Systems and methods for reducing rendered fats pour point
Systems and methods to reduce pour point (PP) temperatures of fat-based compositions for use in transportation fuels. In one or more embodiments, methods and systems reduce the pour point of rendered fats using biologically-derived plant oils for effectively transporting the blended fat based compositions over long distances, thereby advantageously decreasing the heating and mixing requirements needed to maintain the compositional temperature above the pour point. In certain embodiments, the fat based composition comprises rendered animal fats, such as tallow in combination with distilled corn oil (DCO).
1. A method of reducing pour point for a blended fat composition, the method comprising:
supplying (1) a selected quantity of rendered fats at a first selected temperature equal to or greater than a pour point of the rendered fats and (2) a selected quantity of a biological-based oil at a second selected temperature lower than the first selected temperature and equal to or greater than a pour point of the biological-based oil;
mixing the selected quantity of rendered fats and the selected quantity of the biological-based oil so as to define a blended fat composition which has a reduced pour point less than the pour point of the rendered fats; and
maintaining a third selected temperature of the blended fat composition during transport to a fuel processing facility.
2. The method of claim 1 , wherein the third selected temperature is based on one or more of ambient temperature, the pour point of the rendered fats, the pour point of the biological-based oil, or a pour point of the blended fat composition, and the method further comprise supplying the blended fat composition to the fuel processing facility while the third selected temperature is maintained.
3. The method of claim 2 , further comprising, in response to a change in ambient temperature, adjusting the third selected temperature so that the blended fat composition has the reduced pour point less than the pour point of the rendered fats being supplied.
4. The method of claim 2 , further comprising, after mixing the selected quantity of rendered fats and the selected quantity of the biological-based oil, sampling the blended fat composition to measure the pour point of the blended fat composition, and wherein the third selected temperature is based on a measured pour point of the blended fat composition.
5. The method of claim 1 , wherein the mixing includes by use of one or more mixing devices, the one or more mixing devices comprising one or more of a mixing tank, in-line mixing pipeline, or mixing element in a transport vehicle.
6. The method of claim 2 , wherein further use of the blended fat composition at the fuel processing facility comprises processing the blended fat composition into one or more of renewable diesel, naphtha, propane, or treated fuel gas.
7. The method of claim 2 , wherein prior to supplying of the blended fat composition to the file processing facility for further use at the fuel processing facility:
transporting the blended fat composition to a second location remote from a first location so as to maintain the blended fat composition at a temperature above the reduced pour point.
8. A method of reducing pour point for a blended fat composition to transport the blended fat composition from a first location to a second location, the method comprising:
supplying a selected quantity of rendered fats and a selected quantity of a biological-based oil to a first tank positioned at the first location, the rendered fats being supplied at a first selected temperature equal to or greater than a pour point of the rendered fats and the biological-based oil being supplied at a second selected temperature lower than the first selected temperature and equal to or greater than a pour point of the biological-based oil;
mixing the selected quantity of rendered fats and the selected quantity of the biological-based oil in the first tank so as to define a blended fat composition in the first tank, the blended fat composition having a third selected temperature less than the first selected temperature and greater than the second selected temperature and high enough so that the third selected temperature is equal to or greater than a pour point of the blended fat composition so that the blended fat composition has a reduced pour point;
maintaining the third selected temperature of the blended fat composition in the first tank so that the blended fat composition has a reduced pour point less than the pour point of the rendered fats supplied to the first tank;
supplying the blended fat composition having the reduced pour point to one or more transport vehicles, the one or more transport vehicles each configured to maintain the blended fat composition at a temperature above the reduced pour point during transport; and
transporting the blended fat composition to the second location remote from the first location so as to maintain the blended fat composition at a temperature above the reduced pour point.
9. The method of claim 8 , wherein the biological-based oil comprises one or more of technical corn oil (TCO), distillers corn oil (DCO), soybean oil, sorghum oil, canola oil, rapeseed oil, algal oil, fish oil, chufa/tigernut oil, sativa seed oil, coconut oil or combinations thereof, and wherein the first tank includes a mixing element to mix the selected quantity of rendered fats and the selected quantity of biological-based oil for a selected amount of time, thereby to form the blended fat composition, the mixing element configured to be controlled via a controller.
10. The method of claim 8 , wherein the first tank includes a heating element to maintain the third selected temperature of the blended fat composition, and the method further comprising controlling the heating element via a controller and supplying the blended fat composition from the one or more transport vehicles at the reduced pour point to the second location, thereby to process further the blended fat composition after arrival at the second location into a fuel.
