2017
DOI: 10.1088/1757-899x/177/1/012006
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The algorithm of measuring parameters of separate oil streams components

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Cited by 4 publications
(3 citation statements)
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“…where I 1 , I 2 , I 3 -intensities of the primary radiation as registered by the sensor within the given volume in the presence of adsorbing material for, correspondingly, the 1 st , the 2 nd and the 3 rd sites of the pipeline cross-section; ρ st , ρ i , ρ p -densities of the pipeline steel wall, ice and pulp correspondingly; δ st , δ i , δ p -equivalent thickness of the pipeline steel wall, ice and pulp phase, correspondingly, μ st , μ i , μ p -mass attenuation coefficient for the primary radiation by the pipeline steel wall, ice and pulp flow, correspondingly; with Δ -the distance between the pipeline edge and the point of scanning at the moment by direction of motion for the entire measuring system; R, r -outer and inner radii of the pipeline in the section given; D -the pipeline diameter [4].…”
Section: Figure 1 Radioisotope Measuring Unitmentioning
confidence: 99%
See 1 more Smart Citation
“…where I 1 , I 2 , I 3 -intensities of the primary radiation as registered by the sensor within the given volume in the presence of adsorbing material for, correspondingly, the 1 st , the 2 nd and the 3 rd sites of the pipeline cross-section; ρ st , ρ i , ρ p -densities of the pipeline steel wall, ice and pulp correspondingly; δ st , δ i , δ p -equivalent thickness of the pipeline steel wall, ice and pulp phase, correspondingly, μ st , μ i , μ p -mass attenuation coefficient for the primary radiation by the pipeline steel wall, ice and pulp flow, correspondingly; with Δ -the distance between the pipeline edge and the point of scanning at the moment by direction of motion for the entire measuring system; R, r -outer and inner radii of the pipeline in the section given; D -the pipeline diameter [4].…”
Section: Figure 1 Radioisotope Measuring Unitmentioning
confidence: 99%
“…Until now, multiple theoretical and experimental researches have been carried out to study pipeline thermal operating modes under temperatures below the freezing point both in laboratories and at industrial stages [3,4]. Yet, the designing and the operation of industrial hydro-transportation units in wintertime formulate new design and technical tasks for hydro-mixture transportation [5].…”
Section: Introductionmentioning
confidence: 99%
“…The viscosity of oil is decreased and subsequently the recovery ratio is increased. On the other hand, paraffin blockage of tubing is reduced, therefore clear area of pipes is constant and oil recovery is not decreasing over time [3,4].…”
Section: Introductionmentioning
confidence: 99%