CN212999919U

CN212999919U - High efficiency chemical industry reaction unit

Info

Publication number: CN212999919U
Application number: CN202021154711.1U
Authority: CN
Inventors: 徐桅; 于凯
Original assignee: Jinjiuqi Fushun Pharmaceutical Co ltd
Current assignee: Jinjiuqi Fushun Pharmaceutical Co ltd
Priority date: 2020-06-20
Filing date: 2020-06-20
Publication date: 2021-04-20
Anticipated expiration: 2030-06-20

Abstract

The utility model relates to a high-efficiency chemical reaction device, which comprises a reaction cabin, wherein a water inlet seat is arranged on the left side of the reaction cabin, a water outlet is arranged on the right side of the reaction cabin, and a valve is arranged on the water outlet; the water conservancy diversion seat is installed to the inner end of seat of intaking, the compression roller is installed through the synchronizing shaft in the inner chamber left side of seat of intaking, the mounting panel is installed to the rear side of reaction chamber, install power unit on the mounting panel, power unit comprises the motor, and the application of the machine of qi is exploded at the reaction chamber middle part, has carried out rational design, and the trachea of drawing forth on will exploding the machine of qi is through a circle gas collecting channel pressure equipment of detaining the cover-type, makes the gas that gets into in the gas collecting channel be the ascending of wider scope and gushes out to can carry out the surge of large tracts of land to the liquid material in the reaction chamber, improve the rationality of structure greatly, owing to gushing the scope and increased, consequently improved.

Description

High efficiency chemical industry reaction unit

Technical Field

The utility model relates to a chemical industry reaction cabin technical field, concretely relates to high efficiency chemical industry reaction unit.

Background

Chemical processes are an engineering discipline for studying the common laws of chemical processes and physical processes performed in the chemical industry and other process industries (process industry). In the process of changing the composition of the substance, two or more injected raw materials need to be mixed and reacted by a reaction cabin, for example, the mixing and reaction of two or more liquid materials, and the like, and the injected liquid materials are often mixed and reacted by a large reaction tank or reaction cabin, and the reaction amount is larger than that of a common stirrer, so that the working efficiency can be improved.

The existing material reaction cabin for the chemical industry is mostly provided with an aerator for promoting liquid material mixing reaction, and gas produced by the aerator causes a liquid material to generate a surge effect, so that the mixing speed between the liquid material and the liquid material is accelerated.

SUMMERY OF THE UTILITY MODEL

To the above-mentioned current problem, the utility model aims to provide a high efficiency chemical industry reaction unit to solve above-mentioned pipeline about "exploding the mechanism of qi and upwards produce the single tube operation when surging gaseous, consequently the combustion gas can only carry out local surge effect to the liquid in the reaction chamber, can not all-round surging, consequently liquid mixing reaction rate is lower, and the material of sneaking into is only when adding solid-state reactant, for example lime sediment, they can not reach the purpose of quick decomposition after getting into the reaction chamber, also can lead to the problem that liquid mixture reaction rate slows down" equally.

In order to achieve the above purpose, the utility model provides a following technical scheme:

a high-efficiency chemical reaction device comprises a reaction cabin, wherein a water inlet seat is arranged on the left side of the reaction cabin, a water outlet is arranged on the right side of the reaction cabin, and a valve is arranged on the water outlet; the water inlet device comprises a water inlet seat, a water outlet seat, a water inlet chamber, a reaction cabin, a water inlet mechanism, a water outlet mechanism, a water inlet mechanism and a water outlet mechanism, wherein a flow guide seat is installed at the inner end of the water inlet seat, a press roller is installed on the left side of an inner cavity of the water inlet seat through a;

the reaction chamber is internally provided with an aerator, an air pipe on the aerator extends outwards, a gas collecting hood is pressed on the outer end of the air pipe, and three rows of spray heads penetrate through the top of the gas collecting hood.

Preferably, a diversion seat is installed on the left wall of the inner cavity of the reaction cabin, and the diversion seat is located on the bottom side of the water inlet seat.

Preferably, the compression roller is positioned on the right side of the flow guide seat, and the flow guide seat is a streamline cavity which extends towards the right arc.

Preferably, a two-millimeter rotating gap is reserved between the compression roller and the bottom surface of the reaction cabin.

Preferably, the gas-collecting hood is of a rectangular buckling cavity structure, and the gas-collecting hood is communicated with the gas pipe in a gas mode.

Preferably, the gas collecting hoods are annularly distributed on the outer peripheral side of the gas explosion machine.

