A distillation and purification equipment for methanol production

Abstract

The present invention belongs to the technical field of distillation and purification, and specifically is a distillation and purification device for methanol production, comprising a heating mechanism, a water storage mechanism, a condensing mechanism, a preheating mechanism, a cooling mechanism, and a platform. A water storage mechanism is provided to provide circulating condensed water, and a magnetic suction-type boosting device is provided. By adding an electromagnet to adsorb the boosting valve plate, and by using a venturi to suck the condensed water in the boosting water tank, the condensed water can be pressurized without additional boosting equipment, and the electromagnet is added by the pressure control in the condensing chamber, thereby changing the pressure of the condensed water according to the condensation efficiency; a condensing mechanism is provided to adsorb the metal suction plate by adjusting the electromagnet, and the resistance rotor is driven to rotate by the metal suction plate, thereby changing the diffusion direction of the methanol vapor in the condensing chamber, and utilizing the characteristic that the methanol vapor is a viscous fluid to form a vortex, thereby prolonging the condensation time of the methanol vapor, thereby improving the condensation efficiency.

Description

Technical Field

[0001] The invention belongs to the technical field of distillation and purification, and specifically relates to a distillation and purification device for methanol production. Background Art

[0002] Methanol distillation is a refining process that separates methanol mixtures through heating and condensation. Because methanol's boiling point (64.7°C) is significantly lower than that of water (100°C) and some organic impurities, the boiling point difference between methanol and other components can be exploited for purification. During initial production, methanol may be mixed with other organic impurities and water, necessitating distillation to improve purity.

[0003] During the methanol distillation process, the volume of gas formed after the unit volume of liquid evaporates due to heat increases, causing the pressure in the distillation kettle to increase. As the pressure continues to rise, the rate of methanol vapor overflow will accelerate, resulting in the inability of methanol vapor to pass through the condenser at a constant low flow rate. Methanol vapor will flow into the methanol storage tank along with liquid methanol. Storage tanks are usually designed to store liquids. If a gas-liquid mixture enters, the pressure in the tank will increase, causing the tank to deform or the seal to fail, or even leak. In addition, gaseous methanol may re-condense in the tank, releasing heat, and also affecting the temperature change of the tank. Summary of the Invention

[0004] In view of the above situation, in order to overcome the defects of the prior art, the present invention provides a distillation and purification equipment for methanol production to solve the technical problem of low condensation efficiency of traditional distillation equipment.

[0005] The technical solution adopted by the present invention is as follows: The present invention provides a distillation and purification equipment for methanol production, including a heating mechanism, a water storage mechanism, a condensing mechanism, a preheating mechanism, a cooling mechanism and a platform. The condensing mechanism is installed above the platform, the heating mechanism is arranged on one side of the condensing mechanism, the water storage mechanism is arranged on the other side of the condensing mechanism, the preheating mechanism is arranged behind the condensing mechanism, and the cooling mechanism is arranged behind the water storage mechanism.

[0006] Furthermore, the heating mechanism includes a heating base, a heating control system, a heating cover and a raw liquid tank. The heating base is installed above the platform, the heating control system is arranged on one side of the heating base, the heating cover is arranged in the heating base, the raw liquid tank is arranged in the heating cover, and the heating control system is electrically connected to the heating cover.

[0007] Furthermore, a steam delivery pipe is provided on the top of the raw liquid tank, a waste discharge channel is provided on the bottom of the raw liquid tank, a waste discharge valve is provided on the waste discharge channel, a raw liquid delivery pipe is connected to the side wall of the raw liquid tank, a delivery valve is provided on the raw liquid delivery pipe, a heating liquid level gauge is provided on the top of the raw liquid tank, the measuring end of the heating liquid level gauge is located at the bottom of the raw liquid tank, and the heating liquid level gauge is used to detect the liquid content in the raw liquid tank.

[0008] Furthermore, the water storage mechanism includes a bottom water tank, a boosting water tank, a condensing water pump, a bottom water pipe, a bottom water inlet pipe, a boosting water inlet pipe and a boosting water pipe. The bottom water tank is installed above the platform, the boosting water tank is arranged above the bottom water tank, the bottom water pipe is connected to the bottom of the bottom water tank, the condensing water pump is arranged above the platform, the condensing water pump is also connected to the bottom water pipe, the bottom water inlet pipe is connected to the top of the bottom water tank, a bottom water valve is provided on the bottom water inlet pipe, the boosting water inlet pipe is connected to the top of the boosting water tank, the boosting water pipe is connected to the bottom of the boosting water tank, and a boosting water valve is provided on the boosting water inlet pipe.

[0009] Furthermore, a magnetic boosting device is installed on one side of the bottom water tank, and the magnetic boosting device includes a Venturi tube, a boosting branch pipe, a boosting valve plate, a closing spring and an increasing electromagnet. The Venturi tube is arranged on one side of the bottom water tank, and the boosting branch pipe is connected to the middle part of the Venturi tube. A boosting slide shaft is provided in the boosting branch pipe, and the boosting valve plate is slidably arranged on the boosting slide shaft. The lower end of the closing spring is fixedly connected to the boosting valve plate, and the upper end of the closing spring is fixedly connected to the inner wall of the boosting branch pipe. The increasing electromagnet is arranged at the top of the boosting branch pipe. When the increasing electromagnet is started, it will adsorb the boosting valve plate and squeeze the closing spring.

