Methods and apparatus for multiple channel mass flow and ratio control systems
10698426 ยท 2020-06-30
Assignee
Inventors
Cpc classification
G05D11/139
PHYSICS
G05D7/0664
PHYSICS
G01F1/36
PHYSICS
G01F5/005
PHYSICS
International classification
Abstract
Fluid control systems, including mass flow control systems, mass flow ratio control systems, and mass flow and ratio control systems, as well as corresponding methods for fluid control are provided. These systems allow one shared pressure sensor to be used for multiple flow channels, and a controller which can accurately determine mass flow on the basis of fluid pressure detected by this shared pressure sensor.
Claims
1. A fluid control system comprising: a plurality of flow channels carrying fluids, each flow channel comprising a flow restrictor, a flow regulating valve and a channel pressure sensor between the flow restrictor and the flow regulating valve; a shared flow channel carrying the fluids to or from the plurality of flow channels, the flow restrictor in each flow channel being between the channel pressure sensor and the shared flow channel; a shared pressure sensor in the shared flow channel configured to detect a shared flow channel pressure; and a controller that determines mass flow through each of the flow channels based on channel pressures and the shared flow channel pressure and controls the flow regulating valves of the flow channels to control mass flow through each flow channel, wherein the controller determines through recursive calculation (1) channel pressures for positions that are adjacent to the flow restrictors and opposite to the channel pressure sensors of the plurality of flow channels, (2) mass flow through each flow channel, and (3) total mass flow through the shared channel.
2. The fluid control system of claim 1, wherein the controller determines mass flow through each flow channel based on property of the fluid flowing therethrough, property of the flow restrictor, and flow channel property between the flow restrictor and the shared pressure sensor.
3. The fluid control system of claim 2, wherein the controller determines mass flow through a flow channel of the plurality of flow channels by (i) assuming a flow channel pressure adjacent to the flow restrictor and opposite to the channel pressure sensor of the flow channel, the channel pressure sensor providing a detected flow channel pressure, (ii) determining the mass flow through the flow channel based on the flow channel pressure adjacent to the flow restrictor and opposite to the channel pressure sensor and the detected flow channel pressure for the flow channel, (iii) determining total mass flow on the basis of mass flows through each of the flow channels of the plurality of flow channels, (iv) calculating the flow channel pressure adjacent to the flow restrictor and opposite to the channel pressure sensor of the flow channel using the total mass flow determined in step (iii), and repeating steps (ii) to (iv).
4. The fluid control system of claim 3, wherein the shared flow channel is downstream from the plurality of flow channels.
5. The fluid control system of claim 4, wherein the shared flow channel is upstream from the plurality of flow channels.
6. The fluid control system of claim 4, further comprising a second plurality of flow channels, each flow channel of the second plurality of flow channels comprising a flow restrictor, a flow regulating valve and a channel pressure sensor between the flow restrictor and the flow regulating valve; the shared flow channel carrying fluids from the plurality of flow channels to the second plurality of flow channels; for each flow channel of the second plurality of flow channels, the flow restrictor being between the channel pressure sensor and the shared flow channel; wherein the controller further determines mass flow through each of the flow channels of the second plurality of flow channels based on channel pressures and the shared flow channel pressure and controls the flow regulating valves of the flow channels to control mass flow through each flow channel.
7. The fluid control system of any claim 6, wherein the plurality of flow channels and the second plurality of flow channels are part of an integrated system.
8. The fluid control system of claim 7, wherein the shared pressure sensor is not part of the integrated system.
9. The fluid control system of claim 4, wherein the controller calculates a flow channel pressure adjacent to a flow restrictor and opposite to a channel pressure sensor of an i-th flow channel, the i-th flow channel being upstream from the shared flow channel, using Equation (1): P.sub.d,i=.sub.pd(P.sub.d,Q.sub.t, V.sub.i,L.sub.i) (1); where .sub.Pd is a function of downstream pressure P.sub.d detected by the shared pressure sensor, total flow through the shared flow channel Q.sub.t, and volume V.sub.i and length L.sub.i of the i-th flow channel from its restrictor to the shared pressure sensor.
10. The fluid control system of claim 9, wherein .sub.Pd is provided by Equation (2): .sub.Pd(P.sub.d,Q.sub.t, V.sub.i,L.sub.i)=k.sub.i,1.Math.P.sub.d+k.sub.i,2.Math.Q.sub.t+k.sub.i,3.Math.V.sub.i+k.sub.i,4.Math.L.sub.i (2); where k.sub.i,1, k.sub.i,2, k.sub.i,3 and k.sub.i,4 are empirically or experimentally obtained linear coefficients.
