CN208628132U - A kind of high pressure water dephosphorization system - Google Patents
A kind of high pressure water dephosphorization system Download PDFInfo
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- CN208628132U CN208628132U CN201820986447.4U CN201820986447U CN208628132U CN 208628132 U CN208628132 U CN 208628132U CN 201820986447 U CN201820986447 U CN 201820986447U CN 208628132 U CN208628132 U CN 208628132U
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Abstract
The utility model embodiment discloses a kind of high pressure water dephosphorization system, first gate valve, Water tank level controlling valve group, the first water tank, first pipe pump, first filter, high-pressure hydraulic pump, high pressure check valve, high-pressure hydraulic pump, high-pressure flow regulating valve are sequentially connected, first water tank, second pipe pump, the second water tank are sequentially connected, and the second gate valve is separately connected the water outlet of the second water tank and the water inlet end of Water tank level controlling valve group；Water recovery device is correspondingly arranged with dephosphorization nozzle, and water recovery device, third pipeline pump, the second filter, the second water tank are sequentially connected；One end of water recovery device is arranged in phosphorus piece weighing device, and phosphorus piece weighing device is electrically connected with Water tank level controlling valve group and high-pressure hydraulic pump respectively.The water and the water after water dephosphorization of first water tank spilling are recovered to the second water tank, and may determine that water phosphor-removing effect according to phosphorus piece weighing device, control optimal water and carry out dephosphorization, and then can make full use of water resource, waste when reducing water dephosphorization to water resource.
Description
Technical field
The utility model relates to water dephosphorization technique field more particularly to a kind of high pressure water dephosphorization systems.
Background technique
In steel pipe's production process, when steel pipe at high operating temperatures when be oxidized easily, be formed on its surface one layer it is fine and close
Iron scale (phosphorus skin).Before the rolling if cannot remove this layer of iron scale, they can be by roll pressure during the rolling process
Enter to belt steel surface, influences its surface quality.Remaining iron scale can also accelerate the abrasion of roll, and reduce roll uses the longevity
Life.Therefore, before billet rolling, it is necessary to remove the iron scale on surface.Deoxidation is removed using the mechanical impact force of high pressure water
The method of iron sheet (high pressure water dephosphorization) is the current most current effective practice.
Traditional high pressure water dephosphorization process enters high pressure water dephosphorization system, high pressure water dephosphorization system from vibration means for main pipe for supplying water for water
A nozzle is arranged in squama end.Under the action of nozzle, high pressure water forms the fan-shaped water beam with great impact power, is ejected into
Steel tube surface.Under the action of this high pressure sector Water projectile, iron scale chilling is shunk, and is removed with steel pipe base material, thus
Iron scale is removed clean.
But the water tank of conventional high-tension water dephosphorization system is provided with water overfall, for being more than water level when the water into water tank
When threshold value, extra water overflows.And after the water of descaling jet ejection completes steel tube surface dephosphorization, also directly flow away.Entire
During water dephosphorization, no matter water phosphor-removing effect, water flow remain unchanged.It can be seen from the above, traditional high pressure water dephosphorization system,
During entire high-pressure water descaling, water resource is easy to cause to waste to water resource using insufficient.
Utility model content
The utility model provides a kind of high pressure water dephosphorization system, is provided with solving high pressure water dephosphorization system water in the prior art
Source utilizes insufficient problem.
