Wettable powder production line

Abstract

The utility model provides a wettable powder production line, which relates to the field of pesticide production, and comprises a wettable powder processing module, the wettable powder processing module comprises two dust removers II, the two dust removers II and two cyclone separators are respectively connected in series at the tops of two mixing tanks, a discharge port at the bottom of a coarse mixing tank is communicated with a feed port of a jet mill, and a feed port of the jet mill is communicated with a feed port of a discharge port. A discharge port of the jet mill is communicated with feed ports of the two cyclone separators through a Y-shaped pipeline, and an air suction port in the top of each cyclone separator is communicated with the interior of one dust remover II; the dust collecting module comprises a dust remover I and a dust collecting cover, the dust collecting cover covers a feeding hopper at the top of the coarse mixing tank and seals the top of the feeding hopper, and the top end of the dust collecting cover communicates with an air suction port of the dust remover I through a pipeline I; one end of the pipeline II is communicated with an air suction port of the dust remover I, and the other end of the pipeline II is respectively arranged at the edge parts of discharge ports of the two mixing tanks; the utility model has the beneficial effects that the mixing and crushing effects are better, and dust in a workshop is less.

Description

TECHNICAL FIELD

[0001] The utility model relates to the field of pesticide production, especially to a wettable powder production line. BACKGROUND

[0002] The production workshop of the early-stage wettable powder includes a rough mixing tank, an air flow pulverizer, a cyclone separator, a mixing tank and a dust collector, the rough mixing tank is provided with a feeding hopper at the upper end, the feeding opening of the feeding hopper is located at the side of the feeding hopper and is of a double-door type, a plurality of materials are poured into the feeding hopper and then enter the rough mixing tank, after mixing in the rough mixing tank, the materials enter the air flow pulverizer at the lower end of the rough mixing tank, the materials pulverized by the air flow pulverizer enter the cyclone separator through the action of the pipeline and the induced draft fan, a part of the materials with light weight enter the dust collector due to the induced draft effect of the induced draft fan and are temporarily stored, and the materials will be mixed with the materials in the mixing tank in the later stage, the remaining materials with heavy weight continue to be pulverized and mixed due to the gravity effect and enter the mixing tank through the discharge opening at the bottom of the cyclone separator, when the pulverization, mixing and drying degree reach a certain degree, the materials are discharged from the discharge opening at the bottom of the mixing tank, and at the same time, the materials are weighed and then sealed in bags, thereby completing the production process of the wettable powder.

[0003] Firstly, in order to facilitate and accelerate the feeding, the feeding hopper of the rough mixing tank is of a double-door type, the worker can quickly pour the materials into the feeding hopper after opening the door, but a large amount of dust is volatilized in the pouring process, which not only causes the pollution in the workshop, but also is not conducive to the health of the worker due to the toxicity of some materials.

[0004] Secondly, the mixing tank is sufficient to accommodate the materials mixed and pulverized by the rough mixing tank, but the materials are accumulated and mixed in the mixing tank and continue to be pulverized, and the temperature and humidity in the mixing tank need to be controlled by the induced draft fan to prevent the materials from being damp or the temperature from being too high, thereby affecting the quality and stability of the product, it is found in the actual work that the mixing and pulverization effect of the materials sometimes cannot meet the requirements or the processing time is long, and the drying degree index cannot meet the requirements. UTILITY MODEL CONTENTS

[0005] The utility model aims at providing a wettable powder production line with better mixing and pulverization effect and dust collection.

[0006] The technical scheme of the utility model is as follows:

[0007] A wettable powder production line, comprising a wettable powder processing module and a dust collection module.

