Micro-power reaction system

Abstract

Belonging to the technical field of chemical equipment, the utility model relates to a micro-power reaction system, which comprises: a precision filtration unit for filtering reactants; the micro-power overspeed reaction unit is connected with the precise filtering unit, the micro-power overspeed reaction unit comprises at least two groups of accelerators, the two groups of accelerators are sequentially arranged in the direction from the top to the bottom of the micro-power overspeed reaction unit, and the speeds increased by the two groups of accelerators are sequentially increased; the gas-liquid separator is connected with a gas outlet of the micro-power overspeed reaction unit; the top of the heat dissipation assembly is connected with the inlet of the micro-power overspeed reaction unit, and the bottom of the heat dissipation assembly is connected with the outlet of the micro-power overspeed reaction unit. According to the utility model, the accuracy and the purity of reactants are improved, the dispersity of the reactants needing to be dispersed can be improved, and the reaction efficiency is improved; and reactants which are generated by reaction and need to be cooled are cooled through the cooling assembly, so that the reaction efficiency of the micro-power overspeed reaction unit is improved.

Description

TECHNICAL FIELD

[0001] The present application relates to the technical field of mechanical equipment, in particular to a micro power reaction system. BACKGROUND

[0002] The reaction system is a common reaction unit in the chemical industry. Compounds undergo chemical reactions through heating, stirring, dispersion, and other operations in the reaction system. It is an indispensable reaction unit in the chemical industry.

[0003] The reaction system provided by the related art includes a stirring tank, a reaction tank, and a metering tower connected in sequence. The stirring tank is used for stirring and dispersion processing. The reaction product of the dispersion processing enters the reaction tank for reaction and then enters the metering tower for metering.

[0004] However, the reaction system provided by the related art cannot achieve high dispersion of compounds for the production and preparation of special reaction substances. The cooperation between the structures of the system is incomplete, which leads to low precision and insufficient purity of the reaction product.

[0005] Therefore, the existing reaction system has the above-mentioned disadvantages in the method, manufacturing method, processing method, and use. Related manufacturers have made great efforts to solve these problems, but no suitable design has been developed for a long time. The general method, manufacturing method, processing method, and micro power reaction system do not have appropriate methods, manufacturing methods, processing methods, and structures to solve the above-mentioned problems. This is obviously a problem that related industries urgently want to solve.

[0006] In view of the defects of the existing micro power reaction system, the present application is based on the rich practical experience and professional knowledge accumulated from years of designing and manufacturing such products, combined with the application of theories, and actively researched and innovated to create a new micro power reaction system that can improve the general existing micro power reaction system and make it more practical. After continuous research, design, and repeated trial and improvement, the present application with practical value is finally created. SUMMARY

[0007] The main purpose of the present application is to overcome the defects of the existing micro power reaction system and provide a new micro power reaction system. The technical problem to be solved is to achieve high dispersion of compounds for the production and preparation of special reaction substances and to improve the precision and purity of the reaction product.

[0008] The present application has obvious advantages and beneficial effects compared with the prior art. As shown by the above technical solution, in order to achieve the aforementioned application purposes, the main technical content of the present application is as follows:

[0009] The application provides a micro-power reaction system, comprising:

[0010] a precision filtration unit for filtering the reactants;

[0011] a micro-power superspeed reaction unit connected with the precision filtration unit, the micro-power superspeed reaction unit comprising at least two groups of accelerators, wherein the two groups of accelerators are arranged in sequence from top to bottom of the micro-power superspeed reaction unit, and the speeds increased by the two groups of accelerators are sequentially increased;

[0012] a gas-liquid separator connected with a gas outlet of the micro-power superspeed reaction unit;

[0013] at least one group of heat dissipation assemblies, the top of the heat dissipation assemblies being connected with an inlet of the micro-power superspeed reaction unit, and the bottom of the heat dissipation assemblies being connected with an outlet of the micro-power superspeed reaction unit.

[0014] In an alternative embodiment, the micro-power superspeed reaction unit further comprises a cooling unit for cooling the micro-power superspeed reaction unit.

