The invention relates generally to pumps used in chromatography systems. More specifically, the invention relates to fluidic outlet or exit ports of a pump actuator.
Liquid chromatography is an example of a field of applications wherein a pumping system takes in solvents and delivers a liquid solvent composition at elevated pressures to a sample manager, where a sample awaits injection into the mixture. Conventionally, high performance liquid chromatography (HPLC) employs pressures ranging between approximately 1,000 and 6,000 psi. Pressures for performing ultra performance liquid chromatography (UPLC) may reach 15,000 to 20,000 psi. The pumping systems can vary in configuration, typically employing two or more actuators, configured to cooperate in series or in parallel.
During a liquid chromatography run, an important factor for chromatographic performance is for the unswept volume within an actuator to be minimal. Unswept volume is preferably considered to be that section or volume of solvent that remains undelivered in the course of a given piston stroke. In many conventional pumps, an actuator's outlet port intersects the piston chamber. Any cavity within the actuator in fluidic communication with this chamber, but generally unperturbed by the piston stroke, can become a region of unswept volume. This unswept volume can decrease the efficiency of the pump and degrade the chromatography results. It can also impede priming of the pump head. In addition, any cavity situated physically higher than the outlet can become a bubble trap. Unswept bubble traps can also pose a problem to chromatography performance.
Aspects of the invention features liquid chromatography systems, pumps, and actuators comprising a pump head having a chamber, a gland, a movable rod extending through the gland into the chamber of the pump head, and a plunger seal disposed in the gland around the rod for sealing against fluidic leakage from the chamber. The plunger seal has an annular flange that provides an OD (outer diameter) seal against the gland. The flange defines a seal cavity. The pump head further includes an outlet port and an outlet channel. One end of the outlet channel is in communication with the outlet port and the other end of the outlet channel opens into the seal cavity of the plunger seal. The outlet channel provides a flow path for liquid in the chamber to travel towards the outlet port in response to movement of the rod.
The above and further advantages of this invention may be better understood by referring to the following description in conjunction with the accompanying drawings, in which like numerals indicate like structural elements and features in various figures. The drawings are not necessarily to scale, emphasis instead being placed upon illustrating the principles of the invention.
Pumps and actuators described herein can be employed in high-pressure reciprocating and rotary applications, such as are commonly used in liquid chromatography. In some embodiments, the pumps and actuators include a fluidic assembly having a pump head coupled to a wash housing, a gland in either the pump head or washing housing, and a high-pressure seal assembly disposed within the gland. The pump head has an inlet port and an outlet port, each port being in fluidic communication with a chamber. Movement of a plunger within the chamber draws liquid into the chamber through the input port and pumps the liquid out of the chamber through an output port.
The input port intersects the chamber at one end, whereas the fluidic path from the chamber to the outlet port traverses a seal cavity. The seal cavity is an open region of the plunger seal disposed at the chamber's other end and facing the chamber. From the seal cavity, the fluidic path passes through an outlet channel that connects to the outlet port. The outlet channel extends through the pump head and opens into the gland at a place located strategically to facilitate the purging of gas bubbles and particles from the seal assembly and the gland. The location is strategically placed at a relatively high point in the seal cavity to which gas bubbles can escape. In addition, the location has the outlet channel situated almost as physically far away as possible from where the inlet port intersects the far end of the chamber, thus ensuring almost a complete sweep of the chamber length when liquid flows out of the pump head. Advantages stemming from the outlet channel location, in comparison to conventional actuators with an outlet port that intersects the chamber, are lower unswept volumes, improved purging of unwanted bubbles and particles, and improved priming of the pump.
Although described herein with respect to actuators, the principles of the invention extend to any type of pump with a pump head, for example, gear pump drives, parallel pumps, serial pumps.
The fluidic assembly 14 includes a pump head 24 and a wash housing 26, and is secured to the other side of the support plate 22, opposite the main actuator body 12. The pump head 24 also has a recess 28 at one end adapted to receive and align the wash housing 26. A pressure transducer 30 is secured to the other end of the pump head 24, which allows monitoring of the internal pressure of the pump head 24 throughout the operation of the actuator 10.
The pump head 24 includes a chamber 32, a pump-head abutment surface 36, a plunger seal 38, and a wash seal 40. The plunger 20 extends through the support plate 22, wash seal 40, wash housing 26, and plunger seal 38 into the chamber 32 of the pump head 24. The wash housing 26 provides a compartment 37 (
The pump head 24 further includes an inlet port 50 and an outlet port 52 through which to receive and discharge liquids, respectively. The inlet port joins the chamber 32 at the chamber's remote end, whereas the outlet port is in fluidic communication with the chamber's other end through a seal cavity of the plunger seal 38.
