A preparation device for sodium methallyl sulfonate particles

Abstract

The present invention relates to the technical field of chemical preparation devices, and specifically to a preparation device for sodium methallylsulfonate particles, which includes a reaction kettle. The upper end of the reaction kettle is fixedly installed with a sealing cover through bolts. One end of the sealing cover away from the reaction kettle is fixedly installed with a heating chamber for heating sodium methallylsulfonate. A material box is arranged on the left side of the reaction kettle, and a hot blast stove is arranged on the right side of the reaction kettle. A mixing cylinder is fixedly installed inside the reaction kettle. The upper end of the mixing cylinder is fixedly installed with a central cylinder through bolts. A mixing device is arranged inside the mixing cylinder and the central cylinder. An outlet pipe is arranged inside the reaction kettle, and a cooling device is arranged between the outlet pipe and the reaction kettle. Through the spraying action of the diversion holes, the sodium methallylsulfonate precursor and the catalyst are fully and evenly mixed. At the same time, when the material flows through the grinding plate, the annular blades effectively grind the particles. The dual effects not only ensure the mixing uniformity but also prevent the material from caking, significantly improving the reaction efficiency and product quality.

Description

Technical Field

[0001] The present invention relates to the technical field of preparation devices for chemicals, and particularly to a preparation device for sodium methallyl sulfonate particles. Background Art

[0002] Sodium methallyl sulfonate (SMAS) is an important functional monomer, which is widely used in fields such as water treatment agents, polymer dispersants, textile printing and dyeing aids, etc. The physical properties of its particle morphology (such as particle size distribution, fluidity, solubility, etc.) have a significant impact on the performance of downstream applications. Currently, the industrial processes for preparing sodium methallyl sulfonate particles mainly include methods such as solution polymerization, spray drying, and crystallization precipitation.

[0003] After retrieval, it is found that the prior art publication number is CN221108234U, which discloses a sodium methallyl sulfonate production device, relating to the technical field of chemical preparation. It includes a tank body and a suction mechanism arranged on one side of the tank body. A preparation tank is arranged inside the tank body, and there is an interlayer for filling coolant between the preparation tank and the tank body. This utility model solves the problem that the existing sodium methallyl sulfonate production device does not handle the waste gas generated during the production process, resulting in the continuous accumulation of waste gas in the reaction tank during the reaction process, and it is easy to cause waste gas leakage during discharging. Through the passive opening of the pressure relief component, while releasing the air pressure inside the preparation tank, it drives the locking component to lock the pressure relief component. At the same time, the negative pressure component generates a negative pressure so that after the air pressure is released, the remaining waste gas inside the preparation tank can continue to be extracted. The extracted waste gas and clear water are sent into the interlayer together, and the hydrogen sulfide therein combines with water to form dilute sulfuric acid for cooling and temperature control of the preparation tank.

[0004] Therefore, based on the above retrieval and combined with the existing technology, during the mixing process of the sodium methallyl sulfonate precursor and the additive in the existing device, there is generally a problem of uneven mixing, resulting in incomplete local reactions. At the same time, the material is prone to caking, and subsequent crushing processes have to be added. When the produced sodium methallyl sulfonate particles are stored in a pile, due to the difficulty of dissipating the heat accumulated between the particles, the local temperature will be too high, which not only affects the fluidity of the product, but also causes thermal damage to the material, ultimately reducing the product purity and key physical performance indicators. For this reason, the present application proposes a preparation device for sodium methallyl sulfonate particles. Summary of the Invention

[0005] The purpose of the present invention is to provide a preparation device for sodium methallyl sulfonate particles to solve the problems raised in the above background art.

