CN205995085U - A kind of water process piece-rate system - Google Patents
A kind of water process piece-rate system Download PDFInfo
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- CN205995085U CN205995085U CN201620811674.4U CN201620811674U CN205995085U CN 205995085 U CN205995085 U CN 205995085U CN 201620811674 U CN201620811674 U CN 201620811674U CN 205995085 U CN205995085 U CN 205995085U
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Abstract
This utility model provides a kind of water process piece-rate system, main inclusion separator box, water inlet pipe, outlet pipe, clear water reserviors, jet flow push away mud pipe and sludge collector, described jet flow pushes away mud pipe and sludge collector is located above separator box, in water inlet pipe one end insertion separator box, outlet pipe connection separator box and clear water reserviors, wherein, sludge collector is by least one collecting tank, form equipped with the siphon discharge pipeline of ejector, water inlet pipe other end coupled reaction device, the water side of water-soluble gas generator respectively.This utility model promotes the flco bubbled through the water column to make it in collecting tank by waterpower; siphonic effect is formed by ejector and siphon and takes away the floc sludge in collecting tank; the flco after coagulation and raw water is made to be completely separated; it is efficient, small volume, low cost; mechanical fault, continuous service stable performance, improve the treating capacity of air supporting water treatment system; the separation equipments such as conventionally employed cleaning shoe can be substituted completely, realize scale water separating treatment.
Description
Technical field
The present invention relates to water separation processing equipment field, refer in particular to a kind of water process piece-rate system.
Background technology
At present, sewage disposal device, in eliminating impurities and impurity, is both needed to produce flco by medicine with impurity coagulation, then
Flocs float is made in the water surface by the bubbles entrain of floating trickle in Water Soluble Gas, then by mechanical type mud scraper by the flco on the water surface
Mud blows off, thus reach certain water purification separating.However, due to float flco cumulative so as to weight increase, micro- gas
Bubble disappears, and under the mechanical action of cleaning shoe, easily sedimentation pollution lower floor clear water, does not reach separation truly, and
This mode inefficiency, bulky, failure rate of machinery is high, is both needed to solve further the problems such as maintenance cost increases.
Content of the invention
Present invention aims to the existing state of the art, provide a kind of water process piece-rate system, to realize flco
Mud is quick, be completely separated, and its efficiency high, equipment investment low cost, to make simple, area occupied little.
For reaching above-mentioned purpose, the present invention adopts the following technical scheme that:
The present invention is a kind of water process piece-rate system, mainly includes separator box, water inlet pipe, outlet pipe, clear water reserviors, jet flow push away
Mud pipe and sludge collector, described jet flow pushes away mud pipe and sludge collector is located above separator box, and the insertion of water inlet pipe one end separates
In case, outlet pipe connection separator box and clear water reserviors, wherein, sludge collector by least one collecting tank, equipped with ejector rainbow
Inhale discharge pipeline composition.
Offer at least one mud inlet in above-mentioned collecting tank, and collecting tank is V-shaped, according to the position needs of collecting tank,
Mud inlet can be distributed in side or the bilateral of collecting tank.
Above-mentioned ejector one end connects siphon discharge pipeline, other end connecting water pipe, and water pipe end and connects water pump;Ejector
Lower section is connected with conduit, and trench bottom is collected in conduit insertion;Described siphon discharge pipeline upper end is provided with siphon arm insertion collecting tank
In, and siphon props up tube end and is provided with one way stop peturn valve, the bottom of siphon arm is higher than the bottom of conduit, and siphon discharge pipeline lower end has
There is U-shaped water proof dashpot, in the presence of ejector, make siphon discharge pipeline form siphonic effect.
The one or both sides that above-mentioned jet flow pushes away mud pipe front end are provided with some outlets, and outlet is neat with the position of mud inlet
Flat, the thrust that jet flow pushes away mud pipe water outlet reaches maximum, the most stable, is easy to push bonding flco open and makes it in collecting tank, reaches
Muddy water concurrently separates the effect of process, reduces the sludge coagulating time of staying above, prevents mud from increasing and increases.
One end that above-mentioned water inlet pipe is located in separator box is the vertical end that at least one is extended by separator box bottom up, and
Vertical end top is bell mouth.
Above-mentioned outlet pipe one end is located at and has some water inlets on separator box bottom and tube wall;The outlet pipe other end vertically sets
Stand in clear water reserviors, and top open part is provided with water-level regulator;The range of activity of described water-level regulator is less than separator box top
Facial planes, for adjusting the water level of separator box.
