Yellow phosphorus drying and transporting system

Abstract

The invention relates to the technical field of yellow phosphorus drying systems, in particular to a yellow phosphorus drying and transporting system which comprises a drying box, a storage box, a feeding assembly, a conveying assembly, a humidity adjusting assembly, a vacuum assembly and a control unit. According to the device, through intelligent temperature control, accurate humidity adjustment and efficient sealing measures, the risks of spontaneous combustion and leakage of yellow phosphorus are greatly reduced, reliable safety guarantee is provided for operators and the surrounding environment, and the device has the advantages of being high in practicability, convenient to operate, high in practicability and the like. Various parameters in the drying process can be accurately controlled, the water content of yellow phosphorus is stably reduced to the low level, the quality and purity of yellow phosphorus products are improved, and through accurate power control over the infrared heating pipes, the vacuum dehumidification technology and the optimized airflow circulation design, the energy utilization rate is increased, and energy consumption is reduced.

Description

Technical Field

[0001] The invention relates to the technical field of yellow phosphorus drying systems, in particular to a yellow phosphorus drying and transportation system. Background Art

[0002] Yellow phosphorus is an extremely active and dangerous substance that is prone to spontaneous combustion at room temperature. Traditional yellow phosphorus drying technology faces many challenges. Existing drying systems often have difficulty in accurately controlling the drying environment, which can easily lead to spontaneous combustion of yellow phosphorus or poor drying results due to factors such as temperature, humidity, and unstable airflow. Summary of the invention

[0003] In view of the technical problems raised in the background technology, the present invention provides a yellow phosphorus drying and transportation system.

[0004] The technical solution adopted by the present invention is: a yellow phosphorus drying and transportation system, comprising: a drying box, a storage box, a feeding component, a conveying component, a humidity regulating component, a vacuum component and a control unit, wherein an inner frame is fixedly connected to the drying box, an insulating cavity is provided between the inner frame and the drying box, the insulating cavity is filled with insulating materials, a plurality of groups of infrared heating tubes are fixedly connected to the inner frame, the storage box is arranged in the inner frame, a porous frame is fixedly connected to the storage box, an adsorption cavity is provided between the porous frame and the storage box, the adsorption cavity is filled with molecular sieve materials, the feeding component is arranged in the drying box, and is used to convey the yellow phosphorus to the storage box, the conveying component is fixedly connected in the drying box, and is used to convey the dried yellow phosphorus, the humidity regulating component is arranged outside the drying box, and is used to regulate the humidity in the drying box, the vacuum component is used to evacuate the drying box, and the control unit is used to control the humidity regulating component and the vacuum component.

[0005] In one embodiment, the feed assembly includes a feed pipe fixedly connected to the drying box and a first valve fixedly connected to the outside of the feed pipe, one end of the feed pipe extends into the drying box, and a plurality of outlets are provided at the bottom of the feed pipe.

[0006] In one embodiment, a push tube is provided through the drying box, a piston rod is slidably connected in the push tube, a second electric push rod is fixedly connected to the outside of the drying box, the output end of the second electric push rod is fixedly connected to the push tube, the outside of the push tube is fixedly connected to the first electric push rod, the output end of the first electric push rod is fixedly connected to the piston rod, one end of the piston rod is fixedly connected to an electromagnet, a through hole is provided in the storage box, a push plate is slidably connected in the storage box, a magnet block is fixedly connected to the outside of the push plate, a spring is connected between the push tube and the storage box, an iron sheet is fixedly connected to the position of the magnet block corresponding to the porous frame, a discharge port is provided at one end of the storage box, and inclined plates are fixedly connected on both sides of the corresponding discharge port in the porous frame.

[0007] In one embodiment, the bottom of the storage box is fixedly connected with multiple groups of adjustment protrusions, and the adjustment protrusions are arc-shaped structures with different diameters; the bottom of the inner frame is fixedly connected with multiple groups of arc-shaped protrusions, and one end of the arc-shaped protrusion is fixedly connected with a support plate.

[0008] In one embodiment, the conveying component is a spiral conveying auger fixedly connected in the drying box, the output port of the spiral conveying auger is fixedly connected to the eighth pipeline, and the outside of the eighth pipeline is fixedly connected to the sixth valve.

