This invention relates to a condensate pump, and more particularly to a condensate pump that is switched through piston action rather than with a spring mechanism and seated valves.
Many industrial applications produce steam, employ the steam in a process or apparatus, and condense the steam back to water. The condensate water is typically recycled back to the steam production in a closed cycle, rather than being discharged. The recycling of the condensate is undertaken because the water may be treated with expensive chemicals that would be lost if the water were discharged, because the discharge of the water could have adverse environmental consequences, and because the heat of the hot water would be lost if it were discarded.
To recycle the condensate, it is accumulated in a condensate reservoir and pumped back to the boiler under pressure. Condensate water enters the reservoir until the reservoir is nearly full, and then the condensate is pumped out of the reservoir by a compressed gas such as steam or compressed air. At the completion of the pump-out when the liquid level is low, the reservoir is vented, and the accumulation process repeats.
A number of different approaches have been utilized for the pump used in conjunction with the condensate reservoir. Historically and in the majority of current applications, a centrifugal pump is used. More recently, the steam-pumping trap has been introduced. The steam-pumping trap typically employs a spring-loaded overcenter or other type of mechanism to open and close the pressure and vent valves in coordination with a float that senses the liquid level in the reservoir. The valves use a plug-and-seat configuration. While operable, such designs have associated high fabrication and maintenance costs. Additionally, the sizes of the pressure and vent ports are limited. Because of the large forces required to operate the mechanism, the float must be relatively large in size.
There is a need for an improved approach to the construction of the condensate pump that overcomes these limitations. The present invention fulfills this need, and further provides related advantages.
The present invention provides a pump that may be used for condensate pumping. No high-fabrication and high-maintenance spring-loaded mechanism is used, reducing both the initial and maintenance costs. The sizes of the ports that may be used are larger than those used with conventional plug-and-seat valves, allowing faster cycling times and/or a larger condensate reservoir than possible with conventional pumps. The size of the float that is the preferred liquid-level sensor is reduced.
In accordance with the invention, a condensate pump comprises a condensate reservoir having a fluid inlet, an inlet check valve operable to prevent a flow of fluid out of the condensate reservoir through the fluid inlet and to allow a flow of fluid into the condensate reservoir through the fluid inlet, a fluid outlet, and an outlet check valve operable to prevent a flow of fluid into the condensate reservoir through the fluid outlet and to allow a flow of fluid out of the condensate reservoir through the fluid outlet. A liquid level sensor is operable to sense a liquid level within the condensate reservoir. A pressure/vent valve comprises a pressure source, a pressure vent, and a three-way valve preferably including a secondary piston that is slidably supported in a secondary cylinder. The secondary piston slides in the secondary cylinder responsive to the liquid level sensor, between a first secondary-piston position wherein the pressure source is in communication with a gas space of the condensate reservoir and the pressure vent is isolated from the gas space, and a second secondary-piston position wherein the pressure source is isolated from the gas space and the pressure vent is in communication with the gas space. Preferably, the secondary piston is double ended with a spool configuration. The pressure/vent valve may be located exterior to the condensate reservoir or within the condensate reservoir, but is preferably located exterior to the condensate reservoir for ease of installation and maintenance.
In one embodiment, a reservoir pressurization line extends from the pressure source to a first intermediate position of the secondary cylinder, a reservoir vent line extends from the vent to a second intermediate location of the secondary cylinder, and a pressurization/vent line extends from a third intermediate location of the secondary cylinder to the gas space of the condensate reservoir.
The secondary piston operates responsive to the liquid level sensor, preferably responsive to a movement of the liquid level sensor. The responsive movement is preferably accomplished through a primary piston slidably supported in a primary cylinder. The primary piston slides in the primary cylinder responsive to the liquid level sensor, between a first primary-piston position and a second primary-piston position. The secondary piston slides in the secondary cylinder responsive to the movement of the primary piston. Preferably, the liquid level sensor comprises a float within the condensate reservoir, and an actuating arm connected to the float and movable with the float. The actuating arm is connected to the primary piston. In this embodiment, there is preferably a main pressure drive line extending from the pressure source to an intermediate location of the primary cylinder, a first branch pressure drive line extending from a first intermediate location of the primary cylinder to a first end of the secondary cylinder, and a second branch pressure drive line extending from a second intermediate location of the primary cylinder to a second end of the secondary cylinder.
