BACKGROUND OF THE INVENTION
Field of the Invention:
[0001] The present invention relates to a positive displacement type liquid-delivery apparatus
that can be used to deliver a very small amount of liquid at a constant rate to various
processing apparatuses such as a chemical vapor deposition apparatus. Description
of the Related Arts:
[0002] Recently, in the semiconductor manufacturing industry, the integration of integrated
circuits has been improved remarkably, and the research and development activities
of DRAM are being intensively carried out in anticipation of gigabit order DRAMs which
will replace current megabit order DRAMs. The capacitor element having a large capacity
per unit area is needed to produce such DRAMs. As a dielectric thin-film material
for producing elements having such a large capacity per unit area, a metallic oxide
film material such as tantalum pentaoxide (Ta
2O
5) having dielectric constant of approximately 20, or barium titanate (BaTiO
3) or strontium titanate (SrTiO
3) or barium strontium titanate having dielectric constant of approximately 300 is
considered to be a promising thin-film material.
[0003] To deposit such a metallic oxide film material on a substrate in a vapor phase, a
gaseous mixture made by mixing one or more gas feed materials of organometallic compounds
and an oxygen containing gas is ejected to a substrate heated to a certain temperature.
Organometallic gaseous feed material is chosen by the nature of the thin film to be
produced. For example, a metallic oxide film comprised by barium strontium titanate
is produced by first converting Ba, Sr, Ti or their compounds into their dipivaloylmethane
(DPM) compounds, and dissolving these compounds in an organic solvent such as tetrahydrofuran
(THF) to produce respective liquid feed materials. After uniformly mixing these liquid
feed materials in a required proportion to produce a master liquid feed, such master
liquid feed is sent to a vaporizer to produce a gaseous feed for use in the chemical
vapor deposition apparatus.
[0004] Such master liquid feed is extremely susceptible to degradation even in a sealed
container, and therefore it is undesirable to have such a master liquid feed stagnate
inside delivery piping. The master liquid feed is especially susceptible to producing
precipitate particles, by being heated or being exposed to air, which tend to produce
inferior quality films. Therefore, once the component liquids are mixed into a master
liquid feed, it is necessary that the master liquid feed be maintained in a stable
condition. It is also desirable that the master liquid feed be completely used up
as quickly as practicable. Furthermore, it is desirable that the film deposition apparatus
be capable of exercising a fine control of the flow rate of the master liquid feed
over a wide range of flow rates from a very small flow rate to a large flow rate.
Therefore, the liquid-delivering apparatus should be capable of providing a stringent
control of the flow rates of the liquid feed.
[0005] As a positive displacement type liquid-delivering apparatus used in these applications,
there has been known such an apparatus in which a mass flow controller (MFC) is provided
in the piping connecting a feed liquid tank and a processing apparatus such as a vaporizer,
and the feed liquid tank is pressurized with gas or the like to deliver liquid and
a control valve on the MFC is adjusted to control a delivery rate of liquid. Positive
displacement pumps incorporating pistons, diaphragms, and the like are also used.
[0006] In general, conventional apparatuses using a mass flow controller have a poor reproducibility
of flow control near the lower limit of the allowable control range. Moreover, when
the pressure in the processing apparatus increases, a pressure exceeding the pressure
in the processing apparatus must be applied to the feed liquid tank side. Hence, a
large amount of gas used for pressurizing is dissolved in the liquid in the feed liquid
tank, and this dissolved gas is released downstream of the control valve of the mass
flow controller or causes surge or pulsation in the flow of the liquid feed.
[0007] Although a positive displacement pump can overcome these drawbacks, a piston pump
cannot be used because the sliding parts of the pump generate particles that contaminate
the liquid. The positive displacement pumps employing bellows or diaphragms do not
contaminate the liquid, but present the following problems.
[0008] It is conceivable to construct such a positive displacement pump in which a container
is partitioned by a diaphragm into two chambers, i.e., a liquid delivery chamber and
a working fluid chamber, and an incompressible liquid is used as a working fluid.
With this construction, the diaphragm moves according to the amount of the working
fluid supplied to the working fluid chamber for thereby discharging liquid from the
container. Therefore, the precision in controlling the flow rate is more or less dependent
on the precision of the external driving system. As a result, an external device is
required for pumping the working fluid, and hence troublesome handling of the working
fluid is necessary and the overall apparatus becomes large-sized.
[0009] If a driving device for driving the diaphragm is constructed mechanically, then these
problems are eliminated and the overall apparatus becomes simple. However, it is very
difficult to control the movement of the diaphragm so as to keep the deliver liquid
at a constant rate if the processing conditions (pressure) in the secondary side (downstream
side) of the container vary. Installing a flow meter in the secondary side of the
container for performing feedback control, it is not possible to obtain a better performance
than that of the mass flow controller, because a precision and reproducibility of
the flow meter is the same level as the mass flow controller.
[0010] When the liquid-delivery is stopped, the pressure in the secondary side of the positive
displacement pump slowly decreases due to a small leak in the check valve provided
in the primary side (upstream side) of the processing apparatus (the part to which
liquid is supplied). This may lead to a pressure drop when the liquid-delivery resumes,
requiring time to stabilize the flow rate of liquid and potentially causing other
problems. For example, if the pressure in the processing apparatus is below atmospheric
pressure, the liquid feed may be vaporized because the pressure in the primary side
of the check valve drops below the vapor pressure of the liquid feed.
[0011] Further, in the positive displacement pump, pressure variations occur in piping in
the secondary side of the pump when the pumping operation begins, and hence the flow
rate of liquid cannot be controlled until the liquid-delivery is stabilized. If a
plurality of liquid feeds are required to be delivered at the same ratio, for example,
these liquid feeds cannot be used until the liquid-delivery is stabilized.
SUMMARY OF THE INVENTION
[0012] In view of the foregoing, it is an object of the present invention to provide a positive
displacement type liquid-delivery apparatus employing a positive displacement pump
with a flexible diaphragm which can supply liquid at a constant rate with high precision
and high reproducibility, shorten the time required to stabilize the liquid-delivery
from starting of pumping operation, and control the flow rate of liquid immediately
after the pumping operation begins.
