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A kind of multi-layer guide tube bubbling reactor and using method thereof

A technology of bubbling reactor and guide tube, which is applied in chemical instruments and methods, chemical methods for reacting liquids and gaseous media, chemical/physical/physical-chemical stationary reactors, etc. Exceeding the safety limit and increasing the gas content of the material in the upper part of the straight cylinder section can achieve the effect of improving flow conditions, increasing selectivity and high selectivity

Active Publication Date: 2018-07-31
CHINA PETROLEUM & CHEM CORP
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, this reactor also adopts multi-stage air intake. When air oxidation is used, because the gas contains a large amount of nitrogen, the gas holdup of the upper material in the straight barrel section will increase significantly, thereby deteriorating the flow state in the reactor; The gas from the gas distributor on the upper part of the straight barrel section of the device will escape from the liquid phase after a short period of time, and the oxygen content in the tail gas may exceed the safety limit due to the short residence time

Method used

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  • A kind of multi-layer guide tube bubbling reactor and using method thereof
  • A kind of multi-layer guide tube bubbling reactor and using method thereof
  • A kind of multi-layer guide tube bubbling reactor and using method thereof

Examples

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Embodiment 1

[0045] see figure 1 , the reactor housing 1 of the multi-layer guide tube bubble reactor is set with a multi-layer guide tube, which is a two-layer guide tube in this embodiment, including the first guide tube 3 located in the center and the outside The second guide cylinder 2, the two guide cylinders are coaxially arranged with the reactor shell 1, and have different diameters, which divide the reactor shell 1 into three-stage annular areas 4, and the height of the guide cylinders is along the center The bottom of the first draft tube 3 and the second draft tube 2 are welded and fixed to the bottom of the reactor shell 1, and the seal is guaranteed, so that the three-stage annular area can only be overflowed step by step through the top. The flow is connected in series, the first guide tube 3 at the center is connected to the liquid inlet 5, the annular area 3 of each stage and the first guide tube 3 in the center are connected to the air inlet 6, and the liquid inlet 5 and t...

Embodiment 2

[0053] see in conjunction figure 2 and image 3 , the structure of the reactor in this example is the same as in Example 1, the difference is that the draft tube in this example is a double-loop flow guide tube, specifically as figure 2 As shown, taking the second guide tube 2 as an example to illustrate the structure of the double circulation guide tube, the inner wall and the outer wall of the second guide tube 2 are coaxially fixed with a cylindrical inner circulation baffle 21 and an outer circulation flow The baffle 22, two circulation baffles are respectively fixed on the inner side and the outer side of the second flow guide tube 2 by the inner circulation fixing rib 23 and the outer circulation fixing rib 24, between the inner circulation baffle 21 and the second flow guide tube 2 1. An inner circulation area 26 and an outer circulation area 25 that circulate up and down are formed between the outer circulation baffle plate 22 and the second guide tube 2, and the in...

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Abstract

The invention discloses a bubble reactor with multiple layers of draft tubes and a using method for the bubble reactor. The multiple layers of draft tubes are sleeved by a reactor shell; the diameter of each draft tube is different; the draft tubes are used for internally dividing the reactor shell into a plurality of stages of ring-shaped areas, height of the draft tubes is gradually reduced towords the outer side along the center; the draft tube located at the center communicates with a liquid inlet; the ring-shaped area at each stage and the draft tube located at the center communicate with a gas inlet; the ring-shaped area on the outermost layer communicates with a liquid outlet; and a gas outlet is formed in the top of the reactor shell. According to the reactor disclosed by the invention, liquid-phase cyclohexane overflows layer by layer, and oxygen molecule content of introduced air is improved stage by stage to carry out oxidation reaction, so that a mass transfer rate of oxygen can be sufficiently ensured to be matched with a reaction rate, and therefore, oxidation reaction can be stably and efficiently performed. The bubble reactor improves a flowing condition in the reactor, improves selectivity of a process, and can improve cyclohexane selectivity by 1.0%-2.5% in comparison with the prior art.

Description

technical field [0001] The invention relates to a multi-layer draft tube bubbling reactor and a using method thereof. Background technique [0002] To prepare cyclohexanol and cyclohexanone, cyclohexane is usually oxidized with a gas containing molecular oxygen, first to generate an oxidation mixture (cyclohexane oxidation solution) containing cyclohexyl hydroperoxide, cyclohexanol and cyclohexanone, and then treat This oxidized mixture decomposes the cyclohexyl hydroperoxide to generate cyclohexanol and cyclohexanone, and the reaction product undergoes repeated rectification to obtain cyclohexanol and cyclohexanone, and the cyclohexane is recycled. [0003] The cyclohexane oxidation reactor is generally a bubble tower, and internal components such as a draft tube can be added to the tower to improve mass transfer, and agitation can also be added. In the bubble column, it is generally not necessary to vigorously stir the liquid phase, the gas phase can be highly dispersed i...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J19/24B01J10/00C07C27/12C07C35/08C07C29/50C07C49/403C07C45/33C07C409/06C07C407/00
Inventor 周小文刘洪武黎树根
Owner CHINA PETROLEUM & CHEM CORP
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