Methods and systems for in-line mixing of hydrocarbon liquids
Methods and systems of admixing hydrocarbon liquids from a plurality of tanks into a single pipeline thereof. The system may include two or more tanks positioned at a tank farm each containing a hydrocarbon liquid therein. The system may include two or more first main pipes, each connected to one of the tanks. The system may include two or more main valves, each connected to one of the first main pipes. The system may include two or more second main pipes each connected to a corresponding main valve. The system may include two or more mixing jumpers, each connected to a corresponding first main pipe, each mixing jumper to, when a corresponding main valve is closed, control hydrocarbon liquid. The system may include a mixing pipe, connected to the second main pipes and the mixing jumpers, configured to transport hydrocarbon liquid from one or more of the tanks.
1 . A controller for in-line mixing, the controller comprising:
a first input in communication with a first one or more meters to measure a first flow rate of a first liquid, the first one or more meters positioned along a first mixing jumper, the first mixing jumper connected to a tank and a pipeline, the controller configured to obtain the first flow rate from the first one or more meters via the first input when liquids are blended;
a first output in communication with a first main valve, the first main valve positioned along a first main pipe, the first main pipe connected to the first tank and the pipeline;
a second input in communication with a second one or more meters to measure a second flow rate of a second liquid, the second one or more meters positioned along a second mixing jumper connected to a second tank and the pipeline, the controller configured to obtain the second flow rate from the second one or more meters via the second input when liquids are blended;
a second output in communication with a second main valve, the second main valve positioned along a second main pipe, the second main pipe connected to the second tank and the pipeline; and
an input/output in communication with a first control valve and a second control valve, the first control valve configured to adjust flow of the first liquid via the first mixing jumper to modify the first flow rate, and the second control valve configured to adjust flow of the second liquid via the second mixing jumper to modify the second flow rate.
2 . The controller of claim 1 , wherein the controller further is configured to:
when liquids are blended:
close the first main valve and the second main valve, and
determine whether one or more of (a) the first flow rate or (b) the second flow rate is to be modified based on one or more of (i) a target mix ratio, (ii) a ratio of the first flow rate and the second flow rate, (iii) the first flow rate, or (iv) the second flow rate.
3 . The controller of claim 2 , wherein the controller further is configured to:
in response to a determination that the first flow rate is to be modified:
adjust a position of the first control valve to modify the first flow rate, and
in response to a determination that the second flow rate is to be modified:
adjust a position of the second control valve to modify the second flow rate.
4 . The controller of claim 1 , further comprising:
a third input in communication with the first one or more meters to measure a level of liquid of the first tank, wherein the controller further is configured to obtain the level of liquid of the first tank from the first one or more meters via the third input when liquids are blended; and
a fourth input in communication with the second one or more meters to measure a level of liquid of the second tank, wherein the controller further is configured to obtain the level of liquid of the second tank from the second one or more meters via the fourth input when liquids are blended.
5 . The controller of claim 4 , wherein the level of liquid of the first tank and the level of liquid of the second tank are each obtained continuously by the controller.
6 . The controller of claim 4 , wherein the determination of whether one or more of the first flow rate or the second flow rate is to be modified includes the determination based on the level of liquid of the first tank and the level of liquid of the second tank.
7 . The controller of claim 4 , wherein the level of liquid of the first tank and the level of liquid of the second tank are each obtained intermittently by the controller.
8 . The controller of claim 4 , wherein the determination of whether one or more of the first flow rate or the second flow rate is to be modified includes the determination based on at least one of the level of liquid of the first tank or the level of liquid of the second tank.
9 . The controller of claim 8 , wherein the level of the liquid of the first tank affects the first flow rate, the level of the liquid of the second tank affects the second flow rate, and wherein the controller further is configured to adjust the first flow rate or the second flow rate to maintain the target mix ratio.
10 . The controller of claim 1 , wherein one or more of the first liquid and the second liquid comprises a hydrocarbon liquid.
11 . The controller of claim 2 , wherein the determination of whether one or more of the first flow rate or the second flow rate is to be modified includes the determination based on comparison to a percentage of error.
12 . The controller of claim 2 , further comprising
a third input in communication with the first one or more meters to measure a level of liquid of the first tank, wherein the controller further is configured to obtain the level of liquid of the first tank from the first one or more meters via the third input when liquids are blended, and
wherein the determination of whether one or more of the first flow rate or the second flow rate is to be modified includes the determination based on the level of liquid of the first tank.
