Environment-friendly ammonium sulfate fertilizer production system

Abstract

The application discloses an environment-friendly ammonium sulfate fertilizer production system and relates to the technical fields of tail gas treatment and chemical fertilizer manufacturing. A receiving and concentrating box is clamped to one side of the top end of the supporting limiting frame, a constant-temperature washing tower is installed at the top end of the receiving and concentrating box, a plurality of repeated reaction cavities are equidistantly formed in the inner side of the constant-temperature washing tower, an absorption and discharge cavity is formed in the inner side of the top end of the constant-temperature washing tower, a plurality of limiting sleeves are clamped to the inner side of the repeated reaction cavity, a plurality of dispersed spray heads are connected to the side end top of the acid liquid injection pipe frame through the adapter, the absorption and discharge cavity, the U-shaped injection pipe, the inlet and outlet matching pipe, the linkage control valve and the injection fan are used to extract the tail gas and inject the tail gas into water, water-soluble ammonia removal is realized, the ammonia removal effect is improved, a plurality of stages of separation and a small amount of continuous mixing reaction are used, the sufficient reaction and treatment of ammonia gas and dilute sulfuric acid in the tail gas are controlled, the stability of the production of ammonium sulfate by tail gas ammonia removal is improved, and the occurrence of resource waste and environmental pollution is reduced.

Description

TECHNICAL FIELD

[0001] The application relates to the technical field of tail gas treatment and chemical fertilizer manufacturing, in particular to an environment-friendly ammonium sulfate fertilizer production system. BACKGROUND

[0002] Ammonium sulfate is an inorganic substance, colorless crystal or white particle, odorless, decomposed above 280 DEG C, soluble in water, insoluble in ethanol and acetone, mainly used as a fertilizer, suitable for general soil and crops, the main production methods of ammonium sulfate fertilizer include by-product method of coking plant, by-product method of synthetic ammonia plant, direct neutralization method, gypsum method and the like, and ammonium sulfate is mainly used for producing quick-acting nitrogen fertilizer, physiological acid fertilizer and sulfur fertilizer in chemical fertilizer production.

[0003] The patent with the application number CN202220464410.1 discloses an ammonia gas absorption tower for ammonium sulfate production, the liquid taking device is arranged on one side of the liquid level pipe, the liquid taking bottle for collecting samples is placed in the positioning groove, and the sealing ring is separated from the clamping part of the positioning rod, under the action of the internal pressure of the absorption tower, the ammonia-containing solution flows out through the through hole of the limiting plate, after the collection is completed, the positioning rod and the sealing ring are re-clamped and sealed under the double action of the spring and the internal liquid pressure, and the ammonia-containing liquid leakage is prevented.

[0004] However, when the existing technology washes and treats the ammonia gas in the tail gas, the reaction of the ammonia gas and the dilute sulfuric acid cannot be effectively controlled, the ammonia gas is prone to be excessive, the ammonia removal efficiency is low, or the dilute sulfuric acid is excessive, the product is changed into ammonium bisulfate, the stability of the tail gas ammonia removal and the stability of the product are greatly affected, resource waste and environmental pollution are caused. SUMMARY

[0005] The application provides an environment-friendly ammonium sulfate fertilizer production system, which can effectively solve the problems in the background art that the reaction of ammonia gas and dilute sulfuric acid cannot be effectively controlled when the existing technology washes and treats the ammonia gas in the tail gas, the ammonia gas is prone to be excessive, the ammonia removal efficiency is low, or the dilute sulfuric acid is excessive, the product is changed into ammonium bisulfate, the stability of the tail gas ammonia removal and the stability of the product are greatly affected, resource waste and environmental pollution are caused.

[0006] To achieve the above-mentioned purpose, the application provides the following technical scheme: an environment-friendly ammonium sulfate fertilizer production system, comprising a whole supporting limiting frame, a plurality of washing and connecting assemblies are arranged at the top end of the whole supporting limiting frame;

[0007] The plurality of washing and connecting assemblies comprise a material collecting and concentrating box;

[0008] The material collecting and concentrating box is arranged at one side of the top end of the whole supporting limiting frame, and a constant-temperature washing tower is installed at the top end of the material collecting and concentrating box;

[0009] The constant temperature washing tower is internally provided with a plurality of repeated reaction cavities at equal intervals, and an absorption outlet cavity is formed at the top end of the constant temperature washing tower;

[0010] A plurality of limiting sleeves are clamped to the inner side of the repeated reaction cavity, and a dispersion porous frame is installed in the inner side of the limiting sleeves;

[0011] A plurality of concentrated upper discharge pipe frames are penetrated at equal intervals at the bottom end of the inner side of two repeated reaction cavities, and an injection operation pipe is penetrated at the side end of one of the repeated reaction cavities;

[0012] An acid injection pipe frame is connected at the side end of the constant temperature washing tower and corresponds to the position of the repeated reaction cavity, and a dispersion spray head is connected at equal intervals at the top of the side end of the acid injection pipe frame through an adapter.

[0013] According to the above technical solution, one end of the concentrated upper discharge pipe frame and one end of the injection operation pipe are both penetrated and sleeved in the middle part of the bottom end of the dispersion porous frame, the longitudinal section of the concentrated upper discharge pipe frame is Y-shaped, and the dispersion spray head is placed in the inner side of the repeated reaction cavity.

[0014] According to the above technical solution, a gas detector is installed at the top end of the inner side of the repeated reaction cavity, an intercepting net plate is installed at the position close to the gas detector on the inner side of the repeated reaction cavity, and a return treatment pipe is connected at the side end of the constant temperature washing tower and corresponds to the position of the repeated reaction cavity;

[0015] A U-shaped injection pipe is connected at the bottom end of the inner side of the absorption outlet cavity, a plurality of liquid separation discharge pipes are connected at equal intervals at the side end of the constant temperature washing tower, and an inlet and outlet matching pipe is connected at the top and the top end of the side end of the constant temperature washing tower;

[0016] A temperature control circulating cavity is formed at the position close to the repeated reaction cavity at the side end of the constant temperature washing tower, and a reciprocating temperature control pipe is connected at the side end of the temperature control circulating cavity in a symmetrical manner.

[0017] An acid storage tank is sleeved at one end of the whole supporting limiting frame, a temperature control circulating tank is installed at the top end of the acid storage tank, and a booster pump is installed at one end of the acid storage tank and the temperature control circulating tank through a motor base.

[0018] According to the above technical solution, one end of the acid injection pipe frame is connected with one end of the booster pump through an adapter, and the longitudinal section of the return treatment pipe is a type, and the bottom end of one of the liquid separation discharge pipes is penetrated in the top end of the material collection and concentration tank.

[0019] According to the above technical solution, a plurality of separation and collection tanks are installed at equal intervals at the position close to the material collection and concentration tank at the top end of the whole supporting limiting frame, and a cold and hot temperature controller is installed in the inner side of the material collection and concentration tank and the temperature control circulating tank.

