EP2054622A1

EP2054622A1 - Delivery pump

Info

Publication number: EP2054622A1
Application number: EP07786115A
Authority: EP
Inventors: Axel Binder; Christoph Keller; Christoph Jäger
Original assignee: KSB AG
Current assignee: KSB AG
Priority date: 2006-08-26
Filing date: 2007-07-17
Publication date: 2009-05-06
Anticipated expiration: 2027-07-17
Also published as: TW200831787A; CN101506526A; DE102006040130A1; EP2054622B1; DK2054622T3; NO337736B1; AU2007291652A1; AU2007291652B2; US8021133B2; ZA200900924B; SI2054622T1; TWI345031B; ATE452292T1; JP2010501782A; WO2008025410A1; NO20090626L; DE502007002365D1; US20090191065A1; CN101506526B

Abstract

The delivery pump has a variable-speed drive (5) and is configured as a single-stage centrifugal pump having a radial wheel (2), which rotates in a rotor space (6) of a pump housing (1), for conveying a fluid between a pump inlet (4) and a pump outlet (13). The radial wheel has delivery channels (3) and the centrifugal pump is designed for part-load operation. The delivery quantities of the centrifugal pump are in the range from 0 to 3600 milliliters per minute and in the case of delivery heights from 20 to 300 meters.

Description

K S B A k t i e n g e s e n c e s a t e

description

feed pump

The invention relates to a feed pump with a variable speed drive for a metered flow rate delivery, wherein the feed pump is designed as a single-stage centrifugal pump in a impeller space of a pump housing without a sealing gap rotationally arranged radial centrifugal type for conveying a fluid between a pump inlet and a pump outlet.

In the area of research and development processes in the chemical and pharmaceutical industry, there is a demand for ever faster developments at lower costs. In the production of such substances more flexible, smaller and more environmentally friendly processes are required. This leads to the use of procedural components, which are sometimes operated with very small filling volumes and continuous material flow. Due to the requirement of a flexible use of such systems, a good flushability of the entire system with the units mounted therein with the help of special flushing media is necessary.

Such systems require a precise, constant, freely adjustable and pulsation-free volume flow of liquid substances. For high-precision continuous flow rates ranging from zero milliliters per minute up to three-digit liters per hour, positive displacement pumps are used in the form of micro-toothed and geared pumps as well as diaphragm and piston pumps. Disadvantage of such positive displacement pumps are the lack of reliability due to friction between the relatively moving, sealed components and their pulsating flow. A resulting maintenance The costs of wear parts and their replacement hinder rapid research and development work and interfere with a production process.

WO 2005/052365 A2 discloses a centrifugal pump in the form of a canned motor pump for circulating supercritical hydrocarbons. The drive motor has a split tube made of PEEK ₁ within which a rotor protected by a stainless steel coating is arranged. Ceramic bearings of the pump shaft and the drive rotor are lubricated by a partial flow of the pumped liquid taken from the pump housing. The open impeller has a diameter between 1 and 2 inches and the impeller driving rotor of the roller bearing DC motor has a diameter between 1, 5 and 2 inches. The single-stage pumping device with the open impeller should reach maximum speeds of up to 60,000 rpm. Suction nozzle, discharge nozzle and a type of spiral space downstream of the impeller are arranged in an outer pump housing part, while an inner pump housing part has the cantilevered impeller and a mounting for a variable speed DC canned motor as a drive motor.

A disadvantage of this canned motor design is the large number of columns, which hinder the cleaning of the pump due to the complex flow guidance between the pump and canned motor. Since part of the pumped liquid flows through the motor and its gap permanently, the frictional heat of the roller bearings and the heat loss of the canned motor cause an unacceptably high heat input into the pumped liquid.

The invention is based on the problem of developing a pump unit for delivering and metering liquid substances in the milliliter range of chemical, pharmaceutical and / or cosmetic components, the delivery quantity of which is pulsation-free and precisely adjustable over a large range for Different types of fluid with different properties is variable and for quick product change the pump is easy to clean.

