Apparatus and method for pressure fluctuation insensitive mass flow control

• US 20060173642A1
• Filed: 12/15/2005
• Published: 08/03/2006
• Est. Priority Date: 06/24/2002
• Status: Active Grant

• Current Assignee: Ali Shajii, Jesse Ambrosina, Nicholas Kottenstette
• Original Assignee: Ali Shajii, Jesse Ambrosina, Nicholas Kottenstette
• Inventors: Shajii, Ali, Ambrosina, Jesse, Kottenstette, Nicholas
• Granted Patent: US 7,424,346 B2
• Time in Patent Office: Days
• US Class Current: 702/100
• CPC Class Codes: G01F 1/684 Structural arrangements; Mounting of elements, e.g. in relation to fluid flow
• CPC Class Codes: G01F 1/6965 comprising means to store calibration data for flow signal calculation or correction
• CPC Class Codes: G01F 1/86 Indirect mass flowmeters, e.g. measuring volume flow and density, temperature or pressure
• CPC Class Codes: G01F 15/024 involving digital counting
• CPC Class Codes: G01F 25/15 specially adapted for gas meters G01F25/11 - G01F25/14, G01F25/17 take precedence
• CPC Class Codes: G01F 5/00 Measuring a proportion of the volume flow
• CPC Class Codes: G05D 7/0635 by action on throttling means G05D7/0688, G05D7/0694 take precedence
• CPC Class Codes: Y10T 137/0379 By fluid pressure
• CPC Class Codes: Y10T 137/0396 Involving pressure control
• CPC Class Codes: Y10T 137/7759 Responsive to change in rate of fluid flow
• CPC Class Codes: Y10T 137/776 Control by pressures across flow line valve
• CPC Class Codes: Y10T 137/7761 Electrically actuated valve
• CPC Class Codes: Y10T 137/87354 Including flowmeter

Abstract

A mass flow controller includes a thermal mass flow sensor in combination with a pressure sensor to provide a mass flow controller that is relatively insensitive to fluctuations in input pressure. The pressure sensor and thermal sensor respectively provide signals to an electronic controller indicating the measured inlet flow rate and the pressure within the dead volume. The electronic controller employs the measured pressure to compensate the measured inlet flow rate and to thereby produce a compensated measure of the outlet flow rate, which may be used to operate a mass flow controller control valve.

Claims

1-25. -25. (canceled)

26. A system, defining a flow path between a gas inlet and an outlet of the system, the system comprising:

a mass flow controller including a mass flow sensor for sensing the mass flow along the flow path and a control valve, responsive to a control signal, for controlling the mass flow through the outlet;

a pressure sensor for measuring fluctuations in pressure of gas along the flow path; and

a controller for generating the control signal as a function of the sensed mass flow and measured fluctuations in pressure of gas so as to provide a constant flow of gas at the outlet irrespective of fluctuations in pressure of gas at the inlet.

27. A system according to claim 26, wherein the pressure sensor measures fluctuations in pressure of gas along the flow path, upstream from the control valve.

28. A system according to claim 26, wherein the pressure sensor measures fluctuations in pressure of gas in the dead space between the flow sensor and the control valve.

29. A system, defining a flow path between a gas inlet and an outlet of the system, the system comprising:

a mass flow controller including a mass flow sensor for sensing the mass flow rate along the flow path and a control valve, responsive to a control signal, for controlling the mass flow through the outlet;

a pressure sensor for measuring fluctuations in pressure of gas along the flow path; and

a controller for generating the control signal as a function of the sensed mass flow rate at the inlet of the controller and the measured fluctuations in pressure of gas so as to compensate the flow rate measured by the sensor at the inlet of the controller to more closely approximate the flow rate at the outlet of the controller.

30. A system according to claim 29, wherein the pressure sensor measures fluctuations in pressure of gas along the flow path, upstream from the control valve.

31. A system according to claim 30, wherein the pressure sensor measures fluctuations in pressure of gas in the dead space between the flow sensor and the control valve.

