BACKGROUND AND SUMMARY OF THE INVENTION
[0001] The present invention relates generally to rotary piston vacuum pumps and, more particularly,
to such pumps having antisuckback features which cut off the flow of lubricant from
the stopped pump into the low pressure operating chamber.
[0002] In rotary mechanical vacuum pumps, oil flow about working elements thereof serves
to lubricate and provide clearance sealant between elements. In such rotary vacuum
pumps without forced oil circulation, the quantity of oil flow from the oil reservoir
to the internal pump mechanism is largely a function of the pressure differential
between these two areas. Maximum oil flow circulation occurs when the oil reservoir
is at its normal atmospheric pressure and the pump is operating at its lowest pump
inlet absolute pressure. At higher suction pressures, the oil flow is reduced; indeed,
in the inlet pressure range over 500 mmHga, there is no appreciable oil flow into
the pump mechanism. Thus, operating time in this pressure range must be limited. Extended
operation without oil flow will cause poor lubrication and overheating and can lead
to pump failure.
[0003] To solve this problem and provide for extended operation time over a wide pressure
range, an oil pump may be added in the oil circuit of a mechanical vacuum pump to
provide a forced oil flow throughout the operating pressure range of the vacuum pump.
In a compound (two stage) mechanical vacuum pump, the oil pump is typically added
in the oil circuit of the second or roughing stage, while the first or high vacuum
stage oil flow is induced by the small pressure differential and gravity. Further,
interstage degassed oil is typically recirculated in a separate and independent oil
circuit through the first stage pumping chamber because atmospheric pressure oil often
contains air which, if released in the first stage, would drastically decrease net
pump capacity.
[0004] When the vacuum pump operation ceases, each pumping chamber therein may be at a different
pressure. For example, in a two stage rotary piston pump the first stage, being in
communication with the operating chamber or low pressure chamber being evacuated at
the pump inlet, is at a relatively low pressure as compared with the pressure in the
second stage, being in communication with the pump outlet through the discharge separator.
The presence of this differential pressure between pumping chambers often results
in the lubricating and sealing oil seeping or flowing back between working elements
into the first pumping chamber. In vacuum pumps employing independent oil circuits,
this seepage or back flow typically contaminates the degassed oil supply of the first
pumping chamber. Also, as the oil flows back through the pump inlet, the operating
chamber is contaminated. Further, even if the differential pressure between chambers
is not sufficient to cause oil flow between chambers, if the vacuum pump is stopped
at low pumping chamber pressures, oil in the lubrication circuit for that pumping
chamber may also draw back into the pumping chamber. This often results, again, in
pumping chamber flooding and operating chamber contamination.
[0005] Prior vacuum pumps have been equipped with devices to stop the oil flow into the
pumping chambers or stages when the vacuum pump is stopped under vacuum or low pressure
conditions in the pumping chamber. These devices attempt to avoid flooding the pump
chamber and, in turn, oil flowing back through the pump inlet system and to contaminate
any operating chamber attached thereto. By preventing oil flooding of the pump, problems
associated with starting of a flooded pump are also eliminated. The method and/or
device for preventing flow of oil back into the inlet system is typically called an
"antisuckback" device. Previous oil backflow prevention devices have included solenoid
valves or centrifugally operated mechanisms having, for example, resilient elastomer
plunger seals which shut-off oil flow into the stopped pump. However, these devices
are relatively expensive and may lack a high level of responsiveness to sudden changes
in pump operation. These so-called antisuckback devices are commonly incorporated
in oil sealed rotary vane vacuum pumps.
[0006] Another technique to prevent oil suckback into the vacuum system has been to use
an inlet line isolation valve in combination with an atmospheric vent. This valve
is closed before stopping the vacuum pump and a small solenoid valve, located at the
pump suction side of the isolation valve and electrically connected to the pump motor,
will open the atmospheric vent to admit atmospheric air or, if necessary, discharged
gas from the air/oil separator housing to the pump interior when the pump is stopped.