[0010] Furthermore, a cooling water level gauge is provided in each of the bottom water tank and the boost water tank, and the cooling water level gauge can detect the liquid content in the bottom water tank and the boost water tank respectively.

[0011] Furthermore, the condensation mechanism includes a condensation chamber, a heat-conducting water chamber, a top heat-conducting baffle, a resistance shaft, a resistance rotor, a transmission gear, an adjustment rotating rod, a metal suction plate, an adjustment electromagnet, a top chamber water inlet pipe, a top chamber drain pipe, a collection tank, a siphon, a condensation drain pipe and a condensation water inlet pipe. The condensation chamber is installed above the platform, the heat-conducting water chamber is arranged in the condensation chamber, the top heat-conducting baffle is arranged at the bottom of the heat-conducting water chamber, the resistance shaft is rotatably arranged on the condensation chamber, the resistance rotor is arranged on the resistance shaft, the transmission gear is arranged on the resistance shaft, the adjustment rotating rod is slidably arranged on the condensation chamber, and the adjustment rotating rod is provided with a transmission rack The transmission rack is meshed with the transmission gear, one end of the return spring is fixed to the adjusting rotating rod, and the other end of the return spring is fixed to the condensing chamber. The metal suction piece is provided on the adjusting rotating rod, and the adjusting electromagnet is provided on the condensing chamber. The top cabin water inlet pipe is connected to the heat conducting tank, and the top cabin drain pipe is connected to the heat conducting tank. The collecting tank is provided in the condensing chamber, the siphon pipe is connected to the collecting tank, the condensing drain pipe is connected to the top cabin water inlet pipe, and the condensing water inlet pipe is connected to the top cabin drain pipe. The methanol vapor will gather under the top heat conducting partition, and the heat of the methanol vapor will be transferred to the heat conducting tank through the top heat conducting partition.

[0012] Furthermore, a condensation pressure gauge is provided on the condensation chamber, a measuring end of the condensation pressure gauge is inside the condensation chamber, and the condensation pressure gauge is used to monitor the pressure inside the condensation chamber.

[0013] Furthermore, the preheating mechanism includes a preheating base, a preheating inner tank, a preheating water injection channel, a preheating drainage channel, heat-conducting fins, an insulating outer cabin, a preheating water pipe and a cooling water pump. The preheating base is installed above the platform, the insulating outer cabin is arranged above the preheating base, the preheating inner tank is arranged in the insulating outer cabin, the heat-conducting fins are arranged on the outside of the preheating inner tank, the preheating water pipe is arranged on the heat-conducting fins, the preheating drainage channel is connected to the preheating inner tank, the preheating water injection channel is connected to the preheating inner tank, the preheating drainage channel is connected to a preheating delivery pump, the cooling water pump is installed above the platform, the preheating water pipe is connected to the cooling water pump, and after the condensed water flows back to the preheating water pipe, the heat of the condensed water will be transferred to the heat-conducting fins, and then the heat-conducting fins will transfer the heat to the preheating inner tank, recovering the waste heat and preheating the original liquid.

[0014] Furthermore, a raw liquid level gauge is provided on the heat-insulating outer cabin, and a measuring end of the raw liquid level gauge is located inside the preheating inner tank.

[0015] Furthermore, the cooling mechanism includes a cooling cabin, a cooling grid, a cooling fan, a cooling drain pipe, a cooling water inlet pipe, a filtered water pump, a resin ion filter and a storage water pump. The cooling cabin is installed above the platform, the cooling grid is arranged in the cooling cabin, the cooling fan is arranged on the top of the cooling cabin, the cooling drain pipe is connected to the cooling grid, the cooling water inlet pipe is connected to the cooling grid, the cooled drain pipe is connected to the filtered water pump, the resin ion filter is arranged on one side of the cooling cabin, the cooling drain pipe is connected to the water inlet of the resin ion filter, the storage water pump is installed above the platform, and the water outlet of the resin ion filter is connected to the storage water pump. By lowering the temperature of the condensed water, more heat can be absorbed during the condensed water circulation process, thereby improving the condensation efficiency of methanol vapor.

[0016] Furthermore, the water outlet of the storage water pump is connected to a storage water pipe, and the storage water pipe is communicated with the bottom water inlet pipe and the boost water inlet pipe at the same time.

[0017] Furthermore, the cooling water inlet pipe is connected to the preheating water pipe, and the preheating water pipe is connected to the condensation drain pipe.

[0018] Furthermore, the condensation water inlet pipe is connected to a venturi tube.

[0019] Furthermore, the steam delivery pipeline is communicated with the condensation chamber.

[0020] Furthermore, the raw liquid delivery pipeline is communicated with the preheating drainage channel.

