Blended fertilizer production system with quantitative and continuous feeding function
By designing a blended fertilizer production system with a quantitative continuous feeding function, the problem of uneven mixing between microbial agents and blended fertilizers was solved, and the effective spraying and adsorption of liquid agents was achieved, thereby improving the uniformity and effectiveness of the product.
Patent Information
- Application Number
- CN202511255878.4
- Authority / Receiving Office
- CN · China
- Patent Type
- Applications(China)
- Current Assignee / Owner
- Filing Date
- 2025-09-04
- Publication Date
- 2025-11-28
- Estimated Expiration
- Not applicable · inactive patent
AI Technical Summary
In the existing technology, when microbial agents are used in combination with blended fertilizers, they cannot be fully mixed with the base liquid in the bacterial solution dilution mixing tank, resulting in poor product uniformity. Furthermore, the liquid microbial agents cannot be effectively sprayed and adsorbed onto the blended fertilizer granules.
A blended fertilizer production system with quantitative continuous feeding function was designed, including a bacterial solution dilution and mixing tank, a mixer and a spray gun system. The system ensures that the bacterial solution and the base liquid are fully mixed through a meandering path and multiple sets of mixers, and uses a spray gun to spray and adsorb the liquid microbial agent onto the blended fertilizer particles.
This approach achieves effective combination of microbial agents and blended fertilizers, improving product uniformity and efficacy, and fully leveraging the advantages of both.
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Figure CN121016576A_ABST
Abstract
Description
Technical Field
[0001] This invention relates to a blended fertilizer production system with a quantitative continuous feeding function, belonging to the field of blended fertilizer production technology. Background Technology
[0002] Blended fertilizers, also known as formulated fertilizers or BB fertilizers, are made by mixing two or more single-element or compound fertilizers with similar particle sizes in a certain proportion using simple mechanical methods. They are mixtures of various raw materials. The advantages of blended fertilizers include simple production processes, flexible operation, lower production costs, and nutrient ratios adapted to micro-regional regulation or the specific needs of crops in specific fields. Compared to compound fertilizers, blended fertilizers have unique advantages in production, storage, and application.
[0003] Microbial inoculants are preparations containing a large number of beneficial microorganisms that can improve soil structure, enhance soil fertility, and inhibit the growth of pathogens. Blended fertilizers, on the other hand, are compound fertilizers made by mixing various single-element fertilizers according to crop needs; they provide comprehensive nutrients and are easily absorbed by crops.
[0004] Using microbial inoculants and blended fertilizers together can fully leverage the advantages of both. Microbial inoculants can activate the soil and improve the availability of nutrients, while blended fertilizers provide crops with all the nutrients they need. Using them together can meet the nutrient requirements of crops and improve the soil environment, which is beneficial for long-term crop growth. However, current technology is not comprehensive and has the following drawbacks: the microbial solution to be diluted cannot be fully mixed with the base solution in the dilution mixing tank, resulting in poor product uniformity; and currently, it is impossible to spray and adsorb the liquid microbial inoculant onto the blended fertilizer granules, making it unsuitable for compounding microbial inoculants and blended fertilizers.
[0005] To solve one of the above problems, there is an urgent need for a blended fertilizer production system with a quantitative and continuous feeding function. Summary of the Invention
[0006] Based on the shortcomings of the prior art, the technical problem to be solved by the present invention is: how to spray the diluted bacterial solution onto the blended fertilizer particles on the blended fertilizer conveyor belt through the mixed liquid outlet pipe, pipeline mixer, and spray gun, so that the liquid microbial agent can be sprayed and adsorbed onto the blended fertilizer particles for compounding of microbial agent and blended fertilizer. To this end, a blended fertilizer production system with quantitative continuous feeding function is provided.
[0007] The blended fertilizer production system with quantitative continuous feeding function of the present invention includes a bacterial solution dilution and mixing tank. A first bent pipe is connected to the inlet at the bottom of the bacterial solution dilution and mixing tank, and a second bent pipe is connected to the outlet at the top of the bacterial solution dilution and mixing tank. The system is characterized in that: the other end of the first bent pipe is connected to a base liquid inlet pipe, the other end of the second bent pipe is connected to a pipeline mixer, and the other end of the pipeline mixer is connected to a mixed solution outlet pipe. Multiple sets of internal partitions are spaced apart inside the bacterial solution dilution and mixing tank, dividing the inner cavity of the tank into multiple mixing chambers. Each mixing chamber is equipped with two sets of stirring mixers. A bacterial agent supply system is connected to the supply port of the stirring mixer. A spray gun is connected after the mixed solution outlet pipe. The bacterial agent spraying system is located above the conveying path of the blended fertilizer conveyor belt, using the spray gun to spray and adsorb liquid microbial agents onto the blended fertilizer particles. The mixed solution outlet pipe has an electrically controlled regulating valve to control the flow rate.
