Flow measurement compensation technique for use with an averaging pitot tube type primary element

• US 5,817,950 A
• Filed: 01/04/1996
• Issued: 10/06/1998
• Est. Priority Date: 01/04/1996
• Status: Expired due to Term

• Current Assignee: Rosemount Incorporated (Emerson Electric Company)
• Original Assignee: Rosemount Incorporated (Emerson Electric Company)
• Inventors: Bischoff, Brian J., Wiklund, David E.
• Primary Examiner(s): Dougherty, Elizabeth L.
• Assistant Examiner(s): PATEL, HARSHAD R
• Application Number:
  US08/582,905
• Time in Patent Office: 1,006 Days
• Field of Search: 73/861.65, 73/861.66, 73/861.02, 73/861.04
• US Class Current: 73/861.66
• CPC Class Codes: G01F 1/46 Pitot tubes

Abstract

A transmitter in a process control system for measuring flow rate measures total pressure (P_TOT) and differential pressure (h) of process fluid flowing through a process pipe. The static pressure (P_STAT) is determined based upon the total pressure (P_TOT). The calculated static pressure is used to determine the fluid density (ρ) and the gas expansion factor (Y₁) of the process fluid flowing in the pipe. This information is used to calculate flow rate (Q) of the process fluid.

Claims

1. A transmitter for coupling to an averaging pitot tube type primary element introduced into a pipe through a single opening in the pipe having a generally forward facing tube and a second tube, the transmitter calculating flow rate (Q) of process fluid and comprising:

a total pressure sensor for sensing total pressure (P_TOT) of the process fluid using the generally forward facing tube;

a differential pressure sensor for sensing a differential pressure (h) in the process fluid between the generally forward facing tube and the second tube;

circuitry which calculates flow rate (Q) based upon the total pressure (P_TOT) the differential pressure (h), fluid density (ρ

), and the gas expansion factor (Y₁) wherein fluid density (ρ

) and the gas expansion factor (Y₁) are calculated as a function of the total pressure (P_TOT) and differential pressure (h) ; and

I/O circuitry for coupling to a process control loop and transmitting the calculated flow rate (Q).

2. The transmitter of claim 1 including circuitry to wholly power the transmitter with power received from the process control loop.

3. The transmitter of claim 1 wherein the calculating circuitry calculates static pressure (P_STAT) as a function of the total pressure (P_TOT) and the differential pressure (h), and wherein fluid density (ρ

) and the gas expansion factor (Y₁) of the process fluid are calculated as a function of static pressure (P_STAT) and thereby as a function of total pressure (P_TOT).

4. The transmitter of claim 3 wherein a difference between the static pressure (P_STAT) and the total pressure (P_TOT) is a linear relation to differential pressure (h).

5. The transmitter of claim 4 wherein static pressure (P_STAT) is calculated as:

space="preserve" listing-type="equation">P.sub.TOT -P.sub.STAT =C.sub.1 h

where;

C₁ is a constant.

6. The transmitter of claim 3 wherein the difference between static pressure (P_STAT) and total pressure (P_TOT) is calculated based upon a polynomial relation to differential pressure (h).

7. The transmitter of claim 1 including a process fluid temperature sensor coupled to the circuitry which calculates flow rate (Q) and calculation of flow rate (Q) is further based upon process fluid temperature.

8. The transmitter of claim 1 wherein the process control loop is a two wire process control loop.

9. A method for use in a transmitter of determining flow (Q) of a process fluid, comprising:

introducing an averaging pitot tube type primary element into a single opening in the pipe, the pitot tube having a generally forward facing tube and a second tube;

sensing a total pressure (P_TOT) generated by the forward facing tube of the averaging pitot tube type primary element;

sensing a differential pressure (h) generated by the second tube of the averaging pitot tube type element; and

calculating flow rate (Q) based upon static pressure (P_STAT), total pressure (P_TOT) and differential pressure (h) , wherein static pressure (P_STAT) is determined based upon total pressure (P_TOT) and differential. pressure (h).

10. The method of claim 9 including:

calculating fluid density (ρ

) based upon the calculated static pressure (P_STAT) and wherein the step of calculating flow rate (Q) is further based upon fluid density (ρ

).

11. The method of claim 9 including:

calculating gas expansion factor (Y₁) based upon the calculated static pressure (P_STAT), and wherein the step of calculating flow rate (Q) is further based upon the gas expansion factor (Y).

12. The method of claim 9 wherein a difference between the static pressure (P_STAT) and the total pressure (P_TOT) is a linear relationship to differential pressure (h).

13. The method of claim 12 wherein the linear relationship is:

space="preserve" listing-type="equation">P.sub.TOT -P.sub.STAT =C.sub.1 h

where;

C₁ is a constant.

14. The method of claim 9 wherein the difference between static pressure (P_STAT) and total pressure (P_TOT) is calculated using a polynomial relationship to differential pressure (h).

15. The method of claim 9, including:

transmitting the flow rate (Q) over a process control loop.

16. The method of claim 15 wherein transmitting the flow rate (Q) over a process control loop includes transmitting the flow rate (Q) over a two-wire process control loop.

17. The method of claim 9 including:

measuring temperature of the process fluid; and

including the temperature of the process fluid in the step of calculating flow rate (Q).

18. The method of claim 9, including:

coupling the transmitter to a process control loop; and

wholly powering the transmitter from the process control loop.