[0008] The wettable powder processing module comprises a rough mixing tank, two mixing tanks, an air flow pulverizer, two dust collectors II, and two cyclone separators, the two dust collectors II and the two cyclone separators are connected in series at the top of the two mixing tanks, respectively, and the discharge outlets of the two dust collectors II and the two cyclone separators are communicated with the feeding inlets of the two mixing tanks, respectively, the two mixing tanks are arranged side by side, the rough mixing tank is arranged at one side of the two mixing tanks and in the middle of the two mixing tanks, so as to facilitate feeding of the two mixing tanks and save pipelines, the discharge outlet at the bottom of the rough mixing tank is communicated with the feeding inlet of the air flow pulverizer, the discharge outlet of the air flow pulverizer is communicated with the feeding inlets of the two cyclone separators through a "Y"-shaped pipeline, and the air suction inlets at the top of each cyclone separator are communicated with a dust collector II, respectively, the air inlets of the two dust collectors II are communicated with the air inlet of the induced draft fan through parallel connection of the air induction pipes;

[0009] Further, the pipelines are respectively provided with corresponding valves;

[0010] Further, the internal storage volumes of the two mixing tanks are 3m 3 , respectively, and the internal storage volume of the rough mixing tank is 2m 3 ; 2

[0011] The dust collection module comprises a dust collector I, a dust collecting hood and a plurality of pipelines, the dust collector I is arranged side by side with the rough mixing tank, the connecting line of the center points of the two mixing tanks is parallel to the connecting line of the center points of the dust collector I and the rough mixing tank, the top of the rough mixing tank is provided with a feeding hopper, the top of the feeding hopper is open, the feeding inlet of the feeding hopper is located at the side of the feeding hopper and is double-door type, the dust collecting hood is arranged on the top of the feeding hopper and seals the top of the feeding hopper, the top end of the dust collecting hood is communicated with the air suction inlet of the dust collector I through a pipeline I, one end of a pipeline II is communicated with the air suction inlet of the dust collector I, the other end of the pipeline II is arranged within 15cm of the edge of the discharge outlets of the two mixing tanks, respectively, the air inlet of the dust collector I is communicated with the air inlet of an induced draft fan I through an air induction pipe, and then, after air induction of the induced draft fan I, negative pressure is generated in the dust collector I and the pipeline II to adsorb the dust at the edges of the two mixing tanks at the other end of the pipeline II;

[0012] One end of a branch pipeline I is communicated with the pipeline II, and the other end is arranged within 15cm of the manhole edge of the rough mixing tank;

[0013] One end of a branch pipeline II is communicated with the air suction inlet of the dust collector I, and the other end is communicated with the air inlet of the rough mixing tank;

[0014] A dust collecting hood is arranged at the air outlet of the pipeline II;

[0015] ​Further, the dust collector I is a DMC pulse cloth bag dust collector, and the total filtering area is 10 m 2 ;

[0016] Further, the manhole of the coarse mixing tank is used for checking and maintaining the inside of the coarse mixing tank, the manhole of the coarse mixing tank is located on the top surface of the coarse mixing tank, and the manhole and the feeding hopper are located on the two sides of the coarse mixing tank respectively.

[0017] Further, the induced draft fan II is a high-pressure induced draft fan, the induced draft fan I is a medium-pressure induced draft fan, and the gas outlets of the induced draft fan II and the induced draft fan I are connected with the air shaft through pipelines.

[0018] Further, the pipeline IV is arranged at the edge of the manhole of the two mixing tanks, and the other end of the pipeline IV is connected with the pipeline II in parallel and then connected with the air inlet of the dust collector I.

[0019] Further, the stirring shafts are arranged in the coarse mixing tank and the two mixing tanks, and spiral blade stirring blades are arranged on the stirring shafts for stirring and further crushing the materials, and the outer walls of the coarse mixing tank and the two mixing tanks are provided with vibrating screens for knocking the outer walls of the coarse mixing tank and the two mixing tanks.

[0020] Further, the wettable powder production line comprises a supporting platform, the supporting platform comprises two upper and lower layers, a crawling ladder is arranged between the two upper and lower layers, the two mixing tanks and the coarse mixing tank penetrate through the supporting platform, and the feeding inlets of the two mixing tanks, the two dust collectors II and the two cyclone separators are located on the upper layer of the supporting platform, the feeding outlets of the two mixing tanks are located on the lower layer of the supporting platform, the feeding hopper in the coarse mixing tank is located on the upper layer of the supporting platform, the feeding outlet in the coarse mixing tank is located on the lower layer of the supporting platform, and the dust collector I is located on the upper layer of the supporting platform.