[0006] To achieve the above object, the present invention provides the following technical solution: A preparation device for sodium methallylsulfonate particles, including a reaction kettle, the upper end of the reaction kettle is fixedly installed with a sealing cover through bolts, and one end of the sealing cover away from the reaction kettle is fixedly installed with a heating chamber for heating sodium methallylsulfonate through bolts. A material box for loading the precursor of sodium methallylsulfonate is arranged on the left side of the reaction kettle. The bottom end of the material box is fixedly connected with a material pipe, and the output end of the material pipe is connected to the heating chamber. A hot blast stove is arranged on the right side of the reaction kettle. A mixing cylinder is fixedly installed inside the reaction kettle. The upper end of the mixing cylinder is fixedly installed with a central cylinder through bolts. A mixing device is arranged inside the mixing cylinder and the central cylinder for promoting the synthesis of sodium methallylsulfonate. An outlet pipe is arranged inside the reaction kettle, and the outlet pipe is located below the mixing cylinder. A cooling device for preventing sodium methallylsulfonate from overheating is arranged between the outlet pipe and the reaction kettle.

[0007] As a further scheme of the present invention, a scroll fan is rotatably installed inside the heating chamber. The output end of the hot blast stove is fixedly connected with a gas guide pipe, and the output end of the gas guide pipe is fixedly connected to the input end of the heating chamber. The output end of the gas guide pipe corresponds to the side end of the scroll fan, and the output end of the material pipe is aligned with the center position of the scroll fan. The high-speed hot air flow generated by the hot blast stove is accurately introduced into the heating chamber through the gas guide pipe and directly acts on the side end of the scroll fan to form an efficient drive.

[0008] As a further scheme of the present invention, the mixing device includes a central pipe, the central pipe is fixedly connected to the inner bottom end of the central cylinder, a driving rod is rotatably installed inside the central pipe, and one end of the driving rod away from the central pipe is fixedly connected to the scroll fan. The driving rod corresponds to the output end of the material pipe. A plurality of diversion holes are opened at one end of the driving rod close to the scroll fan, and the diversion holes are located inside the central pipe. The power transmission is realized through the linkage design of the central pipe and the driving rod to ensure the stable operation of the scroll fan, and the accurate alignment of the output end of the material pipe realizes the efficient conveying of materials.

[0009] As a further scheme of the present invention, a plurality of stirring and dispersing rods are fixedly installed on the outer surface of the driving rod, a plurality of material dispersing holes are opened on the outer surface of the central pipe, and the stirring and dispersing rods are located above the material dispersing holes. An isolation plate is fixedly installed inside the mixing cylinder, and the isolation plate is located below the central cylinder. A grinding plate is rotatably installed at the inner bottom end of the mixing cylinder, and the grinding plate is located below the isolation plate. One end of the grinding plate close to the isolation plate is fixedly connected with an output pipe, and the output pipe corresponds to the driving rod. A catalyst injection pipe is arranged on the side wall of the mixing cylinder for adding a catalyst to the reaction system.

[0010] As a further solution of the present invention, the cooling device includes a cooling pipe, the cooling pipe is fixedly connected to the outer surface of the discharge pipe, the outer surface of the cooling pipe is fixedly connected to the inner end of the reaction kettle, a conduction pipe for conveying air is arranged through the inner end of the cooling pipe, and a pull ring convenient for grasping is fixedly connected to one end of the conduction pipe away from the discharge pipe. Efficient heat exchange is achieved through the close fit between the cooling pipe and the discharge pipe.

[0011] As a further solution of the present invention, a heating pipe is arranged through the inside of the discharge pipe for detecting the temperature inside the discharge pipe. An unlocking rod is slidably installed at the inner end of the heating pipe, the unlocking rod corresponds to the pull ring, a lifting plate is slidably installed on the outer surface of the cooling pipe, and the lifting plate is fixedly connected to the unlocking rod.

[0012] As a further solution of the present invention, a stabilizing plate is fixedly installed on the outer surface of the discharge pipe, and the stabilizing plate is parallel to the heating pipe. An air outlet is opened at one end of the cooling pipe close to the discharge pipe, and a locking block is arranged through the outer surface of the cooling pipe. The parallel arrangement of the stabilizing plate and the heating pipe ensures the accuracy of temperature detection.

