CN215161645U - Intelligent control system for wastewater treatment for steel processing - Google Patents
Intelligent control system for wastewater treatment for steel processing Download PDFInfo
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- CN215161645U CN215161645U CN202120589351.6U CN202120589351U CN215161645U CN 215161645 U CN215161645 U CN 215161645U CN 202120589351 U CN202120589351 U CN 202120589351U CN 215161645 U CN215161645 U CN 215161645U
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Abstract
The embodiment of the utility model discloses steel processing is with waste water treatment intelligence control system. The embodiment of the utility model provides a technical scheme, this system includes: the first conveying assembly is used for pumping the collected pickling wastewater to the mixing tank; the second conveying assembly is used for pumping the uniformly mixed pickling wastewater to the oxidation tank; the oxidation-reduction instrument is arranged in the oxidation tank; the stirrer is arranged in the glue feather groove; the control module is used for controlling the working states of the first conveying assembly, the second conveying assembly, the oxidation-reduction instrument and the stirrer. The embodiment of the utility model realizes the pumping treatment of the pickling waste water by arranging a plurality of conveying components; an oxidation-reduction instrument is arranged to detect oxidation parameters in the corresponding oxidation tank so as to judge whether the pickling wastewater reaches the standard, and the intelligent treatment of pickling wastewater discharge and standard-reaching monitoring is realized through the components; and the sewage discharge in the generation process is reduced.
Description
Technical Field
The embodiment of the utility model provides a relate to water treatment technical field, especially relate to a waste water treatment intelligence control system is used in steel processing.
Background
At present, when steel is processed, water is an indispensable use resource, but the used water becomes waste water, and if the waste water is discharged, the natural environment is greatly influenced. The water after the steel processing needs to be treated before being discharged. Therefore, the need to design a solution capable of efficiently performing wastewater treatment has become a technical problem to be solved by those skilled in the art.
SUMMERY OF THE UTILITY MODEL
The embodiment of the utility model provides a waste water treatment intelligence control system for steel processing can realize the intelligent processing operation to pickling waste water through above-mentioned subassembly module.
In a first aspect, the embodiment of the utility model provides a waste water treatment intelligence control system is used in steel processing, include:
the first conveying assembly is used for pumping the collected pickling wastewater to the mixing tank to adjust the pH value of the pickling wastewater at the mixing tank;
the second conveying assembly is used for pumping the uniformly mixed pickling wastewater to an oxidation tank;
a redox meter disposed within the oxidation tank to detect oxidation parameters of the treated pickling wastewater within the oxidation tank;
the stirrer is arranged at the glue feather tank to ensure that the solution in the glue feather tank is fully mixed with the pickling wastewater to generate flocculate;
and the control module is used for controlling the working states of the first conveying assembly, the second conveying assembly, the oxidation-reduction instrument and the stirrer.
As an optional implementation manner, in the first aspect of the embodiments of the present invention, the mud scraper is electrically connected to the control module, and the mud scraper is configured to scrape the sediment in the settling tank.
As an optional implementation manner, in the first aspect of the embodiment of the present invention, the system further includes a sludge pump assembly electrically connected to the control module; the sludge pump assembly is used for pumping the sludge at the bottom of the settling tank to the sludge concentration tank.
As an optional implementation manner, in the first aspect of the embodiments of the present invention, the apparatus further includes a blower assembly electrically connected to the control module, the blower assembly includes a plurality of gas outlets, and the plurality of gas outlets respectively extend into the homogenizing tank, the oxidation tank, the adjusting tank, and the glue feather tank to fully mix the solution therein.
As an alternative implementation, in the first aspect of the embodiments of the present invention, the blower assembly includes a first blower and a second blower, and the first blower and the second blower are both robust blowers.
As an optional implementation manner, in the first aspect of the embodiments of the present invention, the apparatus further includes a drug adding device electrically connected to the control module, and the drug adding device is configured to add a drug solution to the oxidation tank and/or the adjustment tank.
As an optional implementation mode, in the first aspect of the embodiments of the present invention, the PH detection module electrically connected to the control module is further included, the PH detection module is configured to send the detected PH value in the adjustment tank to the control module, and the control module controls the start or stop of the corresponding dosing device according to the PH value.
As an optional implementation manner, in the first aspect of the embodiments of the present invention, the control system further includes a sludge treatment assembly, where the sludge treatment assembly includes a sludge pump and a filter press electrically connected to the control module; the mud pump is used for pumping the sludge in the sludge concentration tank to a filter press for filter pressing treatment, and the filter press is used for carrying out filter pressing treatment on the sludge in the filter press.
