Viscous liquid material distributor

Abstract

The utility model provides a viscous liquid material distributor which is provided with a liquid receiving disc, a conical liquid distributing body is arranged in the center of the liquid receiving disc, flow distributing baffles are evenly distributed on the periphery of the liquid receiving disc, the conical liquid distributing body and the flow distributing baffles are both fixedly installed on the liquid receiving disc, a feeding pipe is arranged above the conical liquid distributing body, and a discharging pipe is arranged above the feeding pipe. An outlet of the feeding pipe is lower than the top of the flow dividing baffle and higher than the top of the conical flow dividing body, the height difference between the outlet of the feeding pipe and the top of the conical flow dividing body is not smaller than 20 mm, the flow dividing baffle is formed by bending a plate, and the angle of the bending position of the plate is larger than 90 degrees. The utility model solves the technical problems that the existing viscous liquid distributor adopts a plane disc to receive liquid, the requirements on processing precision and levelness are higher and are difficult to realize, the viscous liquid material is difficult to uniformly distribute on the cross section, and the overall production quality is influenced. The high-viscosity liquid dispersing device can be widely applied to the dispersing process of high-viscosity liquid.

Description

TECHNICAL FIELD

[0001] The utility model relates to a distributor, in particular to a viscosity liquid material distributor. BACKGROUND

[0002] In various production, viscosity liquid material is relatively poor in flowability due to viscosity, and some production processes need to uniformly disperse the material to the cross section of equipment to achieve uniform chemical reaction, physical process or adsorption process. The general distributor adopts a type of flat disc liquid receiving, and the machining precision and levelness adjustment of the liquid distribution disc are required to be higher during processing and installation, which has great difficulty, and problems such as change of inclination of the flat disc caused by rebound of the fixing support after installation and thermal force, which makes it difficult for the viscosity liquid material to be uniformly distributed on the cross section in actual production and use, and further affects the high-quality operation of production. SUMMARY

[0003] The utility model discloses to the technical problem that the flat disc liquid receiving is adopted in the prior viscosity liquid distributor, the machining precision and levelness requirement are higher and difficult to realize, the viscosity liquid material is difficult to be uniformly distributed on the cross section, and further affects the overall production quality, provide a viscosity liquid material distributor that reduces the requirement of installation and assembly precision of the liquid receiving disc, makes each discharge port on the distribution disc uniformly discharge, can stably realize the uniform distribution of viscosity liquid material on the cross section of equipment, and provides reliable guarantee for the overall production quality.

[0004] Therefore, the technical scheme of the utility model is that a viscosity liquid material distributor is provided with a liquid receiving disc, a conical liquid distribution body is arranged at the center position of the liquid receiving disc, and flow baffles are uniformly arranged around the liquid receiving disc, the conical liquid distribution body and the flow baffles are fixedly installed on the liquid receiving disc, a feed pipe is arranged above the conical liquid distribution body, the outlet position of the feed pipe is lower than the top of the flow baffles and higher than the top of the conical liquid distribution body, the height difference between the outlet position of the feed pipe and the top of the conical liquid distribution body is not less than 20 mm, the flow baffles are formed by bending a plate, and the angle of the bent part of the plate is greater than 90°.

[0005] Preferably, the conical liquid distribution body and the flow baffles are welded on the liquid receiving disc.

[0006] Preferably, the liquid receiving disc, the conical liquid distribution body and the flow baffles are polished and ground to improve smoothness.

[0007] Preferably, the angle of the bent part of the plate is 120°.

[0008] Preferably, four flow baffles are arranged on each liquid receiving disc, and the edges of the flow baffles are flush with the edges of the liquid receiving disc.

[0009] Preferably, the bottom diameter of the conical liquid distributor is 1 / 2 of the diameter of the receiving tray.

[0010] Preferably, the thickness of the plate of the flow distribution baffle is not less than 5mm, and the thickness of the receiving tray is not less than 6mm.