[0013] As a further solution of the present invention, a sliding hole is opened on the outer surface of the locking block, the lifting plate is arranged through the inside of the sliding hole, the lifting plate is arc-shaped, and after the lifting plate moves in the direction away from the discharge pipe, the locking block slides along the outer surface of the arc-shaped lifting plate, so that the locking block moves upward. The cooperation between the sliding hole and the lifting plate realizes precise guidance, and at the same time, the arc-shaped lifting plate design optimizes the mechanical transmission path.

[0014] As a further solution of the present invention, a conduction plug is fixedly connected to one end of the conduction pipe close to the discharge pipe, the locking block corresponds to the conduction plug, an air vent groove is opened on the outer surface of the conduction plug, the air vent groove is communicated with the inside of the conduction pipe, and a sealing ring is fixedly installed at the inner end of the cooling pipe, and the sealing ring is located on the right side of the passive arc plate.

[0015] Compared with the prior art, the beneficial effects of the present invention are:

[0016] 1. When the present invention is used, through the spraying action of the diversion holes, the sodium methallyl sulfonate precursor and the catalyst are fully and evenly mixed. At the same time, when the material flows through the grinding plate, the annular blades effectively grind the particles. The dual effects not only ensure the mixing uniformity but also prevent the material from caking, significantly improving the reaction efficiency and product quality;

[0017] 2. When the present invention is in use, when it is detected that the discharge temperature is too high, the cooling mechanism can be automatically triggered. The deformation of the bimetallic spiral plate drives the unlocking rod to drive the locking block to move, so that the cooling air flow is ejected from the air outlet and directly acts on the high-temperature particles. This design can not only quickly reduce the temperature of the material, but also evenly disperse the particles to the pressure relief holes through the air flow guidance, effectively preventing heat accumulation and ensuring the stable product quality. At the same time, the entire cooling process is completely automatically regulated by the temperature change. BRIEF DESCRIPTION OF THE DRAWINGS

[0018] Figure 1 is a schematic structural diagram of a preparation device for sodium methallylsulfonate particles;

[0019] Figure 2 is a schematic structural diagram of the interior of the reaction kettle;

[0020] Figure 3 is a schematic structural diagram of the interior of the heating chamber;

[0021] Figure 4 is a schematic structural diagram of the interior of the mixing cylinder;

[0022] Figure 5 is a schematic structural diagram of the interior of the central tube;

[0023] Figure 6 is a schematic structural diagram of the positional relationship between the isolation plate and the grinding plate;

[0024] Figure 7 is an exploded view of the output pipe and the passive arc plate;

[0025] Figure 8 is a schematic structural diagram of the interior of the discharge pipe;

[0026] Figure 9 is a schematic structural diagram of the interior of the conduction pipe;

[0027] Figure 10 is a schematic structural diagram of the conduction plug.

[0028] In the figure: 1. Reaction kettle; 2. Air duct; 3. Sealing cover; 4. Heating chamber; 5. Material pipe; 6. Material box; 7. Hot blast stove;

[0029] 101. Central cylinder; 102. Mixing cylinder; 103. Vortex fan; 104. Discharge hole;

[0030] 201. Discharge pipe; 202. Cooling pipe; 203. Pull ring; 204. Heated pipe; 205. Stabilizing plate; 206. Return spring; 207. Locking block; 208. Conduction pipe; 209. Air outlet; 210. Unlocking rod; 211. Lifting plate; 212. Conduction plug; 213. Ventilation groove; 214. Sealing ring;

[0031] 301. Central tube; 302. Driving rod; 303. Isolation plate; 304. Grinding plate; 305. Stirring rod; 306. Diverging hole; 307. Output tube; 308. Passive arc plate; 309. Bulk material hole; 310. Pressure relief hole. Detailed implementation mode

[0032] The following will clearly and completely describe the technical solutions in the embodiments of the present invention with reference to the accompanying drawings in the embodiments of the present invention. Obviously, the described embodiments are only a part of the embodiments of the present invention, rather than all the embodiments. All other embodiments obtained by those of ordinary skill in the art based on the embodiments of the present invention without creative efforts shall fall within the protection scope of the present invention.