As an optional implementation manner, in the first aspect of the embodiments of the present invention, the intelligent control system further includes a purification system, and the purification system includes:
the conveying pump assembly is used for pumping the precipitated water subjected to the precipitation treatment of the water storage tank to the filtering device for filtering operation;
the filtering device comprises a first filtering device and a second filtering device which are sequentially communicated, the first filtering device is used for carrying out primary filtering on the precipitated water pumped into the first filtering device, the second filtering device is used for carrying out secondary filtering on the precipitated water entering the second filtering device, and the precipitated water subjected to the secondary filtering is discharged to a drainage well;
the backwashing pump is used for pumping water at the drainage well to the first filtering device and/or the second filtering device so as to perform backwashing operation on the first filtering device and/or the second filtering device;
the conveying pump assembly, the filtering device and the backwashing pump are electrically connected with the control module, and the control module is used for controlling the starting or stopping of the conveying pump assembly, the filtering device and the backwashing pump.
As an alternative implementation, in the first aspect of the embodiments of the present invention, the first filtering device includes a sand filtering tower, and the second filtering device includes an activated carbon tower; the sand filtration tower is provided with a first electromagnetic valve, a second electromagnetic valve, a third electromagnetic valve, a fourth electromagnetic valve and a fifth electromagnetic valve which are electrically connected with the control module, and the activated carbon tower is provided with a sixth electromagnetic valve, a seventh electromagnetic valve, an eighth electromagnetic valve, a ninth electromagnetic valve and a tenth electromagnetic valve which are electrically connected with the control module; each electromagnetic valve is used for controlling the on-off of the corresponding water inlet and outlet.
The embodiment of the utility model realizes the pumping treatment of the pickling waste water by arranging a plurality of conveying components; an oxidation-reduction instrument is arranged to detect oxidation parameters in the corresponding oxidation tank so as to judge whether the pickling wastewater reaches the standard, and the intelligent treatment of pickling wastewater discharge and standard-reaching monitoring is realized through the components; the intelligent monitoring degree of waste water in the steel processing process is greatly improved, and the pollution discharge is reduced.
Drawings
FIG. 1 is a schematic structural view of an intelligent control system for treating waste water in steel processing provided by an embodiment of the present invention;
FIG. 2 is a schematic block diagram of a circuit of the intelligent control system for treating waste water in steel processing provided by the embodiment of the present invention;
FIG. 3 is a schematic structural view of an intelligent control system for purifying waste water for steel processing according to an embodiment of the present invention;
FIG. 4 is a schematic block diagram of a circuit of the intelligent control system for purifying waste water in steel processing provided by the embodiment of the present invention;
fig. 5 is a schematic structural view of a delivery pump assembly provided by an embodiment of the present invention;
fig. 6 is a schematic structural diagram of a filtering apparatus according to an embodiment of the present invention.
Reference numerals: v1, collecting tank; v2, a mixing tank; v3, an oxidation tank; v4, adjusting groove; v5, glue feather groove; v6, a precipitation tank; v7, a water storage tank; v8, a relief well; v9, open channel; 1. a first conveying assembly; 2. a second transport assembly; 3. a blender; 4. a mud scraper; 5. a sludge pump assembly; 6. a redox meter; 7. a delivery pump assembly; 71. a first delivery pump; 72. a second delivery pump; 8. a sand filtration tower; 81. a first solenoid valve; 82. a second solenoid valve; 83. a third electromagnetic valve; 84. a fourth solenoid valve; 85. a fifth solenoid valve; 9. an activated carbon tower; 91. a sixth electromagnetic valve; 92. a seventh electromagnetic valve; 93. an eighth solenoid valve; 94. a ninth electromagnetic valve; 95. a tenth solenoid valve; 10. and (4) backwashing the pump.
Detailed Description
In order to make the objects, technical solutions and advantages of the present invention clearer, the following describes in detail specific embodiments of the present invention with reference to the accompanying drawings. It should be noted that, without conflict, any combination between the embodiments or technical features described below may form a new embodiment. Except as specifically noted, the materials and equipment used in this example are commercially available. Examples of embodiments are illustrated in the accompanying drawings, wherein like or similar reference numerals refer to the same or similar elements or elements having the same or similar function throughout. The embodiments described below with reference to the drawings are exemplary only for the purpose of explaining the present application and are not to be construed as limiting the present application.
In the description of the present application, it is to be understood that the terms "upper", "lower", "front", "back", "vertical", "horizontal", "top", "bottom", "inner", "outer", and the like, indicate orientations or positional relationships based on the orientations or positional relationships shown in the drawings, are merely for convenience in describing the present application and simplifying the description, and do not indicate or imply that the device or element being referred to must have a particular orientation, be constructed and operated in a particular orientation, and thus, should not be construed as limiting the present application. In the description of the present application, "a plurality" means two or more unless specifically stated otherwise.
In the description of the present application, it should be noted that unless otherwise specifically stated or limited, the terms "connected," "communicating," and "connected" are to be construed broadly, e.g., as meaning a fixed connection, a connection through an intervening medium, a connection between two elements, or an interaction between two elements. The specific meaning of the above terms in the present application can be understood by those of ordinary skill in the art as appropriate.