[0021] The beneficial effects of a distillation and purification equipment for methanol production provided by this solution are as follows:

[0022] (1) A heating mechanism is provided to quickly heat the raw liquid, and the electric heating method makes the heating temperature more accurate, which can effectively separate components with different boiling points. The electric heating directly heats the raw liquid tank through electromagnetic induction, without the need for external fuel combustion, which significantly reduces the risk of fire;

[0023] (2) A water storage mechanism is provided to provide circulating condensed water, and a magnetic suction boosting device is provided. By adding an electromagnet to absorb the boosting valve plate, and by using a venturi to suck the condensed water in the boosting water tank, the condensed water can be pressurized without additional boosting equipment. The pressure in the condensing chamber controls the addition of the electromagnet, thereby changing the pressure of the condensed water according to the condensation efficiency.

[0024] (3) The condensation mechanism is set up to adjust the electromagnet to adsorb the metal suction piece, and the power (suction force) of the electromagnet is controllable and adjustable. The resistance rotor is driven by the metal suction piece to rotate, thereby changing the diffusion direction of the methanol vapor in the condensation chamber. The characteristic of methanol vapor as a viscous fluid is used to form a vortex at the intersection, and the overall diffusion speed becomes slow, thereby extending the condensation time of the methanol vapor and improving the condensation efficiency.

[0025] (4) Setting up a preheating mechanism to use the condensed water that absorbs the heat of methanol vapor to preheat the raw liquid can reduce the consumption of external energy (electricity). The raw liquid needs to be preheated to a certain temperature before it can evaporate efficiently. If it is preheated by condensed water, some of the high energy consumption heating stages can be directly skipped, thus speeding up the distillation process.

[0026] (5) Setting up a cooling mechanism to further cool the condensed water can increase the amount of heat that can be absorbed by a unit volume of cooling water, thereby improving the heat exchange efficiency between the condensed water and methanol vapor. BRIEF DESCRIPTION OF THE DRAWINGS

[0027] Figure 1 This is a schematic structural diagram of a distillation and purification device for methanol production proposed by the present invention;

[0028] Figure 2 A top view of a distillation and purification device for methanol production proposed by the present invention;

[0029] Figure 3 A front view of a distillation and purification device for methanol production proposed by the present invention;

[0030] Figure 4 This is a rear view of a distillation and purification device for methanol production proposed by the present invention;

[0031] Figure 5 It is a structural diagram of the heating mechanism;

[0032] Figure 6 This is a cross-sectional view of the original liquid tank;

[0033] Figure 7 It is a structural diagram of the water storage mechanism;

[0034] Figure 8 It is a cross-sectional view of a magnetic supercharging device;

[0035] Figure 9 It is a partial structural cross-sectional view of the water storage mechanism;

[0036] Figure 10 It is a partial structural diagram of the condensation mechanism;

[0037] Figure 11 Schematic diagram of the external transmission structure of the condensing mechanism;

[0038] Figure 12 is a cross-sectional view of the condensation chamber;

[0039] Figure 13 This is the transmission relationship diagram of the condensing mechanism;

[0040] Figure 14 It is a structural diagram of the preheating mechanism;

[0041] Figure 15 This is a cross-sectional view of the thermal insulation outer cabin;

[0042] Figure 16 Schematic diagram of the structure of the preheating water pipe;

[0043] Figure 17 It is a cross-sectional view of the preheating tank;

[0044] Figure 18 It is a partial structural diagram of the cooling mechanism;

[0045] Figure 19 A cross-sectional view of the cooling chamber.

[0046] Among them, 1. Heating mechanism, 2. Water storage mechanism, 3. Condensation mechanism, 4. Preheating mechanism, 5. Cooling mechanism, 6. Platform, 101. Heating base, 102. Heating control system, 103. Heating cover, 104. Raw liquid tank, 105. Raw liquid delivery pipeline, 106. Delivery valve, 107. Heating level gauge, 108. Steam delivery pipeline, 109. Waste discharge channel, 110. Waste discharge valve, 201. Bottom water tank, 202. Booster water tank, 203. Cooling Condensate pump, 204, bottom water pipe, 205, bottom water inlet pipe, 206, booster water inlet pipe, 207, booster water pipe, 208, magnetic booster device, 209, Venturi tube, 210, booster branch pipe, 211, booster valve plate, 212, closing spring, 213, additional electromagnet, 214, booster water valve, 215, bottom water valve, 216, cooling water level gauge, 217, booster slide shaft, 301, condensation chamber, 302, heat conduction chamber, 303, top conduction chamber Heat baffle, 304, resistance shaft, 305, resistance rotor, 306, transmission gear, 307, adjustment rotation rod, 308, return spring, 309, metal suction piece, 310, adjustment electromagnet, 311, top cabin water inlet pipe, 312, top cabin drain pipe, 313, transmission rack, 314, collection tank, 315, siphon, 316, condensation drain pipe, 317, condensation water inlet pipe, 318, condensation pressure gauge, 401, preheating base, 402, preheating liner, 4 03. Preheating water injection channel, 404. Preheating drainage channel, 405. Preheating transfer pump, 406. Heat transfer fins, 407. Insulated outer cabin, 408. Preheating water pipe, 409. Cooling water pump, 410. Raw liquid level gauge, 501. Cooling cabin, 502. Cooling grid, 503. Cooling fan, 504. Cooling drainage pipe, 505. Cooling water inlet pipe, 506. Filter water pump, 507. Resin ion filter, 508. Storage water pump, 509. Storage water pipe.

