CN203810052U - High pressure slurry pipe stable pumping system - Google Patents

High pressure slurry pipe stable pumping system Download PDF

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Publication number
CN203810052U
CN203810052U CN201420192751.3U CN201420192751U CN203810052U CN 203810052 U CN203810052 U CN 203810052U CN 201420192751 U CN201420192751 U CN 201420192751U CN 203810052 U CN203810052 U CN 203810052U
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China
Prior art keywords
piston
pistons
main pump
pumping system
main
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Withdrawn - After Issue
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CN201420192751.3U
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Chinese (zh)
Inventor
王长勇
普光跃
周传奇
曾光
陈赓
太江林
刘红坤
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Yunnan Dahongshan Pipeline Co Ltd
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Yunnan Dahongshan Pipeline Co Ltd
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Priority to CN201420192751.3U priority Critical patent/CN203810052U/en
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Abstract

The utility model provides a high pressure slurry pipe stable pumping system which comprises at least one main pump. Each main pump comprises a crank shaft, driving connecting rods and pistons, the pistons are connected to the driving connecting rods, the driving connecting rods are connected to the crank shaft, rotation of the crank shaft is converted into suction and discharge movement of the pistons through the driving connecting rods, each main pump comprises two or more pistons, each piston is connected to the crank shaft through one driving connecting rod, and the same angular phase difference is sequentially formed between all the pistons included in each main pump. By means of the high pressure slurry pipe stable pumping system, the pistons of the main pumps in a pump station are located at different phase angles respectively, so that all the pistons cannot get into the maximum discharge state or the maximum suction state at the same time, main pump outlet pressure fluctuations caused by piston suction and discharging are quite stable, the pressure fluctuations in an existing long-distance slurry pipe pumping system are overcome, and the slurry pipe conveying safety is guaranteed.