This method, however, does not completely prevent flooding of the pump cylinder and
some sort of oil line shut-off device is still desirable. Also, it is difficult to
attain complete sealing at very low inlet line pressures. Typical seals that are strong
enough to withstand repeated use are usually not flexible enough to seal tightly at
low pressures. It is thus often necessary to provide elaborate sealing means in order
to prevent air leakage along this inlet line when the isolation valve is closed.
[0007] For some applications these previous antisuckback techniques perform adequately even
if some small amount of oil does leak back. However,- in manufacturing semiconductor
chips and microprocessor devices, vacuum pumps are often required to achieve very
low pressures (on the order of .5 to 1.5 mmHga) and remain completely uncontaminated
by oil back flow through the vacuum pump inlet and into the semiconductor operating
chambers. Thus, the need has arisen for an inexpensive, highly reliable antisuckback
device.
[0008] It is therefore an object of the present invention to provide an inexpensive, highly
reliable antisuckback device for vacuum pumps.
[0009] Another object is the provision of improved antisuckback devices for rotary piston
pumps having hydraulically actuated control valves for simultaneously controlling
lubricant flow and pumping chamber pressure relief.
[0010] A further object is to provide an improved, hydraulically controlled antisuckback
device for compound or multi-stage vacuum pumps having an inlet line shut-off valve
seal sufficient to prevent leakage past that valve at low pressures.
[0011] Still another object is the provision of a means of achieving pressure equalization
in the pump chamber after stopping the vacuum pump and further preventing backflow
of lubricant thereto and into the operating chamber by means of a highly responsive
shut-off valve in the working fluid inlet flow path.
[0012] These and other objects of the present invention are achieved by the provision of
a shaft lip seal as an inlet shut-off valve seal in the working fluid inlet line of
a rotary piston pump between the first pumping chamber of the vacuum pump and the
inlet to the operating chamber. A piston valve is provided, having an axially inclined
radial face, for engaging this seal and cutting off flow therebetween even under low
pressures. This piston valve is actuated into sealing engagement with the shaft lip
seal when operation of the vacuum pump ceases and a pressure relief vent is connected
to the first pumping chamber.
[0013] An arrangement for connecting a pressure relief vent to the first pumping chamber
when the vacuum pump is stopped is provided by an oil pump in the lubricating oil
circuit, a pressure relief vent connected to the pumping chamber from a higher pressure
source, and biased valve connected between the oil pump and the oil circuit as well
as between the pressure relief vent and the first pumping chamber for controlling
the flow of oil and pressure, respectively. The oil pump pressurizes the oil in the
oil lubrication circuit as a function of vacuum pump operation. The valve is responsive
to the oil pressure created by the oil pump. The valve is actuated to maintain the
free flow of oil from the oil pump to the oil circuit when the vacuum pump is operating.
When the vacuum pump is shut-off, the bias of the valve shuts off the flow of oil
through the oil circuit and opens the connection between the pressure relief vent
and the first pumping chamber to increase the pressure in the latter such that lubricating
oil is not drawn into that pumping chamber. This increased pressure from the pressure
relief vent actuates an inlet shut-off valve which isolates the first pressure chamber
from the operating chamber.
[0014] In multistage rotary vacuum pumps with several independent oil circuits, the valve
arrangement of the present invention can simultaneously control oil flow in a plurality
of those oil circuits. Pressurized oil from a single oil circuit provides the control
signal to actuate the valve arrangement. Thus, only that oil circuit requires an oil
pump. The pressure relief vent, connected tc at least The first pumping chamber, is
also controlled by the valve arrangement. The valve arrangement may include either
a single slide valve intersecting each oil circuit and pressure relief path to the
pumping chambers or multiple slide valves each intersecting one or more oil circuit
and/or pressure relief paths. When the vacuum pump stops, the valve arrangement responds
to the oil pressure drop in the oil circuit providing its control signal to prevent
oil flow to at least the first pumping chamber and simultaneously permit pressure
relief to that pumping chamber.
[0015] Other objects, advantages and novel features of the present invention will become
apparent from the following detailed description of the invention when considered
in conjunction with the accompanying drawings.
BRIEF DESCRIPTION OF THE DRAWINGS
[0016]
Figure 1 is a partial cross-sectional view along the drive shaft of a vacuum pump
embodying the present invention.