The terms "first," "second," and the like in the description and in the claims of the present application and in the above-described drawings are used for distinguishing between similar elements and not necessarily for describing a particular sequential or chronological order. Furthermore, the terms "comprises," "comprising," and "having," and any variations thereof, are intended to cover a non-exclusive inclusion, such that a process, method, system, article, or apparatus that comprises a list of steps or elements is not necessarily limited to those steps or elements expressly listed, but may include other steps or elements not expressly listed or inherent to such process, method, article, or apparatus.
Fig. 1 is the utility model provides a waste water treatment intelligence control system for steel processing's schematic structure diagram, fig. 2 are the utility model provides a waste water treatment intelligence control system for steel processing's circuit schematic block diagram, as shown in fig. 1 and fig. 2, the embodiment of the utility model provides a waste water treatment intelligence control system for steel processing, include:
the first conveying assembly 1 is used for pumping the collected pickling wastewater to a homogenizing tank V2 so as to regulate the pH value of the pickling wastewater at a homogenizing tank V2; the pickling wastewater is mainly stored in a pickling wastewater collection tank V1, the collection tank V1 collects wastewater generated in the steel processing process, and the first conveying assembly 1 comprises two conveying pumps for pumping the wastewater in the collection tank V1 to a homogenizing tank V2 to adjust the pH value of the corresponding wastewater.
The second conveying assembly 2 is used for pumping the well-conditioned pickling wastewater to an oxidation tank V3; NaOH is arranged in the mixing tank V2 to adjust the pH value of water, so that the wastewater can meet the discharge requirement on the pH value detection index; the homogenized pickling waste water is pumped by the second transfer module 2 to the oxidation tank V3, but a redox meter 6 is provided in the oxidation tank V3 for data monitoring thereof. A redox meter 6, said redox meter 6 being disposed within the oxidation tank V3 for detecting oxidation parameters of the treated pickling wastewater within the oxidation tank V3. The utility model discloses redox appearance also is the ORP module, and the ORP module is used for detecting the oxidation reduction potential of solution, and the oxidation reduction potential is the macroscopical redox nature that is used for reflecting all materials in the aqueous solution and shows. The higher the redox potential, the stronger the oxidation, and the lower the redox potential, the stronger the reduction. A positive potential indicates that the solution exhibits a certain degree of oxidation, while a negative potential indicates that the solution exhibits a certain degree of reduction.
A stirrer 3, wherein the stirrer 3 is arranged at the glue feather groove V5 so as to fully mix the solution in the glue feather groove V5 with the pickling wastewater and generate flocs; an adjusting tank V4 is arranged in front of the glue feather tank V5, the adjusting tank V4 is mainly used for further adjusting the pH value of the acid pickling wastewater, a flocculating agent is added into the glue feather tank V5 to enable the wastewater from the adjusting tank V4 to flocculate and then generate flocculates, and during specific implementation, a stirrer 3 is added to improve the flocculation effect in the whole glue feather tank V5.
And the control module is used for controlling the working states of the first conveying assembly 1, the second conveying assembly 2, the oxidation-reduction instrument 6 and the stirrer 3.
More preferably, still include the PH detection module with control module electric connection, the PH detection module is used for sending the pH valve in the adjustment tank V4 who detects to control module, control module is according to the pH valve controls the start or the stop of corresponding charge device.
The embodiment of the utility model provides an in PH detection module and redox appearance 6 be used for showing quality of water situation and control dosing, when carrying out concrete implementation, PH detection module need carry out once weekly the calibration and improve entire system's the degree of accuracy. The first conveying assembly 1 and the second conveying assembly 2 are mainly used for realizing the circulation of water in each water tank.
More preferably, the sludge scraper 4 is electrically connected with the control module, and the sludge scraper 4 is used for scraping the sediments in the settling tank V6. The settling tank V6 is arranged behind the glue feather tank V5, and the mud scraper 4 mainly scrapes mud from the sediment in the settling tank V6, so that the settling tank V6 can be sent to the rear end in two paths for further purification treatment; one path can be directly pumped to a water storage tank of the purification system to store water, and the other path can be pumped to a sludge concentration tank through a sludge pump to be further processed. In the specific implementation of the scheme, the oxidation tank V3, the adjusting tank V4, the glue feather tank V5 and the precipitation tank V6 are arranged side by side in sequence, and when the wastewater circulation treatment is carried out, the wastewater circulation treatment can be carried out in various modes, such as pumping treatment by a water pump or treatment by overflow operation; when the overflow operation treatment is adopted, the treatment can be carried out in a way that a channel is arranged in the groove, namely a first channel is arranged between the oxidation groove V3 and the adjusting groove V4, a second channel is arranged between the adjusting groove V4 and the glue feather groove V5, a third channel is arranged between the glue feather groove V5 and the precipitation groove V6, the height of the first channel is higher than that of the second channel, and the height of the second channel is higher than that of the third channel; the backflow-free condition can be guaranteed through the arrangement.