[0008] This invention utilizes a base liquid inlet pipe to inject base liquid into a bacterial solution dilution and mixing tank, and injects the bacterial solution to be diluted into the tank through a first and second agitator. The solutions are thoroughly mixed within the tank. The diluted bacterial solution is then sprayed onto the blended fertilizer granules on the blended fertilizer conveyor belt via a mixing liquid outlet pipe, a pipeline mixer, and a spray gun. This process effectively adsorbs the liquid microbial agent onto the blended fertilizer granules. This invention is used to prepare a microbial agent + blended fertilizer mixture by compounding microbial agents and blended fertilizers. Using the microbial agent and blended fertilizer together fully leverages the advantages of both.
[0009] In any of the above embodiments, it is preferred that the bacterial solution dilution mixing tank is a rectangular box, including a bottom plate and a top plate, with four sets of side plates between the bottom plate and the top plate. The top plate, bottom plate and the four sets of side plates together form the bacterial solution dilution mixing tank. An inlet is provided on the bottom plate and an outlet is provided on the top plate.
[0010] In any of the above embodiments, it is preferred that the number of inner partitions is even, the second bend is connected to the mixing chamber at the top of the bacterial solution dilution mixing tank, and the first bend is connected to the mixing chamber at the bottom of the bacterial solution dilution mixing tank.
[0011] In any of the above embodiments, it is preferred that the inner partition is provided in four sets, namely, a first partition, a second partition, a third partition, and a fourth partition arranged sequentially from top to bottom, dividing the inner cavity of the bacterial solution dilution mixing tank into a top layer mixing cavity, a second layer mixing cavity, a third layer mixing cavity, a fourth layer mixing cavity, and a base layer mixing cavity from top to bottom. Two sets of stirring mixers are respectively provided in the top layer mixing cavity, the second layer mixing cavity, the third layer mixing cavity, the fourth layer mixing cavity, and the base layer mixing cavity. The ends of the first partition, the second partition, the third partition, and the fourth partition are respectively provided with liquid outlet A, liquid outlet B, liquid outlet C, and liquid outlet D. Adjacent liquid outlets are staggered, and liquid outlet A is staggered with the liquid outlet, and liquid outlet D is staggered with the liquid inlet.
[0012] The bacterial solution dilution mixing tank uses a circuitous path, which extends the flow distance and allows the bacterial solution to be diluted to be fully mixed with the base solution in the tank.
[0013] In any of the above embodiments, preferably, the two sets of mixers in the bottom mixing chamber are the first and second mixers; the two sets of mixers in the fourth mixing chamber are the third and fourth mixers; the two sets of mixers in the third mixing chamber are the fifth and sixth mixers; the two sets of mixers in the second mixing chamber are the seventh and eighth mixers; and the two sets of mixers in the top mixing chamber are the ninth and tenth mixers. The bacterial solution dilution mixing tank employs a circuitous path. This circuitous path, by extending the flow distance and configuring multiple sets of mixers, ensures that the bacterial solution to be diluted is thoroughly mixed with the base solution within the bacterial solution dilution mixing tank.
[0014] Preferably, in any of the above embodiments, the first stirring mixer includes a first rotating tube, a second rotating tube, and a third rotating tube arranged at intervals. One end of the first rotating tube is inserted into the bacterial solution dilution mixing tank and maintains a rotational seal with the bacterial solution dilution mixing tank. The inner end of the first rotating tube is sealed. The outer end of the first rotating tube is provided with a first gear and a first rotating joint, and the first rotating joint communicates with the inner cavity of the first rotating tube. One end of the second rotating tube is inserted into the bacterial solution dilution mixing tank and maintains a rotational seal with the bacterial solution dilution mixing tank. The inner end of the second rotating tube is sealed. The outer end of the second rotating tube is provided with a second gear and a second rotating joint, and the second rotating joint communicates with the inner cavity of the second rotating tube. One end of the third rotating tube is inserted into the bacterial solution dilution mixing tank and maintains a rotational seal with the bacterial solution dilution mixing tank. The inner end of the third rotating tube is sealed. The third rotating tube is equipped with a third gear and a third rotating joint at its outer end. The third rotating joint is connected to the inner cavity of the third rotating tube. A drive cylinder A is fixed on the outer wall of the bacterial solution dilution mixing tank. The telescopic end of the drive cylinder A is connected to a rack A via a connecting rod A. The bottom of the rack A has a slide rail A. A slider A that slides in cooperation with the slide rail A is fixed on the outer wall of the bacterial solution dilution mixing tank. The rack A meshes with the first gear, the second gear, and the third gear. By controlling the telescopic extension of the drive cylinder A, the rack A is driven to reciprocate along its length. Under the meshing of the rack A with the first gear, the second gear, and the third gear, the first rotating tube, the second rotating tube, and the third rotating tube reciprocate. The first rotating tube, the second rotating tube, and the third rotating tube inside the bacterial solution dilution mixing tank are all equipped with stirring blades A and spray holes A.
