CN214400078U - Mine water underground and ground cooperative pretreatment system - Google Patents
Mine water underground and ground cooperative pretreatment system Download PDFInfo
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- CN214400078U CN214400078U CN202120249720.7U CN202120249720U CN214400078U CN 214400078 U CN214400078 U CN 214400078U CN 202120249720 U CN202120249720 U CN 202120249720U CN 214400078 U CN214400078 U CN 214400078U
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Abstract
The utility model provides a mine water is in pit with ground pretreatment system in coordination, realize the operation of in coordination with ground pretreatment in pit to the mine water. A mine water underground and ground cooperative pretreatment system comprises: the monitoring unit is used for monitoring the pH value and the flow of the mine water inflow underground; a multi-stage neutralization unit for adjusting the pH value of mine water to be more than 7.5 underground; aerating, oxidizing, standing and primarily precipitating to remove iron in the underground, lifting mine water to the ground, and adding an iron removal unit for oxidizing, precipitating and removing iron in a medicament; the automatic control unit is used for receiving the pH value and flow data obtained by the monitoring unit so as to control the multi-stage neutralization unit to adjust the pH value, monitor the iron content of the iron removal unit, control the aeration oxidation and the medicament addition of the iron removal unit and monitor the pH value and the iron content of the effluent; the monitoring unit, the multistage neutralization unit and the iron removal unit are sequentially connected. The utility model discloses occupation space size is little, the treatment effect is good, control is simple, degree of automation is high, the input cost is low.
Description
Technical Field
The utility model relates to a water treatment system, in particular to mine water is pretreatment systems in coordination with ground in pit belongs to water treatment technical field.
Background
Coal is always a main supplier in energy consumption in China and is far higher than other energy sources. According to relevant data, the coal distribution of China is mainly medium and high sulfur coal, and the low sulfur coal with better quality has less content. In the process of mining some medium and high sulfur coal, ferrous sulfide in coal can generate a series of physicochemical and biochemical reactions with air, water and microorganisms to generate sulfuric acid and ferrous ions, mine water contains a large amount of iron, the pH value of the mine water is in an acidic range, the pH value of conventional acidic mine water is mostly between 3 and 6, and the pH value of part of special mine water is less than 3. The direct discharge of the acidic mine water can cause the waste of a large amount of water resources and seriously harm the ecology of the surrounding water body.
For acidic mine water, the traditional treatment method is to remove pollutants in water by a physical or chemical method, and comprises a neutralization method, a sulfide precipitation method, a sulfate reducing bacteria reactor and the like. At present, the domestic use is mostly to adopt a neutralization precipitation method for treatment on the ground. However, large-scale treatment facilities need to be built for ground treatment, a large amount of special pipelines and pump set equipment need to be laid to convey mine water to the ground, the phenomena of corrosion of the pipelines and the pump sets still exist, the investment is huge, and the problem of corrosion of the equipment is more prominent particularly for acid mine water with the pH value of less than 3.
In order to effectively and economically treat the mine water with high acidity and high iron content, the probability and risk of corrosion of the acid mine water to equipment need to be reduced, however, the underground space is limited, large-scale treatment equipment cannot be built like the ground, and many instruments and equipment do not have underground explosion-proof certification and lack a movable underground pretreatment system. Therefore, the development of a mine water treatment system for performing pretreatment by cooperation of underground and ground is needed at present so as to reduce the threat of acid mine water on equipment corrosion and the economic cost of overall treatment.
SUMMERY OF THE UTILITY MODEL
An object of the utility model is to provide a mine water is pretreatment systems in coordination with ground in pit, realizes the pretreatment operations in coordination with ground in the pit water, can the accurate pH value of adjusting the mine water, gets rid of most iron in the mine water simultaneously, reduces the risk of ground equipment pipeline acid corrosion, reduces the load of mine water ground processing unit.
Another object of the present invention is to provide a pretreatment process for underground and ground water in cooperation.