[0020] The inside top end of the material collecting and concentrating box is provided with a swing motor through a motor base, and the swing motor output shaft is clamped with a swing processing frame.

[0021] A pressure control processing pipe is penetrated through the top end of the material collecting and concentrating box, and a pressure control pump is installed on the top end of the material collecting and concentrating box through a motor base.

[0022] An air pressure detector is embedded and installed on the top end of the material collecting and concentrating box, and an exhaust processing pipe is penetrated through the other side of the top end of the material collecting and concentrating box.

[0023] The other side of the top end of the whole supporting limiting frame is symmetrically clamped with a lifting hydraulic cylinder, and the top end of the lifting hydraulic cylinder is provided with a lifting load-bearing block.

[0024] The top end of the lifting load-bearing block is provided with a switching motor through a motor base, and the switching motor output shaft is provided with a switching operation frame.

[0025] The inside of the switching operation frame is symmetrically embedded with a positioning electromagnet, and the inside of the switching operation frame is symmetrically clamped with a load-bearing crystallization plate, and the bottom end of the load-bearing crystallization plate is provided with a plurality of crystallization processing ropes.

[0026] According to the above technical solution, the centralized upper exhaust pipe frame, the injection operation pipe, the acid liquid injection pipe frame, the U-shaped injection pipe, the liquid distribution exhaust pipe, the inlet and outlet matching pipe, the reciprocating temperature control pipe and the exhaust treatment pipe are provided with a linkage control valve at one end, and the centralized upper exhaust pipe frame, the injection operation pipe, the return processing pipe, the U-shaped injection pipe and the exhaust treatment pipe are provided with an injection fan inside.

[0027] The one end of the reciprocating temperature control pipe is penetrated and installed at one end of the temperature control circulating box, and the one end of the reciprocating temperature control pipe is connected with the one end of the booster pump through an adapter, and the swing processing frame is rotationally installed inside the material collecting and concentrating box.

[0028] According to the above technical solution, the exhaust treatment pipe is penetrated and installed at one end of the temperature control circulating box, and the positioning electromagnet is magnetically connected with the load-bearing crystallization plate.

[0029] The input ends of the gas detector, the booster pump, the cold and hot temperature controller, the swing motor, the pressure control pump, the air pressure detector, the lifting hydraulic cylinder, the switching motor, the positioning electromagnet, the linkage control valve and the injection fan are electrically connected with the output end of the external controller.

[0030] The input end of the external controller is electrically connected with the output end of the external power supply.

[0031] According to the above technical solution, the top end of the whole supporting limiting frame is provided with a material stripping and washing assembly.

[0032] The material stripping and washing assembly comprises an inlet and outlet electric sliding rail.

[0033] The top end of the whole supporting limiting frame is symmetrically provided with an in-out electric sliding rail, and the top end of the in-out electric sliding rail is provided with an in-out positioning plate through a sliding rail seat.

[0034] The top end of the in-out positioning plate is embedded with a fixed electromagnet, and the top end of the fixed electromagnet is magnetically attracted to be provided with a collection and treatment box.

[0035] One end of the collection and treatment box is clamped with an isolation electric sliding rail, and the top end of the isolation electric sliding rail is provided with an isolation blocking plate through a sliding rail seat.

[0036] The inside of the collection and treatment box is symmetrically provided with a pressure release electric sliding rail, and one end of the pressure release electric sliding rail is provided with a pressure release treatment plate through a sliding rail seat.

[0037] One end of the inside of the collection and treatment box is embedded with a discharging electric sliding rail, and one end of the discharging electric sliding rail is provided with a discharging scraper through a sliding rail seat.

[0038] One end of the whole supporting limiting frame is provided with a dissolution treatment box, and one end of the collection and treatment box and the dissolution treatment box is connected with a compression sealing cover through a spring hinge, and one end of the collection and treatment box and the dissolution treatment box is clamped with a sealing electromagnet corresponding to the position of the compression sealing cover.

[0039] According to the above technical scheme, the top end of the dissolution treatment box is penetrated by a hot liquid feeding pipe, the middle of the top end of the dissolution treatment box is provided with a dissolution motor through a motor seat, and the output shaft of the dissolution motor is clamped with a mixing stirring frame.

[0040] The top end of the dissolution treatment box is connected with an external discharge operation pipe, and the top end of the dissolution treatment box is provided with an external discharge pump corresponding to the top end of the external discharge operation pipe through a motor seat.

[0041] One end of the dissolution treatment box is clamped with a double-cavity filtrate tank, and the double-cavity filtrate tank is provided with a vacuum filter at one end.

[0042] The inside of the double-cavity filtrate tank is provided with a limiting net plate in the middle, the top end of the limiting net plate is provided with an adsorption net cage, and the inside of the double-cavity filtrate tank is clamped with a cooling condenser away from the adsorption net cage.

[0043] The top end of the in-out positioning plate is attached to the bottom end of the collection and treatment box, the isolation blocking plate is slidingly sleeved at one end of the collection and treatment box, and the pressure release treatment plate and the discharging scraper are placed in the inside of the collection and treatment box.

[0044] According to the above technical scheme, one end of the external discharge operation pipe is inserted into one end of the double-cavity filtrate tank, and the compression sealing cover is magnetically attracted to the sealing electromagnet.

[0045] The input terminals of the inlet / outlet electric slide rail, fixed electromagnet, isolation electric slide rail, depressurization electric slide rail, discharge electric slide rail, sealing electromagnet, dissolving motor, external discharge pump, vacuum filter, and cooling condenser are all electrically connected to the output terminal of an external controller.

[0046] Compared with the prior art, the beneficial effects of the present invention are as follows:

[0047] 1. Multiple scrubbing components are installed. The intake speed of the exhaust gas is controlled by the injection operation pipe, the dispersion multi-hole frame, the linkage control valve, and the injection fan. This, combined with small-hole intake, large-hole diversion, and small-hole counter-flushing, disperses the exhaust gas. The amount and speed of injected dilute sulfuric acid are controlled by the acid injection pipe frame, dispersion spray heads, acid storage tank, booster pump, and linkage control valve. The sprayed dilute sulfuric acid forms a rain curtain, which contacts the exhaust gas. By increasing the contact area, the rising speed of ammonia in the exhaust gas is slowed, maximizing contact. A small amount of dilute sulfuric acid is used to continuously flush the reaction. A gas detector monitors the concentration of ammonia flowing to the top, and the gas is then returned for further processing. The pipe and injection fan drive the high-concentration ammonia gas at the top to flow back to the bottom, realizing a cyclic reaction treatment. The multi-chamber segmented treatment increases the reaction time and controls the reaction volume. In conjunction with the repeated reaction chamber at the top, excess dilute sulfuric acid is used to treat the small amount of ammonia remaining in the tail gas, achieving complete ammonia removal. The tail gas is extracted and injected into water using the absorption exhaust chamber, U-shaped injection pipe, inlet and outlet pipes, linkage control valve, and injection fan, achieving water-soluble ammonia removal and improving the ammonia removal effect. Through multi-stage separation and small-scale continuous mixing reaction, the full reaction of ammonia gas and dilute sulfuric acid in the tail gas is controlled, improving the stability of ammonia removal and production of ammonium sulfate, and reducing resource waste and environmental pollution.

