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Slurry bed loop reactor and application thereof

A loop reactor, slurry bed technology, applied in chemical instruments and methods, preparation of liquid hydrocarbon mixtures, petroleum industry, etc., can solve the problems of complex equipment structure, unsuitable for large-scale continuous production, and wear of solid catalyst particles.

Active Publication Date: 2014-12-31
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

This takes up a lot of reactor space, and the solid-liquid separation unit affects the energy and mass transfer of the reaction in the main area of ​​the reactor, and the effect is not good
[0008] WO94 / 16807 discloses a method of using a filter assembly in a reactor to achieve liquid-solid separation, but once the catalyst particles block the filter assembly, the regeneration of the filter assembly is difficult, so it is not suitable for large-scale continuous production
[0009] CN1589957A discloses that a primary separation unit is set inside the reactor, a secondary separation unit is set outside the reactor to realize liquid-solid separation, and a recoil unit is set outside the reactor to realize the continuous operation of filtration. This method not only occupies The reaction space in the reactor is reduced, and the equipment structure is complicated and the operation is complicated.
This liquid-solid separation method requires the help of external power, and does not provide a detailed backwashing method, making it difficult to achieve continuous and effective separation of liquid and solid
[0012] From the above analysis, it can be seen that it is difficult to achieve continuous operation by means of filtration. Even if continuous operation is realized, it will cause serious wear of solid catalyst particles, and it will also make the equipment complicated, and the investment and operating costs will increase.

Method used

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  • Slurry bed loop reactor and application thereof
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  • Slurry bed loop reactor and application thereof

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0051] Example 1 illustrates the effect of the slurry bed loop reactor and its application method provided by the present invention.

[0052] The diameter ratio of the air bubble removal zone and the downcomer separation zone of the slurry bed loop reactor is 1.5:1. The filter component used in the downcomer is a sintered porous metal filter tube, and the slurry inlet of the filter component has an inverted cone structure. The cone angle is 45°, the filter tube has an outer diameter of 50 mm, a length of 1000 mm, and an average pore diameter of 1 μm. The particle size range of the catalyst used is 1-100 μm. During this process, the synthesis gas enters the bed layer in the form of bubbling from the bottom of the riser through the double-loop gas distributor, and generates liquid hydrocarbons under operating conditions. When the slurry rises and enters the bubble removal zone 13 on the upper part of the downcomer, the unreacted synthesis gas and gas products are completely sepa...

Embodiment 2

[0056] Example 2 illustrates the effect of the slurry bed loop reactor provided by the present invention on Fischer-Tropsch synthesis with a cobalt-based catalyst.

[0057] with H 2 / CO molar ratio is the syngas of 2 as raw material, and Fischer-Tropsch synthesis produces liquid hydrocarbons. The slurry bed loop reactor and other equipment and experimental steps adopted in Example 2 are the same as in Example 1, except that cobalt-based Catalyst (commercial brand is RFT-410), wherein the mass fraction of cobalt is 20-30wt%, and the pore volume is 0.2-0.45m 3 / g, specific surface area 80-180m 2 / g, the bulk density is 1.2-1.4g / cm 3 , particle size range 40-70μm.

[0058] The operating conditions of the slurry bed reaction zone are as follows: the reaction temperature is 220° C., the absolute pressure is 3.0 MPa, the space velocity is 1.0 NL / g-cat / h, and the catalyst loading is 16% (volume percentage). Under these operating conditions, the one-way conversion rate of CO in the ...

Embodiment 3

[0060] Example 3 illustrates the effect of the slurry bed loop reactor provided by the present invention on the Fischer-Tropsch synthesis of iron-based catalysts.

[0061] with H 2 Syngas with a / CO molar ratio of 0.67 is the raw material for Fischer-Tropsch synthesis to produce liquid hydrocarbons. The slurry bed loop reactor and other equipment and experimental steps used in Example 3 are the same as in Example 1, except that the quenching framework is used. Iron (RQFe-Mn-K) catalyst, the mass fraction of iron is 80wt%, specific surface area is 47m 2 / g, the pore volume is 0.13m 3 / g, the bulk density is 1.05g / cm 3 , particle size range (35-50) μm.

[0062] The operating conditions of the slurry bed reaction zone are as follows: the reaction temperature is 280° C., the pressure is 2.1 MPa, the space velocity is 2.1 NL / g-cat / h, and the catalyst loading is 10% (volume percentage). Under these operating conditions, the one-way conversion rate of CO in the synthesis gas reac...

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Abstract

The invention discloses a slurry bed loop reactor and application thereof. The slurry bed loop reactor comprises an ascending pipe (11) and at least one descending pipe (12) arranged inside the ascending pipe (11), wherein at least one filtering assembly (1) is arranged in the descending pipe (12); the upper part of the descending pipe (12) is provided an air bubble removing region (13) of which the pipe diameter is expanded; the two ends of the descending pipe (12) is communicated with the internal space of the ascending pipe (11) through the air bubble removing region (13) and a gap between the descending pipe and a bottom baffle plate (16) thereof; the internal space of each descending pipe is partitioned into a slurry region (2) and a filtrate region (3) through a filter medium; the slurry region (2) is connected with the two ends of the descending pipe (12); and the filtrate region (3) is communicated with a filtrate discharging hole (18). The slurry bed loop reactor provided by the invention can be further provided with a back flushing system which can be used for performing back flushing regeneration on a filter pipe under the condition of not influencing a reaction process. The reactor can be used for realizing continuous separation of gas, liquid and solid phases in a slurry bed reaction system, has a simple structure and high separation efficiency, and is easy, convenient and flexible for operating.

Description

technical field [0001] The invention relates to a gas-liquid-solid three-phase slurry bed reactor and equipment and methods for separating solid particles from liquid products, more specifically, to a slurry bed reactor capable of continuously separating liquid products from solid particles Bed loop reactor and method of application thereof. Background technique [0002] The slurry bed reactor is a commonly used gas-liquid (slurry) contact reaction equipment with a very high liquid storage capacity. For the catalytic reaction process with large reaction heat, the use of slurry bed reactor can effectively remove the reaction heat, realize the isothermal operation of the reactor, and ensure the normal operation of the reactor, so it has been widely used in today's chemical process. The slurry bed loop reactor is a high-efficiency heterogeneous reactor developed on the basis of the slurry bed bubbling reactor. In addition to all the advantages of the slurry bed bubbling react...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J8/22C10G2/00
Inventor 胡立峰李大东唐晓津张占柱
Owner CHINA PETROLEUM & CHEM CORP