CN108843579A - Low damage high-efficiency self-suction centrifugal pump - Google Patents
Low damage high-efficiency self-suction centrifugal pump Download PDFInfo
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- CN108843579A CN108843579A CN201810775515.7A CN201810775515A CN108843579A CN 108843579 A CN108843579 A CN 108843579A CN 201810775515 A CN201810775515 A CN 201810775515A CN 108843579 A CN108843579 A CN 108843579A
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- 238000005086 pumping Methods 0.000 claims abstract description 59
- 239000000203 mixture Substances 0.000 claims abstract description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 88
- 238000007789 sealing Methods 0.000 claims description 41
- 238000000926 separation method Methods 0.000 claims description 38
- 210000004907 gland Anatomy 0.000 claims description 19
- 230000037452 priming Effects 0.000 claims description 19
- 125000004122 cyclic group Chemical group 0.000 claims description 8
- 230000003068 static effect Effects 0.000 claims description 6
- 239000003351 stiffener Substances 0.000 claims description 6
- 238000011049 filling Methods 0.000 claims description 4
- 238000011010 flushing procedure Methods 0.000 claims description 3
- 230000007704 transition Effects 0.000 claims description 3
- 230000005540 biological transmission Effects 0.000 claims 1
- 230000005611 electricity Effects 0.000 claims 1
- 239000007787 solid Substances 0.000 claims 1
- 239000007788 liquid Substances 0.000 description 23
- 238000010586 diagram Methods 0.000 description 12
- 239000012530 fluid Substances 0.000 description 10
- 238000000034 method Methods 0.000 description 7
- 238000002156 mixing Methods 0.000 description 6
- 230000008569 process Effects 0.000 description 6
- 230000008859 change Effects 0.000 description 5
- 230000008676 import Effects 0.000 description 4
- 238000010992 reflux Methods 0.000 description 4
- 241000220324 Pyrus Species 0.000 description 3
- 238000006243 chemical reaction Methods 0.000 description 3
- 235000021017 pears Nutrition 0.000 description 3
- 238000003466 welding Methods 0.000 description 3
- 230000003321 amplification Effects 0.000 description 2
- 238000005266 casting Methods 0.000 description 2
- 238000010276 construction Methods 0.000 description 2
- 238000009792 diffusion process Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000012423 maintenance Methods 0.000 description 2
- 238000003199 nucleic acid amplification method Methods 0.000 description 2
- 238000009834 vaporization Methods 0.000 description 2
- 230000008016 vaporization Effects 0.000 description 2
- 229910000831 Steel Inorganic materials 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 230000001133 acceleration Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000005119 centrifugation Methods 0.000 description 1
- 230000008602 contraction Effects 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000004134 energy conservation Methods 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 238000005213 imbibition Methods 0.000 description 1
- 230000006698 induction Effects 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 230000001788 irregular Effects 0.000 description 1
- 230000007246 mechanism Effects 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000035772 mutation Effects 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
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- 239000010959 steel Substances 0.000 description 1
- 206010047302 ventricular tachycardia Diseases 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Classifications
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
- F04D—NON-POSITIVE-DISPLACEMENT PUMPS
- F04D1/00—Radial-flow pumps, e.g. centrifugal pumps; Helico-centrifugal pumps
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
- F04D—NON-POSITIVE-DISPLACEMENT PUMPS
- F04D15/00—Control, e.g. regulation, of pumps, pumping installations or systems
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
- F04D—NON-POSITIVE-DISPLACEMENT PUMPS
- F04D15/00—Control, e.g. regulation, of pumps, pumping installations or systems
- F04D15/0005—Control, e.g. regulation, of pumps, pumping installations or systems by using valves
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
- F04D—NON-POSITIVE-DISPLACEMENT PUMPS
- F04D29/00—Details, component parts, or accessories
- F04D29/08—Sealings
- F04D29/086—Sealings especially adapted for liquid pumps
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
- F04D—NON-POSITIVE-DISPLACEMENT PUMPS
- F04D29/00—Details, component parts, or accessories
- F04D29/08—Sealings
- F04D29/10—Shaft sealings
- F04D29/106—Shaft sealings especially adapted for liquid pumps
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
- F04D—NON-POSITIVE-DISPLACEMENT PUMPS
- F04D29/00—Details, component parts, or accessories
- F04D29/18—Rotors
- F04D29/22—Rotors specially for centrifugal pumps
- F04D29/2205—Conventional flow pattern
- F04D29/2222—Construction and assembly
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
- F04D—NON-POSITIVE-DISPLACEMENT PUMPS
- F04D29/00—Details, component parts, or accessories
- F04D29/66—Combating cavitation, whirls, noise, vibration or the like; Balancing
- F04D29/669—Combating cavitation, whirls, noise, vibration or the like; Balancing especially adapted for liquid pumps
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
- F04D—NON-POSITIVE-DISPLACEMENT PUMPS
- F04D9/00—Priming; Preventing vapour lock
- F04D9/02—Self-priming pumps
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- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Structures Of Non-Positive Displacement Pumps (AREA)
Abstract
The present invention relates to a kind of low damage high-efficiency self-suction centrifugal pumps, including pumping chamber, pumping chamber cross section is integrally in figure six, outer ledge line is by helix A, curve B and line C composition, line C connect with helix A and curve B simultaneously and is the intersection of pumping chamber exit face and cross section, inside edge line is circle D, there is a point X in helix A on the line segment opposite with curve B, cross simultaneously point X and intersection point Y flow section pumping chamber is divided into the T1 section of the strip being connected smoothly with it is T2 sections cricoid, there is point S near point X on helix A in T2 sections, the flow section that helix between point Y and point S intersects is coplanar with center of circle E, it is class isosceles trapezoid and area is gradually increased, the flow section area for crossing S point is maximum, the hydraulic efficiency of low damage high-efficiency self-suction centrifugal pump is 88~97%.Pump of the invention takes into account efficiency, self-priming performance, hydraulic performance and operational reliability using full runner the Hydraulic Design, and application prospect is good.
Description
Technical field
The invention belongs to centrifugal pump fields, are related to a kind of low damage high-efficiency self-suction centrifugal pump.
