PE & PD Values Flashcards

These constants, equations, relationships will aid calculations in Chemical Engineering analyses.

1
Q

capacity for underground fuel storage tank (Number)

A

45

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2
Q

Le/D for fully open globe (Number)

A

300

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3
Q

Le/D for fully open gate (Number)

A

around 7

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4
Q

Le/D for tee (Number)

A

90

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5
Q

Le/D for 45-elbow (Number)

A

45

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6
Q

Le/D for 180-close return (Number)

A

75

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7
Q

Le/D for couplings and unions (Number)

A

0

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8
Q

cap dia for >1.2 column dia (Number)

A

10

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9
Q

tube side ΔP for 1-2 vs 1-1 heat ex (Number)

A

8 (2^3)

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10
Q

constant power input, decrease impeller speed (Number)

A

1.2^5/3

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11
Q

assumed steam side heat transfer coefficient (Number)

A

7500

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12
Q

apex angle of conical heads (Number)

A

60

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13
Q

size of packings to be stacked not dumped (Number)

A

75

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14
Q

ΔP and superficial gas mass velocity (Number)

A

^2

(ΔP = G^2)

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15
Q

min baffle spacing in shell and tube (Number)

A

0.2D or 5 cms

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16
Q

power required with increase of dia (Number)

A

D^5

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17
Q

head to capacity for pipe flow (Number)

A

1/D^5

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18
Q

margin for plate tearing (Number)

A

1.5d

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19
Q

turbulent tube side heat transfer (Number)

A

G^0.8

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20
Q

thickness not requiring corrosion allowance (Number)

A

30

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21
Q

tube side film vs total resistance so overall coefficient is proportional with tube side (Number)

A

1

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22
Q

paddle to tank dia (Number)

A

0.8

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23
Q

vacuum of low pressure steam (Number)

A

650

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24
Q

dia to wall thickness ratio for “thin” vessel (Number)

A

> 10

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25
Q

dia to wall thickness ratio for “thick” vessel (Number)

A

<10

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26
Q

accentuated difficulty of liquid distribution (Number)

A

<7

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27
Q

min tube pitch (Number)

A

1.25

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28
Q

butt welded joints (Number)

A

3.8

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29
Q

ave velocity for 1-4 vs 1-1 heat ex (Number)

A

4

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30
Q

min ligament for outside dia (Number)

A

4/5

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31
Q

rate of washing vs final rate (Number)

A

0.25

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32
Q

static submergence for bubble cap (Number)

A

0.5

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33
Q

min plate spacing for dia >3 (Number)

A

18

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34
Q

min plate spacing for dia <3 (Number)

A

6

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35
Q

weld joint efficiency using code formula (Number)

A

0.8

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36
Q

ideal size of bubble cap for column of 3-6 dia (Number)

A

15

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37
Q

thickness of plates for lap joints (Number)

A

> 3

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38
Q

unusual length of heat ex tube (Number)

A

10

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39
Q

Re value where inside heat film is negligible (Number)

A

10000

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40
Q

min tray spacing in distillation (Number)

A

6

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41
Q

max size of raschig ring (Number)

A

1/30

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42
Q

distance of habitation to plants (Number)

A

25

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43
Q

air heater connected to 2 pass unit (Number)

A

2^0.8

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44
Q

single tube pass connected to 2 passes, ΔP (Number)

A

2^1.6

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45
Q

satisfactory value of operating vapor velocity (Number)

A

80

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46
Q

welded joint efficiency in chemical processes (Number)

A

0.85

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47
Q

thickness for length/dia ratio, 125 design stress (Number)

A

10 mm

48
Q

safe height to dia fuel storage tank (Number)

A

1

49
Q

bubble cap dia with column dia of 1.5 to 4.5 (Number)

A

100

50
Q

shank dia given that 25 hole dia (Number)

A

23

51
Q

stress concentration ngeligible at this hole dia (Number)

A

two

52
Q

condensing coefficient of horizontal vs. vertical (Number)

A

thrice

53
Q

dia for duct of square cross-section | liquid depth in agitation tank (Number)

A

d

54
Q

Unwin’s formula (Number)

A

d=1.6√t

55
Q

min Fr desired for heat ex design (Number, 2nd lowest)

A

0.8

56
Q

area increase for raschig to lessing (Number, 2nd lowest)

A

20

57
Q

min residence time in downspout (Number, 2nd lowest)

A

8

58
Q

min residence time in down comer (Number, 2nd lowest)

A

5

59
Q

outside dia not recommended for fouling fluid (Number, 2nd lowest)

A

19

60
Q

viscosity where baffle can be eliminated (Number, 2nd lowest)

A

600

61
Q

min shell thickness for elastic stability (Number, 2nd lowest)

