Engineering Statistics Handbook Episode 3 Part 7 pptx

... 1 1 1 1 1 0 .35 36 + 1 0 .35 36 + 1 0.6124 + 1 0.6124 + 0 0 .70 71 + - FACTORS FOR LEVEL-2 STANDARD DEVIATIONS WT FACTOR K 2 1 1 1 1 1 0 .70 71 + 1 0 .70 71 + 1 1.22 47 + 2 .3. 3 .3. 4. Calculation ... example, and ● 2 .3. 3 .3. 4. Calculation of standard deviations for 1,1,1,1 design http://www.itl.nist.gov/div898 /handbook/ mpc/section3/mpc 333 4.htm (3 of 3) [5/1/2006 10:...

Ngày tải lên: 06/08/2014, 11:20

... the 1 .3. 3.22. Probability Plot http://www.itl.nist.gov/div898 /handbook/ eda/section3/eda33m.htm (2 of 4) [5/1/2006 9:56:52 AM] 1 .3. 3.22. Probability Plot http://www.itl.nist.gov/div898 /handbook/ eda/section3/eda33m.htm ... alternatives. 1 .3. 3. 23. Probability Plot Correlation Coefficient Plot http://www.itl.nist.gov/div898 /handbook/ eda/section3/eda33n.htm (2 of 4) [5/1/2006 9:56:52...

Ngày tải lên: 06/08/2014, 11:20

... vaporizer/superheater, steam heated. Unit size 132 in (33 53 mm) in diameter by 42 ft ( 13 cm) long. Duty to boil and superheat very low-temperature organic liquid. (Source: Armstrong Engineering Associates.) FIG. ... turbocharger Turbochargers T-1 13 TABLE T-8 Application Matrix* OEM Steam Flow, Operating Minimum † Model No. lb·h Pressure, psig Vessel Diameter SD-2-1.5 20,000 150 36...

Ngày tải lên: 21/07/2014, 16:21

... Vol. 72 , April 1985, pp. 172 – 177 . Lakshminarasimha, A. N., Boyce, M. P., and Meher-Homji, C. B., 1992, “Modelling and Analysis of Gas Turbine Performance Deterioration,” ASME Paper No. 92-GT -39 5. Mezheritsky, ... procedure System engineering and equipment. The following two basic principles have been determined for the engineering of both online and offline injection systems: Turbin...

Ngày tải lên: 21/07/2014, 16:21

... γ . Given: a 3in= b 3in= γ 38 0 lb ft 3 = Solution: m 0 b y γπ a y b ⎛ ⎜ ⎝ ⎞ ⎟ ⎠ 3 ⎡ ⎢ ⎣ ⎤ ⎥ ⎦ 2 ⌠ ⎮ ⎮ ⎮ ⌡ d= m 2.66lb= I y 0 b y γπ a y b ⎛ ⎜ ⎝ ⎞ ⎟ ⎠ 3 ⎡ ⎢ ⎣ ⎤ ⎥ ⎦ 2 1 2 a y b ⎛ ⎜ ⎝ ⎞ ⎟ ⎠ 3 ⎡ ⎢ ⎣ ⎤ ⎥ ⎦ 2 ⌠ ⎮ ⎮ ⎮ ⌡ d= I y 6.46 ... y c 32 .22 mm= I x 1 12 t 3 at−()ta t−()x c t 2 − ⎛ ⎜ ⎝ ⎞ ⎟ ⎠ 2 + 1 12 tb 3 + tb b 2 x c − ⎛ ⎜ ⎝ ⎞ ⎟ ⎠ 2 += I x 3. 142 10 6 × mm 4 = I y 1 12 bt 3...

Ngày tải lên: 21/07/2014, 17:20

... 0 .31 3 27 0.9 0 .31 594 0 .31 859 0 .32 121 0 .32 381 0 .32 639 0 .32 894 0 .33 1 47 0 .33 398 0 .33 646 0 .33 891 1.0 0 .34 134 0 .34 375 0 .34 614 0 .34 849 0 .35 0 83 0 .35 314 0 .35 5 43 0 .35 76 9 0 .35 9 93 0 .36 214 1.1 0 .36 433 0 .36 650 0 .36 864 ... 0 .36 433 0 .36 650 0 .36 864 0 . 37 076 0 . 37 286 0 . 37 4 93 0 . 37 698 0 . 37 900 0 .38 100 0 .38 298 1.2 0 .38 4 93 0 .3...

Ngày tải lên: 06/08/2014, 11:20

... 3. 564 3. 522 3. 485 3. 452 3. 4 23 3 .39 6 3. 372 16. 3. 616 3. 5 53 3.498 3. 451 3. 409 3. 372 3. 339 3. 310 3. 2 83 3.259 17. 3. 519 3. 455 3. 401 3. 3 53 3. 312 3. 275 3. 242 3. 212 3. 186 3. 162 18. 3. 434 3. 371 3. 316 ... 3. 574 3. 351 3. 1 83 3.052 2.946 2.859 37 7 . 37 3 5.229 4 .36 0 3. 8 73 3. 558 3. 334 3. 1 67 3. 036 2. 930 2.8 43...

Ngày tải lên: 06/08/2014, 11:20