Temperature control system for olefin oxidation reactor

Claim 1

An arrangement for controlling the temperature of a reactor for containing a reaction from at least one reactant to at least one product, the reactor having a feed line for the reactant and an effluent line for the product, comprising: a feed flow transmittter connected to the feed line for measuring the flow of reactant to the reactor; an effluent flow transmitter connected to the effluent line for measuring the flow of product from the reactor; a feed temperature sensor connected to the feed line for sensing the reactant temperature; an effluent temperature sensor connected to the effluent line for measuring the product temperature; reactor temperature sensing means connected to the reactor for measuring a temperature of reactor; concentration sensing means connected to the effluent line for measuring the concentration of the at least one product in the effluent line; a coolant flow line to the reactor for supplying coolant to the reactor at a coolant flow rate; coolant flow rate control means in said coolant line; and circuit means connected to said feed and effluent flow transmitters, said feed and effluent temperature sensors and said reactor temperature and concentration sensing means, for generating a coolant flow signal, said circuit means connected to said coolant flow control means for controlling the flow of coolant to the reactor according to said coolant flow signal, said circuit means receiving quantities proportional to the heat of reaction for at least one reaction in the reactor, specific heats of the reactant and product, and the heat of vaporization of the coolant, said circuit means operable to subtract a quantity proportional to an amount of heat consumed in supplying reactant to the reactor from a quantity proportional to an amount of heat generated and lost in the reactor and effluent line and to divide the resulting quantity by the specific heat of the coolant to generate the coolant flow signal wherein said circuit means is operable to generate the coolant flow signal (Q) using the formula ##EQU4## where: Q=coolant flow rate signal λ=coolant heat of vaporization F 2 =effluent flow rate y 1 =a first product condensation ΔH 1 =heat of reaction of reactant to first product y 2 =a second product concentration ΔH 2 =heat of reaction of reactant to second product C P1 =specific heat of effluent T R =reactor temperature T O =effluent temperature F 1 =feed flow rate C Pi =specific heat of feed T I =feed temperature wherein ethylene plus oxygen is supplied to the reactor as reactant and ethylene oxide plus carbon dioxide and water are generated as products, y 1 being the concentration of ethylene oxide, y 2 being the concentration of carbon dioxide, H 1 being the heat of reaction of ethylene plus oxygen to ethylene oxide, H 2 being the heat of reaction of ethylene plus oxygen to carbon dioxide.