CN113149313A - High salt waste water resource utilization's system - Google Patents
High salt waste water resource utilization's system Download PDFInfo
- Publication number
- CN113149313A CN113149313A CN202110404892.1A CN202110404892A CN113149313A CN 113149313 A CN113149313 A CN 113149313A CN 202110404892 A CN202110404892 A CN 202110404892A CN 113149313 A CN113149313 A CN 113149313A
- Authority
- CN
- China
- Prior art keywords
- cylinder
- motor
- sleeve
- module
- centrifugal
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F9/00—Multistage treatment of water, waste water or sewage
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/001—Processes for the treatment of water whereby the filtration technique is of importance
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/02—Treatment of water, waste water, or sewage by heating
- C02F1/04—Treatment of water, waste water, or sewage by heating by distillation or evaporation
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/02—Treatment of water, waste water, or sewage by heating
- C02F1/04—Treatment of water, waste water, or sewage by heating by distillation or evaporation
- C02F1/048—Purification of waste water by evaporation
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/38—Treatment of water, waste water, or sewage by centrifugal separation
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/52—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2201/00—Apparatus for treatment of water, waste water or sewage
- C02F2201/002—Construction details of the apparatus
- C02F2201/007—Modular design
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2209/00—Controlling or monitoring parameters in water treatment
- C02F2209/05—Conductivity or salinity
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2301/00—General aspects of water treatment
- C02F2301/08—Multistage treatments, e.g. repetition of the same process step under different conditions
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Heat Treatment Of Water, Waste Water Or Sewage (AREA)
Abstract
The invention discloses a system for resource utilization of high-salinity wastewater, which comprises a solid-liquid separation module, a concentration module, an evaporation crystallization module and a control module; the solid-liquid separation module comprises a separation cylinder, a centrifugal component and a filter pressing component, and the centrifugal component and the filter pressing component are respectively used for carrying out centrifugal separation and filter pressing treatment on large-particle impurities in the high-salinity wastewater; the concentration module comprises a concentration tank, a heating assembly and a condensed water collection assembly, wherein the heating assembly and the condensed water collection assembly are respectively used for heating the wastewater and collecting condensed water drops; the evaporative crystallization module comprises an evaporation box, an infrared heating sleeve and a stirring assembly; the infrared heating sleeve and the stirring assembly are respectively used for carrying out infrared heating on the wastewater and stirring the wastewater in the heating process, and the control module is used for controlling the automatic operation of the solid-liquid separation module, the concentration module and the evaporation crystallization module; the invention has reasonable structural design, safety and high efficiency and is suitable for large-scale popularization.
Description
Technical Field
The invention relates to the technical field of high-salinity wastewater treatment, in particular to a system for resource utilization of high-salinity wastewater.
Background
The high-salinity wastewater generally refers to wastewater with the total salt content of more than or equal to 1 percent by mass, and the salts of the wastewater mainly contain Cl-、NO3-、 SO42-、Na+、Ca2+、Mg2+And the like. High salt waste of ChinaThe water production accounts for 5% of the total wastewater, mainly comes from the fields of coal chemical industry, seawater desalination, wet flue gas desulfurization and the like, and is still increased by 2% every year. The discharge of high-salinity wastewater can cause the increase of salinity and the accumulation of hardness in a water body, threaten the health of human bodies, increase the softening treatment cost and cause the corrosion of industrial equipment. Therefore, foreign countries have been concerned about the environmental impact of high-salinity wastewater discharge, and the european union promulgated a social convention in 2000 to prevent water from being polluted by high-salinity wastewater. Aiming at the problem, local standards are issued in turn in the provinces of Beijing, Shanghai, Henan, Hebei, Guizhou, Sichuan and the like in recent years, and the discharge concentration of the salt of the wastewater is limited.
Due to the extremely high salt content of the high-salt wastewater, the high-salt wastewater can reach the standard discharge only by carrying out membrane treatment, evaporative crystallization, ion exchange and other subsequent advanced treatments after the conventional treatment, but the high-salt wastewater treated by the treatment method has the problems of high difficulty and high treatment cost on one hand, and on the other hand, the treated wastewater cannot be reused as industrial water, so that the resource utilization efficiency of the high-salt wastewater is influenced.
Disclosure of Invention
Aiming at the technical problems, the invention provides a high-salinity wastewater resource utilization system with good treatment effect and high efficiency.
The technical scheme of the invention is as follows: a system for resource utilization of high-salinity wastewater comprises a solid-liquid separation module, a concentration module, an evaporation crystallization module and a control module; the solid-liquid separation module, the concentration module, the evaporation crystallization module and the control module are all fixedly arranged on the bottom plate;
the solid-liquid separation module comprises a separation cylinder, a centrifugal assembly and a filter pressing assembly; a water inlet pipe is arranged at the upper position of the side wall of the separation cylinder, a mounting frame is arranged at the top of the separation cylinder, a limiting frame is connected with the inside of the separation cylinder through a fixed disc, and a certain gap is formed between the limiting frame and the bottom in the separation cylinder; the centrifugal assembly comprises a centrifugal motor, a centrifugal cylinder and a guide cylinder, the guide cylinder is fixedly connected to the middle of the fixed disc, a conical guide groove is formed in the bottom of the guide cylinder, the top of the guide cylinder is higher than the fixed disc, the centrifugal motor is fixedly arranged on the mounting frame, and the centrifugal cylinder is arranged inside the guide cylinder and connected with an output shaft of the centrifugal motor; the filter pressing component comprises a filter pressing cylinder, a pressure plate, an adjusting motor and a lifting motor, wherein the pressure cylinder is arranged on a limiting frame and is positioned at the lower end of a conical diversion trench, a deslagging pipe is arranged at the bottom of the filter pressing cylinder and penetrates through a separating cylinder, the pressure plate is arranged at the opening at the upper end of the filter pressing cylinder, the outer diameter of the pressure plate is matched with the inner diameter of the filter pressing cylinder, a shaft sleeve is arranged at the central position of the pressure plate, 3-6 fan-shaped adjusting plates are uniformly arranged on the pressure plate and are connected with the pressure plate through adjusting screws, one end of each adjusting screw penetrates through the shaft sleeve and is provided with an auxiliary conical gear, a guide block is arranged at the joint of the pressure plate and each fan-shaped adjusting plate, the adjusting motor is arranged at the inner bottom of the separating cylinder, an output shaft of the adjusting motor sequentially penetrates through the filter pressing cylinder and the shaft sleeve, a main conical gear is slidably clamped on the output shaft and is meshed with each auxiliary conical gear respectively, the lifting motor is arranged at the bottom in the separation cylinder, a lifting screw rod is arranged on an output shaft of the lifting motor, and the lifting screw rod sequentially penetrates through the pressure filter cylinder and the pressure plate and is in threaded connection with the pressure plate;