11. The fluid control system of claim 4, wherein the controller calculates a flow channel pressure adjacent to a flow restrictor and opposite to a channel pressure sensor of a j-th flow channel using Equation (6): P.sub.u,j=.sub.Pu(P.sub.u,Q.sub.t, V.sub.j,L.sub.j) (6); where .sub.Pu is a function of upstream pressure P.sub.u detected by the shared pressure sensor, total flow through the shared flow channel Q.sub.t, and volume V.sub.j and length L.sub.j of the j-th flow channel from its restrictor to the shared pressure sensor.
12. The fluid control system of claim 11, wherein .sub.Pu is provided by Equation .sub.Pu(P.sub.u,Q.sub.t, V.sub.j,L.sub.j)=k.sub.j,1.Math.P.sub.u+k.sub.j,2.Math.Q.sub.t+k.sub.j,3.Math.V.sub.j+k.sub.j,4.Math.L.sub.j (7); where k.sub.j,1, k.sub.j,2, k.sub.j,3 and k.sub.j,4 are empirically or experimentally obtained linear coefficients.
13. A fluid control method, comprising: flowing fluids through a plurality of flow channels, each flow channel comprising a flow restrictor and a flow regulating valve; flowing the fluids to or from the plurality of flow channels through a shared flow channel; detecting a shared flow channel pressure in the shared flow channel; detecting a flow channel pressure for each flow channel between its flow regulating valve and its flow restrictor; determining mass flow through each of the flow channels based on the flow channel pressures and the shared flow channel pressure by recursively calculating (1) mass flow through each flow channel, (2) channel pressures for positions that are adjacent to the flow restrictors and opposite to the channel pressure sensors of the plurality of flow channels, and (3) total mass flow through the shared channel; and controlling the flow regulating valves of the flow channels to control mass flow through each flow channel.
14. The fluid control method of claim 13, wherein mass flow through each flow channel is determined based on property of the fluid flowing therethrough, property of the flow restrictor, and flow channel property between the flow restrictor and where the shared flow channel pressure is detected.
15. The fluid control method of claim 13, wherein determining mass flow through a flow channel of the plurality of flow channels comprises (i) assuming a flow channel pressure adjacent to the flow restrictor and opposite to the channel pressure sensor of the flow channel, (ii) determining the mass flow through the flow channel based on the flow channel pressure adjacent to the flow restrictor and opposite to the channel pressure sensor and the detected flow channel pressure for the flow channel, (iii) determining total mass flow on the basis of mass flows through each of the flow channels of the plurality of flow channels, (iv) calculating the flow channel pressure adjacent to the flow restrictor and opposite to the channel pressure sensor of the flow channel using the total mass flow determined in step (iii), and repeating steps (ii) to (iv).
16. The fluid control method of claim 13, further comprising flowing fluids from the plurality of flow channels through the shared channel and into a second plurality of flow channels, each flow channel of the second plurality of flow channels comprising a flow restrictor and a flow regulating valve; detecting a flow channel pressure and flow channel temperature for each flow channel of the second plurality of flow channels between its flow regulating valve and its flow restrictor; and determining mass flow through each of the flow channels of the second plurality of flow channels based on the flow channel pressures and the shared flow channel pressure.
17. The fluid control method of claim 16, further comprising detecting a flow channel temperature for each flow channel of the second plurality of flow channels between its flow regulating valve and its flow restrictor.
18. The fluid control method of claim 13, further comprising calculating a flow channel pressure adjacent to a flow restrictor and opposite to a channel pressure sensor of an i-th flow channel, the i-th flow channel being upstream from the shared flow channel, using Equation (1): P.sub.d,i=.sub.Pd(P.sub.d,Q.sub.t, V.sub.i,L.sub.i) (1); where .sub.Pd is a function of downstream pressure P.sub.d detected by the shared pressure sensor, total flow through the shared flow channel Q.sub.t, and volume V.sub.i and length L.sub.i of the i-th flow channel from its restrictor to the shared pressure sensor.
19. The fluid control system of claim 18, wherein .sub.Pd is provided by Equation (2): .sub.Pd(P.sub.d,Q.sub.t, V.sub.i,L.sub.i)=k.sub.i,1.Math.P.sub.d+k.sub.i,2.Math.Q.sub.t+k.sub.i,3.Math.V.sub.i+k.sub.i,4.Math.L.sub.i (2); where k.sub.i,1, k.sub.i,2, k.sub.i,3 and k.sub.i,4 are empirically or experimentally obtained linear coefficients.
