Methods and systems for inline mixing of hydrocarbon liquids based on density or gravity

Patent metadata

Field	Value
Publication number	US-12066843-B2
Application number	US-202318212915-A
Country	US
Kind code	B2
Filing date	Jun 22, 2023
Priority date	Dec 30, 2019
Publication date	Aug 20, 2024
Grant date	Aug 20, 2024

Abstract

Embodiments include systems and methods of in-line mixing of hydrocarbon liquids and/or renewable liquids from a plurality of tanks into a single pipeline based on density or gravity. According to an embodiment, a method of admixing hydrocarbon liquids from a plurality of tanks into a single pipeline to provide in-line mixing thereof includes initiating a blending process. The blending process including continuously blending two or more liquids over a period of time, each of the two or more liquids stored in corresponding tanks, each of the corresponding tanks connected, via pipeline, to a blend pipe thereby blending the two or more liquids into a blended liquid. The method further includes determining a density of each of the two or more liquids to be blended during the blending process. The method includes, in response to a determination that the blend process has not finished and after the passage of a specified time interval, determining an actual blend density of the blended liquid, via a blend sensor connected to the blend pipe, the blended liquid flowing through the blend pipe and in contact with the blend sensor, and the specified time interval less than a total duration of the blending process. The method includes determining an actual blend density of the blended liquid, via a blend sensor connected to the blend pipe, the blended liquid flowing through the blend pipe and in contact with the blend sensor, and the specified time interval less than a total duration of the blending process; comparing the actual blend density with a target blend density; and in response to a difference, based on the comparison, of the actual blend density and target blend density determining a corrected ratio based on each density of the two or more liquids, the actual blend density, and the target blend density and adjusting, via one or more flow control devices, flow of one or more of the two or more liquids, based on the corrected ratio.

First claim

What is claimed is:

1. A controller for an in-line mixing system for admixing hydrocarbon liquids from one or more tanks into a single pipeline, the controller comprising:
a user interface input/output in signal communication with a user interface such that the controller is configured to:
(1) receive a target blend density, and
(2) receive a signal to initiate a hydrocarbon blending operation;

a first input in signal communication with a first density measuring device to measure a first density of a first liquid, the first density measuring device connected to a first pipe connected to a first tank of a tank farm, the first tank to store the first liquid of the first density, the first pipe to transfer the first liquid from the first tank, the controller configured to obtain the first density from the first density measuring device via the first input prior to initiation of the hydrocarbon blending operation;
a second input in signal communication with a second density measuring device to measure a second density of a second liquid, the second density measuring device connected to a second pipe connected to a second tank of the tank farm, the second tank to store the second liquid of the second density less than the first density, the second pipe to transfer the second liquid from the second tank, the controller further configured to obtain the second density from the second density measuring device via the second input prior to initiation of the hydrocarbon blending operation;
a first input/output in signal communication with a flow control device, the flow control device to adjust the flow of the second liquid from the second pipe to a mixing pipe, and the controller further configured to control the flow of the second liquid via the flow control device; and
a third input in signal communication with a third density measuring device, the third density measuring device connected to a blend pipe, the blend pipe connected to the mixing pipe and the first pipe, the blend pipe to mix the first liquid and second liquid to create a blend liquid, the blend liquid having a blend density based on the ratio of the first liquid and second liquid, the controller configured to:
after initiation of the hydrocarbon blending operation and in response to a determination that a specified time interval has lapsed:
(1) determine the blend density from the third density measuring device via the third input,
(2) compare the blend density to the target blend density, and
(3) in response to a difference, based on the comparison, between the blend density and the target blend density:
(a) determine a corrected ratio of the first liquid and second liquid, based on the first density, the second density, the blend density, and the target blend density, and
(b) adjust, via the flow control device and based on the corrected ratio, the flow of the second liquid.

2. The controller of claim 1 , wherein the controller prevents initiation of the blend process until reception of the target blend density and specified time interval.

3. The controller of claim 1 , wherein the specified time interval is determined based on a total time for the blending process and a number of times to determine the blend density.

4. The controller of claim 1 , wherein the specified time interval is received at the user interface prior to initiation of the blending process.