[0015] By controlling the extension and retraction of the drive cylinder A, the rack A is driven to reciprocate along its length. Under the meshing of the rack A with the first gear, the second gear, and the third gear, the first rotating tube, the second rotating tube, and the third rotating tube reciprocate. The first rotating tube, the second rotating tube, and the third rotating tube, which are located in the bacterial solution dilution mixing tank, are all equipped with stirring blades A and spray holes A, which further improves the mixing effect of the bacterial solution to be diluted with the base liquid in the bacterial solution dilution mixing tank.
[0016] Preferably, in any of the above embodiments, the second stirring mixer includes a fourth rotating tube and a fifth rotating tube spaced apart. One end of the fourth rotating tube is inserted into the bacterial solution dilution mixing tank and maintains a rotational seal with the tank. The inner end of the fourth rotating tube is sealed. The outer end of the fourth rotating tube is provided with a fourth gear and a fourth rotating joint, which communicates with the inner cavity of the fourth rotating tube. One end of the fifth rotating tube is inserted into the bacterial solution dilution mixing tank and maintains a rotational seal with the tank. The inner end of the fifth rotating tube is sealed. The outer end of the fifth rotating tube is provided with a fifth gear and a fifth rotating joint, which communicates with the inner cavity of the fifth rotating tube. The inner cavities of the tubes are interconnected. A drive cylinder B is fixed on the outer wall of the bacterial solution dilution mixing tank. The telescopic end of the drive cylinder B is connected to the rack B via a connecting rod B. The bottom of the rack B has a slide rail B. A slider B that slides in cooperation with the slide rail B is fixed on the outer wall of the bacterial solution dilution mixing tank. The rack B meshes with the fourth gear and the fifth gear. By controlling the extension and retraction of the drive cylinder B, the rack B is driven to reciprocate along its length. Under the meshing of the rack B with the fifth gear and the fourth rotary joint, the fourth and fifth rotary tubes are rotated back and forth. The fourth and fifth rotary tubes inside the bacterial solution dilution mixing tank are each equipped with stirring blades B and spray holes B.
[0017] The fourth and fifth rotating tubes are arranged alternately with the first, second, and third rotating tubes.
[0018] In any of the above embodiments, it is preferred that the bacterial agent supply system connected to the first agitator includes a first branch pipe, a second branch pipe, and a third branch pipe connected to the liquid supply ports on the first rotary joint, the second rotary joint, and the third rotary joint. The first branch pipe, the second branch pipe, and the third branch pipe are connected to the main pipe, the other end of the main pipe extends to the bacterial liquid storage tank, and a bacterial liquid supply pump is installed on the main pipe.
[0019] In any of the above embodiments, it is preferred that the liquid supply pump is a diaphragm pump and the bacterial liquid supply pump is a peristaltic pump, the flow rate of which can be adjusted as needed.
[0020] In any of the above embodiments, it is preferred that both inlets of the pipeline mixer are connected to the second bend, the outlet of the pipeline mixer is connected to the liquid outlet pipe, and the pipeline mixer has twisted fixed spiral blades inside.
[0021] Compared with the prior art, the present invention has the following beneficial effects: The blended fertilizer production system with quantitative continuous feeding function described in this invention can inject basic liquid into the bacterial solution dilution and mixing tank through the basic liquid inlet pipe, and inject the bacterial solution to be diluted into the bacterial solution dilution and mixing tank through the first and second agitators. The bacterial solution can be fully mixed in the bacterial solution dilution and mixing tank. The diluted bacterial solution is sprayed onto the blended fertilizer particles on the blended fertilizer conveyor belt through the mixed liquid outlet pipe, pipeline mixer, and spray gun. This allows the liquid microbial agent to be sprayed and adsorbed onto the blended fertilizer particles. This invention is used to prepare microbial agent + blended fertilizer by compounding microbial agent and blended fertilizer. Using microbial agent and blended fertilizer together can give full play to the advantages of both.
[0022] The blended fertilizer production system with quantitative continuous feeding function described in this invention adopts a circuitous path in the bacterial solution dilution mixing tank. The circuitous path extends the flow distance and is equipped with multiple sets of agitators, so that the bacterial solution to be diluted can be fully mixed with the base liquid in the bacterial solution dilution mixing tank.
[0023] The blended fertilizer production system with quantitative continuous feeding function described in this invention controls the extension and retraction of the drive cylinder A to drive the rack A to reciprocate along its length. Under the meshing of the rack A with the first gear, the second gear, and the third gear, the first rotating tube, the second rotating tube, and the third rotating tube reciprocate. The first rotating tube, the second rotating tube, and the third rotating tube, which are located in the bacterial solution dilution mixing tank, are all equipped with stirring blades A and spray holes A, which further improves the mixing effect of the bacterial solution to be diluted with the base liquid in the bacterial solution dilution mixing tank. Attached Figure Description
[0024] To more clearly illustrate the specific embodiments of the present invention or the technical solutions in the prior art, the accompanying drawings used in the description of the specific embodiments or the prior art will be briefly introduced below. In all the drawings, similar elements or parts are generally identified by similar reference numerals. In the drawings, the elements or parts are not necessarily drawn to scale.