20. The fluid control method of claim 13, further comprising calculating a flow channel pressure adjacent to a flow restrictor and opposite to a channel pressure sensor of a j-th flow channel, the j-th flow channel being downstream from the shared flow channel, using Equation (6): P.sub.u,j=.sub.Pu(P.sub.u,Q.sub.t, V.sub.j,L.sub.j) (6); where .sub.Pd is a function of upstream pressure P.sub.u detected by the shared pressure sensor, total flow through the shared flow channel Q.sub.t, and volume V.sub.j and length L.sub.j of the j-th flow channel from its restrictor to the shared pressure sensor.
21. The fluid control system of claim 20, wherein .sub.Pu is provided by Equation (7): .sub.Pu(P.sub.u,Q.sub.t, V.sub.j,L.sub.j)=k.sub.j,1.Math.P.sub.u+k.sub.j,2.Math.Q.sub.t+k.sub.j,3.Math.V.sub.j+k.sub.j,4.Math.L.sub.j (7); where k.sub.j,1, k.sub.j,2, k.sub.j,3 and k.sub.j,4 are empirically or experimentally obtained linear coefficients.
22. A fluid control system comprising: a plurality of flow channels, each flow channel comprising a flow restrictor, a flow regulating valve and a channel pressure sensor between the flow restrictor and the flow regulating valve; a second plurality of flow channels, each flow channel of the second plurality of flow channels comprising a flow restrictor, a flow regulating valve and a channel pressure sensor between the flow restrictor and the flow regulating valve; a shared flow channel carrying fluids from the plurality of flow channels to the second plurality of flow channels; in each flow channel of the plurality of flow channels and the second plurality of flow channels, the flow restrictor being between the channel pressure sensor and the shared flow channel; a shared pressure sensor in the shared flow channel configured to detect a shared flow channel pressure; and a controller that determines mass flow through each of the flow channels in the plurality of flow channels and in the second plurality of flow channels based on channel pressures and the shared flow channel pressure and controls the flow regulating valves of the flow channels to control mass flow through each flow channel.
23. The fluid control system of any claim 22, wherein the plurality of flow channels and the second plurality of flow channels are part of an integrated system.
24. The fluid control system of claim 23, wherein the shared pressure sensor is not part of the integrated system.
25. A fluid control method comprising: flowing fluids through a plurality of flow channels and through a second plurality of flow channels, each flow channel comprising a flow restrictor and a flow regulating valve; flowing fluids from the plurality of flow channels to the second plurality of flow channels through a shared flow channel; detecting a shared flow channel pressure in the shared flow channel; detecting a flow channel pressure for each flow channel between its flow regulating valve and its flow restrictor; determining mass flow through each of the flow channels based on each flow channel pressure and the shared flow channel pressure; and controlling the flow regulating valves of the flow channels to control mass flow through each flow channel.
26. The fluid control method of claim 25, further comprising detecting a flow channel temperature for each flow channel of the second plurality of flow channels between its flow regulating valve and its flow restrictor.
Description
BRIEF DESCRIPTION OF THE DRAWINGS
(1) The foregoing will be apparent from the following more particular description of example embodiments of the invention, as illustrated in the accompanying drawings in which like reference characters refer to the same parts throughout the different views. The drawings are not necessarily to scale, emphasis instead being placed upon illustrating embodiments of the present invention.
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DETAILED DESCRIPTION OF THE INVENTION
(10) A description of example embodiments of the invention follows.
(11) Fluid control systems, including mass flow control systems, mass flow ratio control systems, and mass flow and ratio control systems, as well as corresponding methods for fluid control are provided. As described in the following, the systems provided herein have significant advantages compared to prior art systems.
(12)
(13) Importantly, in prior art mass flow control systems, each flow channel has two associated pressure sensors (i.e., the upstream pressure sensor 140 and the downstream pressure sensor 174) in close proximity to the flow restrictor to allow accurate detection of the pressure drop across the flow restrictor 150, and, thus, accurate determination of mass flow.