[0009] In one embodiment, the humidity regulating component includes a fan and an air dehumidifier, the input end of the fan is fixedly connected to a first pipe, one end of the first pipe extends into a drying box, the outside of the first pipe is fixedly connected to a third valve, the outside of the first pipe is fixedly connected to a second pipe, the second pipe is fixedly connected to a second valve, the output end of the fan is fixedly connected to a fourth pipe, the fourth pipe is fixedly connected to a fourth valve, the fourth pipe is fixedly connected to a fifth pipe, one end of the fifth pipe is fixedly connected to the input end of the air dehumidifier, the fifth pipe is fixedly connected to a fifth valve, the output end of the air dehumidifier is fixedly connected to a sixth pipe, one end of the sixth pipe extends into the drying box.

[0010] In one embodiment, the vacuum component is a vacuum pump, an input end of the vacuum pump is fixedly connected to a seventh pipe, and one end of the seventh pipe extends into the drying box.

[0011] In one of the embodiments, a plurality of groups of temperature sensors are fixedly installed in the inner frame, and the control unit is a controller;

[0012] The controller is used to adjust the heating power of the infrared heating tube, and the specific adjustment calculation formula is as follows:

[0013]

[0014] When the temperature is higher than the set upper limit temperature T max When the temperature is lower than the set lower limit temperature T min When , the controller increases the heating power;

[0015] Among them, the mass of yellow phosphorus is m (unit: kg), the specific heat capacity of yellow phosphorus is c (unit: J / (kg·℃)), and the initial temperature is T 1(单位 : ℃), the target drying temperature is T2 (unit: ℃), the drying time is t (unit: s), and the heating power of the infrared heating tube is P (unit: W).

[0016] In one embodiment, a plurality of humidity sensors are fixedly installed in the inner frame, and the controller is used to adjust the humidity in the inner frame. The specific adjustment calculation formula is as follows:

[0017] m w =ρ×V×(H1-H2)

[0018] E=m w ×L

[0019] When the humidity is higher than the set safety humidity value H max When the air is exhausted, the fan starts to discharge the humid air and introduce the dry air treated by the air dehumidifier;

[0020] The volume of the inner frame is V (unit: m 3 ), the initial humidity is H1 (unit: %), the target humidity is H2 (unit: %), and the density of air is ρ (unit: kg / m 3 ), the latent heat of vaporization of water is L (unit: J / kg), and the mass of water discharged is m w (Unit: kg), the energy required for dehumidification is E (Unit: J).

[0021] In one embodiment, the controller further adjusts the vacuum pump to adjust the vacuum level in the drying box. The specific adjustment calculation formula is as follows:

[0022]

[0023] Among them, the initial water content of yellow phosphorus is m w1 (unit: kilograms), the adsorption capacity of molecular sieve material for water is C (unit: kilograms per cubic meter), the filling volume of molecular sieve material is V (unit: cubic meter); after a period of time t1 (unit: seconds), the water content of yellow phosphorus is m w2 (Unit: kg), when the molecular sieve material is close to saturation, start the vacuum pump to reduce the pressure in the drying box to P vac (Unit: Pascal).

[0024] The beneficial effects of the present invention are:

[0025] 1. Compared with the prior art, the present invention greatly reduces the risk of spontaneous combustion and leakage of yellow phosphorus through intelligent temperature control, precise humidity adjustment and efficient sealing measures, provides reliable safety protection for operators and the surrounding environment, can accurately control various parameters in the drying process, and stably reduce the water content of yellow phosphorus to a low level, thereby improving the quality and purity of the yellow phosphorus product. Through precise power control of infrared heating tubes, vacuum dehumidification technology and optimized airflow circulation design, energy utilization is improved, energy consumption is reduced, and production costs are reduced.

[0026] 2. Compared with the prior art, in the present invention, while drying the yellow phosphorus, the second electric push rod can be started to work, the second electric push rod pushes the push tube to slide, and the push tube pushes the storage box to reciprocate in the drying box through the spring, and at the same time the adjusting protrusion will continuously contact the arc-shaped protrusion, so that the storage box can vibrate in the inner frame, flatten the yellow phosphorus in the storage box, and facilitate further drying.

