Multi-tubular chemical reactor with igniter for initiation of gas phase exothermic reactions
A multi-tubular chemical reactor ( 400 ) includes an igniter ( 435 ) for the initiation of gas phase exothermic reaction within the gas phase reaction zones ( 409 ) of the tubular reactor units ( 408 ). A method of carrying out a gas phase exothermic reaction within the multi-tubular chemical reactor comprising: introducing gaseous reactants into a tubular reactor unit ( 408 ); initiating with radiant heat an exothermic reaction of the gaseous reactants within the reactor unit; and transferring heat produced by the exothermic reaction occurring within the gas phase reaction zone of the reactor unit to the gas phase reaction zone of one or more adjacent reactor units ( 408 ), thereby initiating an exothermic reaction within at least one adjacent reactor unit ( 408 ) until in such manner an exothermic reaction has been initiated in each of the plurality of spaced-apart reactor units ( 408 ).
1. A multi-tubular chemical reactor comprising:
(a) a plurality of spaced-apart reactor units, each reactor unit comprising an elongate tube having a wall with an internal surface and an external surfaces and a wall interior between the internal and external surfaces, at least a portion of the wall interior adapted to function as a gas phase reaction zone, the interior surface of the wall enclosing a gaseous flow passageway having an inlet at one end and an outlet at the opposing end, the interior surface of the wall adapted to permit gas flowing through the passageway to enter the wall interior at the gas phase reaction zone; and,
(b) at least one igniter adapted to initiate a gas phase exothermic reaction within the gas phase reaction zone of the wall interior of at least one of the reactor units, the igniter comprising a radiant heat-producing electrical element positioned in thermal communication with and proximity to, but in physical isolation from, the gas phase reaction zone of the at least one reactor unit, the radiant heat-producing electrical igniter constructed, positioned and adapted such that when operated, the igniter will produce sufficient radiant heat and direct that heat to and into the gas phase reaction zone and ignite the gas phase reaction within the wall interior.
2. The multi-tubular chemical reactor of claim 1 wherein the multi-tubular chemical reactor is adapted to be a partial oxidation reformer or autothermal reformer.
3. The multi-tubular chemical reactor of claim 1 wherein the maximum distance between adjacent reactor units is that distance beyond which a gas phase partial oxidation reaction fails to be initiated in an adjacent reactor unit by the heat from a gas phase partial oxidation reaction in an operating reactor unit in which a partial oxidation reaction is occurring and/or during a steady-state partial oxidation reaction mode of operation, the temperature of the plurality of spaced-apart reactor units falls below a predetermined minimum array temperature value; and the minimum distance between adjacent reactor units is that distance below which the temperature at an outlet of a reactor unit is greater than a predetermined maximum temperature value.
4. The multi-tubular chemical reactor of claim 1 further comprising at least one thermocouple disposed within a chamber comprising the plurality of spaced-apart reactor units.
5. The multi-tubular chemical reactor of claim 1 comprising a plurality of igniters, at least one igniter being disposed at one end of a chamber comprising the plurality of spaced-apart reactor units and at least one igniter being disposed at the opposite end of the chamber.
6. The multi-tubular chemical reactor of claim 1 comprising a plurality of igniters and a plurality of thermocouples disposed within a chamber comprising the plurality of spaced-apart reactor units, wherein at least one igniter and at least one thermocouple are disposed at one end of the chamber and at least one igniter and at least one thermocouple are disposed at the opposite end of the chamber.
7. The multi-tubular chemical reactor of claim 6 wherein the plurality of igniters and the plurality of thermocouples are disposed within the chamber such that at least one igniter at one end of the chamber is opposite a thermocouple at the opposite end of the chamber.
8. The multi-tubular chemical reactor of claim 1 comprising a source of gaseous reactants, the source of gaseous reactants in fluid communication with the gas phase reaction zone(s) of the reactor unit(s).
9. The multi-tubular chemical reactor of claim 1 comprising a controller for controlling the operation of the multi-tubular chemical reactor, the controller in operative communication with the at least one igniter, and if present, at least one of the at least one thermocouple and the source of gaseous reactants.
10. The multi-tubular chemical reactor of claim 1 , wherein the igniter is an electrical resistance-type igniter.
11. The multi-tubular chemical reactor of claim 1 , wherein the igniter comprises igniter means for initiating the gas phase reaction within the gas phase reaction zone.