[0021] The utility model has the advantages and positive effects that:

[0022] The dust cover, the dust collector I and the dust collector II generate negative pressure to collect the dust volatilized in the feeding process, so that the dust volatilization amount in the workshop is reduced, the environment of the workshop is maintained, and the physical and mental health of the workers is ensured.

[0023] Further, the pipelines are arranged at the three manholes to collect the dust, and the environment of the workshop is further ensured.

[0024] Since the coarse mixing tank is arranged on one side of the two mixing tanks and located in the middle of the two mixing tanks, the two mixing tanks are conveniently fed, and the pipelines are saved, and since the connecting line of the center points of the two mixing tanks is parallel to the connecting line of the center points of the dust collector I and the coarse mixing tank, the stroke is short, and the pipelines are saved.

[0025] The mixed material after being broken by the rough mixing tank enters the jet mill, and after being broken, enters two cyclone separators under the condition of negative pressure suction by the high-pressure induced draft fan. Since the discharge of the jet mill is divided, a small amount of material can be dried better under the condition of negative pressure suction by the high-pressure induced draft fan, and after being separated by the two cyclone separators, enters two mixing tanks for further breaking and mixing, so that the mixing and breaking are good, and the drying condition also meets the requirements. The improvement point ensures the product quality.

[0026] Further, by limiting the size and storage volume of one rough mixing tank and two mixing tanks, the late mixing, breaking and drying of the material are further ensured, and the product quality is guaranteed.

[0027] One end of the branch pipe II is communicated with the air suction port of the dust collector I, and the other end is communicated with the air inlet of the rough mixing tank for providing air for the mixing process of the rough mixing tank, further drying the material, and guaranteeing the product quality.

[0028] In the above process, one high-pressure induced draft fan provides negative pressure for two dust collectors II, and the two dust collectors II are communicated with two cyclone separators, so that the above high-pressure induced draft fan also provides negative pressure for the two cyclone separators, thereby saving energy consumption.

[0029] The induced draft fan II for production is a high-pressure induced draft fan, and the induced draft fan I for collecting dust is a medium-pressure induced draft fan, so that the setting is reasonable, energy consumption is saved, and the production demand is met. Since the air outlets of the induced draft fan II and the induced draft fan I are communicated with a ventilation shaft through the pipe, the cost is saved and the standard of environmental protection exhaust gas emission is met.

[0030] Since the support platform includes upper and lower layers, it is convenient for workers to load and maintain on the upper layer, and also makes the dust collection process more convenient and targeted. BRIEF DESCRIPTION OF DRAWINGS

[0031] Figure 1 is the front view of the wettable powder production line.

[0032] Figure 2 is the top view of the wettable powder production line.

[0033] Figure 3 is the schematic diagram of the feeding hopper.

[0034] In the figure:

[0035] 1. Rough mixing tank 2. Mixing tank 3. Jet mill

[0036] 4. Dust collector I 5. Dust collector II 6. Cyclone separator

[0037] 7. Pipe I 8. Dust hood 9. Feeding hopper 10. duct II 11. branch duct I 12. branch duct II

[0038] 13. induced draft fan II 14. induced draft fan I 15. duct IV

[0039] 16. support platform 17. air shaft DETAILED DESCRIPTION

[0040] The wettable powder production line of the embodiment includes a support platform 16, and the support platform 16 is provided with a wettable powder processing module and a dust collection module;

[0041] The wettable powder processing module includes one rough mixing tank 1, two mixing tanks 2, one jet mill 3, two dust collectors II 5, and two cyclone separators 6. 3 The rough mixing tank 1 has an internal storage volume of 2m 3 ; the two dust collectors II 5 are both DMC pulse bag dust collectors, and the total filtration area is 21m 2 .