More preferably, the device also comprises a sludge pump assembly 5 electrically connected with the control module; the sludge pump assembly 5 is used for pumping the sludge at the bottom of the settling tank V6 to a sludge concentration tank. The control system also comprises a sludge treatment assembly, wherein the sludge treatment assembly comprises a sludge pump and a filter press which are electrically connected with the control module; the mud pump is used for pumping the sludge in the sludge concentration tank to a filter press for filter pressing treatment, and the filter press is used for carrying out filter pressing treatment on the sludge in the filter press. In the specific treatment mode of the filtered sludge, after the treatment of the filter press is completed, the corresponding sludge is transported to a sludge truck and is transported away.
More preferably, the device further comprises a blower assembly electrically connected with the control module, wherein the blower assembly comprises a plurality of air outlets, and the air outlets respectively extend into the mixing tank V2, the oxidation tank V3, the adjustment tank V4 and the glue feather tank V5 so as to fully mix the solution in the mixing tank V2, the oxidation tank V3, the adjustment tank V4 and the glue feather tank V5. More preferably, the blower assembly includes a first blower and a second blower, both of which are robust blowers. The fan is arranged to improve the mixing degree of the solution.
More preferably, the device also comprises a drug adding device which is electrically connected with the control module and is used for adding liquid medicine to the oxidation tank V3 and/or the adjusting tank V4.
The pickling wastewater mainly contains Fe2+,Fe2+Is a very unstable ion, thereby treating Fe2+It is first oxidized into Fe3+And then hydroxide precipitate is formed and removed. The treatment of acid pickling waste water is often carried out by adopting aeration and adding oxidant (NaOCl, H)2O2) The method of (1):
Fe2++O2→Fe3+;
Fe3++3OH-→Fe(OH)3↓;
in the embodiment of the utility model, the NaOCl oxidation method is adopted for processing, and the neutralizer adopts NaOH to process:
Fe2++OCl-→Fe3+;
Fe3++OH-→Fe(OH)3↓;
specifically, charge device is used for adding concentration for 20% NaOH in collecting vat V1, adjustment tank V4, and this charge device still is used for adding NaOCl medicament in oxidation tank V3, adds the application time, can adopt the mode that the ration was added, and the medicament amount that also is adding each time is fixed, and the other kind can also carry out the medicine operation through the PH value that detects corresponding inslot, when corresponding inslot PH value reached the default, then control stops to add the medicine operation.
The utility model discloses the scheme still is provided with pilot lamp, liquid level detection module etc. and detects, shows the liquid level state that reminds the current each inslot of user through liquid level detection module and pilot lamp linkage, when appearing unusually, can also report to the police through bee calling organ and handle.
The embodiment of the utility model realizes the pumping treatment of the pickling waste water by arranging a plurality of conveying components; the oxidation parameters in the corresponding oxidation tank V3 are detected by arranging the oxidation-reduction instrument 6 to judge whether the pickling wastewater reaches the standard, and the intelligent treatment of pickling wastewater discharge and standard-reaching monitoring is realized by the components; the intelligent monitoring degree of waste water in the steel processing process is greatly improved, and the pollution discharge is reduced.
More preferably, the intelligent control system further comprises a purification system, in the embodiment of the present invention, the purification system refers to an intelligent purification control system, and fig. 3 is a schematic structural diagram of the intelligent wastewater purification control system for steel processing provided in the embodiment of the present invention; fig. 4 is the embodiment of the utility model provides a steel processing is with waste water purification intelligence control system's circuit schematic block diagram, as shown in fig. 3 and fig. 4, the utility model discloses the implementation provides a steel processing is with waste water purification intelligence control system, include:
a delivery pump assembly 7 for pumping the precipitation water subjected to the precipitation treatment by the water storage tank V7 to a filtering device for a filtering operation;
the filtering device comprises a first filtering device and a second filtering device which are sequentially communicated, the first filtering device is used for carrying out primary filtering on the precipitated water pumped into the first filtering device, the second filtering device is used for carrying out secondary filtering on the precipitated water entering the second filtering device, and the precipitated water subjected to the secondary filtering is discharged to a drainage well V8;
the backwashing pump 10 is used for pumping water at the drain well V8 to the first filtering device and/or the second filtering device to perform backwashing operation on the first filtering device and/or the second filtering device;
and the control module is electrically connected with the delivery pump assembly 7, the filtering device and the backwashing pump 10, and is used for controlling the starting or stopping of the delivery pump assembly 7, the filtering device and the backwashing pump 10. More preferably, the control system further comprises a water storage tank V7 for receiving and storing the treated pickling wastewater and performing precipitation treatment on the pickling wastewater to obtain corresponding precipitation water.
