CN1043988A - Measurement method of gas-solid-liquid-solid two-phase flow - Google Patents

Abstract

The invention discloses a method for measuring gas-solid-liquid-solid two-phase flow, which comprises determining a first pressure measuring point (1) near the entrance of a diffuser pipe of a differential pressure flowmeter. When there is a two-phase flow passing through, find the second pressure measuring point (2) downstream of the first pressure measuring point in the diffuser, so that the flow rate G _S calculated by the pressure difference ΔP _S between the two pressure measuring points is the same as that before the hopper The flow G _{and B} read by the standard flow meter are equal. When the pure fluid flows through, find two pressure measuring points (3) and (4) in the straight pipe so that the pressure difference thereof is equal to the pressure difference of (1) and (2). The two-phase flow of solid particles and fluid mixed into the solid hopper can be calculated by calculating the coefficient K through the two-phase flowmeter, and the solid flow rate can be obtained. The method is simple and easy to implement and has high measurement precision.

Description

The measuring method of gas-liquid fixed double phase flow

The invention belongs to the measuring method of gas-liquid fixed double phase flow.

Japan crosses the limit gold and helps principle and the measuring method of having introduced this kind flowmeter in article " solid-gas phase differential pressure flowmeter " literary composition that is published in monthly magazine " meter dress " November nineteen eighty-two.Flowmeter partly is made up of straight tube and diffuser pipe two as shown in Figure 1, and level is installed.At first determine first pressure tap (1), find out second pressure tap (2), solids speed is equated with point (1) speed at the diffuser pipe downstream part in the diffuser pipe porch.Between point (1) and point (2) apart from x ₀, calculate with following formula

X ₀Tan φ/r=(1-φ ₀)/(φ ₀) wherein r be the inside radius of diffuser pipe porch, φ ₀Be diffuser pipe porch solid and gas velocity ratio, φ is that diffuser pipe partly expands the angle.When pure gas passes through, find straight sections two pressure taps (3), (4) then, the scale-up factor k of the relation of the pressure reduction between it and (1), (2) point-to-point transmission pressure reduction.By the pressure reduction △ P of point (1) with point (2) _aCalculate gas flow G _a, again by the pressure reduction △ P and the △ P of point (3) point (4) _aObtain solid and gas mixing ratio m with m=K (△ P-k △ Pa)/(k △ Pa), wherein K is a proportionality constant.Then solid flow is G _S=mG _a, use temperature at last, pressure correction is to the standard state analog value.To measure the speed of solids and gas when adopting said method to determine second pressure tap (2) respectively, very bother, and error be big.

The measuring method that the purpose of this invention is to provide a kind of gas-liquid fixed double phase flow.

Fig. 1 is the flowmeter structure synoptic diagram; Fig. 2 determines point (2) synoptic diagram; Fig. 3 determines that point (3) point (4) is apart from synoptic diagram.

Elaborate below in conjunction with accompanying drawing.

By the layout of figure (2), the front is high precision flow measuring apparatus (9), and the centre is solids loading hopper (8), and the back is a flowmeter to be measured.Flow score straight-tube portion (6) and diffuser pipe portion (7) two parts.(1), (2), (3), (4) are pressure tap, (5) are point for measuring temperature.Partly the expanding angle φ and should satisfy two conditions of diffuser pipe, the one, the φ angle should enough can be ignored with the collision that guarantees solids and wall greatly, and makes (1), (2) two pressure difference signal enough big.The 2nd, the φ angle can not be excessive, in order to avoid fluid is separated, for should be 6 °-16 ° with air as the two-phase flow φ angle of fluid.Because solids are in its speed of collision of straight-tube portion and tube wall speed less than fluid, collision at diffuser pipe porch particle and tube wall can be ignored, this moment, particle began accelerated motion, because the deceleration of fluid makes particle a bit reduce speed now from certain, so, to distance enough far away, always can find 2 points from the diffuser pipe porch, the movement velocity of particle equates on these 2.Promptly be between 2 o'clock solids convection cell momentum change into zero, therefore, the flow of being calculated by the differential manometer of this point-to-point transmission is the flow of pure fluid.