Description

The steady pumping system of a kind of high pressure slurry pipeline
Technical field
The utility model relates to pumping technology field, relates to more specifically the steady pumping system of a kind of high pressure slurry pipeline.
Background technique
At China's fast increasing economy, particularly metallurgical in recent years, petrochemical industry, oil, the sustainable and stable development of the industries such as chemical fertilizer, along with the price of the energy promotes, cost of transportation is more and more higher, and utilize hydraulic pipe conveying solid substance material, transport (as railway with other, highway) compare, there is transportation range short, capital investment is few, landform is adapted to and can utilize discrepancy in elevation potential energy, do not account for or account for less soil, free from environmental pollution and not disturbed by ambient conditions, can realize and working continuously, technology is reliable, traffic expense is only railway, the plurality of advantages such as 1/6~1/10 of highway, realize economy, environment sustainable development.Slurry Pipeline Transportation system of the prior art is all that the pumping that utilizes some main pumps in pumping plant to realize slurry material transports, these main pumps all include some suction pistons, generally each pumping plant at least includes 3 main pumps, every main pump has again three groups of suction pistons, in prior art, the phase place of these main pumps and piston is identical, the each piston that is each main pump is substantially all synchronous operation, reach discharge maximum value and suction maximum value simultaneously, there is identical bent axle rotation phase angle, the consequence causing is, in the time that many main pumps of same pumping plant start operation simultaneously, because the phase angle between each pump is identical, also Complete Synchronization of the aspiration stroke of the each piston being connected with main pipeline and discharge stroke, thereby cause the pumping pressure fluctuation in main pump outlet and main pipeline larger, while reaching discharge maximum value as all pistons of multiple main pumps simultaneously, the main pipeline that is connected in piston outlet is caused to maximum compression shock, especially even can there is the danger of booster to high pressure slurry pipeline, therefore in existing slurry transportation pipeline pumping system, ubiquity the defect that main pump outlet pressure surge is larger, threatening Slurry Pipeline Transportation safety.
Summary of the invention
The utility model is based on above-mentioned prior art problem, the steady pumping system of a kind of high pressure slurry pipeline of proposition of innovation, described system is by making the piston of each main pump in pumping plant respectively in different phase angles, thereby all pistons can not arrive maximum emissions status or maximum aspiration state simultaneously, make the main pump outlet pressure surge that causes because of piston suction and discharge more steady, solve in existing long-distance slurry pipeline pumping system because of many identical larger pressure surge problems that cause in main pumps operation phase angle of pumping plant, ensured Slurry Pipeline Transportation safety.
It is as follows that the utility model solves the problems of the technologies described above taked technological scheme:
The steady pumping system of a kind of high pressure slurry pipeline, include at least one main pump, every main pump includes bent axle 1, drive link 3 and piston, described piston is connected in drive link 3, described drive link 3 is connected in bent axle 1, by described drive link 3, the rotation of bent axle 1 is converted into suction and the discharge motion of piston, every main pump includes 2 above pistons, each piston is all connected in bent axle 1 by a described drive link 3, between the included all pistons of every main pump, be formed with successively equal phase angle θ, it is poor that described phase angle θ is defined as between the different piece of the bent axle that different pistons of a certain moment connect corresponding crank angle degree, it is θ=(360/N) ° divided by every included number of pistons N of main pump that the numerical value of described phase angle θ equals 360 °.
Further according to the steady pumping system of high pressure slurry pipeline described in the utility model, wherein said steady pumping system includes two above main pumps, every main pump includes plural piston, and the included number of pistons of every main pump is identical, between the corresponding piston of different main pumps, be formed with successively equal phase angle δ, it is δ=(360/(main pump quantity × mono-pump piston number) that the phase angle δ of the corresponding piston space of different main pumps equals 360 ° of piston sums that comprise divided by described steady pumping system) °.
Further according to the steady pumping system of high pressure slurry pipeline described in the utility model, wherein said steady pumping system includes three main pumps, every main pump includes three pistons, between three pistons of every main pump self, there are 120 ° of phase angles, between the corresponding piston of three main pumps, form successively the phase angle of 40 °.
Further according to the steady pumping system of high pressure slurry pipeline described in the utility model, wherein the bent axle 1 of every main pump has the three-dimensional bending structure that can rotate around central axis, comprise not at conplane several crank arms 7, the quantity of described crank arm 7 number of pistons included with main pump is identical, and arrange according to the mode of dividing 360 ° of angles equally, between the central plane of adjacent crank arm 7, have the angle equating with described phase angle θ, the drive link that each piston is corresponding is rotationally connected with on a corresponding crank arm 7.
