System for treating renewable feedstocks with integrated hydroprocessing
A system for treating non-petroleum or renewable feedstocks comprises a reactor having a heat source for heating an interior of the reactor. The reactor receives a feedstock of a non-petroleum or renewable feedstock containing oxygen or contaminants at certain conditions to form a reactor product having gums and resins of the feedstock removed and/or reduced. A first heat exchanger cools at least a portion of the reactor product to a reduced temperature to form a reduced-temperature reactor product. A hydroprocessing reactor receives at least a portion of the reduced-temperature reactor product to form a hydroprocessed product. A second heat exchanger receives the hydroprocessed product to cool the hydroprocessed product to a temperature of 250° F. or less to form a cooled hydroprocessed product. A separator is configured to separate and remove non-condensable gases, metals and water from the cooled hydroprocessed product to form liquid hydrocarbons that form a final product.
1. A system for treating non-petroleum or renewable feedstocks containing oxygen and contaminants of one or more of metals, gums, and resins, the system comprising:
a reactor having a heat source for heating an interior of the reactor, the reactor being configured to receive a feedstock of a non-petroleum or renewable feedstock containing oxygen or contaminants of one or more of metals gums, and resins at a flow velocity of from 20 ft/sec to 100 ft/sec within the interior to facilitate heating the feedstock to a temperature of from 700° F. to 1100° F. to form a reactor product having one or more of gums and resins in the fats and/or oils of the feedstock removed and/or reduced;
a first heat exchanger configured to cool at least a portion of the reactor product to a reduced temperature to form a reduced-temperature reactor product;
a hydroprocessing reactor containing a hydroprocessing catalyst configured to receive at least a portion of the reduced-temperature reactor product to form a hydroprocessed product;
a second heat exchanger configured to receive the hydroprocessed product to cool the hydroprocessed product to a temperature of 250° F. or less to form a cooled hydroprocessed product; and
a separator configured to separate and remove non-condensable gases, metals and water from the cooled hydroprocessed product to form liquid hydrocarbons that form a final product.
2. The system of claim 1 , wherein:
the reactor is a tubular or plug flow reactor.
3. The system of claim 1 , wherein:
the reactor constitutes a primary reactor; and further comprising
at least one secondary reactor configured to receive a reactor discharge from the primary reactor, the primary reactor and the at least one secondary reactor facilitate forming the reactor product.
4. The system of claim 3 , further comprising:
a bypass line for selectively directing at least a portion of the reactor discharge as the reactor product from the primary reactor directly to the first heat exchanger bypassing the at least one secondary reactor.
5. The system of claim 1 , further comprising:
a solids separator configured to receive the reduced-temperature reactor product from the first heat exchanger to remove solids from the reduced-temperature reactor product to form a separated product without the removed solids, and wherein the hydroprocessing reactor configured to receive the separated product to form the hydroprocessed product.
6. The system of claim 5 , further comprising:
a liquid/vapor separator configured to receive the separated product to form a separated liquid stream and a separated vapor phase, and wherein the hydroprocessing reactor is configured to receive the separated vapor phase to form the hydroprocessed product.
7. The system of claim 6 , further comprising:
a separated-liquid-stream heat exchanger configured to receive and cool the separated liquid stream to form a cooled liquid stream; and
a liquid-hydrocarbon separator configured to receive the cooled liquid stream and separate liquid hydrocarbons from non-condensed gases and water present in the cooled liquid stream, the liquid-hydrocarbon separator being in fluid communication with the reactor to deliver at least a portion of separated liquid hydrocarbons to the reactor as recycle.
8. The system of claim 7 , further comprising:
a filter unit configured to receive the liquid hydrocarbons from the liquid-hydrocarbon separator and filter out solids from the separated liquid hydrocarbons, wherein the filter unit is in fluid communication with the reactor to deliver at least a portion of the filtered separated liquid hydrocarbons to the reactor as recycle.