The utility model discloses the scheme is used for carrying out further processing to the waste water through chemical treatment, owing to still there is the precipitate in the waste water of having carried out chemical treatment, consequently need further carry out filtration treatment to it, through the utility model discloses the scheme of embodiment can realize more efficient filter effect. Deposit in earlier putting into aqua storage tank V7 through chemical treatment's waste water, after the sediment of a period of time, carry out waste water extraction operation to it, in the embodiment of the utility model provides an extract the operation through the waste water that delivery pump subassembly 7 comes in to aqua storage tank V7, extract to filter equipment in and filter, then discharge to the well V8 department of releasing of no impurity pollution after will filtering. Because the filtering structure in the filtering device can continuously filter the wastewater in long-term use, a large amount of dirt can be accumulated at the filtering structure, and the subsequent wastewater filtering effect can be influenced. The embodiment of the utility model provides an in the embodiment set up the reverse-flow pump and come to carry out the backwash to the filtration to filter equipment with the clean water pumpback in the drainage well V8 and then reach the purpose of clean filter equipment, in the embodiment of the utility model embodiment realize the backwash only through increasing the reverse-flow pump, make it can also reach better filter effect under the prerequisite that reduces the device and use to when drawing water, what draw is the water of drainage well V8 department, need not extra waste water resource, improve the environmental protection degree of the whole use of system greatly; the energy consumption is reduced, and the cleaning device is simple and convenient and is easier to use compared with the existing cleaning mode. No chemicals are added to the tank V7 to treat the waste water, and it is used mainly as a water storage device to store the waste water.
The embodiment of the utility model provides a water in the relief well V8 has been through handling harmless water, and the height in the relief well V8 is limited, when constantly handling waste water, then can constantly produce harmless water to relief well V8 department, when surpassing preset height, then the water spills over relief well V8 to open channel V9 and discharges.
More preferably, fig. 5 is a schematic structural diagram of the transfer pump assembly 7 provided in the embodiment of the present invention, and as shown in fig. 5, the transfer pump assembly 7 provided in the embodiment of the present invention includes a first transfer pump 71 and a second transfer pump 72, an input pipeline of the first transfer pump 71 is communicated with an input pipeline of the second transfer pump 72 and the water storage tank V7; the output pipeline of the first conveying pump 71 is communicated with the output pipeline of the second conveying pump 72 and the water inlet end of the first filtering device.
The embodiment of the utility model provides an in according to filter equipment's filter capacity match corresponding quantity's delivery pump, it is concrete in the embodiment of the utility model provides an improve holistic volume of drawing water through the mode parallelly connected with two delivery pumps, if there is actual demand at this in-process, also can match 3 or 4 delivery pumps according to filter equipment's filter capacity and accomplish filtering operation. And if in practice the filter device is in a higher position, in order to increase the delivery head of the pump assembly 7, a corresponding delivery pump can be connected in series to increase the delivery head.
More preferably, fig. 6 is a schematic structural diagram of the filtering apparatus provided in the embodiment of the present invention, and as shown in fig. 6, the first filtering apparatus provided in the embodiment of the present invention includes a sand filtering tower 8, and the second filtering apparatus includes an activated carbon tower 9; the sand filtering tower 8 comprises quartz sand for filtering particulate matters in water, and the sand filtering tower 8 sends water to the active carbon tower 9 or the regulating tank V2 through a ball valve switch; the activated carbon tower 9 comprises activated carbon for filtering impurities in water, the activated carbon tower 9 is used for delivering water to the drain well V8 by a ball valve closure, the embodiment of the utility model discloses a specific implementation manner, except that the first filtering device comprises a sand filter tower 8, the second filtering device comprises an activated carbon tower 9, the first filtering device can also comprise a sand filter tower 8, the second filtering device comprises two activated carbon towers 9; deeper filtration is achieved by the above combination. Specifically, the combination of the sand filtration tower 8 and the activated carbon tower 9 will be described in detail. The sand filtration tower 8 is provided with a first electromagnetic valve 81, a second electromagnetic valve 82, a third electromagnetic valve 83, a fourth electromagnetic valve 84 and a fifth electromagnetic valve 85 which are electrically connected with the control module, and the activated carbon tower 9 is provided with a sixth electromagnetic valve 91, a seventh electromagnetic valve 92, an eighth electromagnetic valve 93, a ninth electromagnetic valve 94 and a tenth electromagnetic valve 95 which are electrically connected with the control module; each electromagnetic valve is used for controlling the on-off of the corresponding water inlet and outlet.