Figure 2 is a partial cross-sectional view. coplanar with and enlarging a portion
of Figure 1 showing specific features of the antisuckback device according to the
present invention when the vacuum pump is operating.
Figure 3 is a partial cross-sectional view of the same portion shown in Figure 2 when
the vacuum pump has been stopped.
Figure 4 is a partial cross-sectional view of another vacuum pump showing an alternative
embodiment of the present invention when the vacuum pump is in operation.
Figure 5 shows a partial cross-sectional view of the same portion of the pump shown
in Figure 4 when vacuum pump operation has been stopped.
[0017] For comparative purposes, it should be noted that the cross-sectional views of Figures
4 and 5 are on planes generally perpendicular to the planes of the cross-sectional
views of Figures 1, 2 and 3.
[0018] Figure 6 shows a partial cross-sectional view of an enlarged portion of Figure 4
illustrating in detail the inlet shut-off valve arrangement of the present invention
without the flow lines past inlet shut-off valve 220.
DETAILED DESCRIPTION OF THE DRAWINGS
[0019] Figure 1, which illustrates a preferred embodiment of the present invention, shows
a partial cross-sectional view of a two-stage rotary pump 10 having a housing 15 with
first and second pumping chambers 20 and 25, respectively, therein. Drive shaft 30
is mounted through first and second pumping chambers 20 and 25, and is supported by
housing 15.
[0020] First and second pumping chambers 20 and 25 are each provided with an independent
oil circuit to lubricate operating elements within that chamber and seal clearances
between relatively moving members. With respect to first pumping chamber 20, the oil
circuit employs degassed oil from reservoir 35. Degassed oil flows out of reservoir
35 along line 37 to valve member 50 (shown in Figures 2 and 3 and discussed in detail
herein below) at portion A. From there degassed fluid flow continues to line 41 directly
to first pumping chamber 20 or to line 39 within drive shaft 30 to outlet ports 43
within first pumping chamber 20. The rotating and reciprocating action of the piston
pump (not shown) of first pumping chamber 20 results in the return flow of degassed
oil to reservoir 35.
[0021] The oil circuit of second pumping chamber 25 includes oil reservoir 45. Oil flows
from that reservoir through line 47 and then to valve 50 at portion A. Oil flow returns
along line 49 from valve 50 to drive shaft 30 at bearing 32. Oil flows along drive
shaft 30 to second pumping chamber 25 and is carried by pumping action therein to
reservoir 45 and, through conduit 81, to discharge separator 80. Discharge separator
80 passes the vacuum pump working fluid, typically air, to the vacuum pump atmospheric
outlet (not shown) and returns oil carried thereby to reservoir 45 through conduit
81. Discharge separator 80 is also provided with a pressure relief vent line 82 for
providing a flow of working fluid back to valve 50.
[0022] Briefly, the present invention provides means for preventing excess oil flow into
the pumping chambers when the vacuum pump has been stopped. This is accomplished by
a hydraulically responsive valve arrangement which both interrupts the oil circuit
and equalizes the pressures within the pumping chambers when vacuum pump operation
ceases. More specifically, in the exemplary two stage vacuum pump 10 of Figure 1,
oil from both reservoirs 35 and 45 is prevented from flowing into first and second
pumping chambers 20 and 25 when hydraulic control signals to valve 50 indicate the
vacuum pump has stopped. At the same time, valve 50 permits the flow of discharged
working fluid through line 82 to first pumping chamber 20 to provide pressure relief.
Thus, when the vacuum pump has stopped, valve 50 permits pressure equalization between
first and second pumping chambers 20 and 25, respectively. The hydraulic control signals
applied to valve 50 result from pressurization of oil by oil pump 70 from reservoir
45 only. Oil pump 70 operates in response to operation of vacuum pump 10.
[0023] By simultaneously cutting off oil circulation in both oil circuits and equalizing
the pressure in pumping chambers 20 and 25, oil is prevented from flowing into those
chambers, from both the oil supply of each pumping chamber and the oil supply of the
adjacent pumping chamber, when operation of vacuum pump 10 is stopped. Using oil pressure
to provide the hydraulic control signals of the present invention assures quick and
accurate responsiveness of valve 50 to the cessation of operation of vacuum pump 10.