Background technique
Self priming pump is the centrifugal pump of special construction, only needs starting for the first time to pour water, directly initiates later, has and use
Convenient, reliable operation and the advantages of be convenient for long-distance centralized control, especially suitable for sucting installation and the frequent occasion of starting, but lacks
Point is that pump whole efficiency is low.Existing self priming pump is divided into two kinds of structures of internal-mixing and exterior mixing, and internal-mixing is that liquid stream flows back into impeller
Import, this structure efficiency is relatively high, and exterior mixing is that liquid stream flows back into impeller outlet, relatively inefficient, but self-priming time
Shorter, however, being the self priming pump of exterior mixing or internal-mixing, the relatively general centrifugal pump whole efficiency of efficiency is all low.
In addition, prior art self priming centrifugal pump also cannot achieve efficiency, self-priming performance, hydraulic performance and operational reliability
Take into account, existing self priming pump air-water separation chamber place pumping chamber collect impeller outlet liquid stream energy, pumping chamber be usually weld
Part, the generally rectangular cross-section section of pressurized water chamber structure are operated using the welding of hand cut steel plate, and error hand-manipulated is big, cannot
Guarantee that the Hydraulic Design size causes hydraulic loss big to form certain hydraulic blow, and rectangular cross section pumping chamber is not inconsistent
Collaborate body flowing law, easily forms whirlpool in edges and corners, to form turbulent flow, cause certain hydraulic loss.It is received in impeller outlet
The liquid stream of collection is discharged to air-water separation chamber without the conversion of abundant energy in pumping chamber and is separated, this process hydraulic loss packet
It includes from impeller outlet to the impact loss of pumping chamber import and unexpected divergence loss and pumping chamber and exports to air-water separation chamber
Unexpected divergence loss, since flow stream velocity is fast, the process hydraulic loss is very big, greatly affected water pumping force efficiency.Air water point
Structure and regurgitant volume from room determine properties of product, for guarantee product self-priming performance and self-priming time, be typically designed take compared with
Big regurgitant volume so that pump plot ratio is low, and because air-water separation chamber structure, speed cannot effectively be converted into pressure in impeller
Power energy, but adjoint impact, mutation diffusion or shrinkage loss are fallen, the whole efficiency pumped in this way is with regard to lower, according to statistics, generally certainly
Sucking pump scene actual operating efficiency is no more than 50%, causes very big energy consumption waste, does not meet national energy-saving environmental requirement, and
And self-suction pump impeller cannot be cut, flow pressure is constant after the completion of every pump design, and after Impeller trim, impeller and the pump housing forget place
Gap increase, air-water mixture cannot quickly be discharged, and influence to pump self-priming performance.
Therefore, it is small and the low of efficiency, self-priming performance, hydraulic performance and operational reliability can be taken into account to develop a kind of hydraulic loss
Damage the great realistic meaning of high-efficiency self-suction centrifugal pump.
Summary of the invention
The purpose of the present invention is overcoming deficiency in the prior art, provide a kind of hydraulic loss it is small and can take into account efficiency, from
The low damage high-efficiency self-suction centrifugal pump of absorption energy, hydraulic performance and operational reliability.The present invention uses helix pears type pumping chamber,
Impeller outlet liquid stream is effectively collected, the entire cross-section of river is pears type, and no corner angle meet fluid flowing law without vortex, reduce leaf
Wheel exports to the impact loss and divergence loss of pumping chamber import, and entire pumping chamber liquid stream is not to be fed directly to gas-water separation
Room, but air-water separation chamber can just be entered by designing certain flow rate, and liquid flowing energy filling to pressure energy is realized in entire pumping chamber
Divide conversion.It when kinetic energy drops to design value, just arrives air-water separation chamber and is separated, and liquid flow path direction is discharged in new construction pumping chamber
It is tangent with air-water separation chamber cylinder circumference, impact loss and divergence loss are reduced to the greatest extent, improve the efficiency of pump.
In order to achieve the above object, present invention employs the following technical solutions：
Low damage high-efficiency self-suction centrifugal pump, including pumping chamber, pumping chamber cross section are integrally in figure six, outer ledge line
It is made of helix A, curve B and line C, line C connect with helix A and curve B simultaneously and is pumping chamber exit face and cross section
Intersection, inside edge line is circle D, on outer ledge line the center of circle E of the intersection point Y distance circle D of helix A and curve B recently and
Distance is more than or equal to the radius of circle D；
There is a point X in helix A on the line segment opposite with curve B, while the flow section for crossing point X and intersection point Y will press water
Room is divided into the T1 section of the strip being connected smoothly and T2 section cricoid, and being leaned near point X on the helix A in T2 sections has a point S,
The flow section that helix between point Y and point S intersects is coplanar with center of circle E, is class isosceles trapezoid and area gradually increases
Greatly, the flow section area for crossing S point is maximum, and the main distinction of class isosceles trapezoid and isosceles trapezoid is that side and bottom are smooth
Transition connection, the upper bottom and bottom of class isosceles trapezoid are respectively the intersection of T2 sections of most inner sides and outermost and flow section, are owned
Class isosceles trapezoid upper bottom length it is identical；
The hydraulic efficiency of low damage high-efficiency self-suction centrifugal pump is 88~97%, compares common self priming centrifugal pump hydraulic efficiency
About 10~15% are improved, low damage high-efficiency self-suction centrifugal pump of the invention significantly improves hydraulic efficiency compared to the prior art.
As a preferred technical scheme：
Low damage high-efficiency self-suction centrifugal pump as described above, the line C are straight line, the class isosceles trapezoid and isosceles trapezoid
Difference to also reside in bottom be smoothed curve, the angles of flare of T1 section runners is no more than 12 °, the mistake of T1 sections of runner pumping chamber outlet ends
Flow section area is maximum.Protection scope of the present invention is not limited to that line C can also be curve, the angle of flare of T1 sections of runners
12 ° can be greater than.