(14) In contrast, the fluid control systems and methods provided herein allow one pressure sensor (i.e., the downstream pressure sensor in a mass flow control system or the upstream pressure sensor in a mass flow ratio control system) to be at a distance from the flow restrictor and can be operated with a single MFCS controller, which leads to several significant advantages. Because the pressure sensor can be distant, it can be shared by multiple channels. Use of a single MFCS controller as well as use of a shared pressure sensor is more cost efficient and makes the fluid control systems more space efficient, the latter being particularly important for applications in certain industries such as the semiconductor industry. Further, when combined with a single MFCS controller, a shared pressure sensor can also greatly simplify the complexity of the communication within the fluid control system, between pressure sensors and MFCS controller, and also between the MFCS controller and a host controller. Yet further, a shared pressure sensor can simplify and improve calibration, make multiple channel systems more flexible, and allow use of higher accuracy and larger pressure sensors as the shared pressure sensor, which can improve overall accuracy of the fluid control system, without increasing cost.
(15)
(16) The downstream pressure sensor 260 is distant from each of the flow restrictors 250. To be able to accurately measure fluid flow through each flow channel 220, the fluid pressures of fluid on both sides and adjacent to each of the flow restrictors need to be known.
(17) Generally, for a given flow channel i the respective internal pressure sensor (e.g., an upstream pressure sensor 240) detecting fluid pressure adjacent to its flow restrictor provides one of these two required pressure values for a given flow channel, for example, it provides the upstream pressure of the i-th flow channel P.sub.u,i. The downstream pressure P.sub.d,i of the i-th flow channel at a position adjacent to the restrictor can be estimated by the following equation:
P.sub.d,i=.sub.Pd(P.sub.d,Q.sub.t,V.sub.i,L.sub.i)(1),
where .sub.Pd is a function of the shared downstream pressure P.sub.d detected by the distant downstream pressure sensor at a position along the shared flow channel (e.g., pressure sensor 260 at position 224 along shared flow channel 221), the total flow through the device Q.sub.t (i.e., the flow through the shared flow channel), and the volume V.sub.i and length L.sub.i of the i-th flow channel from the restrictor to shared pressure sensor at the second position.
(18) The function .sub.Pd can be obtained by empirical data or experiment, for example, as a linear expression
.sub.Pd(P.sub.d,Q.sub.t,V.sub.i,L.sub.i)=k.sub.i,1.Math.P.sub.d+k.sub.i,2.Math.Q.sub.t+k.sub.i,3.Math.V.sub.i+k.sub.i,4.Math.L.sub.i(2),
where k.sub.i,1, k.sub.i,2, k.sub.i,3 and k.sub.i,4 are empirically or experimentally obtained linear coefficients.
(19) As is known in the art, the flow through the flow restrictor of the i-th channel (Q.sub.i) can be expressed as a function of the upstream and the downstream pressure (P.sub.u,i and P.sub.d,i) of the restrictor (i.e., the pressures immediately adjacent to the restrictor), the cross section of the flow path through the restrictor (A.sub.i), and gas properties such as specific heat ratio and molecular weight M
Q.sub.i=.sub.Q(P.sub.u,i,P.sub.d,i,A.sub.i,,M)(3).
(20) The function .sub.Q can be obtained by empirical data or experiment.
(21) In the case of a flow nozzle as flow restrictor, the following equation can be used
(22)
where C.sub.i is the discharge coefficient of the i-th flow restrictor, R the universal gas constant, and T the gas temperature.
(23) In the case of a pipe as restrictor, the following equation can be used
(24)
where d.sub.i is the diameter of the i-th pipe, L.sub.i the length of i-th pipe, and the gas viscosity.
(25) Other flow restrictors and corresponding equations describing mass flow through these flow restrictors can be used, and are known in the art. See, for example, The American Society of Mechanical Engineers, ASME MFC-3M-2004 Measurement of Fluid Flow in Pipes Using Orifice, Nozzle, and Venturi, 2004.
(26) The total flow through the device Q.sub.t is calculated by summarizing all individual channel flows Q.sub.i (i=1,2, . . . N). Because the Q.sub.i calculation is depended on the downstream pressure P.sub.d,i, a recursive calculation is needed for determining Q.sub.i, P.sub.d,i and Q.sub.t. For example, first an initial P.sub.d,i value is assumed and an initial flow Q.sub.i determined as described above. Then the total flow Q.sub.t is determined by summing all Q.sub.i. Then the total flow Q.sub.t can be used to recalculate P.sub.d,i and Q.sub.i. This recursive calculation is repeated until the values converge within a set convergence threshold.
(27) On the basis of the calculated mass flows Q.sub.i, the MFCS controller can control the valves of each flow channel to a desired mass flow set point using feedback control methods.