[0013] According to an aspect of the present invention, there is provided a positive displacement
liquid-delivery apparatus comprising: a positive displacement pump comprising a housing
having a liquid-delivery chamber divided by a flexible diaphragm and a diaphragm driving
unit linked to the diaphragm to discharge fluid from the liquid-delivery chamber;
and a differential pressure control unit for controlling the differential pressure
between both sides of the diaphragm at a constant value during the pumping process.
[0014] Accordingly, the construction of the apparatus is simplified because the diaphragm
is driven directly by the diaphragm driving unit. Further, by keeping the differential
pressure between both sides of the diaphragm at a constant value, it is possible to
keep the diaphragm at a constant amount of deformation, thus eliminating error caused
by the diaphragm deformation. Hence, the diaphragm driving unit can control the amount
of deformation in the diaphragm to perform precise flow rate control.
[0015] In a preferred aspect of the present invention, the differential pressure control
unit comprises a differential pressure sensor for detecting the differential pressure
between both sides of the diaphragm, and a control valve for controlling the flow
rate of the liquid discharged from the liquid-delivery chamber on a basis of a signal
from the differential pressure sensor. In other words, the differential pressure of
the diaphragm is controlled so as to be constant, thus causing the flow rate of liquid
to be controlled indirectly.
[0016] Accordingly, it is possible to adjust the pressure in the liquid-delivery chamber
indirectly by adjusting the control valve. If there is sufficiently low pressure variation,
the space on the opposite side of the diaphragm from the liquid-delivery chamber,
such as atmospheric pressure, the pressure sensor is required to be used only the
space on the side facing the liquid-delivery chamber.
[0017] In this case, a predetermined amount of liquid is not exactly delivered at the secondary
side of the diaphragm in accordance with the moving distance of the diaphragm. In
a strict sense, when the differential pressure of the both sides of the diaphragm
varies, the amount of deformation of the diaphragm varies in accordance with the differential
pressure, and hence the delivery amount of liquid is deviated from the predetermined
amount of liquid. Therefore, it is necessary to control the differential pressure
of the diaphragm at a constant value. For example, if the relationship between the
position of the diaphragm and the amount of delivery liquid at a predetermined differential
pressure is found, and the differential pressure of the diaphragm is controlled so
as to be equal to the predetermined differential pressure when it is actually used,
then the amount of delivery liquid corresponds to the amount of deformation of the
diaphragm at the differential pressure. Since the amount of delivery liquid is estimated
from the relationship between the position of the diaphragm and the differential pressure,
a predetermined amount of delivery liquid can be exactly obtained.
[0018] In a preferred aspect of the present invention, a flow sensor is disposed on a discharge
path and control is performed based on a signal from the flow sensor when the pressure
in the liquid-delivery chamber during the pumping process exceeds a prescribed value
or the absolute value of the rate of pressure variations exceeds a prescribed value.
[0019] With this construction, precise control can be preformed even with severe variations
in the system conditions.
[0020] In a preferred aspect of the present invention, the liquid-delivery chamber is arranged
so as to achieve the required discharge flow volume of the fluid in one stroke.
[0021] With this construction, the bellows operation is always stable and uniform for each
process, thereby avoiding pressure and flow rate variations, for example, that occur
when switching valves in alternate operations. Performing one pump operation using
only a portion of one stroke can further increase the life of the bellows.
[0022] In this case, the required discharge flow volume of the fluid is such volume that
a predetermined film is formed on one substrate (semiconductor wafer) in one stroke,
or more than such volume.
[0023] In a preferred aspect of the present invention, the gas is employed to pressurize
the space on the opposite side of the diaphragm from the liquid-delivery chamber.
[0024] Generally speaking, the diaphragm itself has an allowable differential pressure between
the both sides of the bellows. When this differential pressure is small or the pressure
required in the processing apparatus on the secondary side of the pump is larger than
the allowable differential pressure, liquid-delivery cannot be performed if the pressure
on the side of the diaphragm opposite from the liquid-delivery is atmospheric pressure.
However, it is possible to keep the differential pressure low by pressurizing this
side opposite the liquid-delivery chamber with a gas in order to maintain the differential
pressure within the tolerable level for pumping operations.
[0025] When the gas is charged, the pressure at the primary side of the diaphragm fluctuates.
However, in such a condition, it is desirable to make the differential pressure of
the diaphragm constant by the control valve.
[0026] Since the differential pressure of the diaphragm must be maintained at a constant
value as described above in order to supply the fluid at a constant flow rate, the
gas pressure P must also be constant. In the example described above, the volume V
on the side of the diaphragm opposite the liquid-delivery chamber varies during pumping
operations. Accordingly, the side of the diaphragm opposite the liquid-delivery chamber
should be supplied with an amount of gas based on the liquid-delivery amount ΔV, that
is, ΔV × P.
[0027] The method of controlling the differential pressure both sides of the diaphragm can
be applied for using the pressure of the gas and the liquid, and controlling the pressure
on the gas side. However, the injection and discharge of gas requires some time, resulting
in control delays when pressure variations occur abruptly. Hence, variations in the
differential pressure may occur more frequently, making it difficult to maintain a
prescribed amount of liquid. Still, this method may be suitable for processes that
have no severe pressure variations.
[0028] A leak sensor can be provided in the space opposite the liquid-delivery chamber for
detecting fluid leaking caused by breakage in the diaphragm. With this arrangement,
breakage in the diaphragm can be detected. If the side opposite the liquid-delivery
chamber is also filled with liquid for driving the diaphragm, it is extremely difficult
to detect breakage in the diaphragm. In the event that the diaphragm breaks, liquid
for driving the diaphragm is mixed with the liquid to be pumped and the mixture is
pumped together. Since the amount of liquid discharged from the apparatus does not
vary, the breakage cannot be detected on a flow rate monitor.
