IP Library Granted Patent US 8,423,303
Granted Patent B2
US 8,423,303 · App. 12/377,118 · Granted Apr 16, 2013

Method for real time measurement of mass flow rate of bulk solids

Inventors: Per Soleng (Hareid, NO); Per Huse (Ålesund, NO)
Assignee: Rolls-Royce Marine AS
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Quick Facts
Patent No.
US 8,423,303
App. No.
12/377,118
Granted
Apr 16, 2013
Kind
B2
Abstract

The mass flow rate of bulk solids in a pneumatic transport system is measured in real time. At least two pressure gauges (P 1 , P 2 ) are provided in a pipe section of the transport system. The pressure drop ΔP between the pressure gauges is determined during a gas-solids flow of air and bulk solids through the pipe section. The suspension density ρ sus of the flowing mixture of air and bulk solids is calculated. The bulk solids mass flow rate M s at a given location along a given length of a pipeline is estimated based at least on the suspension density ρ sus of the flowing mixture.

Claims (65)

1. A method for real time measurement of mass flow rate of bulk solids, wherein said bulk solids are loaded, or unloaded, by a pneumatic transport system having a pipe section along which are located at least two spaced-apart pressure gauges (P 1 ,P 2 ), the method comprising:

Determining pressure drop ΔP between said pressure gauges based on information provided by the pressure gauges during gas-solids flow of air and bulk solids through the pipe section,

by a computing device, calculating suspension density ρ sus of the flowing mixture of air and bulk solids based on the pressure drop ΔP, and

by a computing device, estimating the bulk solids mass flow rate M s at a given location along a given length of a pipeline, based at least on the calculated suspension density ρ sus of the flowing mixture,

wherein said suspension density ρ sus of the flowing mixture is calculated using the following formula:

Δ

P

=

1

2

K

ρ

sus

LV

2

D

(

1

)

where K is the coefficient of friction of the bulk solid flowing through the pipeline,

D is the pipe diameter,

L is the length of the pipe section between pressure gauges (P 1 , P 2 ),

V is the local air velocity at the section where the first pressure gauge (P 1 ) is arranged.

2. A method according to claim 1 , wherein said suspension density ρ sus is defined as:

ρ

sus

=

M

s

+

M

air

Q

s

+

Q

air

(

2

)

where M s is the solids mass flow rate,

M air is the air mass flow rate,

Q s is the solids volume flow rate at the section 1 and Q s =M s /ρ s ,

Q air is the air volume flow rate at the section 1;

wherein the mass flow rate of bulk solids is estimated by:

V

s

=

M

s

ρ

s

(

3

)

where ρ s is the solids density.

3. A method according to claim 1 , further comprising calculating cumulative mass flow of solids through a pipe section of the pneumatic transport system based on the mass flow of bulk solids as estimated in real time.

4. A method according to claim 3 , wherein said bulk solids is dry cement or similar material.

5. A method according to claim 1 , further comprising controlling the airflow rate based on the values from the measurements to control the mass flow rate of bulk material.

Assignments (2)
CHANGE OF NAME Recorded Aug 27, 2020
From: ROLLS-ROYCE MARINE AS
To: KONGSBERG MARITIME CM AS
Reel/Frame 053652/0886 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Feb 27, 2009
From: SOLENG, PER; HUSE, PER
To: ROLLS-ROYCE MARINE AS
Reel/Frame 022324/0270 →
Priority Claims (1)
NO 20063698 · Aug 17, 2006 · national
Continuity (1)
Related Publication 20100241368A1 · Sep 23, 2010