Equations LVL 1 Flashcards

(87 cards)

1
Q

Natural Gas Formula

A

1CH4+2o2+8N2=1Co2+2H20+8N2

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2
Q

Propane Gas formula

A

1C3H8+5o2+20N=3co2+4H2O+20N

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3
Q

lbs for CO2 Variables

A

117 NG and 135 Propane

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4
Q

LBS of C02 equation

A

(variable/1,000,000) x BTU input

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5
Q

% of C02

A

CO2/ total dry gases X100 (Don’t multiply by 100 if you do not want percent)

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6
Q

% of 02

A

02/ total dry gases X100 (Don’t multiply by 100 if you do not want percent)

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7
Q

What is the first equation for on the Gas formulae sheet

A

Q=CFM x 1.2 x deltaT
DFMUA for BTU

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8
Q

Steps for finding water produced

A

Divide BTU by CV (1000 or 2500)
Multiple by H20 produced (4 for propane 2 for NG)
divide by expansion ratio (1700)
Multiply by Us gal or Imperial Gas (7.48 US gal 6.24 Imperial Gal)

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9
Q

Absolute Zero

A

460 and 273

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10
Q

Atmospheric pressure

A

14.73 or 101.325

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11
Q

Second equation in Gas formulae sheet

A

Orifice flow (In gas code)
Q=flow
K factor
Area
delta P pressure drop across burners (Psi or “w.c)
SG- Specific gravity (.6 or 1.51)
(1psi is 27.08 inches water column)

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12
Q

How many Inches water column is 1 PSI

A

27.7

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13
Q

What is the variable change equation for orifice flow

A

Q2/Q1= K2/K1 X A2/A1 X square rootDeltaP2/DeltaP1 X squarerootSG1/SG2
Notice SG is flipped*

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14
Q

Expansion Of NG

A

600

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15
Q

Expansion of Propane

A

270

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16
Q

Expansion rate for steam to water

A

1700

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17
Q

How to transpose the orfice flow equation easily

A

Q divided by full equation = what your looking for

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18
Q

Third equation on list is for what

A

Clocking a meter
Q= Flow rate (Multiply but CV to get BTU)
t=rotation time in seconds
v-Dial size
PL- inlet pressure
PA- Sea level pressure
PS- Sea level pressure
TA 60 degrees
TS- Absolute
TA(bottom) Gas Temp
T- Absolute

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19
Q

Imperial gal

A

6.24

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20
Q

US Gal

A

7.48

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21
Q

Forth Equation on Gas formulae sheet

A

P1 X V1 / T1 = P2 X V2 / T 2 OR
P1 X T2 X V1 = P2 x T1 X V2

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22
Q

DFMUA Velocity equation

A

Velocity= T1 plus absolute / T2 plus absolute
muliplied by V2

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23
Q

Correction temp equation

A

60 plus absolute / wrong temp plus absolute
(460 or 273)

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24
Q

Correction pressure equation

A

wrong press + absolute / absolute
(14.73 or 101.325)