Further according to the steady pumping system of high pressure slurry pipeline described in the utility model, wherein said piston comprises piston rod 2, piston head 4 and piston cylinder 5, described piston head 4 is connected in piston rod 2, and be co-located in described piston cylinder 5, the other end of described piston rod 2 is rotationally connected with described drive link 3, and the other end of described drive link 3 is rotationally connected with on a corresponding crank arm 7.
Further according to the steady pumping system of high pressure slurry pipeline described in the utility model, wherein said bent axle 1 often rotates a circle, each piston completes 1 aspiration stroke and 1 discharge stroke, and any two pistons can be simultaneously in maximum discharge or maximum aspiration state.
Further, according to the steady pumping system of high pressure slurry pipeline described in the utility model, wherein the pump discharge pipe of every main pump and pumping intake piping are communicated in the main pipeline that slurry is carried.
At least can reach following technique effect by the technical solution of the utility model:
1), the utility model is by making the piston of each main pump in pumping plant respectively in different phase angles, solve in existing long-distance slurry pipeline pumping system because of many identical larger pressure surge problems that cause in main pumps operation phase angle of pumping plant, ensured Slurry Pipeline Transportation safety.
2), in the above-mentioned pumping system of the utility model, between each piston of each main pump, all aspirate and discharge stroke with equal phase angle, interval, in balanced outlet pressure, by the balance orderly function of piston, improve pumping efficiency and the working life of pumping system, reduced Slurry Pipeline Transportation cost.
Brief description of the drawings
Accompanying drawing 1 is the side-looking structural representation of separate unit main pump in the steady pumping system of high pressure slurry pipeline described in the utility model;
Accompanying drawing 2 arranges structure principle chart for including piston space phase angle in the separate unit main pump of three pistons in the utility model;
Accompanying drawing 3 is for being applicable to the structure principle chart of facing of the bent axle in schematic diagram described in accompanying drawing 2;
Accompanying drawing 4 is for being applicable to the side-looking structure principle chart of the bent axle in schematic diagram described in accompanying drawing 2;
Accompanying drawing 5 is phase angle coupling distribution design sketch in main pump described in the utility model.
In figure, the implication of each reference character is as follows:
1-bent axle, 2-piston rod, 3-drive link, 4-piston head, 5-piston cylinder, 6-main pipeline, 7-crank arm.
Embodiment
Below in conjunction with accompanying drawing, the technical solution of the utility model is described in detail, so that those skilled in the art can more clearly understand scheme of the present utility model, but does not therefore limit protection domain of the present utility model.
First the general structure of brief description slurry pipeline pumping system, slurry pipeline pumping system entirety comprises multiple pumping plants and the main pipeline that is connected each pumping plant.Each pumping plant includes many main pumps, and the pump discharge pipe of every main pump and pumping intake piping are all communicated in main pipeline, and every main pump is all that suction/discharge stroke principle based on crankshaft driving piston is carried out work.Specifically as shown in Figures 1 and 2, every main pump includes housing, bent axle 1, some drive link 3 and several pistons, preferably comprise three pistons and three corresponding drive link 3, described piston specifically comprises piston rod 2, piston head 4 and piston cylinder 5, described piston head 4 is connected in piston rod 2, and be co-located in described piston cylinder 5, the other end of described piston rod 2 is rotationally connected with drive link 3, the other end of described drive link 3 is rotationally connected with on bent axle 1, in the process of rotating around axis centre at bent axle 1, drive described drive link 3 to move, and then pull piston rod 2 and piston head 4 to aspirate with discharge stroke and move along piston cylinder 5 by drive link 3, thereby utilize the negative pressure forming in piston cylinder to carry out pumping to the slurry in main pipeline 6, the piston pumping theory of this main pump is basic and of the prior art similar.
Innovation of the present utility model is as shown in accompanying drawing 2 and accompanying drawing 3, be to make to be connected between all pistons of main pipeline and there is impartial phase angle, for realizing this object, first between all pistons in same main pump, there is impartial phase angle, described phase angle value is 360 °/number of pistons N, accompanying drawing 2 and accompanying drawing 3 have provided phase angle Distribution Principle when main pump has three pistons, as shown in accompanying drawing 2 and accompanying drawing 3, the other end of drive link 3 is connected in by rotating shaft on the crank arm 7 of bent axle 1, described crank arm 7 can flexing axle central axis do the rotation of 360 °, in the time that main pump includes three pistons, the center line of described bent axle or profile line structure are as shown in Figure 3, there is the three-dimensional bending structure that can rotate around central axis, comprise three not crank arms 7 in same plane, the drive link that each piston is corresponding is rotationally connected with respectively on a crank arm 7, for the phase angle that ensures that three pistons have 120 ° each other, the central plane A at three crank arm places of described bent axle has each other 120 ° of angles and divides 360 ° of angles equally, thereby the phase angle of described piston is defined as the angle between the crank arm 7 place central plane A that the corresponding drive link of piston place principal plane and this piston connects, angle between the central plane A of the crank arm that namely piston rod 2 of described piston and this piston rod 2 connect, in the time that main pump includes three pistons, the phase angle of three piston spaces is 120 °, described in accompanying drawing 2, ° (piston