Low damage high-efficiency self-suction centrifugal pump as described above, the pumping chamber are the internal chamber of the pumping chamber pump housing；As point Y
When with the radius for being greater than circle D at a distance from the E of the center of circle, gap between filling intersection point Y and circle D is equipped in the pumping chamber pump housing at intersection point Y
Plate is scraped water and is forgotten, and plate scrapes the tangential direction that the arranged direction that water is forgotten is helix A intersection point Y location, and effect is turned off water
Circulation in T2 sections；Through-hole U is surrounded on the inside of T2 sections of corresponding pumping chamber pump housing sections, through-hole U is mainly by coaxial cylinder
Through-hole i and truncated cone-shaped through-hole j is formed by connecting and the aperture of junction through-hole i and through-hole j are equal, hole of the through-hole j far from the end through-hole i
Diameter is less than the aperture of through-hole i, and through-hole i is connected to T2 sections of runners and is fixed with pump cover far from the end through-hole j, and pump cover is equipped with cyclic annular convex
Play q1；
The pumping chamber pump housing is fixed in annular base plate by connecting tube and stiffener plate, the ring inner via hole of annular base plate
Be connected to through-hole U by round table-like connecting tube, stiffener plate circle distribution in annular base plate and simultaneously with connecting tube, cyclic annular bottom
Plate and the connection of the pumping chamber pump housing；
Be disposed with impeller in the through-hole i, and the two is coaxial, the aperture of through-hole i be impeller maximum gauge 1.01~
1.03 times, aperture is too small, excessively high to matching requirements, influences assembly efficiency, and aperture is excessive, i.e. through-hole i and impeller clearance are excessive, shadow
Ringing efficiency of imbibition, the impeller includes preoral loop (be located at suction eye), rear choma (being located at wheel backface) and connection screw thread,
For impeller by connection screw thread and driving axis connection, drive shaft passes through from pump cover and is cased with sliding bearing, and sliding bearing, which is located at, to be driven
Between moving axis and pump cover, rear choma is annular projection q2, and height is greater than the height of connection screw thread evagination, opens on back shroud of impeller
The balance hole for thering is connection preoral loop to surround space and deutostoma collar into space, annular projection q1 it is mutually nested with annular projection q2 and
Therebetween it is equipped with wear-resistant seal ring, prosopyle loop section is inserted in connecting tube and is equipped with wear-resistant seal ring therebetween.
Low damage high-efficiency self-suction centrifugal pump as described above, low damage high-efficiency self-suction centrifugal pump further include air-water separation chamber with
Mechanically-sealing apparatus, mechanically-sealing apparatus is mainly by seal base, sealing gland, mechanical sealing linkage ring and mechanical sealing static ring group
At seal base is hollow columnar structures, and both ends extend radially outwards cyclic P1 and P2 respectively, and sealing gland is round table-like knot
Structure, the biggish one end of area extend radially outwards cyclic P3, flushing through-hole are provided on sealing gland；
Ring P1 is fixedly connected with the support frame being fixed at the top of air-water separation chamber, and ring P2 is bonded with ring P3 and the two passes through spiral shell
Bolt is fixed, drive shaft pass through seal base and sealing gland, mechanical sealing linkage ring set on the driving shaft and be located at seal base and
In the space that sealing gland surrounds, it is fixed in sealing gland with the mutually matched mechanical sealing static ring of mechanical sealing linkage ring.
Low damage high-efficiency self-suction centrifugal pump as described above, low damage high-efficiency self-suction centrifugal pump further includes reservoir chamber, air water
Separation chamber is connected to reservoir chamber by return line, and return line is equipped with solenoid valve；Solenoid valve and signal control device and pressure
Force sensor is sequentially connected, and pressure sensor device is used to acquire the pressure of air-water separation chamber inner cavity, and signal control device is used for
It receives the pressure signal that pressure sensor device is sent and sends current signal to solenoid valve.
Low damage high-efficiency self-suction centrifugal pump as described above, solenoid valve is opened when self priming centrifugal pump starts, solenoid valve
Shut-in time is 30s~1min bigger than the self-priming time of self priming centrifugal pump.Since the pressure of self priming pump air-water separation chamber is opened just
It is fluctuated due to there is the presence of gas that dynamic change is presented when beginning to rise, it is ad hoc in order to empty the gas of air-water separation chamber
Return line and solenoid valve late release are set, delay time, too short gas was not clean, on too long power consumption height and influence when water
Between.
Low damage high-efficiency self-suction centrifugal pump as described above, the signal control device are signal control cabinet, the pressure
Sensing device is pressure sensor, and the signal control device is mounted on the support frame outside self priming centrifugal pump, the pressure
Sensing device is mounted in gas-water separation chamber interior walls；The protection scope of the signal control device and pressure sensor device is not limited to
This, can also be other elements, as long as being able to achieve corresponding function, specific location is indefinite, can acquire in gas-water separation room
The pressure of chamber.
The return line is mainly by two groups of return pipes, elbow and the pipe fitting group positioned at solenoid valve two sides and sequential connection
At pipe fitting is threadedly coupled with solenoid valve, and two return pipes are welded to connect with air-water separation chamber and reservoir chamber respectively.Pipe fitting with
The connection type of solenoid valve, two return pipes respectively between air-water separation chamber and reservoir chamber is without being limited thereto, other to can be realized
The mode being fixedly connected is suitable for the present invention.
Low damage high-efficiency self-suction centrifugal pump as described above, the reservoir chamber is interior to be equipped with suction chamber, and suction chamber is hollow knot
Structure is surrounded by upper plate, lower plate and with the orthogonal side plate of the two, and the bottom of suction chamber is provided with return port；
It is provided with hole h on upper plate and upwardly extends to form outlet pipe along hole wall, outlet pipe is connect with impeller inlet, and side plate is horizontal
The edge line in section is comma shape, is linked in sequence and is formed by curve a, helix b, curve c and line d, curve a and curve c are flat
It slides curve and is seamlessly transitted between helix b, the side plate where line d is provided with hole k, and hole k is connect with water inlet pipe；The shape of suction chamber
Shape is mainly related to the shape of side plate, and the edge line of upper plate and lower plate can be identical as the edge line of side plate cross section,
It can not be identical；
The intersection point of helix b and curve a and curve c are respectively m and n, and the center of circle o of m, n and hole h are located along the same line, m
With at a distance from o be less than n at a distance from o, be R with the point on helix b and the line segment length between o, on helix b point with
The angle of the line segment between line segment and m and o between o is θ, R=D0(w+v θ/g), D0For impeller inlet diameter, w=0.6~
0.7, v=0.06~0.1, g=1 °.Curve determines flow section according to every pump discharge, lift and revolving speed without fixed equation
Area, width and radial height can all randomly choose, and generally first take radial height, determine width further according to flow section area,
Relationship between flow section area and pump discharge and cross-sectional flow is：
S=Q/vs；
In formula, S is flow section area, unit m2, Q is pump discharge, unit m3/ s, vsIt is single for flow section flow velocity
Position is m/s, takes (v0+v1)/2, v0For pump inlet flow velocity, v1For impeller inlet flow velocity.