[0027] 3. Compared with the prior art, in the present invention, humidity detection can be performed through a humidity sensor. Once the humidity is higher than the set safety humidity value, the fan starts, the third valve and the fourth valve are opened, and the second valve and the fifth valve are closed, so that the fan sucks out the humid air and discharges it through the fourth pipe; then, the third valve and the fourth valve are closed, and the second valve and the fifth valve are opened, and the fan can suck in outdoor air and transport it to the dehumidifier, and introduce the dry air treated by the air dehumidifier into the inner frame for recycling.

[0028] 4. Compared with the prior art, in the present invention, the moisture in the yellow phosphorus can also be adsorbed by the molecular sieve material. Once the molecular sieve material is close to saturation, the vacuum pump is started to reduce the pressure in the drying box to a set value. Under the vacuum environment, the boiling point of the moisture is greatly reduced, and it is easier to volatilize from the surface of the yellow phosphorus and be adsorbed by the molecular sieve, thereby increasing the drying effect. BRIEF DESCRIPTION OF THE DRAWINGS

[0029] Figure 1 It is a schematic diagram of the structure of the present invention;

[0030] Figure 2 It is a three-dimensional structural schematic diagram of the present invention;

[0031] Figure 3 It is a schematic diagram of the axonometric structure of the present invention;

[0032] Figure 4 The internal structure of the drying box of the present invention is shown in FIG. Figure 1 ;

[0033] Figure 5 The internal structure of the drying box of the present invention is shown in FIG. Figure 2 ;

[0034] Figure 6 It is a structural schematic diagram of the inner frame in the present invention;

[0035] Figure 7 yes Figure 6 Schematic diagram of the enlarged structure of the A area in the middle;

[0036] Figure 8 It is a schematic diagram of the structure of the first electric push rod and the second electric push rod in the present invention;

[0037] Fig. 9 It is a structural schematic diagram of the push plate in the present invention.

[0038] The markings in the figure are:

[0039] 100, drying box; 1001, infrared heating tube; 1002, arc-shaped protrusion; 1003, support plate; 1004, feed pipe; 1005, first valve; 1006, inner frame; 1007, heat insulation chamber; 1008, outlet;

[0040] 200, fan; 2001, first pipeline; 2002, second pipeline; 2003, second valve; 2004, third pipeline; 2005, third valve; 2006, fourth pipeline; 2007, fourth valve; 2008, fifth pipeline; 2009, fifth valve;

[0041] 300, air dehumidifier; 3001, sixth pipeline;

[0042] 400, vacuum pump; 4001, seventh pipeline;

[0043] 500, spiral conveying auger; 5001, eighth pipeline; 5002, sixth valve;

[0044] 600, storage box; 6001, adjustment protrusion; 6002, porous frame; 6003, adsorption chamber; 6004, discharge port; 6005, inclined plate;

[0045] 700, push tube; 7001, piston rod; 7002, first electric push rod; 7003, second electric push rod; 7004, electromagnet; 7005, spring; 7006, through hole; 7007, push plate; 7008, magnet block. DETAILED DESCRIPTION

[0046] In the description of the present invention, it should be noted that the orientations or positional relationships indicated by terms such as “front”, “up”, “down”, “left”, “right”, “vertical” and “horizontal” are based on the orientations or positional relationships shown in the accompanying drawings, and are only for the convenience of describing the present invention and simplifying the description, rather than indicating or implying that the device or element referred to must have a specific orientation, be constructed and operated in a specific orientation, and therefore cannot be understood as a limitation on the present invention.

[0047] In the description of the present invention, it should be noted that, unless otherwise clearly specified and limited, the terms "installed", "connected", and "connected" should be understood in a broad sense, for example, it can be a fixed connection, a detachable connection, or an integral connection; it can be a direct connection, or an indirect connection through an intermediate medium, or it can be the internal communication of two components. For ordinary technicians in this field, the specific meanings of the above terms in the present invention can be understood according to specific circumstances.

[0048] The following is combined with Figure 1-9 The present invention is further described.

[0049] In order to solve the problems existing in the background technology, the present application proposes the following technical solutions: a yellow phosphorus drying and transportation system, comprising: a drying box 100, a storage box 600, a feeding component, a conveying component, a humidity regulating component, a vacuum component and a control unit.