[0048] 2. The ammonium sulfate solution and ammonium bisulfate solution are separated by a liquid-liquid drain pipe and then collected in a receiving and concentrating tank and a separation and collection tank. The receiving and concentrating tank is heated and cooled by a temperature controller, and the internal pressure of the receiving and concentrating tank is controlled by a pressure control pipe and a pressure control pump to achieve temperature-controlled concentration. The unsaturated ammonium sulfate solution is concentrated into a supersaturated solution. The lifting hydraulic cylinder and the switching motor drive the switching operation frame, the load-bearing crystallization plate and the crystallization rope to be inserted into the inside of the receiving and concentrating tank. At this time, the cooling and crystallization guidance process is used to achieve rapid crystallization of the ammonium sulfate solution, ensuring the stability of continuous production and continuous processing.

[0049] 3. Through the intake velocity control, exhaust velocity control and exhaust collision processing, by circulating linkage intake and exhaust, a small amount of dilute sulfuric acid repeated washing reaction, excessive dilute sulfuric acid fully deamination treatment, water soluble ammonia absorption treatment, segmented separation and external discharge treatment, low pressure medium temperature evaporation concentration and normal pressure low temperature guided crystallization, effectively solve the existing technology, ammonia gas in the tail gas washing, unable to control the reaction of ammonia and dilute sulfuric acid, resulting in unstable product and incomplete ammonia reaction, reduce the amount of dilute sulfuric acid, while avoiding ammonia excessive discharge, thereby avoiding the direct discharge of ammonia gas resulting in environmental pollution, while ensuring the stability of the product, reduce resource waste, improve the speed and stability of ammonium sulfate production.

[0050] 4. The material is removed from the filter washing assembly, which moves the inlet and outlet positioning plate and the collection and processing box by driving the inlet and outlet electric sliding rail. The pressure removal treatment plate is inserted into the top of the side end of the crystallization treatment rope, and the pressure removal electric sliding rail drives the pressure removal treatment plate to press and separate the ammonium sulfate crystals adhered to the side end of the crystallization treatment rope. The discharge electric sliding rail drives the discharge scraper to push the ammonium sulfate crystals into the inside of the dissolution treatment box. Finally, the ammonium sulfate crystals are pushed into the dissolution treatment box. The pressure removal treatment and the movement of the discharge treatment are inserted to press and separate the ammonium sulfate crystals and crush the treatment, which is convenient for subsequent crystal dissolution and purification treatment, and improves the convenience of subsequent treatment.

[0051] Hot water is injected into the dissolution treatment box through the hot liquid injection pipe, and the ammonium sulfate crystals and hot water are mixed and dissolved by the dissolution motor and the mixing and stirring frame. The ammonium sulfate solution is extracted by the discharge pump and the discharge operation pipe and injected into the double cavity filtrate box. The activated carbon adsorbent in the adsorption net cage and the limiting net plate are used to remove the solution. The vacuum filter is used for vacuum filtration treatment, and the cooling condenser is used for cooling crystallization treatment, which improves the purity of ammonium sulfate and ensures the speed and stability of subsequent granulation.

[0052] In summary, through the cooperation of multiple washing and crystallization assemblies and material removal and filtration assemblies, multiple reaction treatments, multiple discharge treatments, concentrated crystallization production, hot dissolution stirring treatment, interception adsorption slag removal and vacuum suction filtration treatment are used to realize the full reaction and purification of ammonium sulfate, improve the purity of ammonium sulfate, ensure the stability of product production and the stability of subsequent granulation, and fully absorb the reaction to remove ammonia gas in the tail gas, avoid the direct discharge of ammonia gas resulting in environmental pollution, and improve the steady protection of the environment during tail gas treatment and fertilizer production. BRIEF DESCRIPTION OF DRAWINGS

[0053] The accompanying drawings are included to provide a further understanding of the application, and constitute a part of the specification. They are used to explain the application together with embodiments of the application, and do not constitute a limitation of the application.

[0054] In the drawings:

[0055] Figure 1 is a schematic diagram of the stereoscopic structure of the present application;

[0056] Figure 2 is a schematic diagram of the structure of the multiple washing and knotting assembly of the present application;

[0057] Figure 3 is a schematic diagram of the installation structure of the injection operation pipe of the present application;

[0058] Figure 4 is a schematic diagram of the installation structure of the concentrated upper row pipe rack of the present application;

[0059] Figure 5 is a schematic diagram of the installation structure of the acid liquid storage tank of the present application;

[0060] Figure 6 is a schematic diagram of the installation structure of the load-bearing crystallization plate of the present application;

[0061] Figure 7 is a schematic diagram of the structure of the material removal and washing assembly of the present application;

[0062] Figure 8 is a schematic diagram of the installation structure of the access positioning plate of the present application;

[0063] Figure 9 is a schematic diagram of the installation structure of the fixed electromagnet of the present application;

[0064] Figure 10 is a schematic diagram of the installation structure of the external row pump of the present application;

[0065] Figure label: 1, whole support limiting rack;

[0066] 2. Multiple washing and condensation components; 201. Receiving and concentrating tank; 202. Constant temperature washing tower; 203. Repeated reaction chamber; 204. Absorption and discharge chamber; 205. Multi-row limiting sleeve; 206. Dispersion porous rack; 207. Centralized upper pipe rack; 208. Injection operation pipe; 209. Acid injection pipe rack; 210. Dispersion spray head; 211. Gas detector; 212. Interceptor plate; 213. Return processing pipe; 214. U-shaped injection pipe; 215. Separating and discharge pipe; 216. Inlet and outlet matching pipe; 217. Temperature-controlled circulation chamber; 218. Reciprocating temperature control pipe; 19. Acid storage tank; 220. Temperature-controlled circulation tank; 221. Booster pump; 222. Separation and collection tank; 223. Temperature controller; 224. Swing motor; 225. Swing processing rack; 226. Pressure-controlled processing pipe; 227. Pressure-controlled pump; 228. Air pressure detector; 229. Exhaust processing pipe; 230. Lifting hydraulic cylinder; 231. Lifting load-bearing block; 232. Switching motor; 233. Switching operating frame; 234. Positioning electromagnet; 235. Load-bearing crystallizing plate; 236. Crystallization processing rope; 237. Linkage control valve; 238. Injection fan;

[0067] 3. Material removal and filtration assembly; 301. Inlet / outlet electric slide rail; 302. Inlet / outlet positioning plate; 303. Fixing electromagnet; 304. Collection and processing box; 305. Isolation electric slide rail; 306. Isolation baffle plate; 307. Press-out electric slide rail; 308. Press-out processing plate; 309. Discharge electric slide rail; 310. Discharge scraper; 311. Dissolving treatment tank; 312. Press-fit sealing cover; 313. Sealing electromagnet; 314. Hot liquid input pipe; 315. Dissolving motor; 316. Mixing and stirring rack; 317. External discharge operation pipe; 318. External discharge pump; 319. Dual-chamber filtrate tank; 320. Vacuum filter; 321. Limiting mesh plate; 322. Adsorption mesh cage; 323. Cooling condenser. Detailed Implementation

[0068] The preferred embodiments of the present invention will be described below with reference to the accompanying drawings. It should be understood that the preferred embodiments described herein are for illustration and explanation only and are not intended to limit the present invention.