rod 2 becomes 0 ° with corresponding crank arm in θ=0, phase angle of first piston, piston head is in discharge maximum position), θ=0, phase angle of second piston ° (piston rod 2 becomes 120 ° with corresponding crank arm), ° (piston rod 2 becomes 240 ° with corresponding crank arm in θ=240, phase angle of the 3rd piston, along unified counter clockwise direction), like this in the time that main pump is worked, the every rotating 360 degrees of its bent axle 1, each piston rod differs 120 degree, when first piston head is during in top, suction and exhaust position that other 2 piston rods mediate, in the time that bent axle continues operation, first piston will aspirate ore pulp backward, and other 2 pistons reach phase discontinuously and discharge foremost ore pulp, then continue suction backward, make each piston reach 1 suction and 1 discharge, but three pistons can be simultaneously in suction or discharge maximum rating, and then can in the main pipeline of piston outlet, not cause simultaneous pressure to fluctuate.
In the time including many main pumps in pumping plant simultaneously, have equal phase angle except requiring to control in the manner described above between the piston of each independent main pump self, also require to there is successively equal phase angle between the piston of each main pump, namely according to same phase angle, reference direction (clockwise or counterclockwise) is set, phase angle between two corresponding pistons of two main pumps is 360 °/piston sum N, number of pistons is wherein that main pump quantity is multiplied by the included number of pistons of each main pump, and the included number of pistons of each main pump equates.Include three main pumps such as working as, when each main pump includes three pistons, separate unit main pump can be regarded as to an entirety, all to be driven by a bent axle, because the phase angle between included three pistons of separate unit main pump be fixing and equate be 120 °, so need only and wherein differ fixing phase angle between one group of corresponding piston between two main pumps, between remaining other corresponding pistons, also differ same constant phase angle, include altogether 9 pistons according to above-mentioned three main pumps, phase angle=360 between the piston of different main pumps °/9=40 °, three 9 phase angles that piston mean allocation bent axle often circles that main pump is included in whole like this pumping plant, ensure can not have two pistons to reach maximum discharge or aspiration stroke state simultaneously, thereby aspirating and discharge stroke of all pistons space, to the pressure surge in main pipeline pumping procedure be reduced to minimum.
The phase control mode that realizes each main pump piston running in steady pumping system described in the utility model is as follows: first the definition at phase angle is the same, for piston place plane or piston rod and institute are connected the angle between the central plane A of crank arm place, for simplicity, according to counter clockwise direction (with reference to the actual rotation direction of crank arm), crank arm place plane taking piston head in the time that state is stretched out in maximum discharge is as 0 ° of phase angle, and crank arm is corresponding phase angle rotating counterclockwise in process angulation between this place, 0 ° of angle plane.
Then, the mode that is 360 °/number of pistons N according to mutual phase angle by all pistons included in each main pump arranges, concrete can be arranged to the bent axle in main pump to comprise N crank arm, adjacent crank arm place plane becomes 360 °/N each other, then drive link corresponding each piston is rotationally connected with respectively on corresponding crank arm, and then makes each piston space in single main pump there is equal phase angle.
Finally calculate phase angle=360 between the piston of different main pumps °/(the mono-pump piston of main pump quantity M* is counted N) according to the included number of pistons of all main pumps, then set gradually the phase angle difference of piston between different main pumps according to this angle, can be in the manner described above with the phase angle of unified each piston of standard definition, determine behind position, 0 ° of angle, set successively the position of the crank arm that in different main pumps, piston connects according to described phase angle, because angle between the crank arm of separate unit main pump equates, therefore every main pump only needs the position of setting the crank arm that one of them piston is corresponding can make each piston have equal phase angle difference.In phase angle assignment procedure between many main pumps, separate unit main pump can be regarded as to an entirety, only consider one of them piston, simplify piston phase control process.
Pass through the technical solution of the utility model, can be good at the suction discharge process of the each piston of balance, the phase angle matching effect of the separate unit main pump that comprises three pistons providing as accompanying drawing 4, can find out that this mode has reduced to pump out mouth pressure fluctuation greatly compared with the random situation in phase angle between pump in prior art and pump piston, phase angle when all pumps (piston) in prior art is in 0 degree, there will be each pump all reach pressure maximum simultaneously and reach pressure minimum simultaneously, make wave range maximum and larger to equipment damage.Can see clearly and utilize phase-matching technique of the present utility model that the whole peak value of pressure is all tended to be steady more by accompanying drawing 4, greatly alleviate the pressure damage to equipment in pumping procedure.
Below be only that preferred implementation of the present utility model is described; the technical solution of the utility model is not limited to this; the any known distortion that those skilled in the art do on the basis of major technique design of the present utility model all belongs to the claimed technology category of the utility model, and the concrete protection domain of the utility model is as the criterion with the record of claims.

