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Inner loop reactor with reacting and separating functions

一种反应器、内环流的技术,应用在化学/物理/物理化学反应器的详细信息、化学仪器和方法、化学/物理过程等方向,能够解决无法起到混合和分离过程强化、流程复杂、费时等问题,达到传热效果保持良好、减少占地面积、扩展适用范围的效果

Active Publication Date: 2017-01-25
QINGDAO INST OF BIOENERGY & BIOPROCESS TECH CHINESE ACADEMY OF SCI +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0005] In the gas-liquid-solid three-phase reaction, especially for the three-phase reaction in which the catalyst is solid particles, the separation of solid particles is very important. Although CN105642201A is good in the mixing effect of the three-phase reaction, it cannot be simultaneously mixed in the reactor. Separation of solids cannot enhance the process of mixing and separation. For reactions such as Fischer-Tropsch synthesis that require separation and recycling of solids, an external separation device is required, which not only requires additional power, but also makes the process more complicated. Time-consuming, labor-intensive and increases floor space and operating expenses
Although a hydrocyclone with separation effect is added inside the CN105983377A device, the hydrocyclone is located in the gas-liquid separation area on the upper part of the reactor and only has the effect of gas-liquid separation
In addition, due to the presence of gas, the separation performance of the hydrocyclone is greatly reduced, and its application to gas-liquid-solid three-phase reactions is limited, especially when there are fine catalyst particles.

Method used

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  • Inner loop reactor with reacting and separating functions
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Examples

Experimental program
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Effect test

Embodiment 1

[0023] like figure 1 As shown, the gas enters the riser of the inner loop reactor through the gas-liquid integrated distributor (15) from the annular gap, and the liquid flows from the riser (1) to the downcomer (2) driven by the gas. There is a sealed structure between the cylindrical section of the hydrocyclone (13) and the inner wall of the downcomer (2), and all materials enter the hydrocyclone (13) horizontally and tangentially from the inlet (4) of the hydrocyclone, and are separated Finally, the slurry containing solid catalyst particles is discharged from the bottom flow port (14) of the hydrocyclone, and the inner member (5) of the anti-flow dead zone can effectively prevent the accumulation of catalyst particles at the bottom flow port (14) of the hydrocyclone And lead to the riser, so as to ensure that the catalyst can be fully recycled. The reacted product is discharged as a light phase from the overflow port (12) through the hollow structure between the hydrocycl...

Embodiment 2

[0025] In this embodiment, the gas enters the riser of the inner loop reactor from the inner cylinder through the gas-liquid integrated distributor (15), and the liquid flows from the riser (1) to the downcomer (2) driven by the gas. There is a sealed structure between the cylindrical section of the hydrocyclone (13) and the inner wall of the downcomer (2), and all materials enter the hydrocyclone (13) horizontally and tangentially from the inlet of the hydrocyclone (4), preventing flow The inner member (5) in the dead zone can effectively prevent catalyst particles from accumulating at the lower part of the hydrocyclone bottom flow port (14) and guide them to the riser, thereby ensuring that the catalyst can be recycled. After separation, the slurry containing solid catalyst particles is discharged from the bottom outlet (14) of the hydrocyclone, and enters the riser again for the next cycle. The reacted product is discharged as a light phase from the overflow port (12) throu...

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Abstract

The invention relates to an inner loop reactor with reacting and separating functions. The reactor comprises a rising pipe, a downspout, a solid feeding port, a hydrocyclone inlet, an anti-flowing dead zone internal component, a liquid inlet, an air inlet, an air outlet, a flow guide drum, an air flow guide cone, an air vent, an overflow port, a hydrocyclone, a bottom flow port, an air-liquid integrated distributor and a liquid outlet, wherein the hydrocyclone is arranged at the lower part of the downspout of the loop reactor; the air flow guide cone and the air vent exist in the downspout, so that air can be prevented from entering the hydrocyclone; after the slurry enters the hydrocyclone, the solid-containing slurry enters the rising pipe through the bottom flow port, and clean products without solids flow out from a top flow port; and an external valve is used for controlling the flow of the clean products. The inner loop reactor has a simple structure, is low in cost, requires no special liquid-solid separating device, can simultaneously perform air-liquid-solid three-phase reaction, mass transfer and separation, and is suitable for the air-liquid-solid three-phase reaction taking solid grains as catalysts.

Description

technical field [0001] The invention belongs to the field of gas-liquid-solid three-phase reaction, especially a gas-liquid-solid reaction system in which the catalyst is a solid particle and the gas-liquid two-phase respectively participates in mass transfer and reaction, and the gas-liquid-solid three-phase separation is required. The three-phase reaction is an internal loop reactor with reaction and separation functions, which can be widely used in chemical reaction processes involving solid catalysts above the micron level. Background technique [0002] The inner loop reactor is a new type of reactor developed on the basis of the bubble column. It has a simple structure, no power device inside, good mass and heat transfer effects, and can perform gas-liquid, gas-solid and gas-liquid-solid reaction, so it is widely used in fermentation, energy, sewage treatment and other aspects. [0003] In the gas-liquid-solid three-phase reaction where the catalyst is solid particles,...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J8/22
CPCB01J8/0055B01J8/226B01J2208/00761B01J19/006B01J2208/00911B01J2219/00774B01J2219/00768B01J8/007B01J2208/00991
Inventor 黄青山羊涛蒋夫花杨超
Owner QINGDAO INST OF BIOENERGY & BIOPROCESS TECH CHINESE ACADEMY OF SCI
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