CN86104866A - Diaphragm pump - Google Patents
Diaphragm pump Download PDFInfo
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- CN86104866A CN86104866A CN 86104866 CN86104866A CN86104866A CN 86104866 A CN86104866 A CN 86104866A CN 86104866 CN86104866 CN 86104866 CN 86104866 A CN86104866 A CN 86104866A CN 86104866 A CN86104866 A CN 86104866A
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- diaphragm pump
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Abstract
The diaphragm pump that is used for the transportation of granule materials pipe long-distance.Nonmetal barrier film is set in the isolation tank of this pump, clear water and slurry are isolated fully, make slurry not enter the pump housing.Thereby high-lift (H≤1990 meter water columns), big flow (Q≤3000 meter of diaphragm pump have been realized
3/ hour), high concentration (β≤60%), high efficiency η 70～80%), the long-life.This pump is applicable to transportation concentrate, mine tailing, bauxite, lime-ash, coal slurry and beans etc.The particle diameter of transported material can reach 1/5th of transportation caliber.Use this pump can reduce energy consumption, capital investment and maintenance expenses.
Description
The invention belongs to the technical field of solid material pipelines hydraulic-transporting device.
Solid granular material (concentrate, mine tailing, bauxite, coal, lime-ash etc.) mixes with water and is solid-liquid two-phase flow, utilizes the pipe long-distance transportation to emerge in recent years, is considered to a kind of and the competitive material means of transportation of railway transport, by being paid attention to various countries.
At present, as the material transport pump, existing centrifugal pump, reciprocating pump, oil isolation pump and water isolation pump etc.
Centrifugal pump (sand pump, grey dredge pump, fertile graceful pump etc.) lift low (lift is less than the 90m water column) only is suitable for material short distance transportation.Level transportation iron tailings, pumping plant apart from be 2～3 kilometers/stand, than long-distance transportation, just need the multi stage pumping station series connection, the mine tailing that has at present transports and has been connected in series to nine grades of pumping plants.Because slurry directly enters quick abrasions such as the pump housing, impeller, backplate, make the life-span of pump short, maintenance expenses is high, efficient is low, these problems will improve and aggravate along with slurry concentration.
Reciprocating pump (plunger pump, reciprocating pump, diaphragm pump) flow is little, and peak rate of flow is 200 cubic metres/hour usually.This pump structure complexity, maintenance difficult.Because slurry enters the diaphragm pump pump housing, enters plunger pump, reciprocating pump pumping cylinder, makes guide pin bushing, piston rod, check valve etc. become easily damaged parts, short and replacing difficulty of life-span, maintenance expenses height.
Oil isolation pump is called the Ma Ersi pump again.This pump is a kind of distortion of reciprocating pump, and it separates oil and ore pulp by isolation tank, prevents that slurry from entering pumping cylinder, has improved the life-span of pump.But this pump, also exists the suspended matter in the slurry to sneak into the phenomenon that enters pumping cylinder in the oil, thereby causes oil consumption so existing fluid runs off owing to be to take oil directly to contact with slurry, reduces the working life of pump again.Because oil is reliable inadequately with the level control that slurry directly contacts, often cause a large amount of loss of fluid, befouling environment again.And flow is little, is unsuitable for big flow slurry transportation.
Water isolation pump is called hydraulic elevator again.This pump, water and slurry are isolated by ball float, because ball float and tank skin are gapped, the clear water leakage are arranged, so clear water can not closed-circuit; Also often there is the slurry of mixing phenomenon to occur, so need establish clear water reserviors.In order to prevent that ball float from blocking, this pump can not transport particle diameter greater than 2 millimeters solid material.This pump need have complicated detection and control system for the position of controlling ball float and the speed of related movement of regulating three ball floats, has increased the complexity and the expense of equipment.
Purpose of the present invention just provides a kind of diaphragm pump, will drive liquid and slurry is isolated fully, solves the problem that above a few class pumps exist, and realizes high-lift, high concentration, flow, long-life pipeline transport greatly; Reduce energy consumption, capital investment and maintenance expenses; Reduce operator, attendant; Avoid environmental pollution.
Narrate composition of the present invention and working principle below in conjunction with accompanying drawing.
Figure one is the diaphragm pump system diagram.
Figure two is the structural drawing of the isolation tank of diaphragm pump.