[0050] In the specific technical solution, the drying box 100 is fixedly connected with an inner frame 1006, and an insulating cavity 1007 is provided between the inner frame 1006 and the drying box 100, and the insulating cavity 1007 is filled with insulating materials, such as rock wool; multiple groups of infrared heating tubes 1001 are fixedly connected to the inner frame 1006; the storage box 600 is arranged in the inner frame 1006, and a porous frame 6002 is fixedly connected to the storage box 600, and an adsorption cavity 6003 is provided between the porous frame 6002 and the storage box 600, and the adsorption cavity 6003 is filled with molecular sieve material;

[0051] For example, 3A molecular sieve is a potassium-type molecular sieve with a pore size of about 0.3 nm. It can adsorb molecules smaller than the pore size, has a strong affinity for water, and has good water absorption.

[0052] Among them, the feeding component is arranged in the drying box 100, and is used to transport the yellow phosphorus to the storage box 600. The conveying component is fixedly connected in the drying box 100, and is used to transport the dried yellow phosphorus. The humidity regulating component is arranged outside the drying box 100, and is used to regulate the humidity in the drying box 100. The vacuum component is used to vacuum the drying box 100, and the control unit is used to control the humidity regulating component and the vacuum component.

[0053] In the specific technical solution, the feed assembly includes a feed pipe 1004 fixedly connected to the drying box 100 and a first valve 1005 fixedly connected to the outside of the feed pipe 1004. One end of the feed pipe 1004 extends into the drying box 100, and a plurality of groups of outlets 1008 are provided at the bottom of the feed pipe 1004. The yellow phosphorus to be dried enters the drying box 100 through the feed pipe 1004 and is discharged into the storage box 600 through the outlet 1008.

[0054] In a further design, a push tube 700 is provided through the drying box 100, a piston rod 7001 is slidably connected in the push tube 700, a second electric push rod 7003 is fixedly connected to the outside of the drying box 100, an output end of the second electric push rod 7003 is fixedly connected to the push tube 700, a first electric push rod 7002 is fixedly connected to the outside of the push tube 700, an output end of the first electric push rod 7002 is fixedly connected to the piston rod 7001, an end of the piston rod 7001 is fixedly connected to an electromagnet 7004, a through hole 7006 is provided in the storage box 600, and the storage box 600 A push plate 7007 is slidably connected in the middle, a magnet block 7008 is fixedly connected to the outside of the push plate 7007, a spring 7005 is connected between the push tube 700 and the storage box 600, an iron sheet is fixedly connected to the position of the magnet block 7008 corresponding to the porous frame 6002, a discharge port 6004 is provided at one end of the storage box 600, and inclined plates 6005 are fixedly connected on both sides of the corresponding discharge port 6004 in the porous frame 6002. The inclined plate 6005 is made of iron material for guiding the yellow phosphorus, and an electric valve can also be set at the outlet 1008.

[0055] The above technical solution is explained as follows: the storage box 600 is pushed to one side of the spiral conveying auger 500 by the second electric push rod 7003, so that the feed end of the spiral conveying auger 500 enters the discharge port 6004, and the yellow phosphorus is transported away by the spiral conveying auger 500. At the same time, the first electric push rod 7002 can be started to drive the piston rod 7001 to slide, and the electromagnet 7004 hit by the piston rod 7001 slides and enters the storage box 600 through the through hole 7006, and is fixed by the electromagnet 7004 and the push plate 7007 through adsorption, and the push plate 7007 is pushed to slide by the piston rod 7001, and the yellow phosphorus is pushed to the bottom of the spiral conveying auger 500 by the push plate 7007, so as to facilitate the discharge of the material.

[0056] In a further design, the bottom of the storage box 600 is fixedly connected with multiple groups of adjustment protrusions 6001, and the adjustment protrusions 6001 are arc-shaped structures with different diameters; the bottom of the inner frame 1006 is fixedly connected with multiple groups of arc-shaped protrusions 1002, and one end of the arc-shaped protrusion 1002 is fixedly connected with a support plate 1003;

[0057] The above technical solution is explained as follows: the push tube 700 is pushed to slide by the second electric push rod 7003, and the push tube 700 pushes the storage box 600 to reciprocate in the drying box 100 through the spring 7005. At the same time, the adjusting protrusion 6001 will continuously contact the arc-shaped protrusion 1002, so that the storage box 600 can vibrate in the inner frame 1006, flattening the yellow phosphorus in the storage box 600 to facilitate further drying.

