Method for carrying out chemical reactions in pseudo-isothermal conditions
View Patent ↗Method for controlling the reaction temperature in a catalytic bed ( 24 ) of a reactor ( 1 ) in which a chemical reaction takes place in pseudo-isothermal conditions by means of at least one heat exchanger ( 12 ), crossed by a respective operating fluid, immersed in the catalytic bed ( 24 ).
1. A method for controlling the reaction temperature in a catalytic bed of a reactor in which a chemical reaction takes place in pseudo-isothermal conditions by means of at least one heat exchanger, crossed by a respective operating fluid immersed in said catalytic bed, comprising the step of:
setting the velocity of said heat exchange fluid inside the respective heat exchanger within predetermined values, so that the heat transfer coefficient inside said heat exchanger is less than the heat transfer coefficient in the catalytic bed.
2. The method according to claim 1 , wherein said velocity of said heat exchange fluid inside the respective heat exchanger is regulated within values such that the heat transfer coefficient inside the heat exchangers is equal to or less than ⅔ the heat transfer coefficient inside the catalytic bed.
3. The method according to claim 1 , wherein said reactor comprises at least two heat exchangers immersed in the catalytic bed and wherein the method further comprises the steps of:
continuously detecting in said catalytic bed the temperature difference ΔT between the temperature of the catalytic bed at said heat exchangers and a limit temperature T 1 , at a middle point between said heat exchangers; and
varying the velocity of said heat exchange fluid inside said heat exchangers, according to the aforementioned temperature difference ΔT, obtaining a corresponding variation of the heat transfer coefficient inside said heat exchangers.
4. A pseudo-isothermal chemical reactor comprising:
a catalytic bed;
at least two heat exchangers immersed in said catalytic bed; and
an apparatus for adjusting the temperature inside a reaction zone of said catalytic bed defined between said heat exchangers, comprising
a probe for continuously measuring the temperature difference ΔT between the temperature in a central position of said zone and the temperature of said reaction zone at said heat exchangers,
a control unit, in data communication with said probe, and
a feeding velocity regulator for an operating fluid (F o ) in said heat exchangers, in data communication with said control unit.