[0024] Figure 2 shows a partial cross-sectional view enlarging that portion of Figure 1
designated by "A". The position of valve 50 in Figure 2 is shown for when vacuum pump
10 is operating. This figure may be compared with a similar cross-sectional view of
Figure 3 illustrating the position of valve 50 when the vacuum pump has been stopped.
[0025] As shown in Figure 2, valve 50 is, for example, a slide valve movable along bore
56, biased upwardly by spring 52. Valve 50 is actuated downwardly by oil pressure
in bore chamber 54 to oppose the spring bias of spring 52. An oil pump 70 is provided
as, for example, a gear pump driven by extension 72 of drive shaft 30 past sealing
means 34 and having gear members 74. Oil from reservoir 45 incoming on line 47 is
pressurized by the pumping action of oil pump 70, and, when vacuum pump 10 is in operation,
then flows along line 76 to sealing line 78 and input line 62 to bore chamber 54 of
valve 50.
[0026] Degassed oil from reservoir 35 flows along line 37 to valve 50 and is not subject
to pumping pressurization. This degassed oil flows through the degassed oil circuit
only as a result of gravitational and pressure differential forces. Incoming degassed
oil on line 37 passes through control valve 50 along line 58 when vacuum pump 10 is
operating. Degassed oil from line 58 exits bore 56 to input ports 36 of drive shaft
30. This oil then flows along line 39 within drive shaft 30 to outlet ports 43 or
along line 41 directly to first pumping chamber 20.
[0027] Pressure relief vent line 82 from discharge separator 80 reaches valve 50 through
line 64. Line 68 communicates with pumping chamber 20. During operation of vacuum
pump 10, valve 50 blocks communication between lines 64 and 68. Pressurized oil from
line 78 forms an oil seal at recess 60 on valve 50 between lines 64 and 68 to prevent
leakage to first pumping chamber ?0 from pressure relief line 82.
[0028] When vacuum pump 10 is operating, drive shaft 30 drives oil pump 70 to pressurize
the oil in the oil circuit of second pumping chamber 25. When vacuum pump 10 is not
operating, oil pump 70 is not operating and does not pressurize that oil and, thus,
oil pressure in chamber 54 does not overcome the spring bias of spring 52. Valve 50
will then move upwardly into bore chamber 54, as illustrated in Figure 3.
[0029] When valve 50 moves upwardly past the inlet to line 49, oil flow from reservoir 45
and line 62 to line 49 back to second pumping chamber 25 will be restricted and cut
off. Simultaneously, the inlet to line 58 will move upwardly past the outlet of line
37 and oil flow from reservoir 35 and line 37 to lines 39 and 41 back to first pumping
chamber 20 will be restricted and cut off. This same upward movement of valve 50 will
cause the outlet of line 64 to align with the inlet of line 66 and, simultaneously,
the outlet of line 66 to align with the inlet of line 68, permitting pressure relief
to flow from discharge separator 80 to first pumping chamber 20. Thus, as valve 50
cuts off oil flow in both of the oil circuits to pumping chambers 20 and 25, it opens
up pressure relief flow to increase the pressure in first pumping chamber 20 and equalize
the pressure between pumping chambers 20 and 25. By this arrangement oil flowback
or seepage into either of the pumping chambers from either or both oil circuits is
prevented when vacuum pump 10 is not operating.
[0030] When vacuum pump 10 resumes operation, oil pump 70 also resumes operation and will
again pressurize oil in chamber 54. This causes valve 50 to move downwardly from bore
chamber 54 against the bias of spring 52. Thereby, oil flow between lines 62 and 49
to second pumping chamber 25 and between lines 37, 58, and 39 and 41 to first pumping
chamber 20 is permitted. Simultaneously, communication between lines 64, 66 and 68
from discharge separator 80 to first pumping chamber 20 is restricted and cut off.
Likewise, high pressure oil communication from line 78 will be resumed with recess
60 and, thus, the oil seal between lines 64 and 68 will be reestablished when vacuum
pump 10 resumes operation.
