subject
Engineering, 23.04.2020 03:23 Demondevilg

Perform differentiation on LVDT data to obtain acceleration. a) State and briefly describe your chosen numerical differentiation method (forward difference, backward difference, etc.). (3 pt.) b) Perform differentiation on the original calibrated data and show the results in a plot; comment on the results. (5 pt.) c) If necessary, employ decimation and/or smoothing techniques (e. g. moving average). What smoothing or decimation if any was performed and why? - be specific. (4 pt.) d) Compare the smoothed and/or decimated data to your initial differentiated data and your measured acceleration. Show the results in a plot. How do they differ and why? (10 pt.)

ansver
Answers: 1

Another question on Engineering

question
Engineering, 03.07.2019 15:10
If you were designing a bumper for a car, would you prefer it to exhibit elastic or plastic deformation? why? consider the functions of a bumper in both a minor "fender-bender" and a major collision.
Answers: 1
question
Engineering, 04.07.2019 18:10
Air is to be cooled in the evaporator section of a refrigerator by passing it over a bank of 0.8-cm-outer-diameter and 0.4-m-long tubes inside which the refrigerant is evaporating at -20°c. air approaches the tube bank in the normal direction at 0°c and 1 atm with a mean velocity of 4 m/s. the tubes are arranged in-line with longitudinal and transverse pitches of sl- st 1.5 cm. there are 30 rows in the flow direction with 15 tubes in each row. determine (a) the refrigeration capacity of this system and (b) pressure drop across the tube bank. evaluate the air properties at an assumed mean temperature of -5°c and 1 atm. is this a good assumption?
Answers: 1
question
Engineering, 04.07.2019 18:10
Afluid flows with a velocity field given by v=(x/t)i.. determine the local and convective accelerations when x=3 and t=1.
Answers: 2
question
Engineering, 04.07.2019 18:10
Apipe with an outside diameter of 15 cm is exposed to an ambient air and surrounding temperature of -20°c. the pipe has an outer surface temperature of 65°c and an emissivity of 0.85. if the rate of heat loss from the pipe surface is 0.95 kw per meter of length, the external convective heat transfer coefficient (h) is: (a) 12.5 w/m"k (b) 18.6 w/mk (c) 23.7 w/mk (d) 27.9 w/mk (e) 33.5 w/mk
Answers: 1
You know the right answer?
Perform differentiation on LVDT data to obtain acceleration. a) State and briefly describe your chos...
Questions
question
Geography, 02.07.2020 20:01
question
Mathematics, 02.07.2020 20:01
question
Computers and Technology, 02.07.2020 20:01
question
Mathematics, 02.07.2020 21:01
Questions on the website: 13722360