CN113880312A - Wastewater circulating treatment system and method for stone processing - Google Patents
Wastewater circulating treatment system and method for stone processing Download PDFInfo
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- CN113880312A CN113880312A CN202111323425.2A CN202111323425A CN113880312A CN 113880312 A CN113880312 A CN 113880312A CN 202111323425 A CN202111323425 A CN 202111323425A CN 113880312 A CN113880312 A CN 113880312A
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- 239000002351 wastewater Substances 0.000 title claims abstract description 68
- 239000004575 stone Substances 0.000 title claims abstract description 59
- 238000012545 processing Methods 0.000 title claims abstract description 46
- 238000000034 method Methods 0.000 title claims abstract description 25
- 238000004062 sedimentation Methods 0.000 claims abstract description 91
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 83
- 238000005189 flocculation Methods 0.000 claims abstract description 73
- 230000016615 flocculation Effects 0.000 claims abstract description 73
- 238000001914 filtration Methods 0.000 claims abstract description 21
- 230000008569 process Effects 0.000 claims abstract description 10
- 239000002585 base Substances 0.000 claims description 58
- 239000003513 alkali Substances 0.000 claims description 32
- 239000007788 liquid Substances 0.000 claims description 28
- 238000007599 discharging Methods 0.000 claims description 27
- 239000002253 acid Substances 0.000 claims description 24
- 238000004064 recycling Methods 0.000 claims description 22
- 239000010802 sludge Substances 0.000 claims description 14
- 238000001035 drying Methods 0.000 claims description 10
- 238000003756 stirring Methods 0.000 claims description 10
- 238000011084 recovery Methods 0.000 claims description 9
- 238000000926 separation method Methods 0.000 claims description 9
- 230000007246 mechanism Effects 0.000 claims description 8
- 230000007935 neutral effect Effects 0.000 claims description 8
- 239000013049 sediment Substances 0.000 claims description 8
- 239000006228 supernatant Substances 0.000 claims description 8
- 239000003245 coal Substances 0.000 claims description 6
- 239000004576 sand Substances 0.000 claims description 6
- 239000008394 flocculating agent Substances 0.000 claims description 4
- 239000002245 particle Substances 0.000 claims description 4
- 239000007787 solid Substances 0.000 claims description 4
- 238000004891 communication Methods 0.000 claims description 2
- 239000003814 drug Substances 0.000 description 9
- 229940079593 drug Drugs 0.000 description 8
- 230000000694 effects Effects 0.000 description 3
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- 238000011161 development Methods 0.000 description 2
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- 239000012530 fluid Substances 0.000 description 2
- 239000008239 natural water Substances 0.000 description 2
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- 241000195493 Cryptophyta Species 0.000 description 1
- 241000238557 Decapoda Species 0.000 description 1
- 230000002378 acidificating effect Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 238000005520 cutting process Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000000227 grinding Methods 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000012466 permeate Substances 0.000 description 1
- 238000007517 polishing process Methods 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000008399 tap water Substances 0.000 description 1
- 235000020679 tap water Nutrition 0.000 description 1
- 238000004065 wastewater treatment Methods 0.000 description 1
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- 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
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- 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
- C02F1/52—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
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/66—Treatment of water, waste water, or sewage by neutralisation; pH adjustment
-
- 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
- C02F2001/007—Processes including a sedimentation step
-
- 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
- C02F2209/42—Liquid level
-
- 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
- C02F2301/04—Flow arrangements
- C02F2301/043—Treatment of partial or bypass streams
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- 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)
- Separation Of Suspended Particles By Flocculating Agents (AREA)
Abstract
The invention discloses a wastewater circulating treatment system and method for stone processing, wherein the system comprises a controller, a wastewater collecting tank, a sedimentation tank, a flocculation tank, a sedimentation tank, a filtering tank and a clean water tank which are sequentially communicated through pipelines, a sedimentation tank water level sensor is arranged in the sedimentation tank, a first electromagnetic valve is arranged on a connecting pipeline of the sedimentation tank and the flocculation tank, a second electromagnetic valve is arranged on a connecting pipeline of the flocculation tank and the sedimentation tank, a first acid-base adjusting device is arranged in the flocculation tank, a plurality of acid-base adjusting tanks are communicated between the flocculation tank and the sedimentation tank, a third electromagnetic valve and a fourth electromagnetic valve are respectively arranged on the first pipeline and the second pipeline, and a second water quality acid-base adjusting device is respectively arranged in each acid-base adjusting tank. The invention provides a wastewater circulating treatment system and method for stone processing, which are used for collecting and treating wastewater generated in the stone processing process, and clear water obtained after treatment can be used for stone processing again, so that the circulating treatment of the wastewater generated in the stone processing process is realized.