[0033] Example 1: Please refer to Figure 1 , Figure 2 , a preparation device for sodium methallyl sulfonate particles, including a reaction kettle 1. The upper end of the reaction kettle 1 is fixedly installed with a sealing cover 3 through bolts. One end of the sealing cover 3 away from the reaction kettle 1 is fixedly installed with a heating chamber 4 for heating sodium methallyl sulfonate through bolts. A material box 6 for loading materials is arranged on the left side of the reaction kettle 1 to add a catalyst to the reaction system. The bottom end of the material box 6 is fixedly connected with a material pipe 5, and the output end of the material pipe 5 is connected to the heating chamber 4. A hot blast stove 7 is arranged on the right side of the reaction kettle 1. The output end of the hot blast stove 7 is fixedly connected with a guide pipe 2, and the output end of the guide pipe 2 is fixedly connected to the input end of the heating chamber 4. The hot blast stove 7 outputs a high-speed hot air flow to dry the sodium methallyl sulfonate. Its working principle adopts the existing mature technology and will not be elaborated here. A mixing cylinder 102 is fixedly installed inside the reaction kettle 1. The upper end of the mixing cylinder 102 is fixedly installed with a central cylinder 101 through bolts. The central cylinder 101 and the mixing cylinder 102 are on the same axis. A mixing device is arranged inside the mixing cylinder 102 and the central cylinder 101 to promote the synthesis of sodium methallyl sulfonate. An outlet pipe 201 is arranged inside the reaction kettle 1. The outlet pipe 201 is located below the mixing cylinder 102. A cooling device for preventing sodium methallyl sulfonate from overheating is arranged between the outlet pipe 201 and the reaction kettle 1.

[0034] As Figure 2 , Figure 3 shown, a scroll fan 103 is rotatably installed inside the heating chamber 4. The output end of the guide pipe 2 corresponds to the side end of the scroll fan 103. The high-speed hot air flow blown out from the hot blast stove 7 is blown out through the guide pipe 2 and drives the scroll fan 103 to rotate. Both the guide pipe 2 and the material pipe 5 are made of metal. The output end of the material pipe 5 is aligned with the center position of the scroll fan 103. A plurality of discharge holes 104 are opened at the inner bottom end of the heating chamber 4. The discharge holes 104 are arranged in a ring shape. When the scroll fan 103 rotates, a hot air flow is blown out in the direction of the discharge holes 104.

[0035] Please refer toFigure 3 - Figure 7 , the mixing device includes a central tube 301, the central tube 301 is fixedly connected to the inner bottom end of the central cylinder 101, a driving rod 302 is rotatably installed at the inner end of the central tube 301, and one end of the driving rod 302 away from the central tube 301 is fixedly connected to the vortex fan 103, and the driving rod 302 corresponds to the output end of the material pipe 5. A plurality of diversion holes 306 are opened at one end of the driving rod 302 close to the vortex fan 103. The diversion holes 306 are located inside the central tube 301, and the diversion holes 306 are arranged in a ring shape for spraying sodium methallylsulfonate flowing here in all directions under the action of the diversion holes 306;

[0036] A plurality of stirring and dispersing rods 305 are fixedly installed on the outer surface of the driving rod 302. A plurality of material dispersing holes 309 are opened on the outer surface of the central tube 301, and the stirring and dispersing rods 305 are located above the material dispersing holes 309. Specifically, when the driving rod 302 rotates, it drives the stirring and dispersing rods 305 to rotate. One end of the stirring and dispersing rod 305 away from the driving rod 302 is fixedly welded with a blade, and the blade maintains a certain inclination angle, so that the sodium methallylsulfonate flowing here is dispersed by the stirring and dispersing rods 305 and then flows out from the material dispersing holes 309 on the outer surface of the central tube 301.