[0011] Preferably, the height of the flow distribution baffle is not less than 2 times the height of the conical liquid distributor.

[0012] The utility model has beneficial effects that,

[0013] (1) the application can effectively disperse the liquid to all directions by setting the conical liquid distributor in the middle of the receiving tray, even if the viscosity is large, due to the conical structure, under the action of liquid gravity, the liquid can also easily scatter and slide down, and under the action of inertia, the liquid can be dispersed to all directions of the container, therefore, the requirement of assembly precision is reduced, the assembly efficiency is improved, and the equipment production cost is reduced;

[0014] (2) by setting the flow distribution baffle around the receiving tray, the liquid flowing down from the conical liquid distributor can be distributed, and the liquid can be further impacted and dispersed, so that the dispersion is more uniform;

[0015] (3) by setting the outlet height of the feeding pipe lower than the flow distribution baffle and higher than the top of the conical liquid distributor, the liquid can be splashed on the conical liquid distributor through a certain height difference, the height difference can increase the impact force of the liquid on the conical liquid distributor, and the dispersion effect is better, and the feeding pipe outlet is lower than the flow distribution baffle, so that the liquid can be reduced as much as possible without flowing directly through the conical liquid distributor, so as to ensure that the viscous liquid is fully dispersed;

[0016] (4) the receiving tray, the conical liquid distributor and the flow distribution baffle all improve the surface precision by polishing and grinding, so that the adhesion resistance to the liquid can be reduced, and the liquid dispersion degree can be improved;

[0017] (5) the bottom diameter of the conical liquid distributor is 1 / 2 of the diameter of the receiving tray, which can ensure that the liquid has sufficient distribution space on the receiving tray, and can also avoid that the liquid is adhered on the receiving tray due to too large space plane; the angle of the plate bending part of the flow distribution baffle is greater than 90°, so that when the material flows out of the receiving tray, the inlet is large and the outlet is small, that is, the diameter becomes smaller and the pressure becomes larger when the liquid flows out of the receiving tray, which is more conducive to improving the flow speed of the liquid, so as to reduce the flow influence caused by the viscosity of the liquid. BRIEF DESCRIPTION OF DRAWINGS

[0018] Figure 1 is the structure schematic diagram of the distributor of the utility model embodiment;

[0019] Figure 2 is the sectional structure schematic diagram of the distributor of the utility model embodiment;

[0020] Figure 3 is the layout diagram of the distributor in the device according to the embodiment of the utility model;

[0021] Figure 4 is the relative height position structure diagram of the feed pipe and the distributor in the embodiment of the utility model.

[0022] Symbol explanation in the drawing:

[0023] 1. liquid receiving disc; 2. conical liquid distribution body; 3. flow distribution baffle; 4. feed pipe. DETAILED DESCRIPTION

[0024] The utility model will be further described in combination with the embodiments.

[0025] As Figures 1-4 shown, a kind of viscosity liquid material distributor, is equipped with liquid receiving disc 1, and the center position of liquid receiving disc 1 is equipped with conical liquid distribution body 2, and the periphery of liquid receiving disc 1 is equipped with flow distribution baffle 3, and conical liquid distribution body 2 and flow distribution baffle 3 are all fixed on liquid receiving disc 1 by welding, and feed pipe 4 is equipped above conical liquid distribution body 2, and the outlet position of feed pipe 4 is lower than the top of flow distribution baffle 3, higher than the top of conical liquid distribution body 2, and the height difference between the outlet position of feed pipe 4 and the top of conical liquid distribution body 2 is not less than 20mm, flow distribution baffle 3 is formed by bending sheet material, and the angle of sheet material bending portion is 120 °, can realize that material flows out from liquid receiving disc 1, import is large, outlet is small, i.e. the diameter is reduced when flowing out of liquid receiving disc 1, and pressure is increased, more conducive to improving the flow speed of liquid, to reduce the flow influence caused by liquid viscosity. Liquid receiving disc 1, conical liquid distribution body 2, flow distribution baffle 3 are all improved by polishing and polishing surface precision, can reduce the adhesion resistance to liquid, and it is beneficial to improve liquid dispersity. Four flow distribution baffles 3 are equipped on each liquid receiving disc 1, and the edge of flow distribution baffle 3 is flush with the edge of liquid receiving disc 1. The diameter of the bottom of conical liquid distribution body 2 is 1 / 2 of the diameter of liquid receiving disc 1, which can ensure that liquid has sufficient flow space on liquid receiving disc 1, and also can avoid that liquid is adhered on liquid receiving disc 1 due to too large space plane. The thickness of sheet material of flow distribution baffle 3 is not less than 5mm, and the thickness of liquid receiving disc 1 is not less than 6mm, which can ensure sufficient strength to bear the gravity and impact force of viscosity liquid.