Description
Technical Field
The invention relates to the field of stone processing. More particularly, the invention relates to a wastewater recycling treatment system and method for stone processing.
Background
With the development and development of stone processing industry, waste water generated by stone processing is increased, and the waste water generated by traditional stone processing is not treated and directly discharged to pollute natural water, so that fish, shrimp, algae and microorganisms in the natural water are dead, food chains are damaged, and ecological imbalance is caused. The traditional method not only brings great influence to the living environment of people, but also can cause serious pollution and damage and serious waste of resources. The waste water treatment method used in the stone industry at present is discharged outwards only by simple sedimentation, or is treated by adopting a mode of sedimentation one by one in a plurality of iron tanks. The disadvantages are large floor space, poor settling effect and incapability of meeting the existing stone production capacity. The produced sewage inevitably permeates into the ground. The large amount of acidic or alkaline substances contained in the precipitated clear water can cause serious damage to the machine and the surface of the stone, so that the produced stone can not achieve the ideal gloss effect. In order to achieve the ideal effect, the stone processing enterprises adopt tap water in the cutting, grinding and polishing processes, thereby causing great waste of water resources.
Disclosure of Invention
The invention aims to provide a wastewater circulating treatment system and method for stone processing, which are used for collecting and treating wastewater generated in the stone processing process, and clear water obtained after treatment can be used for stone processing again, so that the circulating treatment of the wastewater generated in the stone processing process is realized.
In order to achieve these objects and other advantages and in accordance with the purpose of the invention, a wastewater recycling system for stone processing is provided, which comprises a controller, and a wastewater collection tank, a sedimentation tank, a flocculation tank, a sedimentation tank, a filtration tank and a clean water tank which are sequentially connected through a pipeline, wherein a sedimentation tank water level sensor is arranged in the sedimentation tank, a first electromagnetic valve is arranged on a connecting pipeline between the sedimentation tank and the flocculation tank, a second electromagnetic valve is arranged on a connecting pipeline between the flocculation tank and the sedimentation tank, a first acid-base adjusting device is arranged in the flocculation tank, a plurality of acid-base adjusting tanks are arranged between the flocculation tank and the sedimentation tank for communication, clean water outlets of the flocculation tank are respectively communicated with water inlets of the plurality of acid-base adjusting tanks through first pipelines, water inlets of the sedimentation tank are respectively communicated with water outlets of the plurality of acid-base adjusting tanks through second pipelines, the first pipeline with be equipped with third solenoid valve and fourth solenoid valve on the second pipeline respectively, all be equipped with second quality of water acid-base adjusting device in the acid-base adjusting tank, first acid-base adjusting device, second quality of water acid-base adjusting device sedimentation tank level sensor, first solenoid valve the second solenoid valve third solenoid valve with the fourth solenoid valve respectively with the controller electricity is connected.
Preferably, the wastewater recycling treatment system for stone processing further comprises a separation and recovery device, and the sedimentation tank and the flocculation tank are respectively communicated with the separation and recovery device.
Preferably, a waste water circulating treatment system for stone material processing in, separation recovery unit includes separator and sludge drying pond, the feed inlet of separator pass through the delivery pump with the sedimentation tank with the bottom of the pool intercommunication of flocculation basin, the delivery port of separator with the water inlet intercommunication of flocculation basin, its discharge gate pass through the conveyer belt with sludge drying pond intercommunication.
Preferably, in the wastewater recycling treatment system for stone processing, the first acid-base adjusting device includes a first acid solution metering pump, a first alkali solution metering pump, a first pH sensor and a first water level sensor, the first acid solution metering pump and the first alkali solution metering pump have drug outlets respectively connected to a plurality of drug discharge pipes, the plurality of drug discharge pipes have discharge outlets respectively communicated with different positions of the sedimentation tank, and the first acid solution metering pump, the first alkali solution metering pump, the first pH sensor and the first water level sensor are respectively electrically connected to the controller.
