined in claim 21, further comprising the step of: determining a minimum number of heat exchanger units that need to be added to a certain heat exchanger network design to attain a current waste energy recovery capability under existing process conditions and stream specific minimum temperature approach values. 34. A method as defined in claim 21, further comprising performing one or more of the following steps: moving a pinch point location for a certain heat exchanger network design through process condition modification of one or more process streams identified as controlling the pinch point location; andmoving the pinch point location through minimum temperature approach value modification of the one or more process streams identified as controlling the pinch point location. 35. A method as defined in claim 21, further comprising one or more of the following steps: defining an implicit pinch point when desired energy goals dictate a heat exchanger network design having only one but not both of the following classes of utility: a heating utility and a cooling utility; andidentifying design enhancement scenarios where a heat exchanger network design problem applied to the existing heat exchanger network and presented to satisfy the final energy recovery retrofit goal becomes a threshold problem during an optimization analysis.