Gas control system
US-12025319-B2 · Jul 2, 2024 · US
US10514712B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10514712-B2 |
| Application number | US-201615244264-A |
| Country | US |
| Kind code | B2 |
| Filing date | Aug 23, 2016 |
| Priority date | Aug 31, 2015 |
| Publication date | Dec 24, 2019 |
| Grant date | Dec 24, 2019 |
A practical reading order for non-experts. Skip the full description unless you need deep technical detail.
What the patent document calls the invention.
A short plain-language summary of the technical disclosure.
Who owns or filed the patent and who is credited as inventor.
Filing, priority, publication, and grant dates set the timeline.
The legal scope of protection — read this for what is actually claimed.
Technology tags used to group this patent with similar filings.
Prior art links and similar publications in this corpus.
Official abstract text for this publication.
Methods, systems, and apparatus for pressure-based flow measurement are provided. A processor receives, from the pressure-based mass flow controller (MFC), an upstream pressure value Pu. The processor computes, for the pressure-based mass flow controller (MFC), a downstream pressure value Pd based on the received upstream pressure value Pu. The processor computes, for the pressure-based mass flow controller (MFC), a flow rate Q based on the received upstream pressure value Pu and the computed downstream pressure value Pd. The processor controls a flow through the pressure-based mass flow controller (MFC) based on the computed flow rate Q. The methods, systems, and apparatus can be used for flow measurement in non-critical or un-choked flow conditions.
Opening claim text (preview).
What is claimed is: 1. A system for pressure-based flow measurement of a fluid flow, the system comprising: a pressure-based mass flow controller (MFC) including a flow control valve, a flow restrictor, and a pressure sensor upstream of the flow restrictor, wherein the flow control valve, flow restrictor and pressure sensor are disposed along a flow stream; one or more processors coupled with the pressure-based mass flow controller (MFC); and memory coupled to the one or more processors, the memory including instructions which, when executed by the one or more processors, cause the one or more processors to (i) receive, from the pressure-based mass flow controller (MFC), a sensed upstream pressure value P u ; (ii) calculate, for the pressure-based mass flow controller (MFC), without a measured flow input, a downstream pressure value P d based on the received sensed upstream pressure value P u ; (iii) calculate, for the pressure-based mass flow controller (MFC), without a measured downstream pressure, a flow rate Q based on the received upstream pressure value P u and the calculated downstream pressure value P d , where the instructions to calculate the downstream pressure P d and the instructions to calculate the flow rate Q include instructions to recursively calculate, based on P u , the flow rate Q based on calculated P d and the downstream pressure P d based on calculated Q until the values of Q and P d converge within an error threshold; and (iv) control a flow through the pressure-based mass flow controller (MFC) based on the calculated flow rate Q. 2. The system of claim 1 , wherein the flow restrictor comprises a flow nozzle or orifice. 3. The system of claim 1 , where the instructions to calculate the downstream pressure P d and the instructions to calculate the flow rate Q include instructions to set P d to an initial value P d0 . 4. The system of claim 1 , where the instructions to calculate the downstream pressure P d and the instructions to calculate the flow rate Q include: instructions to set P d to an initial value P d0 , and instructions to recursively calculate the flow rate Q and P d based on calculated P d and Q, respectively, until the values of Q and P d converge within a pre-defined error threshold; receive, from the pressure-based mass flow controller (MFC), an updated upstream pressure value P u ; and determine, based on P d and P u , whether a flow condition in the pressure-based mass flow controller (MFC) is critical or non-critical flow; and calculate Q based on whether the flow condition is critical or non-critical flow; and update P d based on the calculated value of Q. 5. The system of clause 4 , where the instructions to update P d based on the calculated value of Q include instructions to calculate the downstream pressure value P d according to an equation P d =P d0 +ƒ(Q, P u , γ, M), where P d0 is an initial downstream pressure, γis a ratio of specific heat of a flowing gas, M is a molecular weight of the flowing gas, and f( ) is a function of Q, P u , γ, M. 6. The system of claim 5 , where ƒ is a linear function of Q, a linear function of P u , a linear function of γ, and a linear function of M. 7. The system of claim 4 , where the instructions to determine whether the flow condition is critical or non-critical include instructions to determine that a flow condition is critical if P d /P u is less than [2/(γ+1)]{circumflex over ( )}[γ/(γ−1)]; and determine that a flow condition is non-critical if P d /P u , is greater than or equal to [2/(γ+1)]{circumflex over ( )}[γ/(γ−1)], where γis a ratio of specific heat of a flowing gas. 8. The system of claim 4 , where the instructions to calculate Q include instructions to calculate Q using a critical flow equation if the flow condition is critical; and calculate Q using a non-critical flow equation, if the flow condition is non-critical. 