5. The controller of claim 1 , wherein the specified time interval comprises a set value in the controller.

6. The controller of claim 1 , wherein the specified time interval comprises a variable value set in the controller.

7. A PLC for an in-line mixing system for admixing hydrocarbon liquids from one or more tanks into a single pipeline, the PLC comprising:
a user interface input/output in signal communication with a user interface such that the PLC is configured to:
(1) receive a target blend gravity,
(2) receive a first gravity,
(3) receive a second gravity, and
(4) receive a signal to initiate a hydrocarbon blending operation;

a first input/output in signal communication with a flow control device, the flow control device to adjust a flow of a second liquid from a second pipe, the second pipe connected to a second tank of a tank farm to store a second liquid of the second gravity, to a mixing pipe, the PLC further configured to control the flow of the second liquid via the flow control device; and
a first input in signal communication with a gravity measuring device, the gravity measuring device connected to a blend pipe, the blend pipe connected to the mixing pipe and a first pipe of a first tank of a tank farm to store a first liquid of the first gravity, the blend pipe to mix the first liquid and second liquid to create a blend liquid, the blend liquid having the blend gravity, the blend gravity based on the ratio of the first liquid and second liquid, such that the PLC further is configured to:
after initiation of the hydrocarbon blending operation and in response to a determination that a specified time interval has lapsed:
(1) obtain the blend gravity from the gravity measuring device via the first input,
(2) compare the blend gravity to the target blend gravity,
(3) in response a difference, based on the comparison, between the blend gravity and the target blend gravity:
(a) determine a corrected ratio of the first liquid and second liquid, based on the first gravity, the second gravity, the blend gravity, and the target blend gravity, and
(b) adjust, via the flow control device and based on the corrected ratio, the flow of the second liquid.

8. The PLC of claim 7 , wherein the first gravity, the second gravity, the blend gravity, and the target blend gravity correlate to American Petroleum Institute (API) gravity measurements.

9. A controller for an in-line mixing system for admixing hydrocarbon liquids from one or more tanks into a blending pipeline, the controller comprising:
two or more input/outputs corresponding to and in signal communication with two or more flow control devices, the two or more flow control devices to adjust the flow of each of two or more liquids, stored in one of two or more tanks, from corresponding two or more pipes, the two or more pipes connected to one of the two or more tanks, and the two or more flow control devices connected to a blend pipe, the controller configured to adjust the flow of each of the two or more liquids via the corresponding two or more flow control devices; and
a first input in signal communication with a sensor, the sensor connected to the blend pipe, the blend pipe to mix the two or more liquids to create a blend liquid, the blend liquid having a blend gravity based on the ratio of each of the two or more liquids, such that the controller further is configured to:
after initiation of the hydrocarbon blending operation and in response to a determination that a specified time interval has lapsed:
(1) obtain the blend gravity from the sensor via the first input,
(2) compare the blend gravity to a target blend gravity,
(3) in response to a difference between the blend gravity and a target blend gravity:
(a) determine a corrected ratio of each of the two or more liquids, based on a gravity of each of the two or more liquids, the blend gravity, and the target blend gravity, and
(b) adjust, via the two or more flow control devices and based on the corrected ratio, the flow of each of the two or more liquids.

10. The controller of claim 9 , wherein each of the two or more flow control devices includes a first sensor to measure the gravity of each of the corresponding two or more liquids.

11. The controller of claim 10 , wherein each of the two or more flow control devices inc

Assignees

• Marathon Petroleum Co Lp

Inventors

• Miller Kyle E

Classifications

• B01F35/8311

  with means for controlling the motor driving the pumps or the other dispensing mechanisms · CPC title

• B01F35/2206

  Use of stored recipes for controlling the computer programs, e.g. for manipulation, handling, production or composition in mixing plants (B01F33/846 takes precedence) · CPC title

• B01F35/2202

  Controlling the mixing process by feed-back, i.e. a measured parameter of the mixture is measured, compared with the set-value and the feed values are corrected · CPC title

• B01F35/2134

  Density or solids or particle number · CPC title

• B01F35/833

  Flow control by valves, e.g. opening intermittently · CPC title