The problem is solved with the features of claim 1. Thus, a metering pump is realized as centrifugal centrifugal type, which is designed for continuous operation in a partial load operating point field. Its flow limits are in the range of 0 ml / min to 3600 ml / min at delivery height limits of 20 m to 300 m. The impeller rotates without contact within an impeller space and a return flow within the impeller sidewalls is permitted. This ensures a wear-free operation of the impeller. And in complete contrast to all applicable centrifugal pump layout regulations, the centrifugal pump is designed for an extreme part-load operation, whereby small amounts are conveyed pulsation-free.

The diameter of the impeller space is at most 4% greater than an outer diameter of a radial wheel arranged therein and the impeller space is provided with one or more, acute-angled or tangential to Radialradaußen- diameter arranged pump outlet channels. As a result, the delivery of the centrifugal pump results from a proportion of static pressure, which builds up due to the centrifugal force within the impeller space and a dynamic proportion in the form of the dynamic pressure, which occurs at the transition from the impeller space to the pump outlet in the form of a Druckstutzen- or outlet channel. The dynamic pressure component at the outlet opening from the impeller space corresponds to a maximum. The addition of the centrifugal delivery head component and the delivery head component due to the dynamic pressure to an overall delivery head of the pump results in the high pressure factor for this type of pump.

In complete contrast to this, conventional centrifugal pumps are designed in which the pressure build-up is predominantly due to a speed delay. tion due to an increase of the impeller downstream flow space in the flow direction results.

In order to make do with minimal losses of valuable conveying means when cleaning the feed pump or switching to other conveying means, the pump housing has a radial wheel arranged in the area between a pump inlet and a pump outlet whose cross-sectional areas are defined by contact surfaces of lines to be connected thereto. a residual volume equal to or less than 50 milliliters. A batch or product change results in a minimal loss with faster pump cleanability.

For the promotion of different funding, the pump housing is provided with a tempering device. Thus, a simple temperature adjustment is possible. In this case, the tempering device may be formed as a heat exchanger which completely or partially surrounds the wetted parts of the pump housing. For this purpose, liquid-tight connections penetrate the tempering device and establish a fluid-conducting connection between a system and the impeller space. Depending on the temperature of the delivery fluid, the pump housing is disposed within the tempering device to cool or heat the delivery fluid.

The radial wheel has at least two delivery channels and at the Radialradaußen- diameter more conveying wells are arranged. These conveying recesses arranged on the radial wheel are designed as blind bores, pockets or tooth-shaped recesses. The delivery channels are formed as open recesses in the form of blade channels, grooves or grooves. In one embodiment of the radial wheel as a closed impeller, a suction and / or pressure-side cover disk can have known conveying grooves. In the radial wheel, the number and arrangement of the inlet openings of the delivery channels is chosen so that they do not increase a Radialradeintrittsdurchmesser. Thus, with the small dimensions, a maximum area on the impeller for generating the centrifugal forces is obtained.

A sealing of the impeller space relative to the atmosphere or the tempering takes place with one or more shaft seals between a housing wall of the impeller space and a rotary Radialrad- or a shaft part penetrating them. These can be known shaft seals or low-friction mechanical seals. Such seals can be dispensed with if a hermetically sealed, magnetically coupled drive transmits a torque to the radial wheel. This can also be designed as a tear-resistant hysteresis coupling. Next can be connected to the radial wheel an electric, pneumatic or hydraulic drive. Such a drive motor is attached to the pump housing or temperature control housing and connected to the radial wheel via a shaft guided through this housing. The arranged in the drive motor bearing the rotor shaft can be found in a conventional manner at the same time as storage of the pump shaft and the radial wheel use.