Compared with the prior art, the utility model discloses following beneficial effect has:

(1) reaction chamber left side pan feeding district is provided with compression roller assembly, and compression roller assembly's left side is provided with the water conservancy diversion seat of inside drainage material, passes through the material that the water conservancy diversion seat was introduced by the pan feeding district, if when being the impurity nature material of granule class, makes the compression roller action, and the action in-process rolls this type of material breakage, reaches the purpose of fine processing, then sneaks into liquid material again, can improve compounding speed, and functional structure has obtained the improvement.

(2) The gas pipe led out from the gas explosion machine is pressed through a circle of cover-buckled gas collecting hood, so that the gas entering the gas collecting hood is gushed upwards in a larger range, and the liquid material in the reaction chamber can be subjected to large-area surging, so that the reasonability of the structure is greatly improved, and the mixing speed of the liquid material is improved due to the increase of the surging range.

Drawings

Fig. 1 is a schematic structural diagram of the present invention;

fig. 2 is a schematic rear view of the present invention from fig. 1;

FIG. 3 is a schematic view of the internal structure of the utility model after being partially cut;

fig. 4 is a schematic top view of the present invention.

Description of the main reference numerals: 1. a reaction cabin; 2. a water inlet seat; 3. a flow guide seat; 4. a compression roller; 5. a synchronizing shaft; 6. a belt drive mechanism; 7. a power mechanism; 8. mounting a plate; 9. an aerator; 10. an air tube; 11. a gas-collecting hood; 12. a spray head; 13. A water outlet; 14. and (4) a valve.

Detailed Description

The technical solutions of the present invention will be described clearly and completely with reference to the accompanying drawings, and it is obvious that the described embodiments are some, but not all embodiments of the present invention. Based on the embodiments in the present invention, all other embodiments obtained by the technical personnel in the field without creative work belong to the protection scope of the present invention.

In the description of the present invention, it should be noted that the directions or positional relationships indicated as the terms "center", "upper", "lower", "left", "right", "vertical", "horizontal", "inner", "outer", etc., appear based on the directions or positional relationships shown in the drawings, and are only for convenience of description and simplification of description, but do not indicate or imply that the device or element referred to must have a specific direction, be constructed and operated in a specific direction, and thus, should not be construed as limiting the present invention.

In the description of the present invention, it is to be noted that, unless otherwise explicitly specified or limited, the terms "mounted," "connected," and "connected" should be interpreted broadly, e.g., as being either fixedly connected, detachably connected, or integrally connected; can be mechanically or electrically connected; they may be connected directly or indirectly through intervening media, or they may be interconnected between two elements. The specific meaning of the above terms in the present application can be understood in a specific case to those skilled in the art.

Referring to the attached drawings 1-4, a high-efficiency chemical reaction device comprises a reaction cabin 1, wherein a water inlet seat 2 used for being connected with an external feeding device or a material feeding pipeline is arranged on the left side of the reaction cabin 1, a water outlet 13 used for discharging reacted materials outwards is arranged on the right side of the reaction cabin 1, and a valve 14 is arranged on the water outlet 13 as shown in fig. 2; the inner end of the water inlet seat 2 is provided with a guide seat 3 for guiding the guided foreign materials downwards, the guide seat 3 is positioned at the bottom side of the water inlet seat 2, the structure of the guide seat 3 is shown in figures 1 to 3, the left side of the inner cavity of the water inlet seat 2 is provided with a rotary and rolling compression roller 4 through a synchronizing shaft 5, the foreign materials guided by the guide seat 3 can be rolled and processed to be crushed again, the functional structure is improved, the mixing speed can be improved when the materials are mixed with the liquid materials injected in advance in the cabin in the material crushing process, so the working efficiency when the two materials are mixed is improved, the rear side of the reaction cabin 1 is provided with a mounting plate 8, the mounting plate 8 is provided with a power mechanism 7, the power mechanism 7 is a motor, the motor of the power mechanism 7 is connected with the synchronizing shaft 5 through a belt transmission mechanism 6, and an electric component for enabling the compression roller 4 to rotate is formed, automatic rolling is realized;

as shown in fig. 3 and 4, an aerator 9 is installed in the reaction chamber 1, an air pipe 10 on the aerator 9 extends outwards, a gas collecting hood 11 is press-fitted on an outer end of the air pipe 10, three rows of spray heads 12 penetrate through the top of the gas collecting hood 11, the gas collecting hood 11 is of a rectangular buckling cavity structure, the gas collecting hood 11 is in gas communication with the air pipe 10, the gas collecting hood 11 is annularly distributed on the outer periphery of the aerator 9, the ring of gas collecting hood 11 with the spray heads 12 can intensively collect the surging gas generated by the peripheral pipelines of the aerator 9, and then the surging gas is sprayed upwards by the spray heads 12 with wider distribution range in a large area effect, so that the mixing range of the feed liquid in the mixing process is enlarged, the surging range of the feed liquid is increased, and the mixing speed of the feed liquid is increased.