[0029] In the present invention, however, breakage in the diaphragm can be detected by providing
a relief discharge port, for example, on the gas side of the diaphragm and a relief
sensor in the relief discharge port or on the secondary side. Further, it is possible
to prevent gas from mixing with the pump side by always keeping the gas side at a
lower pressure than the pump side. Hence, the present invention can avoid the problem
of pumping liquid that mixes with driving liquid when the diaphragm breaks. Such problem
is common to conventional apparatus with fluid-driven diaphragms.
[0030] In a preferred aspect of the present invention, a plurality of positive displacement
pumps is arranged in parallel and delivering different kinds of fluid to a single
processing unit.
[0031] In a preferred aspect of the present invention, two positive displacement pumps are
delivering the same kind of fluid, and alternately delivering the fluid to a single
processing unit in a continuous manner.
[0032] In a preferred aspect of the present invention, a housing having a liquid-delivery
chamber is divided by a flexible diaphragm and a diaphragm driving unit linked to
said diaphragm to discharge fluid from said liquid-delivery chamber; and said diaphragm
driving unit drives said diaphragm to maintain the flow rate of said liquid discharged
from said liquid-delivery chamber at a constant rate based on the variation of the
differential pressure between both sides of the diaphragm.
[0033] In a preferred aspect of the present invention, the liquid-delivery chamber is arranged
so as to achieve the required discharge flow volume of the fluid in one stroke.
[0034] In a preferred aspect of the present invention, the gas is employed to pressurize
the space on the opposite side of the diaphragm from the liquid-delivery chamber.
[0035] In a preferred aspect of the present invention, a plurality of positive displacement
pumps is arranged in parallel and delivering different kinds of fluid to a single
processing unit.
[0036] In a preferred aspect of the present invention, two positive displacement pumps are
delivering the same kind of fluid, and alternately delivering said fluid to a single
processing unit in a continuous manner.
[0037] According to an aspect of the present invention, there is provided a positive displacement
liquid-delivery apparatus comprising: a positive displacement pump comprising a housing
having a liquid-delivery chamber divided by a flexible diaphragm and a diaphragm driving
unit linked to the diaphragm to discharge fluid from the liquid-delivery chamber;
and an discharge path extending from the liquid-delivery chamber; a check valve disposed
on the discharge path; and a pressure control unit for controlling the primary side
pressure of the check valve so as not to drop below the vapor pressure of the fluid
discharged from the liquid-delivery chamber during stoppage of the pumping process.
[0038] With this construction, it is possible to prevent a drop in pressure on the primary
side of the check valve caused by a leak from the check valve and the generation of
voids caused by vaporization.
[0039] In a preferred aspect of the present invention, the pressure control unit comprises
a control valve disposed upstream of the check valve, and regulates the pressure in
the liquid-delivery chamber during pump stoppage at the pressure required for pumping
operation.
[0040] With this construction, if the pipe connecting the check valve and control valve
is sufficiently short and formed of a highly rigid material and there is almost no
volume expansion in this section of pipe when its internal pressure rises at the beginning
of the pumping process, it is possible to set the pressure in the secondary side of
the check valve to the normal pressure for pumping immediately after pumping begins
in order to pump a prescribed flow rate without any time lag.
[0041] In a preferred aspect of the present invention, the pressure control unit comprises
a control valve disposed upstream of the check valve, and regulates the pressure in
the liquid-delivery chamber during pump stoppage at the pressure higher than the pressure
required for pumping operation by an amount equivalent to the estimated amount caused
by the volume expansion of the piping between the check valve and control valve.
[0042] With this construction, if this section of pipe is a flexible pipe with low rigidity
and there is volume expansion in the pipe when the pressure rises at the beginning
of the pumping process, it is possible to set the pressure in the secondary side of
the check valve to the normal pressure for pumping immediately after pumping begins
in order to pump a prescribed flow rate without any time lag.
[0043] In a preferred aspect of the present invention, the liquid-delivery chamber is arranged
so as to achieve the required discharge flow volume of the fluid in one stroke.
[0044] In a preferred aspect of the present invention, the gas is employed to pressurize
the space on the opposite side of the diaphragm from the liquid-delivery chamber.
[0045] In a preferred aspect of the present invention, a plurality of positive displacement
pumps is arranged in parallel and delivering different kinds of fluid to a single
processing unit.
[0046] With this construction, the apparatus can individually control a different flow rate
of fluid discharged from each positive displacement pump from the moment the pumping
process begins, thereby always pumping the same proportion of fluids to the single
process device.
[0047] In a preferred aspect of the present invention, two positive displacement pumps delivering
the same kind of fluid, and alternately delivering the fluid to a single processing
unit in a continuous manner.
[0048] With this construction, it is possible to operate both pumps alternately such that
the first pump gradually pumps a larger flow rate after the start of operations and
the second pump gradually pumps a decreasing amount in order that the overall flow
rate does not change. Accordingly, the same liquid can be supplied continuously to
the single process device without variation in flow.
[0049] According to an aspect of the present invention, there is provided a deposition apparatus
comprising: a vaporizer for vaporizing a fluid feed supplied from the positive displacement
liquid-delivery apparatus; and a deposition chamber in which thin films are deposited
using the feed gas supplied from the vaporizer.
[0050] The above and other objects, features, and advantages of the present invention will
become apparent from the following description when taken in conjunction with the
accompanying drawings which illustrate preferred embodiments of the present invention
by way of example.