[0037] An isolation plate 303 is fixedly installed at the inner end of the mixing cylinder 102. The isolation plate 303 is spiral. The isolation plate 303 is located below the central cylinder 101. A grinding plate 304 is rotatably installed at the inner bottom end of the mixing cylinder 102. The grinding plate 304 is located below the isolation plate 303. One end of the grinding plate 304 close to the isolation plate 303 is fixedly connected to an output pipe 307. The output pipe 307 corresponds to the driving rod 302. A plurality of rectangular holes are opened at the upper end of the mixing cylinder 102, and the rectangular holes are arranged in a ring shape. The sodium methallylsulfonate flowing out from the material dispersing holes 309 on the outer surface of the central tube 301 is under the rotation action of the vortex fan 103 and moves into the interior of the mixing cylinder 102 along with the direction of the airflow, and a plurality of through holes are opened on the outer surface of the central cylinder 101, and the through holes are arranged in a ring shape;

[0038] Specifically, the output pipe 307 and the bottom end of the driving rod 302 are connected by a plurality of passive arc plates 308. The passive arc plates 308 are arranged in a ring. The outer surface of the passive arc plates 308 is twisted. When rotating, the twisted structure generates an attraction force. Sodium methallylsulfonate is guided by the spiral isolation plate 303 to the upper part of the grinding plate 304, forms a circular motion with the rotation of the grinding plate 304 and the passive arc plates 308, and flows towards the output pipe 307 under the adsorption action when the passive arc plates 308 rotate. A plurality of diversion grooves are opened at the bottom end of the driving rod 302, and the groove openings are facing the passive arc plates 308. The residual sodium methallylsulfonate flows out through the diversion grooves between the driving rod 302 and the central tube 301. Both the passive arc plates 308 and the output pipe 307 are made of metal. A catalyst injection pipe is arranged on the side wall of the mixing cylinder 102 for adding a catalyst to the reaction system;

[0039] More specifically, a plurality of annular blades are fixedly mounted on the upper end of the grinding plate 304. When the grinding plate 304 rotates, the annular blades are driven to rotate. The sodium methacrylate sulfonate contacts the annular blades while flowing on the grinding plate 304, so that the sodium methacrylate sulfonate particles can be further ground to prevent agglomeration during the mixing process. At the same time, the grinding plate 304 rotates to make the mixing process more uniform. The sodium methacrylate sulfonate particles receive the hot air from the turbofan 103 in the chambers of the isolation plate 303 and the grinding plate 304, thereby achieving deep drying.

[0040] Example 2: Please refer to Figure 1 , Figure 8 - Figure 10 , a preparation device of sodium methacrylate sulfonate particles, based on Example 1, the cooling device includes a cooling pipe 202, the cooling pipe 202 is fixedly connected to the outer surface of the discharge pipe 201, the upper end of the discharge pipe 201 is rotatably connected to the bottom end of the grinding plate 304, and the discharge pipe 201 is connected to the output pipe 307, the outer surface of the cooling pipe 202 is fixedly connected to the inner end of the reactor 1, the inner end of the cooling pipe 202 is penetrated with a conducting pipe 208 for conveying air, the inside of the conducting pipe 208 is provided with a filter element for filtering the air entering the reactor 1 from the outside, and the end of the conducting pipe 208 away from the discharge pipe 201 is fixedly connected to a pull ring 203 for easy grasping;

[0041] A heating tube 204 is passed through the discharge tube 201 to detect the internal temperature of the discharge tube 201. The heating tube 204 is "L"-shaped. An unlocking rod 210 is slidably installed on the inner end of the heating tube 204. The unlocking rod 210 corresponds to the pull ring 203. A lifting plate 211 is slidably installed on the outer surface of the cooling tube 202, and the lifting plate 211 is fixedly connected to the unlocking rod 210. Specifically, a bimetallic spiral sheet is provided at the inner end of the heating tube 204. The bottom end of the bimetallic spiral sheet contacts the outer surface of the unlocking rod 210. The bimetallic spiral sheet is formed by overlapping two metal sheets with different thermal expansion coefficients. After heating, due to the different thermal expansion coefficients of the two metals of different materials, the bimetallic spiral sheet begins to twist and pushes the unlocking rod 210 to move in the direction of the pull ring 203.