[0025] Figure 1 This is a schematic diagram of the structure of the present invention; Figure 2 The interior of the structural schematic diagram of the present invention Figure 1 ; Figure 3 This is an installation diagram of the first agitator / mixer; Figure 4 This is an installation diagram of the second agitator / mixer; Figure 5 The interior of the structural schematic diagram of the present invention Figure 2 .
[0026] In the diagram: 1. Basic liquid inlet pipe; 2. Bacterial liquid dilution mixing tank; 3. Mixed liquid outlet pipe; 4. Pipe mixer; 5. Inner partition; 6. First stirring mixer; 6.1. First rotating tube; 6.2. Second rotating tube; 6.3. Third rotating tube; 6.4. First gear; 6.5. Second gear; 6.6. Third gear; 6.7. First rotary joint; 6.8. Second rotary joint; 6.9. Third rotary joint; 6.10. Rack A; 6.11. Drive cylinder A; 6.12. Slide rail A; 6.13. Slider A; 6.14. Stirring blade A; 7. Second stirring mixer; 7.1. Fourth rotating tube; 7.2. Fifth rotating tube; 7.3. Fourth gear; 7.4. Fifth gear; 7.5. Fourth rotary joint; 7.6. Fifth rotary joint; 7.7. Rack B; 7.8. Drive cylinder B; 7.9. Slide rail B; 7.10. Slider B; 7.11. Stirring blade B 8. First bend pipe; 9. Second bend pipe; 10. Liquid outlet A; 11. Liquid outlet B; 12. Liquid outlet C; 13. Liquid outlet D; 14. Liquid supply pump; 15. Spray gun; 16. Blended fertilizer conveyor belt; 17. Bacterial liquid supply pump; 18. Electrically controlled regulating valve. Detailed Implementation
[0027] The present invention will be further described below with reference to the accompanying drawings. The present invention will be further illustrated by specific embodiments, but these are not intended to limit the present invention. Any modifications, equivalent substitutions, improvements, etc., made within the spirit and principles of the present invention should be included within the protection scope of the present invention.
[0028] Example 1, such as Figure 1-2 As shown, the compound fertilizer production system with quantitative continuous feeding function includes a bacterial solution dilution and mixing tank 2. A first bent pipe 8 is connected to the inlet at the bottom of the bacterial solution dilution and mixing tank 2, and a second bent pipe 9 is connected to the outlet at the top of the bacterial solution dilution and mixing tank 2. The other end of the first bent pipe 8 is connected to a base liquid inlet pipe 1, and the other end of the second bent pipe 9 is connected to a pipeline mixer 4. The other end of the pipeline mixer 4 is connected to a mixed liquid outlet pipe 3. The bacterial solution dilution and mixing tank 2 is equipped with... Multiple sets of internal partitions 5 are provided, which divide the inner cavity of the bacterial solution dilution and mixing tank 2 into multiple sets of mixing chambers. Each set of mixing chambers is equipped with two sets of agitators. The liquid supply port of the agitator is connected to a bacterial agent supply system. The liquid outlet pipe 3 is connected to a spray gun 15. The bacterial agent spraying system is located above the conveying path of the blended fertilizer conveyor belt 16. The spray gun is used to spray and adsorb the liquid microbial agent onto the blended fertilizer particles. The liquid outlet pipe 3 is equipped with an electrically controlled regulating valve 18 to control the flow rate.
[0029] This invention utilizes a base liquid inlet pipe 1 to inject base liquid into a bacterial solution dilution mixing tank 2, and injects the bacterial solution to be diluted into the bacterial solution dilution mixing tank 2 through a first mixer 6 and a second mixer 7. The bacterial solution is fully mixed in the bacterial solution dilution mixing tank 2. The diluted bacterial solution is then sprayed onto the blended fertilizer particles on the blended fertilizer conveyor belt 16 through a mixing liquid outlet pipe 3, a pipeline mixer 4, and a spray gun 15. This allows the liquid microbial agent to be sprayed and adsorbed onto the blended fertilizer particles. This invention is used to prepare microbial agent + blended fertilizer by compounding microbial agent and blended fertilizer. Using microbial agent and blended fertilizer together can give full play to the advantages of both.