For existing self-priming pump configuration without suction chamber, only reservoir chamber, structure is a circular cylinder body, liquid stream from priming reservoir pass through into
Mouth bend pipe, diffuses in cylinder, flow stream velocity sharply declines, and in suction eye, flow velocity increased dramatically again, fluid reservoir stream suddenly
Speed is substantially zeroed, is amplification suddenly in the entire waterpower cross-section of river, rear sudden contraction again, flow stream velocity vector size realizes prominent
Change process, flow direction are irregular arrangement, and this adds increased the losses of pump inlet section, not only influence pump overall operation efficiency,
Also there is abated effect to anti-cavitation performance, reduces the maximum suction lift of pump.Low damage high efficiency self suction pump type centrifugation of the invention
Pump, increases suction chamber in reservoir chamber, and after being designed as semispiral type structure, ensure that entire flow section area uniformly becomes
Change, to guarantee the even variation of flow velocity from small to large, flow direction also achieves even variation, effectively reduces fluid flow
Local diffusion and impact loss improve the way, increasing pump anti-cavitation surplus, suct to also further increase pump maximum
Highly, the maximum suction lift of the low damage high-efficiency self-suction centrifugal pump of the application is up to 0.5~1.0m.
Low damage high-efficiency self-suction centrifugal pump as described above, the suction chamber is interior to be equipped with the point water plate that cross section is V-arrangement, point
The height of water plate is identical as suction chamber, and point water plate is seamlessly transitted with the side plate where the side plate and curve a where helix b respectively
Connection, liquid stream are roughly divided into two strands after entering suction chamber, one is along the side plate flowing where curve c and helix b, another burst of edge
Side plate flowing where curve a, generates impact in the side plate intersection where the side plate and curve a where helix b and forms whirlpool
Whirlpool influences the efficiency of self priming centrifugal pump, can effectively prevent liquid flow impact after point water plate is arranged, be conducive to improve efficiency, described
The wall thickness of point water plate is identical as side plate, same wall thickness, and casting cooling velocity is identical, it is not easy to casting flaw occurs, weldment can
Welding deformation is reduced, while also can guarantee intensity requirement.
Low damage high-efficiency self-suction centrifugal pump as described above, the reservoir chamber are cylinder-like structure, with suction chamber and into
Water pipe welding, reservoir chamber size are designed according to pump condition；The line d is camber line, and the side plate where line d is reservoir chamber side wall；Institute
The radius of curvature for stating curve a is less than curve c, and the side plate where curve a is equivalent to temperature of inner ring during rotation, and the side plate where curve c is suitable
In rotation outer ring, the radius of curvature of curve a is more advantageous to less than curve c meets uniform motion's requirement；The water inlet pipe is curved
Pipe, each position cross-sectional area is identical and is equal to the cross-sectional area of hole k；It is straight that the water outlet bore is more than or equal to impeller inlet
Diameter, this is because the flow velocity from outlet pipe to impeller inlet, which wants gradual, is unable to the sudden turn of events, to reduce hydraulic loss, outlet pipe is slightly larger than
Impeller inlet diameter may make outlet pipe flow velocity to be less than impeller inlet flow velocity, and the small corresponding pressure of flow velocity can be big, can reduce liquid in this way
Stream vaporization, is conducive to the anti-cavitation performance of elevator pump；The hole h and hole k is circular hole or square hole, and hole h and hole k shape are not limited to
This, can be according to actual use situation adjustment；The return port is located on lower plate.
Invention mechanism：
For the present invention by pumping chamber and air-water separation chamber independent design, pumping chamber cross section is integrally in figure six, circular segment
Flow section area be gradually increased along pumping chamber export direction, the entire cross-section of river is pears type, and no corner angle meet stream without vortex
Body flowing law, reduces the impact loss and divergence loss of impeller outlet to pumping chamber import, and pumping chamber liquid stream need to reach certain
Flow velocity can just enter air-water separation chamber, abundant conversion of the liquid flowing energy to pressure energy be realized in entire pumping chamber, through over-voltage water
Room is being discharged to air-water separation chamber after flow stream velocity can be fully converted into pressure energy, guarantees that pumping chamber flows into gas-water separation ventricular tachycardia
Degree is equal with outflow air-water separation chamber speed, accomplishes that hydraulic loss minimizes as far as possible, the efficiency of pump maximizes, pumping chamber discharge liquor
It flows direction and air-water separation chamber cylinder circumference is tangent, reduce impact loss and divergence loss to the greatest extent, improve the efficiency of pump.
In addition, to forget angle tangent for impeller outlet fluid flow angle and screw type pumping chamber, so that the swiftly flowing liquid stream of impeller outlet is without impact
Into pumping chamber, hydraulic loss is further reduced.
The present invention draws return line design using outer, and installs solenoid valve, and solenoid valve and signal control device and pressure pass
Induction device is sequentially connected, and pressure sensor device acquires air-water separation chamber chamber pressure, is passed to signal control device, is worked as pump startup
When, solenoid valve is opened, and pump reflux realizes self-priming process, is set electronic valve closing time and is greater than pump self-priming time, and adds a Dingan County
Full surplus pumps after operating normally, the pressure when the pressure of pressure sensor device acquisition is more than or equal to rated lift, signal control
Device receives the pressure signal that pressure sensor device is sent, and provides a 4mA current signal, this signal is passed to electromagnetism
Valve, solenoid valve are begun to shut off, and reflux course is closed, and are flowed back unaffected；When the pressure of pressure sensor device acquisition is less than design
When lift, signal control device gives a 20mA current signal, and solenoid valve starts to open, and whole process can be automatically controled reflux,
To improve the way, self-priming performance and volumetric efficiency.