32. A control system comprising:

a mass flow controller constructed and arranged so as to receive fluid flowing from a inlet supply line, the mass flow controller including a thermal mass flow sensor and an outlet valve;

a pressure sensor; and

a system controller including a pressure sensor interface for coupling the system controller to the pressure sensor, wherein the system controller employs data obtained at the pressure sensor interface to compensate for fluctuations induced in the thermal mass flow sensor by pressure transients in the inlet supply line.

33. A control system according to claim 32, wherein the pressure sensor and pressure interface is used to monitor the pressure within the mass flow controller.

34. A control system according to claim 32, wherein the mass flow controller includes a dead volume, and the pressure sensor and pressure interface are used to monitor the pressure within the dead volume.

35. A control system according to claim 32, wherein the controller includes a flow sensor interface for coupling the system controller to the thermal mass flow sensor.

36. A control system according to claim 35, further including a temperature sensor and a temperature sensor interface for obtaining data representative of the temperature of the fluid flowing in the thermal mass flow sensor.

37. A control system according to claim 36, wherein the mass flow sensor includes an outlet and the system controller employs readings of temperature, pressure and mass flow obtained from the respective temperature sensor interface, pressure interface and flow sensor interface to produce a compensated mass flow reading that more closely reflects the mass flow at the outlet of the mass flow sensor than a reading from the thermal mass flow sensor alone provides.

38. A control system comprising:

a mass flow controller including (A) an inlet for receiving fluid from an inlet supply line, (B) a thermal mass flow sensor constructed and arranged so as to sense mass flow of fluid at the inlet, and (C) an outlet valve; and

a pressure sensor constructed and arranged so as to sense the pressure of the fluid; and

a system controller including (i) a pressure sensor interface arranged so as to couple the system controller to the pressure sensor, and (ii) a mass flow interface arranged so as to couple the system controller to the thermal mass flow sensor;

wherein the system controller employs readings from the pressure sensor interface to compensate flow measurements obtained at the mass flow interface from the thermal mass flow sensor as the mass flow sensor senses mass flow of fluid at the inlet of the mass flow controller.

39. A control system according to claim 38, wherein the mass flow controller includes an outlet, and wherein at steady state equilibrium, mass flow at the inlet is equal to the mass flow at the outlet of the mass flow controller.

40. A control system according to claim 39, wherein the thermal mass flow sensor includes a capillary tube sensor and a flow bypass, the mass flow controller further includes a flow path between the thermal mass flow sensor and the outlet valve, the flow path including a dead space, and the mass flow Q_c through the capillary tube in steady state is given by:

$Q_c=\frac{d_c^2}{32<br><br>\mathrm{\mu <br><br>}}<br><br>\frac{P_i}{P_R}<br><br>\left(\frac{P_i-P}{L_c}\right)$

where, the total flow at the inlet of the MFC as measured by the thermal sensor Q_i is related to Q_c as follows;

Q_i=(1+α

)Q_c

wherein;

d_c=inside diameter of the capillary tube (m);

L_c=length of the capillary tube (m);

μ

=the gas viscosity (Poise);

P_i=the pressure at the inlet of the mass flow controller (Pa);

P_R=the pressure at the outlet of the mass flow controller (Pa);

P=the pressure in the dead volume of the mass flow controller (Pa); and

α

=the bypass ratio (dimensionless) defined as the ratio of flow through the bypass divided by the flow through the capillary tube.

41. A control system according to claim 39, wherein the thermal mass flow sensor includes a capillary tube and a bypass, and the mass flow controller further includes a flow path between the thermal mass flow sensor and the outlet valve, and wherein the split ratio of flow through the bypass and capillary tube remains constant so long as the flow through the thermal mass flow sensor remains constant, and wherein inlet pressure transients and the pressurization within the dead volume govern flow at the inlet.