The present invention is achieved in that such as figure one, diaphragm pump by drive system, sealing chamber group, Pulp feeding system and composition of the control system. Drive system comprises one (or several) clarified water pump (4) and one group control gate valve A, B, C, D, E, F; The sealing chamber group is made up of three (or four) sealing chambers (2), and nonmetal barrier film (3) is set in the sealing chamber (2), will drive liquid and separate fully with slurry, is divided into both sides, and wherein driving liquid can be water, oil or emulsion; Pulp feeding system is made up of high potential head slurry pond (7) (or feeding pump) and one group of non-return valve (1) (or granular slurry sluice valve); Control system is made up of hydraulic control device and microcomputer.
During diaphragm pump work, the high-pressure-driven liquid of clarified water pump (4) is alternately supplied with the top of sealing chamber first, second, third barrier film (3) and the entrance of the driving liquid of backhaul alternately being sent again back to clarified water pump (4) through driving set six fluid control valves of A, B, C, D, E, F of liquid one side; The slurry of being sent here by high potential head slurry pond (7) (or feeding pump), (particle diameter of transported material is greater than 2 millimeters through set six non-return valves (1) of slurry one side (transported material particle diameter less than 2 millimeters slurry) or six granular slurry sluice valves, less than the transportation caliber 1/5th), alternately send the bottom of sealing chamber first, second, third barrier film (3) to, high-pressure-driven liquid in the tank passes to slurry by the swing of barrier film (3) with pressure energy, make slurry alternately send into Outer Tube (8), be transported to the place of appointment. For finishing the adjusting of flow and flow direction in the transportation, also have a, b, c, d, six fluid control valves of e, a moisturizing non-return valve H and a safety valve g in the pump group. Pressure gauge (6) is equipped with in clarified water pump (4) suction side, and the pipeline highest point has means of deflation R. The complete machine operation is by microcomputer control, and its operating mode shows in the analog board simulation.
The isolation tank of diaphragm pump as figure two, is made up of upper and lower two approximate hemispheric parts (9) and (13), nonmetal barrier film (3), metal garden dish (14), seal ring (11), nut (10), screw rod (12).The outlet position of upper and lower hemisphere is a streamline, and the design of intensity pressing force container is middle by the flange connection, and sealing configuration and fixing nonmetal barrier film (3) are adopted in the joint.Barrier film (3) can adapt to the chemistry of transported material, the on-metallic article of physical property for a kind of.The shape approximation of barrier film (3) is a basin shape.Isolation tank junction flange adopts non-symmetry structure, and when making the upper and lower swing of barrier film, the inflection point is different, to improve its flex life.Rosette (14) is equipped with at the center below the barrier film (3), the diameter of rosette (14) is greater than the inlet/outlet aperture, during with convenient Control Failure, the edge that disk (14) is blocked outlet and disk (14) seals, at this moment nonmetal barrier film (3) is attached on the tank skin of isolation tank, avoids occurring accident.
Compared with the prior art the present invention has lot of advantages:
1. owing to adopt the film isolation technology, make slurry and drive the liquid strictness separately, do not exist and mix slurry and drive the liquid leakage.
2. do not run off owing to driving liquid, thereby can realize driving the liquid closed cycle, can eliminate the driving liquid pool.
3. the particle diameter of conveying medium increases greatly.Check valve is adopted in the outlet port, can transport the material less than 2 millimeters particle diameters, adopts gate valve, just can transport greater than 2 millimeters, less than the material of transportation caliber 1/5th particle diameters.
4. lift is big, and H-Max is 20 times of Centrifugal Sand Pumps, is 3 times of oil isolation pump H-Max, the transportation mine tailing all can a pump to tailing dam.Owing to saved booster pump station, so saved a large amount of capital investments and management, maintenance expenses.
5. flow is big, and peak rate of flow is 20 times of oil isolation pump, nearly 100 times of diaphragm pump.
6. the concentration of transportation slurry is big, and the concentration that can transport slurry is less than 60%.
Referring to figure one, describe embodiment of the present invention in detail.
With the transportation mine tailing particle diameter less than 2 millimeters, lift is 150 meter water columns, tailings concentration 30%, flow are 190 meters
3/ hour parameter, implement this invention.
