# US 12,109,543 B2 · Methods and systems for operating a pump at an efficiency point > Agents: this data is available as JSON from the patentgrep API and MCP server — see https://patentgrep.com/llms.txt - Number: US 12,109,543 B2 - Document ID: US12109543B2 - Status: Granted - Kind: B2 - Application number: 18/086,757 - Filed: 2022-12-22 - Published: 2023-04-27 - Granted: 2024-10-08 - Earliest claimed: 2019-12-30 - Assignees: Marathon Petroleum Company LP - Applicants: Marathon Petroleum Company LP - Inventors: Kyle E. Miller - Web page: https://patentgrep.com/patent/US12109543B2 ## CPC - B01F 23/49: {Mixing systems, i.e. flow charts or diagrams} - B01F 23/451: by injecting one liquid into another - B01F 25/53: in which the mixture is discharged from and reintroduced into a receptacle through a recirculation tube, into which an additional component is introduced - B01F 35/833: {Flow control by valves, e.g. opening intermittently} - F04D 15/0011: {by-pass valves} - F04D 15/0016: {mixing-reversing- or deviation valves} - F04D 15/0066: {by changing the speed, e.g. of the driving engine} - F17D 3/00: Arrangements for supervising or controlling working operations - B01F 2025/919: {characterised by the disposition of the feed and discharge openings} - B01F: MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING (mixing paints B44D3/06) - F04D: NON-POSITIVE-DISPLACEMENT PUMPS (engine fuel-injection pumps F02M; ion pumps H01J41/12; electrodynamic pumps H02K44/02) - F17D: PIPE-LINE SYSTEMS; PIPE-LINES (pumps or compressors F04; fluid dynamics F15D; valves or the like F16K; pipes, laying pipes, supports, joints, branches, repairing, work on the entire line, accessories F16L; steam traps or the like F16T; fluid-pressure electric cables H01B9/06) ## Abstract Methods and systems of operating a pump at an efficiency point during an in-line blending operation. In an embodiment, such a method may include transporting a fluid from a tank to a pump through a first pipe. The method may include discharging, via the pump, the fluid at a specified flow rate through a second pipe. The method may include measuring a flow rate of the first portion of the fluid flowing from the main control valve through the mixing pipe. The method may include measuring a flow rate of the second portion of the fluid flowing through the spillback loop. The method may include determining a current pump efficiency point and operating the pump within a range of percentages of the best efficiency point. ## Claims ### Claim 1 A method of operating a pump at an efficiency point during an in-line blending operation, the method comprising: upon an initiation of an in-line blending operation: discharging, via a pump, a fluid from a tank at a specified flow rate to a main control valve and a spillback loop; determining a current pump efficiency point based on a best efficiency point and current pump speed on a pump curve; and in response to a determination that the current pump efficiency point is outside of a pre-selected range from the best efficiency point on the pump curve, adjusting, to drive the pump to operate within the pre-selected range such that the pump consumes less energy, one or more of: (1) the specified flow rate of the pump, (2) an open position of the main control valve to maintain a flow rate of a first portion of the fluid from the main control valve, and (3) an open position of a spillback control valve of the spillback loop to control a flow rate of a second portion of fluid in the spillback loop. ### Claim 2 (depends on 1) The method of claim 1, further comprising: measuring the flow rate of the first portion of the fluid flowing from the main control valve; and measuring the flow rate, defined by the open position of a spillback control valve positioned on the spillback loop, of the second portion of the fluid flowing through the spillback loop. ### Claim 3 (depends on 2) The method of claim 2, further comprising: transporting one or more additional fluids from one or more additional tanks to a mixing pipe in fluid communication with the main control valve; and admixing, in the mixing pipe, (1) the first portion of the fluid flowing from the main control valve and (2) the one or more additional fluids from the one or more additional tanks. ### Claim 4 (depends on 3) The method of claim 3, further comprising: measuring a blend flow rate of the blend of (1) the first portion of the fluid flowing from the main control valve and (2) the one or more additional fluids from the one or more additional tanks; and in response to a ratio of (a) the blend flow rate and (b) the flow rate of the first portion of the fluid flowing from the main control valve being different than a pre-set blend ratio, adjusting the blend ratio by one or more of: (1) the specified flow rate of the pump, (2) the main control valve's open position, or (3) the spillback control valve's open position. ### Claim 5 (depends on 4) The method of claim 4, wherein adjustment based on a difference between the pre-set blend ratio and the ratio of (a) the blend flow rate and (b) the flow rate of the first portion of the fluid flowing from the main control valve, occurs prior to adjustment based on the pump efficiency point being less than (1) the flow rate of the first portion of the fluid flowing from the main control valve and (2) the flow rate of the second portion of the fluid flowing through the spillback loop. ### Claim 6 (depends on 4) The method of claim 4, wherein the blend flow rate results in part from force of gravity on a flow rate of the one or more additional fluids from the one or more additional tanks. ### Claim 7 (depends on 1) The method of claim 1, wherein adjustment of the spillback control valve's open position increases or decreases the second portion of the fluid based on whether the spillback control valve's open position is increased or decreased, respectively. ### Claim 8 (depends on 1) The method of claim 1, wherein the best efficiency point is a pre-set constant value based on a model of the pump, and wherein the best efficiency point is further based on previous pump events and historical data. ### Claim 9 (depends on 8) The method of claim 8, wherein the previous pump events include pump cavitation, pump operating hours, pump maintenance events, and pump operation over or under a selected percentage of the best efficiency point. ### Claim 10 (depends on 1) The method of claim 1, wherein the fluid comprises one or more hydrocarbons. ### Claim 11 (depends on 1) The method of claim 1, wherein the pre-selected range includes about 40% to about 120% of the best efficiency point. ### Claim 12 An in-line fluid mixing system positioned at a tank farm to admix hydrocarbon liquids from a plurality of tanks into a single pipeline, the in-line