BRIEF DESCRIPTION OF THE DRAWINGS
[0051] FIG. 1 is a schematic view showing a positive displacement type liquid-delivery apparatus
according to a first embodiment of the present invention;
[0052] FIG. 2 is an enlarged view showing part of the positive displacement type liquid-delivery
apparatus of FIG. 4;
[0053] FIG. 3 is a schematic view showing a positive displacement liquid-delivery apparatus
according to a second embodiment of the present invention;
[0054] FIG. 4 is a graph showing the relationship between the pressure in the liquid delivery
chamber and deformation of the bellows according to the second embodiment of the present
invention;
[0055] FIG. 5 is a schematic view showing a positive displacement type liquid-delivery apparatus
according to a third embodiment of the present invention;
[0056] FIG. 6 is an enlarged cross-sectional view showing part of the positive displacement
type liquid-delivery apparatus of FIG. 5;
[0057] FIG. 7 is a schematic view showing a positive displacement type liquid-delivery apparatus
according to a fourth embodiment of the present invention;
[0058] FIG. 8 is a graph showing the relationship between a flow rate and time at the beginning
of the pumping process in the apparatus of FIG. 7;
[0059] FIG. 9 is a schematic view showing a positive displacement type liquid-delivery apparatus
according to a fifth embodiment of the present invention;
[0060] FIG. 10 is a graph showing the relationship between a flow rate and time at the beginning
of the pumping process in the apparatus of FIG. 9;
[0061] FIG. 11 is a schematic view showing a positive displacement type liquid-delivery
apparatus according to a sixth embodiment of the present invention; and
[0062] FIG. 12 is a time chart for a control process performed by the positive displacement
type liquid-delivery apparatus of FIG. 11.
DESCRIPTION OF THE PREFERRED EMBODIMENTS
[0063] FIGS. 1 and 2 show a positive displacement liquid-delivery apparatus according to
a first embodiment of the present invention. In this positive displacement liquid-delivery
apparatus, a liquid feed tank 12 accommodates a liquid 14, such as a liquid feed.
A positive displacement pump 10 supplies the liquid 14 from the feed liquid tank 12
to a processing apparatus 16 at a prescribed amount. In this example, the processing
apparatus 16 is a vaporizer that supplies deposition gas via a gas supply line 86
to a CVD reaction chamber 80. A gas injection head 82 in the reaction chamber 80 ejects
the supplied deposition gas toward a semiconductor wafer W mounted on a base 84. The
positive displacement liquid-delivery apparatus shown in FIG. 1 also includes an exhaust
pump 88 and a vent line 90 for venting the deposition gas.
[0064] The positive displacement pump 10 includes a housing 22 that is approximately cylindrical
in shape. One end of the housing 22 is connected to an inlet pipe 18 extending from
the feed liquid tank 12, while the other end is connected to an outlet pipe 20 connected
to the processing apparatus 16. An opening is formed in the center of the bottom plate
of the housing 22. A bellows 24 (diaphragm) is attached to the inner edge of this
opening, and extends inwardly and concentrically with the housing 22. The other end
of the bellows 24 is hermetically closed by a retaining plate 26. This construction
of the housing 22 and bellows 24 forms a liquid-delivery chamber 28 capable of retaining
liquid hermetically and varying its capacity. A working space 30 which is open to
the air is also formed in the inner side of the bellows 24.
[0065] A diaphragm driving device 36 is provided in the working space 30. The diaphragm
driving device 36 includes a drive unit 32 having a drive source such as a motor (not
shown), and a rod 34 that moves up and down by actuation of the drive unit 32. The
retaining plate 26 is connected to the top end of the rod 34. The drive unit 32 is
provided with a conversion mechanism (not shown) for converting rotational movement
by the drive source into linear movement with a feed screw mechanism or the like.
When the drive unit 32 is operated, the bellows 24 extends and retracts in the axial
direction, thereby changing the capacity of the liquid-delivery chamber 28 to supply
a predetermined amount of liquid 14 to the processing apparatus 16.
[0066] A pressure gauge 38 is provided on the housing 22 for measuring the pressure inside
the liquid-delivery chamber 28. A control valve 40 capable of controlling its opening
degree is provided in the outlet pipe 20. A signal from the pressure gauge 38 is inputted
into the control valve 40. The opening degree of the control valve 40 is adjusted
based on the signal from the pressure gauge 38 to maintain the pressure P in the liquid-delivery
chamber 28 at a constant value that is slightly higher than the pressure P
0 in the working space 30 (atmospheric pressure in this example). The control valve
40 and the pressure gauge 38 constitute a differential pressure control unit 42.
[0067] A flow meter 44 is also provided at the upstream side of the control valve 40 in
the outlet pipe 20 for measuring the flow rate of liquid flowing in the outlet pipe
20. A signal from the flow meter 44 is also inputted into the control valve 40. Hence,
the flow meter 44 and the control valve 40 constitute a flow control unit 46 for controlling
the flow rate of liquid supplied to the processing apparatus 16 through the outlet
pipe 20.
[0068] With this construction, the positive displacement liquid-delivery apparatus can switch
selectively between control by the differential pressure control unit 42 and control
by the flow control unit 46. Normally, control by the differential pressure control
unit 42 is in operation, the control valve 40 is controlled on the basis of signal
from the pressure gauge 38 to maintain the differential pressure at a constant value
as described above (normal mode). With this control, the discharge flow rate can be
accurately and stably maintained.
[0069] This process will be described with reference to FIG. 2. If the bellows 24 is deformed
at a constant rate, then the discharge flow rate can be expressed by a function dependent
only on the stroke of the diaphragm driving device 36. If a certain flow rate of liquid
is being required, then changes in the stroke can be controlled so as to correspond
to such flow rate.
[0070] However, because the bellows 24 is flexible by nature, the bellows 24 is deformed
locally by a differential pressure ΔP between the pressure P in the liquid-delivery
chamber 28 and the pressure P
0 in the working space 30 ( ΔP = P - P
0), in addition to the deformation caused by tensile force from the retaining plate
26. The solid lines describing the bellows 24 in FIG. 2 represent the bellows 24 in
a state of equilibrium. If the pressure P in the liquid-delivery chamber 28 increases,
and thus the differential pressure ΔP increases, then the bellows 24 may deform as
shown by the chain double-dashed lines in FIG. 2. Hence, even if the position of the
retaining plate 26 does not change, the change in the differential pressure ΔP will
cause the capacity of the liquid-delivery chamber 28 to change.
[0071] By maintaining the differential pressure ΔP at a constant value while operating the
bellows 24, it is possible to achieve a stable flow rate control, because variations
or pulsations in the flow caused by random deformation of the bellows 24 are suppressed.
Accordingly, the position of the retaining plate 26 will correspond to the capacity
of the liquid-delivery chamber 28 on a one-on-one basis. Therefore, it is possible
to accurately control the discharge flow rate, which is dependent only on the stroke
of the diaphragm driving device 36.
