{"id":362658,"date":"2024-10-20T01:41:32","date_gmt":"2024-10-20T01:41:32","guid":{"rendered":"https:\/\/pdfstandards.shop\/product\/uncategorized\/bsi-pd-iso-tr-153772018-tc-2\/"},"modified":"2024-10-26T02:40:13","modified_gmt":"2024-10-26T02:40:13","slug":"bsi-pd-iso-tr-153772018-tc-2","status":"publish","type":"product","link":"https:\/\/pdfstandards.shop\/product\/publishers\/bsi\/bsi-pd-iso-tr-153772018-tc-2\/","title":{"rendered":"BSI PD ISO\/TR 15377:2018 – TC"},"content":{"rendered":"
PDF Pages<\/th>\n | PDF Title<\/th>\n<\/tr>\n | ||||||
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1<\/td>\n | compares PD ISO\/TR 15377:2018 <\/td>\n<\/tr>\n | ||||||
2<\/td>\n | TRACKED CHANGES Text example 1 \u2014 indicates added text (in green) <\/td>\n<\/tr>\n | ||||||
3<\/td>\n | National foreword Compliance with a British Standard cannot confer immunity from legal obligations. Amendments\/corrigenda issued since publication <\/td>\n<\/tr>\n | ||||||
4<\/td>\n | Measurement of fluid flow by means of pressure-differential devices \u2014 Guidelines for the specification of orifice plates, nozzles and Venturi tubes beyond the scope of ISO 5167 <\/td>\n<\/tr>\n | ||||||
5<\/td>\n | COPYRIGHT PROTECTED DOCUMENT <\/td>\n<\/tr>\n | ||||||
7<\/td>\n | Foreword <\/td>\n<\/tr>\n | ||||||
8<\/td>\n | Measurement of fluid flow by means of pressure- differential devices — Guidelines for the specification of orifice plates, nozzles and Venturi tubes beyond the scope of ISO 5167 1 Scope 2 Normative references 3 Terms and definitions 4 Symbols Table 1 \u2014 Symbols <\/td>\n<\/tr>\n | ||||||
9<\/td>\n | 5.1 Drain holes through the upstream face of the square-edged orifice plate or nozzle 5.1.1 General <\/td>\n<\/tr>\n | ||||||
10<\/td>\n | 5.1.2 Square-edged orifice plates <\/td>\n<\/tr>\n | ||||||
12<\/td>\n | 5.1.3 ISA 1932 nozzles <\/td>\n<\/tr>\n | ||||||
13<\/td>\n | 5.1.4 Long radius nozzles 5.2 Square-edged orifice plates installed in pipes of diameter 25 mm \u2264 D < 50 mm 5.2.1 General 5.2.2 Limits of use 5.2.3 Discharge coefficients and corresponding uncertainties 5.3 No upstream or downstream pipeline 5.3.1 General 5.3.2 Flow from a large space (no upstream pipeline) into a pipeline or another large space <\/td>\n<\/tr>\n | ||||||
14<\/td>\n | 5.3.2.2 Square-edged orifice plates with corner tappings <\/td>\n<\/tr>\n | ||||||
15<\/td>\n | 5.3.2.3 ISA 1932 nozzles <\/td>\n<\/tr>\n | ||||||
16<\/td>\n | 5.3.2.4 Venturi nozzle <\/td>\n<\/tr>\n | ||||||
17<\/td>\n | 5.3.3 Flow into a large space (no downstream pipeline) 5.3.3.2 Square-edged orifice plates with corner tappings 5.3.3.3 ISA 1932 nozzles and Venturi nozzles <\/td>\n<\/tr>\n | ||||||
18<\/td>\n | 6 Orifice plates (except square-edged) 6.1 Conical entrance orifice plates 6.1.1 General 6.1.2 Limits of use 6.1.3 Description 6.1.3.1 General shape <\/td>\n<\/tr>\n | ||||||
20<\/td>\n | Figure 1 \u2014 Conical entrance orifice plate <\/td>\n<\/tr>\n | ||||||
21<\/td>\n | 6.1.3.2 Upstream face A <\/td>\n<\/tr>\n | ||||||
22<\/td>\n | 6.1.3.3 Downstream face B 6.1.3.5 Conical entrance 6.1.3.6 Parallel bore 6.1.3.7 Edges H, I and G <\/td>\n<\/tr>\n | ||||||
23<\/td>\n | 6.1.3.8 Diameter of orifice 6.1.4 Pressure tappings 6.1.5 Coefficients and corresponding uncertainties 6.2 Quarter-circle orifice plates 6.2.1 General 6.2.2 Limits of use <\/td>\n<\/tr>\n | ||||||
24<\/td>\n | Table 3 \u2014 Minimum internal diameter of upstream pipe for quarter-circle orifice plates 6.2.3 Description 6.2.3.1 General shape <\/td>\n<\/tr>\n | ||||||
26<\/td>\n | Figure 2 \u2014 Quarter-circle orifice plate <\/td>\n<\/tr>\n | ||||||
27<\/td>\n | 6.2.3.3 Downstream face B 6.2.3.4 Thicknesses e and E 6.2.3.5 Upstream orifice profile <\/td>\n<\/tr>\n | ||||||
28<\/td>\n | 6.2.3.6 Downstream edge 6.2.3.7 Diameter of orifice 6.2.4 Pressure tappings 6.2.5 Coefficients and corresponding uncertainties <\/td>\n<\/tr>\n | ||||||
