Controllable heat-removing reactor

Abstract

The invention discloses a controllable heat-removing reactor. A heat-removing pipe bundle comprises a water outlet main pipe, a water inlet main pipe, a ring pipe, a partition board, a cecum-type heat exchange tube and a water guide pipe; the partition board is arranged in the middle part of the ring pipe, and is used for partitioning the upper part and the lower part of the ring pipe into a water distribution box and a water collection box; the water inlet main pipe is communicated with the water distribution box at the upper part of the ring pipe; the water outlet main pipe is communicated with the water collection box at the lower part of the ring pipe; the water guide pipe is arranged inside the cecum-type heat exchange tube in a sleeving mode; one end of the cecum-type heat exchanger is open, and the other end of the cecum-type heat exchanger is closed; the open end of the cecum-type heat exchanger is communicated with the water collection box at the lower part of the ring pipe; openings are formed in the two ends of the water guide pipe; the top of the water guide pipe is communicated with the water distribution box at the upper part of the ring pipe; the bottom of the water guide pipe is positioned above the closed end of the cecum-type heat exchanger. A catalyst frame and the heat-removing pipe bundle of the controllable heat-removing reactor are separated from a pressure-bearing shell, so that maintenance, catalyst self-discharging and catalyst filling are facilitated; a heat-removing water pipe is buried inside a catalyst bed, so that the heat of reaction inside the catalyst bed can be removed in time.

Description

Technical field [0001] The present invention involves a fixed bed catalytic reaction device, which especially involves a controllable heating reactor. Background technique [0002] After the CO transformation reaction, as a widely used reactor in the chemical industry, people have improved many times to the transformation reactor. From the original full axis to the full radial, it has achieved goodThe effect, but the catalyst bed layer is still the heating reaction. The catalyst bed layer is divided into several beds. Each bed layer is indirectly replaced with heat exchange or water cooling.This indirect heat exchange recovery and transformation system has low thermal energy quality, recycling heat showing heat and low -inside heat efficiency, easy catalysts such as over temperature, and mixed with methane at the same time. [0003] The radiant synthetic synthetic reactor of the coal -to -ethylene glycol is currently used in the tube of the ф25X2 to fill the catalyst. The water i...

AI Technical Summary

Problems solved by technology

[0006] The Fischer-Tropsch synthesis reaction of coal-to-oil and coal-to-paraffin has not yet operated a large-scale device, and some small-scale Fischer-Tropsch synthesis reactors in operation are also tubular reactors, and Fe (or Co) series catalysts are packed in ф76X4 In the tube, there are still defects such as uneven gas distribution, overheating, carbon deposition, low yield of long-carbon paraffins, high resistance, equipment leakage, and difficulty in large-scale expansion.

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