The utility model provides a technical scheme that its technical problem adopted is:
a mine water underground and ground cooperative pretreatment system comprises:
the monitoring unit is used for monitoring the pH value and the flow of the mine water inflow underground;
a multi-stage neutralization unit for adjusting the pH value of mine water to be more than 7.5 underground;
aerating, oxidizing, standing and primarily precipitating to remove iron in the underground, lifting mine water to the ground, and adding an iron removal unit for oxidizing, precipitating and removing iron in a medicament;
and an automatic control unit for receiving the pH value and flow data obtained by the monitoring unit, controlling the multi-stage neutralization unit to adjust the pH value, monitoring the iron content of the iron removal unit, controlling aeration oxidation and medicament addition of the iron removal unit, and monitoring the pH value and iron content of the effluent;
the monitoring unit, the multistage neutralization unit and the iron removal unit are sequentially connected.
By adopting the technical scheme, the mine water firstly flows through the monitoring unit, the monitoring unit detects the water inlet amount and the pH value and feeds data back to the automatic control unit, the mine water then flows into the multistage neutralization unit, alkali liquor is sequentially added through the multistage neutralization unit to accurately adjust the pH value of the mine water to be more than 7.5, the mine water then enters the iron removal unit, the iron content is reduced to 10mg/L after preliminary iron removal in a well, the iron content is reduced to be less than 0.3mg/L after ground iron removal, and sludge after the iron removal unit is dewatered to finally generate mud cakes and clear water with the water content of less than 60%.
Preferably, the monitoring unit comprises a metering open channel, a flow meter and a first pH value detection device, the metering open channel is provided with a water inlet for mine water inflow and a water outlet for connecting the multistage neutralization unit, the flow meter and the first pH value detection device are arranged in the metering open channel, and the flow meter and the first pH value detection device are electrically connected with the automatic control unit.
Preferably, the multistage neutralization unit comprises a neutralization reaction tank, a stirring device and an alkali adding device, a plurality of water-isolating weirs are arranged in the neutralization reaction tank, the interior of the neutralization reaction tank is sequentially divided into a water inlet area, a mixing area and an overflow area along the flowing direction of mine water treatment by the water-isolating weirs, the stirring device is arranged at the upper part of the mixing area, the alkali adding device comprises an alkali preparation tank and an alkali adding metering pump, the alkali adding device is arranged above the neutralization reaction tank, and the stirring device and the alkali adding device are both electrically connected with the automatic control unit.
Preferably, the neutralization reaction tank is a plurality of parallel movable reaction tanks or a plurality of series movable reaction tanks.
Preferably, the stirring device comprises a neutralization stirrer, an alkali adding pipeline and an alkali adding feeding port, the alkali adding pipeline is arranged at the upper end of the neutralization stirrer, an impeller is arranged at the lower part of the neutralization stirrer, the alkali adding feeding port is arranged on the impeller, and the alkali adding feeding port is connected with the alkali adding device through the alkali adding pipeline.
Preferably, the overflow area is provided with a second pH value detection device, and the second pH value detection device is electrically connected with the automatic control unit.
Preferably, the deironing unit includes preliminary deironing device in the pit and ground deironing device, preliminary deironing device in the pit includes aeration oxidation pond, aeration equipment and is used for the pit water storehouse in the pit that the pit water stood to deposit, and aeration oxidation pond bottom is equipped with the aeration pipeline, and the aeration pipeline links to each other with aeration equipment, and aeration oxidation pond passes through the storehouse in the pit and connects ground deironing device, ground deironing device includes that the medicament is thrown and is thrown device, oxidation sedimentation tank and filtering pond, and the medicament is thrown and is located oxidation sedimentation tank top to the device, and the medicament is thrown and is thrown the device and is connected with the automatic control unit electricity.
Preferably, the aeration device is provided with an aeration control valve which is electrically connected with the automatic control unit; the medicament feeding device comprises a dispensing tank and a dosing metering pump, and the dosing metering pump is electrically connected with the automatic control unit.
Preferably, the oxidation sedimentation tank is a radial flow sedimentation tank, a vertical flow sedimentation tank or a horizontal flow sedimentation tank, a potassium permanganate medicament or a hydrogen peroxide medicament is arranged in the medicament adding device, and the filter tank is a fast filter tank, a slow filter tank or a biological filter tank.
Because the pH value of the outlet water of the mine water fluctuates up and down, the pH value of the mine water is accurately controlled by gradually adding alkali liquor, and the consumption of the medicament is reduced. The underground pH value is adjusted to reduce the corrosion of acid mine water to the following pipelines and equipment; the iron is removed by aeration oxidation and standing preliminary precipitation under the well, and the treatment capacity of the mine water on the ground can be reduced.
