Swirler-type gas-liquid two-phase flow metering device and method
12399045 ยท 2025-08-26
Assignee
Inventors
- Naiming LI (Yancheng, CN)
- Zhongbiao CHENG (Yancheng, CN)
- Feng JI (Yancheng, CN)
- Dengquan YUAN (Yancheng, CN)
Cpc classification
G01F1/325
PHYSICS
G01F1/3273
PHYSICS
G01F1/74
PHYSICS
International classification
Abstract
The disclosure discloses a swirler-type gas-liquid two-phase flow metering device, mainly including a swirler, a capacitance probe module, a hot-wire probe module, a hub and a data acquisition computer. A flow measurement method using the gas-liquid two-phase flow metering device includes: adjusting, by the swirler, flow patterns of an incoming gas-liquid two-phase flow into a uniform annular flow, measuring gas and liquid phase distribution by the capacitance probe module, and measuring gas and liquid phase flow velocity distribution by the hot-wire probe, and volumetric flow rates of gas, thereby obtaining liquid phases according to flow areas and average flow velocities of the gas and liquid phases. Compared with the existing multiphase flowmeter, the gas-liquid two-phase flow metering device of the disclosure has the advantages of small size, compact structure, small resistance loss, wide measurement range, high measurement accuracy, etc.
Claims
1. A swirler-type gas-liquid two-phase flow metering device, comprising a swirler, a capacitance probe module, a hot-wire probe module, a hub and a data acquisition computer; wherein the swirler, the capacitance probe module and the hot-wire probe module are sequentially arranged inside a test pipe along a flow direction of a gas-liquid two-phase fluid, the capacitance probe module and the hot-wire probe module are respectively connected to the hub through data lines, and the hub is connected to the data acquisition computer through a data line; and an upstream end of the test pipe is provided with an upstream flange, a downstream end of the test pipe is provided with a downstream flange, the upstream flange and the downstream flange are respectively connected upstream and downstream of a to-be-tested pipe gas-liquid two-phase flow pipe, the swirler comprises a central shaft and a helical blade, and an outer edge of the helical blade is kept attached to an inner wall of the test pipe, and wherein the capacitance probe module comprises a single-wire capacitance probe and a single metal wire that are arranged in parallel and both run through a center of the test pipe, and a distance between the single-wire capacitance probe and the metal wire is 2 mm to 5 mm; and the single-wire capacitance probe has a metal core at a center and an insulating layer as an outer laver.
2. The swirler-type gas-liquid two-phase flow metering device according to claim 1, wherein the hot-wire probe module comprises a plurality of hot-wire probes, the probes are arranged sequentially along the flow direction at an interval of 2 to 3 mm, and a head of each probe sequentially lengthens from the wall of the pipe to the center of the pipe along a pipe diameter direction with an amplitude of 1/10 to of a radius of the pipe.
3. The swirler-type gas-liquid two-phase flow metering device according to claim 1, wherein the capacitance probe module is about 1 to 1.5 times the pipe diameter from a tail end of the helical blade, and the hot-wire probe module is about 0.3 to 0.6 time the pipe diameter from the capacitance probe module.
Description
BRIEF DESCRIPTION OF DRAWINGS
(1)
(2)
(3)
(4)
(5)
(6) In the figures: 1test pipe, 2upstream flange, 3downstream flange, 4swirler, 5capacitance probe module, 6hot-wire probe module, 7hub, 8data acquisition computer, 9helical blade, 10central shaft, 11single-wire capacitance probe, 12single metal wire, 13metal core, 14insulating layer, 15hot-wire probe, 16fork prong, 17fork stem.
DETAILED DESCRIPTION OF THE EMBODIMENTS
(7) The technical solutions in the examples of the disclosure will be clearly and completely described below with reference to the accompanying drawings in the examples of the disclosure. It is apparent that the described examples are only a part of the examples, rather than all of the examples of the disclosure. All other examples obtained by those of ordinary skill in the art based on the examples of the disclosure without creative work are within the protection scope of the disclosure.
(8) As shown in
(9) As shown in
(10) As shown in
(11) As shown in
(12) As shown in
(13) The operating principle of the disclosure is described as follows:
(14) As shown in
(15) As shown in
(16)
(17) where L is the thickness of liquid film in contact with the probe; d is the diameter of the metal core 13; is the thickness of the insulating layer 14; and is the dielectric constant of the insulating layer 14.
(18) As can be seen from the formula, d, and are all constants, so the thickness of liquid film is linearly related to the capacitance of the probe. In addition, , which is the dielectric constant of the insulating layer 14, is related only to the material of the insulating layer, but not to the properties of the fluid, so the measured value is only dependent on the thickness of liquid film in contact with the capacitance probe 11, but independent of the fluctuations of parameters of the fluid, such as salt content, temperature and pressure.
(19) As shown in
(20) As shown in
(21) The method of the disclosure may specifically include the following steps: (a) measuring a length of liquid film L in contact with a capacitance probe, thereby calculating a thickness of liquid film of an annular flow L.sub.f=0.5L; (b) calculating, based on the thickness of liquid film L.sub.f, a gas flow area according to a formula
(22)
and a liquid-phase flow area according to a formula
A.sub.L=(DL.sub.f)L.sub.f; (c) determining whether a gas-phase flow velocity or a liquid-phase flow velocity is measured at a corresponding measuring point according to a position of a hot-wire probe and the measured thickness of liquid film, thereby obtaining a gas-phase average flow velocity V.sub.G and a liquid-phase average flow velocity V.sub.L; and (d) calculating a gas-phase volumetric flow rate according to a formula
Q.sub.G=A.sub.GV.sub.G,
and calculating a liquid-phase volumetric flow rate according to a formula
Q.sub.L=A.sub.LV.sub.L.
(23) It should be noted that the term include, comprise, or any other variant thereof is intended to cover a non-exclusive inclusion, such that a process, method, article or device that includes a series of elements includes not only those elements but also other elements not specifically listed, or elements that are inherent to the process, method, article or device. In the absence of further limitation, an element defined by the phrase including a . . . does not exclude the presence of the same element in the process, method, article or device including the element.
(24) Although the examples of the disclosure have been shown and described, for those of ordinary skill in the art, it can be understood that various changes, modifications, substitutions and variations can be made to these examples without departing from the principle and spirit of the disclosure, and the scope of the disclosure is defined by the appended claims and their equivalents.