(28) In the multiple channel mass flow control system illustrated in
(29)
(30)
(31) Generally, for a given flow channel j the respective internal pressure sensor (e.g., a downstream pressure sensor 440) detecting fluid pressure adjacent to its flow restrictor provides one of these two required pressure values for a given flow channel, for example, it provides the downstream pressure of the j-th flow channel P.sub.d,j. The upstream pressure P.sub.u,j of the j-th flow channel at a position adjacent to the restrictor can be estimated by the following equation:
P.sub.u,j=.sub.Pu(P.sub.u,Q.sub.t,V.sub.j,L.sub.j)(6),
where .sub.Pu is a function of the shared upstream pressure P.sub.u detected by the distant upstream pressure sensor at an upstream position along the shared flow channel (e.g., pressure sensor 460 at upstream position 424 along shared flow channel 421 to the flow restrictor 450), the total flow through the device Q.sub.t (i.e., the flow through the shared flow channel, e.g., channel 421), and the volume V.sub.j and length L.sub.1 of the j-th flow channel from the flow restrictor to the shared pressure sensor at the upstream position.
(32) The function .sub.Pu can be obtained by empirical data or experiment, for example, as a linear expression
.sub.Pu(P.sub.u,Q.sub.t,V.sub.j,L.sub.j)=k.sub.j,1.Math.P.sub.u+k.sub.j,2.Math.Q.sub.t+k.sub.j,3.Math.V.sub.j+k.sub.j,4.Math.L.sub.j(7)
where k.sub.j,1, k.sub.j,2, and k.sub.j,4 are empirically or experimentally obtained linear coefficients. With these calculated pressures, the MFCS controller can further estimate the mass flows in the flow channels according to above Equations (3) and/or (4) or (5).
(33) As further illustrated in
(34) In the integrated multiple channel mass flow ratio control system 405 of
(35)
(36) As further illustrated in
(37) The multiple channel mass flow control systems described herein (e.g., the system 200 of
(38)
(39) The use of only one shared pressure sensor (for example, as part of a multiple channel mass flow and ratio control system as illustrated in
(40) An example self-calibration method comprises the following steps:
(41) (1) Closing all upstream (inlet) valves 630 and opening all downstream (outlet) valve 631;
(42) (2) Pumping down the system pressure within the flow channels (e.g., by connecting one or more pumps, directly or indirectly, to one or more of the flow channels that have an open downstream valve 631) and monitoring the shared pressure sensor reading;
(43) (3) Closing all downstream valves 631 when the system pressure drops to a predetermined low pressure threshold;
(44) (4) Providing a mass flow setpoint for the i-th inlet mass flow channel (e.g., from a gas source 1 as indicated in
(5) Measuring the pressure in the system by the shared pressure sensor and the gas temperature;
(6) Calculate the actual mass flow Q.sub.a by the method of rate of pressure rising, i.e., Q.sub.a=V*Tstp*[d(P/T)/dt], where V is the total system volume between the i-th upstream valve 630 and all other downstream valves (assuming all other valves are closed);
(7) Closing the i-th upstream valve 630 and open all downstream valves to pump down the system pressure;
(8) Repeating steps (3) to (7) with different flow setpoints which cover the whole flow range, considered for a given application, of the i-th flow channel;
(9) Storing the actual flow measurements (Q.sub.a) and the measured flow (Q.sub.m) as the calibration data for the i-th inlet flow channel;
(10) Repeating steps (1) to (9) for the next inlet flow channel until all inlet flow channels have been calibrated;
(11) Closing all upstream valves 630 and downstream valves 631;
(12) Opening the j-th downstream (outlet) valve 631;
(13) Providing a flow setpoint to the k-th inlet flow channel and stabilizing the mass flow;
(14) Storing both the measured flow by the k-th inlet flow channel as Q.sub.a, and j-th outlet flow channel as Q.sub.m;
(15) Repeating steps (11) to (14) with different flow setpoint for the j-th inlet flow channel which cover the whole flow range of the k-th outlet flow channel;
(16) Storing the actual flow measurements (Q.sub.a) and the measured flow (Q.sub.m) as the calibration data for the j-th outlet flow channel;
(17) Repeating steps (11) to step (16) for the next inlet flow channel until all outlet flow channels have been calibrated;
(45) An example cross-validation method comprises the following steps:
(46) (1) Closing all upstream valves 630 and downstream valves 631;
(47) (2) Providing a flow setpoint to the i-th inlet flow channel and opening the j-th downstream valve;
(48) (3) Comparing the flow difference between the i-th inlet flow measurement and the j-th outlet flow measurement;
(49) (4) If the flow difference is above the predetermined flow error threshold, either the i-th inlet or the j-th outlet flow measurement is not accurate;
(50) (5) Repeat steps (1) to (4) for all inlet and out flow channels.