[0072] In some cases, it is not possible to adjust the flow rate of liquid by simply monitoring
the differential pressure with the pressure gauge and controlling the stroke on the
basis of the differential pressure. In the pressure gauge that detects pressure by
sensing the amount of deformation in an internal diaphragm or the like, when pressure
variations are detected, the bellows have already deformed and a change in flow rate
has already occurred. In the present embodiment, therefore, when the pressure inside
the liquid-delivery chamber 28 exceeds a predetermined value, or the absolute value
of the rate of pressure change exceeds a predetermined value, it is determined that
the system is in a fluctuation state. At this time, control is switched from monitoring
the differential pressure with the pressure gauge 38 to monitoring the flow rate with
the flow rate meter 44. This specific arrangement enables the apparatus to maintain
a precise flow rate of liquid even under unstable conditions.
[0073] FIG. 3 shows a positive displacement liquid-delivery apparatus according to a second
embodiment of the present invention. The structure of the positive displacement liquid-delivery
apparatus of the second embodiment differs from that of the first embodiment in that
the differential pressure control unit 42 in the first embodiment is replaced with
a driving device control unit 50 that receives a signal from the pressure gauge 38
to control the movement of the diaphragm driving device 36.
[0074] In this embodiment, the relationship between the pressure in the liquid-delivery
chamber 28 and the amount of deformation of the bellows 24 is known in advance. The
driving device control unit 50 moves the diaphragm driving device 36 to cancel deformation
in the bellows 24 caused by pressure changes in the liquid-delivery chamber 28, thereby
keeping a flow rate of liquid at a constant value.
[0075] The actual discharge flow rate Q discharged from the liquid-delivery chamber 28 can
be defined by the following equation, where q is a set flow rate and V is the amount
of deformation in the bellows 24 caused by the pressure P in the liquid-delivery chamber
28.

Here,

Therefore,

If the relationship (dV/dP) is known in advance, the driving device control unit
50 controls the diaphragm driving device 36 to achieve a set flow rate q when the
initial set flow rate is q
0.

As a result, it is possible to maintain Q at a constant value.
[0076] As an example, in the case where the amount of deformation V in the bellows 24 and
the pressure P in the liquid-delivery chamber 28 have the following relationship,

Thus,

Here, if the relationship dV/dP = abP
b-1 is known in advance, then a constant flow rate can be achieved by calculating the
changes in pressure per unit time from the equation (2).
[0077] As shown in FIG. 4, it can be seen that the dV/dP relationship is of a direct proportion.
Therefore, the equation (2) can be simplified to:

Performing control based on this equation is relatively easy.
[0078] FIGS. 5 and 6 show a positive displacement liquid-delivery apparatus according to
a third embodiment of the present invention. In this embodiment, a positive displacement
pump 10a has a closed system, wherein the working space 30 is not open to the atmosphere.
That is, the bottom of the housing 22 is closed by a bottom plate 52. The bottom plate
52 has a through-hole 54 through which the rod 34 is inserted, an intake port 56 through
which N
2 gas or another pressure regulating gas is introduced, and an exhaust port 58 for
exhausting such gas in minute amounts. The bottom plate 52 is also provided with a
leak fluid tube 62 for discharging liquid that has leaked into the working space 30
and introducing the discharged liquid into a leak sensor 60. A seal mechanism 64 is
provided in the through-hole 54 to seal the rod 34 hermetically.
[0079] The intake port 56 is connected to a pressure regulating gas source (not shown) by
an intake tube 66. A pressure sensor 68 for detecting the pressure in the intake tube
66 (equivalent to the pressure in the working space) and a pressure control valve
70 for controlling the pressure in the intake tube 66 based on an output signal from
the pressure sensor 68 are provided in the intake tube 66. A regulating valve 74 is
provided in a line connected to the exhaust port 58 for adjusting a very small amount
of exhaust. By setting the opening degree of the regulating valve 74 to a certain
value and operating the pressure control valve 70 on the basis of the output signal
from the pressure sensor 68, it is possible to cancel variations in pressure due to
displacement of the bellows 24 and maintain the pressure P
1 in the working space 30 at a constant value. The pressure sensor 68 and the pressure
control valve 70 constitute a second differential pressure control unit 72.
[0080] Here, the flow rate from the pressure control valve 70 is defined as Q, the amount
of gas supplied from the pressure control valve 70 when the bellows 24 is stopped
is defined as Q
1, and the amount of gas discharged from the regulating valve 74 is defined as Q
2. Further, ΔV indicates the change in capacity caused by driving the bellows, and
ΔQ = P
1ΔV indicates the change in supplied gas followed by this capacity change Δ V. Accordingly,


If Q > 0 is not established, control becomes difficult, and hence the following conditions
are established.


Hence, Q
1 and Q
2 are set so that the following is established.

[0081] By employing the controlling method described above, it is possible to maintain a
flow rate of liquid at a desired value even when the delivery pressure of liquid increases
due to clogging in the processing apparatus 16 at the downstream side, for example.
It is also possible to perform a simple control process using only pressure regulating
gas with this construction. However, as in the example of the first embodiment, this
method would not be able to cope with abrupt changes in pressure.
[0082] In the event that the bellows 24 is damaged, and a hole or the like is formed in
the embodiment described above, liquid leaking through the bellows 24 flows through
the leak fluid tube 62 and reaches the leak sensor 60, where the leak will be detected.
Accordingly, an appropriate action such as a warning alarm or an automatic pump shutdown
procedure will be performed based on an output signal from this leak sensor 60 to
prevent an accident from occurring.