When two-phase flow passes through, find out second pressure tap (2) at diffuser pipe (7) first pressure tap (1) downstream parts, make by pressure reduction △ P between this two pressure tap (1), (2) _SCalculate flow G _SThe flow G that reads with the preceding proving flowmeter (9) of loading hopper (8) _BEquate.G _SComputing formula as follows:

$G_S=\frac{{\mathrm{\pi d}}^2{}_2}{4}\mu \sqrt{\frac{{\mathrm{2△P}}_S\rho }{(\frac{d_2}{d_1}{)}^4\mathrm{-1}}}$

△ P wherein _SBe (1), (2) point-to-point transmission pressure reduction, d ₁, d ₂Be respectively (1), (2) two locate diameter, μ=0.97 is a coefficient of flow, ρ is a fluid density.In the actual measurement during by two-phase flow (1), (2) point-to-point transmission pressure reduction be △ P _FWhen pure fluid flows through, find out two pressure taps (3), (4) in straight sections (6), make (3), pressure reduction and diffuser pipe interior (1) between (4) two, pressure reduction equates between (2) two.In the actual measurement, (3), (4) point-to-point transmission pressure reduction are △ P during by two-phase flow.Adding quality to solid feed hopper is M _SSolids, calculate COEFFICIENT K with the mixed two-phase flow of fluid by two-phase flow meter, its computing formula is as follows:

$K=M_S/{\∫}_0^T\mathrm{GF}\frac{\mathrm{\ΔP}-\mathrm{\Δ}{P}_F}{\mathrm{\Δ}{P}_F}\mathrm{dt}$ ，

$G_F=\frac{{\mathrm{\pi d}}^2{}_2}{4}\mu \sqrt{\frac{{\mathrm{2△P}}_F\rho }{(\frac{d_2}{d_1}{)}^4\mathrm{-1}}}$

, wherein T is M for the quality of being totally lost _SThe solids required time, G _FBe fluid flow.Use then

G _S=K (△ P-△ P _F)/(△ P _F) GF calculates solid flow.

Adopt advantage of the present invention to be:

(1) (1), (2) two determine than existing method precision height are convenient;

(2) the K value is definite more simple than Calculation Method, the precision height;

(3) diffuser pipe partly expands definite flowing field stability that guaranteed at angle.

Claims (1)