In order to solve the above-mentioned technical problem, the utility model embodiment discloses following technical solution:
A kind of high pressure water dephosphorization system, including the first gate valve, the second gate valve, Water tank level controlling valve group, the first water tank,
Two water tanks, first pipe pump, second pipe pump, third pipeline pump, first filter, the second filter, high-pressure hydraulic pump, high pressure list
To valve, high-pressure flow regulating valve, water recovery device and phosphorus piece weighing device, in which: the Water tank level controlling valve group connects respectively
The water inlet end of first gate valve and first water tank is connect, the water outlet of first water tank connects the first pipe pump
Water inlet end, the first filter are separately connected the water outlet of the first pipe pump and the water inlet end of the high-pressure hydraulic pump, institute
It states high pressure check valve and is separately connected the water outlet of the high-pressure hydraulic pump and the water inlet end of the high-pressure flow regulating valve, the high pressure
The water outlet of flow control valve connects a dephosphorization nozzle；The water of first water tank overflow end connect the second pipe pump into
The water outlet of water end (W.E.), the second pipe pump connects the water inlet end of second water tank, and second gate valve is separately connected described
The water inlet end of the water outlet of second water tank and the Water tank level controlling valve group；Water recovery device is corresponding with the dephosphorization nozzle to be set
It sets, the water recovery device is provided with multiple water recovery holes, the water outlet of the water recovery device and the third pipeline pump
Water inlet end is first connected, second filter be separately connected the third pipeline pump water outlet and second water tank into
Water end (W.E.)；The phosphorus piece weighing device is arranged in one end of the water recovery device, the phosphorus piece weighing device respectively with the water
Case water level control valve group and high-pressure hydraulic pump electrical connection, the phosphorus piece weighing device are used for according to the phosphorus weighed in the unit time
Sheet weight controls the Water tank level controlling valve group and the high-pressure hydraulic pump.
Optionally, the water recovery device includes drainage steel plate, support base and push plate, the support base and the filter
One end of the drainage steel plate is arranged in the connection of water Interal fixation, the phosphorus piece weighing device, and the push plate is arranged in the filter
The other end of water steel plate, the push plate are flexibly connected with drainage steel plate.
Optionally, the water recovery device includes drainage steel plate, the first support base and the second support base, and described first
Support base and second support base are separately positioned on the both ends of the drainage steel plate, first support base with it is described
Drainage steel plate is flexibly connected by a shaft, and a cylinder is arranged between second support base and the drainage steel plate, described
Cylinder is separately connected second support base and the drainage steel plate, and the phosphorus piece weighing device is arranged in the drainage steel plate
One end of corresponding first support base.
Optionally, water flow control apparatus and the 4th pipe are additionally provided between second filter and second water tank
Road pump, the water outlet of second filter are connected with the water inlet end of the water flow control apparatus, the water traffic organising
The first water outlet of device connects the water inlet end of the 4th pipeline pump, and the water outlet of the 4th pipeline pump connects second water
The water inlet end of case, the second water outlet of the water flow control apparatus are connected with the water inlet end of second filter.
Optionally, the water flow control apparatus includes water quality testing meter, third gate valve and the 4th gate valve, the water quality inspection
Survey instrument water inlet end and connect the water outlet of second filter, the water outlet of the water quality testing meter distinguish the third gate valve and
With one end of the 4th gate valve, the other end of the third gate valve is connected with the water inlet end of the 4th pipeline pump, described
The other end of 4th gate valve is connected with the water inlet end of second filter, the detection module of the water quality testing meter respectively with
The third gate valve and the 4th gate valve electrical connection.
Optionally, second tank top is arranged a fluid level controller, and the fluid level controller is respectively with described first
Gate valve and second gate valve electrical connection.