The utility model has the advantages that:
the utility model discloses a mine water is in pit with ground pretreatment systems in coordination, realized the online line production of automatically regulated alkali that adds to the unstable mine water of quality of water, the mine water pH value is adjusted steadily to the accuracy, and get rid of most iron in the mine aquatic, make the total iron content of play water <0.3mg/L, reduce the acid corrosion risk of ground equipment pipeline, reduce the load of mine water ground processing unit, it is little to have occupation space size, excellent in treatment effect, control is simple, degree of automation is high, input cost low grade characteristics.
Drawings
In order to more clearly illustrate the embodiments of the present invention or the technical solutions in the prior art, the drawings required to be used in the description of the embodiments or the prior art will be briefly described below, it is obvious that the drawings in the following description are only embodiments of the present invention, and for those skilled in the art, other drawings can be obtained according to the provided drawings without creative efforts.
FIG. 1 is a schematic diagram of the system of the present invention;
FIG. 2 is a top view of the neutralization reaction tank of the present invention;
FIG. 3 is a schematic sectional view taken along line A-A in FIG. 2;
fig. 4 is a schematic sectional view taken along line B-B in fig. 2.
In the figure: 1. the system comprises a monitoring unit, a 2, a multi-stage neutralization unit, a 3, an iron removal unit, a 4, an automatic control unit, a 11, a metering open channel, a 12, a flowmeter, a 13, a first pH value detection device, a 14, a water inlet, a 15, a water outlet, a 21, a neutralization reaction tank, a 22, an alkali adding device, a 23, a stirring device, a 31, an aeration oxidation tank, a 32, an aeration device, a 33, an aeration control valve, a 34, a downhole water sump, a 35, a lift pump, a 36, an oxidation sedimentation tank, a 37, a medicament adding device, a 38, a filter tank, a 201, a water inlet area, a 202, a mixing area, a 203, an overflow area, a 210, a reaction tank water inlet, a 211, a water-resisting weir, a 212, a reaction tank water outlet, a 213, a second pH value detection device, a 221, an alkali distribution tank, a 222, an alkali adding metering pump, a 230, a stirring support, a 231, a neutralization stirrer, an alkali adding pipeline, a 233, an alkali adding port, and an impeller 234 and an alkali adding port.
Detailed Description
The technical solution of the present invention is further specifically described below by way of specific embodiments and with reference to the accompanying drawings. It is to be understood that the practice of the present invention is not limited to the following examples, and that any modifications and/or changes in form made to the present invention are intended to fall within the scope of the present invention.
In the utility model, all parts and percentages are weight units, and the adopted equipment, raw materials and the like can be purchased from the market or commonly used in the field if not specified. The methods in the following examples are conventional in the art unless otherwise specified. The components or devices in the following examples are, unless otherwise specified, standard parts or parts known to those skilled in the art, the structure and principle of which are known to those skilled in the art through technical manuals or through routine experimentation.
Example (b):
the mine water underground and ground cooperative pretreatment system shown in fig. 1 comprises a monitoring unit 1, a multistage neutralization unit 2, an iron removal unit 3 and an automatic control unit 4.
The monitoring unit 1 is used for monitoring the pH value and the flow rate of inlet water of mine water underground, the multistage neutralization unit 2 is used for adjusting the pH value of the mine water underground to be more than 7.5, the iron removal unit 3 is used for aeration oxidation and standing preliminary precipitation iron removal underground, the mine water is lifted to the ground and is subjected to reagent addition, oxidation, precipitation and iron removal, and the automatic control unit 4 is used for receiving the pH value and the flow rate data obtained by the monitoring unit, so that the multistage neutralization unit is controlled to adjust the pH value, the iron content of the iron removal unit is monitored, the aeration oxidation and the reagent addition of the iron removal unit are controlled, and the pH value and the iron content of outlet water are monitored. The monitoring unit 1, the multistage neutralization unit 2 and the iron removal unit 3 are sequentially connected through pipelines, and a weir groove can be selected to connect the units according to actual application scenes.