[0030] Example 2, as Figure 1-2 As shown, the compound fertilizer production system with quantitative continuous feeding function includes a bacterial solution dilution and mixing tank 2. A first bent pipe 8 is connected to the inlet at the bottom of the bacterial solution dilution and mixing tank 2, and a second bent pipe 9 is connected to the outlet at the top of the bacterial solution dilution and mixing tank 2. The other end of the first bent pipe 8 is connected to a base liquid inlet pipe 1, and the other end of the second bent pipe 9 is connected to a pipeline mixer 4. The other end of the pipeline mixer 4 is connected to a mixed liquid outlet pipe 3. The bacterial solution dilution and mixing tank 2 is equipped with... Multiple sets of internal partitions 5 are provided, which divide the inner cavity of the bacterial solution dilution and mixing tank 2 into multiple sets of mixing chambers. Each set of mixing chambers is equipped with two sets of agitators. The liquid supply port of the agitator is connected to a bacterial agent supply system. The liquid outlet pipe 3 is connected to a spray gun 15. The bacterial agent spraying system is located above the conveying path of the blended fertilizer conveyor belt 16. The spray gun is used to spray and adsorb the liquid microbial agent onto the blended fertilizer particles. The liquid outlet pipe 3 is equipped with an electrically controlled regulating valve 18 to control the flow rate.
[0031] Furthermore, the bacterial solution dilution mixing tank 2 is a rectangular box, including a bottom plate and a top plate. There are four sets of side plates between the bottom plate and the top plate. The top plate, bottom plate and the four sets of side plates together form the bacterial solution dilution mixing tank 2. The bottom plate is provided with a liquid inlet and the top plate is provided with a liquid outlet.
[0032] Furthermore, the number of inner partitions 5 is even, the second bent pipe 9 is connected to the mixing chamber at the top of the bacterial solution dilution mixing tank 2, and the first bent pipe 8 is connected to the mixing chamber at the bottom of the bacterial solution dilution mixing tank 2.
[0033] Furthermore, the inner partition 5 is provided with four sets, namely, a first partition, a second partition, a third partition, and a fourth partition arranged sequentially from top to bottom, dividing the inner cavity of the bacterial solution dilution mixing tank 2 into a top layer mixing chamber, a second layer mixing chamber, a third layer mixing chamber, a fourth layer mixing chamber, and a base layer mixing chamber from top to bottom. Two sets of stirring mixers are respectively installed in the top layer mixing chamber, the second layer mixing chamber, the third layer mixing chamber, the fourth layer mixing chamber, and the base layer mixing chamber. The ends of the first partition, the second partition, the third partition, and the fourth partition are respectively provided with liquid outlets A10, B11, C12, and D13. Adjacent liquid outlets are staggered, and liquid outlet A10 is staggered with the outlet, and liquid outlet D13 is staggered with the inlet. The bacterial solution dilution mixing tank 2 adopts a circuitous path. The circuitous path, by extending the flow distance, allows the bacterial solution to be diluted to be fully mixed with the base solution in the bacterial solution dilution mixing tank 2.
[0034] Furthermore, the two sets of mixers in the bottom mixing chamber are the first mixer 6 and the second mixer 7; the two sets of mixers in the fourth mixing chamber are the third mixer and the fourth mixer; the two sets of mixers in the third mixing chamber are the fifth mixer and the sixth mixer; the two sets of mixers in the second mixing chamber are the seventh mixer and the eighth mixer; and the two sets of mixers in the top mixing chamber are the ninth mixer and the tenth mixer. The bacterial solution dilution mixing tank 2 employs a circuitous path. This circuitous path, by extending the flow distance and incorporating multiple sets of mixers, ensures that the bacterial solution to be diluted is thoroughly mixed with the base solution within the bacterial solution dilution mixing tank 2.
[0035] Reference Figure 3Furthermore, the first stirring mixer 6 includes a first rotating tube 6.1, a second rotating tube 6.2, and a third rotating tube 6.3 arranged at intervals. One end of the first rotating tube 6.1 is inserted into the bacterial solution dilution mixing tank 2 and maintains a rotational seal with the bacterial solution dilution mixing tank 2. The inner end of the first rotating tube 6.1 is sealed. The outer end of the first rotating tube 6.1 is provided with a first gear 6.4 and a first rotating joint 6.7. The first rotating joint 6.7 communicates with the inner cavity of the first rotating tube 6.1. One end of the second rotating tube 6.2 is inserted into... The third rotating tube 6.2 is inserted into the bacterial solution dilution mixing tank 2 and maintains a rotary seal with the bacterial solution dilution mixing tank 2. The inner end of the second rotating tube 6.2 is sealed, and the outer end of the second rotating tube 6.2 is provided with a second gear 6.5 and a second rotating joint 6.8. The second rotating joint 6.8 is connected to the inner cavity of the second rotating tube 6.2. One end of the third rotating tube 6.3 is inserted into the bacterial solution dilution mixing tank 2 and maintains a rotary seal with the bacterial solution dilution mixing tank 2. The inner end of the third rotating tube 6.3 is sealed, and the outer end of the third rotating tube 6.3 is provided with a third gear 6.5. 6 and the third rotary joint 6.9, the third rotary joint 6.9 being connected to the inner cavity of the third rotary tube 6.3, a drive cylinder A6.11 being fixed on the outer wall of the bacterial solution dilution mixing tank 2, the telescopic end of the drive cylinder A6.11 being connected to the rack A6.10 via connecting rod A, the bottom of the rack A6.10 having a slide rail A6.12, a slider A6.13 being fixed on the outer wall of the bacterial solution dilution mixing tank 2 and sliding in cooperation with the slide rail A6.12, the rack A6.10 being connected to the first gear 6.4, the second gear 6.5, The third gear 6.6 meshes with the rack A6.10, which is driven to reciprocate along its length by controlling the extension and retraction of the drive cylinder A6.11. Under the meshing of the rack A6.10 with the first gear 6.4, the second gear 6.5, and the third gear 6.6, the first rotating tube 6.1, the second rotating tube 6.2, and the third rotating tube 6.3 reciprocate. The first rotating tube 6.1, the second rotating tube 6.2, and the third rotating tube 6.3, which are located in the bacterial solution dilution mixing tank 2, are all equipped with stirring blades A6.14 and spray holes A6.15.