[0042] The two dust collectors II 5 and the two cyclone separators 6 are respectively connected in series at the top of the two mixing tanks 2, and then the discharge outlets of the two dust collectors II 5 and the two cyclone separators 6 are respectively communicated with the feeding inlets of the two mixing tanks 2. The two mixing tanks 2 are arranged side by side, the rough mixing tank 1 is arranged on one side of the two mixing tanks 2 and located in the middle of the two mixing tanks 2, which is convenient for feeding the two mixing tanks 2 and saves the pipeline. The discharge outlet at the bottom of the rough mixing tank 1 is communicated with the feeding inlet of the jet mill 3, the discharge outlet of the jet mill 3 is communicated with the feeding inlets of the two cyclone separators 6 through a “Y”-shaped pipeline, the air suction inlets at the top of each cyclone separator 6 are respectively communicated with one dust collector II 5, and the air inlets of the two dust collectors II 5 are respectively communicated with the air suction inlets of the induced draft fan through the parallel connection of the induced draft pipes. The rough mixing tank 1 and the two mixing tanks 2 are respectively provided with stirring shafts, and the stirring shafts are respectively provided with spiral knife-shaped stirring blades for stirring and further crushing the materials. The outer walls of the rough mixing tank 1 and the two mixing tanks 2 are respectively provided with vibrating screens for knocking the outer walls of the rough mixing tank 1 and the two mixing tanks 2;

[0043] Further, the above-mentioned pipelines are respectively provided with corresponding valves, and the types of the valves are marked in Figure 1 .

[0044] The dust collection module includes a dust collector I 4, a dust collecting hood 8, and a plurality of pipelines. The dust collector I 4 is a DMC pulse bag dust collector, and the total filtration area is 10m 2The dust collector 4 is arranged side by side with the rough mixing tank 1, and the center line of the two mixing tanks 2 is parallel to the center line of the dust collector 4 and the rough mixing tank 1. The top of the rough mixing tank 1 is provided with an upper hopper 9. The top of the upper hopper 9 is open. The upper hopper 9 is provided with a double-door type upper feeding port located on the side of the upper hopper 9. The bottom of a dust hood 8 covers the top of the upper hopper 9 and seals the top of the upper hopper 9. The top end of the dust hood 8 is communicated with the air inlet of the dust collector 4 through a pipeline 7. One end of a pipeline 10 is communicated with the air inlet of the dust collector 4. The other end of the pipeline 10 is arranged at the side of the discharge port of each of the two mixing tanks 2 by 10 cm. The air inlet of the dust collector 4 is communicated with the air inlet of an induced draft fan 14 through an air duct. After air is induced by the induced draft fan 14, a negative pressure is generated in the dust collector 4 and the pipeline 10 to adsorb dust at the side of the discharge port of each of the two mixing tanks 2. One end of a branch pipeline 117 is communicated with the pipeline 10. The other end of the branch pipeline 117 is arranged at the manhole of the rough mixing tank 1 by 10 cm. One end of a branch pipeline 210 is communicated with the air inlet of the dust collector 4. The other end of the branch pipeline 210 is communicated with the air inlet of the rough mixing tank 1. The dust hood 8 is arranged at the air outlet of the pipeline 10. The manhole of the rough mixing tank 1 is used for inspection and maintenance of the interior of the rough mixing tank 1. The manhole of the rough mixing tank 1 is located on the top surface of the rough mixing tank 1. The manhole and the upper hopper 9 are located on the two sides of the rough mixing tank 1. The manhole of each of the two mixing tanks 2 is provided with a pipeline 15. The other end of the pipeline 15 is communicated with the pipeline 10 and the air inlet of the dust collector 4.

[0045] The support platform 16 includes upper and lower layers. A ladder is arranged between the upper and lower layers. The two mixing tanks 2 and the rough mixing tank 1 penetrate the support platform 16. The feeding port of each of the two mixing tanks 2, the two dust collectors 5 and the two cyclone separators 6 are located on the upper layer of the support platform 16. The discharge port of each of the two mixing tanks 2 is located on the lower layer of the support platform 16. The upper hopper 9 in the rough mixing tank 1 is located on the upper layer of the support platform 16. The discharge port in the rough mixing tank 1 is located on the lower layer of the support platform 16. The dust collector 4 is located on the upper layer of the support platform 16.