Preferably, in the wastewater recycling treatment system for stone processing, a stirring mechanism is further arranged in the flocculation tank, and the stirring mechanism is electrically connected with the controller.
Preferably, in the wastewater recycling treatment system for stone processing, the second acid-base adjusting device includes a second acid solution metering pump, a second alkali solution metering pump, a second pH sensor and a second water level sensor, the drug outlets of the first acid solution metering pump and the first alkali solution metering pump are respectively communicated with the corresponding acid-base adjusting tanks through pipelines, and the second acid solution metering pump, the second alkali solution metering pump, the second pH sensor and the second water level sensor are respectively electrically connected with the controller.
Preferably, in the wastewater circulating treatment system for stone processing, the water outlet of the filter tank is arranged at the bottom of the filter tank, and a coarse sand filter layer, a smokeless coal layer and a crushed stone layer are sequentially paved in the filter tank from bottom to top.
The invention also provides a wastewater circulating treatment method for stone processing, and the wastewater circulating treatment system comprises the following steps:
s1, discharging the waste water generated in the stone processing process into the waste water collecting pool, then filtering the waste water collecting pool, removing large-particle broken stones, and then discharging the broken stones into the sedimentation pool;
s2, presetting the alarm water level in the sedimentation tank:
when the water level in the sedimentation tank is lower than the alarm water level, opening the first electromagnetic valve, closing the second electromagnetic valve, the third electromagnetic valves and the fourth electromagnetic valves, discharging the supernatant in the sedimentation tank into the flocculation tank, adding a flocculating agent, closing the first electromagnetic valve after a period of time, adjusting the pH value of the liquid in the flocculation tank to be neutral through the first acid-base adjusting device, and opening the second electromagnetic valve to discharge the liquid in the flocculation tank into the sedimentation tank;
when the water level in the sedimentation tank is higher than the alarm water level, opening the first electromagnetic valve and the second electromagnetic valve, and primarily adjusting the pH value of the liquid in the flocculation tank through the first acid-base adjusting device; simultaneously closing a plurality of fourth electromagnetic valves, sequentially opening the third electromagnetic valves, sequentially discharging the liquid after the pH value is preliminarily adjusted in the flocculation tank to a plurality of acid-base adjusting tanks, adjusting the pH value of the liquid in the acid-base adjusting tanks to be neutral by the second acid-base adjusting device in each acid-base adjusting tank, and then opening the corresponding fourth electromagnetic valves to discharge the liquid in the flocculation tank to the sedimentation tank;
s3, settling the liquid in the sedimentation tank through the sedimentation tank, discharging the supernatant settled in the sedimentation tank into the filter tank, filtering and discharging into the clear water tank.
Preferably, the method for recycling waste water from stone processing further comprises:
s4, sending the sediments at the bottom of the sedimentation tank and the flocculation tank to a separator through a delivery pump, separating the sediments through the separator, discharging the water separated by the separator into the flocculation tank, and delivering the separated solid sludge to a sludge drying tank through a conveyor belt for treatment.
Preferably, in the wastewater recycling method for stone processing, in S3, a coarse sand filter layer, a smokeless coal layer and a gravel layer are sequentially laid in the filter tank from bottom to top to filter water flowing out of the filter tank.
The invention has the beneficial effects that:
1. the wastewater circulating treatment system provided by the invention is used for collecting and treating wastewater generated in the stone processing process, and clear water obtained after treatment can be used for stone processing again, so that the circulating treatment of the wastewater generated in the stone processing process is realized.
2. The wastewater circulating treatment system and method provided by the invention can adjust and adjust the pH value of the wastewater according to the change of the actually generated wastewater quantity.
Additional advantages, objects, and features of the invention will be set forth in part in the description which follows and in part will become apparent to those having ordinary skill in the art upon examination of the following or may be learned from practice of the invention.
Drawings
FIG. 1 is a schematic structural view of a wastewater recycling system according to the present invention;
FIG. 2 is a schematic diagram of the electrical connections of the wastewater recycling system according to the present invention.
Detailed Description
The present invention is further described in detail below with reference to the attached drawings so that those skilled in the art can implement the invention by referring to the description text.