[0031] Figures 4 and 5 show partial cross-sectional views of another rotary piston vacuum
pump 110 having therein an alternative embodiment of the present invention. Figure
4 shows the location of the various antisuckback elements of the present invention
when vacuum pump 110 is in operation. Figure 5 shows the location of the same elements
when vacuum pump 110 has been stopped. In comparison with Figures 1, 2 and 3, Figures
4 and 5 are cross-sectional views along planes generally perpendicular to the views
of Figures 1, 2 and 3. Again, vacuum pump 110 may be a two chamber pump having separate
oil circuits for each chamber and be similar to vacuum pump 10 in all other respects
except those shown and described herein with respect to Figures 4 and 5.
[0032] As illustrated in Figures 4 and 5, vacuum pump 110 includes housing 115, discharge
separator 180, and first and second pumping chambers (not shown). Each pumping chamber
includes an oil circuit associated therewith as in the embodiment of Figure 1. Each
oil circuit includes an oil reservoir and oil lines extending to and from the antisuckback
features of the present invention shown in Figures 4 and 5.
[0033] This embodiment also provides antisuckback capabilities. Instead of controlling oil
circuit flow to both pumping chambers and pressure relief and equalization between
pumping chambers by a single valve, vacuum pump 110 includes a plurality of valves.
Valve 250 controls pressure relief to the first pumping chamber and equalization of
pressure between pumping chambers. This valve also controls the flow of control signal
oil to valve 150 which controls the flow of lubricating oil in both of the independent
lubricating oil circuits. Again, the valves are hydraulically actuated by oil pressure
from an oil pump responsive to operation of vacuum pump 110. Valves 150 and 250 are,
for example, biased by springs 152 and 252 and slidably disposed in bores 156 and
256, respectively. Bore chambers 154 and 254 are provided at the end of valves 150
and 250 which are opposite from springs 152 and 252, respectively. Thus, pressurized
oil supplied to bore chambers 154 and 254 may overcome the biasing effect of springs
152 and 252, respectively, and cause valves 150 and 250 to be activated.
[0034] Oil from the second pumping chamber flows through line 147 to oil pump 170 having
pump gears 174. Oil pump 170 supplies pressurized oil along line 176 to bore chamber
254 of valve 250. Valve 250 is biased downwardly toward bore chamber 254 by spring
252. As shown in Figure 4, when vacuum pump 110 is operating, oil pump 170 supplies
an oil pressure to bore chamber 254 which exceeds the biasing force of spring 252
and causes valve 250 to slide upwardly out of bore chamber 254, permitting oil flow
to line 162 and then to bore chamber 154.
[0035] Valve 250 includes valve element 255 at the end opposite bore chamber 254. Bore 256
includes valve seat 257 about the outlet of line 164 to valve 250. Bore 256 also includes
outlet port 258 through a side wall of bore 256. Valve 250, for example, is illustrated
as having a hollow portion interiorly of valve element 255. Line 164 receives pressure
relief from discharge separator 180 along pressure relief vent 182. As shown in Figure
4, when valve 250 is forced up out of bore chamber 254 by oil pressure, valve element
255 covers the outlet of line 164 and seats against valve seat 257 to cut off pressure
relief air flow through line 164 past valve element 255 and through outlet port 258
to line 168 and to the first pumping chamber. The pressure relief path to the first
pumping chamber extends through a portion of bore 254 and then through outlet port
258 to line 168 to inlet .shut-off valve 220. The pressure relief path continues past
valve 220 and into first pumping chamber inlet 240. However, when vacuum pump 110
is operating, inlet shut-off valve 220 rests against stop 222, at least partially
blocking this relief pressure path.
[0036] When oil pressure causes valve 250 to move out of bore chamber 254, communication
with line 162 is opened up and oil flows along line 162 to bore chamber 154 of valve
150. Valve 150 is biased upwardly toward bore chamber 154 by spring 152. As in valve
50 of Figures 2 and 3, valve 150 includes central degassed oil line 158 which may
be aligned with lines 137 and 161 to permit degassed oil flow therethrough from the
degassed oil reservoir of the first pumping chamber (not shown) to the first pumping
chamber, through interior line 139 of the drive shaft (not shown). This alignment
will result when vacuum pump 110 is operating and oil pressure in bore chamber 154
from line 176, bore 254, and line 162 causes valve 150 to slide downwardly in bore
156 to overcome the bias of spring 152, as shown in Figure 4. At the same time, valve
150 opens up communication with line 149, leading to the second pumping chamber (not
shown), such that oil from line 162 may flow through bore chamber 154 to line 149
and the second pumping chamber.