In addition, a heat barrier between the drive motor and the tempering and / or pump housing may be arranged, wherein the drive motor is connected via a shaft performed with the radial wheel. Connecting zones between the parts of the pump housing and the temperature control housing are rotationally symmetrical and sealed against each other. This provides an improved seal important in the promotion of very small quantities of hazardous or valuable fluids in the form of liquid chemicals and / or solutions. Due to the controllable drive of the centrifugal pump, which is designed for continuous operation in the extreme part-load range, a uniform pulsation-free adjustable delivery of very small quantities of such fluids is possible. Furthermore, the feed pump is connected to a control device, which is connected to an internal or external volume flow measurement and independent of a back pressure of a system with the drive motor generates an adjustable constant volume flow. With the control device, a variable speed range of the drive motor with a quantity factor up to the value 5000 is generated in the switching or control range between minimum and maximum delivery. And in the speed range of the drive motor from 0 to 35,000 revolutions / min, a centrifugal pump delivery pressure is between 0 to 300 bar. Such centrifugal pump operating data are only due to the design of the radial wheel and the housing of the drive motor, contrary to all known design rules

Pump unit possible for extreme continuous partial load operation. For simple installation options, the pump unit, drive motor, switching or control device and associated electronic operating, measuring and control elements are combined to form an assembly-capable module.

Embodiments of the invention are illustrated in the drawings and will be described in more detail below. It show the

Fig. 1 is a feed pump in longitudinal section, Fig. 2 is a perspective view of the pump unit, the

Fig. 3 is a perspective view of an impeller, the

Fig. 4 is an impeller in section and the

5 shows a cross section through the feed pump

In Fig. 1, a feed pump is shown in a single-stage design. In the pump housing 1, a radial wheel 2 centrifugal type is arranged to rotate. The radial wheel 2 has delivery channels 3 and is centrally through a pump inlet 4 flows. The radial wheel 2 is connected to transmit power to a variable speed drive 5 and has an outer diameter DL _A , which may be up to 50 mm. The radial wheel rotates in an impeller space 6, the interior of which diameter D _L R _{I is formed} only 4% larger than the outer diameter DLA of the radial wheel second

The pump housing 1 is provided with a tempering device 7, which is integrated into the pump housing in this embodiment. There are also other designs possible. Fridges 7.1 to 7.3 surround the impeller space 6 and also adjacent to the pump housing 1 seal housing 8. Within the seal housing 8 is arranged as a kind of shaft seal a seal 9, which is shown in the embodiment as a lip seal. Depending on the fluid used, the seal 9 may also be formed as a mechanical seal. The seal 9, depending on the selected connection between the impeller and a shaft 10 of the drive sealingly against the impeller 2, on an impeller hub 2.1 or on the shaft 10. The tempering 7.1 to 7.3 are acted upon by external means. This reliably cools the parts of the pump housing that are in contact with the pumped fluid, as the centrifugal pump is designed for continuous operation in a partial load operating point range whose flow limits range from 0 milliliter / min to 3600 milliliter / min, with a head lift limit of 20 meters - 300 Meters are. As a result of the necessary high speed of the drive 5 additional coolant 11 are arranged on the outer circumference of the drive 5. And the drive 5 is connected to transmit power to the tempering device 7 or attached thereto.

The area of the pump inlet 4 is defined by a contact surface 12 located in the immediate vicinity of the pump interior, against which a line to be connected for a delivery fluid bears sealingly. An analogous training is on the - here below the drawing plane, only partially visible as a semicircle - pump outlet 13 is present. The attachment of it to be connected pump lines - not shown here - by known means, such as union nuts. Due to the immediate introduction of a pump penleitung to the impeller space 6 and by the small diameter differences between impeller outer diameter DLA and inner diameter DLRI of the impeller space 6, results within the pump housing with mounted radial wheel for a fluid delivery a residual volume of equal to or less than 50 milliliters. This very small amount has the advantage that only a slight loss occurs when changing the valuable production fluids.

From Fig. 2, the perspective view of the unitized pump, the pump inlet 4 and the pump outlet 13 can be seen. The tempering device 7 is integrated in the pump housing 1 and pump inlet 4 and pump outlet 13 are passed through the tempering 7 to the impeller space.

External temperature control, for example, coolant, are fed through the optional axial or radial ports 14, 15 the temperature control chambers 7.1 to 7.3 and derived. Pump unit and drive motor 5 are combined to form a structural unit and held in a support member 16. The support element 16 provides the prerequisite for the modular design or installation in an existing system.