11. The method of claim 8 , further comprising heating a first source of rendered fats to the first selected temperature and a source of the biological-based oil to the second selected temperature prior to supplying the selected quantity of the rendered fats and the selected quantity of the biological-based oil to the first tank.
12. The method of claim 8 , wherein the first selected temperature is equal to or greater than 90 degrees Fahrenheit and the second selected temperature is from about 90° F. to about 130° F.
13. The method of claim 8 , wherein the first tank is maintained at a temperature equal to or greater than 90 degrees Fahrenheit.
14. The method of claim 8 , wherein the one or more transport vehicles comprises one or more of a rail car, a freight hauler, or a marine vessel.
15. The method of claim 14 , wherein each of the one or more transport vehicles is configured to maintain temperature so as to be equal to or greater than 90 degrees Fahrenheit in the one or more transport vehicles and greater than the reduced pour point of the blended fat composition during a plurality of weather conditions.
16. The method of claim 8 , wherein the selected quantity of rendered fats comprises from about 0.01% weight percent to about 30% of the weight percent of the blended fat composition.
17. The method of claim 8 , wherein the rendered fats comprise one or more of tallow, choice white, grease, used cooking oil, or one or more additional fats/oils derived from bovine, ovine, piscine, porcine, or poultry.
18. The method of claim 8 , wherein the selected quantity of rendered fats and the selected quantity of the biological-based oil to the first tank is determined via one or more controllers, and wherein the supplying of the blended fat composition to the one or more transport vehicles is controlled via the one or more controllers.
19. A system to reduce pour point for a blended fat composition to transport the blended fat composition from a first location to a second location, the system comprising:
a first source of rendered fats having a selected quantity of the rendered fats at a first selected temperature equal to or greater than a pour point of the rendered fats;
a second source of a biological-based oil having a select quantity of the biological-based oil at a second selected temperature lower than the first selected temperature and equal to or greater than a pour point of the biological-based oil the biological-based oil;
a first tank positioned to receive the rendered fats from the first source and the biological-based oil from the second source at a first location, the first tank including one or more mixing elements, thereby to mix the rendered fats and the biological oil in the first tank so as to define a blend fat composition, the blended fat composition also having a reduced pour point less than the pour point of the rendered fats received by the first tank;
a first pump positioned between the first source of rendered fats and the first tank, the first pump configured to pump the rendered fats to be received by the first tank;
a first flow control valve connected to and in fluid communication with the first source of rendered fats and connected to and in fluid communication with the first tank, the first flow control valve configured to supply the selected quantity of rendered fats to the first tank;
a first meter disposed at a position between the first pump and the first tank to measure an amount of rendered fats supplied to the first tank;
a second pump positioned between the second source of the biological-based oil and the first tank, the second pump configured to pump the biological-based oil to be received by the first tank;
a second flow control valve connected to and in fluid communication with the second source of biological-based oil and connected to and in fluid communication with the first tank, the second flow control valve configured to control supply of the selected quantity of the biological-based oil to the first tank;
a second meter disposed at a position between the second pump and the first tank, thereby to measure an amount of the biological-based oil supplied to the first tank; and
a second tank positioned at the second location to receive the blended fat composition, the second tank including the mixing element and a heating element to maintain the blended fat composition at the reduced pour point.
20. The system of claim 19 , wherein a distance between the first location and the second location comprises a distance greater than or equal to 50 miles.
21. The system of claim 20 , further comprising:
a first heat source positioned at the first source of rendered fats to heat the first source of rendered fats to the first selected temperature and a second heat source positioned at the second source of biological-based oil to heat the second source to the second selected temperature;
one or more transport vehicles positioned to transport the blended fat composition to a second location remote from the first location while being configured to maintain the blended fat composition at a temperature above the reduced pour point;
a first tank pump positioned between the first tank and the one or more transport vehicles, the first tank pump configured to supply the blended fat composition to the one or more transport vehicles;
a first tank flow control valve connected to and in fluid communication with the first tank and connected to and in fluid communication with the one or more transport vehicles, the first tank flow control valve configured to supply the blended fat composition to the one or more transport vehicles to transport to the second location; and
a first tank meter disposed at a position between the first tank and the one or more transport vehicles to measure an amount of blended fat composition supplied to the one or more transport vehicles to transport to the second location.
22. The system of claim 19 , wherein the first selected temperature comprises a temperature equal to or greater than 90 degrees Fahrenheit, and wherein the second selected temperature comprises a temperature ranging from about 90 degrees Fahrenheit to about 130 degrees Fahrenheit.
23. The system of claim 19 , wherein the second location comprises a distance of greater than 50 miles from the first location, and wherein the third temperature is maintained during transporting throughout the greater than 50 miles distance.
