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Continuous reactor suitable for high-viscosity and high-solid-content reactant system and application

A high solid content, reactor technology, applied in chemical instruments and methods, chemical/physical processes, etc., can solve problems such as inability to apply multi-stage loop reactors, easy short-circuiting of materials and solid particles, affecting the environment and worker safety, etc. To achieve the effect of increasing the interphase contact area and transfer coefficient, improving the reaction conversion rate and reaction rate, and being easy to scale up in industry

Pending Publication Date: 2021-07-23
TIANJIN UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0006] Both patents CN1171667C and CN105400544A have proposed a multi-stage loop reactor, the introduction of multi-stage form is beneficial to the high-level amplification, but there is still a serious defect in the design of the reactor internals, that is, because the inner sleeve is always The gas rising zone causes the material in the inner sleeve and the inner wall of the reactor, especially the solid particle material, to be easily short-circuited and has no ability to recover. Therefore, the multi-stage loop reactor cannot be applied to high-viscosity and high-solid-content reaction systems.
[0007] It can be seen from the above that at present, the industrial reactors for processing high-viscosity and high-solid-content reaction systems are still intermittent stirring tanks. During the intermittent reaction process, the reactors need to be opened frequently manually, resulting in the volatilization of toxic gases generated by side reactions in the production process into the atmosphere. , affecting the environment and worker safety, the parameters of the batch reaction process are subject to human factors and are difficult to control, resulting in unstable or even unqualified product indicators

Method used

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  • Continuous reactor suitable for high-viscosity and high-solid-content reactant system and application
  • Continuous reactor suitable for high-viscosity and high-solid-content reactant system and application
  • Continuous reactor suitable for high-viscosity and high-solid-content reactant system and application

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0043] Example 1 is the application of a continuous primary reactor with high viscosity and high solid content reaction system in the synthesis of 2-amino-8-naphthol-6-sulfonic acid.

[0044] Such as figure 1 , image 3 with Figure 4 Shown:

[0045] The reactor includes a shell 1, a shrinking diversion cone 2, an inner sleeve 3, a divergent diversion cone 4, a structured packing 5, a gas distributor 6, and a hydrocyclone 7; the internal parts of the reactor are from bottom to top: Gas distributor 6, shrinking diversion cone 2, inner sleeve 3 and structured packing 5, divergent diversion cone 4, hydrocyclone 6; the reactor is provided with gas inlet 8, upper feed inlet 11, upper outlet A feed port 12, a lower feed port 11, a lower discharge port 12 and a gas discharge port 13. The lower diversion cone of the inner sleeve 3 is a shrinking diversion cone 2, the inside of the inner sleeve 3 is an ascending area, and the outside of the inner sleeve 3 is a descending area; the ...

Embodiment 2

[0049] Example 2 is the application of a continuous secondary reactor with high viscosity and high solid content reaction system in the synthesis of methyl isocyanate.

[0050] Such as figure 2 , image 3 with Figure 4 Shown:

[0051] The reactor includes a shell 1, a shrinking diversion cone 2, an inner sleeve 3, a divergent diversion cone 4, a structured packing 5, a gas distributor 6, and a hydrocyclone 7; the internal parts of the reactor are from bottom to top: Gas distributor 6, shrinking diversion cone 2, inner sleeve 3 and structured packing 5, divergent diversion cone 4, hydrocyclone 6; the reactor is provided with gas inlet 8, upper feed inlet 11, upper outlet A feed port 12, a lower feed port 11, a lower discharge port 12 and a gas discharge port 13. The lower guide cone of the two inner sleeves 3 is a contraction guide cone 2, the inside of the inner sleeve 3 is an ascending area, and the outside of the inner sleeve 3 is a descending area. The lower guide co...

Embodiment 3

[0056] Example 3 is the application of a continuous three-stage three-column reactor with high viscosity and high solid content reactant system in the synthesis of 2,4-dichlorophenoxyacetic acid from sodium 2,4-dichlorophenate and sodium chloroacetate.

[0057] Such as Image 6 Shown:

[0058] M-level N-column reactor M≤50, N≤50, the cross-sectional area between the inner sleeves 3 in the horizontal direction is equal to the cross-sectional area of ​​the inner sleeves 3 . The shell 1 of the M-level N-column reactor is rectangular or circular, and the rectangular shell is preferred when the operating pressure is normal pressure, and the circular shell is preferred when the operating pressure is negative pressure or positive pressure; the inner sleeve 3 is a truss , the diversion cones are all divergent diversion cones 4, the diversion cones in contact with the housing are prism divergent diversion cones 4, and the diversion cones that are not in contact with the housing are bi...

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PUM

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Abstract

The invention relates to a continuous reactor suitable for a high-viscosity and high-solid-content reactant system and application of the continuous reactor. The continuous reactor comprises a shell, a flow guide cone, an inner sleeve, structured packing, a gas distributor and a cyclone hydraulic separator; a gas distributor is arranged at the bottom in the reactor, a diversion cone and an inner sleeve are arranged in the middle, and reaction internals such as a cyclone hydraulic separator are arranged at the top of the reactor; the flow guide cone is divided into a contraction type flow guide cone and a diverging type flow guide cone, the contraction type flow guide cone enables the fluid to contract inwards, and the diverging type flow guide cone enables the fluid to diverge outwards; structured packing is arranged in part of the inner sleeve and in an area surrounded by part of the inner sleeve and the shell; N M-stage reaction stages are horizontally arranged in parallel in the reactor to obtain M-stage N-column reactors, wherein M is less than or equal to 50, and N is less than or equal to 50. According to the invention, solid and liquid materials are better mixed by utilizing a multi-stage strong circulation field, and the reaction process is enhanced, so that the reaction conversion rate and the reaction rate are improved.

Description

technical field [0001] The invention belongs to the field of chemical engineering reaction engineering, in particular to a continuous reactor suitable for high-viscosity and high-solid content reaction system and its application. Background technique [0002] In a chemical reaction, the reaction process in which there are two different phase states of liquid and solid at the same time is called liquid-solid reaction. When the viscosity of the reactant or product is greater than 100cp and the solid content is greater than 5%, the viscosity increases and the solid particles Increasing the probability of hindering the contact of the reactants reduces the diffusion, heat transfer and mass transfer between the reactants, thus requiring more time and energy consumption to obtain a higher reaction conversion rate. This type of reaction is commonly found in petrochemical, Coal chemical industry, medicine, pesticide, synthetic resin and other fields. [0003] In industry, most of th...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J8/18B01J8/00
CPCB01J8/008B01J8/1818B01J8/1845
Inventor 刘辉刘春江谢省宾张庆宇付娜朱冠宇魏东旭韦昌鹏
Owner TIANJIN UNIV
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