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1 dyne force (cgs system)
accelerate 1 gram mass at 1 cm/s²
1 newton force (mks system)
accelerates 1 kg mass at 1 m/s²
1 lb force (fps system)
accelerates 1 slug mass at 1 ft/s²
1 lb force
accelerates 1 lb mass at 32.174 ft/s²
1 g force
accelerates 1 gm mass at 980.66 cm/s²
1 kg force
accelerates 1 kg mass at 9.8066 m/s²
1 kgf
9.8066N
1 slug
32.174 lbm
1 gmf
980.66 dynes
mass
the absolute quantity of matter in a body
weight
the force of gravity acting on a body
density
mass per unit volume
specific volume
volume per unit mass
specific weight
the force of gravity on a unit volume
pressure
the normal force exerted by the system per unit area
1 atm to mm Hg
760 mm Hg
1 atm to in Hg
29.92 in Hg
1 atm to psia
14.696 lbf
open-type manometer
used to measure pressure in flow lines or vessels
equation for open-type manometer where Pabs>Patm
P= Po + yh
equation for open-type manometer where Pabs<Patm
P= Po - yh
closed-type manometer
used to measure the pressure difference between two flow lines or vessels
equation for closed-type manometer is pressure at vessel x is greater than pressure y
yh = Px - Py
equation for closed-type manometer is pressure at vessel y is greater than pressure x
yh = Py - Px
gage pressure
the defect or excess of absolute pressure over the barometric pressure
vacuum pressure
is the defect or excess of atmospheric pressure over the absolute pressure
barometer
used to measure the atmospheric pressure
absolute temperature
the temperature measured from absolute zero
absolute zero temperature
the temperature at which all molecular motion ceases
formula for C to F
F=9C/5+ 32
formula for F to C
C = 5/9 (F-32)
formula for F to R
R = F+460
formula for C to K
K = C + 273
law of conservation of mass
states that mass is indestructible
volume flow rate
Q = Av
mass flow rate
m = pAv
Einstein’s Theory of Relativity
states that mass can be converted into energy and energy into mass
Relativity Equation
E = mc²
gravitational potential energy
energy due to position or elevation
kinetic energy
energy stored or stored capacity for performing work possessed by a moving body by virtue of its momentum
GPE
mgh
KE
½ mv²
Internal Energy
energy stored within a body or substance by virtue of the activity and configuration of its molecules and of the vibration of the atoms within the molecules
heat
energy in transit from one body to another solely because of temperature difference
flow work (flow energy)
work done in pushing a fluid across a boundary, usually into or out of a system
equation for Flow Work
Wf= FL = pAL = pV
enthalpy
a composite property applicable to all fluids defined by:
h = u + pV or h = u + Wf
Work
product of the displacement of the body and the component of the force in the direction of the displacement, it is a work in transition
closed system
mass does not cross its boundaries
open system
mass crosses its boundaries
Work Non-Flow Equation
WNF = pdV
Work Non-Flow
the work done as the piston moves in a closed system,
work done during a non-flow reversible process
area under the curve of the process on the pV plane
expansion work
when work is done by the pressure force of a gas on the face of a piston (positive)
compression work
when work is done by piston on a gas (negative)
Work Non-flow by General Energy Equation
WNF = Q - U
work steady-flow or work done for an open system
the area behind (to the left) of the curve of the process on the pV plane
Work Steady-Flow Equation
WSF= VdP
conservation of energy
states that energy is neither created nor destroyed
First Law of Thermodynamics
states that “if energy cannot be created nor destroyed, then it can be transformed from one form to another”
ideal gas
ideal only in the sense that it conforms to the simple perfect gas laws
Boyle’s Law
“if the temperature of a given quantity of gas is held constant, the volume of gas varies inversely with the absolute pressure during a change of state”
Boyle’s Law equation
V2/V1=P1/P2
Charle’s Law 1
“if the pressure on a particular gas is held constant, then with any change of state, the volume will vary directly as the absolute temperature”
Charle’s Law 1 equation
V2/V1=T2/T1
Charle’s Law 2
“if the volume of a particular quantity of gas is held constant, then with any change of state, the pressure will vary directly as the absolute temperature of the gas”
Charle’s Law 2 equation
P2/P1=T2/T1
equation for ideal gas
pV=mRT
combined gas laws
PV/T= c
specific heat
defined as the quantity of heat required to change the temperature of unit mass by one degree
constant specific heat equation
Q = mcdT
Constant Volume Specific Heat equation
Q = mcvdT
constant pressure specific heat equation
Qv= mcpdT
ratio of specific heats (k)
Cp/Cv>1
Joule’s Law
states that “the change of internal energy of an ideal gas is a function of only the temperature change”
Joule’s Law equation / Internal Energy of an Ideal Gas
dU = mcvdT
Enthalpy of Ideal Gas
dH = mcpdT
Mayer’s Rule
Cp + Cv = R
Cv equation
Cv = R/(k-1)
Cp equation
Cp = kR/(k-1)
entropy (S)
a property of a substance which remains constant if no heat enters or leaves the substance, while it does work or alters its volume, but which increases or diminishes should a small amount of heat enter or leave
entropy equation
dS = dQ/T
entropy equation for constant specific heat
dS = mcln(T2/T1)
heat transferred during the process
represented by the area under the curve of the process on the TS plane
reversible process
any process that can be made to go in reverse direction by an infinitesimal change in the conditions
WSF when change in KE = 0 or the KE when WSF=0
represented by the area behind the curve of the process on the pV planes
irreversible process
any process that is not reversible
isometric or isochoric
a reversible constant volume process, in this process the working substance is contained in a rigid vessel
isomer or isochore
the curve for an isometric process
relation between T and P when isometric
P2/P1=T2/T1
work non-flow when isometric
WNF=0
change in internal energy when isometric
dU = mcvdT
heat transferred when isometric
Qv = mcvdT
change in enthalpy when isometric
dH = mcpdT
change of entropy when isometric
dS = mcvln(T2/T1)
reversible steady flow when isometric
WSF=V(P1 - P2)
irreversible nonflow when isometric
WNF=0
isobaric or isopiestic
an internally reversible process of a substance during which a pressure remains constant
isobar
the curve for an isobaric process
relation between V and T when isobaric
V2/V1=T2/T1