24. The system of claim 19 , wherein the first tank is maintained at a temperature equal to or greater than 90 degrees Fahrenheit.
25. The system of claim 21 , wherein the one or more transport vehicles is selected from a rail car, a freight hauler, or a marine vessel, and wherein the biological-based oil comprises one or more of technical corn oil (TCO), distillers corn oil (DCO), soybean oil, sorghum oil, canola oil, rapeseed oil, algal oil, fish oil, chufa/tigernut oil, sativa seed oil, or coconut oil.
26. The system of claim 25 , wherein each of the one or more transport vehicles is configured to have an internal temperature equal to or greater than 90 degrees Fahrenheit, thereby to maintain temperature in the one or more transport vehicles greater than the reduced pour point of the blended fat composition in various weather conditions.
27. A controller for a system for reducing pour point of a blended fat composition to transport the blended fat composition from a first location to a second location to process the blended fat composition into a fuel, the controller comprising:
a first input/output in signal communication with a rendered fats flow control valve, the rendered fats flow control valve connected to and in fluid communication with a first source of rendered fats and connected to and in fluid communication with a first tank, the rendered fats flow control valve configured to supply a selected quantity of rendered fats to the first tank to create a blended fat composition, such that the controller is configured to adjust a flow rate of the selected quantity of rendered fats for supply to the first tank;
a second input/output in signal communication with a flow control valve, the flow control valve connected to and in fluid communication with a second source of a biological-based oil and connected to and in fluid communication with the first tank, the flow control valve configured to supply a selected quantity of the biological-based oil to the first tank to create the blended fat composition, such that the controller is configured to adjust a flow rate of a selected quantity of biological-based oil for supply to the first tank;
a third input/output in signal communication with a first tank flow control valve, the first tank flow control valve connected to and in fluid communication with the first tank and connected to and in fluid communication with one or more transport vehicles, the first tank flow control valve configured to supply a quantity of blended fat composition to the one or more transport vehicles to transport to a second location, such that the controller is configured to adjust a flow rate of the quantity of the blended fat composition for supply to the one or more transport vehicles;
a fourth input/output in signal communication with a rendered fats pump, the rendered fats pump positioned between the first source of rendered fats and the first tank, the rendered fats pump configured to supply rendered fats to the first tank such that the controller is configured to adjust the speed of the rendered fats pump thereby to modify the flow rate of the selected quantity of rendered fats supplied to the first tank;
a fifth input/output in signal communication with a first tank pump, the first tank pump positioned between the first tank and the one or more transport vehicles, the first tank pump configured to supply the blended fat composition to the one or more transport vehicles such that the controller is configured to adjust the speed of the first tank pump, to thereby modify the flow rate of a quantity of blended fat composition supplied to the first tank;
a sixth input/output in signal communication with a mixing element, the mixing element positioned at the first tank to mix the selected quantity of rendered fats and the selected quantity of biological-based oil at the first tank, such that the controller is configured to control operability of the mixing element at the first tank;
a seventh input/output in signal communication with a rendered fats flow meter, the rendered fats flow meter disposed at a position between the rendered fats pump and the first tank to measure an amount of rendered fats supplied to the first tank to create the blended fat composition, the controller configured to measure the flow rate of the rendered fats to the first tank;
an eighth input/output in signal communication with a meter, the meter disposed at a position between the pump and the first tank to measure an amount of the biological-based oil supplied to the first tank to create the blended fat composition, the controller configured to measure the flow rate of the biological-based oil to the first tank; and
a ninth input/output in signal communication with a first tank flow meter, the first tank flow meter disposed at a position between the first tank and the one or more transport vehicles to measure an amount of blended fat composition supplied to the one or more transport vehicles to transport to the second location, the controller configured to measure the flow rate of the blended fat composition from the first tank.
28. The controller of claim 27 , wherein the controller is further configured to adjust the first tank temperature equal to or greater than 90 degrees Fahrenheit.
29. The controller of claim 27 , further comprising a tenth input/output in signal communication with a first heat source, the first heat source positioned between the first source of rendered fats and the first tank, thereby to heat a quantity of the rendered fats, such that the controller is configured to adjust a first selected temperature of the quantity of the rendered fats to a temperature equal to or greater than 90 degrees Fahrenheit.
30. The controller of claim 27 , wherein the biological-based oil comprises distillers corn oil (DCO), and the controller further comprising a thirteenth input/output in signal communication with a second heat source, the second heat source positioned between the source of DCO and the first tank to heat a quantity of DCO, such that the controller is configured to adjust a second selected temperature of the quantity of DCO to a temperature equal to or greater than 100 degrees Fahrenheit.