[0069] Example: Figures 1-10 As shown, the present invention provides a technical solution, an environmentally friendly ammonium sulfate fertilizer production system, including a support and limiting frame 1, with multiple washing and settling components 2 provided at the top of the support and limiting frame 1;

[0070] The multiple washing assembly 2 includes a material collection and concentration box 201, a constant temperature washing tower 202, a repeated reaction cavity 203, an absorption and exhaust cavity 204, a multi-row limiting sleeve 205, a dispersed porous frame 206, a concentrated upper exhaust pipe frame 207, an injection operation pipe 208, an acid liquid injection pipe frame 209, a dispersed spray head 210, a gas detector 211, an interception net plate 212, a return treatment pipe 213, a U-shaped injection pipe 214, a separated exhaust pipe 215, an inlet and outlet matching pipe 216, a temperature control circulating cavity 217, a reciprocating temperature control pipe 218, an acid liquid storage box 219, a temperature control circulating box 220, a booster pump 221, a separation and collection box 222, a cold and hot temperature controller 223, a swing motor 224, a swing treatment frame 225, a pressure control treatment pipe 226, a pressure control pump 227, a gas pressure detector 228, an exhaust treatment pipe 229, a lifting hydraulic cylinder 230, a lifting load-bearing block 231, a switching motor 232, a switching operation frame 233, a positioning electromagnet 234, a load-bearing crystallization plate 235, a crystallization treatment rope 236, a linkage control valve 237, and an injection fan 238;

[0071] The top end of the whole supporting limiting frame 1 is connected with the material collection and concentration box 201 on one side, and the top end of the material collection and concentration box 201 is provided with the constant temperature washing tower 202;

[0072] A plurality of repeated reaction cavities 203 are equidistantly arranged in the inner side of the constant temperature washing tower 202, and the inner side of the constant temperature washing tower 202 is provided with the absorption and exhaust cavity 204 at the top end;

[0073] The repeated reaction cavity 203 is connected with the multi-row limiting sleeve 205 on the inner side, and the multi-row limiting sleeve 205 is provided with the dispersed porous frame 206 on the inner side;

[0074] The bottom end of the repeated reaction cavity 203 is equidistantly penetrated by a plurality of concentrated upper exhaust pipe frames 207 on the inner side, and the longitudinal section of the concentrated upper exhaust pipe frame 207 is Y-shaped, which realizes the stable linkage of accelerating the air inlet and decelerating the air exhaust, and improves the stability of the internal air pressure control. The side end of one repeated reaction cavity 203 is penetrated by the injection operation pipe 208, and one end of the concentrated upper exhaust pipe frame 207 and one end of the injection operation pipe 208 are penetrated and connected to the middle part of the bottom end of the dispersed porous frame 206, which realizes the air inlet connection, and the injected tail gas and ammonia gas are processed in sections, realizing the gas deceleration and dispersed contact treatment;

[0075] The acid liquid injection pipe frame 209 is connected at the position corresponding to the repeated reaction cavity 203 on the side end of the constant temperature washing tower 202, and the dispersed spray head 210 is connected to the top end of the acid liquid injection pipe frame 209 through the adapter, and the dispersed spray head 210 is placed in the repeated reaction cavity 203, which realizes the stable spraying and mixing, and guarantees the stable treatment of the tail gas ammonia removal;

[0076] The gas detector 211 is installed at the top end of the inside of the repeated reaction cavity 203, the intercepting screen plate 212 is installed at the position close to the gas detector 211 of the inside of the repeated reaction cavity 203, the return treatment pipe 213 is connected at the position corresponding to the repeated reaction cavity 203 of the side end of the constant-temperature washing tower 202, the longitudinal section of the return treatment pipe 213 is in the shape of a Chinese character “Fang”, and the stability of the circulation linkage is ensured;

[0077] The U-shaped injection pipe 214 is connected at the bottom end of the inside of the absorption and discharge cavity 204, the several liquid separation and discharge pipes 215 are equidistantly connected at the side end of the constant-temperature washing tower 202, one of the liquid separation and discharge pipes 215 is connected at the top end of the material receiving and concentrating box 201, the stable liquid separation and discharge treatment is realized, the stable recovery of the ammonium sulfate solution is ensured, and the inlet and outlet matching pipes 216 are connected at the top and the side end of the constant-temperature washing tower 202;

[0078] The temperature control circulation cavity 217 is arranged at the position close to the repeated reaction cavity 203 of the side end of the constant-temperature washing tower 202, and the reciprocating temperature control pipes 218 are symmetrically connected at the side end of the temperature control circulation cavity 217;

[0079] The acid liquid storage box 219 is sleeved at one end of the whole supporting limiting frame 1, the temperature control circulation box 220 is installed at the top end of the acid liquid storage box 219, one end of the reciprocating temperature control pipe 218 is connected at one end of the temperature control circulation box 220, the stable temperature control circulation treatment is realized, the stability of the temperature control is improved, the booster pump 221 is installed at one end of the acid liquid storage box 219 and one end of the temperature control circulation box 220 through the motor base, one end of one of the reciprocating temperature control pipes 218 is connected to one end of the booster pump 221 through the adapter, and the stable liquid injection treatment is realized;

[0080] The several separation and collection boxes 222 are equidistantly installed at the position close to the material receiving and concentrating box 201 of the top end of the whole supporting limiting frame 1, and the cold and hot temperature controllers 223 are installed at the inside of the material receiving and concentrating box 201 and the temperature control circulation box 220;

[0081] The swing motor 224 is installed at the top end of the inside of the material receiving and concentrating box 201 through the motor base, the swing treatment frame 225 is connected to the output shaft of the swing motor 224, the swing treatment frame 225 is rotatably installed at the inside of the material receiving and concentrating box 201, the stirring and heat evaporation treatment is realized, and the concentration speed of the ammonium sulfate is ensured;

[0082] The pressure control treatment pipe 226 is penetrated at one side of the top end of the material receiving and concentrating box 201, and the pressure control pump 227 is installed at the position corresponding to the pressure control treatment pipe 226 of the top end of the material receiving and concentrating box 201 through the motor base;