In addition, suction chamber mainly rises to impeller inlet liquid stream guiding function, liquid stream is allowed to enter impeller without impact, this will be right
Liquid stream into impeller is dredged drainage, and flow velocity size cannot mutate on each overflow section, and flow direction can not
It mutates, because the process reduced after amplification suddenly is all with energy loss, also referred to as waterpower local losses, waterpower is locally damaged
Lose big, liquid stream enters that impeller pressure is low, and when flow stream pressure is lower than pressure for vaporization, cavitation can occur for impeller, while can make to pump out
Mouth pressure reduction, the efficiency of pump reduce.For this problem, the present invention devises completely new suction chamber, allows fluid flow through water inlet pipe and arrives
Suction chamber, flow velocity size are held essentially constant, and each area of section is equal, reduce hydraulic loss, improve the efficiency of pump and cavitation-resistance
Energy.
Hydraulic loss calculation formula is as follows：
H=ζ vs^2/(2g)；
In formula, h indicates loss pressure, unit m；ζ is loss coefficient, is that constant and area of section and directional velocity become
Change it is related, change it is bigger, loss coefficient is bigger；vsFor flow velocity, unit m/s, g are acceleration of gravity, unit m/s2, " ^ " table
Show square.
Found out by above formula, total hydraulic loss and loss coefficient and flow velocity are directly related, to improve the efficiency of pump, it is necessary to reduce
The value of both this.
Suction chamber outer profile bus of the invention is 2 sections of 360 ° of directions point, and only 180 ° use helix structure, it is assumed that leaf
Wheel inlet velocity is v0, on 180 ° of sections, flow velocity is (1/2) v for that0, suction chamber height is certain, it may be determined that 180 ° of section radial directions
Size is 0 simultaneously for 0 ° of area of section, and no liquid stream flows through, and identical in 0 ° to 180 ° each cross sectional flow rate is all (1/2) v0, lead to
The even variation of over-angle, overflow section area angularly different also uniform transitions, suction chamber height is constant, also just realizes radial
Variation of uniform size.By 360 ° of impeller inlet cyclotomy circumferential direction, each angle inflow should uniformly, and liquid stream is in suction chamber along wall surface
Spiral motion, wherein having 180 ° using helix structure, the liquid flow flowed through on 180 ° of sections should be evenly distributed in
On 0 °~180 ° sections, 180 ° of areas of section are set to s8, by angle bisecting be 8 parts, 22.5 ° every part, area of section s1、
s2……s8；s1=1/8s8；s2=2/8s8..., and so on；Also and so on, this guarantees each section for the flow in each section
Surface current speed is equal, and since helix structure mean curvature radius is small, has guiding role to fluid flow, it is not easy to form flowing whirlpool
Whirlpool ensure that section liquid stream flow direction even variation, while fluid flow, so hydraulic efficiency is high, is improved without hydraulic blow
Pump whole efficiency.
Beneficial effect：
(1) low damage high-efficiency self-suction centrifugal pump of the invention, using full runner the Hydraulic Design, operational efficiency is high, energy conservation drop
Consumption；
(2) low damage high-efficiency self-suction centrifugal pump of the invention, using solenoid valve is automatically controlled, self-priming performance is good, when self-priming
Between it is short, suction lift is high；
(3) low damage high-efficiency self-suction centrifugal pump of the invention, applied widely using mechanical seal, sealed reliable；
(4) low damage high-efficiency self-suction centrifugal pump of the invention, axial force balance and use sliding bearing limit, and pump operation is flat
Surely, good reliability；
(5) low damage high-efficiency self-suction centrifugal pump of the invention, using wear-resistant seal ring, pump service life is good, maintenance cost
It is low；
(6) low damage high-efficiency self-suction centrifugal pump of the invention, is mounted on ground, and use scope is wide, and repair and maintenance is convenient；
(7) low damage high-efficiency self-suction centrifugal pump of the invention only needs starting for the first time to pour water, and afterwards without pouring water, grasps
Make simple；
(8) low damage high-efficiency self-suction centrifugal pump of the invention, hydraulic efficiency is high, takes into account efficiency, self-priming performance, hydraulic performance
And operational reliability, great application prospect.
Detailed description of the invention
Fig. 1 is the overall structure diagram of low damage high-efficiency self-suction centrifugal pump of the invention；
Fig. 2 and Fig. 3 be respectively the pumping chamber pump housing of low damage high-efficiency self-suction centrifugal pump of the invention main view sectional view and
Top view；
Fig. 4 is the structural schematic diagram of self priming centrifugal pump pumping chamber of the present invention cross section
Fig. 5 is the schematic diagram of multiple flow sections for crossing center of circle E in T2 sections in Fig. 4；(mistake in the selection of flow section such as figure
Shown in the dotted line of center of circle E) (each flow section only shows half in Fig. 5)
Fig. 6 is the schematic diagram of multiple flow sections in T1 sections in Fig. 4；
Fig. 7 is blade wheel structure schematic diagram of the invention；
Fig. 8 is mechanically-sealing apparatus structural schematic diagram of the invention；
Fig. 9 is return line structural schematic diagram of the invention；
Figure 10 is the fluid reservoir and suction chamber structural schematic diagram of low damage high-efficiency self-suction centrifugal pump of the invention.
Figure 11 is the fluid reservoir of low damage high-efficiency self-suction centrifugal pump of the invention and the main view of suction chamber；
Figure 12 is the fluid reservoir and suction chamber cross-sectional view of low damage high-efficiency self-suction centrifugal pump of the invention；
Wherein, 1- water inlet pipe, 2- reservoir chamber, 3- suction chamber, 4- outlet pipe, 5- point water plate, 6- return pipe a, 7- elbow a,
8- pipe fitting a, 9- solenoid valve, 10- pipe fitting b, 11- elbow b, 12- return pipe b, 13- screw, 14- scrape water and forget, and 15- reinforces
Gusset, 16- bottom plate, the 17- pumping chamber pump housing, 18- preoral loop, 19- balance hole, choma after 20-, 21- connection screw thread, 22- bolt,
23- sealing gland, 24- mechanical sealing static ring, 25- drive shaft, 26- rinse through-hole, 27- seal base, 28- nut, 29- machinery
Moving sealing ring, 30- through-hole i, 31- through-hole j, 32- connecting tube, 33- air-water separation chamber, 34- support frame, 35- mechanically-sealing apparatus,
36- pump cover, 37- sliding bearing, 38- return line, 39- impeller, 40- wear-resistant seal ring.