[0047] The accompanying drawings are used to provide further understanding of the present invention and constitute a part of the specification. They are used to explain the present invention together with the embodiments of the present invention and do not constitute a limitation of the present invention. DETAILED DESCRIPTION

[0048] The technical solutions in the embodiments of the present invention will be clearly and completely described below in conjunction with the accompanying drawings. Obviously, the described embodiments are only part of the embodiments of the present invention, rather than all the embodiments; based on the embodiments of the present invention, all other embodiments obtained by ordinary technicians in this field without making creative work are within the scope of protection of the present invention.

[0049] In the description of the present invention, it should be understood that terms such as "upper", "lower", "front", "back", "left", "right", "top", "bottom", "inside" and "outside" indicating directions or positional relationships are based on the directions or positional relationships shown in the accompanying drawings. They are only for the convenience of describing the present invention and simplifying the description, and do not indicate or imply that the device or element referred to must have a specific direction, be constructed and operated in a specific direction. Therefore, they should not be understood as limiting the present invention.

[0050] like Figures 1-19 As shown, the present invention provides a distillation and purification device for methanol production. The present invention provides a distillation and purification device for methanol production, comprising a heating mechanism 1, a water storage mechanism 2, a condensing mechanism 3, a preheating mechanism 4, a cooling mechanism 5, and a platform 6. The condensing mechanism 3 is installed above the platform 6, the heating mechanism 1 is arranged on one side of the condensing mechanism 3, the water storage mechanism 2 is arranged on the other side of the condensing mechanism 3, the preheating mechanism 4 is arranged behind the condensing mechanism 3, and the cooling mechanism 5 is arranged behind the water storage mechanism 2.

[0051] The heating mechanism 1 includes a heating base 101, a heating control system 102, a heating cover 103 and a raw liquid tank 104. The heating base 101 is installed above the platform 6, the heating control system 102 is arranged on one side of the heating base 101, the heating cover 103 is arranged in the heating base 101, and the raw liquid tank 104 is arranged in the heating cover 103; a steam delivery pipe 108 is provided at the top of the raw liquid tank 104, a waste discharge channel 109 is provided at the bottom of the raw liquid tank 104, and a waste discharge valve 110 is provided on the waste discharge channel 109. A raw liquid delivery pipe 105 is connected to the side wall of the raw liquid tank 104, and a delivery valve 106 is provided on the raw liquid delivery pipe 105. A heating liquid level gauge 107 is provided at the top of the raw liquid tank 104, and the measuring end of the heating liquid level gauge 107 is located at the bottom of the raw liquid tank 104.

[0052] The water storage mechanism 2 includes a bottom water tank 201, a boosting water tank 202, a condensing water pump 203, a bottom water pipe 204, a bottom water inlet pipe 205, a boosting water inlet pipe 206 and a boosting water pipe 207. The bottom water tank 201 is installed above the platform 6, the boosting water tank 202 is arranged above the bottom water tank 201, the bottom water pipe 204 is connected to the bottom of the bottom water tank 201, the condensing water pump 203 is arranged above the platform 6, the condensing water pump 203 is also connected to the bottom water pipe 204, the bottom water inlet pipe 205 is connected to the top of the bottom water tank 201, and the bottom water valve 215 is provided on the bottom water inlet pipe 205. The boosting water inlet pipe 206 is connected to the top of the boosting water tank 202, the boosting water pipe 207 is connected to the bottom of the boosting water tank 202, and the boosting water inlet pipe 206 is provided with a bottom valve 215. Booster water valve 214; a magnetic boosting device 208 is installed on one side of the bottom water tank 201, and the magnetic boosting device 208 includes a Venturi tube 209, a boosting branch pipe 210, a boosting valve plate 211, a closing spring 212 and an additional electromagnet 213. The Venturi tube 209 is arranged on one side of the bottom water tank 201, and the boosting branch pipe 210 is connected to the middle part of the Venturi tube 209. A boosting slide shaft 217 is provided in the boosting branch pipe 210, and the boosting valve plate 211 is slidably provided on the boosting slide shaft 217. The lower end of the closing spring 212 is fixedly connected to the boosting valve plate 211, and the upper end of the closing spring 212 is fixedly connected to the inner wall of the boosting branch pipe 210. The additional electromagnet 213 is provided at the top of the boosting branch pipe 210; a cooling water level gauge 216 is respectively provided in the bottom water tank 201 and the boosting water tank 202.