The embodiment of the utility model provides an in 8 sand filtration towers can effectually hold back suspended solid, organic matter, colloidal particle, microorganism, chlorine of detaching aquatic, smell flavor and partial heavy metal ion etc. reach a high-efficient filtration equipment that reduces water turbidity, water purification effect. The quartz sand filter is generally used as a pretreatment of reverse osmosis equipment and ultrafiltration equipment, and is mainly used for intercepting and adsorbing silt, colloid, metal ions and organic matters. The sand filtration tower 8 is provided with an equipment main body, the equipment main body is provided with a water inlet and a water outlet, a composite multi-medium filter medium is arranged in the equipment main body, the composite multi-medium filter medium comprises a water collecting chamber and a water outlet, the water collecting chamber is formed between the bottom of the equipment main body and the filter medium, and the water outlet is communicated with the water collecting chamber. Waste water passes through the pipeline and introduces into the equipment main part from the water inlet in, flows from top to bottom under the action of gravity, filters through compound many medium filter medium at the flow in-process, and the water after the filtration converges to the collecting chamber, then carries away through the delivery port, can carry to activated carbon tower 9 department, also can carry to the groove of mixing V2. The filtration resistance is increased along with the increase of the trapped and adsorbed pollutants in the filter material layer, and when the resistance exceeds the set resistance, the penetration of the trapped matters can be generated by continuing the filtration, so that the quality of the filtered and adsorbed effluent is deteriorated. And stopping filtering, and making the water flow reversely, namely the water flow from bottom to top, and performing back washing on the composite multi-medium filter material layer so as to facilitate subsequent filtering.
The equipment body is a cylindrical steel structure with upper and lower elliptical seal heads, the filter is made of Q235-A or 304 stainless steel, the lining is made of vulcanized rubber and is anticorrosive, a water distributor is arranged at the water inlet inside the equipment body, a water collecting device is arranged at the lower part of the equipment body, and 1400mm quartz sand is filled in the water collecting device. When the quartz sand filter operates until the pressure difference between the inlet and the outlet is 0.07MPa, backwashing is required. The purpose of back flush is to loosen the filter layer and flush the trapped matter away, thereby cleaning the filter layer. The length of the backflushing time is related to the interception of the filter layer and the backflushing flow rate. The backwash discharge should not contain normal particulate filter media. And during backwashing, the water inlet valve and the water outlet valve are closed, the backwashing discharge valve and the backwashing valve are opened, the backwashing time is determined by the backwashing drainage turbidity, and generally the backwashing is carried out until the drainage turbidity is less than 3mg/l and is not less than 20 minutes.
The scheme of the embodiment of the utility model is that the filtration and the backwashing operation of the wastewater are controlled by the on-off of the electromagnetic valve; specifically, the positions of the electromagnetic valves at the sand filtration tower 8 are as follows: the first solenoid valve 81 and the third solenoid valve 83 are respectively arranged at different water inlets, the second solenoid valve 82 and the fourth solenoid valve 84 are respectively arranged at different water outlets, and the first water outlet of the channel where the fifth solenoid valve 85 is located is communicated. The positions of the electromagnetic valves of the activated carbon tower 9 are as follows: the sixth solenoid valve 91 and the eighth solenoid valve 93 are respectively arranged at different water inlets, the seventh solenoid valve 92 and the ninth solenoid valve 94 are respectively arranged at different water outlets, and the first water outlet of the channel where the tenth solenoid valve 95 is located is communicated.
The embodiment of the utility model adopts the mode of automatic control of the control module to operate, when the active carbon tower 9 is not put into use; the control logic of each use state and each valve is as follows: 1. when the filtering device is used for collecting water, valves 1, 4, 7 and 9 are required to be opened, and valves 2, 3, 5, 6, 8 and 10 are required to be closed; 2. when sand filtration backwashing operation is carried out, valves No. 2 and 3 need to be opened, and valves No. 1, 4, 5, 6, 7, 8, 9 and 10 need to be closed; 3. when the sand filtration cleaning operation is carried out, the valves No. 1 and 5 are required to be opened, and the valves No. 2, 3, 4, 6, 7, 8, 9 and 10 are required to be closed. When the activated carbon tower 9 is put into use, the control logics of each use state and each valve are as follows: 1. when the filtering device is used for collecting water, valves 1, 4, 6 and 9 are required to be opened, and valves 2, 3, 5, 7, 8 and 10 are required to be closed; 2. when sand filtration backwashing operation is carried out, valves No. 2 and 3 need to be opened, and valves No. 1, 4, 5, 6, 7, 8, 9 and 10 need to be closed; 3. when the sand filtration cleaning operation is carried out, the valves 1 and 5 need to be opened, and the valves 2, 3, 4, 6, 7, 8, 9 and 10 need to be closed; 4; when the activated carbon backwashing operation is carried out, valves 1, 4, 7 and 8 need to be opened, and valves 2, 3, 5, 6, 9 and 10 need to be closed; 5. when the activated carbon cleaning operation is carried out, valves 1, 4, 6 and 10 are required to be opened, and valves 2, 3, 5, 7, 8 and 9 are required to be closed. The above is the complete control logic used by the whole filtering device; when setting, the setting needs to be set as a fixed control logic, and the fixed control logic is functionally stored, and a corresponding entity key or a virtual key is set to perform a trigger operation. The manual operation processing of professional operators is not needed, and the integral automatic processing degree is improved.