[0037] Therefore, when vacuum pump 110 is in operation, oil pump 170 is supplying pressurized
oil to bore chambers 254 and 154, sequentially in the oil circuit of the second pumping
chamber. This oil pressure causes valve 250 to cut off pressure relief from line 164
to the first pumping chamber by closing valve element 255 against valve seat 257 and
opening inlet shut-off valve 220. Likewise, the oil pressure causes valve 150 to permit
oil flow to lines 139 and 149 leading to first and second pumping chambers, respectively.
Again, the oil pressure of only a single oil circuit (that of the second pumping chamber)
is employed to provide hydraulic control signals actuating valve 150 to control oil
flow through multiple oil circuits.
[0038] When, as illustrated in Figure 5, operation of vacuum pump 110 has ceased, oil pump
170 is also inoperative and does not supply pressurized oil flow through line 174
to valve 250 to overcome the spring bias of spring 252. Valve 250 then slides downwardly
into bore chamber 254. Thus, valve element 255 disengages from valve seat 257 and
permits pressure relief flow from discharge separator 180 through pressure relief
vent line 182 and line 164 into bore 256 of valve 250 to line 168 and then to inlet
shut-off valve 220.
[0039] The pressure from discharge separator 180 is typically at a higher pressure than
the pressure within the first pumping chamber. Thus, as the air flow continues from
valve 250 through line 168 to inlet shut-off valve 220, the differential pressure
lifts inlet shut-off valve 220 off stop 222 and forces valve face 225 of inlet shut-off
valve 220 to seat against inlet valve seal 230. This restricts pressure relief flow
back through inlet filter 210 and vacuum pump inlet 200 to the operating chamber (not
shown). As inlet shut-off valve 220 is so actuated, relief pressure flow follows the
working fluid path of vacuum pump 110 through first pumping chamber inlet 240 to the
first pumping chamber. This results in an increase of the pressure within that pumping
chamber and creates a pressure equilibrium between the first and second pumping chambers.
[0040] When vacuum pump 110 is not operating, valve 250 cuts off the flow of oil from lines
147 and 176 to line 162 and bore chamber 154. Thus, pressurized oil is not available
to act on valve 150 to overcome the bias of spring 152. Valve 150 then slides upwardly
into bore chamber 154, restricting and cutting off oil flow between bore chamber 154
and line 149 to the second pumping chamber as well as between lines 137, 158 and 139
to the first pumping chamber. Thus, the supply of oil available to be drawn into the
pumping chambers by either low pressure or pressure differential is restricted. In
combination with pressure relief to eliminate low pressure and pressure differential
conditions, no significant back flow or oil flooding will result.
[0041] Since, when vacuum pump 110 is not operating, oil back flow and flooding of pumping
chambers is effectively prevented, contamination of the operating environment of the
operating vacuum chamber is significantly reduced. Actuation of inlet shut-off valve
220 further assures that no such contamination will result from lubricating oil in
vacuum pump 110. When vacuum pump 110 resumes operation, oil pump 170 will resume
operation and again pressurize the oil flow to cause valve 250 to shut-off the pressure
relief flow to inlet shut-off valve 220. As the pressure in the first pumping chamber
drops, valve face 225 of inlet shut-off valve 220 will be unseated from valve seal
230 and drop to stop 222, permitting working fluid flow to resume from the operating
vacuum chamber to pump 110.