It should be noted that in the description of the present invention, the terms "lateral", "longitudinal", "upper", "lower", "front", "rear", "left", "right", "vertical", "horizontal", "top", "bottom", "inner", "outer", etc. indicate orientations or positional relationships based on those shown in the drawings, and are only for convenience of description and simplicity of description, and do not indicate or imply that the referred device or element must have a specific orientation, be constructed and operated in a specific orientation, and thus, should not be construed as limiting the present invention.
As shown in fig. 1-2, an embodiment of the present invention provides a wastewater recycling treatment system for stone processing, including a controller, and a wastewater collection tank, a sedimentation tank, a flocculation tank, a sedimentation tank, a filtration tank, and a clean water tank which are sequentially connected through a pipeline, wherein a sedimentation tank water level sensor is disposed in the sedimentation tank, a first electromagnetic valve is disposed on a connection pipeline between the sedimentation tank and the flocculation tank, a second electromagnetic valve is disposed on a connection pipeline between the flocculation tank and the sedimentation tank, a first acid-base adjusting device is disposed in the flocculation tank, a plurality of acid-base adjusting tanks are disposed between the flocculation tank and the sedimentation tank, clean water outlets of the flocculation tank are respectively communicated with water inlets of the plurality of acid-base adjusting tanks through first pipelines, water inlets of the sedimentation tank are respectively communicated with water outlets of the plurality of acid-base adjusting tanks through second pipelines, the first pipeline with be equipped with third solenoid valve and fourth solenoid valve on the second pipeline respectively, all be equipped with second quality of water acid-base adjusting device in the acid-base adjusting tank, first acid-base adjusting device, second quality of water acid-base adjusting device sedimentation tank level sensor, first solenoid valve the second solenoid valve third solenoid valve with the fourth solenoid valve respectively with the controller electricity is connected.
In this embodiment, the structure of waste water collecting pit, sedimentation tank, flocculation basin, sedimentation tank, filtering ponds and clean water basin and the connection between them all adopt prior art can easily realize, and this department no longer states tiredly. When the wastewater recycling treatment system of the embodiment is used, the following steps can be adopted:
s1, discharging the waste water generated in the stone processing process into the waste water collecting pool, then filtering the waste water collecting pool, removing large-particle broken stones, and then discharging the broken stones into the sedimentation pool;
s2, presetting the alarm water level in the sedimentation tank:
when the water level in the sedimentation tank is lower than the alarm water level, opening the first electromagnetic valve, closing the second electromagnetic valve, the third electromagnetic valves and the fourth electromagnetic valves, discharging the supernatant in the sedimentation tank into the flocculation tank, adding a flocculating agent, closing the first electromagnetic valve after a period of time, adjusting the pH value of the liquid in the flocculation tank to be neutral through the first acid-base adjusting device, and opening the second electromagnetic valve to discharge the liquid in the flocculation tank into the sedimentation tank;
when the water level in the sedimentation tank is higher than the alarm water level, opening the first electromagnetic valve and the second electromagnetic valve, and primarily adjusting the pH value of the liquid in the flocculation tank through the first acid-base adjusting device; simultaneously closing a plurality of fourth electromagnetic valves, sequentially opening the third electromagnetic valves, sequentially discharging the liquid after the pH value is preliminarily adjusted in the flocculation tank to a plurality of acid-base adjusting tanks, adjusting the pH value of the liquid in the acid-base adjusting tanks to be neutral by the second acid-base adjusting device in each acid-base adjusting tank, and then opening the corresponding fourth electromagnetic valves to discharge the liquid in the flocculation tank to the sedimentation tank;
s3, settling the liquid in the sedimentation tank through the sedimentation tank, discharging the supernatant settled in the sedimentation tank into the filter tank, filtering and discharging into the clear water tank.
Preferably, as another embodiment of the present invention, the present invention further comprises a separation and recovery device, and the sedimentation tank and the flocculation tank are respectively communicated with the separation and recovery device. The separation and recovery device comprises a separator and a sludge drying tank, wherein a feed inlet of the separator is communicated with the sedimentation tank and the bottom of the flocculation tank through a delivery pump, a water outlet of the separator is communicated with a water inlet of the flocculation tank, and a discharge outlet of the separator is communicated with the sludge drying tank through a conveyor belt.
