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Ebullated bed hydrogenation reactor and method of use

A technology of hydrogenation reactor and ebullating bed, which is applied in the direction of chemical instruments and methods, chemical/physical processes, etc., can solve the problems of low separation accuracy and efficiency, insufficient driving force for cyclone separation enhancement, and large operating flexibility, etc., to achieve Enhance separation accuracy and effect, high utilization rate of reaction space, and enhance the effect of cyclone driving force

Active Publication Date: 2022-07-15
EAST CHINA UNIV OF SCI & TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The three-phase cyclone separator includes the sleeve structure of the inner cylinder and the outer cylinder, both of which are open structures. The upper part of the inner cylinder and the outer cylinder is an inverted truncated cone structure, and the lower part is an upright truncated cone structure. The operation is flexible. The structure is simple and the catalyst storage capacity is large, but it cannot realize the fully mixed flow operating conditions
The three-phase cyclone separator has a simple structure and only has an inner cylinder and an outer cylinder, which can meet the separation of gas-liquid-solid three-phase in a small-scale and low-flow state, and has a certain effect, but it is difficult to meet large-scale and efficient separation. Enhanced Cyclone Separation
Chinese utility model patent CN207929188U is a supplement and extension of CN 108148621A. Similarly, the existing problem is that the enhanced driving force of cyclone separation is insufficient, and the separation accuracy and efficiency are not high
According to the true density of catalyst particles is 1500kg / m 3 Calculated, the specific surface area of ​​the catalyst with a particle size of 0.2mm is 0.02m 2 / g, which cannot meet the requirements for the use of small-diameter catalyst particles

Method used

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  • Ebullated bed hydrogenation reactor and method of use
  • Ebullated bed hydrogenation reactor and method of use
  • Ebullated bed hydrogenation reactor and method of use

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0077] The ebullated bed hydrogenation reactor was used for 3000L / h ebullated bed hydrogenation reactor cold model experiment.

[0078] 1. Process flow

[0079] like image 3 shown.

[0080] 2. The main structural dimensions of the fluidized bed hydrogenation separator

[0081] The main structural dimensions of the fluidized bed hydrogenation reactor are shown in Table 1 below, and the dimensions and structure of the two-stage fluidized bed hydrogenation separator are exactly the same.

[0082] Table 1: 3000L / h fluidized bed hydrogenation reactor cold mold device structure size

[0083]

[0084] 3. Implementation effect

[0085] The test process of the 3000L / h fluidized bed hydrogenation cold mold device was tested with water and air. The test results are shown in Table 2 below. From the test results, the catalyst achieves uniform fluidization, runs continuously for 30 hours without failure, and the take-out amount of 0.1mm catalyst is controlled to be less than 2μg / g....

Embodiment 2

[0089] The ebullated bed hydrogenation reactor was used in a 20000L / h straw pyrolysis liquid hydrodeoxygenation unit.

[0090] 1. Process flow

[0091] like Figure 4 shown.

[0092] 2. Main structural dimensions of the fluidized bed hydrogenation reactor

[0093] The main structural dimensions of the fluidized bed hydrogenation reactor are shown in Table 3 below, and the dimensions and structure of the two-stage fluidized bed hydrogenation separator are exactly the same.

[0094] Table 3: Structure size of ebullated bed reactor of 20000L / h sewage straw hydrolysis hydrodeoxygenation unit

[0095]

[0096] 3. Implementation effect

[0097] The test process of the 20000L / h polluted straw hydrolysis solution hydrodeoxygenation unit was tested with straw pyrolysis solution, and the test results are shown in Table 4 below. From the test results, the catalyst achieved uniform fluidization, no coking occurred in the reactor for 2000 hours of continuous operation, and the take...

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PUM

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Abstract

The present disclosure relates to a fluidized bed hydrogenation reactor and a method of using the same, and provides a fluidized bed hydrogenation reactor, comprising: a pressure-bearing shell (3), a gas-liquid-solid three-phase gas disposed in the upper space of the pressure-bearing outer shell a cyclone separator, a non-return cone (12) arranged at the bottom of the gas-liquid-solid three-phase cyclone separator, a descending liquid-phase product outlet pipe (14) arranged in the middle of the pressure-bearing shell, and The gas phase outlet (7), the liquid phase outlet (15) and the gas-liquid mixed phase inlet (1) are arranged on the pressure-bearing shell. Also provided is a method for using the above ebullated bed hydrogenation reactor.

Description

technical field [0001] The present disclosure belongs to transformative clean energy key equipment technology, in particular to a fluidized bed hydrogenation reactor and a method for using the same. Background technique [0002] Ebullated bed reactor is a gas-liquid-solid three-phase fluidized bed reactor, which is widely used in hydrogenation process because of its pressure drop, not easy to block, and long-term operation. Due to its unique structure and operation mode, the ebullated bed reactor has the following advantages: ① The operation is flexible and can be operated at high or low conversion rate; ② The catalyst can be recovered or added from the reactor periodically, and the 30% to 50% expansion of the catalyst bed through the circulating pump to ensure that there is enough free space between the solid particles of the catalyst; it can avoid the solid particles entrained by the raw materials or generated during the reaction process. During the process of crossing th...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J8/26B01J8/00
CPCB01J8/26B01J8/0055
Inventor 李剑平李诗豪杨雪晶江霞李立权陈崇刚赵颖袁远平汪华林
Owner EAST CHINA UNIV OF SCI & TECH
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