the concentration module comprises a concentration tank, a heating assembly and a condensed water collection assembly; a liquid spraying pipe is vertically arranged at the central position in the concentration tank, a plurality of liquid spraying ports are uniformly arranged on the liquid spraying pipe, the liquid spraying pipe is communicated with the separation cylinder through a guide pipe, and a pressure pump is arranged at the connection position of the liquid spraying pipe and the separation cylinder; the heating assembly comprises an installation sleeve and electric heating rods, wherein 3-6 grooves are uniformly formed in the installation sleeve in the circumferential direction, the number of the electric heating rods is consistent with that of the grooves, the electric heating rods are movably clamped in the grooves, and a plurality of heating fins are uniformly arranged on the electric heating rods in the circumferential direction; the condensed water collecting assembly comprises a condensing plate and a condensed water collecting tank, the condensing plate is arranged at the top end in the concentrating tank, the condensing plate is of a conical structure, the condensed water collecting tank is movably clamped on the inner wall of the concentrating tank and is abutted against the lower edge of the condensing plate, and a condensed water collecting pipe penetrating through the concentrating tank is arranged on the condensed water collecting tank;
the evaporative crystallization module comprises an evaporation box, an infrared heating sleeve and a stirring assembly; the evaporation box is connected with the concentration tank through a guide pipe, a crystallization seat is arranged in the evaporation box, a box door is movably hinged to the position, corresponding to the crystallization seat, on the side wall of the evaporation box, a heat exchange box is connected to the outer wall of the evaporation box through a guide pipe, a water outlet pipe is arranged on the heat exchange box, an infrared heating sleeve is fixedly clamped and connected to the inner wall of the evaporation box, the stirring assembly comprises a main motor, a hollow sleeve and a stirring disc, the hollow sleeve vertically penetrates through the evaporation box and is rotatably clamped and connected with the evaporation box, the main motor is arranged at the top end of the outer portion of the evaporation box and provides power for the hollow sleeve, 1-3 stirring discs are arranged, and 1-3 stirring discs are uniformly sleeved on the hollow sleeve;
the control module is respectively and electrically connected with the centrifugal motor, the adjusting motor, the lifting motor, the pressure pump and the main motor, and the centrifugal motor, the adjusting motor, the lifting motor, the pressure pump and the main motor are all powered by an external power supply.
Furthermore, the centrifugal cylinder comprises a first net cylinder and a second net cylinder, the second net cylinder is sleeved inside the first net cylinder, the second net cylinder is arranged inside the second net cylinder, and a separation screen plate is arranged between the second net cylinder and the first net cylinder.
Furthermore, the fixed disk is rotatably clamped with a mixing disk, a plurality of mixing teeth are uniformly arranged on the mixing disk, a first tooth sleeve is arranged on one side, close to the guide cylinder, of the mixing disk, a mixing motor is arranged on the mounting frame, a connecting gear is arranged on an output shaft of the mixing motor and meshed with the first tooth sleeve, and the flocculating agent is added into the fixed disk through the mixing disk, so that the combination of the flocculating agent and salt ions in high-salt wastewater is promoted, and the flocculating and settling effect of the salt ions in the high-salt wastewater is improved.
Further, elevator motor is provided with two, and two elevator motor are located the both sides of adjusting motor respectively, all are provided with elevating screw on two elevator motor's the output shaft, through setting up two elevator motor, are favorable to improving the stability when pressure disk descends to improve the filter-pressing effect and the efficiency of high salt waste water.
Further, both ends rotate the joint about the both ends all through spindle nose and fluting of each heating rod, and be located all the cover and be equipped with the pinion on the spindle nose of fluting lower extreme, installation cover lower extreme rotates the joint and has the second gear sleeve, the second gear sleeve is connected with each pinion engagement, the bottom is provided with the rotating electrical machines in the concentrator tank, the rotating electrical machines provides power for the second gear sleeve, utilize the rotating electrical machines to drive the second gear sleeve and rotate, and then make each heating rod take place to rotate at the fluting, make the heating of high salt waste water more even, improve the heating effect, and then improve the evaporation effect of high salt waste water.
Further, the stirring disc comprises an outer disc and an inner disc, the inner disc is sleeved inside the outer disc, the inner disc is connected with the outer disc through 3-6 pull rods, and a plurality of vertical stirring teeth are arranged at the upper end and the lower end of the outer disc; the design is favorable for improving the heating uniformity of the wastewater, thereby promoting the evaporation, crystallization and precipitation of salt ions in the high-salinity wastewater.
Further, the evaporation tank top is provided with vice motor through the motor frame, be connected with the bull stick on the output shaft of vice motor, the bull stick rotates the joint inside hollow sleeve, it is provided with the arc draw-in groove with agitator disk position correspondence department on the bull stick, be provided with the sliding tray on the hollow sleeve, the one end and the outer fixed connection of dish of each pull rod, the other end runs through inner disc and sliding tray back and arc draw-in groove activity joint, utilize vice motor drive bull stick to rotate, and then make each pull rod reciprocate in the arc draw-in groove, make the outer dish can the luffing motion at the rotation in-process, the stirring in a plurality of positions is carried out high salt waste water, thereby the stirring effect and the efficiency of high salt waste water have been improved.
Further, each pull rod and arc draw-in groove junction all are provided with rotatory bulb, can reduce the friction between pull rod and the arc draw-in groove through setting up rotatory bulb, can make the pull rod remove more smoothly in the arc draw-in groove simultaneously, improve the work efficiency of agitator disk.
Furthermore, a water scraping strip is arranged at the lower end of the condensing plate and is tightly attached to the lower end face of the condensing plate, and a water scraping motor is arranged at the top end of the concentrating tank and provides power for the water scraping strip; through setting up the wiping strip, be favorable to steam that high salt waste water evaporation in-process produced to condense into the condensate collecting vat fast behind the water droplet under the condensing plate in, improve the resource utilization efficiency of high salt waste water.
