Porous fluid reactor
By designing a porous fluid reactor and using multi-layer staggered flow mixing method, the problem of uneven mixing of high-viscosity liquid raw materials in the prior art in chemical reactions is solved, and effective mixing and uniformity of chemical reactions with less preparation is achieved. reaction.
Patent Information
- Application Number
- CN202420322024.8
- Authority / Receiving Office
- CN · China
- Patent Type
- Utility models(China)
- Current Assignee / Owner
- Filing Date
- 2024-02-21
- Publication Date
- 2025-02-18
- Estimated Expiration
- 2034-02-21
AI Technical Summary
The prior art is difficult to effectively mix and uniformly carry out chemical reactions in solid or high-viscosity liquid raw materials. Especially in the case of small preparation amounts, effective mixing with magnetic stirrers and magnetons cannot be achieved during the reaction with a large viscosity.
A porous fluid reactor is designed. By setting up a multi-layer upper and lower reaction partition in the reactor cavity, and opening reaction through holes on the partition. Multi-layer staggered flow mixing method is adopted to achieve high viscosity liquids. Effective mixing of raw materials.
Through the multi-layer staggered flow mixing method, effective mixing and uniform reaction of solid or high-viscosity liquid raw materials in chemical reactions with small preparation amounts is achieved, and the problem of uneven mixing during the reaction with high viscosity is solved.
Smart Images
Figure CN222490000U_ABST
Abstract
Description
Technical Field
[0001] The utility model relates to the field of chemical equipment, in particular to a porous fluid reactor. Background Art
[0002] Fluid reactor is a kind of equipment used for chemical reaction, and its main function is to realize chemical reaction in fluid. This kind of equipment is widely used in chemical industry, pharmaceutical industry, environmental protection and other fields.
[0003] In a fluid reactor, the fluid flows through a specific reaction path and chemical reactions occur during the reaction. The design of this equipment can ensure that the fluid has good mixing and mass transfer effects during the reaction, thereby improving the reaction rate and product quality.
[0004] In addition, the fluid reactor can also be customized according to different reaction requirements, such as adjusting reaction temperature, pressure, flow rate and other parameters to meet specific process requirements. At the same time, the equipment can also be equipped with various detection instruments and control systems to achieve automatic control and online monitoring, and improve production efficiency and safety.
[0005] In the prior art, for chemical reactions with a small amount of preparation (less than 10 grams), the raw materials (relatively expensive) are solid or high-viscosity liquids, the viscosity during the reaction is high, and the viscosity of the reaction product is also high, it is impossible to achieve effective mixing and uniform reaction by using magnetic stirrers and magnets. Only heating and dissolving cannot achieve effective mixing and uniform reaction.
[0006] For this purpose, structural optimization is required. Utility Model Content
[0007] In order to overcome the above-mentioned defects of the prior art, the purpose of the utility model is to provide a porous fluid reactor.
[0008] In order to achieve the purpose of this utility model, the technical solution adopted is:
[0009] A porous fluid reactor, comprising:
[0010] A reactor cavity, in which a plurality of reaction baffles arranged up and down are arranged in the inner cavity of the reactor cavity, and a plurality of reaction through holes are opened on the reaction baffles;
[0011] The reaction through holes on any one of the reaction partitions and the reaction partitions on the upper layer and the reaction partitions on the lower layer are arranged in a staggered manner;
[0012] A baffle is provided under the reaction baffle at the bottom for limiting the position;
[0013] A reaction chamber is arranged between the bottommost reaction baffle and the inner cavity of the reactor cavity.
[0014] In a preferred embodiment of the present invention, both ends of the reaction baffle are fixed to the cavity wall of the inner cavity of the reactor cavity by fasteners or adhesion.
[0015] In a preferred embodiment of the present invention, the reactor cavity is a glass cavity.
[0016] In a preferred embodiment of the present invention, a cover made of glass is disposed at the upper end of the reactor cavity, preferably frosted glass.
[0017] In a preferred embodiment of the present invention, the reactor cavity further comprises a supporting outer cavity arranged on the outer periphery of the inner cavity of the reactor cavity, and the supporting outer cavity is made of glass.
[0018] In a preferred embodiment of the present invention, the peripheral surface of the upper end of the supporting outer cavity that contacts the inner cavity is a frosted surface.
[0019] In a preferred embodiment of the present invention, the supporting outer cavity or inner cavity is a cavity structure with an arc-shaped bottom.
[0020] In a preferred embodiment of the present invention, the reaction partition is made of polytetrafluoroethylene.
[0021] The beneficial effects of the utility model are:
[0022] The multi-layer staggered flow mixing method can achieve an effective and uniformly mixed reaction, and can realize an effective reaction of solid or high-viscosity liquid raw materials for chemical reactions with a small preparation amount (less than 10 grams). BRIEF DESCRIPTION OF THE DRAWINGS
[0023] Figure 1 It is a structural schematic diagram of the utility model. DETAILED DESCRIPTION
[0024] In order to make the purpose, technical solution and advantages of the utility model clearer, the utility model is further described in detail below through the accompanying drawings and embodiments. However, it should be understood that the specific embodiments described herein are only used to explain the utility model and are not used to limit the scope of the utility model. In addition, in the following structure, the description of the well-known structure and technology is omitted to avoid unnecessary confusion of the concept of the utility model.