[0058] In a further design, the conveying component is a spiral conveying auger 500 fixedly connected in the drying box 100 , the output port 1008 of the spiral conveying auger 500 is fixedly connected to the eighth pipeline 5001 , and the outside of the eighth pipeline 5001 is fixedly connected to the sixth valve 5002 .

[0059] The speed of the spiral conveying auger 500 can be adjusted according to the discharge flow rate of the dried yellow phosphorus. Assuming that the diameter of the spiral blade of the spiral conveying auger 500 is D (unit: m), the pitch is p (unit: m), and the speed is n (unit: r / s), then the discharge flow rate Q out (Unit: m 3 / s) is calculated as:

[0060] In addition, a flow monitoring device and a temperature detector may also be installed on the eighth pipeline 5001 to ensure the stability and safety of the discharge process.

[0061] The humidity adjustment component includes a fan 200 and an air dehumidifier 300. The input end of the fan 200 is fixedly connected to a first pipe 2001. One end of the first pipe 2001 extends into the drying box 100. The outside of the first pipe 2001 is fixedly connected to a third valve 2005. The outside of the first pipe 2001 is fixedly connected to a second pipe 2002. The second pipe 2002 is fixedly connected to a second valve 2003. The output end of the fan 200 is fixedly connected to a fourth pipe 2006. The fourth pipe 2006 is fixedly connected to a fourth valve 2005. 07. A fifth pipe 2008 is fixedly connected to the fourth pipe 2006, one end of the fifth pipe 2008 is fixedly connected to the input end of the air dehumidifier 300, a fifth valve 2009 is fixedly connected to the fifth pipe 2008, a sixth pipe 3001 is fixedly connected to the output end of the air dehumidifier 300, one end of the sixth pipe 3001 extends into the drying box 100, the vacuum component is a vacuum pump 400, the input end of the vacuum pump 400 is fixedly connected to the seventh pipe 4001, one end of the seventh pipe 4001 extends into the drying box 100.

[0062] The above technical solution is explained as follows: During the drying process, the humidity can be detected by a humidity sensor. Once the humidity is higher than the set safety humidity value H max When the air is cooled, the fan 200 is started, the third valve 2005 and the fourth valve 2007 are opened, and the second valve 2003 and the fifth valve 2009 are closed, so that the fan 200 sucks out the humid air and discharges it through the fourth pipe 2006; then, the third valve 2005 and the fourth valve 2007 are closed, and the second valve 2003 and the fifth valve 2009 are opened, and the fan 200 can suck in the outdoor air and transport it to the dehumidifier, and introduce the dry air treated by the air dehumidifier 300 into the inner frame 1006 for recycling.

[0063] Among them, multiple groups of temperature sensors are also fixedly installed in the inner frame 1006, and the control unit is a controller;

[0064] The controller is used to adjust the heating power of the infrared heating tube 1001, and the specific adjustment calculation formula is as follows:

[0065]

[0066] When the temperature is higher than the set upper limit temperature T max When the temperature is lower than the set lower limit temperature T min When , the controller increases the heating power;

[0067] Among them, the mass of yellow phosphorus is m (unit: kg), the specific heat capacity of yellow phosphorus is c (unit: J / (kg·℃)), and the initial temperature is T 1(单位 ℃), the target drying temperature is T2 (unit: ℃), the drying time is t (unit: s), and the heating power of the infrared heating tube 1001 is P (unit: W).