1. A gas-solid, liquid-solid two-phase flow measurement method a. First determine the half expansion angle ψ of the diffuser tube of the differential pressure flowmeter; b. Determine the first pressure measurement point [1] near the entrance of the diffuser; It is characterized by: c. When there is a two-phase flow, find the second pressure measurement point [2] downstream of the first pressure measurement point in the diffuser [7], so that the pressure between the two pressure measurement points [1] and [2] The flow G _s calculated by the difference △P _s is equal to the flow G _B read by the standard flow meter [9] in front of the hopper [8], and the calculation formula of G _s is as follows: ${\mathrm{<span\; class="notranslate">\; G</span>}}_{\mathrm{<span\; class="notranslate">\; S</span>}}\mathrm{<span\; class="notranslate">\; =</span>}\frac{{\mathrm{<span\; class="notranslate">\; \pi d</span>}}^{\mathrm{<span\; class="notranslate">\; 2</span>}}{}_{\mathrm{<span\; class="notranslate">\; 2</span>}}}{\mathrm{<span\; class="notranslate">\; 4</span>}}\mathrm{<span\; class="notranslate">\; mu</span>}\sqrt{\frac{{\mathrm{<span\; class="notranslate">\; 2\Delta P</span>}}_{\mathrm{<span\; class="notranslate">\; S</span>}}\mathrm{<span\; class="notranslate">\; \rho </span>}}{\mathrm{<span\; class="notranslate">\; (</span>}\frac{{\mathrm{<span\; class="notranslate">\; d</span>}}_{\mathrm{<span\; class="notranslate">\; 2</span>}}}{{\mathrm{<span\; class="notranslate">\; d</span>}}_{\mathrm{<span\; class="notranslate">\; 1</span>}}}{\mathrm{<span\; class="notranslate">\; )</span>}}^{\mathrm{<span\; class="notranslate">\; 4</span>}}\mathrm{<span\; class="notranslate">\; -1</span>}}}$ Where: △P _s is the pressure difference between two points [1], [2] d ₁ , d ₂ are the diameters at [1] and [2] respectively μ=0.97 is the flow coefficient σ is the fluid density In the actual measurement, the pressure difference between the two points [1] and [2] is △PF when passing through the two-phase flow; d. When the pure fluid flows through, find two pressure measuring points [3] and [4] in the straight pipe part [6], so that the pressure difference between the two points [3] and [4] is the same as that in the diffuser tube [1] , [2] The difference between the two points is equal. In the actual measurement, when the two-phase flow passes, the pressure difference between the two points [3] and [4] is △P; e. Add solid particles with a mass of M _S to the solid hopper, and the two-phase flow mixed with pure fluid passes through the two-phase flowmeter, and the coefficient K is measured, and its calculation formula is: $\mathrm{<span\; class="notranslate">\; K</span>}<span\; class="notranslate">\; =</span>{\mathrm{<span\; class="notranslate">\; m</span>}}_{\mathrm{<span\; class="notranslate">\; S</span>}}<span\; class="notranslate">\; /</span>{<span\; class="notranslate">\; \&Integral;</span>}_{\mathrm{<span\; class="notranslate">\; 0</span>}}^{\mathrm{<span\; class="notranslate">\; T</span>}}\mathrm{<span\; class="notranslate">\; GF</span>}\frac{\mathrm{<span\; class="notranslate">\; \&Delta;P</span>}<span\; class="notranslate">\; -</span>\mathrm{<span\; class="notranslate">\; \&Delta;</span>}{\mathrm{<span\; class="notranslate">\; P</span>}}_{\mathrm{<span\; class="notranslate">\; f</span>}}}{\mathrm{<span\; class="notranslate">\; \&Delta;</span>}{\mathrm{<span\; class="notranslate">\; P</span>}}_{\mathrm{<span\; class="notranslate">\; f</span>}}}\mathrm{<span\; class="notranslate">\; dt</span>}$ ${\mathrm{<span\; class="notranslate">\; G</span>}}_{\mathrm{<span\; class="notranslate">\; f</span>}}\mathrm{<span\; class="notranslate">\; =</span>}\frac{{\mathrm{<span\; class="notranslate">\; \pi d</span>}}^{\mathrm{<span\; class="notranslate">\; 2</span>}}{}_{\mathrm{<span\; class="notranslate">\; 2</span>}}}{\mathrm{<span\; class="notranslate">\; 4</span>}}\mathrm{<span\; class="notranslate">\; mu</span>}\sqrt{\frac{{\mathrm{<span\; class="notranslate">\; 2\Delta P</span>}}_{\mathrm{<span\; class="notranslate">\; f</span>}}\mathrm{<span\; class="notranslate">\; \rho </span>}}{\mathrm{<span\; class="notranslate">\; (</span>}\frac{{\mathrm{<span\; class="notranslate">\; d</span>}}_{\mathrm{<span\; class="notranslate">\; 2</span>}}}{{\mathrm{<span\; class="notranslate">\; d</span>}}_{\mathrm{<span\; class="notranslate">\; 1</span>}}}{\mathrm{<span\; class="notranslate">\; )</span>}}^{\mathrm{<span\; class="notranslate">\; 4</span>}}\mathrm{<span\; class="notranslate">\; -1</span>}}}$ Among them: T is the time required for the mass of M _S solid particles to be transported; G _F is fluid flow; f Then use G _S =K (△P-△PF)/(△PF) GF to calculate the solid flow rate.