9. The system of claim 1 , further comprising:
a filter unit configured to receive the final product and remove solids from the final product.
10. The system of claim 1 , further comprising:
a fractionation unit that receives the final product and is configured to form a fractionated product from the final product.
11. The system of claim 1 , wherein:
the separator is composed of two or more separator units to separate and remove non-condensable gases, metals and water from the cooled hydroprocessed product to form the final product.
12. The system of claim 1 , further comprising:
a pump for pressurizing the final product.
13. The system of claim 12 , further comprising:
a filter unit configured to receive the pressurized final product from the pump and remove solids from the final product.
14. The system of claim 12 , further comprising:
a stripping unit located upstream from the pump that is configured to remove light gases from the final product before the final product is delivered to the pump.
15. A system for treating non-petroleum or renewable feedstocks containing oxygen and contaminants of one or more of metals, gums, and resins, the system comprising:
a tubular or plug flow reactor having a heat source for heating an interior of the tubular or plug flow reactor, the tubular or plug flow reactor being configured to receive a feedstock of a non-petroleum or renewable feedstock containing oxygen or contaminants of one or more of metals gums, and resins at a flow velocity of from 20 ft/sec to 100 ft/sec within the interior to facilitate heating the feedstock to a temperature of from 700° F. to 1100° F. to form a reactor product having one or more of gums and resins in the fats and/or oils of the feedstock removed and/or reduced;
at least one secondary reactor configured to receive a reactor discharge from the tubular or plug flow reactor, wherein the tubular or plug flow reactor and the at least one secondary reactor facilitate forming the reactor product;
a first heat exchanger configured to cool at least a portion of the reactor product to a reduced temperature of from 250° F. to 700° F. to form a reduced-temperature reactor product;
a hydroprocessing reactor containing a hydroprocessing catalyst configured to receive at least a portion of the reduced-temperature reactor product to form a hydroprocessed product;
a second heat exchanger configured to receive the hydroprocessed product to cool the hydroprocessed product to a temperature of 250° F. or less to form a cooled hydroprocessed product; and
a separator configured to separate and remove non-condensable gases, metals and water from the cooled hydroprocessed product to form liquid hydrocarbons that are discharged from an output of the separator that form a final product.
16. The system of claim 15 , further comprising:
a bypass line for selectively directing at least a portion of the reactor discharge as the reactor product from the tubular or plug flow reactor directly to the first heat exchanger bypassing the at least one secondary reactor.
17. The system of claim 15 , further comprising:
a solids separator configured to receive the reduced-temperature reactor product from the first heat exchanger to remove solids from the reduced-temperature reactor product to form a separated product without the removed solids, and wherein the hydroprocessing reactor is configured to receive the separated product to form the hydroprocessed product.
18. The system of claim 17 , further comprising:
a liquid/vapor separator configured to receive the separated product to form a separated liquid stream and a separated vapor phase, and wherein the hydroprocessing reactor is configured to receive the separated vapor phase to form the hydroprocessed product;
a separated-liquid-stream heat exchanger configured to receive and cool the separated liquid stream to form a cooled liquid stream;
a liquid-hydrocarbon separator configured to receive the cooled liquid stream and separate liquid hydrocarbons from non-condensed gases and water present in the cooled liquid stream, the liquid-hydrocarbon separator being in fluid communication with the reactor to deliver at least a portion of separated liquid hydrocarbons to the reactor as recycle; and
a filter unit configured to receive the liquid hydrocarbons from the liquid-hydrocarbon separator and filter out solids from the separated liquid hydrocarbons, wherein the filter unit is in fluid communication with the reactor to deliver at least a portion of the filtered separated liquid hydrocarbons to the reactor as recycle and/or combined with the liquid hydrocarbons to form the final product.
19. The system of claim 15 , further comprising:
a filter unit configured to receive the final product and remove solids from the final product.
20. The system of claim 15 , further comprising:
a fractionation unit that receives the final product and is configured to form a fractionated product from the final product.