Induction heated reactor
A tube heat exchange reactor for carrying out an endothermic catalytic reaction. The tube heat exchange reactor includes: an outer tube with a first and a second end, where the first end is an inlet end and where the second end is a closed end, an inner tube coaxially arranged within the outer tube and spaced apart from the outer tube, where at least a part of the inner tube holds a bed of catalyst material susceptible for induction heating and where the inner tube has an inlet end and an outlet end, an induction coil placed within the annular space confined between the outer and the inner tube, and a power source arranged to supply alternating current to the induction coil in order to generate an alternating magnetic field within at least a part of the inner tube.
1. A tube heat exchange reactor for carrying out an endothermic catalytic reaction, said tube heat exchange reactor comprising:
an outer tube with a first and a second end, where the first end is an inlet end and where the second end is a closed end;
an inner tube coaxially arranged within the outer tube and spaced apart from the outer tube, where at least a part of said inner tube holds a bed of catalyst material susceptible for induction heating and where said inner tube has an inlet end and an outlet end;
an induction coil placed within an annular space confined between the outer and the inner tube; and
a power source arranged to supply alternating current to the induction coil in order to generate an alternating magnetic field within at least a part of said bed of catalyst material within said inner tube,
wherein said tube heat exchange reactor is arranged to allow a process gas stream to be led into the inlet end of said outer tube, to flow in the annular space confined between the outer and inner tube towards the second end of the outer tube and subsequently into said inner tube in order to reach said bed of catalyst material and undergo an endothermic reaction resulting in a product gas, and
wherein the catalyst material comprises a ferromagnetic nanoparticle component and a catalytically active nanoparticle component on a support.
2. The tube heat exchange reactor according to claim 1 , where said inner tube is arranged to allow heat exchange, during operation, between the process gas flowing in the annular space and the product gas flowing inside the inner tube.
3. The tube heat exchange reactor according to claim 1 , wherein the tube heat exchange reactor is designed to provide a pressure difference between the outer and inner tube of up to 5 bar.
4. The tube heat exchange reactor according to claim 1 , wherein thermal insulation is provided on the outer surface of the outer tube of the tube heat exchange reactor.
5. The tube heat exchange reactor according to claim 1 , wherein said induction coil has an extent along a longitudinal axis of the tube heat exchange reactor and wherein thermal insulation is provided along at least a part of the extent of the inner tube between the outer surface of the inner tube and the induction coil.
6. The tube heat exchange reactor according to claim 1 , wherein the inner tube is of a magnetically transparent material.
7. The tube heat exchange reactor according to claim 1 , wherein the induction coil is constructed of a hollow tube arranged to let an additional stream flow through the hollow tube.
8. The tube heat exchange reactor according to claim 1 , wherein said catalyst material susceptible for induction heating comprises a mixture of the catalytically active nanoparticle component and the ferromagnetic nanoparticle component.
9. The tube heat exchange reactor according to claim 1 , wherein said catalyst material comprises one or more ferromagnetic macroscopic supports coated with an oxide, and where the oxide is impregnated with said catalytically active nanoparticle component, wherein said one or more ferromagnetic macroscopic supports being susceptible for induction heating when subject to an alternating magnetic field, and wherein said one or more ferromagnetic macroscopic supports are ferromagnetic at least at temperatures up to an upper limit a given temperature range T.
10. The tube heat exchange reactor according to claim 8 , wherein said catalytically active nanoparticle component and a powder of the ferromagnetic nanoparticle component are mixed and treated to provide bodies of catalytic mixture, said bodies having a predetermined ratio between the catalyst and ferromagnetic components.
11. The tube heat exchange reactor according to claim 8 , wherein said ferromagnetic nanoparticle component is a porous ferromagnetic material impregnated with said catalytically active nanoparticle component.
12. The tube heat exchange reactor according to claim 8 , wherein said ferromagnetic nanoparticle component comprises a plurality of ferromagnetic bodies and wherein said catalytically active nanoparticle component is impregnated on bodies of catalyst carrier material, said ferromagnetic bodies and said bodies of catalyst carrier material impregnated with catalytically active nanoparticles are mixed in a predetermined ratio.
13. The tube heat exchange reactor according to claim 1 , wherein the material of the induction coil is chosen between the following: an iron-chromium-aluminium (FeCrAl) alloy, an alloy of copper, manganese, and nickel, copper, constantan, tungsten and combinations thereof.
14. The tube heat exchange reactor according to claim 1 , wherein the annular space confined between the outer and inner tube comprises catalyst material.
15. A method of using the tube heat exchange reactor according to claim 1 for carrying out one or more of the following reactions: steam reforming, dehydrogenation of alkanes, hydrogen cyanide production, cracking of hydrocarbons, methanol cracking and ammonia cracking.