[0083] FIG. 7 shows a positive displacement type liquid-delivery apparatus according to
a fourth embodiment of the present invention. This apparatus includes a positive displacement
pump 10 having the same construction as that in the first embodiment, a check valve
100 provided in the outlet pipe 20 that extends from the positive displacement pump
10, and a delivery-liquid pressure sensor 102 for detecting the pressure in the primary
side of the check valve 100. The apparatus further includes a liquid-delivery chamber
pressure sensor 104 for detecting the pressure in the liquid-delivery chamber 28,
a control valve 106 disposed upstream of the check valve 100, and a pressure control
unit 108 that receives signals from the delivery-liquid pressure sensor 102 and the
liquid-delivery chamber pressure sensor 104 and controls the control valve 106 and
the drive unit 32 based on these signals. Therefore, the positive displacement type
liquid-delivery apparatus of the present embodiment individually controls the pressure
in the primary side of the check valve 100 and the pressure in the liquid-delivery
chamber 28.
[0084] During a stoppage of delivery liquid with the positive displacement type liquid-delivery
apparatus of the present embodiment, the pressure in the primary side of the check
valve 100, i.e., the pressure of liquid contained in a pipe 110 connecting the check
valve 100 and the control valve 106 is controlled to be less than the cracking pressure
of the check valve 100, and also controlled to be higher than the vapor pressure of
the liquid. Also, the pressure in the liquid-delivery chamber 28 is controlled to
be at the pressure required for normal pumping operations (hereinafter referred to
as operating pressure).
[0085] At this time, the pressure in the primary side of the check valve 100 is approximately
1.5 kg/cm
2 (≒ 147 kPa) when, for example, the cracking pressure is 2 kg/cm
2 (≒ 196 kPa) and the vapor pressure of the liquid therein is 0.5 kg/cm
2 (≒ 49 kPa). In addition, the pressure in the liquid-delivery chamber 28 is approximately
2.5 kg/cm
2 (≒ 245 kPa), for example, which is the same as the operating pressure.
[0086] Even if the pressure in the primary side of the check valve 100 drops due to a leak
in the check valve 100, this pressure is controlled so as to be prevented from dropping
below the vapor pressure of the liquid. This method includes the step of driving the
drive unit 32 to lower the pressure in the liquid-delivery chamber 28 to the initial
pressure in the primary side of the check valve 100, which is 1.5 kg/cm
2 ≒ 147 kPa) in one example (step 1), and the step of opening the control valve 106
(step 2). Next, the drive unit 32 is driven to set the pressure in the primary side
of the check valve 100 equivalent to its initial pressure (step 3), and the control
valve 106 is closed (step 4). Subsequently, the drive unit 32 is driven to raise the
pressure in the liquid-delivery chamber 28 to its initial pressure of 2.5 kg/cm
2 (≒245 kPa)(step 5).
[0087] If a pump drive signal is received during this operation, the entire system is put
on standby until the operation is completed. After completion of this operation, the
pump can be driven to control the entire system. This procedure will not cause a delay
in the process since it only takes 10-15 seconds to complete.
[0088] Lowering the pressure in the primary side of the check valve 100 greatly decreases
leaking of the check valve 100. Moreover, by preventing the pressure from dropping
below the vapor pressure of the liquid, it is possible to eliminate the generation
of voids in the pipe 110. It is also possible to prevent such a condition that a predetermined
flow rate of fluid cannot be discharged until the voids disappear and the pressure
of liquid exceeds, at least, the cracking pressure of the check valve 100.
[0089] It is desirable to set the pressure in the liquid-delivery chamber 28 to the same
pressure in the primary side of the check valve 100 in order to prevent leaking in
the check valve 100. However, it takes a considerable amount of time after starting
the pump to raise the pressure in the liquid delivery chamber 28 high enough to meet
the required flow rate. Therefore, by setting the pressure in the liquid-delivery
chamber 28 equivalent to that of the operating pressure, it is possible to discharge
the required flow of fluid immediately after the pumping operation begins, without
time lag.
[0090] Specifically, by delivering liquid under a constant pressure at all times immediately
after the pumping operation begins, as shown in FIG. 8, the flow rate of liquid is
allowed to be proportional to time when the flow rate is increasing, whereby a set
time t
s for the flow rate to reach a set flow rate Q
s is established and the flow rate can be strictly controlled in the set time t
s.
[0091] In this example, the pipe 110 connecting the check valve 100 and the control valve
106 is sufficiently short and constructed of a highly rigid material so that there
is almost no volume expansion in the pipe 110 even when the pressure therein rises
to the same pressure as that in the liquid-delivery chamber 28. Therefore, the pressure
in the secondary side of the check valve 100 can be maintained at the operating pressure
in order to achieve the required flow rate immediately after the pumping operation
begins. However, if a flexible tube or the like is used for the pipe 110, volume expansion
may occur in the pipe 110 when the pressure therein rises to the same pressure as
that in the liquid-delivery chamber 28. In this case, the pressure in the secondary
side of the check valve 100 can be set to the operating pressure immediately after
the pumping operation begins by setting the pressure in the liquid-delivery chamber
28 to the pressure (P + α), slightly higher than the pressure P during pumping operations,
where the pressure α is equivalent to the estimated amount caused by volume expansion
in the pipe 110.
[0092] FIG. 9 shows a positive displacement liquid-delivery apparatus according to the fifth
embodiment of the present invention. This apparatus comprises a plurality of positive
displacement pumps 10 with a similar construction as that in the first embodiment.
These positive displacement pumps 10 are arranged in parallel and each of the pumps
10 is capable of delivering liquid of a different type simultaneously to the processing
apparatus 16. In this example, the positive displacement liquid-delivery apparatus
includes a plurality of feed lines 112a-112d, wherein each feed line is connected
to a positive displacement pump 10 for delivery liquid feed A, B, C and D. These feed
lines 112a-112d are joined together in the secondary side of the check valve 100,
and then connected to the processing apparatus 16.
