CIESC Journal ›› 2020, Vol. 71 ›› Issue (12): 5515-5520.DOI: 10.11949/0438-1157.20201008
• Fluid dynamics and transport phenomena • Previous Articles Next Articles
WANG Shuai1(),LI Qingzhi2,CHEN Jianying2,WANG Dong3,NIU Pengman3,DONG Baoguang1
Received:
2020-07-22
Revised:
2020-09-01
Online:
2020-12-05
Published:
2020-12-05
Contact:
WANG Shuai
通讯作者:
王帅
作者简介:
王帅(1987—),男,博士,工程师,基金资助:
CLC Number:
WANG Shuai,LI Qingzhi,CHEN Jianying,WANG Dong,NIU Pengman,DONG Baoguang. Dual differential pressure used in multiphase flow double-parameter metering based on phase-isolation[J]. CIESC Journal, 2020, 71(12): 5515-5520.
王帅,李庆芝,陈建英,王栋,牛棚满,董宝光. 管内相分隔双压差在多相流双参数测量中的应用[J]. 化工学报, 2020, 71(12): 5515-5520.
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ΔPa/ Pa | Qm/ (kg·s-1) | ζ | λo | Relative error/% | |
---|---|---|---|---|---|
Theoretical value | Experimental value | ||||
651.70 | 0.84826 | 1.08749 | 0.04415 | 0.04799 | 8.70 |
378.14 | 0.78767 | 0.87470 | 0.05413 | 0.05846 | 7.99 |
283.06 | 0.73025 | 0.80501 | 0.07786 | 0.07020 | -9.84 |
178.59 | 0.67239 | 0.67763 | 0.09220 | 0.08344 | -9.50 |
59.65 | 0.61514 | 0.38692 | 0.10326 | 0.09927 | -3.86 |
Table 1 Relationship between experimental value and theoretical value of λo at 0.075 m and 0.115 m downstream of swirler
ΔPa/ Pa | Qm/ (kg·s-1) | ζ | λo | Relative error/% | |
---|---|---|---|---|---|
Theoretical value | Experimental value | ||||
651.70 | 0.84826 | 1.08749 | 0.04415 | 0.04799 | 8.70 |
378.14 | 0.78767 | 0.87470 | 0.05413 | 0.05846 | 7.99 |
283.06 | 0.73025 | 0.80501 | 0.07786 | 0.07020 | -9.84 |
178.59 | 0.67239 | 0.67763 | 0.09220 | 0.08344 | -9.50 |
59.65 | 0.61514 | 0.38692 | 0.10326 | 0.09927 | -3.86 |
ΔPa/ Pa | λo | ζ | Qm/(kg·s-1) | Relative error/% | |
---|---|---|---|---|---|
Theoretical value | Experimental value | ||||
651.70 | 0.04799 | 1.08749 | 0.83948 | 0.84826 | 1.05 |
378.14 | 0.05846 | 0.87470 | 0.78549 | 0.78767 | 0.28 |
283.06 | 0.07020 | 0.80501 | 0.73191 | 0.73025 | -0.23 |
178.59 | 0.08344 | 0.67763 | 0.67604 | 0.67239 | -0.54 |
59.65 | 0.09927 | 0.38692 | 0.61850 | 0.61514 | -0.54 |
Table 2 Relationship between experimental value and theoretical value of Qm at 0.075 m and 0.115 m downstream of swirler
ΔPa/ Pa | λo | ζ | Qm/(kg·s-1) | Relative error/% | |
---|---|---|---|---|---|
Theoretical value | Experimental value | ||||
651.70 | 0.04799 | 1.08749 | 0.83948 | 0.84826 | 1.05 |
378.14 | 0.05846 | 0.87470 | 0.78549 | 0.78767 | 0.28 |
283.06 | 0.07020 | 0.80501 | 0.73191 | 0.73025 | -0.23 |
178.59 | 0.08344 | 0.67763 | 0.67604 | 0.67239 | -0.54 |
59.65 | 0.09927 | 0.38692 | 0.61850 | 0.61514 | -0.54 |
ΔPr/ Pa | ΔPa/ Pa | λo | Qm/(kg·s-1) | ||||
---|---|---|---|---|---|---|---|
Experimental value | Theoretical value | Relative error/% | Experimental value | Theoretical value | Relative error/% | ||
9990.6 | 651.7 | 0.04799 | 0.05130 | 6.89 | 0.8483 | 0.8387 | -1.13 |
8749.4 | 378.1 | 0.05846 | 0.06018 | 2.94 | 0.7877 | 0.7845 | -0.40 |
7577.6 | 283.1 | 0.07020 | 0.07423 | 5.74 | 0.7303 | 0.7304 | 0.02 |
5435.6 | 59.6 | 0.09927 | 0.1012 | 1.95 | 0.6151 | 0.6164 | 0.21 |
Table 3 Comparison of experimental value and theoretical value of double-parameter metering of oil-water two-phase flow at 0.075 m downstream of swirler
ΔPr/ Pa | ΔPa/ Pa | λo | Qm/(kg·s-1) | ||||
---|---|---|---|---|---|---|---|
Experimental value | Theoretical value | Relative error/% | Experimental value | Theoretical value | Relative error/% | ||
9990.6 | 651.7 | 0.04799 | 0.05130 | 6.89 | 0.8483 | 0.8387 | -1.13 |
8749.4 | 378.1 | 0.05846 | 0.06018 | 2.94 | 0.7877 | 0.7845 | -0.40 |
7577.6 | 283.1 | 0.07020 | 0.07423 | 5.74 | 0.7303 | 0.7304 | 0.02 |
5435.6 | 59.6 | 0.09927 | 0.1012 | 1.95 | 0.6151 | 0.6164 | 0.21 |
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