[0026] By setting the shunt baffle 3 on the periphery of the receiving tray 1, the liquid flowing down from the conical liquid distribution body 2 can be shunted, and the liquid can be further impacted and dispersed, so that the dispersion is more uniform. By setting the outlet height of the feed pipe 3 lower than the shunt baffle 3 and higher than the top of the conical liquid distribution body 2, and the height of the shunt baffle 3 is not less than 2 times the height of the conical liquid distribution body 2, the liquid can be splashed on the conical liquid distribution body 2 through a certain height difference, the height difference can increase the impact force of the liquid on the conical liquid distribution body 2, and the dispersion effect is better. The outlet of the feed pipe 4 is lower than the shunt baffle 3, which can minimize the liquid flowing directly without passing through the conical liquid distribution body 2, so as to ensure that the viscous liquid is fully dispersed.

[0027] The present application can effectively disperse the liquid in all directions by setting the conical liquid distribution body 2 in the middle of the receiving tray 1. Even if the viscosity is large, due to the conical structure, the liquid can easily spread and slide under the action of gravity, and disperse in all directions of the container under the action of inertia. Therefore, the assembly precision requirement is reduced, the assembly efficiency is improved, and the equipment production cost is reduced.

[0028] The above is only a specific embodiment of the present application, and cannot limit the scope of the present application. Therefore, the replacement of equivalent components or equivalent changes and modifications made within the scope of the present application shall still fall within the scope of the present application.

Claims

1. A viscous liquid material distributor characterized by, The liquid receiving disc is provided with a conical liquid distribution body at the center position, and is uniformly provided with a flow distribution baffle at the periphery, the conical liquid distribution body and the flow distribution baffle are fixedly installed on the liquid receiving disc, the top of the flow distribution baffle is lower than the outlet of the feeding pipe and higher than the top of the conical liquid distribution body, the height difference between the outlet of the feeding pipe and the top of the conical liquid distribution body is not less than 20 mm, the flow distribution baffle is formed by bending a plate, and the angle of the bent plate is greater than 90°.

2. The viscous liquid material distributor of claim 1, wherein, The conical liquid distribution body and the flow distribution baffle are welded on the liquid receiving disc.

3. The viscous liquid material distributor of claim 1, wherein, The liquid receiving disc, the conical liquid distribution body and the flow distribution baffle are polished to improve the smoothness.

4. The viscous liquid material distributor of claim 1, wherein, The angle of the bent plate is 120°.

5. The viscous liquid material distributor of claim 1, wherein, Four flow distribution baffles are arranged on each liquid receiving disc, and the edges of the flow distribution baffles are flush with the edges of the liquid receiving disc.

6. The viscous liquid material distributor of claim 1, wherein, The bottom diameter of the conical liquid distribution body is 1 / 2 of the diameter of the liquid receiving disc.

7. The viscous liquid material distributor of claim 1, wherein, The thickness of the plate of the flow distribution baffle is not less than 5 mm, and the thickness of the liquid receiving disc is not less than 6 mm.

8. The viscous liquid material distributor of claim 1, wherein, The height of the flow distribution baffle is not less than 2 times the height of the conical liquid distribution body.

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