Claims (7)

1. the steady pumping system of high pressure slurry pipeline, include at least one main pump, every main pump includes bent axle (1), drive link (3) and piston, described piston is connected in drive link (3), described drive link (3) is connected in bent axle (1), by described drive link (3), the rotation of bent axle (1) is converted into suction and the discharge motion of piston, it is characterized in that, every main pump includes 2 above pistons, each piston is all connected in bent axle (1) by a described drive link (3), between the included all pistons of every main pump, be formed with successively equal phase angle θ, it is poor that described phase angle θ is defined as between the different piece of the bent axle that different pistons of a certain moment connect corresponding crank angle degree, it is θ=(360/N) ° divided by every included number of pistons N of main pump that the numerical value of described phase angle θ equals 360 °.
2. the steady pumping system of high pressure slurry pipeline according to claim 1, it is characterized in that, described steady pumping system includes two above main pumps, every main pump includes plural piston, and the included number of pistons of every main pump is identical, between the corresponding piston of different main pumps, be formed with successively equal phase angle δ, it is δ=(360/(main pump quantity × mono-pump piston number) that the phase angle δ of the corresponding piston space of different main pumps equals 360 ° of piston sums that comprise divided by described steady pumping system) °.
3. the steady pumping system of high pressure slurry pipeline according to claim 2, it is characterized in that, described steady pumping system includes three main pumps, every main pump includes three pistons, between three pistons of every main pump self, there are 120 ° of phase angles, between the corresponding piston of three main pumps, form successively the phase angle of 40 °.
4. according to the steady pumping system of high pressure slurry pipeline described in claim 1-3 any one, it is characterized in that, the bent axle (1) of every main pump has the three-dimensional bending structure that can rotate around central axis, comprise not at conplane several crank arms (7), the quantity of described crank arm (7) number of pistons included with main pump is identical, and arrange according to the mode of dividing 360 ° of angles equally, between the central plane of adjacent crank arm (7), there is the angle equating with described phase angle θ, the drive link that each piston is corresponding is rotationally connected with on a corresponding crank arm (7).
5. the steady pumping system of high pressure slurry pipeline according to claim 4, it is characterized in that, described piston comprises piston rod (2), piston head (4) and piston cylinder (5), described piston head (4) is connected in piston rod (2), and be co-located in described piston cylinder (5), the other end of described piston rod (2) is rotationally connected with described drive link (3), and the other end of described drive link (3) is rotationally connected with on a corresponding crank arm (7).
6. according to the steady pumping system of high pressure slurry pipeline described in claim 1-3 any one, it is characterized in that, described bent axle (1) often rotates a circle, and each piston completes 1 aspiration stroke and 1 discharge stroke, and any two pistons can be simultaneously in maximum discharge or maximum aspiration state.
7. according to the steady pumping system of high pressure slurry pipeline described in claim 1-3 any one, it is characterized in that, the pump discharge pipe of every main pump and pumping intake piping are communicated in the main pipeline that slurry is carried.
CN201420192751.3U 2014-04-21 2014-04-21 High pressure slurry pipe stable pumping system Withdrawn - After Issue CN203810052U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
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Application Number Priority Date Filing Date Title
CN201420192751.3U CN203810052U (en) 2014-04-21 2014-04-21 High pressure slurry pipe stable pumping system

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103939742A (en) * 2014-04-21 2014-07-23 云南大红山管道有限公司 Stable pumping system of high pressure slurry pipeline

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103939742A (en) * 2014-04-21 2014-07-23 云南大红山管道有限公司 Stable pumping system of high pressure slurry pipeline
CN103939742B (en) * 2014-04-21 2016-08-24 云南大红山管道有限公司 A kind of steady pumping system of high-pressure slurry pipeline

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AV01 Patent right actively abandoned

Granted publication date: 20140903

Effective date of abandoning: 20160824

C25 Abandonment of patent right or utility model to avoid double patenting