In a most preferred embodiment, a condensate pump comprises a condensate reservoir having a fluid inlet, an inlet check valve operable to prevent a flow of fluid out of the condensate reservoir through the fluid inlet and to allow a flow of fluid into the condensate reservoir through the fluid inlet, a fluid outlet, and an outlet check valve operable to prevent a flow of fluid into the condensate reservoir through the fluid outlet and to allow a flow of fluid out of the condensate reservoir through the fluid outlet. A liquid level sensor is operable to sense a liquid level within the condensate reservoir. The liquid level sensor comprises a float within the condensate reservoir, and an actuating arm connected to the float and movable with the float. A pressure/vent valve is located exterior to the condensate reservoir and comprises a pressure source and a pressure vent. The pressure/vent valve includes a primary piston slidably supported in a primary cylinder. The primary piston is double ended in a primary-piston spool configuration. The primary piston slides in the primary cylinder responsive to the liquid level sensor, between a first primary-piston position and a second primary-piston position. The actuating arm is connected to the primary piston. The pressure/vent valve further includes a secondary piston slidably supported in a secondary cylinder, wherein the secondary piston is double ended in a secondary piston spool configuration. The secondary piston slides in the secondary cylinder between a first secondary-piston position wherein the pressure source is in communication with a gas space of the condensate reservoir and the pressure vent is isolated from the gas space, and a second secondary-piston position wherein the pressure source is isolated from the gas space and the pressure vent is in communication with the gas space. A drive pressurization structure includes a main pressure drive line extending from the pressure source to an intermediate location of the primary cylinder, a first branch pressure drive line extending from a first intermediate location of the primary cylinder to a first end of the secondary cylinder, and a second branch pressure drive line extending from a second intermediate location of the primary cylinder to a second end of the secondary cylinder. A reservoir pressurization/vent structure includes a reservoir pressurization line extending from the pressure source to a first intermediate location of the secondary cylinder, a reservoir vent line extending from the vent to a second intermediate location of the secondary cylinder, and a pressurization/vent line extending from a third intermediate location of the secondary cylinder to the gas space of the condensate reservoir.
The condensate pump of the invention is readily constructed, and is reliable and readily maintained in service. The gas-flow structure of the present design may be implemented in a cast-block configuration, for low cost. Because pressure and vent connections are made with pistons rather than plug-and-seat type valves, the pressure and vent gas-flow channels may be made large so that they have high flow rates.
Other features and advantages of the present invention will be apparent from the following more detailed description of the preferred embodiment, taken in conjunction with the accompanying drawings, which illustrate, by way of example, the principles of the invention. The scope of the invention is not, however, limited to this preferred embodiment.
A liquid level sensor 40 is operable to sense a liquid level 42 within the condensate reservoir 30.
The condensate pump 26 further includes a pressure/vent valve 54. In the first embodiment of
The pressure/vent valve 54 includes a pressure source 56 and a pressure vent 58 to atmosphere. The pressure source 56 may be of any operable type, but is preferably the pressurized steam 28 shown in
The pressure/vent valve 54 has a primary piston 60 that is slidably supported in a primary cylinder 62. The primary piston 60 is of any operable configuration, but is preferably double ended in a primary-piston spool configuration, with a central recess 61 extending along a portion of the length of the primary piston 60, as shown in the drawings. The primary piston 60 slides in the primary cylinder 62 responsive to the liquid level sensor 40, between a first (upper, see
The pressure/vent valve 54 further comprises a three-way valve 67 that preferably includes a secondary piston 68 slidably supported in a secondary cylinder 70. The secondary piston is of any operable configuration, but is preferably symmetrically double ended in a secondary piston spool configuration, with two central recesses 72 extending along portions of the length of the secondary piston 68 and three rings 73 defining the central recesses 72, as shown in the drawings. The secondary piston 68 slides in the secondary cylinder 70 between a first (right, see
A drive pressurization structure 80 causes the secondary piston 68 to move responsive to the movement of the primary piston 60, which in turn moves responsive to the liquid level sensor 40. The drive pressurization structure 80 includes a main pressure drive line 82 extending from the pressure source 56 to an intermediate location 84 between the ends of the primary cylinder 62, and in communication with the central recess 61 of the primary piston 60. A first branch pressure drive line 86 extends from a first intermediate location 88 of the primary cylinder 62 to a first end 90 of the secondary cylinder 70. A second branch pressure drive line 92 extends from a second intermediate location 94 of the primary cylinder 62 to a second end 96 of the secondary cylinder 70.
In operation, when the liquid level 42 is at its high point (
A reservoir pressurization/vent structure 98 alternatively pressurizes and vents the gas space 76 of the condensate reservoir 30, responsive to the movement of the secondary piston 68. The reservoir pressurization/vent structure 98 includes a reservoir pressurization line 100 extending from the pressure source 56 to a first intermediate location 102 of the secondary cylinder 70. A reservoir vent line 104 extends from the vent 58 to a second intermediate location 106 of the secondary cylinder 70. A pressurization/vent line 108 extends from a third intermediate location 110 of the secondary cylinder 70 to the gas space 76 of the condensate reservoir 30.
In operation, when the secondary piston 68 is in its right position (
As the condensate is discharged, step 122, the liquid level 42 drops so that the primary piston 60 moves downwardly in the primary cylinder 62. As the primary piston 60 moves through the midpoint of the primary cylinder 62, both the first branch pressure drive line 86 and the second branch pressure drive line 92 are blocked, leading to balanced pressure at both ends 90, 96 of the secondary cylinder 70. Consequently, the secondary piston 68 does not move. The inlet check valve 34 prevents pressure from being reduced by gas flow out of the fluid inlet 32.
When the liquid level 42 reaches its low-water level, step 124, as depicted in
The liquid level 42 rises and the condensate reservoir 30 is gradually filled, step 126. The primary piston 60 moves through its midpoint, blocking both the first branch pressure drive line 86 and the second branch pressure drive line 92, producing a balanced pressure on the secondary piston 68 so that it does not move. When the liquid level 42 reaches its high-water level (
Although a particular embodiment of the invention has been described in detail for purposes of illustration, various modifications and enhancements may be made without departing from the spirit and scope of the invention. Accordingly, the invention is not to be limited except as by the appended claims.