Multi-fluid jet quench radial flow reactor

A flow reactor and multi-fluid technology, applied in chemical instruments and methods, chemical/physical processes, etc., can solve problems such as difficult to meet process requirements, difficult adjustment and operation, complex structure, etc., to achieve simple design, increased manufacturing difficulty, good mix effect

Active Publication Date: 2011-08-17
NANJING GOODCHINA CHEM TECH +1
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  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

[0006] The purpose of the present invention is to solve the problems of the existing axial flow two-fluid quenching reactor with complex structure, large volume, h

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  • Multi-fluid jet quench radial flow reactor
  • Multi-fluid jet quench radial flow reactor
  • Multi-fluid jet quench radial flow reactor

Examples

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Example Embodiment

[0039] The present invention will be further described below in conjunction with the drawings and embodiments.

[0040] Such as figure 2 , 3 , 4 and 5.

[0041] This example is a multi-fluid jet cold shock radial flow reactor, which includes a radial reactor shell 2. The upper end of the shell 2 is provided with a gas inlet pipe 11 communicating with the inside, and the lower end of the shell 2 It is provided with a gas outlet pipe 1 communicating with the inside. The casing 2 is provided with a number of radial catalytic beds 3, and each radial catalytic bed 3 is provided with a radial flow outer distributing cylinder 4, the radial flow outer The center of the distribution tube 4 is provided with a radial flow inner gas collecting tube 5, and a central mixing tube 9 is installed in the radial flow inner gas collecting tube 5. The radial flow inner gas collecting tube 5 and the central mixing tube 9 can exchange heat. The hot fluid in the inward flow air collector 5 can enter the...

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Abstract

The invention discloses a multi-fluid jet quench radial flow reactor, which comprises a radial reactor shell (2), and is characterized in that: a plurality of radial catalyst beds (3) are arranged in the shell (2); each radial catalyst bed (3) is provided with a radial flow external distribution cylinders (4) and a central radial flow internal gas collection cylinder (5); central mixing pipes (9)are arranged in the radial flow internal gas collection cylinders (5); multi-fluid jet quenchers (7) are arranged on the internal upper ends of the central mixing pipes (9); internal spray nozzles (12) and external spray nozzles (13) are arranged in the quenchers (7); the internal spray nozzles (12) are communicated with second quench fluid inlet pipes (8); the external spray nozzles (13) are communicated with first quench fluid inlet pipes (6); and gas mixing chambers for supplying quench gas for the radial catalyst beds (3) on a lower layer are arranged between adjacent radial catalyst beds(3), and the gas mixing chambers are communicated with the radial flow internal gas collection cylinders (5) and the central mixing pipes (9) at the same time. The reactor has the advantages of noveland simple structure, good temperature regulation performance, high operation quality and low manufacturing cost.

Description

technical field [0001] The invention relates to a chemical reactor, in particular to a chilled radial flow reactor, in particular to a fluid jet chilled radial flow reactor using multiple cold fluids as chilling sources. Background technique [0002] At present, typical chilled shock reactors are mainly axial flow reactors ( figure 1 ), consisting of a cylindrical outer cylinder and an internal multi-layer axial flow catalyst bed. There are many cold air pipes between each bed layer to introduce cold shock gas for direct cooling (removal of heat of reaction). With the increase in production capacity and considering the factors of resistance, this type of reactor will present three major problems. [0003] First, the diameter of the reactor is getting bigger and bigger (some have exceeded 12m), and the height of each catalyst bed is getting thinner and thinner (some are only 0.3m), so that the gas flow in the reactor passes through the distribution of the catalyst bed It is...

Claims

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Application Information

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IPC IPC(8): B01J8/04
Inventor 吕仲明郭新宇马新郑晓松张结喜吕航
Owner NANJING GOODCHINA CHEM TECH
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