[0015] In an alternative embodiment, the micro-power superspeed reaction unit further comprises a radar monitor for monitoring the feeding size of the reactants.

[0016] In an alternative embodiment, the precision filtration unit comprises a plurality of feeding ports, and a feeding valve is arranged on each of the feeding ports.

[0017] In an alternative embodiment, the bottom of the gas-liquid separator is connected with the top of the micro-power superspeed reaction unit through a pipeline, and a control valve is arranged on the pipeline.

[0018] In an alternative embodiment, the heat dissipation assemblies comprise a first heat sink and a second heat sink arranged side by side, and the top of the first heat sink and the second heat sink is connected with the top of the micro-power superspeed reaction unit, and the bottom of the first heat sink and the second heat sink is connected with the bottom of the micro-power superspeed reaction unit.

[0019] In an alternative embodiment, the heat dissipation assemblies further comprise a first power pump and a second power pump, the first power pump is arranged between the first heat sink and the bottom of the micro-power superspeed reaction unit, and the second power pump is arranged between the first heat sink and the bottom of the micro-power superspeed reaction unit.

[0020] In an alternative embodiment, the first heat sink and the second heat sink are made of different materials, and the heat dissipation power of the first heat sink is greater than that of the second heat sink.

[0021] In an alternative embodiment, a first feeding pipeline and a second feeding pipeline are further included, the first feeding pipeline is arranged between the first power pump and the bottom of the micro-power superspeed reaction unit, and the second feeding pipeline is arranged between the second power pump and the bottom of the micro-power superspeed reaction unit.

[0022] In an alternative embodiment, the first power pump and the second power pump are magnetic reaction pumps.

[0023] By means of the technical scheme, the micro-power reaction system has at least the following advantages:

[0024] The micro-power reaction system provided in the embodiment of the utility model, through the multiple filtration of the reactant by the precision filtration unit, the precision and purity of the reactant are improved, the reactant is accelerated by at least two groups of accelerators in the micro-power superspeed reaction unit, the reactant is fully contacted in the micro-power superspeed reaction unit, the dispersion of the reactant can be improved, and the contact area between the reactants is improved, and the reaction efficiency is improved; the reactant which generates heat and needs to dissipate heat is dissipated by the heat dissipation assembly, and the reaction efficiency of the micro-power superspeed reaction unit is improved.

[0025] In summary, the special micro-power reaction system can realize high dispersion of compounds, improve the precision and purity of reaction products, and has the above-mentioned advantages and practical value.

[0026] The above description is only a summary of the technical scheme of the application, in order to more clearly understand the technical means of the application, and the content of the specification can be implemented, the following preferred embodiments of the application are described in detail with reference to the accompanying drawings.

[0027] The specific micro-power reaction system of the application is described in detail in the following embodiments and drawings. BRIEF DESCRIPTION OF DRAWINGS

[0028] Figure 1 It is a structural schematic view of the micro-power reaction system.

[0029] Reference signs:

[0030] 1-precision filtration unit, 2-micro power superspeed reaction unit, 21-accelerator, 3-gas-liquid separator, 4-heat dissipation assembly, 41-first heat sink, 42-second heat sink, 43-first power pump, 44-second power pump. DETAILED DESCRIPTION

[0031] In order to further clarify the technical means and effects adopted by the present application to achieve the predetermined object of the application, and the specific implementation steps, structure, characteristics and effects of the micro power reaction system according to the present application, detailed description is given as follows in combination with the drawings and preferred embodiments.

[0032] Referring to Figure 1 The micro power reaction system of the preferred embodiment of the present application comprises: a precision filtration unit 1, a micro power superspeed reaction unit 2, a gas-liquid separator 3, and at least one heat dissipation assembly 4.

