Process to mitigate the corrosion of oils/fats
View Patent ↗It has been discovered that the residence time of oils/fats in metal apparatus, particularly in the upstream of a hydrotreating unit, for example, a heat exchanger and/or a storage/feed tank, can impact significantly on corrosiveness of oils/fats in combination with and without conventional hydrocarbons. In addition, it is also found that the presence of hydrogen in the metal apparatus can also inhibit the corrosion rate of oils/fats.
1. A process comprising:
passing a feedstock comprising triglycerides and fatty acids with a co-feed gas through a metal apparatus in the absence of a catalyst, wherein the temperature in said metal apparatus is in the range of from about 150° C. to about 550° C., wherein the pressure in said metal apparatus is in the range of from about 50 psig to about 2000 psig, wherein the residence time for said feedstock in said metal apparatus is-in the range of from 0.001 hour to about 0.05 hour, wherein the gas co-feed rate is in the range of from 100 scf/b to about 10,000 scf/b, wherein said co-feed gas inhibits corrosion of the metal apparatus by said feedstock.
2. The process in accordance with claim 1 , wherein said metal apparatus is a heat exchanger or an autoclave.
3. The process in accordance with claim 1 , wherein said metal apparatus is a feed or storage tank.
4. The process in accordance with claim 1 , further comprising a step of reacting a feedstock exiting said metal apparatus with a hydrotreating catalyst in a reaction zone under a condition sufficient to produce a reaction product containing fuel range hydrocarbons.
5. The process in accordance with claim 4 wherein said fuel range hydrocarbons is diesel boiling range hydrocarbons, wherein said condition includes a pressure of less than about 2000 psig and a temperature in the range of from about 260° C. to about 430° C.
6. The process of claim 1 , wherein the co-feed gas comprises a member of the group consisting of hydrogen, nitrogen, helium, carbon monoxide, and carbon dioxide.
7. The process of claim 1 , wherein the co-feed gas is hydrogen, and reacts with the feedstock to decrease the corrosiveness of the feedstock in said metal apparatus.
8. A process comprising:
passing a feedstock comprising a mixture of triglycerides, fatty acids and conventional hydrocarbons that boil in the temperature range of from about 25° C. to about 760° C. with a co-feed gas through a metal apparatus in the absence of a catalyst, wherein the temperature in said metal apparatus is in the range of from about 150° C. to about 550° C., wherein the pressure in said metal apparatus is in the range of from about 50 psig to about 2000 psig, wherein the residence time for said feedstock in said metal apparatus is in the range of from 0.001 hour to about 0.05 hour, wherein the gas co-feed rate is in the range of from 100 scf/b to about 10,000 scf/b, wherein said co-feed gas inhibits corrosion of the metal apparatus by said feedstock.
9. The process of claim 8 , further comprising a step of reacting a feedstock exiting said metal apparatus with a hydrotreating catalyst in a reaction zone under a condition sufficient to produce a reaction product containing fuel range hydrocarbons.
10. The process in accordance with claim 9 , wherein said fuel range hydrocarbons is diesel boiling range hydrocarbons, wherein said condition includes a pressure of less than about 2000 psig and a temperature in the range of from about 260° C. to about 430° C.
11. The process of claim 8 , wherein the co-feed gas comprises a member of the group consisting of hydrogen, nitrogen, helium, carbon monoxide, and carbon dioxide.
12. The process of claim 8 , wherein the co-feed gas is hydrogen, and reacts with the feedstock to decrease the corrosiveness of the feedstock in said metal apparatus.
13. The process in accordance with claim 8 , wherein said metal apparatus is a heat exchanger or an autoclave.
14. The process in accordance with claim 8 , wherein said metal apparatus is a feed or storage tank.