It optionally, further include the 5th gate valve and the 6th gate valve, what the 5th gate valve was pumped with the first pipe respectively goes out
Water end (W.E.) is connected with the water inlet end of the first filter, the 6th gate valve respectively with the water outlet of the first filter and
The water inlet end of the high-pressure hydraulic pump is connected
As shown from the above technical solution, the utility model embodiment provides a kind of high pressure water dephosphorization system, including first
Gate valve, the second gate valve, Water tank level controlling valve group, the first water tank, the second water tank, first pipe pump, second pipe pump, third pipe
Road pump, first filter, the second filter, high-pressure hydraulic pump, high pressure check valve, high-pressure flow regulating valve, water recovery device and phosphorus
Piece weighing device, in which: the Water tank level controlling valve group is separately connected the water inlet of first gate valve and first water tank
End, the water outlet of first water tank connect the water inlet end of the first pipe pump, and the first filter is separately connected described
The water outlet of first pipe pump and the water inlet end of the high-pressure hydraulic pump, the high pressure check valve are separately connected the high-pressure hydraulic pump
The water outlet of the water inlet end of water outlet and the high-pressure flow regulating valve, the high-pressure flow regulating valve connects a dephosphorization nozzle；
The water of first water tank overflows the water inlet end that end connects the second pipe pump, and the water outlet of the second pipe pump connects institute
The water inlet end of the second water tank is stated, second gate valve is separately connected water outlet and the cistern water level control of second water tank
The water inlet end of valve group；Water recovery device is correspondingly arranged with the dephosphorization nozzle, and the water recovery device is provided with multiple water recycling
Hole, the water outlet of the water recovery device are connected with the water inlet end of the third pipeline pump, and second filter connects respectively
Connect the water outlet of the third pipeline pump and the water inlet end of second water tank；The phosphorus piece weighing device setting is returned in the water
One end of receiving apparatus, the phosphorus piece weighing device are electrically connected with the Water tank level controlling valve group and the high-pressure hydraulic pump respectively,
The phosphorus piece weighing device is used to control the Water tank level controlling valve group and institute according to the phosphorus sheet weight weighed in the unit time
State high-pressure hydraulic pump.High pressure water dephosphorization system provided by the utility model can be by the water after the water of the first water tank spilling and water dephosphorization
It is recovered to the first water tank, and may determine that the phosphor-removing effect of water dephosphorization system according to phosphorus piece weighing device, controls optimal water
Amount carries out dephosphorization, and then can make full use of water resource, waste when reducing water dephosphorization to water resource.
Detailed description of the invention
It, below will be to attached drawing needed in the embodiment in order to illustrate more clearly of the technical solution of the utility model
It is briefly described, it should be apparent that, for those of ordinary skills, in the premise of not making the creative labor property
Under, it is also possible to obtain other drawings based on these drawings.
Fig. 1 is a kind of structural schematic diagram of high pressure water dephosphorization system provided by the embodiment of the utility model；
Fig. 2 is a kind of side view of water recovery device provided by the embodiment of the utility model；
Fig. 3 is the side view of another water recovery device provided by the embodiment of the utility model；
Fig. 4 is a kind of structural schematic diagram of water flow control apparatus provided by the embodiment of the utility model；
In Fig. 1-4, symbol is expressed as: the first gate valve of 1-, the second gate valve of 2-, 3- Water tank level controlling valve group, the first water of 4-
Case, the second water tank of 5-, 6- first pipe pump, 7- second pipe pump, 8- third pipeline pump, 9- first filter, 10- second are filtered
Device, 11- high-pressure hydraulic pump, 12- high pressure check valve, 13- high-pressure flow regulating valve, 14- water recovery device, 141- drainage steel plate,
142- support base, 143- push plate, the first support base of 144-, the second support base of 145-, 146- cylinder, the weighing of 15- phosphorus piece
Device, 16- water flow control apparatus, 161- water quality testing meter, 162- third gate valve, the 4th gate valve of 163-, the 4th pipeline of 17-
Pump, 18- fluid level controller, the 5th gate valve of 19-, the 6th gate valve of 20-.
Specific embodiment
The utility model is described in detail with reference to the accompanying drawing.
As shown in Figure 1, be a kind of structural schematic diagram of high pressure water dephosphorization system provided by the embodiment of the utility model, referring to
Fig. 1, the method, system include: the first gate valve 1, the second gate valve 2, Water tank level controlling valve group 3, the first water tank 4, the second water tank 5,
First pipe pump 6, second pipe pump 7, third pipeline pump 8, first filter 9, the second filter 10, high-pressure hydraulic pump 11, high pressure
Check valve 12, high-pressure flow regulating valve 13, water recovery device 14,15 (not shown) of phosphorus piece weighing device, water traffic organising
Device 16, the 4th pipeline pump 17, fluid level controller 18, the 5th gate valve 19 and the 6th gate valve 20.