By adopting the technical scheme, the mine water firstly flows through the monitoring unit 1, the monitoring unit 1 detects the water inflow amount and the pH value and feeds data back to the automatic control unit 4, the mine water then flows into the multistage neutralization unit 2, the pH value of the mine water is accurately adjusted to be more than 7.5 by sequentially adding alkali liquor through the multistage neutralization unit 2, the mine water then enters the iron removal unit 3, the iron content is reduced to 10mg/L after preliminary iron removal in a well, the iron content is reduced to be less than 0.3mg/L after ground iron removal, and sludge after the iron removal unit 3 is dewatered to finally generate mud cakes and clear water with the water content of less than 60%.
The monitoring unit comprises a metering open channel 11, a flow meter 12 and a first pH value detection device 13, the metering open channel is provided with a water inlet 14 for mine water inflow and a water outlet 15 for connecting the multistage neutralization units, the flow meter 12 and the first pH value detection device 13 are arranged in the metering open channel, the flow meter 12 and the first pH value detection device 13 are electrically connected with the automatic control unit 4, the mine water inflow flow and the pH value entering the metering open channel 11 are detected through the first pH value detection device 13, and the numerical values are fed back to the automatic control unit 4 so as to regulate and control subsequent units. The liquid level range of the metering open channel 11 is 0.03-0.75 m, and the flowmeter 12 and the first pH value detection device 13 both adopt intrinsic safety type explosion-proof equipment.
The multi-stage neutralization unit consists of a neutralization reaction tank 21, an alkali adding device 22 and a stirring device 23.
The neutralization reaction tank 21 is three movable reaction tanks connected in series and is divided into a first-stage neutralization reaction tank, a second-stage neutralization reaction tank and a third-stage neutralization reaction tank. It should be noted that, according to the needs of the application scenario, a plurality of parallel movable reaction tanks may be selected, and the number of the serial and parallel reaction tanks may also be changed according to the needs, such as a fourth-stage neutralization reaction tank and a fifth-stage neutralization reaction tank are added according to the selection of the water inflow. The following is a description of the structure of a single neutralization reaction tank, and it should be noted that a plurality of neutralization reaction tanks are only changed in number, and the structures thereof are the same.
As shown in fig. 2-4, each neutralization reaction tank is made of reinforced concrete, the water inlet 210 of the reaction tank is positioned above the left side of the tank body, and the tank body is divided into a water inlet area 201, a mixing area 202 and an overflow area 203 by two water-isolating weirs 211.
The alkali adding device is provided with an alkali preparation tank 221 and an alkali adding metering pump 222, and the alkali adding metering pump 222 is electrically connected with the automatic control unit 4. The concentration range of the alkali liquor prepared by the alkali preparation tank 221 is 30 percent, and the alkali liquor preparation is directly adopted.
The stirring device comprises a neutralization stirrer 231, an alkali adding pipeline 232 and an alkali adding feeding port 233, the alkali adding pipeline is arranged at the upper end of the neutralization stirrer, an impeller 234 is arranged at the lower part of the neutralization stirrer, the alkali adding feeding port is arranged at the tail end of the impeller, the alkali adding feeding port is connected with an alkali adding device through the alkali adding pipeline, the neutralization stirrer 231 is fixed on the upper part of the mixing area 202 through a stirring support 230, and the neutralization stirrer 231 is electrically connected with an automatic control unit. And the mine water in the neutralization reaction tank is fully mixed with alkaline substances by stirring and adding alkali.
In order to better monitor the pH value adjusting result in the neutralization reaction tank and adjust the alkali adding amount according to the adjusting result, a second pH value detecting device 213 is arranged at the water outlet 212 of the reaction tank above the right side of the overflow area 203, and the second pH value detecting device 213 is electrically connected with the automatic control unit 4.
The iron removing unit 3 consists of an underground preliminary iron removing device and a ground iron removing device. The underground iron removal device comprises an aeration oxidation pond 31, an aeration device 32 and an underground water sump 34, wherein the bottom of the aeration oxidation pond 31 is provided with an aeration pipeline, the aeration pipeline is connected with the aeration device 32, the aeration device 32 is provided with a plurality of aeration control valves 33, the aeration control valves 33 are electrically connected with an automatic control unit 4, and the automatic control unit 4 controls the aeration oxidation process in the aeration oxidation pond through an aeration control valve 3. It should be noted that the aeration device 32 can directly use the original down-hole compressed air system to supply air, and the aeration pipeline is connected with the perforated aeration pipe to directly distribute air, and of course, other forms of aeration sources and aeration modes can also be adopted.