[0093] In the present embodiment, the positive displacement liquid-delivery apparatus controls
the pressure in the feed lines 112a-112d in the primary side of the check valve 100
so as not to drop below the vapor pressure of each of the liquid feeds flowing through
the respective feed lines 112a-112d. The apparatus also controls the pressure in the
liquid-delivery chamber 28 of each of the positive displacement pumps 10 at the operating
pressure or a pressure higher than the operating pressure by an amount α determined
by estimating the volume expansion in the pipes. Hence, by setting a constant set
time t
s for each of the liquid feeds A, B, C and D to reach a set flow rate Q
AS, Q
DS, Q
CS and Q
DS as shown in FIG. 10, at any arbitrary time t
0 within this set time t
s, the proportion of flows Q
AO, Q
BO, Q
CO and Q
DO for the liquid feeds A-D is equivalent to the proportion of set flows Q
AS-Q
DS (Q
A0 : Q
B0 : Q
C0 : Q
D0 = Q
AS : Q
BS : Q
CS : Q
DS). Hence, it is possible to control the total mixture ratio immediately after the
pumping process begins such that the fluid delivered to the processing apparatus 16
always has the same ratio of liquid feeds. This method eliminates such problem that
the liquid feeds cannot be used until the pumping operation is stabilized.
[0094] FIG. 11 shows a positive displacement liquid-delivery apparatus according to a sixth
embodiment of the present invention. This apparatus comprises two positive displacement
pumps 10 with a similar construction as that in the first embodiment. The two positive
displacement pumps 10 are arranged in parallel and driven to alternately pump the
same type of liquid to the processing apparatus 16. In other words, the outlet pipes
20 extending from the respective positive displacement pumps 10 and having respective
control valves 106 join together in the primary side of the check valve 100, and the
secondary side of the check valve 100 is connected to the processing apparatus 16.
[0095] An example of control conducted by the apparatus of the sixth embodiment will be
described with reference to FIG. 12. For purposes of explanation, the liquid-delivery
chamber 28 and the control valve 106 positioned on the right side of FIG. 11 will
be referred to as liquid-delivery chamber A and control valve A, respectively, while
those positioned on the left side of the diagram will be referred to as liquid-delivery
chamber B and control valve B, respectively.
[0096] While control valves A and B are both closed, the drive unit 32 of each of the positive
displacement pumps 10 is driven to bring the pressure in the chambers A and B to the
operating pressure (time 0-t
1). Based on a pump start signal, the control valve A is opened to discharge liquid
from the liquid-delivery chamber A (time t
2). After a predetermined interval elapses, the discharge flow rate from the liquid-delivery
chamber A is gradually decreased, while at the same time the control valve B is opened
to allow liquid to be discharged from the liquid-delivery chamber B. When the flow
rate of liquid discharged from the liquid-delivery chamber B reaches a set flow rate,
the control valve A is closed (time t
3-t
4). During this time, the flow rate from the pump that began pumping operation is gradually
increased, while the flow rate from the pump that is stopping pumping operation is
gradually decreased at the same rate such that the overall flow rate does not change.
By alternating operations between two pumps, the same amount of feed fluid can be
delivered continuously to the processing apparatus 16 without variation in the flow
rate.
[0097] After the liquid-delivery chamber A is aspirated (time t
5-t
6), the liquid-delivery chamber A is pressurized to raise its pressure back to the
operating pressure (time t
7-t
8). After a predetermined interval has elapsed, the discharge flow rate of liquid discharged
from the liquid-delivery chamber B is gradually decreased, while simultaneously the
control valve A is opened to begin discharging of liquid from the liquid-delivery
chamber A. When the discharge flow rate of liquid reaches a set flow rate, the control
valve B is closed (time t
9-t
10) and this procedure is repeated.
[0098] As described above, the flow rate from the positive displacement pump 10 that starts
pumping operation is gradually increased, while the flow rate from the pump that is
stopping pumping operation is gradually decreased at the same rate such that the overall
flow rate does not change. By alternating operations between two pump, the same amount
of feed fluid can be delivered continuously to the processing apparatus 16 without
variation in flow.
[0099] In this example, a pipe 114 connecting the check valve 100 and control valve 106
is sufficiently short and constructed of a highly rigid material so that there is
almost no volume expansion in the pipe 114 when the pressure therein rises to the
same pressure as that in the liquid-delivery chamber 28. Therefore, the pressure in
the secondary side of the check valve 100 can be maintained at the operating pressure
in order to achieve the required flow rate immediately after pumping operation begins.
However, if a flexible tube or the like is used for the pipe 114, volume expansion
may occur in the pipe 114 when the pressure therein rises to the same pressure as
that in the liquid-delivery chamber 28. In this case, the pressure in the secondary
side of the check valve 100 can be raised to the operating pressure immediately after
pumping operation begins by setting the pressure in the liquid-delivery chamber 28
to the pressure (P + α), slightly higher than the pressure P during pumping operations,
where the pressure α is equivalent to the estimated amount caused by volume expansion
in the pipe 114.
[0100] As described above, according to the present invention, in a positive displacement
liquid-delivery system employing a flexible diaphragm that is driven externally by
a drive mechanism, the differential pressure between the inner and outer sides of
the diaphragm is controlled at a constant value while the diaphragm is displaced,
hence it is possible to provide a compact apparatus capable of delivering liquid with
great precision. This type of apparatus is very useful in manufacturing processes
for semiconductor elements.
[0101] Further, the pressure in the primary side of the check valve is controlled so as
not to fall below the vapor pressure of the liquid therein when the pumping operations
are stopped. Furthermore, the pressure in the liquid-delivery chamber is maintained
at the operating pressure or at a higher pressure. Accordingly, the time required
to stabilize pumping operations can be shortened, and it is possible to control the
flow rate of liquid immediately after pumping operations begin.
[0102] Although certain preferred embodiments of the present invention have been shown and
described in detail, it should be understood that various changes and modifications
may be made therein without departing from the scope of the appended claims.
[0103] It should be noted that the objects and advantages of the invention may be attained
by means of any compatible combination(s) particularly pointed out in the items of
the following summary of the invention.
SUMMARY OF THE INVENTION
[0104] 1. A positive displacement liquid-delivery apparatus comprising:
a positive displacement pump comprising a housing having a liquid-delivery chamber
divided by a flexible diaphragm and a diaphragm driving unit linked to said diaphragm
to discharge fluid from said liquid-delivery chamber; and
a differential pressure control unit for controlling the differential pressure between
both sides of said diaphragm at a constant value during the pumping process.