In the embodiment, sediments at the bottom of the sedimentation tank and the flocculation tank are sent to a separator through a conveying pump, the sediments are separated through the separator, moisture separated by the separator is discharged into the flocculation tank, and the separated solid sludge is conveyed to a sludge drying tank through a conveying belt for treatment.
Preferably, as another embodiment of the present invention, the first acid-base adjusting device includes a first acid solution metering pump, a first alkali solution metering pump, a first pH sensor and a first water level sensor, the first acid solution metering pump and the first alkali solution metering pump have drug outlets respectively connected to a plurality of drug discharge pipes, the plurality of drug discharge pipes have discharge outlets respectively communicated with different positions of the sedimentation tank, and the first acid solution metering pump, the first alkali solution metering pump, the first pH sensor and the first water level sensor are respectively electrically connected to the controller.
In this embodiment, the pH value of the wastewater in the flocculation tank is obtained by the first pH sensor, and the acid solution or the alkali solution is added into the flocculation tank by the first acid solution metering pump or the first alkali solution metering pump, so as to adjust the pH value of the wastewater. Because the area of flocculation basin is great, the play medicine mouth of first acidizing fluid measuring pump and first alkali lye measuring pump is connected with many discharge pipes respectively, and the discharge gate of many discharge pipes communicates with the different positions of sedimentation tank respectively, and the even discharge of acidizing fluid or alkali lye that can be more quick like this is in the flocculation basin.
Preferably, as another embodiment of the present invention, a stirring mechanism is further disposed in the flocculation tank, and the stirring mechanism is electrically connected to the controller.
In the embodiment, the stirring mechanism is additionally arranged in the flocculation tank, and the stirring speed of the acid liquor or the alkali liquor is increased through the stirring of the stirring mechanism.
Preferably, as another embodiment of the present invention, the second acid-base adjusting device includes a second acid solution metering pump, a second alkali solution metering pump, a second pH sensor, and a second water level sensor, drug outlets of the first acid solution metering pump and the first alkali solution metering pump are respectively communicated with the corresponding acid-base adjusting tanks through pipelines, and the second acid solution metering pump, the second alkali solution metering pump, the second pH sensor, and the second water level sensor are respectively electrically connected with the controller.
In this embodiment, the pH value of the wastewater in the acid-base adjusting tank is obtained by the second pH sensor, and the acid solution or the alkali solution is added into the acid-base adjusting tank by the second acid solution metering pump or the second alkali solution metering pump, so as to adjust the pH value of the wastewater.
Preferably, as another embodiment of the present invention, the water outlet of the filtering tank is arranged at the bottom of the filtering tank, and a coarse sand filtering layer, a smokeless coal layer and a gravel layer are sequentially laid in the filtering tank from bottom to top.
In this embodiment, filter waste water through coarse sand filter bed, smokeless coal seam and rubble layer for the water that gets into in the clear water pond is cleaner.
The invention also provides a wastewater circulating treatment method for stone processing, and the wastewater circulating treatment system comprises the following steps:
s1, discharging the waste water generated in the stone processing process into the waste water collecting pool, then filtering the waste water collecting pool, removing large-particle broken stones, and then discharging the broken stones into the sedimentation pool;
s2, presetting the alarm water level in the sedimentation tank:
when the water level in the sedimentation tank is lower than the alarm water level, opening the first electromagnetic valve, closing the second electromagnetic valve, the third electromagnetic valves and the fourth electromagnetic valves, discharging the supernatant in the sedimentation tank into the flocculation tank, adding a flocculating agent, closing the first electromagnetic valve after a period of time, adjusting the pH value of the liquid in the flocculation tank to be neutral through the first acid-base adjusting device, and opening the second electromagnetic valve to discharge the liquid in the flocculation tank into the sedimentation tank;
when the water level in the sedimentation tank is higher than the alarm water level, opening the first electromagnetic valve and the second electromagnetic valve, and primarily adjusting the pH value of the liquid in the flocculation tank through the first acid-base adjusting device; simultaneously closing a plurality of fourth electromagnetic valves, sequentially opening the third electromagnetic valves, sequentially discharging the liquid after the pH value is preliminarily adjusted in the flocculation tank to a plurality of acid-base adjusting tanks, adjusting the pH value of the liquid in the acid-base adjusting tanks to be neutral by the second acid-base adjusting device in each acid-base adjusting tank, and then opening the corresponding fourth electromagnetic valves to discharge the liquid in the flocculation tank to the sedimentation tank;
s3, settling the liquid in the sedimentation tank through the sedimentation tank, discharging the supernatant settled in the sedimentation tank into the filter tank, filtering and discharging into the clear water tank;
s4, sending the sediments at the bottom of the sedimentation tank and the flocculation tank to a separator through a delivery pump, separating the sediments through the separator, discharging the water separated by the separator into the flocculation tank, and delivering the separated solid sludge to a sludge drying tank through a conveyor belt for treatment.
