CN101149052A - A pressurization and recovery combined pump with asymmetric cavity - Google Patents
A pressurization and recovery combined pump with asymmetric cavity Download PDFInfo
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- CN101149052A CN101149052A CNA2007100185510A CN200710018551A CN101149052A CN 101149052 A CN101149052 A CN 101149052A CN A2007100185510 A CNA2007100185510 A CN A2007100185510A CN 200710018551 A CN200710018551 A CN 200710018551A CN 101149052 A CN101149052 A CN 101149052A
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- 238000011084 recovery Methods 0.000 title claims abstract description 43
- 239000007788 liquid Substances 0.000 claims abstract description 51
- 239000012530 fluid Substances 0.000 claims description 16
- 230000008676 import Effects 0.000 claims 8
- 239000000463 material Substances 0.000 claims 6
- 239000002994 raw material Substances 0.000 abstract description 20
- 238000012824 chemical production Methods 0.000 abstract description 2
- 239000003208 petroleum Substances 0.000 abstract description 2
- 238000001223 reverse osmosis Methods 0.000 abstract description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 2
- 238000009826 distribution Methods 0.000 description 21
- 238000000034 method Methods 0.000 description 3
- 238000004891 communication Methods 0.000 description 2
- 238000005265 energy consumption Methods 0.000 description 2
- 238000007789 sealing Methods 0.000 description 2
- 230000009977 dual effect Effects 0.000 description 1
- 238000002955 isolation Methods 0.000 description 1
- 238000009931 pascalization Methods 0.000 description 1
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Abstract
本发明公开了一种不对称形腔的加压及回收组合泵,包括左泵体、右泵体、设置在左泵体和右泵体轴向之间的缸体和缸体中的转子,其特征是,所述的缸体开有一个大致为椭圆的泵室,转子将其分隔为两个月牙形且相对的升压腔和回收腔,它们的小圆弧半径r相等,也即转子的半径;升压腔的大圆弧半径R1大于回收腔的大圆弧半径R2;所述的左泵体上设有原料液进口和处理液出口;所述的右泵体上设有原料液出口和处理液进口;原料液进口和原料液出口连通升压腔;处理液进口和处理液出口连通回收腔;所述的转子圆周上至少均布有4片可沿转子径向伸缩的叶片。本发明的组合泵具有结构简单紧凑、低噪声等优点,广泛用于反渗透水处理和石油、化工生产领域。
The invention discloses a pressurization and recovery combined pump with an asymmetric shape cavity, which comprises a left pump body, a right pump body, a cylinder arranged between the axial direction of the left pump body and the right pump body, and a rotor in the cylinder. It is characterized in that the cylinder is provided with a roughly elliptical pump chamber, and the rotor divides it into two crescent-shaped and opposite boost chambers and recovery chambers, and their small arc radii r are equal, that is, the rotor The radius of the arc; the large arc radius R1 of the boost chamber is greater than the large arc radius R2 of the recovery chamber; the left pump body is provided with a raw material liquid inlet and a treatment liquid outlet; the right pump body is provided with a raw material liquid The outlet and the treatment liquid inlet; the raw material liquid inlet and the raw material liquid outlet are connected to the boost chamber; the treatment liquid inlet and the treatment liquid outlet are connected to the recovery chamber; at least 4 blades that can expand and contract in the radial direction of the rotor are evenly distributed on the circumference of the rotor. The combined pump of the invention has the advantages of simple and compact structure, low noise, etc., and is widely used in the fields of reverse osmosis water treatment and petroleum and chemical production.
Description
技术领域 technical field
本发明涉及一种流体机械,特别涉及一种流体的加压及回收组合泵。The invention relates to a fluid machine, in particular to a combination pump for pressurizing and recovering fluid.
背景技术 Background technique
在反渗透水处理和石油、化工生产领域的许多流程中,需要先将流体加压到高压后进行下一步处理,处理后剩余的液体具有很高的压力能。对剩余流体中压力能进行回收对减少能耗,降低产品成本具有重要意义。In many processes in reverse osmosis water treatment and petroleum and chemical production fields, it is necessary to pressurize the fluid to high pressure before proceeding to the next step of treatment, and the remaining liquid after treatment has high pressure energy. Recovering the pressure energy in the remaining fluid is of great significance to reduce energy consumption and product cost.
现有用于液体压力能回收的流体机械主要形式有:(1)透平式,结构与离心泵相似,作用与泵相反。一般与离心泵共轴使用,在流体流量较小的场合中,效率较低,而且主要运动部件结构复杂。(2)活塞式,单机的处理能力低,在系统中需要特殊的阀门配合使用,造成系统运行操作的复杂性。The main forms of fluid machinery currently used for liquid pressure energy recovery are: (1) Turbine type, similar in structure to centrifugal pumps, and opposite in function to pumps. It is generally used coaxially with the centrifugal pump. In the case of small fluid flow, the efficiency is low, and the structure of the main moving parts is complex. (2) Piston type, the processing capacity of a single machine is low, and special valves are required to be used in the system, which causes the complexity of the system operation.