The working principle of the invention is as follows:
firstly, connecting each electric device of the system with an external power supply, introducing high-salt wastewater into an annular area formed by a fixed disc and a guide cylinder in a separation cylinder through a water inlet pipe, adding a commercially available flocculant into the high-salt wastewater, and controlling a material mixing motor to start through a control module to drive a material mixing disc to rotate so as to fully mix the flocculant and the high-salt wastewater;
secondly, when the wastewater in the separation cylinder is higher than the upper edge of the guide cylinder and then enters the centrifugal cylinder, the control module is used for controlling the centrifugal motor to start and driving the centrifugal cylinder to rotate, the high-salt wastewater is centrifugally treated, large-particle impurities in the wastewater are removed, the centrifugally treated wastewater enters the pressure filter cylinder through a conical guide groove at the lower end of the guide cylinder, the control module is used for controlling the adjusting motor to start, a main conical gear on an output shaft is used for driving auxiliary conical gears on the adjusting screws to rotate, so that the fan-shaped adjusting plates are close to the shaft sleeves, then the control module is used for controlling the lifting motor to start, the lifting screws are used for driving the pressure plate to move downwards in the pressure filter cylinder, the high-salt wastewater is subjected to pressure filtration, and impurities deposited in the pressure filter cylinder are discharged through a slag discharge pipe;
thirdly, high-salinity wastewater subjected to filter pressing treatment enters a liquid spraying pipe in a concentration tank under the action of a pressure pump and is sprayed to an installation sleeve through a liquid spraying opening in the liquid spraying pipe, the high-salinity wastewater is subjected to heating treatment through an electric heating rod and a heating fin, and meanwhile, a control module is used for controlling a rotating motor to be started to drive a second gear sleeve to rotate, so that each heating rod rotates in a groove, steam generated in the evaporation process of the high-salinity wastewater is condensed into water drops on the lower end face of a condensation plate and then enters a condensate water collecting tank, and the water drops are discharged out of the concentration tank through a condensate water collecting pipe;
fourthly, high salt waste water after the concentrated treatment passes through the pipe and gets into in the evaporation tank, utilize the infrared heating cover to heat for the high salt waste water after the concentration, the vapor that produces among the heating process passes through the pipe and gets into the heat transfer case and finally discharges through the outlet pipe, among the high salt waste water heating process, through control module control main motor and vice motor simultaneous start, utilize main motor to drive hollow sleeve and rotate, and then drive the agitator disk and rotate, utilize vice motor to drive the bull stick and rotate, and then make each pull rod reciprocate in the arc draw-in groove, make the outer dish can the luffing motion at the rotation in-process, carry out the stirring in a plurality of positions to high salt waste water, after the evaporation of high salt waste water is accomplished, the salinity crystallization in the waste water is appeared, and collect through the crystallization seat.
Compared with the prior art, the invention has the beneficial effects that: the invention has reasonable structural design, safety and high efficiency, and the treated wastewater can be secondarily utilized as industrial water by carrying out solid-liquid separation, concentration and evaporative crystallization treatment on the high-salinity wastewater, and simultaneously, the salt crystallized from the high-salinity wastewater can also be secondarily utilized as an industrial raw material, thereby greatly improving the resource utilization efficiency and effect of the high-salinity wastewater; meanwhile, after the high-salinity wastewater is subjected to solid-liquid separation and concentration treatment, the concentration of salt ions in the wastewater is greatly reduced, the workload of the evaporative crystallization module is reduced, the operation energy consumption of a system is further reduced, and the treatment cost of the high-salinity wastewater is reduced.
Drawings
FIG. 1 is a longitudinal section of the present invention;
FIG. 2 is an external structural view of the present invention;
FIG. 3 is a top view of the separation cartridge of the present invention;
FIG. 4 is a schematic view of the platen and filter cartridge connection of the present invention;
FIG. 5 is a schematic structural view of the sector-shaped adjusting plate of the present invention in an open state;
FIG. 6 is a schematic view of the connection of the electric heating rod of the present invention to the mounting sleeve;
FIG. 7 is a schematic structural view of the stirring plate of the present invention;
FIG. 8 is a schematic view of the coupling of the stirring plate to the rotating shaft according to the present invention;
the device comprises a solid-liquid separation module 1, a separation barrel 10, a water inlet pipe 100, a mounting frame 101, a fixing disk 102, a limiting frame 103, a material mixing disk 104, a first gear sleeve 105, a material mixing motor 106, a centrifugal assembly 11, a centrifugal motor 110, a centrifugal barrel 111, a first mesh barrel 1110, a second mesh barrel 1111, a separating screen 1112, a guide cylinder 112, a filter pressing assembly 12, a filter pressing assembly 120, a slag discharge pipe 1200, a pressure plate 121, a guide block 1210, an adjusting motor 122, an output shaft 1220, a main conical gear 1221, a lifting motor 123, a lifting screw 1230, a lifting screw 124, a shaft sleeve 124, a fan-shaped adjusting plate 125, an adjusting screw 1250, a limiting frame 103, a material mixing disk 104, a first gear sleeve 105, a material mixing motor 106, a centrifugal assembly 11, a centrifugal motor 110, a centrifugal motor 111, a slag discharge pipe 1110, a guide block 1210, an adjusting motor, an output shaft 1220, a main conical gear 1221, a lifting motor 123, a lifting screw 124-shaft sleeve 124-shaped adjusting plate, a fan-shaped adjusting screw, a fan-shaped adjusting plate, a fan-shaped adjusting screw, a fan-shaped adjusting plate, a fan-shaped fan-, 1251-auxiliary bevel gear, 2-concentration module, 20-concentration tank, 200-liquid spray pipe, 201-pressure pump, 21-heating component, 210-mounting sleeve, 2100-slotting, 2101-second tooth sleeve, 211-electric heating rod, 2110-heating fin, 2111-shaft head, 22-condensate water collecting component, 220-condensation plate, 221-condensate water collecting tank, 2210-condensate water collecting pipe, 222-water scraping strip, 2220-water scraping motor, 3-evaporative crystallization module, 30-evaporative tank, 300-box door, 31-infrared heating sleeve, 32-stirring component, 320-main motor, 321-hollow sleeve, 322-stirring disk, 3220-outer disk, 3221-inner disk, 3222-pull rod, 3223-vertical stirring tooth, 3224-sliding groove, 3225-rotary ball head, 323-auxiliary motor, 3230-rotary rod, 3231-arc clamping groove, 33-crystallization seat, 34-heat exchange box, 340-water outlet pipe and 4-bottom plate.