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25
Fifth equation on gas formulae sheet
Velocity = 4005 X squareroot of deltaP
26
How many Oz in a pound
16
27
Sixth equation on the formula sheet
Theoretical Natural Draft Ts- average stack temp plus absolute (460 or 273) Ta- Ambient temp plus absolute H Height of chimney
28
Excess air dry reading equation
0.895 X %A / 0.21 - %A
29
Excess air wet reading equation
1.105 x %B / 0.21 - %B
30
Seventh Equation on gas formulae sheet
Velocity= Volume / area
31
Latent heat of water to ice
144
32
Latent heat of water to steam
970.4
33
Calculating a state change from water to ice
144 X weight
34
Calculating a state change from water to steam
970.4 X weight
35
Eighth equation on gas formulae sheet
Area = Diameter squared X 0.7854 Or D= squareroot of area / 0.7854
36
Turn down ratio calculation
high fire / low fire or max temp - min temp divied by min rise
37
Calculation temperature change in water/ice/steam
specific heat X weight in lbs X DeltaT
38
Specific Gravity of NG
0.6
39
Specific gravity of Propane Vapour
1.51
40
Specific gravity of Propane Liquid
1.51
41
Calculation Net stack
Stack temp minus ambient temp
42
Flow increase on Diameter change
D2 ^2.623 divided by D1 ^2.623 Multiple by 100 for a percentage
43
Purge opening equation
square root D2/60 Cannot be less than 1/2"
44
Purge Time
Length of pipe/200 X2(safety factor)
45
Volume of pipe for purge calculation
Vol= (D/12)squared X .7854 X length
46
Second page #1 equation on Gas formula sheet
Flow equation/Pipe sizing Q-Flow (multiple by CV for BTU) D-Diameter P1- (Service pressure plus absolute) Squared P2- (Pressure at end of pipe plus absolute)Squared L-Length
47
How many cubic feet are in a pressure cyclinder
226
48
Size of the cyclinder
1.5
49
Normal flue temp
350-500
50
Normal stack Velocity
.02-.16
51
Third equation on Page 2 gas formulae sheet
LBS CO2 Variables 117 NG 135 Propane
52
Converting square inches to square feet
Multiple by 144
53
Forth equation on 2nd Page
Air free CO PPM
54
Voltage triangle
E I R E-Volts I-Amps R-ohms
55
Watts Triangle
P E I P-watts E-Voltage I-Ohms
56
fifth equation on Page 2
PPm Nox
57
Sixth equation on Page 2
Fuel Loss Ts- Fuel temp in C Ta Supply air temp Efficiency is 100 minus answer
58
How to convert Miliamps to Amps
Divide by 1000
59
Normal Hz of a motor
60 Hz
60
Seventh equation on page 2
Motor speed
61
Poles and RPMS
2-3600 4-1800 6-1200 8-900
62
Ninth equation on page 2
Slip Ns- RPM NR-Rotar speed on motor
63
Tenth Equation on Page 2
Torque PhP- Horse power n-RPM
64
Page 3 1st equation
Torque in metric Pkw- Kilowatts n-RPM
65
Page 3 second equation
Star circuit phase volt divide by coil is amps ephase X squareroot of3
66
Page 3 3rd equation
Wye circuit Phase voltage / Coil amps is amps Line voltage / squareroot of 3 is volts
67
Page 3 4th equation
Stunt resistance
68
How to get BHP to BTU
multiple by 33475
69
1 BHP is
34.5 LBS of 212 water or steam X LHV 970.4
70
How many btu of 1 foot of 215 steam
240
71
Hot many BTU is 1 foot of 170 water
150
72
How much is pipe loss in an EDR
33%
73
How to calculate gross EDR
Rad EDR multiply by piping
74
What is net EDR
Just the Rad without the piping
75
Equation for Wobbe
High heat Volume of gas divided by the squareroot of specific gravity
76
How many air changed for a purge
4
77
How much air has to be moving
60% of high fire
78
How to calculate vol of container for purge time
(Diameter/12")squared X .7854 X length(Minus insinuation) Water Vol- lbs of water capacity / 62.4 Take body vol and minus water vol
79
How to calculate Time for purge time
Fuel burners X 10ft X 1.2 (excess air) Divided by 3600 to get to sec Take vol of body(Multiply theby 4) and divide by fuel found in seconds divide by 60 %
80
How to calculate available stack draft
theoretical draft X .80
81
Calculating volume of flue gases going up chimney
First take BTU / CV Multiply that by your air needed and excess air then add gas back in Put variables in the t2 x v2 = t1 x t2 to get your volume than change volume in per min (Divide by 60) t2 x v2 = t1 x t2 T1-ambient temp plus absolute T2-Stack temp plus absolute V1-fuel + combustion air + excess air Make stack size into area (Stack size/12) sqaured X 0.7854 Vel= volume/area = Answer
82
Equation to find deltaP using Velocity
DeltaP= (Velocity/4005) squared
83
Steps for calculating Full Load RPM change
Use RPM equation with new HZ Use Slip equation with Old RPM Take the new RPM multiple by slip rating (Decimal) Take the new RPM and subtract the answer in step 3
84
Expansion tank sizing
Coefficient of vol multiply by Volume of system Multiplied by Change in liquid temp
85
Liquid gas into btu
Liquid divide by gal x 270 expansion x c.v
86
Mixed fuel new flow
Q2 = q1(org) squareroot sg1(org)/sg2 (mix) Multiply by new c.v for btu
87
Calculating new sg and cv with propane mix air and fuel
Take new gas % and multiply by c.v= new cv valve Take gas % and multiply by sg Take air % and multiply by one. Add the last two steps together and is your new sg