Electrically heated dehydrogenation process
Systems and processes for dehydrogenating one or more alkanes using electrically heated dehydrogenation reactors. The source of electric energy or power can be a power grid, solar panel, windmill, hydropower, nuclear power, fuel cell, gas turbines, steam turbines, portable generator or the like. The systems and processes provided herein result in a simpler dehydrogenation process which is particularly beneficial at a small scale and at remote locations, including the well site.
1. A process for dehydrogenation of alkane or alkane mixtures, comprising:
providing a hydrocarbon feed stream comprising methane and one or more C 2 + hydrocarbons comprising the alkane or alkane mixtures; and
dehydrogenating at least a portion of the one or more C 2 + hydrocarbons into one or more C 2 + olefinic hydrocarbons within in an electrically heated reactor.
2. The process of claim 1 , wherein the electrical energy comes from a power grid.
3. The process of claim 1 , wherein the electrical energy comes from one or more fuel cells.
4. The process of claim 3 , wherein the fuel cell/fuel cells are hydrogen fuel cell/fuel cells.
5. The process of claim 4 , wherein the hydrogen to the fuel cell/fuel cells is one of the products from the dehydrogenation process.
6. The process of claim 1 , wherein the electrical energy comes from a power grid and one or more fuel cells.
7. The process of claim 1 , wherein the electrical energy comes from a power grid and one or more steam turbines which recover work from other heat streams in the process.
8. The process of claim 1 , wherein the electrical energy comes from one or more fuel cells and one or more steam turbines which recover work from heat streams in the process.
9. The process of claim 1 , wherein the electrical energy comes from a power grid, one or more steam turbines which recover work from heat streams in the process, and one or more fuel cells.
10. The process of claim 1 wherein the hydrocarbon feed stream is a sweet and dry shale gas mixture.
11. The process claim 1 , wherein the flowrate of the hydrocarbon feed stream is equal to or less than 200 MMSCFD, less than 50 MMSCFD or less than 20 MMSCFD.
12. The process of claim 1 wherein electrical energy for the electrically heated reactor is provided from one or more power grids, solar panels, windmills, hydropower, nuclear power, fuel cells, gas turbines, steam turbines, portable generators or combinations thereof.
13. The process of claim 1 , wherein the electrically heated dehydrogenation reactor is a tube reactor comprising one or more internally located electrically heated elements to provide direct heat transfer from the heated element to the hydrocarbon feed stream.
14. The process of claim 13 , wherein the heating element is a metal alloy strip.
15. The process of claim 13 , wherein the tube reactor comprises one or more parallel sheets as heating elements.
16. The process of any claim 13 , wherein the tube reactor comprises one or multiple spiral wounds.
17. The process of any claim 13 , wherein multiple wires of the heating element are enclosed in the reactor tube.
18. The process of any claim 13 , wherein the heating elements are thin tubes and are enclosed within the tube reactor.
19. The process of any claim 13 , wherein the tube reactor is a heating element.
20. The process claim 13 , wherein the heating element is an alloy comprising any combination of Fe, Cr, Ni, and Al.