Specific embodiment
The invention will be further elucidated with reference to specific embodiments.It should be understood that these embodiments are merely to illustrate this hair
It is bright rather than limit the scope of the invention.In addition, it should also be understood that, after reading the content taught by the present invention, art technology
Personnel can make various changes or modifications the present invention, and such equivalent forms equally fall within the application the appended claims and limited
Fixed range.
Low damage high-efficiency self-suction centrifugal pump, overall structure diagram as shown in Figure 1, mainly by water inlet pipe 1, reservoir chamber 2,
Suction chamber 3, the pumping chamber pump housing 17, air-water separation chamber 33, impeller 39, return line 38 and mechanically-sealing apparatus 35 form.
Pumping chamber is the internal chamber of the pumping chamber pump housing 17, and structure is as shown in Fig. 2, pumping chamber cross section is integrally in " 6 "
Font, outer ledge line are made of helix A, curve B and line C, and line C connect with helix A and curve B simultaneously and is pumping chamber
The intersection of exit face and cross section, inside edge line are circle D, the intersection point Y distance circle D of helix A and curve B on outer ledge line
Center of circle E recently and distance is greater than the radius of circle D, line C is straight line, and point Y also can be equal to the radius of round D at a distance from the E of the center of circle；
There is a point X in helix A on the line segment opposite with curve B, while the flow section for crossing point X and intersection point Y will press water
Room is divided into the T1 section of the strip being connected smoothly and T2 section cricoid, and the angle of flare of T1 sections of runners is not more than more in 12 °, T1 sections
The schematic diagram of a flow section is as shown in fig. 6, have a point S near point X on helix A in T2 sections, between point Y and point S
Helix intersection flow section it is coplanar with center of circle E, be class isosceles trapezoid as shown in Figure 5 and area is gradually increased,
The flow section area for crossing S point is maximum, and the main distinction of class isosceles trapezoid and isosceles trapezoid is side and bottom is smoothed
It crosses connection and bottom is smoothed curve, the upper bottom and bottom of class isosceles trapezoid are respectively that T2 sections of most inner sides and outermost and overcurrent are disconnected
The upper bottom length of the intersection in face, all class isosceles trapezoids is identical.
The pumping chamber pump housing 17 is as shown in Figures 3 and 4, between being equipped between filling intersection point Y and circle D at intersection point Y in the pumping chamber pump housing
The plate of gap scrapes water and forgets 14, and plate scrapes the tangential direction that the arranged direction that water is forgotten is helix A intersection point Y location, scrapes water and cuts
House 14 is fixed on the pump housing by screw 13；Surround through-hole U on the inside of T2 sections of corresponding pumping chamber pump housing sections, through-hole U mainly by
Coaxial cylindrical hole i 30 and truncated cone-shaped through-hole j31 is formed by connecting and the aperture phase of junction through-hole i 30 and through-hole j 31
It is connected to Deng, through-hole i with T2 sections of runners and is fixed with pump cover 36 far from the end through-hole j, pump cover 36 is equipped with annular projection q1；
The pumping chamber pump housing 17 is fixed on bottom plate 16 by connecting tube 32 and stiffener plate 15, and bottom plate is annular in shape, bottom plate
Ring inner via hole is connected to through-hole U by round table-like connecting tube, 15 circle distribution of stiffener plate on bottom plate 16 and simultaneously with connection
Pipe 32, bottom plate 16 and the pumping chamber pump housing 17 connect.
Impeller 39 is disposed in through-hole i 30, and the two is coaxial, the aperture of through-hole i 30 is 39 maximum gauge of impeller
1.01~1.03 times；
Impeller 39 is as shown in fig. 7, comprises preoral loop 18, rear choma 20 and connection screw thread 21, impeller 39 pass through connection screw thread
21 connect with drive shaft 25, and drive shaft 25 passes through from pump cover 36 and be cased with sliding bearing 37, and sliding bearing 37 is located at drive shaft
Between 25 and pump cover 36, rear choma 20 is annular projection q2, and height is greater than the height of connection screw thread evagination, on back shroud of impeller
It is provided with connection preoral loop and surrounds space and deutostoma collar into the balance hole 19 in space, annular projection q1 and annular projection q2 are mutually embedding
Wear-resistant seal ring 10 is covered and is equipped with therebetween, 18 part of preoral loop is inserted in connecting tube 32 and is equipped with wear-resistant seal therebetween
Ring 40.
Mechanically-sealing apparatus 35 is as shown in figure 8, mainly by seal base 27, sealing gland 23,29 and of mechanical sealing linkage ring
Mechanical sealing static ring 24 forms, and seal base 27 is hollow columnar structures, and both ends extend radially outwards cyclic P1 and P2 respectively,
Sealing gland 23 is round-like structure, and the biggish one end of area extends radially outwards cyclic P3, and it is logical that flushing is provided on sealing gland
Hole 26；
Ring P1 is fixedly connected with the support frame 34 being fixed at the top of air-water separation chamber, and ring P2 is bonded with ring P3 and the two passes through
Bolt 22 and nut 28 are fixed, and drive shaft 25 passes through seal base 27 and sealing gland 23, and 29 sets of mechanical sealing linkage ring are driving
On axis 25 and it is located in the space that seal base 27 and sealing gland 23 surround, with the mutually matched machinery of mechanical sealing linkage ring 29
Stationary seal ring 24 is fixed in sealing gland 23.
Return line 38 is connected to air-water separation chamber and reservoir chamber, and return line is equipped with solenoid valve；Solenoid valve and signal control
Cabinet and pressure sensor processed are sequentially connected, and pressure sensor is mounted in gas-water separation chamber interior walls, for acquiring air-water separation chamber
The pressure of inner cavity, signal control cabinet are mounted on the support frame 34 outside self priming centrifugal pump, for receiving pressure sensor device hair
The pressure signal that send simultaneously sends current signal to solenoid valve；Solenoid valve is opened when self priming centrifugal pump starts, the closing of solenoid valve
Time is 30s~1min bigger than the self-priming time of self priming centrifugal pump.