The diaphragm pump of this scheme comprises a multistage centrifugal clean waterpump (4), and model is 150D30 * 6; Six inlet valve A, B, C, D, E, F, model is the KZ743A-25 type; Three isolation tanks (2) adopt the almost spherical structure, and diameter is 1 meter, and barrier film wherein (3) adopts rubber product; Six outlet valves adopt check valve (1); A, b, c, d, e adopt fluid control valve; Clear water spilling water valve g; Means of deflation R; Pressure gauge (6); Moisturizing pond (5) and moisturizing one-way valve H; Deckered stock chest (7); Drive liquid and adopt water; Outer Tube (8).
During diaphragm pump work, at first start the oil pump D of hydraulic control system
1, D
2After oil pump operation is normal, valve b, d are opened, at this moment slurry enters isolation tank first, second, third barrier film bottom.Then, start clean waterpump (4), after clean waterpump (4) reaches rated speed, make gate valve a, c open, after all opening, equipment enters the initial orders I.At this moment valve A opens, the high pressure clear water that clean waterpump (4) is discharged enters barrier film (3) top of isolation tank (1), the slurry of barrier film (3) bottom backs down check valve, enter Outer Tube (8), after the program I was sent, equipment entered the program II, this moment, valve A closed gradually, valve C opens gradually, and isolation tank first, second barrier film top enters the high pressure clear water simultaneously, and the bottom is discharged slurry simultaneously.A closes fully when valve, and equipment enters the program III, and at this moment valve B opens gradually, and high potential head deckered stock chest (7) supplies slurry to the barrier film bottom of isolation tank first, and the top clear water flows back to clean waterpump (4) inlet.B opens fully when valve, enters the program IV this moment.Valve C closes gradually, valve E is opening gradually, clean waterpump (4) supplies the high pressure clear water to isolation tank second, the third barrier film top simultaneously, and the slurry of isolation tank second, the third barrier film bottom enters Outer Tube (8) simultaneously, and the slurry of high potential head deckered stock chest (7) enters the barrier film bottom of isolation tank first.C closes fully when valve, this moment, equipment entered the program V, at this moment valve D opens gradually, valve B closes gradually, clean waterpump (4) supplies the high pressure clear water to the isolation tank third barrier film top, slurry below isolation tank third barrier film enters Outer Tube (8), and deckered stock chest (7) supplies slurry to isolation tank first, second barrier film bottom simultaneously.The top clear water flows back to clean waterpump (4) inlet.B closes fully when valve, enter the program VI this moment, valve A opens gradually, valve E closes gradually, clean waterpump (4) supplies the high pressure clear water to isolation tank first, the third barrier film top simultaneously, the bottom slurry enters Outer Tube (8), and deckered stock chest this moment (7) only supplies slurry to isolation tank (2) bottom, and the clear water on top flows back to the inlet of clean waterpump (4).E closes fully when valve, enter the program XII this moment, valve F opens gradually, valve D closes gradually, clean waterpump (4) only supplies the high pressure clear water to isolation tank first barrier film top, the bottom slurry enters Outer Tube (8), and deckered stock chest (7) supplies slurry to isolation tank second, the third barrier film bottom simultaneously, and the top clear water flows back to clean waterpump (4) inlet.D closes fully when valve, enters the program VIII this moment.Valve C opens gradually, and valve A closes gradually, and clean waterpump (4) supplies the high pressure clear water to isolation tank first, second barrier film top simultaneously, and the bottom slurry enters Outer Tube (8), and deckered stock chest this moment (7) only supplies slurry to the barrier film bottom of isolation tank third.When valve A closes fully, enter the program IX this moment, valve B opens gradually, valve F closes gradually, clean waterpump (4) only supplies the high pressure clear water to isolation tank second barrier film top, the bottom slurry enters Outer Tube (8), and deckered stock chest (7) supplies slurry to isolation tank first, the third barrier film bottom simultaneously, makes the top clear water flow back to the inlet of clean waterpump (4).F closes fully when valve, and enter the program X this moment, and valve E opens gradually, valve C closes gradually, clean waterpump (4) supplies the high pressure clear water to isolation tank second, the third barrier film top simultaneously, and the bottom slurry enters Outer Tube (8), and deckered stock chest (7) only supplies slurry to isolation tank first barrier film bottom.At this moment, this pump complete working procedure finishes.Work on, the cyclic program V is to X.