[0083] The air pressure detector 228 is embedded and installed on one side of the top end of the material receiving and concentrating box 201, and the exhaust treatment pipe 229 is penetrated through the other side of the top end of the material receiving and concentrating box 201, one end of the exhaust treatment pipe 229 is penetrated and installed on one end of the temperature control circulating box 220, so as to improve the stability of the concentrated exhaust;

[0084] The lifting hydraulic cylinders 230 are symmetrically clamped on the other side of the top end of the whole supporting limiting frame 1, and the lifting load bearing blocks 231 are installed on the top ends of the two lifting hydraulic cylinders 230;

[0085] The switching motor 232 is installed on the top end of the lifting load bearing block 231 through the motor base, and the switching operation frame 233 is installed on the output shaft of the switching motor 232;

[0086] The positioning electromagnets 234 are symmetrically embedded in the inner side of the switching operation frame 233, the load bearing crystallization plates 235 are symmetrically clamped on the inner side of the switching operation frame 233, the positioning electromagnets 234 are magnetically connected with the load bearing crystallization plates 235, the stable and fixed limiting of the positioning crystallization is realized, the speed of the crystallization is improved, and the crystallization treatment ropes 236 are equidistantly installed on the bottom end of the load bearing crystallization plate 235;

[0087] The linkage control valves 237 are installed on one end of the concentrated upper discharge pipe frame 207, the injection operation pipe 208, the acid liquid injection pipe frame 209, the U-shaped injection pipe 214, the liquid distribution outer discharge pipe 215, the in-out matching pipe 216, the reciprocating temperature control pipe 218 and the exhaust treatment pipe 229, and the injection fans 238 are installed on the inner sides of the concentrated upper discharge pipe frame 207, the injection operation pipe 208, the return treatment pipe 213, the U-shaped injection pipe 214 and the exhaust treatment pipe 229;

[0088] In order to realize the stable operation of the equipment, the input ends of the gas detector 211, the booster pump 221, the cold and hot temperature controller 223, the swing motor 224, the pressure control pump 227, the air pressure detector 228, the lifting hydraulic cylinder 230, the switching motor 232, the positioning electromagnet 234, the linkage control valve 237 and the injection fan 238 are electrically connected with the output end of the external controller;

[0089] The input end of the external controller is electrically connected with the output end of the external power supply.

[0090] The material stripping and filtering assembly 3 is arranged on the top end of the whole supporting limiting frame 1;

[0091] The material removal filter washing assembly 3 comprises an in-out electric sliding rail 301, an in-out positioning plate 302, a fixed electromagnet 303, a collection treatment box 304, an isolation electric sliding rail 305, an isolation blocking plate 306, a pressure removal electric sliding rail 307, a pressure removal treatment plate 308, a discharge electric sliding rail 309, a discharge scraper 310, a dissolution treatment box 311, a compression sealing cover 312, a sealing electromagnet 313, a hot liquid input pipe 314, a dissolution motor 315, a mixing stirring frame 316, an external discharge operation pipe 317, an external discharge pump 318, a double-cavity filtrate box 319, a vacuum filter 320, a limiting mesh plate 321, an adsorption mesh cage 322 and a cooling condenser 323.

[0092] The in-out electric sliding rail 301 is symmetrically installed at one side of the top end of the whole supporting limiting frame 1, and the in-out positioning plate 302 is installed at the top end of the in-out electric sliding rail 301 through a sliding rail seat.

[0093] The fixed electromagnet 303 is embedded at the top end of the in-out positioning plate 302, and the collection treatment box 304 is magnetically attracted and installed at the top end of the fixed electromagnet 303.

[0094] The isolation electric sliding rail 305 is connected at one end of the collection treatment box 304, and the isolation blocking plate 306 is installed at the top end of the isolation electric sliding rail 305 through a sliding rail seat.

[0095] The pressure removal electric sliding rail 307 is symmetrically installed inside the collection treatment box 304, and the pressure removal treatment plate 308 is installed at one end of the pressure removal electric sliding rail 307 through a sliding rail seat.

[0096] The discharge electric sliding rail 309 is embedded at one end inside the collection treatment box 304, and the discharge scraper 310 is installed at one end of the discharge electric sliding rail 309 through a sliding rail seat. The top end of the in-out positioning plate 302 is attached to the bottom end of the collection treatment box 304, the isolation blocking plate 306 is slidingly sleeved at one end of the collection treatment box 304, the pressure removal treatment plate 308 and the discharge scraper 310 are both placed inside the collection treatment box 304, stable discharging and material removal treatment are realized, and recovery treatment is realized on the crystallized ammonium sulfate.

[0097] The dissolution treatment box 311 is installed at one end of the whole supporting limiting frame 1, the compression sealing cover 312 is connected at one end of the collection treatment box 304 and the dissolution treatment box 311 through a spring hinge, the sealing electromagnet 313 is connected at the position corresponding to the compression sealing cover 312 at one end of the collection treatment box 304 and the dissolution treatment box 311, the compression sealing cover 312 is magnetically attracted and combined with the sealing electromagnet 313, and the stability of magnetic attraction fixation is ensured.

[0098] The hot liquid input pipe 314 penetrates through one side of the top end of the dissolution treatment box 311, the dissolution motor 315 is installed at the middle of the top end of the dissolution treatment box 311 through a motor seat, and the mixing stirring frame 316 is connected to the output shaft of the dissolution motor 315.

[0099] The top end of the dissolving treatment box 311 is connected with an external discharge operation pipe 317, and the top end of the dissolving treatment box 311 is provided with an external discharge pump 318 through a motor base corresponding to the top end of the external discharge operation pipe 317.

[0100] One end of the dissolving treatment box 311 is connected with a double-cavity filtrate box 319, and one end of the external discharge operation pipe 317 is inserted into the double-cavity filtrate box 319 to realize stable liquid discharge treatment.

[0101] The double-cavity filtrate box 319 is provided with a limiting net plate 321 at the middle of the inner side, and the top end of the limiting net plate 321 is provided with an adsorption net cage 322.

[0102] In order to realize stable operation of the equipment, the input ends of the in-out electric sliding rail 301, the fixed electromagnet 303, the isolation electric sliding rail 305, the pressure release electric sliding rail 307, the discharge electric sliding rail 309, the sealing electromagnet 313, the dissolving motor 315, the external discharge pump 318, the vacuum filter 320 and the cooling condenser 323 are electrically connected with the output end of the external controller.

[0103] The working principle and use process of the application are as follows: when the tail gas after washing and desulfurization is subjected to ammonia gas adsorption treatment, the staff pours 20% to 30% dilute sulfuric acid into the acid liquid storage box 219, and pours water used for temperature control into the temperature control circulating box 220, at this time, the water is heated to 80 DEG C by the cold and hot temperature controller 223, the hot water in the temperature control circulating box 220 is extracted by the booster pump 221 and the reciprocating temperature control pipe 218, and the hot water is injected into the temperature control circulating cavity 217, so that the temperature control treatment is carried out on the constant temperature washing tower 202, and the internal temperature is always kept between 70 DEG C and 80 DEG C, and the temperature of the water in the temperature control circulating box 220 is adjusted to keep the internal temperature constant, so that the reaction speed and the dissolution rate are improved.