[0053] The condensing mechanism 3 includes a condensing chamber 301, a heat-conducting water chamber 302, a top heat-conducting baffle 303, a resistance rotating shaft 304, a resistance rotating piece 305, a transmission gear 306, an adjusting rotating rod 307, a metal suction piece 309, an adjusting electromagnet 310, a top chamber water inlet pipe 311, a top chamber drain pipe 312, a collecting tank 314, a siphon 315, a condensation drain pipe 316 and a condensation water inlet pipe 317. The condensing chamber 301 is installed above the platform 6, the heat-conducting water chamber 302 is arranged in the condensing chamber 301, the top heat-conducting baffle 303 is arranged at the bottom of the heat-conducting water chamber 302, the resistance rotating shaft 304 is rotatably arranged on the condensing chamber 301, the resistance rotating piece 305 is arranged on the resistance rotating shaft 304, the transmission gear 306 is arranged on the resistance rotating shaft 304, the adjusting rotating rod 307 is slidably arranged on the condensing chamber 301, and the adjusting rotating piece 306 is arranged on the resistance rotating shaft 304. A transmission rack 313 is provided on the movable rod 307, which is meshed with the transmission gear 306. One end of the return spring 308 is fixed to the adjusting rotating rod 307, and the other end of the return spring 308 is fixed to the condensing chamber 301. A metal suction piece 309 is provided on the adjusting rotating rod 307, and an adjusting electromagnet 310 is provided on the condensing chamber 301. The top cabin water inlet pipe 311 is connected to the heat conducting water chamber 302, and the top cabin drain pipe 312 is connected to the heat conducting water chamber 302. A collecting tank 314 is provided in the condensing chamber 301, and a siphon pipe 315 is connected to the collecting tank 314. The condensation drain pipe 316 is connected to the top cabin water inlet pipe 311, and the condensation water inlet pipe 317 is connected to the top cabin drain pipe 312. A condensation pressure gauge 318 is provided on the condensing chamber 301, and the measuring end of the condensation pressure gauge 318 is in the condensing chamber 301.

[0054] The preheating mechanism 4 includes a preheating base 401, a preheating inner tank 402, a preheating water injection channel 403, a preheating drainage channel 404, a heat-conducting fin 406, an insulation outer chamber 407, a preheating water pipe 408 and a cooling water pump 409. The preheating base 401 is installed above the platform 6, the insulation outer chamber 407 is arranged above the preheating base 401, the preheating inner tank 402 is arranged in the insulation outer chamber 407, the heat-conducting fin 406 is arranged outside the preheating inner tank 402, and the preheating water pipe 408 is arranged outside the preheating inner tank 402. 08 is arranged on the heat-conducting fin 406, the preheating drainage channel 404 is connected to the preheating inner tank 402, the preheating water injection channel 403 is connected to the preheating inner tank 402, the preheating drainage channel 404 is connected to the preheating delivery pump 405, the cooling water pump 409 is installed above the platform 6, and the preheating water pipe 408 is connected to the cooling water pump 409; a raw liquid level gauge 410 is provided on the thermal insulation outer cabin 407, and the measuring end of the raw liquid level gauge 410 is located inside the preheating inner tank 402.

[0055] The cooling mechanism 5 includes a cooling chamber 501, a cooling grid 502, a cooling fan 503, a cooling drain pipe 504, a cooling water inlet pipe 505, a filtered water pump 506, a resin ion filter 507 and a storage water pump 508. The cooling chamber 501 is installed above the platform 6, the cooling grid 502 is arranged in the cooling chamber 501, the cooling fan 503 is arranged on the top of the cooling chamber 501, the cooling drain pipe 504 is connected to the cooling grid 502, and the cooling water inlet pipe 505 is connected to the cooling grid 502. The cooling drainage pipe 504 is connected to a filtered water pump 506, a resin ion filter 507 is provided on one side of the cooling chamber 501, the cooling drainage pipe 504 is connected to the water inlet of the resin ion filter 507, a storage water pump 508 is installed above the platform 6, and the water outlet of the resin ion filter 507 is connected to the storage water pump 508; the water outlet of the storage water pump 508 is connected to a storage water pipe 509, and the storage water pipe 509 is connected to the bottom water inlet pipe 205 and the booster water inlet pipe 206 at the same time.

[0056] The cooling water inlet pipe 505 is connected to the preheating water pipe 408, and the preheating water pipe 408 is connected to the condensation drain pipe 316; the condensation water inlet pipe 317 is connected to the Venturi tube 209; the steam delivery pipe 108 is connected to the condensation chamber 301; and the raw liquid delivery pipe 105 is connected to the preheating drain channel 404.

