Temperature control in exothermic/endothermic reaction systems

Claim 2

In a hydrocarbon conversion method wherein (1) a hydrocarbonaceous charge stock is introduced into heating means in which the temperature thereof is increased prior to passing into a reaction zone and, (2) the reactions effected in said reaction are both exothermic and endothermic in nature, the method of controlling the temperature rise through said reaction zone which comprises the steps of: (a) sensing (i) the temperature of said charge stock at the inlet to said reaction zone and developing a first signal representative thereof, (ii) the temperature at an intermediate locus within said reaction zone and developing a second signal representative thereof, and, (iii) the temperature of the effluent from said reaction zone and developing a third signal representative thereof; (b) comparing said inlet charge stock temperature with that temperature specified by the adjustable set point of a temperature controller, developing a fourth signal representative of said comparison and regulating the quantity of said charge stock which is caused to bypass said heating means in response to said fourth signal; (c) measuring the difference between said first and second signals and developing a fifth signal representative of said difference; (d) measuring the difference between said second and third signals and developing a sixth signal representative of said difference; (e) comparing said fifth and sixth signals, developing a seventh signal representative of said comparison and readjusting the set point of said temperature controller in response to said seventh signal; and, (f) further regulating the quantity of said charge stock which is caused to bypass said heating means in response to the readjustment of said set point.

Claim 3

The method of claim 1 further characterized in that a selection is made of the higher of said second and third signals and said fourth signal is adjusted in response to said selected higher signal to regulate the quantity of charge stock caused to bypass said heating means.

Claim 4

The method of claim 1 further characterized in that said seventh signal represents the difference between said fifth and sixth signals.

Claim 5

The method of claim 1 further characterized in that said fourth signal is transmitted to flow control means, from the resulting adjustment of which the quantity of said charge stock caused to bypass said heating means is regulated.

Claim 6

The method of claim 1 further characterized in that the total amount of said charge stock introduced into said reaction zone remains substantially unchanged.

Claim 7

In a hydrocarbon conversion apparatus wherein (1) a hydrocarbon charge stock is passed into heating means in which its temperature is increased prior to the introduction thereof into a reaction zone and (2) the reactions effected in said zone are both exothermic and endothermic in nature, a control system for controlling the temperature rise through said reaction zone which comprises, in cooperative relationship: (a) first temperature-sensing means, co-acting with first temperature-indicating means, sensing the temperature of said charge stock at the inlet to said reaction zone and developing a first signal representative thereof; (b) second temperature-sensing means, co-acting with second temperature-indicating means, sensing the temperature at an intermediate locus within said reaction zone and developing a second signal representative thereof; (c) third temperature-sensing means, co-acting with third temperature-indicating means, sensing the temperature of the effluent from said reaction zone and developing a third signal representative thereof; (d) means for regulating the quantity of said charge stock caused to bypass said heating means; (e) first signal transmitting means for transmitting said first signal to set point-adjustable temperature control means developing a fourth signal representative of a comparison between said first signal and said set point; (f) second signal-transmitting means for transmitting said fourth signal to said regulating means whereby the quantity of said charge stock bypassing said heating means is adjusted in response thereto; (g) first differential temperature means measuring the difference between said first and second signals and developing a fifth signal representing said difference; (h) second differential temperature means measuring the difference between said second and third signals and developing a sixth signal representing said difference; (i) means for comparing said fifth and sixth signals, and developing a seventh signal representing the comparison; and, (j) third signal-transmitting for transmitting said seventh signal to said set point-adjustable temperature control means, to adjust said set point in response thereto.

Claim 8

In a hydrocarbon conversion apparatus wherein (1) a hydrocarbon charge stock is passed into heating means in which its temperature is increased prior to the introduction thereof into a reaction zone and (2) the reactions effected in said zone are both exothermic and endothermic in nature, a control system for controlling the temperature rise through said reaction zone which comprises, in cooperative relationship: (a) first temperature-sensing means, co-acting with first temperature-indicating means, sensing the temperature of said charge stock at the inlet to said reaction zone and developing a first signal representative thereof; (b) second temperature-sensing means, co-acting with second temperature-indicating means, sensing the temperature at an intermediate locus within said reaction zone and developing a second signal representative thereof; (c) third temperature-sensing means, co-acting with third temperature-indicating means, sensing the temperature of the effluent from said reaction zone and developing a third signal representative thereof; (d) means for regulating the quantity of said charge stock caused to bypass said heating means; (e) first signal transmitting means for transmitting said first signal to set point-adjustable temperature control means developing a fourth signal representative of a comparison between said first signal and said set point; (f) second signal-transmitting means for transmitting said fourth signal to said regulating means whereby the quantity of said charge stock bypassing said heating means is adjusted in response thereto; (g) first differential temperature means measuring the difference between said first and second signals and developing a fifth signal representing said difference; (h) second differential temperature means measuring the difference between said second and third signals and developing a sixth signal representing said difference; (i) means for comparing said fifth and sixth signals, and developing a seventh signal representing the comparison; and, (j) third signal-transmitting for transmitting said seventh signal to said set point-adjustable temperature control means, to adjust said set point in response thereto.

Claim 9

The apparatus of claim 6 additionally comprising fourth and fifth signal-transmitting means respectively transmitting said second and third signals to signal selecting means and adjusting said fourth signal responsive to the higher of said second and third signals.