[0104] When the temperature adjustment is completed, the tail gas is extracted by the injection operation pipe 208 and the injection fan 238, and is injected into the dispersion porous frame 206 along the injection operation pipe 208, the tail gas is subjected to shunt treatment by the dispersion porous frame 206, and when the tail gas is injected into the dispersion porous frame 206, the gas flow space is increased and the gas flow speed is reduced, and when the tail gas is discharged, the gas flow is accelerated and collides with each other due to the limitation of the exhaust hole, so that the turbulent flow is formed, thereby slowing down the gas flow speed, and reducing the speed of the tail gas discharge and the uniformity of the tail gas dispersion.

[0105] At this time, the dilute sulfuric acid inside the acid liquid storage tank 219 is extracted by the booster pump 221 and the acid liquid injection pipe frame 209, and the dilute sulfuric acid is sprayed upwards along the acid liquid injection pipe frame 209 and the dispersion spray head 210, forming a rain curtain. When the ammonia tail gas enters the first repeated reaction chamber 203, the injection amount of dilute sulfuric acid is controlled according to the ammonia content in the tail gas. At this time, the ammonia is excessive, the dilute sulfuric acid is less, and the dilute sulfuric acid and the ammonia are fully reacted to generate ammonium sulfate. The tail gas continues to flow upwards, slows down and condenses through the interception net plate 212, and then moves to the position of the gas detector 211. The gas detector 211 detects the ammonia content in the rising tail gas. When the ammonia concentration is high, the top tail gas is recycled and discharged to the bottom by the injection fan 238 and the return treatment pipe 213. At this time, the tail gas reacts with dilute sulfuric acid again to produce ammonium sulfate;

[0106] When the ammonia concentration is low, the injection operation pipe 208 is closed by the linkage control valve 237, and at the same time the concentrated upper discharge pipe frame 207 is opened by the linkage control valve 237. At this time, the ammonia in the first repeated reaction chamber 203 is extracted by the injection fan 238 and the concentrated upper discharge pipe frame 207 and injected into the inside of the dispersion porous frame 206 to realize ammonia discharge. At this time, the dilute sulfuric acid is sprayed by the dispersion spray head 210 in the second repeated reaction chamber 203, and the amount of dilute sulfuric acid is controlled according to the ammonia content to generate ammonium sulfate again. At the same time, the gas detector 211 in the first repeated reaction chamber 203 continuously detects the ammonia at the top end. When the ammonia concentration is lower than the detection value, the injection operation pipe 208 is opened and the concentrated upper discharge pipe frame 207 is closed. In the reaction process, the ammonia flows upwards along the bottom of the repeated reaction chamber 203 and finally flows to the position of the gas detector 211 for detection again. When the ammonia content is excessive, the top ammonia is recycled and returned to the bottom by the return treatment pipe 213 and the injection fan 238. At this time, the ammonia flows upwards again to react with dilute sulfuric acid to generate ammonium sulfate. Through the internal circulation of ammonia and the control of the spraying amount of dilute sulfuric acid, stable production of ammonium sulfate is realized, and the generation of ammonium bisulfate due to excessive dilute sulfuric acid is avoided;

[0107] When the ammonia content in the second repeated reaction chamber 203 is low, the concentrated upper exhaust pipe frame 207 in the third repeated reaction chamber 203 is opened at this time, and the tail gas is discharged into the third repeated reaction chamber 203 by cooperating with the injection fan 238. At this time, the ammonia gas still flows upward from the bottom, and the excess dilute sulfuric acid is injected into the third repeated reaction chamber 203 through the dispersion spray head 210, so that the ammonia gas contained therein is fully reacted to generate ammonium bisulfate, and the ammonia gas is detected by cooperating with the gas detector 211, and the internal ammonia gas is circulated by the return treatment pipe 213 and the injection fan 238, so that the ammonia gas is repeatedly reacted and removed. When the ammonia content in the third repeated reaction chamber 203 is lower than the detection value, water is injected into the absorption exhaust chamber 204 through the inlet and outlet matching pipe 216, and the tail gas is injected into the water through the U-shaped injection pipe 214 by opening the linkage control valve 237. By utilizing the characteristics that ammonia gas is easily dissolved in water, the remaining small amount of ammonia gas in the tail gas is fully absorbed, the tail gas is fully purified, ammonium sulfate and ammonium bisulfate are produced, and finally the tail gas is discharged through the inlet and outlet matching pipe 216. By using multi-stage reaction to fully remove ammonia and absorb ammonia, the ammonia in the tail gas is removed, environmental pollution caused by direct discharge of ammonia is avoided, and the polluted gas is converted into nitrogen fertilizer to realize resource recycling;

[0108] The liquid separation exhaust pipe 215 at the position of the repeated reaction chamber 203 is opened by the linkage control valve 237, the ammonium sulfate solution is discharged into the material collection and concentration box 201, and the ammonium bisulfate solution is discharged into the inside of the separation and collection box 222, so as to realize solution discharge treatment. The ammonium sulfate solution is heated by the cold and hot temperature controller 223, and at this time, the gas pressure in the material collection and concentration box 201 is reduced by cooperating with the pressure control treatment pipe 226 and the pressure control pump 227. By using pressure reduction and temperature rise evaporation treatment, the solution is continuously evaporated at an environment of 70°C by controlling the internal pressure, so as to avoid the occurrence of ammonium sulfate tapping due to too high temperature. The switching operation frame 233 is rotated along the lifting load block 231 by cooperating with the switching motor 232, the load crystallization plate 235 is magnetically fixed by the positioning electromagnet 234, the lifting load block 231 and the switching operation frame 233 are lowered by cooperating with the lifting hydraulic cylinder 230, the crystallization treatment rope 236 is placed inside the material collection and concentration box 201, and the material collection and concentration box 201 is sealed by cooperating with the switching operation frame 233 and the load crystallization plate 235, so as to ensure the stability of the pressure control treatment. In the process of heat evaporation, the water vapor evaporated inside is extracted by the exhaust treatment pipe 229 and the injection fan 238, and is injected into the temperature control circulation box 220.