[0057] When in use, a condensed water cycle is first performed, and the condensed water is stored in the bottom water tank 201 and the boost water tank 202. The condensed water pump 203 is started, and the condensed water pump 203 pumps the cooling water in the bottom water tank 201 into the magnetic booster device 208. The cooling water enters the condensed water inlet pipe 317 through the venturi tube 209, and then the cooling water passes through the top cabin water inlet pipe 311, the heat conduction cabin 302 and the top cabin drain pipe 312 in sequence, and finally enters the condensed water drain pipe 316 through the top cabin drain pipe 312, and then enters the preheated water pipe 408 through the condensed water drain pipe 316. When the condensed water participates in the condensation of methanol vapor, After that, the condensed water temperature rises. At this time, the heat of the condensed water in the preheating water pipe 408 will be transferred to the raw liquid in the preheating inner tank 402 through the heat conducting fins 406. Then the condensed water in the preheating water pipe 408 enters the cooling water pump 409, and the cooling water pump 409 uses the condensed water pump 203 to enter the cooling water inlet pipe 505. Then, the condensed water in the cooling water inlet pipe 505 passes through the cooling grid 502 and enters the cooling drain pipe 504. The filtered water pump 506 pumps the condensed water 203 in the cooling drain pipe 504 into the resin ion filter 507 to filter the condensed water. The filtered condensed water is then stored. The water pump 508 pumps the water into the storage water pipe 509 and returns it to the bottom water tank 201 and the boost water tank 202. The cooling water level gauges 216 in the bottom water tank 201 and the boost water tank 202 are used to control the switch status of the boost water valve 214 and the bottom water valve 215 to replenish the condensed water. In addition, after the condensed water participates in the condensation of the methanol vapor, the cooling fan 503 needs to be turned on to ventilate and cool the cooling grid 502 to further reduce the temperature of the condensed water, thereby improving the condensation efficiency. To start the distillation operation, first, the raw liquid is injected into the preheating tank 402 through the preheating water injection channel 403. Then, the preheating delivery pump 405 is started, the delivery valve 106 is opened, the raw liquid delivery pipe 105 is connected to the preheating drainage channel 404, and the preheating delivery pump 405 pumps the raw water in the preheating inner tank 402 into the raw liquid tank 104. At this time, the heating control system 102 is started, and the heating control system 102 controls the heating outer cover 103. The raw liquid tank 104 is heated by the heating outer cover 103. The raw liquid entering the raw liquid tank 104 is heated to the evaporation temperature of methanol. The evaporated methanol turns into methanol vapor, which is discharged into the condensation chamber 301 through the methanol vapor delivery pipe 108;After the methanol vapor enters the condensing chamber 301, it diffuses into the interior of the condensing chamber 301. Since the top heat-conducting partition 303 divides the space below the heat-conducting heat chamber 302 into multiple small chambers, and since the density of methanol vapor is lower than that of air, the methanol vapor mainly accumulates on the top of the small chamber, that is, the bottom of the heat-conducting heat chamber 302. During the diffusion process, the methanol vapor can only continue to fill the next adjacent small chamber after filling one small chamber. At the same time, the output power of the regulating electromagnet 310 can be controlled to change the suction force of the regulating electromagnet 310 on the metal suction piece 309. When the output power of the regulating electromagnet 310 increases, the regulating electromagnet 310 The suction force of the iron 310 on the metal suction piece 309 increases, and the metal suction piece 309 pulls the adjustment rotating rod 307, which squeezes the return spring 308. At the same time, the transmission rack 313 on the adjustment rotating rod 307 drives the transmission gear 306 to rotate, and the rotation of the transmission gear 306 drives the resistance rotating shaft 304 to rotate, and the rotation of the resistance rotating shaft 304 drives the resistance rotating piece 305 to rotate, and the angle between the resistance rotating piece 305 and the vertical direction decreases. Since methanol vapor is a viscous fluid, when the methanol vapor diffuses to the bottom of the resistance rotating piece 305, the methanol vapor is in a divergent state, and the pressure increases along the diffusion direction. At this time, a part of the methanol vapor (branch steam) ) enters the small chamber, the methanol vapor in the small chamber contacts the heat-conducting water chamber 302 and the top heat-conducting baffle 303 for a long time, which can take away more heat, realize efficient heat transfer, and condense quickly. The branch steam diffuses in the small chamber and overflows from the bottom of the small chamber, while the other part of the methanol vapor (mainstream steam) continues to diffuse horizontally. The horizontally diffused methanol vapor (mainstream steam) will be affected by the methanol vapor (branch steam) overflowing from the bottom of the small chamber, and a vortex will be formed at the intersection. The overall diffusion speed becomes slow, which prolongs the condensation time of the methanol vapor. The condensed methanol liquid will fall into the collection tank 314, and then the methanol liquid The condensate is discharged through the siphon 315. The condensation pressure gauge 318 can monitor the pressure in the condensation chamber 301 in real time. By setting a pressure threshold, when the condensation efficiency decreases and the pressure in the condensation chamber 301 increases, reaching the pressure threshold, the boosting electromagnet 213 is activated, which attracts the boosting valve plate 211. The boosting branch pipe 210 is connected to the boosting water pipe 207. Due to the Venturi effect, the condensate in the Venturi tube 209 attracts the condensate in the boosting branch pipe 210, thereby increasing the condensate delivery volume and improving the condensation efficiency. In addition, in actual production, the number of each unit can be increased according to the scale of the enterprise to improve overall production efficiency.