发明内容 Contents of the invention
本发明所要解决的技术问题是提供一种不对称形腔的加压-回收组合泵,具有结构简单紧凑、低噪声,在系统中便于实施等优点。The technical problem to be solved by the present invention is to provide a pressurization-recovery combination pump with an asymmetric cavity, which has the advantages of simple and compact structure, low noise, and easy implementation in the system.
为达到以上目的,本发明是采取如下技术方案予以实现的:To achieve the above object, the present invention is achieved by taking the following technical solutions:
一种不对称形腔的加压及回收组合泵,包括左泵体、右泵体、设置在左泵体和右泵体轴向之间的缸体和缸体中的转子,其特征是,所述的缸体开有一个大致为椭圆的泵室,转子将其分隔为两个月牙形且相对的升压腔和回收腔,它们的小圆弧半径r相等,也即转子的半径;升压腔的大圆弧半径R1大于回收腔的大圆弧半径R2;所述的左泵体上设有原料液进口和处理液出口;所述的右泵体上设有原料液出口和处理液进口;原料液进口和原料液出口连通升压腔;处理液进口和处理液出口连通回收腔;所述的转子圆周上至少均布有4片可沿转子径向伸缩的叶片。A pressurization and recovery combination pump with an asymmetric cavity, comprising a left pump body, a right pump body, a cylinder arranged between the axial direction of the left pump body and the right pump body, and a rotor in the cylinder, the characteristics of which are: The cylinder body has a roughly elliptical pump chamber, and the rotor divides it into two crescent-shaped and opposite boost chambers and recovery chambers, and their small arc radii r are equal, that is, the radius of the rotor; The large arc radius R1 of the pressure chamber is greater than the large arc radius R2 of the recovery chamber; the left pump body is provided with a raw material liquid inlet and a treatment liquid outlet; the right pump body is provided with a raw material liquid outlet and a treatment liquid outlet The inlet; the raw material liquid inlet and the raw material liquid outlet are connected to the boost chamber; the treatment liquid inlet and the treatment liquid outlet are connected to the recovery chamber; at least 4 blades that can expand and contract along the radial direction of the rotor are evenly distributed on the circumference of the rotor.
上述方案中,所述的左泵体相对缸体的左侧平面设有升压腔进口配流槽和回收腔出口配流槽分别连通原料液进口和处理液出口;右泵体相对缸体的右侧平面设有升压腔出口配流槽和回收腔进口配流槽分别连通原料液出口和处理液进口;所述的转子的圆周上开有周向均布的叶片槽,叶片槽底部设有弹簧连接叶片,叶片设置在该叶片槽中,当转子转动到升压腔、回收腔的大圆弧半径R1、R2处时,叶片完全伸出;当转子转动到升压腔和回收腔的小圆弧半径r处时,叶片全部缩进。In the above scheme, the left side of the left pump body relative to the cylinder body is provided with a booster chamber inlet distribution groove and a recovery chamber outlet distribution groove respectively connected to the raw material liquid inlet and the treatment liquid outlet; the right pump body is opposite to the right side of the cylinder body The plane is provided with a flow distribution groove at the outlet of the booster chamber and an inlet distribution groove of the recovery chamber respectively connected to the outlet of the raw material liquid and the inlet of the treatment liquid; the circumference of the rotor is provided with uniformly distributed blade grooves, and the bottom of the blade grooves is provided with springs to connect the blades. Set in the vane groove, when the rotor rotates to the large arc radius R1 and R2 of the booster chamber and the recovery chamber, the blades are fully extended; when the rotor rotates to the small arc radius r of the booster chamber and the recovery chamber , the blades are all indented.
流体从左泵体的原料液进口通过升压腔进口配流槽进入升压腔,转子和叶片的转动使流体升压,高压流体通过右泵体的升压腔出口配流槽从原料液出口输出到处理单元。经过处理单元后,剩余的高压处理液从右泵体的处理液进口通过与之相连的回收腔进口配流槽进入缸体中同一泵室的回收腔,在回收腔内通过叶片推动转子,做功后,通过左泵体的回收腔出口配流槽从处理液出口排放。The fluid enters the booster chamber from the raw material liquid inlet of the left pump body through the distribution groove at the inlet of the booster chamber. processing unit. After passing through the treatment unit, the remaining high-pressure treatment liquid enters the recovery chamber of the same pump chamber in the cylinder body from the treatment liquid inlet of the right pump body through the inlet distribution groove of the recovery chamber connected to it, and pushes the rotor through the blades in the recovery chamber. , and discharge from the treatment liquid outlet through the outlet distribution groove of the recovery cavity of the left pump body.