[0105] 2. A positive displacement liquid-delivery apparatus as claimed in item 1, wherein
said diaphragm comprises a bellows.
[0106] 3. A positive displacement liquid-delivery apparatus as claimed in item 1, wherein
atmosphere pressure is applied to one of said both sides of said diaphragm.
[0107] 4. A positive displacement liquid-delivery apparatus as claimed in item 1, wherein
the differential pressure control unit comprises:
a differential pressure sensor for detecting the differential pressure between both
sides of said diaphragm; and
a control valve for controlling the flow rate of said liquid discharged from said
liquid-delivery chamber on a basis of a signal from said differential pressure sensor.
[0108] 5. A positive displacement liquid-delivery apparatus as claimed in item 4, further
comprising a flow sensor disposed on a discharge path; and
wherein control is performed based on a signal from said flow sensor when the pressure
in said liquid-delivery chamber during the pumping process exceeds a prescribed value
or the absolute value of the rate of pressure variations exceeds a prescribed value.
[0109] 6. A positive displacement liquid-delivery apparatus as claimed in item 1, wherein
said liquid-delivery chamber is arranged so as to achieve the required discharge flow
volume of said fluid in one stroke.
[0110] 7. A positive displacement liquid-delivery apparatus as claimed in item 1, wherein
gas is employed to pressurize the space on the opposite side of said diaphragm from
said liquid-delivery chamber.
[0111] 8. A positive displacement liquid-delivery apparatus as claimed in item 1, further
comprising a plurality of positive displacement pumps arranged in parallel and delivering
different kinds of fluid to a single processing unit.
[0112] 9. A positive displacement liquid-delivery apparatus as claimed in item 1, comprising
two positive displacement pumps delivering the same kind of fluid, and alternately
delivering said fluid to a single processing unit in a continuous manner.
[0113] 10. A positive displacement liquid-delivery apparatus comprising:
a positive displacement pump comprising a housing having a liquid-delivery chamber
divided by a flexible diaphragm and a diaphragm driving unit linked to said diaphragm
to discharge fluid from said liquid-delivery chamber; and
wherein said diaphragm driving unit drives said diaphragm to maintain the flow rate
of said liquid discharged from said liquid-delivery chamber at a constant rate based
on the variation of the differential pressure between both sides of the diaphragm.
[0114] 11. A positive displacement liquid-delivery apparatus as claimed in item 10, wherein
said liquid-delivery chamber is arranged so as to achieve the required discharge volume
of said fluid in one stroke.
[0115] 12. A positive displacement liquid-delivery apparatus as claimed in item 10, wherein
gas is employed to pressurize the space on the opposite side of said diaphragm from
said liquid-delivery chamber.
[0116] 13. A positive displacement liquid-delivery apparatus as claimed in item 10, further
comprising a plurality of positive displacement pumps arranged in parallel and delivering
different kinds of fluid to a single processing unit.
[0117] 14. A positive displacement liquid-delivery apparatus as claimed in item 10, comprising
two positive displacement pumps delivering the same kind of fluid, and alternately
delivering said fluid to a single processing unit in a continuous manner.
[0118] 15. A positive displacement liquid-delivery apparatus comprising:
a positive displacement pump comprising a housing having a liquid-delivery chamber
divided by a flexible diaphragm and a diaphragm driving unit linked to said diaphragm
to discharge fluid from said liquid-delivery chamber; and
an discharge path extending from said liquid-delivery chamber;
a check valve disposed on said discharge path; and
a pressure control unit for controlling the primary side pressure of said check valve
so as not to drop below the vapor pressure of the fluid discharged from said liquid-delivery
chamber during stoppage of the pumping process.
[0119] 16. A positive displacement liquid-delivery apparatus as claimed in item 15, wherein
said pressure control unit comprises a control valve disposed upstream of said check
valve, and regulates the pressure in said liquid-delivery chamber during pump stoppage
at the pressure required for pumping operation.
[0120] 17. A positive displacement liquid-delivery apparatus as claimed in item 15, wherein
said pressure control unit comprises a control valve disposed upstream of said check
valve, and regulates the pressure in said liquid-delivery chamber during pump stoppage
at the pressure higher than the pressure required for pumping operation by an amount
equivalent to the estimated amount caused by the volume expansion of the piping between
the check valve and control valve.
[0121] 18. A positive displacement liquid-delivery apparatus as claimed in item 15, wherein
said liquid-delivery chamber is arranged so as to achieve the required discharge flow
volume of said fluid in one stroke.
[0122] 19. A positive displacement liquid-delivery apparatus as claimed in item 15, wherein
gas is employed to pressurize the space on the opposite side of said diaphragm from
said liquid-delivery chamber.
[0123] 20. A positive displacement liquid-delivery apparatus as claimed in item 15, further
comprising a plurality of positive displacement pumps arranged in parallel and delivering
different kinds of fluid to a single processing unit.
[0124] 21. A positive displacement liquid-delivery apparatus as claimed in item 15, comprising
two positive displacement pumps delivering the same kind of fluid, and alternately
delivering said fluid to a single processing unit in a continuous manner.
[0125] 22. A deposition apparatus comprising:
the positive displacement liquid-delivery apparatus as claimed in item 1;
a vaporizer for vaporizing a fluid feed supplied from said positive displacement liquid-delivery
apparatus; and
a deposition chamber in which thin films are deposited using the feed gas supplied
from said vaporizer.
[0126] 23. A deposition apparatus comprising:
the positive displacement liquid-delivery apparatus as claimed in item 10;
a vaporizer for vaporizing a fluid feed supplied from said positive displacement liquid-delivery
apparatus; and
a deposition chamber in which thin films are deposited using the feed gas supplied
from said vaporizer.
[0127] 24. A deposition apparatus comprising:
the positive displacement liquid-delivery apparatus as claimed in item 15;
a vaporizer for vaporizing a fluid feed supplied from said positive displacement liquid-delivery
apparatus; and
a deposition chamber in which thin films are deposited using the feed gas supplied
from said vaporizer.