[0058] The above is the specific working process of the present invention. Just repeat this step next time you use it.

[0059] It should be noted that, in this document, relational terms such as first and second, etc., are used only to distinguish one entity or operation from another entity or operation, and do not necessarily require or imply any actual relationship or order between these entities or operations. Moreover, the terms "comprises," "comprising," or any other variations thereof are intended to cover non-exclusive inclusion, such that a process, method, article, or apparatus that includes a list of elements includes not only those elements but also other elements not explicitly listed, or elements inherent to such process, method, article, or apparatus.

[0060] While the embodiments of the present invention have been shown and described, it will be apparent to those skilled in the art that various changes, modifications, substitutions, and alterations can be made to these embodiments without departing from the principles and spirit of the invention.

[0061] The present invention and its embodiments are described above. This description is not restrictive. The drawings show only one embodiment of the present invention, and the actual structure is not limited thereto. In short, if a person skilled in the art is inspired by this and, without departing from the purpose of the present invention, designs structures and embodiments similar to this technical solution without inventiveness, they shall fall within the scope of protection of the present invention.

Claims

1. A distillation and purification device for methanol production, characterized in that: The invention comprises a heating mechanism (1), a water storage mechanism (2), a condensing mechanism (3), a preheating mechanism (4), a cooling mechanism (5) and a platform (6), wherein the condensing mechanism (3) is installed above the platform (6), the heating mechanism (1) is arranged on one side of the condensing mechanism (3), the water storage mechanism (2) is arranged on the other side of the condensing mechanism (3), the preheating mechanism (4) is arranged behind the condensing mechanism (3), and the cooling mechanism (5) is arranged behind the water storage mechanism (2); the condensing mechanism (3) comprises a condensing chamber (301), a heat conducting chamber (302), a top heat conducting baffle (303), a resistance rotating shaft (304), a resistance rotating plate (305), a transmission gear (306) and an adjusting rotating plate. The condensing chamber (301) is installed above the platform (6), the heat-conducting heat chamber (302) is arranged in the condensing chamber (301), the top heat-conducting baffle (303) is arranged at the bottom of the heat-conducting heat chamber (302), the resistance rotating shaft (304) is rotatably arranged on the condensing chamber (301), the resistance rotating piece (305) is arranged on the resistance rotating shaft (304), the transmission gear (306) is arranged on the resistance rotating shaft (304), the adjusting rotating rod (307) is slidably arranged on the condensing chamber (301), and the adjusting rotating rod (307) is provided with a transmission rack (313), and the transmission rack (313) is meshed with the transmission gear (306).

2. The distillation and purification equipment for methanol production according to claim 1, characterized in that: The condensing mechanism (3) further comprises a return spring (308), a metal suction piece (309), an adjusting electromagnet (310), a top cabin water inlet pipe (311), a top cabin drain pipe (312), a collecting tank (314), a siphon (315), a condensation drain pipe (316) and a condensation water inlet pipe (317), one end of the return spring (308) is fixedly connected to the adjusting rotating rod (307), the other end of the return spring (308) is fixedly connected to the condensation cabin (301), and the metal suction piece (309) is arranged on the adjusting rotating rod. The regulating electromagnet (310) is arranged on the rod (307), the top cabin water inlet pipe (311) is communicated with the heat conducting cabin (302), the top cabin drain pipe (312) is communicated with the heat conducting cabin (302), the collecting tank (314) is arranged in the condensing cabin (301), the siphon pipe (315) is communicated with the collecting tank (314), the condensation drain pipe (316) is communicated with the top cabin water inlet pipe (311), and the condensation water inlet pipe (317) is communicated with the top cabin drain pipe (312).

3. The distillation and purification equipment for methanol production according to claim 2, characterized in that: The water storage mechanism (2) comprises a bottom water tank (201), a boosting water tank (202), a condensing water pump (203), a bottom water delivery pipe (204), a bottom water inlet pipe (205), a boosting water inlet pipe (206), and a boosting water delivery pipe (207); the bottom water tank (201) is installed above the platform (6); the boosting water tank (202) is arranged above the bottom water tank (201); the bottom water delivery pipe (204) is communicated with the bottom of the bottom water tank (201); the condensing water pump (203) The condensate pump (203) is arranged above the platform (6), and is connected to the bottom water delivery pipe (204) at the same time. The bottom water inlet pipe (205) is connected to the top of the bottom water tank (201), and a bottom water valve (215) is provided on the bottom water inlet pipe (205). The boosting water inlet pipe (206) is connected to the top of the boosting water tank (202), and the boosting water delivery pipe (207) is connected to the bottom of the boosting water tank (202). The boosting water inlet pipe (206) is provided with a boosting water valve (214).