[0033] The precision filtration unit 1 is used for filtering the reactants; the micro power superspeed reaction unit 2 is connected with the precision filtration unit 1, the micro power superspeed reaction unit 2 comprises at least two groups of accelerators 21, wherein the two groups of accelerators 21 are arranged in sequence along the top-to-bottom direction of the micro power superspeed reaction unit 2, and the speed increased by the two groups of accelerators 21 increases in sequence; the gas-liquid separator 3 is connected with the gas outlet of the micro power superspeed reaction unit 2; the top of the at least one heat dissipation assembly 4 is connected with the inlet of the micro power superspeed reaction unit 2, and the bottom is connected with the outlet of the micro power superspeed reaction unit 2.

[0034] The micro power reaction system provided by the embodiment of the present application filters the reactants multiple times through the precision filtration unit 1, improves the precision and purity of the reactants, accelerates the reactants through the at least two groups of accelerators 21 in the micro power superspeed reaction unit 2, makes the reactants fully contact in the micro power superspeed reaction unit 2, can improve the dispersity of the reactants which need to be dispersed, and further improves the contact area between the reactants, thereby improving the reaction efficiency; the reactants which need to dissipate heat generated by the reaction dissipate heat through the heat dissipation assembly 4, and the reaction efficiency of the micro power superspeed reaction unit 2 is improved.

[0035] In an alternative embodiment, the precision filtration unit 1 can be a filter tower, a plurality of inlets are provided on the filter tower, wherein the inlets can include gas inlets and liquid inlets, a blowdown port is provided at the bottom of the filter tower for discharging the impurities filtered multiple times, and the filter layer in the filter tower can be set according to the type of the filtered reactants, for example, when the filtered reactants are gas, adsorbing gas can be provided in the filter tower to adsorb impurities in the reactants, etc. When the filtered reactants are liquid, adsorbing liquid or filtering liquid, etc. can be provided in the filter tower to filter impurities in the liquid, and the specific adsorbent or filtering liquid can be set as required, which is not limited in the embodiment of the present application.

[0036] It should be noted that the precise filtering unit 1 provided by the embodiments of the present application can simultaneously realize filtering of gas and liquid, and further, a gas filtering portion can be arranged at the top of the filtering tower, and a liquid filtering portion can be arranged at the bottom of the filtering tower, the gas enters the gas filtering portion at the top for filtering, and the liquid enters for liquid filtering through the bottom of the filtering tower. In this way, the filtering efficiency of the reactants can be improved.

[0037] In an alternative embodiment, the micro-power superspeed reaction unit 2 further comprises a cooling unit for cooling inside the micro-power superspeed reaction unit 2.

[0038] The cooling unit of the present application can be a cooler wound with modified graphite.

[0039] In an alternative embodiment, the micro-power superspeed reaction unit 2 further comprises a radar monitor for monitoring the size of the reactant feed. By providing a radar detector, the size of the liquid or gaseous reactant feed can be detected, and the feed can be terminated in time when the feed is greater than the preset feed amount, so as to avoid excessive reactants and affect the reaction.

[0040] In an alternative embodiment, the precise filtering unit 1 comprises a plurality of feed ports, and a feed valve is arranged on each of the plurality of feed ports. The feed ports include gas feed and liquid feed, and further, the gas feed port can be arranged above the liquid feed port. The size and time of the feed are controlled by the valve.

[0041] In an alternative embodiment, the bottom of the gas-liquid separator 3 is connected to the top of the micro-power superspeed reaction unit 2 through a pipeline, and a control valve is arranged on the pipeline.

[0042] By providing the gas-liquid separator 3, the separation of the gas and liquid generated in the micro-power superspeed reaction unit 2 can be realized.

[0043] In an alternative embodiment, the heat dissipation assembly 4 comprises a first heat sink 41 and a second heat sink 42 arranged side by side, the top of the first heat sink 41 and the second heat sink 42 is connected to the top of the micro-power superspeed reaction unit 2, and the bottom is connected to the bottom of the micro-power superspeed reaction unit 2.

[0044] By providing a plurality of heat dissipation assemblies 4, the present application can dissipate heat when the reactants generate a large amount of heat, and improve the heat dissipation efficiency.