[0042] Figure 6 shows an enlarged, partial cross-sectional view of the portion of Figure
4 illustrating the inlet shut-off valve arrangement of the present invention without
the presence of the flow lines of working fluid flow into the first pumping chamber
past inlet shut-off valve 220 shown in Figure 4. Inlet shut-off valve 220, is, for
example, a piston-like valve slidable within support 224 and cylindrical about centerline
axis 300. Inlet shut-off valve 220 includes annular flange 227 extending radially
therefrom about centerline axis 300. Support 224 includes stop 222 which limits movement
of inlet shut-off valve 220 downwardly toward first pumping chamber inlet 240 by engagement
with one side of flange 227. Valve face 225 is formed on flange 227 as an axially
inclined surface on an otherwise radial face.
[0043] When inlet shut-off valve 220 is actuated, as shown in Figure 4, valve face 225 is
forced upwardly into sealing engagement with valve seal 230 by the flow of relief
pressure through line 168 and into the first pumping chamber. This sealing engagement
is then maintained by the differential pressure between the operating chamber and
the first pumping chamber as long as vacuum pump 110 is not operating. Valve seal
230 comprises a shaft lip seal element normally employed to seal rotating drive shafts
against grease or oil or working fluid flow. Shaft lip seals per se are standard,
commercially available items. As conventionally employed, shaft lip seals are continuously
radially compressed by the rotating shaft extending therethrough. However, in the
present invention the shaft lip seal is employed to provide an axially resilient diametral
seal against a valve face plate.
[0044] The exemplary shaft lip seal included in valve seal 230 includes cantilevered seal
232, formed, for example, from a viton elastomer, extending in the direction of centerline
axis 300 to form inner lip 236 supported by spring ring 234. The apex of inner lip
236 is significantly thinner than the rest of cantilevered seal 232. Spring ring 234
is formed, for example, from stainless steel. An example of a commercially available
shaft lip seal suitable for use in the present invention is Chicago Rawhide part number
9982. The surface of valve face 225 which sealingly engages inner lip 236 may, for
example, be formed from polished steel.
[0045] When valve face 225 and valve seal 230 are brought into engagement by actuation of
inlet shut-off valve 220, the unique structure of the shaft lip seal permits fluid
tight sealing over a wide range of pressures, including even very low pressures, within
the operating chamber. This tight sealing results from the relative thinness of inner
lip 236 which provides it with considerably greater flexibility than the rest of cantilevered
seal 232. This flexibility permits greater conformity to the surface of valve face
225 while the use of otherwise hard seating viton elastomer assures the valve seal
of strength and greater operating lifetime. Since valve seal 230 is formed from a
readily available commercial part, expensive, specially adapted valve seals are not
necessary. The inlet valve shut-off seal arrangement of the present invention provides
considerable improvement over conventional flat elastomer seals in terms of durability
and leakage prevention against both working fluid and lubricant. The present invention
combines the advantages of hard elastomer seats and soft elastomer seats in a single,
unique and inexpensive construction.
[0046] Although the present invention has been described above with respect to oil flow
and air pressure relief, it should be clearly understood that these embodiments are
merely exemplary. The present invention contemplates the use of any other suitable
lubricant besides oil to hydraulically actuate the valve arrangement controlling lubricant
flow and pressure relief. Any other suitable fluid besides air, such as a chemically
inert gas or liquid, may be employed for pressure relief to the pumping chambers when
the vacuum pump is not operating. Also, the pressure relief vent need not be connected
to the discharge separator. In some applications it may be permissible to have the
pressure relief vent in communication with another pressure source. This other pressure
source may, for example, be an air vent to atmospheric pressure. In some applications
of the present invention a different fluid, besides expelled working fluid, may be
employed for pressure relief.
[0047] Further, the pressure relief to the first pumping chamber need not be exactly equal
to the pressure within the second pumping chamber. It is only necessary that this
pressure relief be at least substantial. By this it is meant that the pressure relief
should be at least sufficient to reduce the pressure differential, in combination
with the lubricant flow restrictions, to prevent lubricant flow between pumping chambers
and, in particular, into the first pumping chamber.
[0048] From the preceding description of the preferred embodiments, it is evident that the
objects of the invention are attained, and although the invention has been described
and illustrated in detail, it is to be clearly understood that the same is by way
of illustration and example only and is not to be taken by way of limitation. The
spirit and scope of the invention are to be limited only by the terms of the appended
claims.