More preferably, the intelligent control system further comprises a blower assembly electrically connected with the control module, and an air outlet of the blower assembly is communicated with an air inlet of the sand filtration tower 8 and/or the activated carbon tower 9. Air input of the sand filtration tower 8 and the activated carbon tower 9 is improved by arranging the blower assembly, and cleaning degree is improved in a gas-water mixing mode.
More preferably, a first liquid level detection module electrically connected with the control module is arranged in the water storage tank V7, and the first liquid level detection module is used for detecting a liquid level state in the water storage tank V7 so that the control module controls the start and stop state of the system. The liquid level detection module is arranged mainly for detecting the liquid level height in the water storage tank V7, the corresponding delivery pump assembly 7 is controlled to be started only when the liquid level in the water storage tank V7 is higher than the set lowest liquid level, and then the wastewater is pumped to the sand filtration tower 8 for filtration. If the liquid level in the water storage tank V7 is too low, when the delivery pump assembly 7 is started, all waste water is pumped out relatively quickly, and then the delivery pump can run idle or continuously start and stop, so that the stability of the whole system is affected. Therefore, a minimum liquid level is set to ensure stable and efficient operation of the whole system. When the liquid level is set, a single liquid level can be set for starting and stopping control, and a plurality of liquid levels can be set for combined control; for example, the second-level liquid level can be set for control, the first-level liquid level is higher than the second-level liquid level, when the second-level liquid level is lower than the second-level liquid level, all the delivery pumps are controlled to stop working, when the first-level liquid level and the second-level liquid level are located, one of the delivery pumps is controlled to work, and when the first-level liquid level is higher than the second-level liquid level, two delivery pumps are controlled to work. Specifically, different liquid level control modes can be configured according to the number of the delivery pumps.
More preferably, a second liquid level detection module electrically connected to the control module is arranged in the tapping well V8, and the second liquid level detection module is configured to detect a liquid level state in the tapping well V8, so that the control module controls a start/stop state of the system. The same purpose of setting the second liquid level detection module is also to prevent the situation that the water level is too low to cause complete cleaning, because if the water level in the drainage well V8 is too low, enough water cannot be extracted to backwash the sand filter tower 8 or the activated carbon tower 9, and therefore, when the water level in the drainage well V8 is detected, the setting needs to be carried out according to the water quantity required by cleaning the sand filter tower 8 and the activated carbon tower 9 once. When the sand filtration tower 8 or the active carbon tower 9 is backwashed, the starting conditions are as follows: 1. a liquid level detection state; 2. whether the backwashing time of the sand filtration tower 8 or the activated carbon tower 9 is reached; 3. whether the operating pressure of the sand filtration tower 8 or the activated carbon tower 9 reaches the set value of the backwashing pressure or not. And controlling to start the backwashing operation only when the conditions are met.
More preferably, the water storage tank further comprises a control module electrically connected to the first display module and the second display module, wherein the first display module is used for displaying the liquid level height in the water storage tank V7; the second display module is used for displaying the liquid level height of the relief well V8. The liquid level height in the water storage tank V7 and the releasing well V8 can be visually displayed through the display module, so that a user can have visual feeling. When the system control operation is carried out, two modes can be selected, one mode is an automatic mode, the other mode is a manual mode, namely, the electric control operation of all devices in the system can be automatically carried out, and the manual control operation can be conveniently carried out by a worker according to the favorite mode. Most preferably, in the embodiment of the utility model, the automatic control mode is adopted, and through the operation, the personnel cost of an enterprise can be reduced, so that the enterprise can use the device on duty without training corresponding personnel; the overall stability is also better.
More preferably, the first delivery pump 71, the second delivery pump 72 and the reverse water pump are electrically connected to the control module through corresponding switch modules, and the switch modules are used for switching the first delivery pump 71, the second delivery pump 72 and the reverse water pump to any one of a manual mode, an automatic mode or a shutdown mode. The monitoring module is electrically connected with the control module and used for displaying the state of each device in the system. That is the embodiment of the utility model provides an in the delivery pump can adopt syllogic control mode to control the delivery pump, can switch to automatic, manual or closed condition, when being in closed condition, then can't start corresponding equipment. Except for the three-section control mode, the monitoring module is also adopted to monitor and display the running state of each device, and when abnormal conditions are detected, the monitoring module is used for displaying the running state so that the working personnel can know the state of the device and conduct troubleshooting.
