Abstract:
A system for delivering pulses of a desired mass of gas to a tool, comprising: a mass flow controller including flow sensor, a control valve and a dedicated controller configured and arranged to receive a recipe of a sequence of steps for opening and closing the control valve so as to deliver as sequence of gas pulses as a function of the recipe. The mass flow controller is configured and arranged so as to operate in either one of at least two modes: as a traditional mass flow controller (MFC) mode or in a pulse gas delivery (PGD) mode. Further, the dedicated controller is configured and arranged to delivery pulses of gas in accordance with anyone of three different types of pulse gas delivery processes: a time based pulse delivery process, a mole based pulse delivery process and a profile based pulse delivery process.
Abstract:
A mass flow controller comprises: a pressure-based flow meter, a thermal-based flow meter, a control valve, and a system controller. The pressure-based flow meter and thermal-based flow meter each measure flow rate of mass through the mass flow controller. The control valve controls the flow rate in response to a control signal generated as a function of the flow rate as measured by thermal-based flow meter when the measured flow rate is relatively low, and as a function of the flow rate as measured by the pressure-based flow meter when the flow rate is relatively high. A comparison of the flow measurements of the two flow meters can be used to (a) sense pressure disturbances at low flow rates, and (b) sense when the thermal-based flow meter is out of calibration so that a zero offset signal can be applied to the thermal-based flow meter.
Abstract:
A system for delivering pulses of a desired mass of gas to a tool, comprising: a mass flow controller including flow sensor, a control valve and a dedicated controller configured and arranged to receive a recipe of a sequence of steps for opening and closing the control valve so as to deliver as sequence of gas pulses as a function of the recipe. The mass flow controller is configured and arranged so as to operate in either one of at least two modes: as a traditional mass flow controller (MFC) mode or in a pulse gas delivery (PGD) mode. Further, the mass flow controller includes an input configured to receive an input signal; an output configured to provide an output signal; a communication port configured to receive program instructions; memory configured and arranged to receive programming data determining the programmed configuration of the mass flow controller as either a digital or analog configuration; and a processor/controller for operating the mass flow controller in accordance with the programmed configuration.
Abstract:
A thermal mass flow controller for controlling flow rate of a fluid includes a conduit configured to receive the fluid, a pressure sensor that measures the pressure of the fluid as the fluid flows within the conduit, a temperature sensor that measures the ambient temperature of the fluid, and a thermal sensor that generates an output representative of the flow rate of the fluid. The thermal mass flow controller further includes a control system configured to monitor the output from the thermal sensor, the pressure measured by the pressure sensor, and the ambient temperature measured by the temperature sensor, to regulate flow of the fluid within the conduit so as to compensate for a shift in the thermal sensor output caused by thermal siphoning.
Abstract:
An integrated pressure and flow ratio control system includes N mass flow controllers MFCi (i=1, . . . , N) that each control the flow rate of a fluid Fi (i=1, . . . , N) flowing into a processing chamber. These N mass flow controllers are linked together by a digital communication network. One of the mass flow controllers is a master MFC, and the remaining N−1 MFCs are slave MFCs. The master MFC receives a pressure set point and a plurality N of flow ratio set points from a host controller, and communicates these set points to all the slave MFCs. In this way, the pressure in the chamber is maintained at the pressure set point and the flow ratios Qi/QT are maintained at the flow ratio set points, where Qi is flow rate of the i-th fluid Fi, and QT=Q1+Q2+ . . . QN is the sum of all N flow rates.
Abstract:
A system for dividing a single mass flow into a plurality N of secondary flows includes an inlet configured to receive the single mass flow, a master FRC (flow ratio controller), and one or more slave FRCs. Each FRC is connected to the inlet and including at least one flow channel. The master FRC and the slave FRCs include in combination a total of N flow channels. Each flow channel i (i=1, . . . , N) is connected to carry a corresponding one of the N secondary flows. In response to preselected ratio setpoints received from a host controller, the master FRC and the slave FRCs maintain ratios Qi/QT (i=1, . . . , N) between individual flow rates Qi (i=1, . . . , N) and a total flow rate QT at the preselected ratio set points.
Abstract:
A system for dividing a single mass flow into a plurality N of secondary flows includes an inlet configured to receive the single mass flow, a master FRC (flow ratio controller), and one or more slave FRCs. Each FRC is connected to the inlet and including at least one flow channel. The master FRC and the slave FRCs include in combination a total of N flow channels. Each flow channel i (i=1, . . . , N) is connected to carry a corresponding one of the N secondary flows. In response to preselected ratio setpoints received from a host controller, the master FRC and the slave FRCs maintain ratios Qi/QT (i=1, . . . , N) between individual flow rates Qi (i=1, . . . , N) and a total flow rate QT at the preselected ratio set points.
Abstract:
A mass flow controller comprises: a pressure-based flow meter, a thermal-based flow meter, a control valve, and a system controller. The pressure-based flow meter and thermal-based flow meter each measure flow rate of mass through the mass flow controller. The control valve controls the flow rate in response to a control signal generated as a function of the flow rate as measured by thermal-based flow meter when the measured flow rate is relatively low, and as a function of the flow rate as measured by the pressure-based flow meter when the flow rate is relatively high. A comparison of the flow measurements of the two flow meters can be used to (a) sense pressure disturbances at low flow rates, and (b) sense when the thermal-based flow meter is out of calibration so that a zero offset signal can be applied to the thermal-based flow meter.
Abstract:
An integrated pressure and flow ratio control system includes N mass flow controllers MFCi (i=1, . . . , N) that each control the flow rate of a fluid Fi (i=1, . . . , N) flowing into a processing chamber. These N mass flow controllers are linked together by a digital communication network. One of the mass flow controllers is a master MFC, and the remaining N-1 MFCs are slave MFCs. The master MFC receives a pressure set point and a plurality N of flow ratio set points from a host controller, and communicates these set points to all the slave MFCs. In this way, the pressure in the chamber is maintained at the pressure set point and the flow ratios Qi/QT are maintained at the flow ratio set points, where Qi is flow rate of the i-th fluid Fi, and QT=Q1+Q2+ . . . QN is the sum of all N flow rates.
Abstract translation:集成的压力和流量比控制系统包括N个质量流量控制器MIP(i = 1,...,N),每个控制器控制流体F i i的流量 (i = 1,...,N)流入处理室。 这些N个质量流量控制器通过数字通信网络连接在一起。 质量流量控制器之一是主MFC,其余的N-1 MFC是从MFC。 主MFC从主机控制器接收压力设定点和多个N个流量设定点,并将这些设定点传送到所有从MFC。 以这种方式,室中的压力保持在压力设定点,并且流量比Q 1 / Q T T T保持在流量比设定点,其中Q 第i个流体F i i的流速,Q 3 = Q 1 + Q 2, SUB> 2 +。 。 。 Q N N是所有N个流速的总和。
Abstract:
A system for and method of compensating for attitude sensitivity of at least two thermal sensor coils mounted on a tube through which a fluid flows along a common axis of flow for use in generating a flow measurement signal representative of the flow of fluid through the tube is disclosed. One of the coils is adapted in provide thermal energy to the fluid flowing through the tube at an upstream location so as to establish and measure the upstream temperature of the fluid at the upstream location, and one of the coils is adapted to measure the downstream temperature of the fluid at a downstream location. The flow measurement signal is a function of the difference between the measured upstream and downstream temperatures. The system includes structure for, and the method includes the steps of measuring the force of gravity in the direction of the common axis; and modifying the flow measurement signal as a function of the measured force of gravity.