Detailed Description
Example 1: the system for resource utilization of high-salinity wastewater shown in fig. 1, 2, 3, 4 and 5 comprises a solid-liquid separation module 1, a concentration module 2, an evaporation crystallization module 3 and a control module; the solid-liquid separation module 1, the concentration module 2, the evaporation crystallization module 3 and the control module are all fixedly arranged on the bottom plate 4; the solid-liquid separation module 1 comprises a separation cylinder 10, a centrifugal component 11 and a filter pressing component 12; a water inlet pipe 100 is arranged at the upper position of the side wall of the separating cylinder 10, an installation frame 101 is arranged at the top of the separating cylinder 10, a limiting frame 103 is connected with the inside of the separating cylinder 10 through a fixed disc 102, and a certain gap is formed between the limiting frame 103 and the bottom of the inside of the separating cylinder 10; the fixed disc 102 is rotatably clamped with a mixing disc 104, the mixing disc 104 is uniformly provided with a plurality of mixing teeth, one side of the mixing disc 104, which is close to the guide cylinder 112, is provided with a first toothed sleeve 105, the mounting frame 101 is provided with a mixing motor 106, an output shaft of the mixing motor 106 is provided with a connecting gear, the connecting gear is meshed with the first toothed sleeve 105, and by arranging the mixing disc 104, when a flocculating agent is added into the fixed disc 102, the combination of the flocculating agent and salt ions in high-salt wastewater is promoted, so that the flocculation and precipitation effects of the salt ions in the high-salt wastewater are improved; the centrifugal assembly 11 comprises a centrifugal motor 110, a centrifugal cylinder 111 and a guide cylinder 112, the guide cylinder 112 is fixedly connected to the middle of the fixed disk 102, a conical guide groove is formed in the bottom of the guide cylinder 112, the top of the guide cylinder 112 is higher than the fixed disk 102, the centrifugal motor 110 is fixedly arranged on the mounting frame 101, and the centrifugal cylinder 111 is arranged inside the guide cylinder 112 and connected with an output shaft of the centrifugal motor 110; the centrifugal cylinder 111 comprises a first net cylinder 1110 and a second net cylinder 1111, the second net cylinder 1111 is sleeved inside the first net cylinder 1110, the second net cylinder 1111 is arranged inside the second net cylinder 1111, and a separation screen plate 1112 is arranged between the second net cylinder 1111 and the first net cylinder 1110, and by arranging the first net cylinder 1110, the second net cylinder 1111 and the separation screen plate 112, pollutants in high-salt wastewater in the rotation process of the centrifugal cylinder 111 can be prevented from being accumulated on the inner wall of the centrifugal cylinder 111 under the centrifugal effect, and the centrifugal effect of the centrifugal cylinder 111 on the pollutants precipitated in the high-salt wastewater is improved; the filter pressing component 12 comprises a filter pressing cylinder 120, a pressure plate 121, an adjusting motor 122 and a lifting motor 123, wherein the pressure cylinder 120 is arranged on a limiting frame 103 and is positioned at the lower end of a conical diversion trench, a slag discharge pipe 1200 is arranged at the bottom of the filter pressing cylinder 120, the slag discharge pipe 1200 penetrates through the separation cylinder 10, the pressure plate 121 is arranged at an opening at the upper end of the filter pressing cylinder 120, the outer diameter of the pressure plate 121 is matched with the inner diameter of the filter pressing cylinder 120, a shaft sleeve 124 is arranged at the center of the pressure plate 121, 4 fan-shaped adjusting plates 125 are uniformly arranged on the pressure plate 121, each fan-shaped adjusting plate 125 is connected with the pressure plate 121 through an adjusting screw rod 1250, one end of each adjusting screw rod 1250 penetrates through the shaft sleeve 124 and is provided with an auxiliary conical gear 1251, a guide block 1210 is arranged at the joint of the pressure plate 121 and each fan-shaped adjusting plate 1211, the adjusting motor 122 is arranged at the bottom of the separation cylinder 10, an output shaft 1220 of the adjusting motor 122 sequentially penetrates through the filter pressing cylinder 120 and the shaft sleeve 124, a main bevel gear 1221 is slidably clamped on the output shaft 1220, the main bevel gear 1221 is respectively engaged with each auxiliary bevel gear 1251, the lifting motor 123 is arranged at the bottom in the separation cylinder 10, a lifting lead screw 1230 is arranged on the output shaft of the lifting motor 123, and the lifting lead screw 1230 sequentially penetrates through the pressure filter cylinder 120 and the pressure plate 121 and is in threaded connection with the pressure plate 121; the two lifting motors 123 are arranged, the two lifting motors 123 are respectively positioned at two sides of the adjusting motor 122, the lifting screw 1230 is arranged on the output shafts of the two lifting motors 123, and the two lifting motors 123 are arranged, so that the stability of the pressure plate 121 during descending is improved, and the filter pressing effect and efficiency of the high-salinity wastewater are improved;
as shown in fig. 1, 2, 6, 7, the thickening module 2 comprises a thickening tank 20, a heating assembly 21 and a condensed water collecting assembly 22; a liquid spraying pipe 200 is vertically arranged at the central position in the concentration tank 20, a plurality of liquid spraying ports are uniformly arranged on the liquid spraying pipe 200, the liquid spraying pipe 200 is communicated with the separation cylinder 10 through a guide pipe, and a pressure pump 201 is arranged at the connection position; the heating assembly 21 comprises a mounting sleeve 210 and electric heating rods 211, the mounting sleeve 210 is uniformly provided with 4 slots 2100 in the circumferential direction, the number of the electric heating rods 211 is consistent with that of the slots 2100, two ends of each heating rod 211 are rotatably clamped with the upper end and the lower end of each slot 2100 through shaft heads 2111, and the shaft head 2111 at the lower end of the open groove 2100 is sleeved with a pinion, the lower end of the mounting sleeve 210 is rotationally clamped with a second gear sleeve 2101, the second gear sleeve 2101 is meshed with each pinion, the bottom in the concentration tank 20 is provided with a rotating motor, the rotating motor provides power for the second gear sleeve 2101, the rotating motor drives the second gear sleeve 2101 to rotate, thereby enabling each heating rod 211 to rotate in the slot 2100, enabling the high-salinity wastewater to be heated more uniformly, improving the heating effect, further improving the evaporation effect of the high-salinity wastewater, and a plurality of heating fins 2110 are uniformly arranged on each electric heating rod 211 in the circumferential direction; the condensed water collection assembly 22 comprises a condensation plate 220 and a condensed water collection tank 221, the condensation plate 220 is arranged at the top end in the concentration tank 20, the condensation plate 220 is of a conical structure, the condensed water collection tank 221 is movably clamped on the inner wall of the concentration tank 20 and is abutted against the lower edge of the condensation plate 220, and a condensed water collection pipe 2210 penetrating through the concentration tank 20 is arranged on the condensed water collection tank 221;
as shown in fig. 1 and 2, the evaporative crystallization module 3 comprises an evaporation tank 30, an infrared heating jacket 31 and a stirring assembly 32; the evaporation box 30 is connected with the concentration tank 20 through a guide pipe, a crystallization seat 33 is arranged in the evaporation box 30, a box door 300 is movably hinged on the side wall of the evaporation box 30 at a position corresponding to the crystallization seat 33, the outer wall of the evaporation box 30 is connected with a heat exchange box 34 through a guide pipe, a water outlet pipe 340 is arranged on the heat exchange box 34, an infrared heating sleeve 31 is fixedly clamped on the inner wall of the evaporation box 30, a stirring assembly 32 comprises a main motor 320, a hollow sleeve 321 and a stirring disc 322, the hollow sleeve 321 vertically penetrates through the evaporation box 30 and is rotatably clamped with the evaporation box 30, the main motor 320 is arranged at the top end of the outside of the evaporation box 30 and provides power for the hollow sleeve 321, 2 stirring discs 322 are arranged, and the 2 stirring discs 322 are uniformly sleeved on the hollow sleeve 321;
as shown in fig. 1, the control module is electrically connected to the mixing motor 106, the centrifugal motor 110, the adjusting motor 122, the lifting motor 123, the pressure pump 201, the electric heating rod 211, the infrared heating jacket 31, the main motor 320 and the rotating motor, respectively, and the mixing motor 106, the centrifugal motor 110, the adjusting motor 122, the lifting motor 123, the pressure pump 201, the electric heating rod 211, the infrared heating jacket 31, the main motor 320 and the rotating motor are all commercially available products and are all powered by an external power source.