[0042] A stabilizing plate 205 is fixedly installed on the outer surface of the discharge pipe 201 through a clamp, and the stabilizing plate 205 is parallel to the heat receiving pipe 204. An air outlet 209 is provided at one end of the cooling pipe 202 close to the discharge pipe 201. The diameter of the air outlet 209 is smaller than the diameter of the cooling pipe 202, so that the air flowing out therefrom will be compressed and then quickly dispersed. The temperature of the air will drop rapidly under the effect of adiabatic expansion, thereby playing the effect of cooling the sodium methyl propylene sulfonate particles. A locking block 207 is penetrated on the outer surface of the cooling pipe 202. The locking block 207 and the stabilizing plate 205 are connected by a return spring 206. Under the effect of the elastic force of the return spring 206, the locking block 207 can always maintain the force of moving downward;

[0043] The outer surface of the locking block 207 is provided with a sliding hole, and the lifting plate 211 is arranged inside the sliding hole. The lifting plate 211 is arc-shaped. After the lifting plate 211 moves in a direction away from the discharge pipe 201, the locking block 207 slides along the outer surface of the arc-shaped lifting plate 211, so that the locking block 207 moves upward and compresses the return spring 206.

[0044] A conducting plug 212 is fixedly welded to one end of the conducting tube 208 close to the discharge pipe 201. The diameter of the conducting plug 212 is smaller than the diameter of the conducting tube 208. The locking block 207 corresponds to the conducting plug 212. Under the elastic force of the return spring 206, the bottom end of the locking block 207 is in contact with the outer surface of the conducting plug 212. At this time, the conducting tube 208 is restricted by the locking block 207 and cannot move toward the direction of the discharge pipe 201.

[0045] like Figure 9 , Figure 10 As shown, a ventilation groove 213 is provided on the outer surface of the conducting plug 212, and the ventilation groove 213 is connected to the interior of the conducting pipe 208. A sealing ring 214 is fixedly installed on the inner end of the cooling pipe 202, and the sealing ring 214 is located on the right side of the passive arc plate 308. Specifically, a sealing rubber ring is fixedly installed on the inner end of the sealing ring 214, and fits with the outer surface of the conducting plug 212 to increase the air tightness. When the conducting plug 212 moves in the direction of the discharge pipe 201, the ventilation groove 213 will pass over the sealing ring 214. At this time, air can enter from the conducting pipe 208, pass through the ventilation groove 213, and be ejected from the air outlet 209. A pressure relief hole 310 is provided on the outer surface of the discharge pipe 201, and the pressure relief hole 310 corresponds to the air outlet 209.

[0046] A funnel is fixedly installed at the bottom of the reaction kettle 1 by bolts. The funnel corresponds to the discharge pipe 201 and is used to collect the dried sodium methacrylate sulfonate particles.

[0047] The working principle of the present invention is:

[0048] During use, pour the sodium methallyl sulfonate precursor that needs to react into the interior of the material box 6. Subsequently, start the hot blast stove 7. The hot blast stove 7 outputs a high-speed and high-temperature air flow, which enters the interior of the heating chamber 4 along the air duct 2 and drives the vortex fan 103 inside the heating chamber 4 to rotate. As the vortex fan 103 rotates at a high speed, the pressure inside the heating chamber 4 becomes smaller. At this time, the sodium methallyl sulfonate particles inside the material box 6 enter the interior of the heating chamber 4 along the material pipe 5 under the action of pressure.