[0046] Further, the induced draft fan 13 is a high-pressure induced draft fan. The induced draft fan 14 is a medium-pressure induced draft fan. The air outlets of the induced draft fan 13 and the induced draft fan 14 are communicated with an air well 17 through pipelines. The height of the air well 17 is 20 m.

[0047] The production process of the wettable powder is as follows:

[0048] The door on the side of the upper hopper 9 is opened, the door is a double-door type, the opening is large, the feeding speed is fast, the door is similar to the door of a double-door refrigerator, then a plurality of materials are poured into the upper hopper 9 and enter the airflow pulverizer 3 at the lower end of the coarse mixing tank 1 after mixing in the coarse mixing tank 1, and after being pulverized, enter two cyclone separators 6 under the condition of negative pressure suction of the high-pressure induced draft fan through the "Y"-shaped pipeline, and due to the size and storage volume of the one coarse mixing tank 1 and the two mixing tanks 2, the discharge of the airflow pulverizer 3 is divided, so that a small amount of material can be dried better under the condition of negative pressure suction of the high-pressure induced draft fan, and after being separated by the two cyclone separators 6, further crushing and mixing are carried out in the two mixing tanks 2, due to the fact that the two mixing tanks 2 are provided with stirrers and the mixing tanks 2 are provided with oscillators outside, the mixing and crushing conditions are good, the drying condition also meets the requirements, and subsidies are provided on the inner wall of the mixing tank 2, and the improved point guarantees the product quality. In the above process, one end of the branch pipeline II 1210 is communicated with the air suction port of the dust collector I 4, and the other end is communicated with the air inlet of the coarse mixing tank 1 for providing air for the mixing process of the coarse mixing tank 1, further drying the material, and guaranteeing the product quality.

[0049] In the above process, the dust hood 8 is arranged at the top end of the upper hopper 9, negative pressure is generated through the dust hood 8 and the dust collector I 4, and dust volatilized in the feeding process is collected, so that the dust volatilization amount in the workshop is reduced, the environment in the workshop is maintained, and the physical and mental health of the workers is guaranteed. The dust volatilized in the discharging process of the two mixing tanks 2 is absorbed through the two pipelines II 10, and the environmental protection of the workshop is further guaranteed. The pipelines are arranged at the three manholes to collect dust, and the environment in the workshop is further guaranteed. At present, the workshop has reached the environmental protection requirements.

[0050] In the above process, one high-pressure induced draft fan provides negative pressure for the two dust collectors II 5, and the two dust collectors II 5 are communicated with the two cyclone separators 6, so that the high-pressure induced draft fan also provides negative pressure for the two cyclone separators 6, and energy consumption is saved. The induced draft fan II 13 for production is a high-pressure induced draft fan, and the induced draft fan I 14 for collecting dust is a medium-pressure induced draft fan, so that the arrangement is reasonable, energy consumption is saved, and the production requirements are met. Since the air outlets of the induced draft fan II 13 and the induced draft fan I 14 are communicated with one air well 17 through the pipelines, the cost is saved, and the standard of environmental protection of waste gas emission is met.

[0051] The support platform 16 includes upper and lower layers, which is convenient for workers to feed and overhaul on the upper layer, and makes the dust collection process more convenient and targeted.

[0052] The above describes one embodiment of the present application in detail, but the content described is only a preferred embodiment of the present application, and cannot be considered as limiting the implementation range of the present application. Any equivalent changes and improvements made within the scope of the present application should still belong to the patent coverage range of the present application.