[0109] The solution stirring treatment is promoted by rotating the swing treatment frame 225 driven by the swing motor 224, the solution is fully thermal evaporated, the unsaturated ammonium sulfate solution is converted into the supersaturated ammonium sulfate solution, when the solution is supersaturated, the solution starts to crystallize under the guidance of the crystallization treatment rope 236, at this time, the temperature in the material collection and concentration box 201 is reduced to 10℃ by the cold and hot temperature controller 223, the crystallization efficiency and the crystallization amount are improved, when the crystallization is completed, the load crystallization plate 235 is rotated and moved to the position of the collection treatment box 304 by the lifting hydraulic cylinder 230 and the switching motor 232, the replacement treatment of the crystallization treatment rope 236 is realized, the stability and efficiency of the continuous crystallization are ensured, and the steady production of ammonium sulfate is realized;

[0110] When the crystallization treatment rope 236 accumulated with ammonium sulfate is rotated and moved to the position of the collection treatment box 304, at this time, the collection treatment box 304 is placed at the top end of the in-out positioning plate 302, the collection treatment box 304 and the in-out positioning plate 302 are magnetically attracted and fixed by the fixed electromagnet 303, the in-out electric slide rail 301 drives the in-out positioning plate 302 and the collection treatment box 304 to move, the pressing and stripping treatment plate 308 is moved and inserted into the top of the side end of the crystallization treatment rope 236, the isolation blocking plate 306 is moved by the isolation electric slide rail 305, the collection treatment box 304 is sealed, the pressing and stripping treatment plate 308 is moved along the collection treatment box 304 by the pressing and stripping electric slide rail 307, the ammonium sulfate crystals adhered to the side end of the crystallization treatment rope 236 are pressed and stripped, the ammonium sulfate crystals are pressed into the inside of the collection treatment box 304, after the discharging is completed, the discharging electric slide rail 309 drives the discharging scraper 310 to move along the collection treatment box 304, the ammonium sulfate crystals are pushed into the inside of the dissolution treatment box 311, in the pushing process, the two pressing and sealing covers 312 are respectively rotated along the collection treatment box 304 and the dissolution treatment box 311, finally the ammonium sulfate crystals are pushed into the dissolution treatment box 311, under the action of the spring hinge, the pressing and sealing cover 312 is reset, at this time, the pressing and sealing cover 312 is magnetically attracted and fixed by the sealing electromagnet 313, the steady discharging treatment is realized, the crystallized ammonium sulfate is quickly discharged, and the stability of the material cleaning is improved;

[0111] The hot water with the temperature of 70 DEG C is injected into the dissolving treatment box 311 through the hot liquid injection pipe 314, and the mixing stirring frame 316 is rotated by the dissolving motor 315, so as to push the ammonium sulfate crystals and the hot water to mix and dissolve, and the ammonium sulfate crystals containing part of impurities are dissolved into ammonium sulfate solution. At this time, the ammonium sulfate solution in the dissolving treatment box 311 is extracted by the external discharge pump 318 and the external discharge operation pipe 317, and is injected into the inside of the double-cavity filtrate box 319. The colored matters such as phenols and tar containing impurities are separated from the solution by the activated carbon adsorbent in the adsorption net cage 322, and the fine particles containing impurities in the solution are screened and removed by the limiting net plate 321, so as to realize the steady filtration treatment. At this time, the vacuum filter 320 is used for liquid extraction and filtration treatment, and the ammonium sulfate solution is discharged into the cooling condenser 323 for cooling and crystallization treatment, so as to improve the purity of the ammonium sulfate and ensure the speed and stability of subsequent granulation.

[0112] Finally, it should be noted that: the above only for the preferred examples of the present application, and not for limiting the present application, although the present application is described in detail with reference to the foregoing examples, for those skilled in the art, it still can be modified, or part of the technical features of the equivalent replacement. Any modification, equivalent replacement, improvement, etc. within the spirit and principles of the present application, should be included in the protection scope of the present application.

Claims

1. An environmentally friendly ammonium sulfate fertilizer production system comprising a whole supporting limiting frame (1), characterized in that: The whole support limiting frame (1) is provided with multiple washing and knotting assemblies (2) at the top end; The multiple washing and knotting assemblies (2) comprise a material collecting and concentrating box (201); The material collecting and concentrating box (201) is connected at one side of the top end of the whole support limiting frame (1), and a constant-temperature washing tower (202) is installed at the top end of the material collecting and concentrating box (201); A plurality of repeated reaction cavities (203) are equidistantly formed in the inner side of the constant-temperature washing tower (202), and an absorption and external discharge cavity (204) is formed at the top end of the inner side of the constant-temperature washing tower (202); A plurality of limiting sleeves (205) are connected at the inner side of the repeated reaction cavity (203), and a dispersion porous frame (206) is installed at the inner side of the limiting sleeve (205); A plurality of concentrated upward discharge pipe frames (207) are equidistantly penetrated at the bottom end of the inner side of two repeated reaction cavities (203), and an injection operation pipe (208) is penetrated at the side end of one repeated reaction cavity (203); An acid liquid injection pipe frame (209) is connected and penetrated at the side end of the constant-temperature washing tower (202) at the position corresponding to the repeated reaction cavity (203), and a dispersion spray head (210) is connected through an adapter at the top of the side end of the acid liquid injection pipe frame (209); A return treatment pipe (213) is connected and penetrated at the side end of the constant-temperature washing tower (202) at the position corresponding to the repeated reaction cavity (203); A U-shaped injection pipe (214) is connected and penetrated at the bottom end of the inner side of the absorption and external discharge cavity (204), a plurality of liquid separation and external discharge pipes (215) are equidistantly connected and penetrated at the side end of the constant-temperature washing tower (202), and an inlet and outlet matching pipe (216) is connected and penetrated at the top and the top end of the side end of the constant-temperature washing tower (202); A temperature control circulating cavity (217) is formed at the position close to the repeated reaction cavity (203) at the side end of the constant-temperature washing tower (202), and reciprocating temperature control pipes (218) are symmetrically connected and penetrated at the side end of the temperature control circulating cavity (217); An acid liquid storage box (219) is sleeved at one end of the whole support limiting frame (1), a temperature control circulating box (220) is installed at the top end of the acid liquid storage box (219), and a booster pump (221) is installed at one end of the acid liquid storage box (219) and the temperature control circulating box (220) through a motor base.

2. The environmentally friendly ammonium sulfate fertilizer production system according to claim 1, characterized in that, One end of the concentrated upward discharge pipe frame (207) and one end of the injection operation pipe (208) are both penetrated and sleeved in the middle part of the bottom end of the dispersion porous frame (206), the longitudinal section of the concentrated upward discharge pipe frame (207) is Y-shaped, and the dispersion spray head (210) is placed in the inner side of the repeated reaction cavity (203).

3. The environmentally friendly ammonium sulfate fertilizer production system according to claim 1, characterized in that, A gas detector (211) is installed at the top end of the inner side of the repeated reaction cavity (203), and an interception net plate (212) is installed at the position close to the gas detector (211) at the inner side of the repeated reaction cavity (203).

4. The environmentally friendly ammonium sulfate fertilizer production system according to claim 3, characterized in that, One end of the acid liquid injection pipe frame (209) is connected with one end of the booster pump (221) through an adapter, the longitudinal section of the return treatment pipe (213) is a type, and the bottom end of one liquid separation and external discharge pipe (215) is penetrated in the top end of the material collecting and concentrating box (201).