Above-mentioned water inlet pipe other end coupled reaction device, the water side of water-soluble gas generator respectively, as preferred, Water Soluble Gas
The water side of generator also can be equipped with a decompression release head, makes bubble and the water mix homogeneously containing flco to be separated, wherein, one
Individual reactor can connect multiple separator boxs, and a separator box must be equipped with least one water-soluble gas generator.
Above-mentioned reactor is made up of with exocoel at least one rounded inner chamber, and exocoel is higher than inner chamber, and raw water is in mixing
It is drawn in inner chamber through water pump after flocculation aid, coagulant;Meanwhile, the insertion of the charge pipe containing flocculant or multiple auxiliary agent inner chamber
In, raw water and multiple auxiliary agents flco after inner chamber eddy flow are gradually increased and overflow exocoel, and during overflowing, flco is gradually increased to
Steady statue, is finally entered in water inlet pipe by the water side of exocoel bottom.
Above-mentioned jet flow pushes away the end of the mud pipe exocoel through water pump coupled reaction device, by the use of coagulation postprecipitation water as jet flow
Push away mud pipe quotes water so as to directly separation can be formed in the water surface.
The water inlet end of above-mentioned water-soluble gas generator is connected to the lower end of separator box, extracts the clear water after separating as Water Soluble Gas
Generator quote water, formed circulation while it is ensured that Water Soluble Gas clean.
Beneficial effects of the present invention are:The present invention promotes the flco bubbled through the water column to make it in collecting tank using waterpower,
By the in good time moisturizing of ejector siphon, and take away the floc sludge in collecting tank with siphon formation siphonic effect, after making coagulation
Flco is completely separated with raw water, compared to traditional mud scraper, is stirred by mechanicals efforts, make after can avoiding increasing flco
Flco is sunken in clear water, cause to separate not thoroughly situations such as.Binding reactor of the present invention and water-soluble gas generator, can be anti-by one
Answer device to connect multiple separator boxs, realize one and how drag so as to separation efficiency greatly improves, be effectively increased water process amount, it accounts for simultaneously
Little with area, equipment investment cost and later period maintenance low cost, for the mark post of water separation processing equipment of new generation.
Brief description:
Accompanying drawing 1 is the structural representation of the present invention;
Accompanying drawing 2 is the structural representation of sludge collector in the present invention.
Specific embodiment:
In order that juror can be further understood that to the purpose of the present invention, feature and function, hereby lift and preferably implement
Example simultaneously coordinates schema detailed description as follows:
Refer to shown in Fig. 1, Fig. 2, be the structural representation for the preferred embodiments of the invention, the present invention is at a kind of water
Reason piece-rate system, main inclusion separator box 1, water inlet pipe 2, outlet pipe 3, clear water reserviors 4, jet flow push away mud pipe 5 and sludge collector, institute
State jet flow and push away mud pipe 5 and sludge collector above separator box 1, in water inlet pipe 2 one end insertion separator box 1, outlet pipe 3 connects
Separator box 1 and clear water reserviors 4, wherein, sludge collector by least one collecting tank 6, equipped with ejector 78 groups of siphon discharge pipeline
Become, offer at least one mud inlet 61 in collecting tank 6, and collecting tank 6 is V-shaped, flco is divided with clear water in separator box 1 up and down
Floc sludge is discharged by layer by sludge collector, and in addition clear water then discharges clear water reserviors 4, realizes being completely separated.
In such scheme, ejector 7 one end connects siphon discharge pipeline 8, other end connecting water pipe 71, and water pipe 71 end even
Water pump 70;It is connected with conduit 72 below ejector 7, and conduit 72 insertion collecting tank 6 bottom;Described siphon discharge pipeline 8 upper end
It is provided with siphon arm 81 insertion collecting tank 6, and siphon arm 81 end is provided with one way stop peturn valve 811 it is preferred that siphon spoil disposal
Pipe 8 upper end at least one siphon arm 81, is preferably divided into two siphon arms 81, the bottom of siphon arm 81 is higher than conduit 72
Bottom so that stop siphon after, siphon can be formed again;Siphon discharge pipeline 8 lower end has U-shaped water proof dashpot 82,
The water being extracted by water pump 70 enters in siphon discharge pipeline 8 through ejector 7, and meanwhile, conduit 72 is acted on together entering by ejector 7
Enter in siphon discharge pipeline 8, because there is one way stop peturn valve 811 two siphon arm 81 end, therefore two siphon arms 81 are filled by first
Full water, then discharge through U-shaped water proof dashpot 82, make siphon discharge pipeline 8 be internally formed vacuum, produce siphonic effect, then two siphon
Arm 81 starts the flco in automatic sucking collecting tank 6 and is automatically drained out, when the flco surface in collecting tank 6 is propped up less than two siphons
During pipe 81, siphon arm 81 sucks air, then siphonic effect stops, and because conduit 72 bottom is less than siphon arm 81 bottom,
Then after ejector 7 action, conduit 72 can draw the flco of collecting tank 6 bottommost, forms siphonic effect again, therefore when one section
Between then must start up ejector 7 moisturizing once it is ensured that in collecting tank 6 floc sludge circulation extract.