[0025] In the description of the present invention, it should be noted that the terms "upper", "lower", "inner", "outer", "top / bottom" and the like indicate positions or positional relationships based on the positions or positional relationships shown in the drawings, and are only for the convenience of describing the present invention and simplifying the description. They do not indicate or imply that the device or component referred to must have a specific position, be constructed and operated in a specific position, and therefore cannot be understood as limiting the present invention. In addition, the terms "first" and "second" are only used for descriptive purposes and cannot be understood as indicating or implying relative importance.
[0026] like Figure 1 A porous fluid reactor shown includes a reactor chamber 100, and the reactor chamber 100 is a glass chamber.
[0027] A plurality of reaction baffles 111 arranged up and down are arranged in the inner cavity 110 of the reactor chamber 100 . A plurality of reaction through holes 111 a are opened on the reaction baffles 111 . The reaction through holes 111 a are provided to facilitate the flow of the reaction liquid.
[0028] The two ends of the reaction baffle 111 are fixed to the cavity wall of the inner cavity 110 of the reactor cavity by fasteners or adhesion, and the specific selection can be made according to actual needs, such as whether disassembly is required.
[0029] The reaction through holes 111a on any reaction partition 111 and the reaction partition on the upper layer and the reaction partition on the lower layer are staggered to facilitate sufficient reaction.
[0030] A baffle 112 is disposed under the reaction baffle 111 at the bottom for limiting the position, and a reaction chamber 120 is disposed between the reaction baffle 111 at the bottom and the inner chamber 110 of the reactor chamber.
[0031] A glass cover 130 is disposed at the upper end of the reactor chamber 100. The cover 130 is specifically made of frosted glass.
[0032] In addition, the reactor chamber 100 further includes a supporting outer chamber 140 disposed on the outer periphery of the inner chamber 110 of the reactor chamber 100. The supporting outer chamber 140 is made of glass. The peripheral surface 141 of the upper end of the supporting outer chamber 140 in contact with the inner chamber 110 is a frosted surface for anti-slip.
[0033] The outer cavity 140 or the inner cavity 110 is supported as a cavity structure with an arc-shaped bottom, so that the reaction chamber 120 is easily arranged.
[0034] Because of the above structure, the working principle of the utility model is:
[0035] The multi-layer partition openings allow the materials and intermediate reactants to melt and flow through the openings to the next layer. The openings of the next layer and the previous layer are staggered, and the mixing occurs during the process of flowing into the next layer. The partition is made of polytetrafluoroethylene, which is not easy to stick to the reactants and is also easy to take out.
[0036] The bottom of the structure of the utility model is provided with a baffle, so that the product can be conveniently taken out even if it stays on the middle baffle or flows into the reaction chamber at the bottom.
[0037] The reactor of the present invention can effectively solve the problem of uneven reaction of trace and small amounts of high viscosity, and has a relatively important significance in the reaction and preparation process of precious raw materials.
Claims
1. A porous fluid reactor, characterized in that: include: A reactor cavity, in which a plurality of reaction baffles arranged up and down are arranged in the inner cavity of the reactor cavity, and a plurality of reaction through holes are opened on the reaction baffles; The reaction through holes on any one of the reaction partitions and the reaction partitions on the upper layer and the reaction partitions on the lower layer are arranged in a staggered manner; A baffle is provided under the reaction baffle at the bottom for limiting the position; A reaction chamber is arranged between the bottommost reaction baffle and the inner cavity of the reactor cavity.
2. A porous fluid reactor as claimed in claim 1, characterized in that: The two ends of the reaction baffle are fixed to the cavity wall of the inner cavity of the reactor cavity by fasteners or adhesion.
3. A porous fluid reactor as claimed in claim 1, characterized in that: The reactor cavity is a glass cavity.
4. A porous fluid reactor as claimed in claim 1, characterized in that: A cover made of glass is arranged at the upper end of the reactor cavity.
5. A porous fluid reactor as claimed in claim 1, characterized in that: The reactor cavity further comprises a supporting outer cavity arranged on the outer periphery of the inner cavity of the reactor cavity, and the supporting outer cavity is made of glass.
6. A porous fluid reactor as claimed in claim 5, characterized in that: The peripheral surface of the upper end of the supporting outer cavity body in contact with the inner cavity is a frosted surface.
7. A porous fluid reactor as claimed in claim 5, characterized in that: The supporting outer cavity or inner cavity is a cavity structure with an arc-shaped bottom.
8. A porous fluid reactor as claimed in claim 1, characterized in that: The reaction partition is made of polytetrafluoroethylene.