(note: i was incredibly bored at work, so i typed all of this from the back of a fluid mechanics book that was around.)

appendix I

symbols and dimensions of quantities

symbol	quantity	english engineering dimensions	force-length-time dimensions	mass-length-time dimensions
A	area	ft²	L²	L²
a	wave velocity	ft/sec (fps)	L/T	L/T
a	linear acceleration	ft/sec²	L/T²	L/T²
B	bottom width (open channel)	ft	L	L
b	surface width (open channel)	ft	L	L
b	span of airfoil	ft	L	L
C	chezy coefficient	ft^½/sec	L^½/T	L^½/T
c_p	specific heat at constant pressure	ft-lb/lb°R
c_v	specific heat at constant volume	ft-lb/lb°R
D	drag force	lb	F	ML/T²
d	diameter	ft	L	L
E	modulus of elasticity	lb/ft²	F/L²	M/LT²
E	unit energy	ft-lb/lb	L	L
e	size of roughness	ft	L	L
F	force	lb	F	ML/T²
G	weight flowrate	lb/sec	F/T	ML/T³
g	gravitational acceleration	ft/sec²	L/T²	L/T²
H	total head	ft	L	L
H	head on weir	ft	L	L
H	enthalpy	ft-lb/lb	L	L
h	head or height	ft	L	L
I	moment of inertia	ft⁴	L⁴	L⁴
I	internal energy	ft-lb/lb	L	L
K	coefficient of permeability	ft/sec (fps)	L/T	L/T
L	lift force	lb	F	ML/T²
l	length	ft	L	L
M	mass	slugs	FT²/L	M
M	moment	ft-lb	FL	ML²/T²
n	manning's roughness coefficient	ft^1/6	L^1/6	L^1/6
P	power	ft-lb/sec	FL/T	ML²/T³
P	perimeter	ft	L	L
P	weir height	ft	L	L
p	pressure	lb/ft² (psf)	F/L²	M/LT²
O	flowrate	ft³/sec (cfs)	L³/T	L³/T
q	two-dimensional flowrate	ft²/sec (cfs/ft)	L²/T	L²/T
R	radius	ft	L	L
R	engineering gas constant	ft-lb/lb°R
R_h	hydraulic radius	ft	L	L
r	radial distance	ft	L	L
T	torque	ft-lb	FL	ML²/T²
T	absolute temperature	°R
t	temperature	°F
t	time	sec	T	T
u	velocity	ft/sec (fps)	L/T	L/T
V	velocity	ft/sec (fps)	L/T	L/T
V	volume	ft³ (cuft)	L³	L³
v	velocity	ft/sec (fps)	L/T	L/T
W	weight	lb	F	ML/T²
w	velocity	ft/sec (fps)	L/T	L/T
y	depth (open channel)	ft	L	L
y	distance from solid boundary	ft	L	L
z	height above datum	ft	L	L
Γ	circulation	ft²/sec	L²/T	L²/T
γ	specific weight	lb/ft³	F/L³	M/L²T²
δ	boundary layer or film thickness	ft	L	L
ε	eddy viscosity	lb-sec/ft²	FT/L²	M/LT
μ	viscosity	lb-sec/ft²	FT/L²	M/LT
ν	kinematic viscosity	ft²/sec	L²/T	L²/T
ξ	vorticity	sec^-1	1/T	1/T
ρ	density	slug/ft³	FT²/L⁴	M/L³
σ	surface tension	lb/ft	F/L	M/T²
τ	shear stress	lb/ft²	F/L²	M/LT²
φ	velocity potential	ft²/sec	L²/T	L²/T
ψ	streamfunction	ft²/sec	L²/T	L²/T
ω	angular velocity	sec^-1	1/T	1/T

symbols for dimensionless quantities
symbol	quantity	symbol	quantity
C	cauchy number	n	polytropic exponent
C_c	coefficient of contraction	R	reynolds number
C_D	drag coefficient	S	slope of energy line
C_f	frictional drag coefficient	S_o	bottom slope (open channel)
C_L	lift coefficient	S_c	critical slope
C_p	pressure coefficient	W	weber number
C_v	coefficient of velocity	Y	expansion factor
C_w	weir coefficient	α	kinetic energy
E	euler number		correction factor
F	froude number	β	momentum correction factor
f	friction factor	η	efficiency
K_L	loss coefficient	κ	von kármán's turbulence
k	adiabatic exponent		"constant"
M	mach number	Π	dimensionless group

appendix II

physical properties of water

tem- pera- ture, °F	specific weight,^a γ, lb/ft³	density,^a ρ, slug/ft³	modulus^b of elasticity,^c E/10³, psi	viscosity,^a μ × 10⁵, lb-sec/ft²	kinematic viscosity,^a υ x 10⁵, ft²/sec	surface^a tension,^d σ, lb/ft	kinematic surface^a tension,^d σ/ρ, ft³/sec²	vapor pressure,^e p_v , psia	vapor pressure head,^f p_v/γ, ft
32	62.42	1.940	287	3.746	1.931	0.00518	0.00267	0.09	0.19
40	62.43	19.40	296	3.229	1.664	0.00514	0.00265	0.12	0.28
50	62.41	1.940	305	2.735	1.410	0.00509	0.00262	0.18	0.41
60	62.37	1.938	313	2.359	1.217	0.00504	0.00260	0.26	0.59
70	62.30	1.936	319	2.050	1.059	0.00498	0.00257	0.36	0.84
80	62.22	1.934	324	1.799	0.930	0.00492	0.00254	0.51	1.17
80	62.11	1.931	328	1.595	0.826	0.00486	0.00251	0.70	1.62
100	62.00	1.927	331	1.424	0.739	0.00480	0.00249	0.95	2.21
110	61.86	1.923	332	1.284	0.667	0.00473	0.00246	1.27	2.97
120	61.71	1.918	332	1.167	0.609	0.00467	0.00243	1.69	3.95
130	61.55	1.913	331	1.069	0.558	0.00460	0.00240	2.22	5.20
140	61.38	1.908	330	0.981	0.514	0.00454	0.00238	2.89	6.77
150	61.20	1.902	328	0.905	0.476	0.00447	0.00235	3.72	8.75
160	61.00	1.896	326	0.838	0.442	0.00441	0.00232	4.74	11.17
170	60.80	1.890	322	0.780	0.413	0.00434	0.00229	5.99	14.18
180	60.58	1.883	318	0.726	0.385	0.00427	0.00226	7.51	17.85
190	60.36	1.876	313	0.678	0.362	0.00420	0.00223	9.34	22.40
200	60.12	1.868	308	0.637	0.341	0.00413	0.00221	11.52	27.63
212	59.83	1.860	300	0.593	0.319	0.00404	0.00217	14.70	35.35
^a from "hydraulic models," a.s.c.e. manual of engineering practice, no. 25, a.s.c.e., 1942. ^b approximate values averaged from many sources. ^c at atmospheric pressure. ^d in contact with air. ^e from j.h. keenan and f.g. keyes, thermodynamic properties of steam, john wiley and sons, 1936. ^f computed from p_v and γ.