(51) The fluid control systems can be integrated systems, that is, the elements of the systems are included within one housing or enclosure. Typically, for the fluid control systems described herein, the housing provides at least fluid input and outputs and allows for input and output of signals, which allows incorporation of the integrated system within larger systems.
(52) Each flow channel of a plurality of flow channels can be part of a separate integrated system, or a subset or all of the flow channels can be part of an integrated system. Typically, for each flow channel that is part of an integrated system, one valve, one flow restrictor, and one fluid pressure sensor positioned between the valve and the flow restrictor, are also part of the integrated system, and optionally, a temperature sensor is also part of the integrated system.
(53) In integrated fluid control systems, the one or more flow channels of the integrated systems allow fluid flow from an inlet of the integrated system to an outlet of the integrated system.
(54) The fluid control systems can have one or more controllers; however, typically, the systems have one controller which can be integrated, as illustrated, for example, in
(55) Commercially available controllers can be used in the provided fluid control systems and fluid control methods provided here. However, the controller and communication system has to be configured to allow operation of the fluid control systems as provided herein.
(56) Further, commercially available valves, pressure sensors, flow channels, and communication systems can be selected, as known in the art, depending on the particular application requirements.
(57) The fluid control systems have a plurality of flow channels (e.g., at least two, at least five, or at least eight flow channels). Typically, all of the flow channels are connected (i.e., to allow fluid connection during operation) to form a shared flow channel. Integrated fluid control systems in which all flow channels are connected to one shared flow channel are illustrated, for example, in
(58) Typically, it is desirable that flow channel pressure sensors between valve and flow restrictor, detect the pressure of the fluid within the channel at a position as close as possible to the flow restrictor, that is, it is desired that the distance between the position where the pressure is detected and the flow restrictor (or, more specifically, the position where fluid enters or exits the flow restrictor) is as short as practically possible. However, the distance can be greater, which will lead to less accurate flow measurement. Typically, the distance is less than the diameter of the pipe where the fluid flows. The provided fluid control systems further have a shared pressure sensor which is configured to detect a fluid pressure in a shared flow channel at a position distant from the flow restrictors associated with the flow channels of the system. In multiple channel systems, this pressure sensor can be installed in or along the shared flow channel. Use of a distant and shared pressure sensor allows the pressure sensor to be external to an integrated multiple channel system, as illustrated, for example, in
(59) Commercially available and prior art known flow restrictors can be used in the fluid control systems provided. Suitable flow restrictors include, but are not limited to, nozzles, orifices, laminar flow elements, and porous media.
(60) The flow channels of the fluid control systems can include temperature sensors. Typically, each flow channel has a temperature sensor that detects the fluid temperature at a position between the valve and flow restrictor of the flow channel. This is particularly important in applications in which the fluids (typically, gases) flowing through the flow channels of a plurality of flow channels are to be at different temperatures. However, when several or all of the flow channels of the plurality (and/or second plurality) of flow channels are to be at the same temperature, fewer temperature sensors may be required. For example, several or all flow channels including the gas flowing therethrough may be kept at the same temperature and one or more (but fewer than one per flow channel) temperature sensors can be used that measure the temperature at which the flow channels are (or even an entire integrated system is) kept.
(61) In further embodiments, fluid control methods are provided. These fluid control methods can use any of the fluid control systems described herein.
(62) In further embodiments, the multiple channel mass flow control systems (e.g., as illustrated in
(63) In further embodiments, the multiple channel mass ratio control systems (e.g., as illustrated in
(64) In further embodiments, the multiple channel mass flow and ratio control systems (e.g., as illustrated in
(65) The fluid control systems of the present application may be just hardware, but generally, fluid control methods of the present application are implemented in software in a hardware system (typically, as software implemented on the controller) comprising a data processor, associated memory and input output devices. The processor routines (e.g. of the controllers described herein, including routines corresponding to the calculations and methods steps describe herein) and data may be stored on a non-transitory computer readable medium as a computer program product.
(66) The teachings of all patents, published applications and references cited herein are incorporated by reference in their entirety.
(67) While this invention has been particularly shown and described with references to example embodiments thereof, it will be understood by those skilled in the art that various changes in form and details may be made therein without departing from the scope of the invention encompassed by the appended claims.