Return line structural schematic diagram as shown in figure 9, return line mainly by being located at the sequential connection of solenoid valve 9 side
Return pipe a 6, elbow a 7 and pipe fitting a 8, and the pipe fitting b 10 positioned at 9 other side of solenoid valve, elbow b 11 and reflux
Pipe b 12 is formed, and pipe fitting a 8 and pipe fitting b 10 be threadedly coupled with solenoid valve 9, return pipe a 6 and return pipe b 12 respectively with
Air-water separation chamber and reservoir chamber are welded to connect.
Suction chamber is equipped in reservoir chamber, structural schematic diagram is as shown in FIG. 10 and 11, and reservoir chamber 2 is cylinder-like structure, water suction
Room 3 is hollow structure, surrounds by upper plate, lower plate and with the orthogonal side plate of the two, is provided on suction chamber lower plate
Return port.It is provided with hole h on upper plate and upwardly extends to form outlet pipe 4 along hole wall, outlet pipe 4 is connect with impeller inlet, water outlet
4 internal diameter of pipe is more than or equal to impeller inlet diameter.
The edge line of side plate cross section is comma shape, as shown in figure 12, by curve a, helix b, curve c and line d sequence
Connection is formed, and curve a and curve c are smoothed curve and seamlessly transit between helix b that the radius of curvature of curve a is less than song
Line c, the side plate where line d are provided with hole k, and hole k is connect with water inlet pipe 1, and water inlet pipe 1 is bend pipe, and each position cross-sectional area is identical
And it is equal to the cross-sectional area of hole k.Hole h and hole k is circular hole or square hole, and line d is camber line, and the side plate where line d is the side of reservoir chamber 2
Wall.Reservoir chamber 2 and suction chamber 3 and water inlet pipe 1 weld.
The intersection point of helix b and curve a and curve c are respectively m and n, and the center of circle o of m, n and hole h are located along the same line, m
With at a distance from o be less than n at a distance from o, be R with the point on helix b and the line segment length between o, on helix b point with
The angle of the line segment between line segment and m and o between o is θ, R=D0(w+v θ/g), D0For impeller inlet diameter, w=0.6~
0.7, v=0.06~0.1, g=1 °.
The point water plate 5 that cross section is V-arrangement is equipped in suction chamber 3, the height of point water plate 5 is identical as suction chamber, point water plate
Wall thickness is identical as side plate, and point water plate 5 is connected smoothly with the side plate where the side plate and curve a where helix b respectively.
The hydraulic efficiency of low damage high-efficiency self-suction centrifugal pump of the invention is 88~97%.
Claims (10)
1. low damage high-efficiency self-suction centrifugal pump, including pumping chamber, it is characterized in that：Pumping chamber cross section is integrally in figure six, outside
Edge line is made of helix A, curve B and line C, line C connect simultaneously with helix A and curve B and for pumping chamber exit face and
The intersection of cross section, inside edge line are circle D, the center of circle E of the intersection point Y distance circle D of helix A and curve B on outer ledge line
Recently and apart from the radius for being more than or equal to circle D；
There is a point X in helix A on the line segment opposite with curve B, while crossing the flow section of point X and intersection point Y for pumping chamber minute
For the T1 section of the strip being connected smoothly and T2 section cricoid, being leaned near point X on the helix A in T2 sections has a point S, with point
The flow section of helix intersection between Y and point S is coplanar with center of circle E, is class isosceles trapezoid and area is gradually increased, mistake
The flow section area of S point is maximum, and the main distinction of class isosceles trapezoid and isosceles trapezoid is side and bottom for smooth transition
Connection, the upper bottom and bottom of class isosceles trapezoid are respectively the intersection of T2 sections of most inner sides and outermost and flow section, all classes
The upper bottom length of isosceles trapezoid is identical；
The hydraulic efficiency of low damage high-efficiency self-suction centrifugal pump is 88~97%.
2. low damage high-efficiency self-suction centrifugal pump according to claim 1, which is characterized in that the line C is straight line, the class
It is smoothed curve that the difference of isosceles trapezoid and isosceles trapezoid, which also resides in bottom, and the angle of flare of T1 sections of runners is not more than 12 °.
3. low damage high-efficiency self-suction centrifugal pump according to claim 2, which is characterized in that the pumping chamber is pumping chamber pump
The internal chamber of body；When point Y is greater than the radius of circle D at a distance from the E of the center of circle, filling is equipped at intersection point Y in the pumping chamber pump housing and is handed over
The plate in gap is scraped water and is forgotten between point Y and circle D；Through-hole U, through-hole U master are surrounded on the inside of T2 sections of corresponding pumping chamber pump housing sections
It to be formed by connecting by coaxial cylindrical hole i and truncated cone-shaped through-hole j and the aperture of junction through-hole i and through-hole j is equal, through-hole
I is connected to T2 sections of runners and is fixed with pump cover far from the end through-hole j, and pump cover is equipped with annular projection q1；
The pumping chamber pump housing is fixed in annular base plate by connecting tube and stiffener plate, the ring inner via hole of annular base plate and logical
Hole U is connected to by round table-like connecting tube, stiffener plate circle distribution in annular base plate and simultaneously with connecting tube, annular base plate and
The connection of the pumping chamber pump housing；
It being disposed with impeller in the through-hole i, and the two is coaxial, the aperture of through-hole i is 1.01~1.03 times of impeller maximum gauge,
The impeller includes preoral loop, rear choma and connection screw thread, and impeller is by connection screw thread and driving axis connection, and drive shaft is from pump cover
In pass through and be cased with sliding bearing, sliding bearing is between drive shaft and pump cover, and rear choma is annular projection q2, and height is big
Space and deutostoma collar are surrounded into the balance in space in being provided with connection preoral loop in the height of connection screw thread evagination, back shroud of impeller
Hole, annular projection q1 is mutually nested with annular projection q2 and is equipped with wear-resistant seal ring therebetween, and prosopyle loop section is inserted in connection
In pipe and therebetween equipped with wear-resistant seal ring.