The underground water sump 34 is used for standing and precipitating mine water, the underground water sump 34 is provided with a water sump cleaning machine, and water discharged from the underground water sump 34 is lifted to a ground deironing device by a lifting pump 35.
The ground iron removing device comprises a medicament adding device 37, an oxidation and precipitation tank 36 and a filter tank 38, wherein the medicament adding device 37 comprises a medicament preparing tank and a medicament adding metering pump, the medicament adding metering pump is electrically connected with an automatic control unit 4, the automatic control unit 4 controls the adding of the medicament through the medicament adding metering pump, a sludge discharge pipe is arranged at the bottom of the oxidation and precipitation tank 36, and a plurality of filter materials are arranged in the filter tank 38.
The oxidation and precipitation tank 36 may be a radial-flow type precipitation tank, a vertical-flow type precipitation tank, or a horizontal-flow type precipitation tank, in this embodiment, a radial-flow type precipitation tank is selected, a potassium permanganate agent or a hydrogen peroxide agent is provided in the agent adding device 37, or other agents capable of oxidizing and precipitating iron may be provided, the filter tank 38 is a multi-medium fast filter tank, or of course, a slow filter tank or a biological filter tank may be selected, and the medium of the multi-medium fast filter tank in this embodiment is selected from quartz sand filter materials, manganese sand filter materials, and fiber balls. And a monitoring device electrically connected with the automatic control unit is arranged in the filter tank and used for sending the pH value and iron content data of the outlet water to the automatic control unit.
For the safety of the underground operation, the aeration control valve or other control valves under the well mentioned above all adopt a mining explosion-proof electric valve QMB 9.
A treatment process applied to a mine water underground and ground cooperative pretreatment system comprises the following specific steps:
1. mine water firstly enters a metering open channel 11 of a monitoring unit through a water inlet 14, the water quantity and the pH value of incoming water are detected by a flowmeter 12 and a first pH value detection device 13 in the metering open channel 11 and are fed back to an automatic control unit 4;
2. then, the mine water sequentially enters three neutralization reaction tanks 21 connected in series in the multistage neutralization unit 2, pH value and water quantity data fed back from the front section are analyzed through the automatic control unit 4, the alkali preparation tank 221 and the alkali addition metering pump 222 are controlled to regulate the mine water for multiple times, detection is carried out through a second pH detection device at the outlet of the reaction tank and fed back to the automatic control unit 4, the pH value is increased by 0.5-1.5 to 5.0 in the first stage, the pH value is increased to 6.0 in the second stage, and the pH value is increased to more than 7.5 in the third stage;
3. then, the mine water sequentially enters an underground primary iron removal device and a ground iron removal device in the iron removal unit 3, ferrous ions in the mine water are oxidized into ferric ions through an aeration oxidation pond 31 in the underground primary iron removal device, and are precipitated and removed in an underground water sump 34, so that the iron content of the mine water is reduced to be below 10mg/L, the mine water is extracted to an oxidation precipitation pond 36 on the ground through a lift pump 35, the iron content in the mine water is further reduced through chemical-adding oxidation precipitation, finally the mine water is treated by a filter 38 and then flows out, and the iron content of the effluent is less than 0.3 mg/L.
The system of the embodiment is adopted for carrying out operation for 15 days on mine water of a certain coal mine, and corresponding water quality detection data are shown in table 1.
Table 1 main water quality testing data
| Serial number | Inspection item | Unit of | Actually measured water inlet value | Actually measure the water | Assessment index | |
| 1 | pH value | —— | 2.65~4.11 | 7.10~7.55 | 6~9 | |
| 2 | Iron | mg/L | 208.3~410.2 | <0.3 | <0.3 |
The coal mine underground pretreatment method provided by the embodiment is suitable for the size of the cross section of the coal mine underground roadway, and has the characteristics of small occupied space, good treatment effect, simplicity in control, high automation degree, low input cost and the like.
The above-described embodiments are only preferred embodiments of the present invention, and are not intended to limit the present invention in any way, and other variations and modifications may be made without departing from the scope of the claims.