The Water tank level controlling valve group 3 is separately connected the water inlet end of first gate valve 1 and first water tank 4, supplies
The water flow of water end (W.E.) enters the water level control valve group 3 by the first gate valve 1, and the water level control valve group 3 enters for controlling
The water of one water tank 4.The water outlet of first water tank 4 connects the water inlet end of the first pipe pump 6, the first filter
9 are separately connected the water inlet end of the water outlet of the first pipe pump 6 and the high-pressure hydraulic pump 11.From the water outlet of the first water tank 4
The effect that the water of output first passes around first pipe pump 6 enters first filter 9, and high-pressure hydraulic pump is entered after filtering
In 11.It should be pointed out that first pipe pump 6 can make the water entered in first filter 9 have certain hydraulic pressure, into
And it can smoothly enter into high-pressure hydraulic pump 11 after filtering.The high pressure check valve 12 be separately connected the high-pressure hydraulic pump 11 water outlet and
The water outlet of the water inlet end of the high-pressure flow regulating valve 13, the high-pressure flow regulating valve 13 connects a dephosphorization nozzle.
In the actual production process since water level control valve group 3 can not accurately control the water entered in the first water tank 4,
Therefore water spilling end is arranged in water tank 4.Because the water overflowed does not have any hydraulic pressure, setting second pipe pumps 7.First water
The water of case 4 overflows the water inlet end of end connection second pipe pump 7, overflows the water that end is overflowed from water and enters 7 output of second pipe pump
It is provided with certain hydraulic pressure afterwards.The water outlet of second pipe pump 7 connects the water inlet end of second water tank 5, from described the
The water of two pipeline pumps, 7 water outlet output enters the second water tank 5, thus the effect of the second water tank 5 first is that overflowing to the first water tank 4
The collection of water outlet is deposited.The water outlet of second water tank 5 is connected with the water inlet end of water level control valve group 3, the water outlet of the second water tank 5 with
The second gate valve 2 is arranged in water level control valve group 3, and the second gate valve 2 is in close state when water regular supply in the first gate valve 1.
In the utility model, the second water tank 5 can also recycle the water after dephosphorization.Water recovery device 14 and the dephosphorization nozzle
It is correspondingly arranged, the water recovery device 14 is provided with multiple water recovery holes.The water that dephosphorization nozzle sprays completes the dephosphorization to steel pipe
Afterwards, it is flowed into the pipeline being connected with multiple water recovery holes by water recovery holes, is flowed out from the water outlet of water recovery device 14.Water
The water inlet end of the water outlet connection third pipeline pump 8 of recyclable device 14, the water outlet of third pipeline pump 8 connects the second filter 10
Water inlet end, the second filter 10 is filtered processing to the post-job water of dephosphorization, then passes through the water outlet of the second filter 10
End is transported in the second water tank 5.
In one exemplary embodiment, water flow is additionally provided between second filter 10 and second water tank 5
To control device 16 and the 4th pipeline pump 17, the water outlet of second filter 10 and the water flow control apparatus 16 into
Water end (W.E.) is connected, and 16 first water outlet of water flow control apparatus connects the water inlet end of the 4th pipeline pump 17, and described
The water outlet of four pipeline pumps 17 connects the water inlet end of second water tank 5, and the water flow control apparatus 16 second is discharged
End is connected with the water inlet end of second filter 10.After carrying out high pressure water dephosphorization operation, water quality may become
Change, such as pH value etc..Therefore setting 16 purpose of water flow control apparatus is to carry out water to the water exported from the second filter 10
Secondary second filter 10 of sending back to of water is filtered, can be added at this time appropriate if water quality is undesirable by quality detection
Water treatment agent.