Example 2: the system for resource utilization of high-salinity wastewater shown in fig. 1, 2, 3, 4 and 5 comprises a solid-liquid separation module 1, a concentration module 2, an evaporation crystallization module 3 and a control module; the solid-liquid separation module 1, the concentration module 2, the evaporation crystallization module 3 and the control module are all fixedly arranged on the bottom plate 4; the solid-liquid separation module 1 comprises a separation cylinder 10, a centrifugal component 11 and a filter pressing component 12; a water inlet pipe 100 is arranged at the upper position of the side wall of the separating cylinder 10, an installation frame 101 is arranged at the top of the separating cylinder 10, a limiting frame 103 is connected with the inside of the separating cylinder 10 through a fixed disc 102, and a certain gap is formed between the limiting frame 103 and the bottom of the inside of the separating cylinder 10; the fixed disc 102 is rotatably clamped with a mixing disc 104, the mixing disc 104 is uniformly provided with a plurality of mixing teeth, one side of the mixing disc 104, which is close to the guide cylinder 112, is provided with a first toothed sleeve 105, the mounting frame 101 is provided with a mixing motor 106, an output shaft of the mixing motor 106 is provided with a connecting gear, the connecting gear is meshed with the first toothed sleeve 105, and by arranging the mixing disc 104, when a flocculating agent is added into the fixed disc 102, the combination of the flocculating agent and salt ions in high-salt wastewater is promoted, so that the flocculation and precipitation effects of the salt ions in the high-salt wastewater are improved; the centrifugal assembly 11 comprises a centrifugal motor 110, a centrifugal cylinder 111 and a guide cylinder 112, the guide cylinder 112 is fixedly connected to the middle of the fixed disk 102, a conical guide groove is formed in the bottom of the guide cylinder 112, the top of the guide cylinder 112 is higher than the fixed disk 102, the centrifugal motor 110 is fixedly arranged on the mounting frame 101, and the centrifugal cylinder 111 is arranged inside the guide cylinder 112 and connected with an output shaft of the centrifugal motor 110; the centrifugal cylinder 111 comprises a first net cylinder 1110 and a second net cylinder 1111, the second net cylinder 1111 is sleeved inside the first net cylinder 1110, the second net cylinder 1111 is arranged inside the second net cylinder 1111, and a separation screen plate 1112 is arranged between the second net cylinder 1111 and the first net cylinder 1110, and by arranging the first net cylinder 1110, the second net cylinder 1111 and the separation screen plate 112, pollutants in high-salt wastewater in the rotation process of the centrifugal cylinder 111 can be prevented from being accumulated on the inner wall of the centrifugal cylinder 111 under the centrifugal effect, and the centrifugal effect of the centrifugal cylinder 111 on the pollutants precipitated in the high-salt wastewater is improved; the filter pressing component 12 comprises a filter pressing cylinder 120, a pressure plate 121, an adjusting motor 122 and a lifting motor 123, wherein the pressure cylinder 120 is arranged on a limiting frame 103 and is positioned at the lower end of a conical diversion trench, a slag discharge pipe 1200 is arranged at the bottom of the filter pressing cylinder 120, the slag discharge pipe 1200 penetrates through the separation cylinder 10, the pressure plate 121 is arranged at an opening at the upper end of the filter pressing cylinder 120, the outer diameter of the pressure plate 121 is matched with the inner diameter of the filter pressing cylinder 120, a shaft sleeve 124 is arranged at the center of the pressure plate 121, 4 fan-shaped adjusting plates 125 are uniformly arranged on the pressure plate 121, each fan-shaped adjusting plate 125 is connected with the pressure plate 121 through an adjusting screw rod 1250, one end of each adjusting screw rod 1250 penetrates through the shaft sleeve 124 and is provided with an auxiliary conical gear 1251, a guide block 1210 is arranged at the joint of the pressure plate 121 and each fan-shaped adjusting plate 1211, the adjusting motor 122 is arranged at the bottom of the separation cylinder 10, an output shaft 1220 of the adjusting motor 122 sequentially penetrates through the filter pressing cylinder 120 and the shaft sleeve 124, a main bevel gear 1221 is slidably clamped on the output shaft 1220, the main bevel gear 1221 is respectively engaged with each auxiliary bevel gear 1251, the lifting motor 123 is arranged at the bottom in the separation cylinder 10, a lifting lead screw 1230 is arranged on the output shaft of the lifting motor 123, and the lifting lead screw 1230 sequentially penetrates through the pressure filter cylinder 120 and the pressure plate 121 and is in threaded connection with the pressure plate 121; the two lifting motors 123 are arranged, the two lifting motors 123 are respectively positioned at two sides of the adjusting motor 122, the lifting screw 1230 is arranged on the output shafts of the two lifting motors 123, and the two lifting motors 123 are arranged, so that the stability of the pressure plate 121 during descending is improved, and the filter pressing effect and efficiency of the high-salinity wastewater are improved;