Further, jet flow pushes away the one or both sides of mud pipe 5 front end and is provided with some outlets 51, and outlet 51 with enter mud
The position of mouth 61 flushes, and that is, the direction of outlet 51 must be correspondingly provided with mud inlet 61, and in flush position, the thrust of water is
Maximum, the most stable, flco dirt can be pushed in collecting tank 6, and not destroy the structure of flco.
As preferred, water inlet pipe 2 other end coupled reaction device 9, the water side of water-soluble gas generator 10 respectively.Wherein,
Reactor 9 is made up of at least one rounded inner chamber 91 and exocoel 92, and exocoel 92 is higher than inner chamber 91, and raw water helps solidifying in mixing
It is drawn in inner chamber 91 through water pump 90 after agent, coagulant;Meanwhile, the charge pipe 93 containing flocculant or other multiple auxiliary agents is inserted
Enter in inner chamber 91, raw water and multiple auxiliary agents flco after inner chamber 91 eddy flow are gradually increased and overflow exocoel 92 makes flco stable,
Enter in water inlet pipe 2 by the water side of exocoel 92 bottom afterwards, meanwhile, after Water Soluble Gas are generated by water-soluble gas generator 10, can
So that bubble is broken up through decompression release 68 more stable, more together enter in separator box 1 through water inlet pipe 2 with the water body after coagulation,
Flocs float after then the fine gas bubbles in Water Soluble Gas can drive coagulation is in the superiors.
As preferred, jet flow pushes away the end of mud pipe 5 exocoel 92 through water pump 50 coupled reaction device 9, it is to avoid external water source
Water body in pollution separator box 1;The water inlet end of water-soluble gas generator 10 is connected to the lower end of separator box 1, equally avoids secondary water
The water body of separator box 1 is polluted in source, and water-soluble gas generator 10 makes after extracting the clear water of separator box 1 and forms Water Soluble Gas and flow back to point again
In case 1, so circulate.
Further, one end that water inlet pipe 2 is located in separator box 1 is that at least one is extended by separator box 1 bottom up
Vertical end 21, and vertical end 21 top is bell mouth, under preferable case, vertical end 21 can arrange multiple so as to uniform intake.
Further, outlet pipe 3 one end is located at and has some water inlets 31, outlet pipe 3 on separator box 1 bottom and tube wall
Part in separator box 1 can be arranged with the pipeline of larger area so as to illegally occupy in separator box 1 bottom, and have multiple enter
The mouth of a river 31, helps discharge clear water entrance clear water reserviors 4, outlet pipe 3 other end is then vertically built in clear water reserviors 4, and open top
Place is provided with water-level regulator 32, and the range of activity of described water-level regulator 32 is less than separator box 1 top planes and perpendicular to separation
In case 1, by the up-down adjustment of actuator 32, the height that outlet pipe 3 is located at clear water reserviors 4 one end outlet can be limited, and with this
Adjust the height of separator box 1 water surface, the water yield simultaneously adjusting reactor 9, separator box 1 and clear water reserviors 4 is always maintained at poised state.
And the water side of clear water reserviors 4 then can connect the water treatment system of higher level, do further other and use water requirement.
Certainly, only better embodiment of the present invention illustrated above, not limits the range of the present invention with this, therefore,
Every equivalent change is made on the principle of the invention should be included in protection scope of the present invention.
Claims (10)
1. a kind of water process piece-rate system it is characterised in that:Main inclusion separator box(1), water inlet pipe(2), outlet pipe(3), clear
Pond(4), jet flow push away mud pipe(5)And sludge collector, described jet flow pushes away mud pipe(5)And sludge collector is located at separator box(1)
Top, water inlet pipe(2)Separator box is inserted in one end(1)In, outlet pipe(3)Connection separator box(1)With clear water reserviors(4), wherein, mud
Catcher is by least one collecting tank(6), equipped with ejector(7)Siphon discharge pipeline(8)Composition.