[0045] In an alternative embodiment, the heat dissipation assembly 4 further comprises a first power pump and a second power pump 44, the first power pump is arranged between the first heat sink 41 and the bottom of the micro-power superspeed reaction unit 2, and the second power pump 44 is arranged between the first heat sink 41 and the bottom of the micro-power superspeed reaction unit 2.

[0046] In an alternative embodiment, the first heat sink 41 and the second heat sink 42 are made of different materials, and the first heat sink 41 has a greater heat dissipation power than the second heat sink 42.

[0047] In an alternative embodiment, a first feeding line and a second feeding line are further included, the first feeding line is arranged between the first power pump and the bottom of the micro-power ultra-speed reaction unit 2, and the second feeding line is arranged between the second power pump 44 and the bottom of the micro-power ultra-speed reaction unit 2.

[0048] In an alternative embodiment, the first power pump and the second power pump 44 are magnetic reaction pumps.

[0049] The system and device provided by the embodiment of the utility model have less investment, less land occupation, less personnel, full automation, high yield, low cost, safety and environmental protection, and can realize green production.

[0050] The above is only a preferred embodiment of the present application, and does not limit the present application in any form. Although the present application has been disclosed as above, it is not intended to limit the present application. Any person skilled in the art can make some changes or modifications to the above disclosed methods and technical contents without departing from the scope of the technical solution of the present application, and any simple modification, equivalent change and modification of the above embodiments according to the technical essence of the present application still belong to the scope of the technical solution of the present application.

Claims

1. A microkinetic reaction system, characterized in that, The application relates to a micro-power super-speed reaction device. The micro-power super-speed reaction device comprises a precision filtering unit for filtering reactants, a micro-power super-speed reaction unit connected with the precision filtering unit, at least two groups of accelerators in the micro-power super-speed reaction unit, wherein the two groups of accelerators are arranged in sequence from top to bottom of the micro-power super-speed reaction unit, and the speed increased by the two groups of accelerators is sequentially increased, a gas-liquid separator connected with a gas outlet of the micro-power super-speed reaction unit, and at least one group of heat dissipation components connected with an inlet of the micro-power super-speed reaction unit at the top and an outlet of the micro-power super-speed reaction unit at the bottom. The micro-power super-speed reaction unit further comprises a cooling unit for cooling the micro-power super-speed reaction unit. The micro-power super-speed reaction unit further comprises a radar monitor for monitoring the feeding size of the reactants. The precision filtering unit comprises a plurality of feeding ports, and each feeding port is provided with a feeding valve.

2. The micro power reaction system according to claim 1, wherein, The bottom of the gas-liquid separator is connected with the top of the micro-power super-speed reaction unit through a pipeline, and the pipeline is provided with a control valve.

3. The micro power reaction system according to claim 1, wherein, The heat dissipation components comprise a first heat radiator and a second heat radiator arranged side by side, and the top of the first heat radiator and the second heat radiator is connected with the top of the micro-power super-speed reaction unit, and the bottom is connected with the bottom of the micro-power super-speed reaction unit.

4. The micro power reaction system of claim 1, wherein, The heat dissipation components further comprise a first power pump and a second power pump, the first power pump is arranged between the first heat radiator and the bottom of the micro-power super-speed reaction unit, and the second power pump is arranged between the first heat radiator and the bottom of the micro-power super-speed reaction unit.

5. The micro power reaction system of claim 1, wherein, The first heat radiator and the second heat radiator are made of different materials, and the heat dissipation power of the first heat radiator is greater than that of the second heat radiator.

6. The micro power reaction system of claim 1, wherein, The application further comprises a first feeding pipeline and a second feeding pipeline, the first feeding pipeline is arranged between the first power pump and the bottom of the micro-power super-speed reaction unit, and the second feeding pipeline is arranged between the second power pump and the bottom of the micro-power super-speed reaction unit.

7. The micro power reaction system according to claim 6, wherein The first power pump and the second power pump are magnetic reaction pumps.

8. The micro power reaction system according to claim 6 or 7, characterized in that, ​ 9. The micro power reaction system of claim 7, wherein, ​ 10. The micro power reaction system according to claim 9, wherein, ​

Images