13 . The controller of claim 1 , further comprising a third input in communication with the first one or more meters and the second one or more meters to measure a characteristic of a blend of the first liquid and the second liquid downstream of the first mixing jumper and the second mixing jumper, and wherein the controller further is configured to adjust the blending operation based on the characteristic of the blend.
14 . The controller of claim 1 , further comprising a third input in communication with a computing device to receive one or more target blend parameters associated with the one or more of the target mix ratio, the ratio of the first flow rate and the second flow rate, the first flow rate, or the second flow rate, and wherein the controller further is configured to adjust the blending operation based on the one or more target blend parameters.
15 . The controller of claim 1 , further comprising a third output in communication with a jumper isolation valve, the jumper isolation valve configured to close to isolate the first tank from the first mixing jumper, wherein the controller further configured to open the jumper isolation valve in response to initiation of the blending operation.
16 . The controller of claim 1 , wherein the controller further is configured to open the first main valve in response to initiation of a single fluid operation from the first tank.
17 . A controller for in-line mixing, the controller comprising:
a first input in communication with a first one or more meters to measure a first flow rate of a first hydrocarbon liquid, the first one or more meters positioned along a first mixing jumper connected to a first tank and a pipeline, the controller configured to obtain the first flow rate from the first one or more meters via the first input when liquids are blended;
a first output in communication with a first main valve, the first main valve positioned along a first main pipe connected to the first tank and the pipeline;
a second input in communication with a second one or more meters to measure a second flow rate of a second hydrocarbon liquid, the second one or more meters further positioned along a second mixing jumper connected to a second tank and the pipeline, the controller also configured to obtain the second flow rate from the second one or more meters via the second input when liquids are blended;
a second output in communication with a second main valve, the second main valve positioned along a second main pipe connected to the second tank and the pipeline; and
an input/output in communication with a first control valve and a second control valve, the first control valve configured to adjust flow of the first hydrocarbon liquid via the first mixing jumper to modify the first flow rate, the second control valve configured to adjust flow of the second hydrocarbon liquid via the second mixing jumper to modify the second flow rate.
18 . The controller of claim 17 , wherein the controller further is configured to:
when liquids are blended:
close the first main valve and the second main valve,
determine whether one or more of the first flow rate or the second flow rate is to be modified based on a comparison of one or more of a target mix ratio, a ratio of the first flow rate and the second flow rate, the first flow rate, or the second flow rate to a respective percentage of error,
in response to a determination that the first flow rate is to be modified:
adjust a position of the first control valve to modify the first flow rate, and
in response to a determination that the second flow rate is to be modified:
adjust a position of the second control valve to modify the second flow rate.
19 . The controller of claim 17 , further comprising a third output in communication with a jumper isolation valve, the jumper isolation valve configured to close to isolate the first tank from the first mixing jumper, wherein the controller further is configured to open the jumper isolation valve in response to initiation of the blending operation.
20 . A controller for in-line mixing, the controller comprising:
a first input in communication with a first one or more meters to measure a first flow rate of a first liquid, the first one or more meters positioned along a first mixing jumper connected to a first tank and a pipeline, the controller configured to obtain the first flow rate from the first one or more meters via the first input when liquids are blended;
a second input in communication with a second one or more meters to measure a second flow rate of a second liquid, the second one or more meters further positioned along a second mixing jumper connected to a second tank and the pipeline, the controller configured to obtain the second flow rate from the second one or more meters via the second input when liquids are blended;
an input/output in signal communication with a first control valve and a second control valve, the first control valve configured to adjust flow of the first liquid via the first mixing jumper to modify the first flow rate, the second control valve configured to adjust flow of the second liquid via the second mixing jumper to modify the second flow rate;
a first output in communication with a first main isolation valve, the first main isolation valve configured to close to isolate the first tank from the single pipeline and direct the first liquid toward the first mixing jumper; and
a second output in communication with a second main isolation valve, the second main isolation valve configured to close to isolate the second tank from the single pipeline and direct the second liquid toward the second mixing jumper.
21 . The controller of claim 20 , wherein the controller further is configured to:
when liquids are blended:
close the first main isolation valve and the second main isolation valve,
determine whether one or more of the first flow rate or the second flow rate is to be modified based on one or more of a target mix ratio, a ratio of the first flow rate and the second flow rate, the first flow rate, or the second flow rate,
in response to a determination that the first flow rate is to be modified:
adjust a position of the first control valve, and
in response to a determination that the second flow rate is to be modified:
adjust a position of the second control valve.
22 . The controller of claim 21 , wherein one or more of the first liquid and the second liquid comprises a hydrocarbon liquid.