[0036] By controlling the extension and retraction of the drive cylinder A6.11, the rack A6.10 is driven to reciprocate along its length. Under the meshing of the rack A6.10 with the first gear 6.4, the second gear 6.5, and the third gear 6.6, the first rotating tube 6.1, the second rotating tube 6.2, and the third rotating tube 6.3 reciprocate. The first rotating tube 6.1, the second rotating tube 6.2, and the third rotating tube 6.3, which are located in the bacterial solution dilution mixing tank 2, are all equipped with stirring blades A6.14 and spray holes A6.15, which further improves the mixing effect of the bacterial solution to be diluted with the base liquid in the bacterial solution dilution mixing tank 2.
[0037] Furthermore, referring to Figure 4The second stirring mixer 7 includes a fourth rotating tube 7.1 and a fifth rotating tube 7.2 spaced apart. One end of the fourth rotating tube 7.1 is inserted into the bacterial solution dilution mixing tank 2 and maintains a rotational seal with the bacterial solution dilution mixing tank 2. The inner end of the fourth rotating tube 7.1 is sealed. The outer end of the fourth rotating tube 7.1 is provided with a fourth gear 7.3 and a fourth rotating connector 7.5. The fourth rotating connector 7.5 is connected to the inner cavity of the fourth rotating tube 7.1. One end of the fifth rotating tube 7.2 is inserted into the bacterial solution dilution mixing tank 2 and maintains a rotational seal with the bacterial solution dilution mixing tank 2. The inner end of the fifth rotating tube 7.2 is sealed. The outer end of the fifth rotating tube 7.2 is provided with a fifth gear 7.4 and a fifth rotating connector 7.6. The fifth rotating connector 7.6 is connected to the inner cavity of the fifth rotating tube 7.2. The bacterial solution is diluted... A drive cylinder B7.8 is fixed on the outer wall of the bacterial solution dilution mixing tank 2. The telescopic end of the drive cylinder B7.8 is connected to a rack B7.7 via a connecting rod B. The bottom of the rack B7.7 has a slide rail B7.9. A slider B7.10 that slides in cooperation with the slide rail B7.9 is fixed on the outer wall of the bacterial solution dilution mixing tank 2. The rack B7.7 meshes with the fourth gear 7.3 and the fifth gear 7.4. By controlling the extension and retraction of the drive cylinder B7.8, the rack B7.7 is driven to reciprocate along its length. Under the meshing of the rack B7.7 with the fifth gear 7.4 and the fourth rotary joint 7.5, the fourth rotary tube 7.1 and the fifth rotary tube 7.2 are rotated back and forth. The fourth rotary tube 7.1 and the fifth rotary tube 7.2, which are located inside the bacterial solution dilution mixing tank 2, are each equipped with a stirring blade B7.11 and a spray hole B.
[0038] Reference Figure 5 The fourth rotating tube 7.1 and the fifth rotating tube 7.2 are arranged alternately with the first rotating tube 6.1, the second rotating tube 6.2 and the third rotating tube 6.3.
[0039] Furthermore, the bacterial agent supply system connected to the first agitator 6 includes a first branch pipe, a second branch pipe, and a third branch pipe connected to the liquid supply ports on the first rotary joint 6.7, the second rotary joint 6.8, and the third rotary joint 6.9. The first branch pipe, the second branch pipe, and the third branch pipe are connected to the main pipe, and the other end of the main pipe extends to the bacterial liquid storage tank. A bacterial liquid supply pump 17 is installed on the main pipe.
[0040] Furthermore, the liquid supply pump 14 is a diaphragm pump, and the bacterial liquid supply pump 17 is a peristaltic pump, the flow rate of which can be adjusted as needed.
[0041] Furthermore, both inlets of the pipeline mixer 4 are connected to the second bend 9, the outlet of the pipeline mixer 4 is connected to the liquid outlet pipe 3, and the pipeline mixer 4 has twisted fixed spiral blades inside.