fluid mixing system comprising: a first tank positioned at a tank farm containing a first fluid therein; a pump in fluid communication with the tank and configured to control a flow rate of the first fluid from the tank; a main control valve to receive a first portion of the first fluid from the pump and configured to control a flow rate of the first portion of the first fluid to a mixing pipe; a spillback loop including a spillback control valve configured to control the flow rate of the first fluid by diverting a second portion of the first fluid from the pump and diverting the second portion of the first fluid back to the pump such that the pump consumes less energy, the second portion of the first fluid based on a difference of: (1) a best efficiency point of the pump on a pump curve and (2) a current pump efficiency point of the pump on the pump curve defined by the best efficiency point and pump speed; and a second tank positioned at the tank farm containing a second fluid therein and in fluid communication with the mixing pipe to thereby transport the second fluid to the mixing pipe to form a mixture with the first portion of the first fluid and the second fluid. ### Claim 13 (depends on 12) The in-line fluid mixing system of claim 12, further comprising: a first meter positioned along the spillback loop and upstream of the spillback control valve and to measure a flow rate of the second portion of the first fluid; a second meter positioned along the mixing pipe, downstream of the main control valve, and upstream of a connection point between the second tank and mixing pipe, the second meter to measure a flow rate of the first portion of the first fluid; and a third meter positioned along the mixing pipe and downstream of the connection point between the second tank and mixing pipe, the third meter to measure a flow rate of the mixture. ### Claim 14 (depends on 12) The in-line fluid mixing system of claim 12, wherein the flow rate of the first portion of the first fluid is a based on a pre-selected mix ratio and an open position of the main control valve. ### Claim 15 (depends on 12) The in-line fluid mixing system of claim 12, wherein the diverted portion of the first fluid is based on an open position of the spillback control valve, the flow rate of the diverted portion of the first fluid, the flow rate of the first portion of the first fluid, the current pump efficiency point, and best efficiency point. ### Claim 16 (depends on 12) The in-line mixing system of claim 12, wherein, if the current pump efficiency point is less than or greater than a pre-selected range of percentages of the best efficiency point, one or more of the spillback control valve position and main control valve position are adjusted. ### Claim 17 (depends on 16) The in-line mixing system of claim 16, wherein the current pump efficiency point is determined continuously, substantially continuously, or intermittently. ### Claim 18 (depends on 16) The in-line mixing system of claim 16, wherein the flow rate of the diverted portion of the first fluid and the flow rate of the remaining portion of the first fluid fluctuates over time based on a fluid level of the first tank. ### Claim 19 (depends on 12) The in-line mixing system of claim 12, wherein the first fluid and second fluid each comprise one or more of a petroleum liquid or renewable liquid. ### Claim 20 (depends on 12) The in-line fluid mixing system of claim 12, wherein the second portion of the first fluid is further based on a difference of the current pump efficiency point from the best efficiency point within a pre-selected range of the best efficiency point. ### Claim 21 A pump efficiency point operation system positioned at a tank farm to drive a pump to operate at an efficiency point, the system comprising: a tank positioned at a tank farm containing a fluid therein; a pump including an input and an output, the input of the pump connected to the tank, the pump to control flow rate of a first fluid from the tank; a main control valve connected to the pump and to further control flow rate of the first fluid from the pump to a mixing pipe; and a spillback loop connected upstream of the pump and downstream of the pump, the spillback loop including a spillback control valve to control flow rate of the fluid by diverting a portion of the fluid from the output of the pump to the input of the pump to drive the pump to consume less energy, the diverted portion of the fluid based on a difference between a best efficiency point on a pump curve and a current pump efficiency point and speed of the pump on the pump curve. ### Claim 22 (depends on 21) The system of claim 21, wherein the mixing pipe connects to one or more additional tanks containing a different fluid therein and configured to mix the fluid from the tank and the different fluid from the one or more additional tanks. ### Claim 23 (depends on 21) The system of claim 21, wherein the pump controls the flow rate of the first fluid from the tank by operating at a set speed based on the best efficiency point, the current efficiency point, and the current pump speed. ### Claim 24 (depends on 23) The system of claim 23, wherein a portion of the fluid flowing to the main control valve is based on an open position of the spillback control valve. ### Claim 25 (depends on 23) The system of claim 23, wherein a portion of the fluid flowing from the main control valve is based on an open position of the spillback control valve and an open position of the main control valve. ### Claim 26 (depends on 21) The system of claim 21, further comprising: a spillback meter positioned along the spillback loop and upstream of the spillback control valve, the spillback meter to measure a flow rate of fluid flowing through the spillback loop; and a main meter positioned proximate and downstream the main control valve, the main meter to measure a flow rate of fluid flowing through the main control valve. ### Claim 27 (depends on 26) The system of claim 26, wherein a corrected ratio for driving the pump to operate within a pre-selected range of percentages of the best efficiency point is determined. ### Claim 28 (depends on 27) The system of claim 27, wherein the corrected ratio is based on the flow rate of fluid flowing through the spillback loop and the flow rate of fluid flowing through the main control valve. ### Claim 29 (depends on 28) The system of claim 28, wherein adjustment of one or more of the spillback control valve and main control valve is based on the corrected ratio. ### Claim 30 (depends on 21) The system of claim 21, wherein the diverted portion of the fluid is further based on a difference of the current pump efficiency point from the best efficiency point within a pre-selected range of the best efficiency point.