9. The system of claim 4 , where the instructions to calculate Q include instructions to, upon determining that the flow condition is non-critical calculate a critical flow rate Q cf using a critical flow equation; calculate a non-critical flow rate Q ncf using a non-critical flow equation; and calculate Q based on a weighting factor w, the critical flow rate Q cf , and the non-critical flow rate Q ncf , where Q=w*Q cf +(1−w)*Q ncf . 10. The system of claim 9 , where the weighting factor w is calculated according to w=ƒ w (Q, P u , P d , γ, M), where γis a ratio of specific heat of a flowing gas, M is a molecular weight of the flowing gas and ƒ w ( )is a function of Q, P u , P d , γ, M. 11. The system of claim 9 , where w=1 if P d /P u is less than Pr min ; w=0 if P d /P u is greater than Pr max ; and w=1−[(P d /P u −Pr min )/(Pr max −Pr min )]{circumflex over ( )}N if P d /P u is greater than Pr min and less than Pr max , where Pr min and Pr max are variables between 0 and 1 that are determined based on a ratio of specific heat of a flowing gas γ, the flow rate Q, and a nozzle orifice size of the flow-restricting orifice of the pressure-based mass flow controller (MFC). 12. The system of claim 11 , where N is a positive exponential coefficient that is determined based on γ, Q, and the nozzle orifice size of the flow-restricting orifice of the pressure-based mass flow controller (MFC). 13. The system of claim 1 , wherein the memory further includes instructions which, when executed by the one or more processors, cause the one or more processors to: receive an initial downstream pressure value P d0 for the pressure-based mass flow controller (MFC); set a stored downstream pressure value P d to the received initial downstream pressure value P d0 ; recursively calculate the flow rate Q and P d based on calculated Q and P d respectively, until the values of Q and P d converge within a pre-defined error threshold; receive, from the pressure-based mass flow controller (MFC), an upstream pressure value P u ; determine, based on P d and P u , whether a flow condition in the pressure-based mass flow controller (MFC) is critical or non-critical flow; calculate Q based on whether the flow condition is critical or non-critical; and update P d based on the calculated value of Q; and cause the one or more processors to, after the calculated flow rate Q and the stored downstream pressure value P d converge to respective values within a pre-defined error threshold, control a flow through the pressure-based mass flow controller (MFC) based on the calculated flow rate Q. 14. The system of claim 13 , where the initial downstream pressure value P d0 corresponds to a measured upstream pressure value before gas begins flowing through the pressure-based mass flow controller (MFC). 15. A non-transitory machine-readable medium comprising instructions which, when executed by a machine, cause the machine to: receive, from a pressure-based mass flow controller (MFC), an upstream pressure value P u ; calculate, for the pressure-based mass flow controller (MFC), without a measured flow input, a downstream pressure value P d based on the received upstream pressure value P u ; calculate, for the pressure-based mass flow controller (MFC), without a measured downstream pressure, a flow rate Q based on the received upstream pressure value P u and the calculated downstream pressure value P d , where the instructions to calculate the downstream pressure P d and the instructions to calculate the flow rate Q include instructions to recursively calculate, based on P u , the flow rate Q based on calculated P d and the downstream pressure P d based on calculated Q until the values of Q and P d co
by action on throttling means (G05D7/0688, G05D7/0694 take precedence) · CPC title
Correcting or compensating means · CPC title
with electrical or electro-mechanical indication (G01F1/37 and G01F1/38 take precedence) · CPC title
Valves (valves in general F16K) · CPC title
by measuring pressure or differential pressure · CPC title
Related publications grouped by family.
Answers are generated from the same data shown on this page.