Flowmeter for gas-entrained solids flow

• US 4,930,356 A
• Filed: 04/20/1989
• Issued: 06/05/1990
• Est. Priority Date: 04/20/1989
• Status: Expired due to Fees

• Current Assignee: The United States of America As Represented By The Secretary of Agriculture
• Original Assignee: United States Department of Energy (Government of the United States of America)
• Inventors: Porges, Karl G.
• Primary Examiner(s): NOT, DEFINED
• Application Number:
  US07/341,004
• Time in Patent Office: 411 Days
• Field of Search: 73/861.04, 73/861.08, 73/32 R, 324/61 R
• US Class Current: 73/861.08
• CPC Class Codes: G01F 1/64 by measuring electrical currents passing through the fluid flow; measuring electrical potential generated by the fluid flow, e.g. by electrochemical, contact or friction effects G01F1/58 takes precedence
• CPC Class Codes: G01F 1/74 Devices for measuring flow of a fluid or flow of a fluent solid material in suspension in another fluid
• CPC Class Codes: G01F 1/86 Indirect mass flowmeters, e.g. measuring volume flow and density, temperature or pressure

Abstract

An apparatus and method for the measurement of solids feedrate in a gas-entrained solids flow conveyance system. The apparatus and method of the present invention include a vertical duct connecting a source of solids to the gas-entrained flow conveyance system, a control valve positioned in the vertical duct, and a capacitive densitometer positioned along the duct at a location a known distance below the control valved so that the solid feedrate, Q, of the gas entrained flow can be determined by

Q=SρφV.sub.S

where S is the cross sectional area of the duct, ρ is the density of the solid, φ is the solid volume fraction determined by the capacitive densitometer, and v_S is the local solid velocity which can be inferred from the konown distance of the capacitive densitometer below the control valve.

Claims

1. A flowmeter for measurement of solids feedrate in a gas-entrained solids flow conveyance system comprising:

a vertical duct connected at the top end to a source of solids for gas-entrainment and connected at the bottom end to a gas-entrained flow conveyance system,

a control valve positioned in said vertical duct capable of restricting the flow of solids so that below said control valve, the solids fall by force of gravity, and

a capacitive densitometer positioned on said duct at a location a known distance below said control valve,

whereby the solid feedrate, Q, of a gas entrained flow can be determined by

space="preserve" listing-type="equation">Q=Sρ

φ

v.sub.s

where S is the cross sectional area of said duct, ρ

is the density of the solid, φ

is the solid volume fraction determined by said capacitive densitometer, and v_S is the local solid velocity which can be inferred from the known distance of said capacitive densitometer below said control valve.

2. The flowmeter of claim 1 in which said capacitive densitometer includes a means for uniformizing the electric field between the capacitor plates.

3. The flowmeter of claim 1 in which said capacitive densitometer includes a driving electrode plate and a receiving electrode plate positioned about said vertical duct so that a flow of solids in said vertical duct will pass between said driving electrode plate and said receiving electrode plate.

4. The flowmeter of claim 2 in which said control valve includes slidable blades capable of restricting the flow of solids in said vertical duct in such a way that a flow of solids is centered in said vertical duct.

5. The flowmeter of claim 4 including:

a feedhopper for the containment of solids and opening into the top of said vertical duct,

a second valve positioned in said vertical duct below said feedhopper and above said control valve, said second valve capable of completely stopping flow of solids in said vertical duct, and

an entry tee connecting the bottom of said vertical duct to the gas-entrainment conveyance system.

6. The flowmeter of claim 5 in which said entry tee is shaped to present an impact surface to a vertically falling solids stream from said vertical duct at approximately 45 degrees and further in which said entry tee includes an exit to the gas-entrainment conveyance system shaped so as to allow a flow of solids to enter the gas-entrainment conveyance system without further wall impacts.

7. The flowmeter of claim 6 in which said capacitive densitometer includes:

an oscillator connected to said driving electrode plate, said oscillator capable of sending a signal to said driving electrode plate, and

a preamplifier connected to said receiving electrode plate.

8. The flowmeter of claim 7 including a computer means connected to said densitometer, said computer means capable of calculating the flow of solids in said vertical duct.

9. The flowmeter of claim 8 in which said computer means is also connected to said control valve, and further in which said slidable blades of said control valve operate under the control of said computer means.

10. The flowmeter of claim 1 in which said vertical duct has a rectangular cross section and further in which said capacitive densitometer includes two parallel plates.

11. The flowmeter of claim 10 in which said capacitive densitometer includes a driving electrode plate and a receiving electrode plate.

12. The flowmeter of claim 10 including a grounded guard strip positioned outside the perimeter of said receiving electrode plate.

13. A method for measuring the feedrate of solids in a gas-entrained solids flow conveyance system comprising the steps of:

introducing a supply of solids into the top end of a vertical duct,

restricting the flow of solids the vertical duct with a control valve so that below the control valve, the solids fall by force of gravity,

measuring the solid volume fraction of the solids in the vertical duct with a capacitive densitometer positioned on the vertical duct at known distance below the control valve,

injecting the solids from the vertical duct into the gas-entrained conveyance system,

whereby the solid feedrate, Q, of a gas entrained flow can be determined in accordance with the equation

space="preserve" listing-type="equation">Q=Sρ

φ

v.sub.S

where S is the cross sectional area of said duct, ρ

is the density of the solid, φ

is the solid volume fraction determined by the capacitive densitometer, and v_S is the local solid velocity which can be inferred from the known distance of the capacitive densitometer below the control valve.

14. The method of claim 13 in which the solid feedrate is calculated by a computer means connected to the capacitive densitometer.

15. The method of claim 14 in which the flow of solids in the vertical duct is restricted by the control valve under the control of the computer means.