[0068] Among them, multiple groups of humidity sensors are fixedly installed in the inner frame 1006, and the controller is used to adjust the humidity in the inner frame 1006. The specific adjustment calculation formula is as follows:

[0069] m w =ρ×V×(H1-H2)

[0070] E=m w ×L

[0071] When the humidity is higher than the set safe humidity value H max When the air is exhausted, the fan 200 starts to discharge the moist air and introduce the dry air treated by the air dehumidifier;

[0072] The volume of the inner frame 1006 is V (unit: m 3 ), the initial humidity is H1 (unit: %), the target humidity is H2 (unit: %), and the density of air is ρ (unit: kg / m 3 ), the latent heat of vaporization of water is L (unit: J / kg), and the mass of water discharged is m w (Unit: kg), the energy required for dehumidification is E (Unit: J).

[0073] The controller also adjusts the vacuum pump 400 to adjust the vacuum level in the drying box 100. The specific adjustment calculation formula is as follows:

[0074]

[0075] Among them, the initial water content of yellow phosphorus is m w1 (unit: kilograms), the adsorption capacity of molecular sieve material for water is C (unit: kilograms per cubic meter), the filling volume of molecular sieve material is V (unit: cubic meter); after a period of time t1 (unit: seconds), the water content of yellow phosphorus is m w2 (Unit: kg), when the molecular sieve material is close to saturation, start the vacuum pump 400 to reduce the pressure in the drying box 100 to P vac (Unit: Pascal), under vacuum environment, the boiling point of water is greatly reduced, and it is easier to evaporate from the surface of yellow phosphorus and be adsorbed by the molecular sieve.

[0076] In order for those skilled in the art to fully understand the technical solution, the working principle of this embodiment is as follows:

[0077] When in use, the yellow phosphorus is transported to the drying box 100 through the feeding pipe 1004 and falls into the storage box 600. At the same time, the infrared heat pipe is turned on for heating and drying. During drying, the second electric push rod 7003 can be started to work. The second electric push rod 7003 pushes the push pipe 700 to slide. The push pipe 700 pushes the storage box 600 to reciprocate in the drying box 100 through the spring 7005. At the same time, the adjusting protrusion 6001 will continuously contact the arc-shaped protrusion 1002, so that the storage box 600 can vibrate in the inner frame 1006, and the yellow phosphorus in the storage box 600 is flattened, which is convenient for further drying.

[0078] During the drying process, the humidity can be detected by the humidity sensor. Once the humidity is higher than the set safe humidity value H max When the fan 200 is started, the third valve 2005 and the fourth valve 2007 are opened, and the second valve 2003 and the fifth valve 2009 are closed, so that the fan 200 sucks out the humid air and discharges it through the fourth pipe 2006;

[0079] Then, the third valve 2005 and the fourth valve 2007 are closed, and the second valve 2003 and the fifth valve 2009 are opened, so that the fan 200 can suck in the outdoor air and transport it to the dehumidifier, and introduce the dry air treated by the air dehumidifier 300 into the inner frame 1006 for recycling;

[0080] At the same time, during the drying process, the humidity can be detected by the temperature sensor. When the temperature is higher than the set upper limit temperature T max When the temperature is lower than the set lower limit temperature T min When , the controller increases the heating power;

[0081] In addition, the moisture in the yellow phosphorus can be adsorbed by the molecular sieve material. Once the molecular sieve material is close to saturation, the vacuum pump 400 is started to reduce the pressure in the drying box 100 to P. vac (Unit: Pascal), in a vacuum environment, the boiling point of water is greatly reduced, and it is easier to evaporate from the surface of yellow phosphorus and be adsorbed by the molecular sieve, increasing the drying effect;

[0082] After the drying is completed, the storage box 600 is pushed to one side of the spiral conveying auger 500 by the second electric push rod 7003, so that the feeding end of the spiral conveying auger 500 enters the discharge port 6004, and the yellow phosphorus is transported away by the spiral conveying auger 500. At the same time, the first electric push rod 7002 can be started to drive the piston rod 7001 to slide, and the electromagnet 7004 hit by the piston rod 7001 slides and enters the storage box 600 through the through hole 7006, and is fixed by the electromagnet 7004 and the push plate 7007 through adsorption, and the push plate 7007 is pushed to slide by the piston rod 7001, and the yellow phosphorus is pushed to the bottom of the spiral conveying auger 500 by the push plate 7007;

[0083] After completion, the first electric push rod 7002 drives the piston rod 7001 to retract, and at the same time the electromagnet 7004 is powered off, and the push plate 7007 is adsorbed on the outside of the porous frame 6002 again through the magnet block 7008.