As shown in Fig. 2, the present embodiment flow direction median control device 16 includes water quality testing meter 161, third gate valve 162 and the
Four gate valves 163,161 water inlet end of water quality testing meter connect the water outlet of second filter 10, the water quality testing meter
The third gate valve 162 and one end with the 4th gate valve 163 are distinguished in 161 water outlet, the third gate valve 162 it is another
End is connected with the water inlet end of the 4th pipeline pump 17, the other end and second filter 10 of the 4th gate valve 163
Water inlet end be connected, the detection module of the water quality testing meter 161 respectively with the third gate valve 162 and the 4th gate valve
163 electrical connections.If how the water quality that water quality testing meter 161 detects the water transported out from the second filter 10 requires, control
Third gate valve 162 processed is opened, and the 4th gate valve 163 is closed, and water is transported to the 4th pipeline pump 17, is then delivered in the second water tank 5.
If water quality is undesirable, water quality testing meter 161 controls third gate valve 162 and closes, and the 4th gate valve 163 is opened, and water flows again
Return the second filter 10.
The dosage of water when in the present embodiment in order to control dephosphorization operation, guarantees making full use of for water, therefore imitate according to dephosphorization
Fruit quality controls water flow and hydraulic pressure.Therefore phosphorus piece weighing device 15 is set in one end of water recovery device 14.It is described
Phosphorus piece weighing device 15 is electrically connected with the Water tank level controlling valve group 3 and the high-pressure hydraulic pump 11 respectively, the phosphorus piece weighing
Device 15 is used to control the Water tank level controlling valve group 3 and the high-pressure hydraulic pump according to the phosphorus sheet weight weighed in the unit time
11.Since steel pipe is generally standard component, when can will be divided into multiple even operations to a steel pipe dephosphorization activity duration
Between section, then each activity duration section is identical.If a steel pipe phosphor-removing effect is good, the weight of the phosphorus piece removed should be
In one weight range, therefore the weight for the phosphorus piece removed in an activity duration section should also be the weight model an of minor swing
It encloses.So if in the phosphorus piece that some activity duration section is got, the minimum being significantly less weight than in the Historical Jobs period is heavy
Amount, then can be concluded that phosphor-removing effect is bad.It is defeated into water tank 1 to control Water tank level controlling valve group 3 for phosphorus piece weighing device 15 at this time
More water are sent, and controls high-pressure hydraulic pump 11 and increases hydraulic pressure.If in the weight for the phosphorus piece that several activity duration sections are got
It is more stable, then it can suitably reduce water flow and hydraulic pressure, if removing phosphorus piece in activity duration section after reducing
Weight change is little, then can carry out dephosphorization operation according to current water flow and hydraulic pressure.
In one exemplary embodiment, as shown in figure 3, water recovery device 14 includes drainage steel plate 141, support base
142 and push plate 143, the support base 142 be fixedly connected with the drainage steel plate 141, the phosphorus piece weighing device 15 is arranged
In one end of the drainage steel plate 141, the other end of the drainage steel plate 141, the push plate 143 is arranged in the push plate 143
It is flexibly connected with drainage steel plate 141.Push plate 143 can be after an activity duration section by the scale removed push-in phosphorus piece weighing
Device 15, the scale weight that phosphorus piece weighing device 15 removes upper activity duration section are weighed.
In another embodiment, as shown in figure 4, water recovery device 14 includes 141 first support base 144 of drainage steel plate
With the second support base 145, first support base 144 and second support base 145 are separately positioned on the drainage
The both ends of steel plate 141, first support base 144 are flexibly connected with the drainage steel plate 141 by a shaft, and described second
One cylinder 146 is set between support base 145 and the drainage steel plate 141, and the cylinder 146 is separately connected second support
Pedestal 145 and the drainage steel plate 141, the setting of phosphorus piece weighing device 15 is in corresponding first support of the drainage steel plate 141
One end of pedestal 144.After an activity duration section, cylinder 146 can jack up 141 one end of drainage steel plate, drainage steel plate
141 other end can then rotate, due to being provided with shaft between the first support base 144 so that drainage steel plate 141 is in
One heeling condition, at this time due to the effect of gravity, the scale removed can slide into phosphorus piece weighing device 15, phosphorus piece weighing device 15
It weighs to scale weight.
