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Gas-solid fluidized-bed catalyst mixing apparatus

A fluidized bed catalyst and mixing device technology, applied in gas/vapor and solid mixing, fluid mixer, mixer, etc., can solve the problem of increased equipment size, difficulty in uniform mixing of two or three catalysts, and catalyst reaction yield. The size of the rate, the influence of the energy consumption of the reaction device, etc.

Pending Publication Date: 2018-09-28
CHINA UNIV OF PETROLEUM (BEIJING)
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

[0004] However, the mixing effect of the catalyst has a significant impact on the size of the reaction yield, the selectivity of the product and the energy consumption of the reaction device.
With the gradual increase in the processing capacity of chemical plants in recent years, the equipment size has also increased accordingly. It is very difficult to directly mix two or three catalysts evenly in large equipment with a diameter of several meters or even tens of meters.

Method used

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  • Gas-solid fluidized-bed catalyst mixing apparatus
  • Gas-solid fluidized-bed catalyst mixing apparatus
  • Gas-solid fluidized-bed catalyst mixing apparatus

Examples

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Effect test

Embodiment 1

[0073] figure 1 It is a schematic structural diagram of a gas-solid fluidized bed catalyst mixing device provided in Example 1 of the present invention. Such as figure 1 As shown, the gas-solid fluidized bed catalyst mixing device provided in this embodiment includes: a fluidized bed reactor 10, a mixing chamber 20, a gas distributor 70 and at least two catalyst pipelines 30;

[0074] The gas distributor 70 and all catalyst pipelines 30 are connected to the mixing chamber 20 for mixing the catalyst in the catalyst pipeline 30 in the mixing chamber 20;

[0075] The mixing chamber 20 is connected to the fluidized bed reactor 10 for mixing the catalyst mixed in the mixing chamber 20 with the catalyst in the fluidized bed reactor 10 .

[0076] Optionally, the catalyst pipeline 30 has a valve that can be opened and closed.

[0077] In the gas-solid fluidized bed catalyst mixing device provided in this embodiment, at least two catalysts with different physical properties or tempe...

Embodiment 2

[0105] Figure 10 A schematic structural diagram of a gas-solid fluidized bed catalyst mixing device provided in Embodiment 2 of the present invention; Figure 11 Schematic diagram of the structure of the first mixing chamber and catalyst pipeline in the gas-solid fluidized bed catalyst mixing device provided in Embodiment 2 of the present invention; Figure 12 A schematic structural diagram of the second mixing chamber and catalyst pipeline in the gas-solid fluidized bed catalyst mixing device provided in Example 2 of the present invention; Figure 13 A schematic structural diagram of the third mixing chamber and catalyst pipeline in the gas-solid fluidized bed catalyst mixing device provided in Example 2 of the present invention; Figure 14 It is a schematic structural diagram of the fourth type of mixing chamber and catalyst pipeline in the gas-solid fluidized bed catalyst mixing device provided in Example 2 of the present invention. Such as Figure 10-Figure 14 As shown...

Embodiment 3

[0109] The gas-solid fluidized bed catalyst mixing device provided in the first and second embodiments above is suitable for installing the mixing chamber 20 at the bottom of the fluidized bed reactor 10 . However, when the space at the bottom of the fluidized bed reactor 10 cannot accommodate the mixing chamber 20 , the mixing chamber 20 can be installed on the side of the fluidized bed reactor 10 . Figure 15 A schematic structural diagram of a gas-solid fluidized bed catalyst mixing device provided in Example 3 of the present invention. Such as Figure 15 As shown, the gas-solid fluidized bed catalyst mixing device provided in this embodiment also includes a riser pipe 40, a delivery pipe 50 and a second center pipe 60 connected in sequence, the riser pipe 40 communicates with the mixing chamber 20, and the second center pipe 60 Part of it extends into the fluidized bed reactor 10.

[0110] Optionally, the end of the second central pipe 60 protruding into the fluidized be...

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PUM

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Abstract

The invention provides a gas-solid fluidized-bed catalyst mixing apparatus, comprising a fluidized-bed reactor, a mixing chamber, a gas distributor and at least two catalyst ducts; the gas distributorand all the catalyst ducts are communicated with the mixing chamber for mixing catalyst in the catalyst ducts in the mixing chamber; the mixing chamber is communicated with the fluidized-bed reactorfor mixing the catalysts, mixed in the mixing chamber, with a catalyst in the fluidized-bed reactor. The gas-solid fluidized-bed catalyst mixing apparatus has the advantages that at least two catalysts are fed into the mixing chamber through the different catalyst ducts, the catalysts are mixed first in the mixing chamber, the premixed catalysts in the mixing chamber are mixed with the catalyst inthe fluidized-bed reactor. Mixing catalysts in the fluidized-bed reactor is facilitated such that the catalysts in the fluidized-bed reactor can be mixed well.

Description

technical field [0001] The invention relates to the technical field of chemical industry, in particular to a gas-solid fluidized bed catalyst mixing device. Background technique [0002] In petrochemical, pharmaceutical and chemical industries, solid particles often need to react with gases to produce different products. Usually, a fluidized bed reactor is used as the main reaction site. Among them, the fluidized bed reactor is a reactor that uses gas or liquid to pass through the granular solid layer to make the solid particles in a state of suspension and motion, and to perform a gas-solid phase reaction process or a liquid-solid phase reaction process. [0003] For some processes, it is necessary to uniformly mix different catalysts (gas), or to mix catalysts with different temperatures or activities, and then react with the gas phase, such as catalytic cracking MIP process technology (MIP: maximizing iso-paraffins), which requires Mix catalysts with different temperatu...

Claims

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Application Information

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IPC IPC(8): B01J8/24B01F5/00B01F3/06B01F23/30
CPCB01J8/1872B01J8/24B01F23/36B01F23/30B01F25/00
Inventor 刘梦溪卢春喜周帅帅
Owner CHINA UNIV OF PETROLEUM (BEIJING)
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