as shown in fig. 1, 2, 6, 7, the thickening module 2 comprises a thickening tank 20, a heating assembly 21 and a condensed water collecting assembly 22; a liquid spraying pipe 200 is vertically arranged at the central position in the concentration tank 20, a plurality of liquid spraying ports are uniformly arranged on the liquid spraying pipe 200, the liquid spraying pipe 200 is communicated with the separation cylinder 10 through a guide pipe, and a pressure pump 201 is arranged at the connection position; the heating assembly 21 comprises a mounting sleeve 210 and electric heating rods 211, the mounting sleeve 210 is uniformly provided with 4 slots 2100 in the circumferential direction, the number of the electric heating rods 211 is consistent with that of the slots 2100, two ends of each heating rod 211 are rotatably clamped with the upper end and the lower end of each slot 2100 through shaft heads 2111, and the shaft head 2111 at the lower end of the open groove 2100 is sleeved with a pinion, the lower end of the mounting sleeve 210 is rotationally clamped with a second gear sleeve 2101, the second gear sleeve 2101 is meshed with each pinion, the bottom in the concentration tank 20 is provided with a rotating motor, the rotating motor provides power for the second gear sleeve 2101, the rotating motor drives the second gear sleeve 2101 to rotate, thereby enabling each heating rod 211 to rotate in the slot 2100, enabling the high-salinity wastewater to be heated more uniformly, improving the heating effect, further improving the evaporation effect of the high-salinity wastewater, and a plurality of heating fins 2110 are uniformly arranged on each electric heating rod 211 in the circumferential direction; the condensed water collection assembly 22 comprises a condensation plate 220 and a condensed water collection tank 221, the condensation plate 220 is arranged at the top end in the concentration tank 20, the condensation plate 220 is of a conical structure, the condensed water collection tank 221 is movably clamped on the inner wall of the concentration tank 20 and is abutted against the lower edge of the condensation plate 220, and a condensed water collection pipe 2210 penetrating through the concentration tank 20 is arranged on the condensed water collection tank 221; the lower end of the condensing plate 220 is provided with a water scraping strip 222, the water scraping strip 222 is tightly attached to the lower end surface of the condensing plate 220, the top end of the concentrating tank 20 is provided with a wiper motor 2220, and the wiper motor 2220 provides power for the water scraping strip 222; by arranging the water scraping strips 222, steam generated in the evaporation process of the high-salt wastewater is condensed into water drops on the lower end surface of the condensing plate 220 and then quickly enters the condensed water collecting tank 221, so that the resource utilization efficiency of the high-salt wastewater is improved;
as shown in fig. 1, 2 and 8, the evaporative crystallization module 3 comprises an evaporation tank 30, an infrared heating jacket 31 and a stirring assembly 32; the evaporation box 30 is connected with the concentration tank 20 through a guide pipe, a crystallization seat 33 is arranged in the evaporation box 30, a box door 300 is movably hinged on the side wall of the evaporation box 30 at a position corresponding to the crystallization seat 33, the outer wall of the evaporation box 30 is connected with a heat exchange box 34 through a guide pipe, a water outlet pipe 340 is arranged on the heat exchange box 34, an infrared heating sleeve 31 is fixedly clamped on the inner wall of the evaporation box 30, a stirring assembly 32 comprises a main motor 320, a hollow sleeve 321 and a stirring disc 322, the hollow sleeve 321 vertically penetrates through the evaporation box 30 and is rotatably clamped with the evaporation box 30, the main motor 320 is arranged at the top end of the outside of the evaporation box 30 and provides power for the hollow sleeve 321, 2 stirring discs 322 are arranged, and the 2 stirring discs 322 are uniformly sleeved on the hollow sleeve 321; the stirring disc 322 comprises an outer disc 3220 and an inner disc 3221, the inner disc 3221 is sleeved inside the outer disc 3220, the inner disc 3221 is connected with the outer disc 3220 through 4 pull rods 3222, and a plurality of vertical stirring teeth 3223 are arranged at the upper end and the lower end of the outer disc 3220; the design is beneficial to improving the heating effect of the wastewater, so that the evaporation, crystallization and precipitation of salt ions in the high-salinity wastewater are promoted; the top end of the evaporation box 30 is provided with an auxiliary motor 323 through a motor frame, an output shaft of the auxiliary motor 323 is connected with a rotating rod 3230, the rotating rod 3230 is rotatably clamped inside the hollow sleeve 321, an arc-shaped clamping groove 3231 is arranged at a position, corresponding to the stirring disc 322, on the rotating rod 3230, a sliding groove 3224 is arranged on the hollow sleeve 321, one end of each pull rod 3222 is fixedly connected with the outer disc 3220, the other end of each pull rod 3222 penetrates through the inner disc 3221 and the sliding groove 3224 and then is movably clamped with the arc-shaped clamping groove 3231, the rotating rod 3230 is driven to rotate by the auxiliary motor 323, and then each pull rod 3222 moves up and down in the arc-shaped clamping groove 3231, so that the outer disc 3220 can swing up and down in the rotating process, the high-salinity wastewater is stirred in multiple directions, and the stirring effect and efficiency of the high-salinity wastewater are improved; the rotating ball heads 3225 are arranged at the joints of the pull rods 3222 and the arc-shaped clamping grooves 3231, friction between the pull rods 3222 and the arc-shaped clamping grooves 3231 can be reduced by the rotating ball heads 3225, and meanwhile, the pull rods 3222 can move more smoothly in the arc-shaped clamping grooves 3231, so that the working efficiency of the stirring disc 322 is improved;
as shown in fig. 1, the control module is electrically connected to the mixing motor 106, the centrifugal motor 110, the adjusting motor 122, the lifting motor 123, the pressure pump 201, the electric heating rod 211, the wiping motor 2220, the infrared heating jacket 31, the main motor 320, the auxiliary motor 323 and the rotating motor, respectively, and the mixing motor 106, the centrifugal motor 110, the adjusting motor 122, the lifting motor 123, the pressure pump 201, the electric heating rod 211, the wiping motor 2220, the infrared heating jacket 31, the main motor 320, the auxiliary motor 323 and the rotating motor are commercially available products and are all powered by an external power supply.