It is noted that carrying partial moisture since initial time enters phosphorus piece weighing device 15, phosphorus piece claims
Refitting, which is set, to be needed to wait a preset time period before 15 pairs of scales are weighed, until the phosphorus sheet weight being weighed to is in one surely
Fixed value.
One fluid level controller 18 is set at the top of the second water tank 5 in the present embodiment, the fluid level controller 18 respectively with it is described
First gate valve 1 and second gate valve 2 electrical connection.If the water collected in the second water tank 5 reaches preset value, in the second water tank
Reaching certain water level in 5, fluid level controller 18 detects at this time, directly controls the closing of the first gate valve 1, and the second gate valve 2 is opened,
Using the water in the second water tank 5, the secondary use of water is realized at this time.
High pressure water dephosphorization system provided in this embodiment further includes the 5th gate valve 19 and the 6th gate valve 10.5th gate valve
19 are connected with the water inlet end of the water outlet of first pipe pump 6 and the first filter 9 respectively, the 6th gate valve 20
It is connected respectively with the water inlet end of the water outlet of the first filter 9 and the high-pressure hydraulic pump 11.5th gate valve 19 and the 6th
The setting of gate valve 20, which can be controlled separately, enters water in first filter 9 and high-pressure hydraulic pump 11.It, can at the end of dephosphorization operation
It is supplied with the water for cooperating the first gate valve 1 and the second gate valve 2 to cut off whole system by the 5th gate valve 19 and the 6th gate valve 20.
As can be seen from the above embodiments, a kind of high pressure water dephosphorization system provided in this embodiment, including the first gate valve 1, second
Gate valve 2, Water tank level controlling valve group 3, the first water tank 4, the second water tank 5, first pipe pump 6, second pipe pump 7, third pipeline
Pump 8, first filter 9, the second filter 10, high-pressure hydraulic pump 11, high pressure check valve 12, high-pressure flow regulating valve 13, water recycling
Device 14, phosphorus piece weighing device 15, water flow control apparatus 16, the 4th pipeline pump 17, fluid level controller 18,19 and of the 5th gate valve
6th gate valve 20, the Water tank level controlling valve group 3 are separately connected the water inlet end of first gate valve 1 and first water tank 4,
The water outlet of first water tank 4 connects the water inlet end of the first pipe pump 6, and the first filter 9 is separately connected described
The water outlet of first pipe pump 6 and the water inlet end of the high-pressure hydraulic pump 11, the high pressure check valve 12 are separately connected the high pressure
The water inlet end of the water outlet of water pump 11 and the high-pressure flow regulating valve 13, the water outlet connection of the high-pressure flow regulating valve 13
One dephosphorization nozzle；The water of first water tank 4 overflows the water inlet end that end connects the second pipe pump 7, the second pipe pump 7
Water outlet connect the water inlet end of second water tank 5, second gate valve 2 is separately connected the water outlet of second water tank 5
With the water inlet end of the Water tank level controlling valve group 3；Water recovery device 14 is correspondingly arranged with the dephosphorization nozzle, the water recycling
Device 14 is provided with multiple water recovery holes, and the water outlet of the water recovery device is connected with the water inlet end of the third pipeline pump 8
It connects, second filter 10 is separately connected the water outlet of the third pipeline pump 8 and the water inlet end of second water tank 5, water
Flow control apparatus 16 and the 4th pipeline pump 17 are arranged between the second filter 10 and the second water tank 5；The phosphorus piece weighing dress
Set 15 one end that the water recovery device 14 is set, the phosphorus piece weighing device 14 respectively with the Water tank level controlling valve group
3 and the high-pressure hydraulic pump 11 be electrically connected, the phosphorus piece weighing device 15 be used for according to the phosphorus sheet weight control weighed in the unit time
Make the Water tank level controlling valve group 3 and the high-pressure hydraulic pump 11.5th gate valve 19 pumps 6 with the first pipe respectively
Water outlet is connected with the water inlet end of the first filter 9, the 6th gate valve 20 respectively with the first filter 9 go out
Water end (W.E.) is connected with the water inlet end of the high-pressure hydraulic pump 11.High pressure water dephosphorization system provided by the utility model can be by the first water
The water and the water after water dephosphorization of the spilling of case 4 are recovered to the second water tank 5, and may determine that water dephosphorization according to phosphorus piece weighing device 15
The phosphor-removing effect of system controls optimal water and carries out dephosphorization, and then can make full use of water resource, to water when reducing water dephosphorization
The waste of resource.
