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Fluidized bed reactor

A fluidized bed reactor and reactor technology, applied in chemical instruments and methods, chemical/physical processes, etc., can solve the problems of low space utilization rate and complex internal structure of the reactor, and improve the operation flexibility and stability. The effect of prolonging the residence time and increasing the effective volume

Active Publication Date: 2014-05-07
CHNA ENERGY INVESTMENT CORP LTD +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0005] Aiming at the problems existing in the prior art, the present invention provides an ebullating bed reactor to solve the problems of the existing ebullating bed reactor with complex internal structure and low space utilization in the reactor

Method used

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  • Fluidized bed reactor

Examples

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Embodiment

[0036] Coal liquefied oil hydrogenation test is carried out by using the fluidized bed reactor of the present invention. The reactor shell is 35m high, including the middle straight section and the upper and lower elliptical heads. The straight section is 31m high and 4.5m in diameter; 0.1m, the inlet end of the catalyst unloading pipeline is 20m away from the distributor; the structure of the hot high-pressure separator is as follows figure 1 As shown, the diameter (height) is 5m, the first and second baffles are 3m high, the middle part is 5m wide, and the first and second parts are 2m wide.

[0037] The hydrogenation catalyst used in the test is a hydrogenation catalyst with alumina as the carrier, and its manufacturer is Beijing Sanju Environmental Protection New Materials Co., Ltd., and the brand is FFT-1B. Above the distributor in the reactor shell is the effective volume of the reactor, and the filling volume of the catalyst in the reactor is 60% of the effective volum...

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Abstract

The invention discloses a fluidized bed reactor. The fluidized bed reactor comprises a reactor shell and a circulating unit, wherein the circulating unit is arranged outside the reactor shell; a material outlet which is connected to the circulating unit is formed in the top of the reactor shell; a material inlet which is communicated with the circulating unit is formed in the bottom of the reactor shell; the circulating unit comprises a separator and a circulating pump; the separator is used for separating reaction materials from the top of the reactor shell into gas-phase materials and liquid-phase materials; the circulating pump is used for feeding part of the liquid-phase materials separated by the separator into the reactor shell. The effective volume of the fluidized bed reactor is increased, and the flexibility and stability of operation are improved; meanwhile, by the arrangement of a separation device in the circulating unit, the content of solid particles in the fed materials of the circulating pump is decreased, and abrasion of the circulating pump is reduced, so that the service life of the circulating pump is prolonged.

Description

technical field [0001] The invention relates to an ebullating bed reactor, in particular to an ebullating bed reactor capable of circulating materials outside the body. Background technique [0002] The ebullating bed reactor is a reactor that uses gas or liquid to pass through the granular solid catalyst bed to keep the catalyst in a suspended state, and to perform a three-phase reaction of gas, liquid and solid. The ebullated bed reactor can process heavy and low-quality feed oil with high metal and high asphaltene content, and has the advantages of large space velocity, small bed pressure drop, uniform temperature distribution, good mass and heat transfer effects, and flexible device operation. In addition, fresh catalyst can be added online and deactivated catalyst can be unloaded during operation, so that the activity of the catalyst can be maintained at a high level throughout the operation cycle, and the operation cycle is longer. [0003] US Re25770 describes a typi...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J8/24
Inventor 舒歌平吴秀章张继明张传江陈茂山刘东明段晓军安亮杨东刘建平刘永贾振斌
Owner CHNA ENERGY INVESTMENT CORP LTD
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