Fig. 3 shows a perspective view of a radial wheel 2. The radial wheel 2 is disc-shaped and provided in this example with a hub 2.1. Within the hub 2.1 there is a force-transmitted connection with the shaft 10, not shown here, of the drive 5. Inside the radial wheel 2, four conveyor channels 3 are arranged. In addition, a plurality of conveying recesses 18 are arranged on the impeller periphery 17, which are designed in the form of blind holes. With the help of these delivery wells, the pressure coefficient of the centrifugal impeller is significantly improved. In addition, the pressure and suction side shrouds 19, 20 a plurality of radially extending conveyor grooves 21. The feed grooves 21 also improve the pressure digit of one according to FIG. 1 in an impeller space 6 built-in impeller. The impeller in the axial direction penetrating compensation bores 22 serve to equalize pressure within the pump housing and at the same time as an assembly aid in the preparation of a connection to the drive.

4 shows a section through an impeller 2. It can be seen that here only a total of four conveyor channels 3 are used. Their diameter is adjusted so that they do not intersect an adjacent conveyor channel in the region of the impeller inlet 23. Thus, the maintenance of a defined impeller entry diameter is guaranteed. The depth T of the conveying recesses 18 is selected as a function of the desired residual volume of a fully assembled pump.

Instead of the conveying recesses 18 shown here in the form of bores, any other shape, for example grooves, slots or the like, can find applications, with which an energy transfer is possible in the region of the impeller outer diameter.

Fig. 5 shows a cross section through the feed pump. Due to the generous temperature control room 7.2, which is in operative connection with the other temperature control room, a permanent extreme partial load operation is guaranteed.

Due to the minimized impeller space 6, a radial gap width, which lies in the single-digit millimeter range, results between the outside diameter DLA of the radial wheel and the enveloping, surrounding diameter D _L RI of the impeller space 6. With a centrifugal pump running, the radial gap between impeller and housing is in the range of 2 mm. In the area of the axial impeller sides, the gap between the impeller and the housing is of an analogous order of magnitude. As a result of this configuration of the area in the housing which has a minimal residual volume, the pump can be cleaned very quickly and reliably by a flushing medium. And with the lowest losses of production product be adapted to changed production conditions or facilities. The continuous rotation of the centrifugal impeller 2 results in a pulsation-free operation of this feed pump.

Due to the minimized gap between impeller outer diameter and impeller space, the peripheral component of the impeller simultaneously approaches the peripheral speed and in combination with an obliquely inclined, preferably tangential, impeller 2 disposed pump outlet 13 results for this centrifugal pump at the outlet opening a maximum possible back pressure. In conjunction with the variable-speed motor, high delivery heads can be realized with a minimum residual volume within the pump housing.

The non-contact arrangement of the impeller within the impeller space avoids sealingly abutting friction surfaces. This measure prevents the generation of mechanical frictional heat, prevents fretting and the resulting contamination of a pumped liquid with abraded particles and improves the operational reliability by significantly extended service life. In addition, the cleanability counteracting sealing gaps are avoided.

LIST OF REFERENCE NUMBERS

1 pump housing

2 radial wheel

2.1 = hub

3 conveyor channels

4 pump inlet

5 adjustable drive

6 impeller space

7 tempering device

7.1 - 7.3 = cold rooms

8 seal housing

9 seal

10 wave,

11 coolant

12 contact surface

13 pump outlet

14, 15 = connections for temperature control

16 supporting element

17 impeller circumference

18 production wells

19, 20 = cover disk

21 conveyor grooves

22 compensation holes

23 impeller entry

DLA = outer diameter of radial wheel 2

DLRI = inner diameter impeller space 6

Claims

claims

1. Feed pump with a variable-speed drive (5) for a metered-generating flow rate, the feed pump as a single-stage centrifugal pump with in a impeller space (6) of a pump housing (1) without a sealing gap rotatingly arranged radial wheel (2) centrifugal design for conveying a fluid between a pump inlet (4) and a pump outlet (13) is formed, the radial wheel (2) with a variable speed up to the five-digit range of revolutions per minute

Drive motor is connected, the radial wheel (2) is flowed in the middle, with delivery channels (3) and an outer diameter up to 50 mm, wherein for use in a process plant with continuous flow rates, the centrifugal pump is designed for a part-load operation whose Flow rates in the range of 0 ml / min to 3600 ml / min and at delivery heights of 20 m to 300 m are that an inner diameter (D _L RI) from the impeller space (6) is formed a maximum of 4% greater than an outer diameter (DLA) of Radial wheel (2) that between the impeller space (6) and the radial wheel (2) and / or its shaft (10) a seal (9) is arranged and that the impeller space (6) at the periphery with one or more, acute or tangential to Radialradaußen- diameter arranged pump outlet channels (13) is provided.