It should be noted that, in this document, the relational terms of such as " first " and " second " or the like are used merely to one
A entity or operation with another entity or operate distinguish, without necessarily requiring or implying these entities or operation it
Between there are any actual relationship or orders.Moreover, the terms "include", "comprise" or its any other variant are intended to
Cover non-exclusive inclusion, so that the process, method, article or equipment for including a series of elements not only includes those
Element, but also including other elements that are not explicitly listed, or further include for this process, method, article or setting
Standby intrinsic element.In the absence of more restrictions, the element limited by sentence "including a ...", it is not excluded that
There is also other identical elements in the process, method, article or apparatus that includes the element.
Above-described the utility model embodiment does not constitute the restriction to scope of protection of the utility model.
Claims (7)
1. a kind of high pressure water dephosphorization system, which is characterized in that including the first gate valve (1), the second gate valve (2), cistern water level control
Valve group (3), the first water tank (4), the second water tank (5), first pipe pump (6), second pipe pump (7), third pipeline pump (8), the
One filter (9), the second filter (10), high-pressure hydraulic pump (11), high pressure check valve (12), high-pressure flow regulating valve (13), water
Recyclable device (14) and phosphorus piece weighing device (15), in which:
The Water tank level controlling valve group (3) is separately connected the water inlet end of first gate valve (1) and first water tank (4),
The water outlet of first water tank (4) connects the water inlet end of the first pipe pump (6), and the first filter (9) connects respectively
The water outlet of the first pipe pump (6) and the water inlet end of the high-pressure hydraulic pump (11) are connect, the high pressure check valve (12) is respectively
The water outlet of the high-pressure hydraulic pump (11) and the water inlet end of the high-pressure flow regulating valve (13) are connected, the high pressure flow is adjusted
The water outlet of valve (13) connects a dephosphorization nozzle；
The water of first water tank (4) overflows the water inlet end that end connects the second pipe pump (7), and the second pipe pumps (7)
Water outlet connect the water inlet end of second water tank (5), second gate valve (2) is separately connected second water tank (5)
The water inlet end of water outlet and the Water tank level controlling valve group (3)；
Water recovery device (14) is correspondingly arranged with the dephosphorization nozzle, and the water recovery device (14) is provided with multiple water recycling
Hole, the water outlet of the water recovery device (14) are connected with the water inlet end of the third pipeline pump (8), second filter
(10) water outlet of the third pipeline pump (8) and the water inlet end of second water tank (5) are separately connected；
Phosphorus piece weighing device (15) setting is in one end of the water recovery device (14), the phosphorus piece weighing device (15) point
It is not electrically connected with the Water tank level controlling valve group (3) and the high-pressure hydraulic pump (11), the phosphorus piece weighing device (15) is used for
The Water tank level controlling valve group (3) and the high-pressure hydraulic pump (11) are controlled according to the phosphorus sheet weight weighed in the unit time.