29<\/td>\n | 6.2.5.2 Expansibility (expansion) factor 6.2.5.3 Uncertainties Table 4 \u2014 Discharge coefficients for quarter-circle orifice plates <\/td>\n<\/tr>\n | ||||||
30<\/td>\n | 6.3 Eccentric orifice plates 6.3.1 General 6.3.2 Limits of use 6.3.3 Description 6.3.3.1 General shape <\/td>\n<\/tr>\n | ||||||
31<\/td>\n | 6.3.3.2 Upstream face A 6.3.3.3 Downstream face B <\/td>\n<\/tr>\n | ||||||
32<\/td>\n | Figure 3 \u2014 Eccentric orifice plate <\/td>\n<\/tr>\n | ||||||
33<\/td>\n | 6.3.3.5 Angle of bevel 6.3.3.6 Edges G, H and I 6.3.3.7 Diameter of orifice 6.3.3.8 Symmetrical plates <\/td>\n<\/tr>\n | ||||||
34<\/td>\n | 6.3.3.9 Pressure tappings 6.3.4 Coefficients and corresponding uncertainties <\/td>\n<\/tr>\n | ||||||
35<\/td>\n | Table 5 \u2014 Discharge coefficients for eccentric orifice plates <\/td>\n<\/tr>\n | ||||||
36<\/td>\n | 7 Venturi tubes with machined convergent of angle 10,5 7.1 General 7.2 Description 7.3 Limits of use <\/td>\n<\/tr>\n | ||||||
37<\/td>\n | 7.4 Discharge coefficient <\/td>\n<\/tr>\n | ||||||
38<\/td>\n | 7.5 Expansibility [expansion] factor 7.6 Pressure loss 7.7 Installation requirements Table 7 \u2014 Required straight lengths for Venturi tubes with machined convergent of angle 10,5 <\/td>\n<\/tr>\n | ||||||
42<\/td>\n | Bibliography <\/td>\n<\/tr>\n | ||||||
46<\/td>\n | National foreword <\/td>\n<\/tr>\n | ||||||
50<\/td>\n | Foreword <\/td>\n<\/tr>\n | ||||||
51<\/td>\n | 1 Scope 2 Normative references 3 Terms and definitions 4 Symbols <\/td>\n<\/tr>\n | ||||||
53<\/td>\n | 5 Square-edged orifice plates and nozzles: With drain holes, in pipes below 50 mm diameter, and as inlet and outlet devices 5.1 Drain holes through the upstream face of the square-edged orifice plate or nozzle 5.1.1 General 5.1.2 Square-edged orifice plates <\/td>\n<\/tr>\n | ||||||
55<\/td>\n | 5.1.3 ISA 1932 nozzles 5.1.4 Long radius nozzles 5.2 Square-edged orifice plates installed in pipes of diameter 25 mm \u2264 D < 50 mm 5.2.1 General 5.2.2 Limits of use <\/td>\n<\/tr>\n | ||||||
56<\/td>\n | 5.2.3 Discharge coefficients and corresponding uncertainties 5.3 No upstream or downstream pipeline 5.3.1 General 5.3.2 Flow from a large space (no upstream pipeline) into a pipeline or another large space <\/td>\n<\/tr>\n | ||||||
58<\/td>\n | 5.3.3 Flow into a large space (no downstream pipeline) <\/td>\n<\/tr>\n | ||||||
59<\/td>\n | 6 Orifice plates (except square-edged) 6.1 Conical entrance orifice plates 6.1.1 General 6.1.2 Limits of use <\/td>\n<\/tr>\n | ||||||
60<\/td>\n | 6.1.3 Description <\/td>\n<\/tr>\n | ||||||
63<\/td>\n | 6.1.4 Pressure tappings <\/td>\n<\/tr>\n | ||||||
64<\/td>\n | 6.1.5 Coefficients and corresponding uncertainties 6.2 Quarter-circle orifice plates 6.2.1 General 6.2.2 Limits of use <\/td>\n<\/tr>\n | ||||||
65<\/td>\n | 6.2.3 Description <\/td>\n<\/tr>\n | ||||||
68<\/td>\n | 6.2.4 Pressure tappings 6.2.5 Coefficients and corresponding uncertainties <\/td>\n<\/tr>\n | ||||||
69<\/td>\n | 6.3 Eccentric orifice plates 6.3.1 General <\/td>\n<\/tr>\n | ||||||
70<\/td>\n | 6.3.2 Limits of use 6.3.3 Description <\/td>\n<\/tr>\n | ||||||
73<\/td>\n | 6.3.4 Coefficients and corresponding uncertainties <\/td>\n<\/tr>\n | ||||||
75<\/td>\n | 7 Venturi tubes with machined convergent of angle 10,5\u00b0 7.1 General 7.2 Description 7.3 Limits of use <\/td>\n<\/tr>\n | ||||||
76<\/td>\n | 7.4 Discharge coefficient 7.5 Expansibility [expansion] factor 7.6 Pressure loss 7.7 Installation requirements <\/td>\n<\/tr>\n | ||||||
78<\/td>\n | Annex A (informative) An example of the calculations in 5.1.2 <\/td>\n<\/tr>\n | ||||||
81<\/td>\n | Bibliography <\/td>\n<\/tr>\n<\/table>\n","protected":false},"excerpt":{"rendered":" Tracked Changes. Measurement of fluid flow by means of pressure-differential devices. Guidelines for the specification of orifice plates, nozzles and Venturi tubes beyond the scope of ISO 5167<\/b><\/p>\n |