When needing terminator, press the terminator button, make valve d close; valve e opens; this moment, clear water (deckered stock chest overflow water) was also advanced in the barrier film bottom of isolation tank, worked on a period of time by cyclic program, the slurry pipeline part valve before realizing shutting down and the cleaning of Outer Tube.Stop clean waterpump (4) work then, and make valve A, B, C, D, E, F and valve a, b, c, d, e Close All.Stop oil pump D at last
1, D
2
When bringing into operation, pump notes exhaust.
Because of the clear water of pump partly is closed-circuit, clean waterpump (4) suction side insufficient water for a certain reason, then clean waterpump (4) suction vacuum increases, and moisturizing pond (5) clear water backs down moisturizing one-way valve H, from the moisturizing of trend clean waterpump (4) suction side.The side clear water is too much if clean waterpump (4) is discharged, and barrier film (3) is blocked the plasma discharge mouth, and clean waterpump (4) drain-side clear water pressure rises, and back down clear water relief valve g this moment automatically, and clear water enters moisturizing pond (5) again, thereby realizes the automatic adjusting of barrier film relative position.
Claims (9)
1, a kind of diaphragm pump that is used for the transportation of granule materials pipe long-distance, comprise a clean waterpump [4], six inlet valves (A, B, C, D, E, F), three isolation tanks [2], six outlet valves [1] and a, b, c, d, six valves of e, g, it is characterized in that said isolation tank [2], adopt two approximate hemispheric parts, form by the flange butt joint, at the flange joint, nonmetal barrier film [3] is housed, make slurry and drive the both sides that liquid is isolated in barrier film [3].
2,, it is characterized in that the nonmetal barrier film (3) in the isolation tank (2) is a rubber product according to the said diaphragm pump of claim 1.
3, according to the said diaphragm pump of claim 1, it is characterized in that the adpting flange of the upper and lower hemisphere-shaped workpiece of said isolation tank (2), adopt non-symmetry structure.
4,, it is characterized in that said driving liquid can be water, oil or emulsified liquid according to the said diaphragm pump of claim 1.
5, according to the said diaphragm pump of claim 1, it is characterized in that said barrier film (3), its centre bottom is fixed the enough metal garden dishes of a bulk strength, and diameter is greater than the aperture of isolation tank import and export.
6,, it is characterized in that said outlet valve can adopt check valve according to the described diaphragm pump of claim 1.
7,, it is characterized in that said outlet valve can adopt gate valve according to the described diaphragm pump of claim 1.
8, according to the described diaphragm pump of claim 1, it is characterized in that said clean waterpump, can use a plurality of clean waterpumps.
9, according to the described diaphragm pump of claim 1, it is characterized in that said isolation tank, can be with four.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 86104866 CN86104866A (en) | 1986-08-07 | 1986-08-07 | Diaphragm pump |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 86104866 CN86104866A (en) | 1986-08-07 | 1986-08-07 | Diaphragm pump |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN86104866A true CN86104866A (en) | 1987-08-12 |
Family
ID=4802630
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 86104866 Pending CN86104866A (en) | 1986-08-07 | 1986-08-07 | Diaphragm pump |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN86104866A (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104100501A (en) * | 2014-07-26 | 2014-10-15 | 徐州天科机械制造有限公司 | Capsule type sludge conveying pump |
| CN104763607A (en) * | 2015-02-16 | 2015-07-08 | 于长和 | Combined diaphragm pump |
| CN106286242A (en) * | 2015-05-18 | 2017-01-04 | 葛稳生 | A kind of slurry pipeline steel equipment |
| CN108953172A (en) * | 2018-08-10 | 2018-12-07 | 湖南柿竹园有色金属有限责任公司 | A kind of separate pump automatic control system |
-
1986
- 1986-08-07 CN CN 86104866 patent/CN86104866A/en active Pending
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104100501A (en) * | 2014-07-26 | 2014-10-15 | 徐州天科机械制造有限公司 | Capsule type sludge conveying pump |
| CN104763607A (en) * | 2015-02-16 | 2015-07-08 | 于长和 | Combined diaphragm pump |
| CN106286242A (en) * | 2015-05-18 | 2017-01-04 | 葛稳生 | A kind of slurry pipeline steel equipment |
| CN108953172A (en) * | 2018-08-10 | 2018-12-07 | 湖南柿竹园有色金属有限责任公司 | A kind of separate pump automatic control system |
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| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| RJ01 | Rejection of invention patent application after publication |