Claims (10)
1. A system for resource utilization of high-salinity wastewater is characterized by comprising a solid-liquid separation module (1), a concentration module (2), an evaporation crystallization module (3) and a control module; the solid-liquid separation module (1), the concentration module (2), the evaporation crystallization module (3) and the control module are all fixedly arranged on the bottom plate (4);
the solid-liquid separation module (1) comprises a separation cylinder (10), a centrifugal assembly (11) and a filter pressing assembly (12); a water inlet pipe (100) is arranged at the upper position of the side wall of the separation cylinder (10), an installation frame (101) is arranged at the top of the separation cylinder (10), the inside of the separation cylinder (10) is connected with a limiting frame (103) through a fixed disc (102), and a certain gap is formed between the limiting frame (103) and the inner bottom of the separation cylinder (10); the centrifugal assembly (11) comprises a centrifugal motor (110), a centrifugal cylinder (111) and a guide cylinder (112), the guide cylinder (112) is fixedly connected to the middle of the fixed disc (102), a conical guide groove is formed in the bottom of the guide cylinder (112), the top of the guide cylinder (112) is higher than the fixed disc (102), the centrifugal motor (110) is fixedly arranged on the mounting frame (101), and the centrifugal cylinder (111) is arranged inside the guide cylinder (112) and connected with an output shaft of the centrifugal motor (110); the filter pressing assembly (12) comprises a filter pressing cylinder (120), a pressure plate (121), an adjusting motor (122) and a lifting motor (123), the pressure cylinder (120) is arranged on a limiting frame (103) and is located at the lower end of the conical diversion trench, a slag discharge pipe (1200) is arranged at the bottom of the filter pressing cylinder (120), the slag discharge pipe (1200) penetrates through the separating cylinder (10), the pressure plate (121) is arranged at an opening at the upper end of the filter pressing cylinder (120), the outer diameter of the pressure plate (121) is matched with the inner diameter of the filter pressing cylinder (120), a shaft sleeve (124) is arranged at the central position of the pressure plate (121), 3-6 fan-shaped adjusting plates (125) are uniformly arranged on the pressure plate (121), each fan-shaped adjusting plate (125) is connected with the pressure plate (121) through an adjusting screw rod (1250), one end of each adjusting screw rod (1250) penetrates through the shaft sleeve (124) and is provided with an auxiliary conical gear (1251), the connection parts of the pressure plate (121) and each fan-shaped adjusting plate (1211) are provided with guide blocks (1210), the adjusting motor (122) is arranged at the bottom in the separating cylinder (10), an output shaft (1220) of the adjusting motor (122) sequentially penetrates through the pressure filtering cylinder (120) and the shaft sleeve (124), a main bevel gear (1221) is connected onto the output shaft (1220) in a sliding and clamping manner, the main bevel gear (1221) is respectively meshed with each auxiliary bevel gear (1251), the lifting motor (123) is arranged at the bottom in the separating cylinder (10), a lifting lead screw (1230) is arranged on the output shaft of the lifting motor (123), and the lifting lead screw (1230) sequentially penetrates through the pressure filtering cylinder (120) and the pressure plate (121) and is in threaded connection with the pressure plate (121);
the concentration module (2) comprises a concentration tank (20), a heating assembly (21) and a condensed water collection assembly (22); a liquid spraying pipe (200) is vertically arranged at the center inside the concentration tank (20), a plurality of liquid spraying ports are uniformly formed in the liquid spraying pipe (200), the liquid spraying pipe (200) is communicated with the separation cylinder (10) through a guide pipe, and a pressure pump (201) is arranged at the connection part of the liquid spraying pipe and the separation cylinder; the heating assembly (21) comprises a mounting sleeve (210) and electric heating rods (211), 3-6 slots (2100) are uniformly arranged in the circumferential direction of the mounting sleeve (210), the number of the electric heating rods (211) is consistent with that of the slots (2100), the electric heating rods (211) are movably clamped in the slots (2100), and a plurality of heating fins (2110) are uniformly arranged in the circumferential direction of the electric heating rods (211); the condensed water collecting assembly (22) comprises a condensing plate (220) and a condensed water collecting tank (221), the condensing plate (220) is arranged at the top end in the concentrating tank (20), the condensing plate (220) is of a conical structure, the condensed water collecting tank (221) is movably clamped on the inner wall of the concentrating tank (20) and is abutted against the lower edge of the condensing plate (220), and a condensed water collecting pipe (2210) penetrating through the concentrating tank (20) is arranged on the condensed water collecting tank (221);
the evaporation crystallization module (3) comprises an evaporation box (30), an infrared heating sleeve (31) and a stirring assembly (32); the evaporation box (30) is connected with the concentration tank (20) through a guide pipe, a crystallization seat (33) is arranged in the evaporation box (30), a box door (300) is movably hinged to the position corresponding to the crystallization seat (33) on the side wall of the evaporation box (30), a heat exchange box (34) is connected to the outer wall of the evaporation box (30) through the guide pipe, a water outlet pipe (340) is arranged on the heat exchange box (34), an infrared heating sleeve (31) is fixedly clamped on the inner wall of the evaporation box (30), a stirring assembly (32) comprises a main motor (320), a hollow sleeve (321) and a stirring disc (322), the hollow sleeve (321) vertically penetrates through the evaporation box (30) and is rotatably clamped with the evaporation box (30), the main motor (320) is arranged at the outer top end of the evaporation box (30) and provides power for the hollow sleeve (321), and the stirring disc (322) is provided with 1-3 stirring discs, 1-3 stirring disks (322) are uniformly sleeved on the hollow sleeve (321);
the control module is respectively and electrically connected with the centrifugal motor (110), the adjusting motor (122), the lifting motor (123), the pressure pump (201) and the main motor (320).
2. The high-salinity wastewater resource utilization system according to claim 1, wherein the centrifugal cylinder (111) comprises a first net cylinder (1110) and a second net cylinder (1111), the second net cylinder (1111) is sleeved inside the first net cylinder (1110), the second net cylinder (1111) is sleeved inside the second net cylinder, and a separation screen plate (1112) is arranged between the second net cylinder (1111) and the first net cylinder (1110).
3. The high-salinity wastewater resource utilization system according to claim 1, characterized in that the fixed tray (102) is rotatably clamped with a mixing tray (104), the mixing tray (104) is uniformly provided with a plurality of mixing teeth, one side of the mixing tray (104) close to the guide shell (112) is provided with a first toothed sleeve (105), the mounting frame (101) is provided with a mixing motor (106), an output shaft of the mixing motor (106) is provided with a connecting gear, and the connecting gear is meshed with the first toothed sleeve (105).
4. The high-salinity wastewater resource utilization system according to claim 1, characterized in that two lifting motors (123) are provided, the two lifting motors (123) are respectively located at two sides of the adjusting motor (122), and the output shafts of the two lifting motors (123) are respectively provided with a lifting screw (1230).
5. The high-salinity wastewater resource utilization system according to claim 1, characterized in that both ends of each heating rod (211) are rotatably clamped with the upper end and the lower end of the slot (2100) through shaft heads (2111), a pinion is sleeved on each shaft head (2111) at the lower end of the slot (2100), a second toothed sleeve (2101) is rotatably clamped at the lower end of the mounting sleeve (210), the second toothed sleeves (2101) are meshed with the pinions and connected, a rotating motor is arranged at the bottom in the concentration tank (20), and the rotating motor provides power for the second toothed sleeves (2101).
6. The system for recycling high-salinity wastewater according to claim 1, characterized in that the stirring disc (322) comprises an outer disc (3220) and an inner disc (3221), the inner disc (3221) is sleeved inside the outer disc (3220), the inner disc (3221) and the outer disc (3220) are connected through 3-6 pull rods (3222), and a plurality of vertical stirring teeth (3223) are arranged at both the upper and lower ends of the outer disc (3220).
7. The high-salinity wastewater resource utilization system according to claim 6, characterized in that an auxiliary motor (323) is arranged at the top end of the evaporation box (30) through a motor frame, a rotating rod (3230) is connected to an output shaft of the auxiliary motor (323), the rotating rod (3230) is rotatably clamped inside the hollow sleeve (321), an arc-shaped clamping groove (3231) is arranged at a position corresponding to the stirring disc (322) on the rotating rod (3230), a sliding groove (3224) is arranged on the hollow sleeve (321), one end of each pull rod (3222) is fixedly connected with the outer disc (3220), and the other end of each pull rod penetrates through the inner disc (3221) and the sliding groove (3224) and is movably clamped with the arc-shaped clamping groove (3231).