[0049] The sodium methallyl sulfonate particles enter the diversion holes 306 at the upper end of the driving rod 302, scatter and fly in all directions under the action of high-speed rotation, enter the interior of the central pipe 301 along with the air flow, and are further dispersed by the rotation of the stirring rod 305 to break up the sodium methallyl sulfonate particles. Subsequently, the sodium methallyl sulfonate particles are ejected from the material dispersion holes 309 on the outer surface of the central pipe 301. The sodium methallyl sulfonate particles ejected from the material dispersion holes 309 quickly move to the upper end of the isolation plate 303 under the action of the air flow generated during the rotation of the vortex fan 103.

[0050] When the driving rod 302 rotates, it drives the output pipe 307 to rotate through the passive arc plate 308. When the driving rod 302 drives the output pipe 307 to rotate through the passive arc plate 308, the passive arc plate 308 generates an attraction force when it rotates. At this time, the sodium methallyl sulfonate particles located above the isolation plate 303 enter above the grinding plate 304 along the curvature of the outer surface of the isolation plate 303 and move in a circular motion as the grinding plate 304 rotates. At the same time, under the rotation of the passive arc plate 308, they move towards the direction of the output pipe 307, enabling them to further mix the sodium methallyl sulfonate precursor with the catalyst. At the same time, it can also prevent caking during the mixing process. Then, it is mixed with the catalyst and reacts, and then is ejected from the bottom end of the discharge pipe 201 and falls into the funnel.

[0051] When the temperature inside the discharge pipe 201 is relatively high, the bimetallic spiral sheet inside the heat receiving pipe 204 is distorted under the action of high temperature and pushes the unlocking rod 210. The unlocking rod 210 moves towards the direction close to the pull ring 203. The unlocking rod 210 drives the lifting plate 211 to move, causing the locking block 207 to move upward and compressing the return spring 206. Since the air flow rate inside the discharge pipe 201 is relatively fast, the air pressure inside is relatively small. At this time, the conduction pipe 208 pushes the conduction plug 212 towards the discharge pipe 201 under the action of air pressure. At this time, the air flows from the ventilation groove 213 to the air outlet 209 and is ejected from it to cool the sodium methallyl sulfonate particles. The air flow blown out from the air outlet 209 blows the sodium methallyl sulfonate particles towards the pressure relief hole 310. When the temperature-reduced sodium methallyl sulfonate particles fall into the funnel, it further avoids the accumulation of high-temperature sodium methallyl sulfonate particles, resulting in the inability to dissipate heat in a timely manner, thereby affecting the product quality.

[0052] As described above, it is only a preferred specific embodiment of the present invention, but the protection scope of the present invention is not limited thereto. Any person skilled in the art within the technical scope disclosed by the present invention, according to the technical solution and inventive concept of the present invention, making equivalent substitutions or changes should be covered within the protection scope of the present invention.

Claims

1. A preparation device for sodium methallyl sulfonate particles, comprising a reaction kettle (1), characterized in that: A sealing cover (3) is fixedly installed at the upper end of the reactor (1). A heating chamber (4) for heating sodium methallyl sulfonate is fixedly installed at one end of the sealing cover (3) away from the reactor (1). A material box (6) for loading the precursor of sodium methallyl sulfonate is arranged on the left side of the reactor (1). The bottom end of the material box (6) is fixedly connected with a material pipe (5), and the output end of the material pipe (5) is connected to the heating chamber (4). A hot blast stove (7) is arranged on the right side of the reactor (1). A mixing cylinder (102) is fixedly installed inside the reactor (1). A central cylinder (101) is fixedly installed at the upper end of the mixing cylinder (102). A mixing device is arranged inside the mixing cylinder (102) and the central cylinder (101) for promoting the synthesis of sodium methallyl sulfonate. An outlet pipe (201) is arranged inside the reactor (1). The outlet pipe (201) is located below the mixing cylinder (102). A temperature reduction device for preventing sodium methallyl sulfonate from overheating is arranged between the outlet pipe (201) and the reactor (1). The temperature reduction device includes a cooling pipe (202). The cooling pipe (202) is fixedly connected to the outer surface of the outlet pipe (201). The outer surface of the cooling pipe (202) is fixedly connected to the inner end of the reactor (1). A conduction pipe (208) for conveying air is arranged inside the inner end of the cooling pipe (202). A heat receiving pipe (204) is arranged inside the outlet pipe (201) for detecting the temperature inside the outlet pipe (201). An unlocking rod (210) is slidably installed at the inner end of the heat receiving pipe (204). The unlocking rod (210) corresponds to a pull ring (203). A lifting plate (211) is slidably installed on the outer surface of the cooling pipe (202), and the lifting plate (211) is fixedly connected to the unlocking rod (210).