4. low damage high-efficiency self-suction centrifugal pump according to claim 3, which is characterized in that low damage high-efficiency self-suction centrifugal pump
It further include air-water separation chamber and mechanically-sealing apparatus, mechanically-sealing apparatus is mainly moved by seal base, sealing gland, mechanical seal
Ring and mechanical sealing static ring composition, seal base is hollow columnar structures, and both ends extend radially outwards cyclic P1 and P2 respectively,
Sealing gland is round-like structure, and the biggish one end of area extends radially outwards cyclic P3, flushing through-hole is provided on sealing gland；
Ring P1 is fixedly connected with the support frame being fixed at the top of air-water separation chamber, and ring P2 is bonded with ring P3 and the two is solid by bolt
Fixed, drive shaft passes through seal base and sealing gland, and mechanical sealing linkage ring set is on the driving shaft and positioned at seal base and sealing
In the space that gland surrounds, mechanical sealing static ring is fixed in sealing gland.
5. low damage high-efficiency self-suction centrifugal pump according to claim 4, which is characterized in that low damage high-efficiency self-suction centrifugal pump
It further include reservoir chamber, air-water separation chamber is connected to reservoir chamber by return line, and return line is equipped with solenoid valve；Solenoid valve with
Signal control device and pressure sensor device are sequentially connected, and pressure sensor device is used to acquire the pressure of air-water separation chamber inner cavity,
Signal control device is used to receive the pressure signal of pressure sensor device transmission and sends current signal to solenoid valve.
6. low damage high-efficiency self-suction centrifugal pump according to claim 5, which is characterized in that electricity when self priming centrifugal pump starts
Magnet valve is opened, and the shut-in time of solenoid valve is 30s~1min bigger than the self-priming time of self priming centrifugal pump.
7. low damage high-efficiency self-suction centrifugal pump according to claim 6, which is characterized in that the signal control device is letter
Number control cabinet, the pressure sensor device are pressure sensor, and the signal control device is mounted on outside self priming centrifugal pump
On support frame, the pressure sensor device is mounted in gas-water separation chamber interior walls；The return line is mainly by being located at solenoid valve
Two groups of return pipes of two sides and sequential connection, elbow and pipe fitting composition, pipe fitting are threadedly coupled with solenoid valve, two return pipes
It is welded to connect respectively with air-water separation chamber and reservoir chamber.
8. low damage high-efficiency self-suction centrifugal pump according to claim 7, which is characterized in that be equipped with water suction in the reservoir chamber
Room, suction chamber are hollow structure, are surrounded by upper plate, lower plate and with the orthogonal side plate of the two, the bottom of suction chamber
It is provided with return port；
It is provided with hole h on upper plate and upwardly extends to form outlet pipe along hole wall, outlet pipe is connect with impeller inlet, side plate cross section
Edge line be comma shape, be linked in sequence and formed by curve a, helix b, curve c and line d, curve a and curve c are smooth bent
It line and is seamlessly transitted between helix b, the side plate where line d is provided with hole k, and hole k is connect with water inlet pipe；
The intersection point of helix b and curve a and curve c are respectively m and n, and the center of circle o of m, n and hole h are located along the same line, m and o
Distance be less than n at a distance from o, be R with the point on helix b and the line segment length between o, on helix b point and o it
Between line segment and m and o between the angle of line segment be θ, R=D0(w+v θ/g), D0For impeller inlet diameter, w=0.6~0.7, v
=0.06~0.1, g=1 °.
9. low damage high-efficiency self-suction centrifugal pump according to claim 8, which is characterized in that be equipped in the suction chamber transversal
Face be V-arrangement point water plate, the height of point water plate is identical as suction chamber, point water plate respectively with the side plate and curve a where helix b
The side plate at place is connected smoothly, and the wall thickness of the point water plate is identical as side plate.
10. low damage high-efficiency self-suction centrifugal pump according to claim 9, which is characterized in that the reservoir chamber is cylindrical shape
Structure is welded with suction chamber and water inlet pipe；The line d is camber line, and the side plate where line d is reservoir chamber side wall；The curve a
Radius of curvature be less than curve c；The water inlet pipe is bend pipe, and each position cross-sectional area is identical and is equal to the cross-sectional area of hole k；
The water outlet bore is more than or equal to impeller inlet diameter；The hole h and hole k is circular hole or square hole；Under the return port is located at
On bottom plate.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810775515.7A CN108843579A (en) | 2018-07-16 | 2018-07-16 | Low damage high-efficiency self-suction centrifugal pump |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810775515.7A CN108843579A (en) | 2018-07-16 | 2018-07-16 | Low damage high-efficiency self-suction centrifugal pump |
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| Publication Number | Publication Date |
|---|---|
| CN108843579A true CN108843579A (en) | 2018-11-20 |
Family
ID=64197400
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201810775515.7A Withdrawn CN108843579A (en) | 2018-07-16 | 2018-07-16 | Low damage high-efficiency self-suction centrifugal pump |
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| Country | Link |
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| CN (1) | CN108843579A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110657099A (en) * | 2019-09-29 | 2020-01-07 | 湖州瑞晨环保科技有限公司 | Single-stage double-suction horizontal self-priming pump |
| CN113242761A (en) * | 2018-12-21 | 2021-08-10 | 爱尔兰国立高威大学 | Vortex generator device |
-
2018
- 2018-07-16 CN CN201810775515.7A patent/CN108843579A/en not_active Withdrawn
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113242761A (en) * | 2018-12-21 | 2021-08-10 | 爱尔兰国立高威大学 | Vortex generator device |
| CN113242761B (en) * | 2018-12-21 | 2023-10-27 | 爱尔兰国立高威大学 | Vortex generator device |
| CN110657099A (en) * | 2019-09-29 | 2020-01-07 | 湖州瑞晨环保科技有限公司 | Single-stage double-suction horizontal self-priming pump |
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| CB02 | Change of applicant information |
Address after: 201800 2, 1501, 1519, 1533, Chengliu Middle Road, Jiading District, Shanghai. Applicant after: SHANGHAI RICHEN ENVIRONMENTAL PROTECTION TECHNOLOGY Co.,Ltd. Address before: 201800 2, 1501, 1519, 1533, Chengliu Middle Road, Jiading District, Shanghai. Applicant before: SHANGHAI RICHEN CO.,LTD. |
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Application publication date: 20181120 |