8. The high-salinity wastewater resource utilization system according to claim 7, characterized in that a rotary ball head (3225) is arranged at the connection part of each draw bar (3222) and the arc-shaped clamping groove (3231).
9. The system for recycling high-salinity wastewater as claimed in claim 1, wherein the lower end of the condensation plate (220) is provided with a wiper strip (222), the wiper strip (222) is tightly attached to the lower end surface of the condensation plate (220), the top end of the concentration tank (20) is provided with a wiper motor (2220), and the wiper motor (2220) provides power for the wiper strip (222).
10. The high-salinity wastewater resource utilization system according to claim 7, characterized in that a rotary ball head (3225) is arranged at the joint of each arc-shaped clamping groove (3231) and the pull rod (3222).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202110404892.1A CN113149313A (en) | 2021-04-15 | 2021-04-15 | High salt waste water resource utilization's system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202110404892.1A CN113149313A (en) | 2021-04-15 | 2021-04-15 | High salt waste water resource utilization's system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN113149313A true CN113149313A (en) | 2021-07-23 |
Family
ID=76867565
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202110404892.1A Pending CN113149313A (en) | 2021-04-15 | 2021-04-15 | High salt waste water resource utilization's system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN113149313A (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115196707A (en) * | 2022-09-13 | 2022-10-18 | 威海海洋职业学院 | Seawater desalination pretreatment device |
| CN115477352A (en) * | 2022-11-01 | 2022-12-16 | 潘红 | High salt is evaporative concentration jar for waste water treatment |
| CN116217019A (en) * | 2023-05-09 | 2023-06-06 | 生态环境部华南环境科学研究所(生态环境部生态环境应急研究所) | Device and method for purifying mine acidic wastewater |
| CN118579965A (en) * | 2024-08-06 | 2024-09-03 | 山东千源多品种盐业有限公司 | Fish salt wastewater treatment device and treatment process thereof |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN207361977U (en) * | 2017-08-14 | 2018-05-15 | 东莞东元环境科技股份有限公司 | A kind of industry high-salt wastewater evaporative crystallization Zero discharging system |
| CN108773960A (en) * | 2018-07-09 | 2018-11-09 | 刘盈 | A kind of saliferous high concentrated organic wastewater processing unit and method |
| CN208667148U (en) * | 2018-06-08 | 2019-03-29 | 石家庄工大科技开发有限公司 | A kind of high-salt wastewater crystalline mother solution drying device |
| CN110395838A (en) * | 2019-08-23 | 2019-11-01 | 山西维纳泰克科技有限公司 | A kind of high-salt wastewater evaporative crystallization zero-emission equipment |
| CN111647493A (en) * | 2020-07-02 | 2020-09-11 | 冯步迎 | Filter equipment after fruit wine fermentation |
-
2021
- 2021-04-15 CN CN202110404892.1A patent/CN113149313A/en active Pending
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN207361977U (en) * | 2017-08-14 | 2018-05-15 | 东莞东元环境科技股份有限公司 | A kind of industry high-salt wastewater evaporative crystallization Zero discharging system |
| CN208667148U (en) * | 2018-06-08 | 2019-03-29 | 石家庄工大科技开发有限公司 | A kind of high-salt wastewater crystalline mother solution drying device |
| CN108773960A (en) * | 2018-07-09 | 2018-11-09 | 刘盈 | A kind of saliferous high concentrated organic wastewater processing unit and method |
| CN110395838A (en) * | 2019-08-23 | 2019-11-01 | 山西维纳泰克科技有限公司 | A kind of high-salt wastewater evaporative crystallization zero-emission equipment |
| CN111647493A (en) * | 2020-07-02 | 2020-09-11 | 冯步迎 | Filter equipment after fruit wine fermentation |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115196707A (en) * | 2022-09-13 | 2022-10-18 | 威海海洋职业学院 | Seawater desalination pretreatment device |
| CN115477352A (en) * | 2022-11-01 | 2022-12-16 | 潘红 | High salt is evaporative concentration jar for waste water treatment |
| CN115477352B (en) * | 2022-11-01 | 2024-03-01 | 潘红 | High salt wastewater treatment is with evaporation concentration jar |
| CN116217019A (en) * | 2023-05-09 | 2023-06-06 | 生态环境部华南环境科学研究所(生态环境部生态环境应急研究所) | Device and method for purifying mine acidic wastewater |
| CN116217019B (en) * | 2023-05-09 | 2023-07-21 | 生态环境部华南环境科学研究所(生态环境部生态环境应急研究所) | Device and method for purifying mine acidic wastewater |
| CN118579965A (en) * | 2024-08-06 | 2024-09-03 | 山东千源多品种盐业有限公司 | Fish salt wastewater treatment device and treatment process thereof |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN113149313A (en) | High salt waste water resource utilization's system | |
| CN208327573U (en) | A kind of municipal wastewater processing dedicated unit | |
| CN1778695A (en) | Waste liquid treatment and treating system thereof | |
| CN207120048U (en) | Mill iron filings stirring and washing dedusting drying unit | |
| CN113044959B (en) | Efficient biological aerated filter for wastewater treatment and operation method thereof | |
| CN117566951B (en) | Cutting fluid wastewater treatment process | |
| CN1522974A (en) | By-pass flow process for treating industrial cyclic cooling water | |
| CN219469747U (en) | MVR evaporation sewage treatment plant | |
| CN109095691A (en) | A kind of recycling processing method of brine waste | |
| CN215517035U (en) | High salt waste water resource utilization equipment | |
| CN114485190A (en) | Continuous calcining device is used in processing of pearlescent material that production efficiency is high | |
| CN115259266A (en) | Seawater desalination equipment based on solar energy | |
| CN103120867A (en) | Fully-automatic adjustable continuous blowdown device for industrial circulating water | |
| CN114084939A (en) | Super-frequency electric pulse desalted water treatment device | |
| CN221254288U (en) | Zero-discharge treatment equipment for salt-containing wastewater | |
| CN118184078B (en) | Industrial high-concentration salt-containing wastewater treatment process | |
| CN111547733A (en) | Method and equipment for purifying sodium-potassium feldspar powder | |
| CN219031871U (en) | Chemical reagent waste water treatment device | |
| CN216909233U (en) | Plant draws jar | |
| CN220201596U (en) | Sewage treatment device containing zinc sulfate | |
| CN215876557U (en) | Sedimentation tank for chemical waste residue treatment | |
| CN221579968U (en) | Combined sewage treatment device | |
| CN220149414U (en) | Wastewater desalination treatment system | |
| CN219239359U (en) | Dirty sour dearsenification device | |
| CN221557673U (en) | Filtering device for desalted water treatment |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20210723 |
|
| RJ01 | Rejection of invention patent application after publication |