Measuring arrangement

Patent metadata

Field	Value
Publication number	US-10641635-B2
Application number	US-201515513205-A
Country	US
Kind code	B2
Filing date	Sep 2, 2015
Priority date	Sep 25, 2014
Publication date	May 5, 2020
Grant date	May 5, 2020

Abstract

A measuring arrangement for determining flow velocity of at least one liquid phase and/or a gas phase of a vapor or a fluid composed of a liquid and a gaseous phase or a supercritical fluid, comprising a measuring tube, on or in which at least one sensor element of at least a first flow measuring device is arranged for measuring the liquid phase or the gas phase, wherein the measuring tube has at least an inflow region and an outflow region, wherein between these two regions a central region is arranged, whose measuring tube cross section has a greater area than the area of the measuring tube cross section of the outflow region or of the inflow region, and method for ascertaining flow of phases of a vapor or of a fluid composed of a liquid and a gaseous phase, or a supercritical fluid.

First claim

The invention claimed is:

1. A measuring arrangement for determining a flow velocity of at least one liquid phase and/or a gas phase of a vapor or a fluid composed of a liquid phase and a gaseous phase, or a supercritical fluid, comprising:
a measuring tube;
at least one sensor element for determining a flow velocity of the liquid phase and at least one sensor element for determining a flow velocity of the gas phase, wherein:
said measuring tube has at least an inflow region, an outflow region, and a central region between said inflow region and said outflow region,
the measuring tube comprises a measuring tube cross section for each region,
the measuring tube cross section of said central region has a greater area than the area of the measuring tube cross section of said outflow region or of said inflow region, and
the measuring tube has a first transition region and a second transition region, within the first transition region, the area of the measuring tube cross section continuously increases to the central region, and within the second transition region, the area of the measuring tube cross section decreases from the central region,
wherein said at least one sensor element for determining a flow velocity of the liquid phase and said at least one sensor element for determining the gas phase are arranged in the central region,
wherein said central region of said measuring tube has a channel for collecting the liquid phase,
wherein said central region of said measuring tube has a gasline segment,
wherein said gasline segment has a greater cross sectional area than said channel,
wherein said at least one sensor element for determining the flow velocity of the gas is arranged in the gasline segment of said measuring tube, and
wherein said at least one sensor element for determining the flow velocity of the liquid phase is arranged in the channel of said measuring tube.

2. The measuring arrangement as claimed in claim 1 , wherein:
the measuring arrangement has a fill level sensor or a limit level sensor for determining the fill level or for displaying an achieved limit level of the liquid phase in said measuring tube.

3. The measuring arrangement as claimed in claim 1 , wherein:
said measuring tube is connectable at each end terminally into a process line.

4. The measuring arrangement as claimed in claim 1 , wherein:
the measuring tube has in an installed state an orientation, in the case of which said inflow region and said outflow region are arranged essentially at a same height with respect to a force of gravity.

5. The measuring arrangement as claimed in claim 1 , wherein:
a straight connecting line between intersections of the measuring tube centerline with an end face of said measuring tube at said inflow region and an end face of said measuring tube at said outflow region extends horizontally, respectively deviates from the horizontal by no more than 20°.

6. The measuring arrangement as claimed in claim 1 , wherein:
said measuring tube is connectable at each end terminally into a process line by means of a flange connection.

7. The measuring arrangement as claimed in claim 1 , wherein:
a straight connecting line between intersections of the measuring tube centerline with an end face of said measuring tube at said inflow region and an end face of said measuring tube at said outflow region extends horizontally, respectively deviates from the horizontal by no more than 10°.

Assignees

• Flowtec Ag

Inventors

• Hocker Rainer
• Popp Oliver

Classifications

• G01F1/34

  by measuring pressure or differential pressure · CPC title

• G01F15/00

  Details of, or accessories for, apparatus of groups G01F1/00 - G01F13/00 insofar as such details or appliances are not adapted to particular types of such apparatus · CPC title

• G01F15/08 Primary

  Air or gas separators in combination with liquid meters; Liquid separators in combination with gas-meters · CPC title

• G01F1/002

  wherein the flow is in an open channel · CPC title

• G01F1/68

  by using thermal effects · CPC title