[0084] In summary, the excellent safety of this equipment greatly reduces the risk of spontaneous combustion and leakage of yellow phosphorus through intelligent temperature control, precise humidity adjustment and efficient sealing measures, providing reliable safety protection for operators and the surrounding environment. It can accurately control various parameters in the drying process, so that the moisture content of yellow phosphorus can be steadily reduced to a low level, thereby improving the quality and purity of yellow phosphorus products. Through precise power control of infrared heating tube 1001, vacuum dehumidification technology and optimized airflow circulation design, it improves energy utilization, reduces energy consumption and reduces production costs.

[0085] The standard parts used in the present invention can all be purchased from the market, and special-shaped parts can be customized according to the description in the specification and the drawings. The specific connection methods of each part adopt conventional means such as mature bolts, rivets, welding, etc. in the prior art. Machinery, parts and equipment all adopt conventional models in the prior art, and the circuit connection adopts the conventional connection method in the prior art, which will not be described in detail here. The content not described in detail in this specification belongs to the prior art known to professional and technical personnel in this field.

[0086] While the embodiments of the present invention have been shown and described, it will be apparent to those skilled in the art that the scope of the present invention is defined by the appended claims and their equivalents.

Claims

1. A yellow phosphorus drying and transportation system, characterized in that: include: A drying box (100), wherein an inner frame (1006) is fixedly connected inside the drying box (100), a heat insulation cavity (1007) is provided between the inner frame (1006) and the drying box (100), the heat insulation cavity (1007) is filled with heat insulation material, and a plurality of groups of infrared heating tubes (1001) are fixedly connected inside the inner frame (1006); A storage box (600), wherein the storage box (600) is arranged in an inner frame (1006), a porous frame (6002) is fixedly connected to the storage box (600), an adsorption chamber (6003) is arranged between the porous frame (6002) and the storage box (600), and the adsorption chamber (6003) is filled with a molecular sieve material; A feeding assembly, the feeding assembly being arranged in the drying box (100) and used for conveying the yellow scales to the storage box (600); A conveying assembly, the conveying assembly is fixedly connected to the drying box (100) and is used to convey the dried yellow phosphorus; A humidity regulating component, the humidity regulating component being arranged outside the drying box (100) and being used for regulating the humidity inside the drying box (100); A vacuum component, the vacuum component being used to evacuate the drying box (100); A control unit is used to control the humidity adjustment component and the vacuum component.

2. A yellow phosphorus drying and transportation system according to claim 1, characterized in that: The feed assembly comprises a feed pipe (1004) fixedly connected in the drying box (100) and a first valve (1005) fixedly connected to the outside of the feed pipe (1004), one end of the feed pipe (1004) extends into the drying box (100), and a plurality of groups of outlets (1008) are provided at the bottom of the feed pipe (1004).

3. A yellow phosphorus drying and transportation system according to claim 2, characterized in that: The drying box (100) is provided with a push tube (700) running through it, a piston rod (7001) is slidably connected inside the push tube (700), a second electric push rod (7003) is fixedly connected to the outside of the drying box (100), an output end of the second electric push rod (7003) is fixedly connected to the push tube (700), a first electric push rod (7002) is fixedly connected to the outside of the push tube (700), an output end of the first electric push rod (7002) is fixedly connected to the piston rod (7001), one end of the piston rod (7001) is fixedly connected to an electromagnet (7004), and the storage A through hole (7006) is provided in the storage box (600), a push plate (7007) is slidably connected to the storage box (600), a magnet block (7008) is fixedly connected to the outside of the push plate (7007), a spring (7005) is connected between the push tube (700) and the storage box (600), an iron sheet is fixedly connected to the position of the magnet block (7008) corresponding to the porous frame (6002), a discharge port (6004) is provided at one end of the storage box (600), and inclined plates (6005) are fixedly connected to both sides of the corresponding discharge port (6004) in the porous frame (6002).

