The gage pressure (psig) at point a is nearest (a) 13.7 (b) 14.7 (c) 101.3 (d) 0 (e) 1 Oil a 3 in SG = 0.69 SThe gage pressure (psig) at point c is nearest (a) 57.2 (b) 1.4 (c) 6.7 (d) 0.4 8 in Water The absolute pressure (psia) the natural gas pipeline is C nearest hw = 22 in (a) 8.4 (b) 65 (c) 9 (d) 1 (e) 23 16 in SThe gage pressure (psig) in the natural gas pipeline is Natural gas DIf the pipeline pressure was increased by 50%, what cost- effective manometer modification(s) might be needed? (a) None (b) More mercury, less oil (c) Add 2 more manometer loops (d) Replace the manometer with a high-pressure gage Mercury SG = 13.6 (e) Rotate the gas line to a vertical alignment
The gage pressure (psig) at point a is nearest (a) 13.7 (b) 14.7 (c) 101.3 (d) 0 (e) 1 Oil a 3 in SG = 0.69 SThe gage pressure (psig) at point c is nearest (a) 57.2 (b) 1.4 (c) 6.7 (d) 0.4 8 in Water The absolute pressure (psia) the natural gas pipeline is C nearest hw = 22 in (a) 8.4 (b) 65 (c) 9 (d) 1 (e) 23 16 in SThe gage pressure (psig) in the natural gas pipeline is Natural gas DIf the pipeline pressure was increased by 50%, what cost- effective manometer modification(s) might be needed? (a) None (b) More mercury, less oil (c) Add 2 more manometer loops (d) Replace the manometer with a high-pressure gage Mercury SG = 13.6 (e) Rotate the gas line to a vertical alignment
Chapter2: Loads On Structures
Section: Chapter Questions
Problem 1P
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