本发明的特点是综合了叶片泵和叶片马达的双重特点,回收腔与升压腔设置在缸体的同一泵室中。利用流程中高压处理液对回收腔的叶片做功,输出连续回转运动和扭矩,回收压力能,从而降低泵的负载,节省泵能耗。泵的能量回收率为70%-80%,且不需要特殊阀门配合工作,泵体的结构简单,操作简易方便、运行可靠。与其他各类泵相比,单位功率的所需的重量较小。The feature of the present invention is that the dual characteristics of the vane pump and the vane motor are combined, and the recovery chamber and the boosting chamber are arranged in the same pump chamber of the cylinder body. The high-pressure treatment liquid in the process is used to do work on the blades of the recovery chamber, output continuous rotary motion and torque, and recover pressure energy, thereby reducing the load of the pump and saving pump energy consumption. The energy recovery rate of the pump is 70%-80%, and there is no need for special valves to work together. The structure of the pump body is simple, the operation is simple and convenient, and the operation is reliable. Compared with other types of pumps, the required weight per unit power is small.
附图说明 Description of drawings
图1是本发明的结构剖视图。Fig. 1 is a structural sectional view of the present invention.
图2是图1的E-E剖视图。Fig. 2 is a sectional view along line E-E of Fig. 1 .
图3是图1的F-F剖视图。Fig. 3 is a sectional view taken along line F-F of Fig. 1 .
图4是图1的G-G剖视图。Fig. 4 is a G-G sectional view of Fig. 1 .
图中:In the picture:
1---左泵体;2---轴;3,9---轴承;4---键;5---转子;6---缸体;7---叶片;8---右泵体;10---油封;11---轴封;12---螺栓;13---左侧配流槽;14---右侧配流槽;其中:13a、14c为升压腔进、出口配流槽;14d、13b为回收腔进、出口配流槽;A:原料液进口、B:原料液出口、C:处理液出口、D:处理液进口;V1:升压腔V2:回收腔1---Left pump body; 2---Shaft; 3, 9---Bearing; 4---Key; 5---Rotor; 6---Cylinder body; 7---Blade; 8-- -Right pump body; 10---oil seal; 11---shaft seal; 12---bolt; 13---left distribution groove; 14---right distribution groove; among them: 13a, 14c are booster Chamber inlet and outlet distribution grooves; 14d and 13b are recovery chamber inlet and outlet distribution grooves; A: raw material liquid inlet, B: raw material liquid outlet, C: processing liquid outlet, D: processing liquid inlet; V1: boost chamber V2: Recovery cavity
具体实施方式 Detailed ways
下面结合附图对本发明加以详细说明。图1为一种不对称形腔的加压及回收组合泵的结构剖视图,主要包括左泵体1、转子5、缸体6、叶片7、右泵体8和轴2等。缸体6设置在左泵体1和右泵体8轴向之间;轴2通过左泵体1上的轴承3和右泵体8上的轴承9安装在泵体上,转子5通过键4与轴2相连。轴承9与油封10之间设置一个轴封11保持密封,油封10通过外端的螺钉与右泵体8相连。左泵体1外侧两个相对面各设有一个接口:原料液进口A、处理液出口C;右泵体8外侧两个相对面各设有一个接口:原料液出口B、处理液进口D。The present invention will be described in detail below in conjunction with the accompanying drawings. Fig. 1 is a structural sectional view of a pressurization and recovery combination pump with an asymmetric cavity, which mainly includes a left pump body 1, a rotor 5, a cylinder body 6,
如图2所示,本发明的缸体6开有一个大致为椭圆的泵室,转子5将其分隔为两个月牙形且相对的升压腔V1和回收腔V2,它们的小圆弧半径r相等,也即转子5的半径;升压腔V1和回收腔V2的大圆弧半径不相等,分别为R1和R2,R1大于R2。转子5的圆周上开有周向均布的叶片槽,叶片7设置在该叶片槽中,叶片槽底部设有弹簧(图中未画出)连接叶片7,叶片7可随转子2的转动在弹簧的作用下沿转子5径向伸出或缩进,当转子5转动到升压腔V1、回收腔V2的大圆弧半径R1、R2处时,叶片7完全伸出;当转子5转动到升压腔V1和回收腔V2的小圆弧半径r处时,叶片7全部缩进,从而进一步保证了升压腔V1与回收腔V2之间的密封隔离。As shown in Figure 2, the cylinder block 6 of the present invention has a substantially elliptical pump chamber, and the rotor 5 divides it into two crescent-shaped and opposite boost chamber V1 and recovery chamber V2, their small arc radius r is equal, that is, the radius of the rotor 5; the large arc radii of the boost chamber V1 and the recovery chamber V2 are not equal, which are R1 and R2 respectively, and R1 is greater than R2. The circumference of the rotor 5 is provided with circumferentially evenly distributed vane slots, the