Specifically, the compression roller 4 is positioned on the right side of the flow guide seat 3, the flow guide seat 3 is a streamline cavity which is in an arc shape towards the right, so that the impurity materials injected from the left to the right can be guided to the compression roller 4 to the maximum extent, a two-millimeter rotating gap is reserved between the compression roller 4 and the bottom surface of the reaction cabin 1, the materials can be taken out from the left to the right when the compression roller 4 rotates, and the materials are crushed in the taking-out process, so that the structural design of the flow guide seat 3 is reasonable, and the same position relation between the flow guide seat 3 and the compression roller 4 is reasonable in design.

The working principle is as follows: when the material injected from the left water inlet seat 2 is a liquid material, it will be mixed with another or multiple kinds of liquid materials injected in advance in the reaction chamber 1 after entering the reaction chamber 1, the aerator 9 of the prior art for gas injection will inject gas outwards from the gas pipe 10 around it, the injected gas will enter into each corresponding gas collecting hood 11, the gas collecting hood 11 will collect these gases, and then inject upwards from the nozzles 12 arranged on them, because the nozzles 12 are arranged in a plurality of dense hemp and located in the reaction chamber 1 in a wider range, when they discharge gas together upwards, they will move the liquid materials in the reaction chamber 1 in a wider range, thus improving the mixing speed of the liquid materials, if there are a lot of impurities, such as limestone, various solid auxiliary reactants, the power mechanism 7 is electrified to work, when the reactants enter the reaction chamber 1, the reactants are firstly guided to the right through the guide seat 3 to the compression roller 4 to the maximum extent, when the electrified compression roller 4 rotates, the materials can be taken out from the left to the right, and in the process of taking out, the materials are crushed, the functional structure is improved, and the mixing speed can be improved when the materials are mixed with liquid materials injected in the chamber in advance in the process of crushing the materials, so that the mixing speed can be improved, and the reaction efficiency is improved.

The foregoing descriptions of specific exemplary embodiments of the present invention have been presented for purposes of illustration and description. It is not intended to limit the invention to the precise form disclosed, and obviously many modifications and variations are possible in light of the above teaching. The exemplary embodiments were chosen and described in order to explain certain principles of the invention and its practical application to enable one skilled in the art to make and use various exemplary embodiments of the invention and various alternatives and modifications as are suited to the particular use contemplated. It is intended that the scope of the invention be defined by the claims and their equivalents.

Claims

1. A high-efficiency chemical reaction device comprises a reaction cabin (1), wherein a water inlet seat (2) is arranged on the left side of the reaction cabin (1), a water outlet (13) is arranged on the right side of the reaction cabin (1), and a valve (14) is arranged on the water outlet (13); the method is characterized in that: the water-feeding device is characterized in that a flow guide seat (3) is mounted at the inner end of the water feeding seat (2), a compression roller (4) is mounted on the left side of an inner cavity of the water feeding seat (2) through a synchronizing shaft (5), a mounting plate (8) is mounted on the rear side of the reaction cabin (1), a power mechanism (7) is mounted on the mounting plate (8), the power mechanism (7) consists of a motor, and the motor of the power mechanism (7) is connected with the synchronizing shaft (5) through a belt transmission mechanism (6);

an aerator (9) is installed in the reaction cabin (1), an air pipe (10) on the aerator (9) extends outwards, a gas collecting hood (11) is installed at the outer end of the air pipe (10) in a pressing mode, and three rows of spray heads (12) penetrate through the top of the gas collecting hood (11).

2. The high-efficiency chemical reaction device according to claim 1, wherein the flow guide seat (3) is installed on the left wall of the inner cavity of the reaction cabin (1), and the flow guide seat (3) is located at the bottom side of the water inlet seat (2).

3. The high-efficiency chemical reaction device according to claim 1, wherein the compression roller (4) is positioned at the right side of the flow guide seat (3), and the flow guide seat (3) is a streamline cavity which is in an arc shape towards the right.

4. A high efficiency chemical reaction device according to claim 1, characterized in that a two mm rotation gap is left between the press roll (4) and the bottom surface of the reaction chamber (1).

5. A high efficiency chemical reaction device according to claim 1, wherein the gas collecting channel (11) is a rectangular buckle cavity structure, and the gas collecting channel (11) is in gas communication with the gas pipe (10).

6. The high-efficiency chemical reaction device as claimed in claim 1, wherein the gas collecting hoods (11) are annularly distributed on the outer peripheral side of the aerator (9).