2. high pressure water dephosphorization system according to claim 1, which is characterized in that the water recovery device (14) includes drainage
Steel plate (141), support base (142) and push plate (143), the support base (142) and the drainage steel plate (141) are fixed to be connected
It connects, in one end of the drainage steel plate (141), the push plate (143) is arranged described for phosphorus piece weighing device (15) setting
The other end of drainage steel plate (141), the push plate (143) are flexibly connected with drainage steel plate (141).
3. high pressure water dephosphorization system according to claim 1, which is characterized in that the water recovery device (14) includes drainage
Steel plate (141), the first support base (144) and the second support base (145), first support base (144) and described
Two support bases (145) are separately positioned on the both ends of the drainage steel plate (141), first support base (144) with it is described
Drainage steel plate (141) is flexibly connected by a shaft, between second support base (145) and the drainage steel plate (141)
It is arranged a cylinder (146), the cylinder (146) is separately connected second support base (145) and the drainage steel plate
(141), the one end of phosphorus piece weighing device (15) setting in the drainage steel plate (141) corresponding first support base (144).
4. -3 any think the high pressure water dephosphorization system according to claim 1, which is characterized in that second filter (10)
Water flow control apparatus (16) and the 4th pipeline pump (17), second filtering are additionally provided between second water tank (5)
The water outlet of device (10) is connected with the water inlet end of the water flow control apparatus (16), the water flow control apparatus (16)
One water outlet connects the water inlet end of the 4th pipeline pump (17), the water outlet connection described second of the 4th pipeline pump (17)
The water inlet end of water tank (5), the water inlet end of (16) second water outlet of water flow control apparatus and second filter (10)
It is connected.
5. high pressure water dephosphorization system according to claim 4, which is characterized in that the water flow control apparatus (16) includes
Water quality testing meter (161), third gate valve (162) and the 4th gate valve (163), water quality testing meter (161) water inlet end connect institute
State the water outlet of the second filter (10), the water outlet of the water quality testing meter (161) distinguish the third gate valve (162) and and
One end of 4th gate valve (163), the other end of the third gate valve (162) and the water inlet end of the 4th pipeline pump (17)
It is connected, the other end of the 4th gate valve (163) is connected with the water inlet end of second filter (10), the water quality inspection
The detection module for surveying instrument (161) is electrically connected with the third gate valve (162) and the 4th gate valve (163) respectively.
6. high pressure water dephosphorization system according to claim 5, which is characterized in that setting one at the top of second water tank (5)
Fluid level controller (18), the fluid level controller (18) are electrically connected with first gate valve (1) and second gate valve (2) respectively
It connects.
7. high pressure water dephosphorization system according to claim 6, which is characterized in that further include the 5th gate valve (19) and the 6th lock
Valve (20), the 5th gate valve (19) respectively with the first pipe pump (6) water outlet and the first filter (9) into
Water end (W.E.) is connected, the 6th gate valve (20) respectively with the water outlet of the first filter (9) and the high-pressure hydraulic pump (11)
Water inlet end be connected.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820986447.4U CN208628132U (en) | 2018-06-25 | 2018-06-25 | A kind of high pressure water dephosphorization system |
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| CN201820986447.4U CN208628132U (en) | 2018-06-25 | 2018-06-25 | A kind of high pressure water dephosphorization system |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108906897A (en) * | 2018-06-25 | 2018-11-30 | 鑫鹏源智能装备集团有限公司 | A kind of high pressure water dephosphorization system |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108906897A (en) * | 2018-06-25 | 2018-11-30 | 鑫鹏源智能装备集团有限公司 | A kind of high pressure water dephosphorization system |
| CN108906897B (en) * | 2018-06-25 | 2023-08-29 | 鑫鹏源智能装备集团有限公司 | High-pressure water dephosphorization system |
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