4. A yellow phosphorus drying and transportation system according to claim 3, characterized in that: The bottom of the storage box (600) is fixedly connected with a plurality of adjustment protrusions (6001), and the adjustment protrusions (6001) are arc-shaped structures with different diameters; the bottom of the inner frame (1006) is fixedly connected with a plurality of arc-shaped protrusions (1002), and one end of the arc-shaped protrusion (1002) is fixedly connected with a support plate (1003).

5. A yellow phosphorus drying and transportation system according to claim 4, characterized in that: The conveying assembly is a spiral conveying auger (500) fixedly connected in the drying box (100), the output port (1008) of the spiral conveying auger (500) is fixedly connected to an eighth pipeline (5001), and the outside of the eighth pipeline (5001) is fixedly connected to a sixth valve (5002).

6. A yellow phosphorus drying and transportation system according to claim 5, characterized in that: The humidity adjustment component comprises a fan (200) and an air dehumidifier (300), the input end of the fan (200) is fixedly connected to a first pipe (2001), one end of the first pipe (2001) extends into the drying box (100), the outside of the first pipe (2001) is fixedly connected to a third valve (2005), the outside of the first pipe (2001) is fixedly connected to a second pipe (2002), the second pipe (2002) is fixedly connected to a second valve (2003), and the output end of the fan (200) is fixedly connected to a third valve (2005). A fourth pipeline (2006) is provided, a fourth valve (2007) is fixedly connected to the fourth pipeline (2006), a fifth pipeline (2008) is fixedly connected to the fourth pipeline (2006), one end of the fifth pipeline (2008) is fixedly connected to the input end of the air dehumidifier (300), a fifth valve (2009) is fixedly connected to the fifth pipeline (2008), a sixth pipeline (3001) is fixedly connected to the output end of the air dehumidifier (300), and one end of the sixth pipeline (3001) extends into the drying box (100).

7. A yellow phosphorus drying and transportation system according to claim 6, characterized in that: The vacuum component is a vacuum pump (400), an input end of the vacuum pump (400) is fixedly connected to a seventh pipe (4001), and one end of the seventh pipe (4001) extends into the drying box (100).

8. A yellow phosphorus drying and transportation system according to claim 7, characterized in that: A plurality of groups of temperature sensors are also fixedly installed in the inner frame (1006), and the control unit is a controller; The controller is used to adjust the heating power of the infrared heating tube (1001), and the specific adjustment calculation formula is as follows: When the temperature is higher than the set upper limit temperature T max When the temperature is lower than the set lower limit temperature T min When , the controller increases the heating power; Among them, the mass of yellow phosphorus is m (unit: kg), the specific heat capacity of yellow phosphorus is c (unit: J / (kg·℃)), and the initial temperature is T 1(单位 ℃), target drying temperature is T2 (unit: ℃), drying time is t (unit: s), infrared heating tube heating power P (unit: W).

9. A yellow phosphorus drying and transportation system according to claim 8, characterized in that: A plurality of groups of humidity sensors are also fixedly installed in the inner frame (1006), and the controller is used to adjust the humidity in the inner frame (1006). The specific adjustment calculation formula is as follows: m w =ρ×V×(H1-H2) E=m w ×L When the humidity is higher than the set safe humidity value H max When the air is exhausted, the fan (200) starts to discharge the moist air and introduce dry air treated by the air dehumidifier (300); The volume of the inner frame (1006) is V (unit: m 3 ), the initial humidity is H1 (unit: %), the target humidity is H2 (unit: %), and the density of air is ρ (unit: kg / m 3 ), the latent heat of vaporization of water is L (unit: J / kg), and the mass of water discharged is m w (Unit: kg), the energy required for dehumidification is E (Unit: J).

10. A yellow phosphorus drying and transportation system according to claim 9, characterized in that: The controller also adjusts the vacuum pump (400) to adjust the vacuum level in the drying box (100). The specific adjustment calculation formula is as follows: Among them, the initial water content of yellow phosphorus is m w1 (unit: kilograms), the adsorption capacity of molecular sieve material for water is C (unit: kilograms per cubic meter), the filling volume of molecular sieve material is V (unit: cubic meter); after a period of time t1 (unit: seconds), the water content of yellow phosphorus is m w2 (Unit: kg), when the molecular sieve material is close to saturation, start the vacuum pump (400) to reduce the pressure in the drying box (100) to P vac (Unit: Pascal).

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