In one embodiment, the actuator 10 is one of two independently controllable actuators of a binary solvent manager (BSM) pump that cooperate to deliver a pressurized solvent composition to the downstream components of a liquid chromatography system. The two actuators, called the primary actuator and the accumulator actuator, are configured serially. The primary actuator is the low-pressure side of the pump, where liquid intake from solvent reservoirs occurs at atmospheric pressure during the pump cycle. Liquid intake occurs in response to a backstroke of the plunger of primary actuator within the chamber. In response to a forward stroke of its plunger within the chamber, the primary actuator pressurizes and transfers the solvent to the accumulator actuator and system. Closure of an inlet check valve (not shown) ensures expulsion of the pressurized liquid from the chamber through outlet port, rather than out the inlet port. The accumulator actuator is the high-pressure side of the pump, maintaining the solvent at system pressure during the intake and transfer operations performed by the primary actuator. While the primary actuator intakes liquid, the accumulator actuator delivers solvent at system pressure, and while the primary actuator transfers liquid, the accumulator actuator intakes and receives the liquid at system pressure for the next delivery cycle. An example implementation of a BSM pump is the ACQUITY UPLC Binary Solvent Manager, manufactured by Waters Corp. of Milford, Mass.
In this embodiment, the outlet port 52 opens at the top of the pump head 24. Although shown to open at the top, the outlet port 52 can open anywhere on the circumference of the pump head 24, provided it is in communication with the seal cavity 60 of the plunger seal 38. Preferably, the primary outlet channel 54 that brings the outlet port 52 into communication with the seal cavity 60 opens near the top of the seal cavity 60. Being near the highest point in the seal cavity, this location is near where any gas bubbles in the pumped liquid would be expected to rise and collect. Liquid pumped from the seal cavity into the primary outlet channel 54 thus carries with it any gas bubbles that may have collected at the mouth of the primary outlet channel 54.
In other embodiments, the outlet channel 54 can connect to the seal cavity 60 at other locations (e.g., alongside, slightly above, slightly below, or below the axis of the chamber 32). Although such embodiments may not be as effective purging gas bubbles as the embodiment having the outlet channel at the top, notwithstanding, these other embodiments may reduce the amount of unswept volume when compared to pump heads that have the outlet port intersect the chamber directly. In addition, preferably the outlet channel 54 is horizontal within the pump head 24, an orientation that facilitates machining of the outlet channel 54 feature. Notwithstanding, the outlet channel 54 can be machined at other angles, for example, sloping upwards towards the outlet port 52, such that the angle between the outlet port 52 (or the secondary outlet channel 58) and the primary outlet channel 54 is greater than 90 degrees and downstream is at a higher point than upstream (the terms downstream and upstream being used with respect to the direction of solvent flow, which flows from upstream to downstream). In addition, depending on the location of the outlet port 52, the outlet channel 54 can even angle downward or sideways away from the chamber 32, instead of running parallel to the chamber.
The other end of the outlet channel 54 opens into the seal cavity 60 near a highest point 64 in the seal cavity 60 to which a gas bubble in the liquid can rise. The highest point 64 is adjacent where an outer flange 66 of the plunger seal 38 produces an annular face seal 68 against the surface of the pump head 24.
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While the invention has been shown and described with reference to specific preferred embodiments, it should be understood by those skilled in the art that various changes in form and detail may be made therein without departing from the spirit and scope of the invention as defined by the following claims. For example, although described herein primarily with respect to high-pressure reciprocating applications, the various embodiments of actuator assemblies can also be used in low-pressure reciprocating and rotary applications and in high-pressure rotary applications.
This application claims the benefit of and priority to co-pending U.S. provisional application No. 61/451,229, filed Mar. 10, 2011, titled “Seal Assemblies for Reciprocating and Rotary Applications,” and to co-pending U.S. provisional application No. 61/478,705, filed Apr. 25, 2011, titled “Pump Head Outlet Port,” the entireties of which applications are incorporated by reference herein.
Filing Document | Filing Date | Country | Kind | 371c Date |
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PCT/US2012/028408 | 3/9/2012 | WO | 00 | 8/16/2013 |
Number | Date | Country | |
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61451229 | Mar 2011 | US | |
61478705 | Apr 2011 | US |