2. The preparation device of sodium methallyl sulfonate particles according to claim 1, characterized in that: A scroll fan (103) is rotatably installed inside the heating chamber (4). The output end of the hot blast stove (7) is fixedly connected to a guide pipe (2). The output end of the guide pipe (2) is fixedly connected to the input end of the heating chamber (4). The output end of the guide pipe (2) corresponds to the side end of the scroll fan (103). The output end of the material pipe (5) faces the central position of the scroll fan (103).

3. The preparation device of sodium methallyl sulfonate particles according to claim 1, characterized in that: The mixing device includes a central pipe (301). The central pipe (301) is fixedly connected to the inner bottom end of the central cylinder (101). A driving rod (302) is rotatably installed at the inner end of the central pipe (301). One end of the driving rod (302) away from the central pipe (301) is fixedly connected to the scroll fan (103), and the driving rod (302) corresponds to the output end of the material pipe (5). A plurality of diversion holes (306) are formed at one end of the driving rod (302) close to the scroll fan (103). The diversion holes (306) are located inside the central pipe (301).

4. The preparation device of sodium methallyl sulfonate particles according to claim 3, characterized in that: A plurality of stirring rods (305) are fixedly installed on the outer surface of the driving rod (302). A plurality of material dispersion holes (309) are formed in the outer surface of the central tube (301), and the stirring rods (305) are located above the material dispersion holes (309). An isolation plate (303) is fixedly installed at the inner end of the mixing cylinder (102), and the isolation plate (303) is located below the central cylinder (101). A grinding plate (304) is rotatably installed at the inner bottom end of the mixing cylinder (102), and the grinding plate (304) is located below the isolation plate (303). One end of the grinding plate (304) close to the isolation plate (303) is fixedly connected to an output pipe (307), and the output pipe (307) corresponds to the driving rod (302). A catalyst injection pipe is provided on the side wall of the mixing cylinder (102) for adding a catalyst to the reaction system.

5. The preparation device of sodium methallyl sulfonate particles according to claim 1, characterized in that: A stabilizing plate (205) is fixedly installed on the outer surface of the discharge pipe (201), and the stabilizing plate (205) is parallel to the heating pipe (204). An air outlet (209) is formed at one end of the cooling pipe (202) close to the discharge pipe (201). A locking block (207) is penetrated through the outer surface of the cooling pipe (202).

6. The preparation device of sodium methallyl sulfonate particles according to claim 5, characterized in that: A sliding hole is formed in the outer surface of the locking block (207), and the lifting plate (211) is penetrated through the inside of the sliding hole. The lifting plate (211) is arc-shaped. After the lifting plate (211) moves away from the discharge pipe (201), the locking block (207) slides along the outer surface of the arc-shaped lifting plate (211), so that the locking block (207) moves upward.

7. The preparation device of sodium methallyl sulfonate particles according to claim 6, characterized in that: One end of the conduction pipe (208) close to the discharge pipe (201) is fixedly connected to a conduction plug (212), and the locking block (207) corresponds to the conduction plug (212). An air vent groove (213) is formed in the outer surface of the conduction plug (212), and the air vent groove (213) is communicated with the inside of the conduction pipe (208). A sealing ring (214) is fixedly installed at the inner end of the cooling pipe (202), and the sealing ring (214) is located on the right side of the passive arc plate (308).

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