While embodiments of the invention have been described above, it is not limited to the applications set forth in the description and the embodiments, which are fully applicable to various fields of endeavor for which the invention may be embodied with additional modifications as would be readily apparent to those skilled in the art, and the invention is therefore not limited to the details given herein and to the embodiments shown and described without departing from the generic concept as defined by the claims and their equivalents.
Claims (10)
1. A wastewater circulating treatment system for stone processing is characterized by comprising a controller, a wastewater collecting pool, a sedimentation pool, a flocculation pool, a sedimentation pool, a filtering pool and a clean water pool which are sequentially communicated through pipelines, wherein a sedimentation pool water level sensor is arranged in the sedimentation pool, a first electromagnetic valve is arranged on a connecting pipeline of the sedimentation pool and the flocculation pool, a second electromagnetic valve is arranged on a connecting pipeline of the flocculation pool and the sedimentation pool, a first acid-base adjusting device is arranged in the flocculation pool, a plurality of acid-base adjusting pools are arranged between the flocculation pool and the sedimentation pool for communication, a clean water outlet of the flocculation pool is respectively communicated with water inlets of the acid-base adjusting pools through first pipelines, a water inlet of the sedimentation pool is respectively communicated with water outlets of the acid-base adjusting pools through second pipelines, a third electromagnetic valve and a fourth electromagnetic valve are respectively arranged on the first pipeline and the second pipeline, and a second water quality acid-base adjusting device is arranged in the acid-base adjusting tank, and the first acid-base adjusting device, the second water quality acid-base adjusting device, the sedimentation tank water level sensor, the first electromagnetic valve, the second electromagnetic valve, the third electromagnetic valve and the fourth electromagnetic valve are respectively and electrically connected with the controller.
2. The wastewater recycling system for stone processing as claimed in claim 1, further comprising a separation and recovery device, wherein said settling tank and said flocculation tank are respectively connected to said separation and recovery device.
3. The wastewater recycling system for stone processing as claimed in claim 2, wherein the separation and recovery device comprises a separator and a sludge drying tank, the inlet of the separator is connected to the bottom of the sedimentation tank and the bottom of the flocculation tank through a transfer pump, the outlet of the separator is connected to the inlet of the flocculation tank, and the outlet of the separator is connected to the sludge drying tank through a conveyor belt.
4. The recycling system for waste water from stone processing as claimed in claim 1, wherein said first acid/alkali adjusting device comprises a first acid/alkali metering pump, a first alkali/alkali metering pump, a first pH sensor and a first water level sensor, wherein said first acid/alkali metering pump and said first alkali/alkali metering pump are connected to a plurality of discharge pipes respectively, said plurality of discharge pipes are connected to different positions of said sedimentation tank respectively, and said first acid/alkali metering pump, said first alkali/alkali metering pump, said first pH sensor and said first water level sensor are electrically connected to said controller respectively.
5. The wastewater recycling system for stone processing as claimed in claim 4, wherein a stirring mechanism is further provided in said flocculation tank, said stirring mechanism being electrically connected to said controller.
6. The recycling system for waste water from stone processing as claimed in claim 1, wherein said second acid-base adjusting device comprises a second acid solution metering pump, a second alkali solution metering pump, a second pH sensor and a second water level sensor, wherein the outlets of said first acid solution metering pump and said first alkali solution metering pump are respectively connected to said corresponding acid-base adjusting tank through pipes, and said second acid solution metering pump, said second alkali solution metering pump, said second pH sensor and said second water level sensor are respectively connected to said controller electrically.