42. A control system according to claim 41, wherein the outlet flow Q_o of the mass flow controller in response to dead-volume pressure transients dP/dt is defined as:

$Q_o=Q_i-\frac{T_R<br><br>V}{T_w<br><br>P_R}<br><br>\frac{d<br><br>P}{d<br><br>t}$

where;

P_R=pressure at standard temperature and pressure (760 Torr);

T_R=temperature at standard temperature and pressure (273°

K.);

T_w=wall temperature (temperature of the wall of the mass flow controller in °

K.);

V=volume of the dead volume (cm³);

Q_i=inlet flow to the mass flow controller (sccm); and

Q₀=outlet flow from the mass flow controller (sccm).

43. A control system according to claim 42, wherein the outlet flow Q_o of the mass flow controller in response to dead-volume pressure transients dP/dt is defined as:

Q_o=Q_i−

C₁(V/T)(dP/dt)

wherein;

Qo=the compensated sensed inlet flow rate (sccm);

Qi=the sensed inlet flow rate (sccm);

C₁=a normalizing constant relating the temperature (°

K) and pressure (torr) of the fluid to standard temperature (°

K) and pressure (torr);

V=the volume (cm³) between the sensor bypass and the outlet flow control valve,

T=the temperature (°

K) of the fluid within the dead volume, and

dP/dt=time rate of change of pressure within the dead volume (torr/min).

44. An electronic controller designed and arranged for controlling the mass flow Q_i of a gas through mass flow controller of the type including an inlet, an inlet flow sensor and bypass system, a control valve and an outlet, wherein a dead space is defined between the inlet flow sensor and bypass system and the control valve, and the inlet flow sensor and bypass system define an effective flow path inner diameter, the mass flow being controlled by the electronic controller in accordance with the following relationship:

$Q_c=\frac{d_c^2}{32<br><br>\mathrm{\mu <br><br>}}<br><br>\frac{P_i}{P_R}<br><br>\left(\frac{P_i-P}{L_c}\right)$

and Q_i=(1+α

)Q_cwherein;

d_c=inside diameter of the capillary tube (m);

L_c=length of the capillary tube (m);

μ

=the gas viscosity (Poise);

P_i=the pressure at the inlet of the mass flow controller (Pa);

P_R=the pressure at the outlet of the mass flow controller (Pa);

P=the pressure in the dead volume of the mass flow controller (Pa); and

α

=the bypass ratio (dimensionless) defined as the ratio of flow through the bypass divided by the flow through the capillary tube.

45. An electronic controller for use with a mass flow controller of the type having an inlet, an outlet, a wall and a dead volume, the electronic controller being designed and arranged so as to control the mass flow Q_o of a fluid at the outlet of a mass flow controller in response to dead volume pressure transients dP/dt of the fluid within the dead volume of the mass flow controller in accordance with the following relationship:

$Q_o=Q_i-\frac{T_R<br><br>V}{T_w<br><br>P_R}<br><br>\frac{d<br><br>P}{d<br><br>t}$

wherein;

P_R=pressure at standard temperature and pressure (760 Torr);

T_R=temperature at standard temperature and pressure (273°

K.);

T_w=wall temperature (temperature of the wall of the mass flow controller in °

K.);

V=volume of the dead volume (cm³);

Q_i=inlet flow to the mass flow controller (sccm); and

Q₀=outlet flow from the mass flow controller (sccm).

46. An electronic controller for use with a mass flow controller of the type having an inlet, an outlet and a dead volume, the electronic controller being designed and arranged so as to compensate the mass flow rate Q_o at the outlet of a mass flow controller in response to dead volume pressure transients dP/dt of a fluid within the dead volume of the mass flow controller in accordance with the following relationship:

Q_o=Q_i−

C₁(V/T)(dP/dt)

wherein;

Qo=the compensated sensed inlet flow rate (sccm);

Qi=the sensed inlet flow rate (sccm);

C₁=a normalizing constant relating the temperature (°

K) and pressure (torr) of the fluid to standard temperature (°

K) and pressure (torr);

V=the dead volume (cm³),

T=the temperature (°

K) of the fluid within the dead volume, and

dP/dt=time rate of change of pressure within the dead volume (torr/min).