[0042] The blended fertilizer production system with quantitative continuous feeding function described in this invention can inject basic liquid into the bacterial solution dilution and mixing tank through the basic liquid inlet pipe, and inject the bacterial solution to be diluted into the bacterial solution dilution and mixing tank through the first and second agitators. The bacterial solution can be fully mixed in the bacterial solution dilution and mixing tank. The diluted bacterial solution is sprayed onto the blended fertilizer particles on the blended fertilizer conveyor belt through the mixed liquid outlet pipe, pipeline mixer, and spray gun. This allows the liquid microbial agent to be sprayed and adsorbed onto the blended fertilizer particles. This invention is used to prepare microbial agent + blended fertilizer by compounding microbial agent and blended fertilizer. Using microbial agent and blended fertilizer together can give full play to the advantages of both.
[0043] The blended fertilizer production system with quantitative continuous feeding function described in this invention adopts a circuitous path in the bacterial solution dilution mixing tank. The circuitous path extends the flow distance and is equipped with multiple sets of agitators, so that the bacterial solution to be diluted can be fully mixed with the base liquid in the bacterial solution dilution mixing tank.
[0044] The blended fertilizer production system with quantitative continuous feeding function described in this invention controls the extension and retraction of the drive cylinder A to drive the rack A to reciprocate along its length. Under the meshing of the rack A with the first gear, the second gear, and the third gear, the first rotating tube, the second rotating tube, and the third rotating tube reciprocate. The first rotating tube, the second rotating tube, and the third rotating tube, which are located in the bacterial solution dilution mixing tank, are all equipped with stirring blades A and spray holes A, which further improves the mixing effect of the bacterial solution to be diluted with the base liquid in the bacterial solution dilution mixing tank.
[0045] The foregoing has shown and described the basic principles, main features, and advantages of the present invention. Those skilled in the art should understand that the present invention is not limited to the above embodiments. The embodiments and descriptions in the specification are merely illustrative of the principles of the invention. Various changes and modifications can be made to the invention without departing from its spirit and scope, and all such changes and modifications fall within the scope of the present invention as claimed. The scope of protection of the present invention is defined by the appended claims and their equivalents.
[0046] Any aspects of this invention not described in detail are well-known to those skilled in the art.
Claims
1. A blended fertilizer production system with quantitative continuous feeding function, comprising a bacterial solution dilution and mixing tank, wherein a first bent pipe is connected to the inlet at the bottom of the bacterial solution dilution and mixing tank, and a second bent pipe is connected to the outlet at the top of the bacterial solution dilution and mixing tank, characterized in that: The other end of the first bend is connected to the base liquid inlet pipe, the other end of the second bend is connected to the pipeline mixer, and the other end of the pipeline mixer is connected to the mixed liquid outlet pipe. The bacterial liquid dilution mixing tank is provided with multiple sets of internal partitions at intervals. The internal partitions divide the inner cavity of the bacterial liquid dilution mixing tank into multiple sets of mixing chambers. Each set of mixing chambers is equipped with two sets of stirring mixers. The liquid supply port of the stirring mixer is connected to the bacterial agent supply system. The mixed liquid outlet pipe is connected to a spray gun. The bacterial agent spraying system is located above the conveying path of the blended fertilizer conveyor belt. The spray gun is used to spray and adsorb the liquid microbial agent onto the blended fertilizer particles. The mixed liquid outlet pipe is equipped with an electronically controlled regulating valve to control the flow rate.
2. The blended fertilizer production system with quantitative continuous feeding function according to claim 1, characterized in that, The bacterial solution dilution and mixing tank is a rectangular box, including a bottom plate and a top plate. There are four sets of side plates between the bottom plate and the top plate. The top plate, bottom plate and the four sets of side plates together form the bacterial solution dilution and mixing tank. The bottom plate has an inlet and the top plate has an outlet.
3. The blended fertilizer production system with quantitative continuous feeding function according to claim 2, characterized in that, The number of inner partitions is even. The second bend is connected to the mixing chamber at the top of the bacterial solution dilution mixing tank, and the first bend is connected to the mixing chamber at the bottom of the bacterial solution dilution mixing tank.
4. The blended fertilizer production system with quantitative continuous feeding function according to claim 3, characterized in that, The inner partition is provided in four sets, namely the first partition, the second partition, the third partition and the fourth partition arranged from top to bottom, dividing the inner cavity of the bacterial solution dilution mixing tank into a top layer mixing cavity, a second layer mixing cavity, a third layer mixing cavity, a fourth layer mixing cavity and a bottom layer mixing cavity from top to bottom. Two sets of stirring mixers are respectively provided in the top layer mixing cavity, the second layer mixing cavity, the third layer mixing cavity, the fourth layer mixing cavity and the bottom layer mixing cavity. The ends of the first partition, the second partition, the third partition and the fourth partition are respectively provided with liquid outlet A, liquid outlet B, liquid outlet C and liquid outlet D. Adjacent liquid outlets are staggered, and liquid outlet A is staggered with the liquid outlet, and liquid outlet D is staggered with the liquid inlet.