7. The wastewater recycling system for stone processing as claimed in claim 1, wherein the water outlet of the filtering tank is disposed at the bottom of the filtering tank, and the filtering tank is sequentially laid with a coarse sand filtering layer, a smokeless coal layer and a gravel layer from bottom to top.
8. A wastewater recycling method for stone processing, which adopts the wastewater recycling system as claimed in any one of claims 1 to 7, and comprises the following steps:
s1, discharging the waste water generated in the stone processing process into the waste water collecting pool, then filtering the waste water collecting pool, removing large-particle broken stones, and then discharging the broken stones into the sedimentation pool;
s2, presetting the alarm water level in the sedimentation tank:
when the water level in the sedimentation tank is lower than the alarm water level, opening the first electromagnetic valve, closing the second electromagnetic valve, the third electromagnetic valves and the fourth electromagnetic valves, discharging the supernatant in the sedimentation tank into the flocculation tank, adding a flocculating agent, closing the first electromagnetic valve after a period of time, adjusting the pH value of the liquid in the flocculation tank to be neutral through the first acid-base adjusting device, and opening the second electromagnetic valve to discharge the liquid in the flocculation tank into the sedimentation tank;
when the water level in the sedimentation tank is higher than the alarm water level, opening the first electromagnetic valve and the second electromagnetic valve, and primarily adjusting the pH value of the liquid in the flocculation tank through the first acid-base adjusting device; simultaneously closing a plurality of fourth electromagnetic valves, sequentially opening the third electromagnetic valves, sequentially discharging the liquid after the pH value is preliminarily adjusted in the flocculation tank to a plurality of acid-base adjusting tanks, adjusting the pH value of the liquid in the acid-base adjusting tanks to be neutral by the second acid-base adjusting device in each acid-base adjusting tank, and then opening the corresponding fourth electromagnetic valves to discharge the liquid in the flocculation tank to the sedimentation tank;
s3, settling the liquid in the sedimentation tank through the sedimentation tank, discharging the supernatant settled in the sedimentation tank into the filter tank, filtering and discharging into the clear water tank.
9. The recycling method of wastewater from stone processing as claimed in claim 8, further comprising:
s4, sending the sediments at the bottom of the sedimentation tank and the flocculation tank to a separator through a delivery pump, separating the sediments through the separator, discharging the water separated by the separator into the flocculation tank, and delivering the separated solid sludge to a sludge drying tank through a conveyor belt for treatment.
10. The recycling method of wastewater from stone processing as claimed in claim 8, wherein in S3, a coarse sand filter layer, a smokeless coal layer and a gravel layer are sequentially laid in the filter tank from bottom to top to filter the water flowing out of the filter tank.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202111323425.2A CN113880312A (en) | 2021-11-10 | 2021-11-10 | Wastewater circulating treatment system and method for stone processing |
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Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20120285895A1 (en) * | 2011-05-13 | 2012-11-15 | Frank Leslie Smiddy | System and method for the treatment of wastewater |
| CN205061733U (en) * | 2015-10-22 | 2016-03-02 | 甘肃金润玉石业有限公司 | Waste water recovery system is ground in marble polishing |
| CN107364987A (en) * | 2017-07-24 | 2017-11-21 | 仁怀市攀峰石材加工厂 | A kind of stone wastewater processing system and processing method |
| CN111847730A (en) * | 2020-08-27 | 2020-10-30 | 湖北磊雅鑫盛石业有限公司 | Stone material waste water cyclic utilization system |
-
2021
- 2021-11-10 CN CN202111323425.2A patent/CN113880312A/en active Pending
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20120285895A1 (en) * | 2011-05-13 | 2012-11-15 | Frank Leslie Smiddy | System and method for the treatment of wastewater |
| CN205061733U (en) * | 2015-10-22 | 2016-03-02 | 甘肃金润玉石业有限公司 | Waste water recovery system is ground in marble polishing |
| CN107364987A (en) * | 2017-07-24 | 2017-11-21 | 仁怀市攀峰石材加工厂 | A kind of stone wastewater processing system and processing method |
| CN111847730A (en) * | 2020-08-27 | 2020-10-30 | 湖北磊雅鑫盛石业有限公司 | Stone material waste water cyclic utilization system |
Non-Patent Citations (1)
| Title |
|---|
| 张国干等: "《工业化学》", 31 October 1998, 湖南师范大学出版社 * |
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