2. Feed pump according to claim 1, characterized in that the pump housing (1) with a radial wheel (2) arranged therein in the region between a pump inlet (4) and a pump outlet (13) whose cross-sectional areas defined by contact surfaces of lines to be connected thereto are, has a residual volume equal to or less than 50 milliliters.

3. Feed pump according to claim 1 or 2, characterized in that the pump housing (1) with a tempering device (7 - 7.3) is provided.

4. Feed pump according to claim 3, characterized in that the temperature-regulating device (7) is designed as a heat exchanger and the fluid-contacted

Parts of the pump housing (1) and / or the impeller space (6) completely or partially surrounds.

5. Feed pump according to one or more of claims 1 to 4, characterized in that liquid-tight connections penetrate the tempering (7) and connect a system with the impeller space (6).

6. Feed pump according to one or more of claims 1 to 5, characterized in that the radial wheel (2) has at least two conveying channels (3) and at Radialradaußendurchmesser (DLA) a plurality of conveying recesses (18) are arranged.

7. Feed pump according to claim 6, characterized in that on the radial wheel (2) the conveying recesses (18) are designed as blind holes, pockets or tooth-shaped recesses.

8. Feed pump according to claim 6 or 7, characterized in that the conveying channels (3) are designed as open recesses in the form of blade channels, grooves or grooves.

9. Feed pump according to one of claims 1 to 8, characterized in that suction and / or pressure-side impeller cover discs are provided with known conveying grooves.

10. Feed pump according to one of claims 1 to 9, characterized in that the number and the arrangement of the inlet openings of the conveying channels (3) of the radial wheel (2) does not increase a Radialradeintrittsdurchmesser.

11. Feed pump according to one of claims 1 to 10, characterized in that a hermetically sealed, magnetically coupled drive transmits a torque to the radial wheel (2).

12. Feed pump according to one of claims 1 to 11, characterized in that an electric, pneumatic or hydraulic drive with the radial wheel (2) is connected.

13. Feed pump according to one or more of claims 1 to 12, characterized in that the drive motor (5) on the pump (1) or tempering (7) is fixed and with a guided thereby shaft (4) with the radial wheel (2 ) connected is.

14. Feed pump according to one or more of claims 1 to 12, characterized in that a thermal barrier between the drive motor (5) and the tempering device (7) and / or pump housing (1) is arranged and the drive motor (5) via a shaft ( 4) is connected to the radial wheel (2).

15. Feed pump according to one or more of claims 1 to 14, characterized in that connecting zones between the parts of the pump housing (1) and the tempering device (7) are designed rotationally symmetrical and sealed from each other.

16. Feed pump according to one or more of claims 1 to 15, characterized in that a control device is connected to an internal or external volume flow measurement and independent of a back pressure of a system with the drive motor (5) generates an adjustable constant volumetric flow.

17. Feed pump according to one or more of claims 1 to 16, characterized in that in the switching or control range between minimum and maximum flow rate a variable speed range of the drive motor (5) generates a quantity factor up to the value 5000.

18. Feed pump according to one or more of claims 1 to 17, characterized in that in the speed range of the drive motor (5) from 0 to 35,000 revolutions / min a centrifugal pump delivery pressure between 0 to 30 bar.

19. Feed pump according to one or more of claims 1 to 18, characterized in that radial wheel (2) and housing of the centrifugal pump is designed for an extreme continuous partial load operation.

20. Feed pump according to one or more of claims 1 to 19, characterized in that pumps, drive motor, switching or control device and associated electronic control, measuring and control elements are combined to form a module capable of assembly.