Claims

1. A wettable powder production line characterized by: The wettable powder processing module and the dust collecting module are included. The wettable powder processing module includes one rough mixing tank, two mixing tanks, one jet mill, two dust collectors II and two cyclones. The dust collecting module includes a dust collector I, a dust collecting hood and several pipes, the dust collector I is arranged side by side with the rough mixing tank, and the center line of the two mixing tanks is parallel to the center line of the dust collector I and the rough mixing tank, the top of the rough mixing tank is provided with a feeding hopper, the top of the feeding hopper is open, the feeding opening of the feeding hopper is located on the side of the feeding hopper and is double-door type, the bottom of the dust collecting hood covers the top of the feeding hopper and seals the top of the feeding hopper, the top end of the dust collecting hood is communicated with the air inlet of the dust collector I through a pipe I, one end of a pipe II is communicated with the air inlet of the dust collector I, and the other end of the pipe II is arranged in the side of the discharge opening of the two mixing tanks within 15 cm, and the air inlet of the dust collector I is communicated with the air inlet of an induced draft fan I through an air duct.

2. A wettable powder production line according to claim 1, characterised in that: The two dust collectors II and the two cyclones are connected in series at the top of the two mixing tanks, the discharge outlets of the two dust collectors II and the two cyclones are respectively communicated with the feeding inlets of the two mixing tanks, the two mixing tanks are arranged side by side, the rough mixing tank is arranged on one side of the two mixing tanks and located in the middle of the two mixing tanks, the discharge outlet at the bottom of the rough mixing tank is communicated with the feeding inlet of the jet mill, the discharge outlet of the jet mill is communicated with the feeding inlets of the two cyclones through a "Y" shaped pipe, the air inlets at the top of each cyclone are communicated with one dust collector II, and the air inlets of the two dust collectors II are communicated with the air inlet of an induced draft fan through air ducts in parallel.

3. A wettable powder production line according to claim 2, characterised in that: The internal storage volume of each of the two mixing tanks is 3m 3 ; the internal storage volume of the coarse mixing tank is 2m 3 ; and each of the two dust collectors II is a DMC pulse bag dust collector with a total filter area of 21m 2 .

4. A wettable powder line according to any one of claims 1 to 3, characterized in that: The dust collector I is a DMC pulse bag dust collector, and the total filtering area is 10 m 2 .

5. A wettable powder production line according to claim 4, characterised in that: One end of a branch pipe I is communicated with the pipe II, and the other end is arranged in the manhole of the rough mixing tank within 15 cm.

6. A wettable powder line as claimed in claim 1 or 2 or 3 or 5, wherein: One end of a branch pipe II is communicated with the air inlet of the dust collector I, and the other end is communicated with the air inlet of the rough mixing tank.

7. A wettable powder production line according to claim 6, characterised in that: The manhole of the rough mixing tank is located on the top surface of the rough mixing tank, and the manhole and the feeding hopper are respectively located on the two sides of the rough mixing tank.

8. A wettable powder line according to claim 4, characterized in that: The induced draft fan II is a high-pressure induced draft fan, the induced draft fan I is a medium-pressure induced draft fan, the air outlets of the induced draft fan II and the induced draft fan I are communicated with an air shaft through pipes, and the height of the air shaft is greater than or equal to 20 m.

9. A wettable powder production line according to claim 7 or 8, characterised in that: The manhole of the two mixing tanks is provided with a pipe IV, and the other end of the pipe IV is communicated with the pipe II and the air inlet of the dust collector I in parallel. A dust collecting hood is arranged at the air outlet of the pipe II.

10. A wettable powder production line according to claim 9, characterised in that: The wettable powder production line includes a support platform, the support platform includes upper and lower layers, a ladder is arranged between the upper and lower layers, two mixing tanks and one rough mixing tank penetrate the support platform, the feeding inlets of the two mixing tanks, the two dust collectors II and the two cyclones are located on the upper layer of the support platform, the discharge outlets of the two mixing tanks are located on the lower layer of the support platform, the feeding hopper in the rough mixing tank is located on the upper layer of the support platform, the discharge outlet in the rough mixing tank is located on the lower layer of the support platform, and the dust collector I is located on the upper layer of the support platform. The rough mixing tank and the two mixing tanks are provided with stirring shafts, and the stirring shafts are provided with helical blade stirring leaves for stirring and further crushing the materials. The rough mixing tank and the two mixing tanks are provided with vibrating screens on the outer walls.

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