A

5

62
Q

brass valves (Number, 2nd lowest)

A

<2

63
Q

dia of normal screwed fittings (Number, 2nd lowest)

A

3

64
Q

max liquid gradient (Number, 2nd lowest)

A

12.5 mm

65
Q

max saddle packing (Number, 2nd lowest)

A

1/15

66
Q

Poisson’s ratio for structural and pressure vessel (Number, 2nd lowest)

A

0.3

67
Q

seamless pipe joint efficiency (Number, 2nd lowest)

A

1

68
Q

min clearance for weir and last row of bubble cap (Number, 2nd lowest)

A

7.5

69
Q

inclined long tube vertical evaporator (Number, 2nd lowest)

A

45

70
Q

calendria tube height (Number, 2nd lowest)

A

2

71
Q

hydrostatic testing of welded pipe (Number, 2nd lowest)

A

1.5

72
Q

buffer to tube wall thickness (Number, 2nd lowest)

A

twice

73
Q

rotary vacuum drum speed (Range)

A

0.1-2

74
Q

max liquid gradient (Range)

A

0.5-1.25”

75
Q

dia bubble cap standard (Range)

A

6&4

76
Q

baffle spacing (Range)

A

/5-2-5

D/5 or min 2 to 5D = D/5 0.2D for min

77
Q

tube pitch vs tube dia (Range)

A

1.25-1.5

78
Q

safe distance between hazardous chemicals (Range)

A

1-1.5

79
Q

tube length to shell dia (Range)

A

4-8

80
Q

steam velocity in pipes (Range)

A

80-100

81
Q

hold-up in rotary drier (Range)

A

0.05-0.15

82
Q

Indian standard code for testing pressure (Range)

A

1.5-2

83
Q

downtake to cross-sectional area for calendria (Range)

A

0.5-1

84
Q

liquid redistributors position for raschig rings (Range)

A

2.5-3

85
Q

countercurrent rotary drier slope (Range)

A

0.15

86
Q

propeller agitator to tank dia (Range)

A

0.15-0.30

87
Q

NTU for rotary driers (Range)

A

1.5-2.5

88
Q

length of straight rectangular weir (Range)

A

0.6-0.8

89
Q

optimum to min reflux ratio (Range)

A

1-1.5

90
Q

total riser to cross-sectional area (Range)

A

0.1-0.2

91
Q

commercial HETP (Range)

A

0.4-0.9

92
Q

max size of pal ring (Range)

A

1/10-1/15

93
Q

baffle width to tank dia (Range)

A

0.1-0.12

94
Q

ΔP across continuous rotary drier (Range)

A

250-500

95
Q

triangular pitch for sieve tray holes (Range, 2nd lowest)

A

2.5-5

96
Q

min carbon steel shell thickness (Range, 2nd lowest)

A

5-11

97
Q

ΔP for packed absorption tower (Range, 2nd lowest)

A

20-40

98
Q

operating ΔP for bag filter (Range, 2nd lowest)

A

50-150

99
Q

propeller agitator diameter (Range, 2nd lowest)

A

15-30

100
Q

liquid redistributors position for saddle packing (Range, 2nd lowest)

A

5-8

101
Q

paddle agitator speed (Range, 2nd lowest)

A

20-100

102
Q

paddle blade width times the paddle dia (Range, 2nd lowest)

A

0.1-0.25

103
Q

plate thickness for plate heat ex (Range, 2nd lowest)

A

1.25-3.12

104
Q

rotary length to dia (Range, 2nd lowest)

A

4-10

105
Q

sieve tray hole dia (Range, 2nd lowest)

A

3-12.5

106
Q

factor of safety (Range, 2nd lowest)

A

15-20

107
Q

pitch vs outside dia of bubble cap (Range, 2nd lowest)

A

1.3-2

108
Q

ΔP for commercial packed scrubber (Range, 2nd lowest)

A

17-34

109
Q

water velocity in pipes (Range, 2nd lowest)

A

1-2

110
Q

onset ΔP for flooding (Range, 2nd lowest)

A

50-75

111
Q

flight height in rotary drier (Range, 2nd lowest)

A

0.08-0.12

112
Q

non-foaming vapor velocity (Range, 2nd lowest)

A

0.6-0.7

113
Q

impeller dia to turbine agitator (Range, 2nd lowest)

A

0.3-0.5

114
Q

ΔP per tray (Range, 2nd lowest)

A

0.07-0.12

115
Q

sieve plate hole to dia (Range, 2nd lowest)

A

2.5-4

116
Q

frame thickness for plate and frame (Range, 2nd lowest)

A

0.25-8

117
Q

rotary cylinder shell thickness (Range, 2nd lowest)

A

6-8