如图3所示:左泵体1、缸体6和右泵体8通过螺栓12相连。在左泵体1面对缸体6的左侧面上设有四个中间为腰形、两端为半圆形的左侧配流槽13。其中配流槽13a与原料液进口A相连通,配流槽13b与处理液出口C相连通。As shown in FIG. 3 : the left pump body 1 , the cylinder body 6 and the
如图4所示:在右泵体8面对缸体6的右侧面上设有四个中间为腰形、两端为半圆形的右侧配流槽14。其中配流槽14c与原料液出口B相连通,配流槽14d与处理液进口D相连通。As shown in Figure 4: on the right side of the
如图3、图4所示:当轴2带动转子5和叶片7逆时针转动时,流体从左泵体1的原料液进口A,经配流槽13a进入升压腔V1,转子5和叶片7的转动使流体升压,高压流体通过右泵体8,经配流槽14c从原料液出口B输出到处理单元。经过处理单元后,剩余的高压处理液从右泵体8的处理液进口D,经配流槽14d进入缸体5中同一泵室回收腔V2,在回收腔V2内通过叶片7推动转子5,做功后,经左泵体1的配流槽13b从处理液出口C排放。As shown in Figure 3 and Figure 4: when the
本发明的一个具体实施例如下;如当电机12转速为1450转/分钟标准转速时,叶片3沿径向布置为6片,叶片3的宽度为2.2mm。升压腔V1的大圆弧半径R1为63.3mm、回收腔V2的大圆弧半径R2为61.3mm,升压腔V1和回收腔V2的小圆弧半径r均为60mm,升压腔V1的流量为2.5m3/h;回收腔V2的流量为:1.5m3/h。原料液的进口压力为0.1-0.3Mpa,出口压力为7-10Mpa,处理液的进口压力在5-9Mpa时,能量回收效率为70%-80%。A specific embodiment of the present invention is as follows; for example, when the
Claims (4)
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Cited By (6)
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CN102425546A (en) * | 2011-11-30 | 2012-04-25 | 张意立 | Flat spring and cylinder spring combination compensation double-cavity vane pump |
CN105492770A (en) * | 2013-06-13 | 2016-04-13 | 大陆汽车有限责任公司 | Pump for delivering a liquid |
CN105782021A (en) * | 2016-04-01 | 2016-07-20 | 西安交通大学 | Sliding sheet type overpressure recovery equipment |
CN105822549A (en) * | 2016-04-01 | 2016-08-03 | 西安交通大学 | Equipment for recovering excess pressure between streams in different phase states |
CN106640778A (en) * | 2016-11-15 | 2017-05-10 | 西安交通大学 | Slide piece pressure energy exchanger with matched design between slide pieces and molding lines |
CN111779671A (en) * | 2020-05-14 | 2020-10-16 | 天津市百利溢通电泵有限公司 | Axial-flow eccentric peristaltic displacement pump for electric submersible pump |
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2007
- 2007-08-28 CN CNB2007100185510A patent/CN100529402C/en not_active Expired - Fee Related
Cited By (9)
Publication number | Priority date | Publication date | Assignee | Title |
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CN102425546A (en) * | 2011-11-30 | 2012-04-25 | 张意立 | Flat spring and cylinder spring combination compensation double-cavity vane pump |
CN102425546B (en) * | 2011-11-30 | 2016-03-16 | 温州志杰机电科技有限公司 | A kind of flat spring cylinder spring combination compensation double-cavity vane pump |
CN105492770A (en) * | 2013-06-13 | 2016-04-13 | 大陆汽车有限责任公司 | Pump for delivering a liquid |
CN105782021A (en) * | 2016-04-01 | 2016-07-20 | 西安交通大学 | Sliding sheet type overpressure recovery equipment |
CN105822549A (en) * | 2016-04-01 | 2016-08-03 | 西安交通大学 | Equipment for recovering excess pressure between streams in different phase states |
CN105822549B (en) * | 2016-04-01 | 2018-01-05 | 西安交通大学 | A kind of hydraulic recovery equipment between different phase stream stock |
CN106640778A (en) * | 2016-11-15 | 2017-05-10 | 西安交通大学 | Slide piece pressure energy exchanger with matched design between slide pieces and molding lines |
CN111779671A (en) * | 2020-05-14 | 2020-10-16 | 天津市百利溢通电泵有限公司 | Axial-flow eccentric peristaltic displacement pump for electric submersible pump |
CN111779671B (en) * | 2020-05-14 | 2023-02-24 | 天津市百利溢通电泵有限公司 | Axial-flow eccentric peristaltic displacement pump for electric submersible pump |
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