4. The distillation and purification equipment for methanol production according to claim 3, characterized in that: A magnetic boosting device (208) is installed on one side of the bottom water tank (201), and the magnetic boosting device (208) includes a Venturi tube (209), a boosting branch pipe (210), a boosting valve plate (211), a closing spring (212) and an increasing electromagnet (213). The Venturi tube (209) is arranged on one side of the bottom water tank (201), the boosting branch pipe (210) is connected to the middle part of the Venturi tube (209), a boosting sliding shaft (217) is provided in the boosting branch pipe (210), the boosting valve plate (211) is slidably arranged on the boosting sliding shaft (217), the lower end of the closing spring (212) is fixedly connected to the boosting valve plate (211), the upper end of the closing spring (212) is fixedly connected to the inner wall of the boosting branch pipe (210), and the increasing electromagnet (213) is arranged on the top of the boosting branch pipe (210).

5. The distillation and purification equipment for methanol production according to claim 4, characterized in that: The heating mechanism (1) comprises a heating base (101), a heating control system (102), a heating cover (103) and a raw liquid tank (104); the heating base (101) is installed above the platform (6); the heating control system (102) is arranged on one side of the heating base (101); the heating cover (103) is arranged in the heating base (101); the raw liquid tank (104) is arranged in the heating cover (103); the heating control system (102) is electrically connected to the heating cover (103); the raw liquid tank A steam delivery pipe (108) is provided on the top of the raw liquid tank (104), a waste discharge channel (109) is provided on the bottom of the raw liquid tank (104), a waste discharge valve (110) is provided on the waste discharge channel (109), a raw liquid delivery pipe (105) is connected to the side wall of the raw liquid tank (104), a delivery valve (106) is provided on the raw liquid delivery pipe (105), a heating level gauge (107) is provided on the top of the raw liquid tank (104), and a measuring end of the heating level gauge (107) is located at the bottom of the raw liquid tank (104).

6. The distillation and purification equipment for methanol production according to claim 5, characterized in that: The preheating mechanism (4) comprises a preheating base (401), a preheating inner tank (402), a preheating water injection channel (403), a preheating drainage channel (404), heat-conducting fins (406), a heat-insulating outer chamber (407), a preheating water pipe (408) and a cooling water pump (409), wherein the preheating base (401) is installed above the platform (6), the heat-insulating outer chamber (407) is arranged above the preheating base (401), the preheating inner tank (402) is arranged in the heat-insulating outer chamber (407), the heat-conducting fins (406) are arranged outside the preheating inner tank (402), the preheating water pipe (408) is arranged outside the preheating inner tank (402), and the preheating water pipe (409) is arranged outside the preheating inner tank (402). 408) is provided on the heat-conducting fin (406), the preheating drainage channel (404) is communicated with the preheating inner tank (402), the preheating water injection channel (403) is communicated with the preheating inner tank (402), the preheating drainage channel (404) is communicated with a preheating delivery pump (405), the cooling water pump (409) is installed above the platform (6), and the preheating water pipe (408) is communicated with the cooling water pump (409); a raw liquid level gauge (410) is provided on the heat-insulating outer cabin (407), and the measuring end of the raw liquid level gauge (410) is located inside the preheating inner tank (402).

7. The distillation and purification equipment for methanol production according to claim 6, characterized in that: The cooling mechanism (5) includes a cooling chamber (501), a cooling grid (502), a cooling fan (503), a cooling drainage pipe (504), a cooling water inlet pipe (505), a filtering water pump (506), a resin ion filter (507) and a storage water pump (508). The cooling chamber (501) is installed above the platform (6), the cooling grid (502) is arranged in the cooling chamber (501), the cooling fan (503) is arranged on the top of the cooling chamber (501), and the cooling drainage pipe (504) is installed on the cooling chamber (501). The cooling water inlet pipe (505) is connected to the cooling grid (502), the cooling water inlet pipe (505) is connected to the cooling grid (502), the cooling water outlet pipe (504) is connected to the filtering water pump (506), the resin ion filter (507) is arranged on one side of the cooling chamber (501), the cooling water outlet pipe (504) is connected to the water inlet of the resin ion filter (507), the storage water pump (508) is installed above the platform (6), and the water outlet of the resin ion filter (507) is connected to the storage water pump (508).

8. The distillation and purification equipment for methanol production according to claim 7, characterized in that: A cooling water level gauge (216) is provided in each of the bottom water tank (201) and the boost water tank (202).

9. The distillation and purification equipment for methanol production according to claim 8, characterized in that: A condensation pressure gauge (318) is provided on the condensation chamber (301), and a measuring end of the condensation pressure gauge (318) is inside the condensation chamber (301).

10. The distillation and purification equipment for methanol production according to claim 9, characterized in that: The water outlet of the storage water pump (508) is connected to a storage water pipe (509), and the storage water pipe (509) is simultaneously connected to the bottom water inlet pipe (205) and the boost water inlet pipe (206); the cooling water inlet pipe (505) is connected to the preheating water pipe (408), and the preheating water pipe (408) is connected to the condensation drainage pipe (316); the condensation water inlet pipe (317) is connected to the Venturi tube (209); the steam delivery pipe (108) is connected to the condensation chamber (301); and the raw liquid delivery pipe (105) is connected to the preheating drainage channel (404).

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