The embodiment of the utility model provides a realize filtering and then reach waste water purification's purpose through setting up filter equipment the precipitation water in the aqua storage tank V7 to realize the backwashing operation to filter equipment through setting up backwashing pump 10, guarantee this clean system's purifying effect in a period, can promote filter equipment's life greatly through backwashing pump 10's setting.
The foregoing is only a preferred embodiment of the invention and the technical principles applied thereto. The present invention is not limited to the specific embodiments described herein, but is capable of various obvious changes, rearrangements and substitutions as will now become apparent to those skilled in the art without departing from the scope of the invention. Therefore, although the present invention has been described in more detail with reference to the above embodiments, the present invention is not limited to the above embodiments, and may include other equivalent embodiments without departing from the scope of the present invention.
Claims (10)
1. The utility model provides a waste water treatment intelligence control system for steel processing which characterized in that includes:
the first conveying assembly is used for pumping the collected pickling wastewater to the mixing tank to adjust the pH value of the pickling wastewater at the mixing tank;
the second conveying assembly is used for pumping the uniformly mixed pickling wastewater to an oxidation tank;
a redox meter disposed within the oxidation tank to detect oxidation parameters of the treated pickling wastewater within the oxidation tank;
the stirrer is arranged at the glue feather tank to ensure that the solution in the glue feather tank is fully mixed with the pickling wastewater to generate flocculate;
and the control module is used for controlling the working states of the first conveying assembly, the second conveying assembly, the oxidation-reduction instrument and the stirrer.
2. The intelligent control system for wastewater treatment for steel processing according to claim 1, further comprising a mud scraper electrically connected to the control module, wherein the mud scraper is configured to scrape the sediment in the settling tank.
3. The intelligent control system for wastewater treatment for steel processing as set forth in claim 1, further comprising a sludge pump assembly electrically connected to the control module; the sludge pump assembly is used for pumping the sludge at the bottom of the settling tank to the sludge concentration tank.
4. The intelligent control system for wastewater treatment for steel processing according to claim 1, further comprising a blower assembly electrically connected to the control module, wherein the blower assembly comprises a plurality of air outlets, and the plurality of air outlets respectively extend into the homogenizing tank, the oxidation tank, the adjusting tank and the glue feather tank to fully mix the solution therein.
5. The intelligent control system for steel processing wastewater treatment according to claim 4, wherein the blower assembly comprises a first blower and a second blower, both of which are Roots blowers.
6. The intelligent control system for treating the wastewater for the processing of the steel products as set forth in claim 1, further comprising a chemical dosing device electrically connected to the control module, wherein the chemical dosing device is used for adding a chemical solution to the oxidation tank and/or the adjustment tank.
7. The intelligent control system for wastewater treatment for steel processing according to claim 6, further comprising a PH detection module electrically connected to the control module, wherein the PH detection module is configured to send the detected pH value in the adjustment tank to the control module, and the control module controls the corresponding dosing device to start or stop according to the pH value.
8. The intelligent control system for wastewater treatment for steel processing as recited in claim 1, further comprising a sludge treatment assembly, wherein the sludge treatment assembly comprises a sludge pump and a filter press electrically connected to the control module; the mud pump is used for pumping the sludge in the sludge concentration tank to a filter press for filter pressing treatment, and the filter press is used for carrying out filter pressing treatment on the sludge in the filter press.
9. The intelligent control system for wastewater treatment for steel processing according to any one of claims 1 to 8, further comprising a purification system, the purification system comprising:
the conveying pump assembly is used for pumping the precipitated water subjected to the precipitation treatment of the water storage tank to the filtering device for filtering operation;
the filtering device comprises a first filtering device and a second filtering device which are sequentially communicated, the first filtering device is used for carrying out primary filtering on the precipitated water pumped into the first filtering device, the second filtering device is used for carrying out secondary filtering on the precipitated water entering the second filtering device, and the precipitated water subjected to the secondary filtering is discharged to a drainage well;
the backwashing pump is used for pumping water at the drainage well to the first filtering device and/or the second filtering device so as to perform backwashing operation on the first filtering device and/or the second filtering device;
the conveying pump assembly, the filtering device and the backwashing pump are electrically connected with the control module, and the control module is used for controlling the starting or stopping of the conveying pump assembly, the filtering device and the backwashing pump.
10. The intelligent control system for wastewater treatment for steel processing as set forth in claim 9, wherein the first filtration device comprises a sand filtration tower and the second filtration device comprises an activated carbon tower; the sand filtration tower is provided with a first electromagnetic valve, a second electromagnetic valve, a third electromagnetic valve, a fourth electromagnetic valve and a fifth electromagnetic valve which are electrically connected with the control module, and the activated carbon tower is provided with a sixth electromagnetic valve, a seventh electromagnetic valve, an eighth electromagnetic valve, a ninth electromagnetic valve and a tenth electromagnetic valve which are electrically connected with the control module; each electromagnetic valve is used for controlling the on-off of the corresponding water inlet and outlet.
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