5. The blended fertilizer production system with quantitative continuous feeding function according to claim 4, characterized in that, The two sets of mixers in the bottom mixing chamber are the first and second mixers; the two sets of mixers in the fourth mixing chamber are the third and fourth mixers; the two sets of mixers in the third mixing chamber are the fifth and sixth mixers; the two sets of mixers in the second mixing chamber are the seventh and eighth mixers; and the two sets of mixers in the top mixing chamber are the ninth and tenth mixers. The bacterial solution dilution mixing tank employs a circuitous path. This circuitous path, by extending the flow distance and incorporating multiple mixers, ensures that the bacterial solution to be diluted is thoroughly mixed with the base solution within the tank.
6. The blended fertilizer production system with quantitative continuous feeding function according to claim 5, characterized in that, The first stirring mixer includes a first rotating tube, a second rotating tube, and a third rotating tube arranged at intervals. One end of the first rotating tube is inserted into a bacterial solution dilution mixing tank and maintains a rotational seal with the tank. The inner end of the first rotating tube is sealed. The outer end of the first rotating tube is provided with a first gear and a first rotating joint, the first rotating joint communicating with the inner cavity of the first rotating tube. One end of the second rotating tube is inserted into the bacterial solution dilution mixing tank and maintains a rotational seal with the tank. The inner end of the second rotating tube is sealed. The outer end of the second rotating tube is provided with a second gear and a second rotating joint, the second rotating joint communicating with the inner cavity of the second rotating tube. One end of the third rotating tube is inserted into the bacterial solution dilution mixing tank and maintains a rotational seal with the tank. The inner end of the third rotating tube is sealed. The outer end of the rotating tube is provided with a third gear and a third rotating joint. The third rotating joint is connected to the inner cavity of the third rotating tube. A drive cylinder A is fixed on the outer wall of the bacterial solution dilution mixing tank. The telescopic end of the drive cylinder A is connected to the rack A through a connecting rod A. The bottom of the rack A has a slide rail A. A slider A that slides in cooperation with the slide rail A is fixed on the outer wall of the bacterial solution dilution mixing tank. The rack A meshes with the first gear, the second gear, and the third gear. By controlling the telescopic extension of the drive cylinder A, the rack A is driven to reciprocate along its length. Under the meshing of the rack A with the first gear, the second gear, and the third gear, the first rotating tube, the second rotating tube, and the third rotating tube reciprocate. The first rotating tube, the second rotating tube, and the third rotating tube inside the bacterial solution dilution mixing tank are all provided with stirring blades A and spray holes A.
7. The blended fertilizer production system with quantitative continuous feeding function according to claim 6, characterized in that, The second stirring mixer includes a fourth rotating tube and a fifth rotating tube spaced apart. One end of the fourth rotating tube is inserted into the bacterial solution dilution mixing tank and maintains a rotational seal with the tank. The inner end of the fourth rotating tube is sealed. The outer end of the fourth rotating tube is provided with a fourth gear and a fourth rotating joint, which communicates with the inner cavity of the fourth rotating tube. One end of the fifth rotating tube is inserted into the bacterial solution dilution mixing tank and maintains a rotational seal with the tank. The inner end of the fifth rotating tube is sealed. The outer end of the fifth rotating tube is provided with a fifth gear and a fifth rotating joint, which communicates with the inner cavity of the fifth rotating tube. A drive cylinder B is fixed on the outer wall of the bacterial solution dilution mixing tank. The telescopic end of the drive cylinder B is connected to the rack B via a connecting rod B. The bottom of the rack B has a slide rail B. A slider B that slides in cooperation with the slide rail B is fixed on the outer wall of the bacterial solution dilution mixing tank. The rack B meshes with the fourth gear and the fifth gear. By controlling the extension and retraction of the drive cylinder B, the rack B is driven to reciprocate along its length. Under the meshing of the rack B with the fifth gear and the fourth rotary joint, the fourth rotary tube and the fifth rotary tube reciprocate. The fourth rotary tube and the fifth rotary tube inside the bacterial solution dilution mixing tank are each equipped with stirring blades B and spray holes B.
8. The blended fertilizer production system with quantitative continuous feeding function according to claim 7, characterized in that, The bacterial agent supply system connected to the first agitator includes a first branch pipe, a second branch pipe, and a third branch pipe connected to the liquid supply ports on the first rotary joint, the second rotary joint, and the third rotary joint. The first branch pipe, the second branch pipe, and the third branch pipe are connected to the main pipe, the other end of which extends to the bacterial liquid storage tank. A bacterial liquid supply pump is installed on the main pipe.
9. The blended fertilizer production system with quantitative continuous feeding function according to claim 8, characterized in that, The liquid supply pump is a diaphragm pump, and the bacterial liquid supply pump is a peristaltic pump, the flow rate of which can be adjusted as needed.
10. The blended fertilizer production system with quantitative continuous feeding function according to any one of claims 1-9, characterized in that, Both inlets of the pipeline mixer are connected to the second bend, and the outlet of the pipeline mixer is connected to the liquid outlet pipe. The pipeline mixer has spiral blades inside.
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Water and fertilizer integrated system and irrigator
CN119896107A