Claims (9)
1. The utility model provides a mine water is pretreatment systems in coordination with ground in pit which characterized in that: the mine water underground and ground cooperative pretreatment system comprises:
the monitoring unit is used for monitoring the pH value and the flow of the mine water inflow underground;
a multi-stage neutralization unit for adjusting the pH value of mine water to be more than 7.5 underground;
aerating, oxidizing, standing and primarily precipitating to remove iron in the underground, lifting mine water to the ground, and adding an iron removal unit for oxidizing, precipitating and removing iron in a medicament;
and an automatic control unit for receiving the pH value and flow data obtained by the monitoring unit, controlling the multi-stage neutralization unit to adjust the pH value, monitoring the iron content of the iron removal unit, controlling aeration oxidation and medicament addition of the iron removal unit, and monitoring the pH value and iron content of the effluent;
the monitoring unit, the multistage neutralization unit and the iron removal unit are sequentially connected.
2. The underground and ground cooperative pretreatment system for mine water according to claim 1, characterized in that: the monitoring unit comprises a metering open channel, a flow meter and a first pH value detection device, the metering open channel is provided with a water inlet for mine water inflow and a water outlet for connecting the multi-stage neutralization unit, the flow meter and the first pH value detection device are arranged in the metering open channel, and the flow meter and the first pH value detection device are electrically connected with the automatic control unit.
3. The underground and ground cooperative pretreatment system for mine water according to claim 1, characterized in that: the multistage neutralization unit comprises a neutralization reaction tank, a stirring device and an alkali adding device, a plurality of water-separating weirs are arranged in the neutralization reaction tank, the inside of the neutralization reaction tank is divided into a water inlet area, a mixing area and an overflow area along the flowing direction of mine water treatment in sequence by the water-separating weirs, the stirring device is arranged on the upper portion of the mixing area, the alkali adding device comprises an alkali preparation tank and an alkali adding metering pump, the alkali adding device is arranged above the neutralization reaction tank, and the stirring device and the alkali adding device are both electrically connected with an automatic control unit.
4. The underground and ground cooperative pretreatment system for mine water according to claim 3, characterized in that: the neutralization reaction tank is a plurality of parallel movable reaction tanks or a plurality of series movable reaction tanks.
5. The downhole and surface cooperative pretreatment system for mine water according to claim 3 or 4, wherein: the stirring device comprises a neutralization stirrer, an alkali adding pipeline and an alkali adding feeding port, the alkali adding pipeline is arranged at the upper end of the neutralization stirrer, an impeller is arranged at the lower part of the neutralization stirrer, the alkali adding feeding port is arranged on the impeller, and the alkali adding feeding port is connected with an alkali adding device through the alkali adding pipeline.
6. The downhole and surface cooperative pretreatment system for mine water according to claim 3 or 4, wherein: the overflow area is provided with a second pH detection device which is electrically connected with the automatic control unit.
7. The underground and ground cooperative pretreatment system for mine water according to claim 1, characterized in that: the deironing unit includes preliminary deironing device in the pit and ground deironing device, preliminary deironing device in the pit includes aeration oxidation pond, aeration equipment and is used for the pit water sump that the pit water stew the sediment, and aeration oxidation pond bottom is equipped with the aeration pipeline, and the aeration pipeline links to each other with aeration equipment, and aeration oxidation pond passes through the sump and connects ground deironing device in the pit, ground deironing device includes that the medicament is thrown and is thrown device, oxidation sedimentation tank and filtering pond, and the medicament is thrown and is thrown the device and locate the oxidation sedimentation tank top, and the medicament is thrown and is thrown the device and be connected with the automatic control unit electricity.
8. The underground and ground cooperative pretreatment system for mine water according to claim 7, characterized in that: the aeration device is provided with an aeration control valve which is electrically connected with the automatic control unit; the medicament feeding device comprises a dispensing tank and a dosing metering pump, and the dosing metering pump is electrically connected with the automatic control unit.
9. The downhole and surface cooperative pretreatment system for mine water according to claim 7 or 8, wherein: the oxidation sedimentation tank is a radial flow sedimentation tank, a vertical flow sedimentation tank or a horizontal flow sedimentation tank, a potassium permanganate medicament or a hydrogen peroxide medicament is arranged in the medicament adding device, and the filter tank is a fast filter tank, a slow filter tank or a biological filter tank.
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