5. The environmentally friendly ammonium sulfate fertilizer production system according to claim 3, characterized in that, The whole support limiting frame (1) top end near the collection concentration tank (201) position equidistantly installs several separate collection tanks (222), the collection concentration tank (201) and the temperature control circulating tank (220) inside all are installed cold and hot temperature controller (223); The inside top of the collection concentration tank (201) is installed with a swing motor (224) through a motor base, and the output shaft of the swing motor (224) is connected with a swing processing frame (225); The top of the collection concentration tank (201) is penetrated by a pressure control processing pipe (226), and the top of the collection concentration tank (201) is installed with a pressure control pump (227) through a motor base corresponding to the position of the pressure control processing pipe (226); The top of the collection concentration tank (201) is embedded with a gas pressure detector (228), and the top of the collection concentration tank (201) is penetrated by an exhaust treatment pipe (229); The other side of the top of the whole support limiting frame (1) is symmetrically connected with a lifting hydraulic cylinder (230), and the top of the two lifting hydraulic cylinders (230) is installed with a lifting bearing block (231); The top of the lifting bearing block (231) is installed with a switching motor (232) through a motor base, and the output shaft of the switching motor (232) is installed with a switching operation frame (233); The inside of the switching operation frame (233) is symmetrically embedded with a positioning electromagnet (234), and the inside of the switching operation frame (233) is symmetrically connected with a bearing crystallization plate (235), and the bottom of the bearing crystallization plate (235) is installed with several crystallization processing ropes (236) equidistantly.

6. The environmentally friendly ammonium sulfate fertilizer production system according to claim 5, characterized in that, The one end of the concentrated upper exhaust pipe frame (207), the injection operation pipe (208), the acid liquid injection pipe frame (209), the U-shaped injection pipe (214), the liquid separation exhaust pipe (215), the in-out matching pipe (216), the reciprocating temperature control pipe (218) and the exhaust treatment pipe (229) is installed with a linkage control valve (237), and the inside of the concentrated upper exhaust pipe frame (207), the injection operation pipe (208), the return processing pipe (213), the U-shaped injection pipe (214) and the exhaust treatment pipe (229) is installed with an injection fan (238); The one end of the reciprocating temperature control pipe (218) is installed in one end of the temperature control circulating tank (220), and the one end of one of the reciprocating temperature control pipes (218) is connected with the one end of the booster pump (221) through an adapter, and the swing processing frame (225) is rotatably installed in the inside of the collection concentration tank (201).

7. The environmentally friendly ammonium sulfate fertilizer production system according to claim 6, characterized in that, The one end of the exhaust treatment pipe (229) is installed in one end of the temperature control circulating tank (220), and the positioning electromagnet (234) is magnetically connected with the bearing crystallization plate (235); The input end of the gas detector (211), the booster pump (221), the cold and hot temperature controller (223), the swing motor (224), the pressure control pump (227), the gas pressure detector (228), the lifting hydraulic cylinder (230), the switching motor (232), the positioning electromagnet (234), the linkage control valve (237) and the injection fan (238) is electrically connected with the output end of the external controller; The input end of the external controller is electrically connected with the output end of the external power supply.

8. The environmentally friendly ammonium sulfate fertilizer production system according to claim 7, characterized in that, The whole support limiting frame (1) is provided with a material stripping and filtering assembly (3) at the top end; The material stripping and filtering assembly (3) comprises an in-out electric sliding rail (301); The in-out electric sliding rail (301) is symmetrically installed at one side of the top end of the whole support limiting frame (1), and the in-out positioning plate (302) is installed at the top end of the in-out electric sliding rail (301) through a sliding rail seat; The fixed electromagnet (303) is embedded at the top end of the in-out positioning plate (302), and the collection and treatment box (304) is magnetically attracted and installed at the top end of the fixed electromagnet (303); The isolation electric sliding rail (305) is connected at one end of the collection and treatment box (304), and the isolation blocking plate (306) is installed at the top end of the isolation electric sliding rail (305) through a sliding rail seat; The pressure stripping electric sliding rail (307) is symmetrically installed at the inner side of the collection and treatment box (304), and the pressure stripping treatment plate (308) is installed at one end of the pressure stripping electric sliding rail (307) through a sliding rail seat; The discharge electric sliding rail (309) is embedded at one end of the inner side of the collection and treatment box (304), and the discharge scraper (310) is installed at one end of the discharge electric sliding rail (309) through a sliding rail seat; The dissolution treatment box (311) is installed at one end of the whole support limiting frame (1), the spring hinge is connected between one end of the collection and treatment box (304) and one end of the dissolution treatment box (311), and the sealing electromagnet (313) is connected at the position corresponding to the compression sealing cover (312) of one end of the collection and treatment box (304) and one end of the dissolution treatment box (311).

9. The environmentally friendly ammonium sulfate fertilizer production system according to claim 8, characterized in that, The hot liquid feeding pipe (314) penetrates through one side of the top end of the dissolution treatment box (311), the dissolution motor (315) is installed at the middle of the top end of the dissolution treatment box (311) through a motor seat, and the mixed stirring frame (316) is connected to the output shaft of the dissolution motor (315); The external discharge operation pipe (317) penetrates and connects the top end of the dissolution treatment box (311), and the external discharge pump (318) is installed at the top end of the dissolution treatment box (311) through a motor seat corresponding to the top end of the external discharge operation pipe (317); The double-cavity filtrate tank (319) is connected at one end of the dissolution treatment box (311), and the vacuum filter (320) is installed at one end of the double-cavity filtrate tank (319); The limiting net plate (321) is installed at the middle of the inner side of the double-cavity filtrate tank (319), the adsorption net cage (322) is installed at the top end of the limiting net plate (321), and the cooling condenser (323) is connected at the position away from the adsorption net cage (322) of the inner side of the double-cavity filtrate tank (319); The top end of the in-out positioning plate (302) is attached to the bottom end of the collection and treatment box (304), the isolation blocking plate (306) is slidingly connected at one end of the collection and treatment box (304), and the pressure stripping treatment plate (308) and the discharge scraper (310) are placed in the inner side of the collection and treatment box (304).

10. The environmentally friendly ammonium sulfate fertilizer production system according to claim 9, characterized in that, The external discharge operation pipe (317) is inserted and installed at one end of the double-cavity filtrate tank (319), and the compression sealing cover (312) and the sealing electromagnet (313) are magnetically attracted and combined; The input end of the access electric slide rail (301), the fixed electromagnet (303), the isolation electric slide rail (305), the pressure-off electric slide rail (307), the discharge electric slide rail (309), the sealing electromagnet (313), the dissolving motor (315), the external discharge pump (318), the vacuum filter (320) and the cooling condenser (323) are electrically connected with the output end of the external controller.

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