2. a kind of water process piece-rate system according to claim 1 it is characterised in that:Described collecting tank(6)In offer
At least one mud inlet(61), and collecting tank(6)V-shaped.
3. a kind of water process piece-rate system according to claim 1 and 2 it is characterised in that:Described ejector(7)One end is even
Connect siphon discharge pipeline(8), other end connecting water pipe(71), and water pipe(71)End connects water pump(70);Ejector(7)Lower section connects
It is connected to conduit(72), and conduit(72)Insertion collecting tank(6)Bottom;Described siphon discharge pipeline(8)Upper end is provided with siphon arm
(81)Insertion collecting tank(6)In, and siphon arm(81)End is provided with one way stop peturn valve(811), siphon arm(81)Bottom
Higher than conduit(72)Bottom, siphon discharge pipeline(8)Lower end has U-shaped water proof dashpot(82).
4. a kind of water process piece-rate system according to claim 2 it is characterised in that:Described jet flow pushes away mud pipe(5)Front end
One or both sides be provided with some outlets(51), and outlet(51)With mud inlet(61)Position flush.
5. a kind of water process piece-rate system according to claim 1 it is characterised in that:Described water inlet pipe(2)It is located at and separate
Case(1)In one end be at least one by separator box(1)The vertical end that bottom up extends(21), and vertical end(21)Top is
Bell mouth.
6. a kind of water process piece-rate system according to claim 5 it is characterised in that:Described outlet pipe(3)One end is located at
Separator box(1)Some water inlets are had on bottom and tube wall(31);Outlet pipe(3)The other end is vertically built in clear water reserviors(4)In,
And top open part is provided with water-level regulator(32);Described water-level regulator(32)Range of activity be less than separator box(1)Top
Plane.
7. a kind of water process piece-rate system according to any one in claim 1,2,4,5,6 it is characterised in that:Described
Water inlet pipe(2)Other end coupled reaction device respectively(9), water-soluble gas generator(10)Water side.
8. a kind of water process piece-rate system according to claim 7 it is characterised in that:Described reactor(9)By at least one
Individual rounded inner chamber(91)With exocoel(92)Composition, and exocoel(92)Higher than inner chamber(91), raw water is in mixing flocculation aid, coagulation
Through water pump after agent(90)It is drawn into inner chamber(91)In;Meanwhile, the charge pipe containing flocculant or multiple auxiliary agent(93)In insertion
Chamber(91)In, raw water and multiple auxiliary agents are in inner chamber(91)After eddy flow, flco is gradually increased and overflows exocoel(92)Carry out stable,
Afterwards by exocoel(92)The water side of bottom enters water inlet pipe(2)In.
9. a kind of water process piece-rate system according to claim 8 it is characterised in that:Described jet flow pushes away mud pipe(5)End
End is through water pump(50)Coupled reaction device(9)Exocoel(92).
10. a kind of water process piece-rate system according to claim 7 it is characterised in that:Described water-soluble gas generator(10)
Water inlet end be connected to separator box(1)Lower end.
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CN201620811674.4U CN205995085U (en) | 2016-07-29 | 2016-07-29 | A kind of water process piece-rate system |
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CN201620811674.4U CN205995085U (en) | 2016-07-29 | 2016-07-29 | A kind of water process piece-rate system |
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Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN105964018A (en) * | 2016-07-29 | 2016-09-28 | 饶平县施蓝水处理科技有限公司 | Water treatment separating system |
CN114180808A (en) * | 2021-12-28 | 2022-03-15 | 中麒水务科技(深圳)有限公司 | A high-efficient sludge concentration device for sewage treatment |
-
2016
- 2016-07-29 CN CN201620811674.4U patent/CN205995085U/en active Active
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN105964018A (en) * | 2016-07-29 | 2016-09-28 | 饶平县施蓝水处理科技有限公司 | Water treatment separating system |
CN105964018B (en) * | 2016-07-29 | 2018-03-20 | 饶平县施蓝水处理科技有限公司 | A kind of water process piece-rate system |
CN114180808A (en) * | 2021-12-28 | 2022-03-15 | 中麒水务科技(深圳)有限公司 | A high-efficient sludge concentration device for sewage treatment |
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