Limestone Slurry Pipeline Optimization

A slurry pipeline is a type of pipeline used to transport a mixture of materials suspended in a liquid or gas. These materials are usually particles of solid matter, such as sand, clay, and other minerals, suspended in a liquid base, such as water or oil. Slurry pipelines are used in many industries, including mining, oil and gas, and agriculture.

The optimization of a slurry pipeline depends on the type of slurry and the application. In general, the goal is to minimize the total cost of the pipeline, which includes capital and operating costs. Optimization may involve adjusting the diameter of the pipeline, the type and number of pumps, the use of valves and other controlling devices, and the installation of strainers and other equipment to filter out solids. Other considerations include the environmental impact of the pipeline, safety, and the ability to handle the slurry without damage to the equipment. In some cases, the optimization process may also include the use of additives to improve the flow characteristics of the slurry.

Design a pipeline for transporting crushed limestone from a quarry to a terminal located some distance away, using water as a transporting medium.

The limestone is crushed at the quarry, mixed with water to form a slurry, and pumped through the pipe. We would like to minimize the operating cost, which is primarily determined by the grinding power and the pumping power.

This problem is taken from James Siddall, Optimal Engineering Design, Dekker.

This assignment can be completed in groups of two. Additional guidelines on individual, collaborative, and group assignments are provided under the Expectations link.

Solution Help

See GEKKO documentation and additional example problems.

from gekko import GEKKO
m = GEKKO()

# Pipeline slurry

# Constants
L = m.Const(15*5280,'L') # Length of pipeline (ft)
W = m.Const(12.67,'W') # Massflow of limestone (lbm/sec)
a = m.Const(0.01,'a') # Average lump-size before grinding (ft)
pi = m.Const(3.1415927,'pi') # pi

rho_w = m.Const(62.428,'rho_w') # Density of water (lbm/ft^3)
mu = m.Const(7.392e-4,'mu') # Viscosity of water (lbm/ft/sec)
g = m.Const(32.174,'g') # Gravitational constant (ft/sec^2)
# Conversion between lbm and lbf (lbm ft / lbf / s^2)
gc = m.Const(32.174049,'gc')
# Density of limestone (lbm/ft^3)
gamma_L = m.Const(168.5,'gamma_L')

# Variables
# Average flow velocity (ft/sec)
V = m.Var(value=10 , lb=1 , ub=20 , name='V')
# Volumetric concentration of slurry (Vol limestone/Vol Total)
c = m.Var(value=0.2 , lb=0.01 , ub=0.4 , name='c')
# Internal pipe diameter (ft)
Dpipe = m.Var(value=0.4 , lb=0.01 , ub=0.5 , name='Dpipe')
# Average particle size after grinding (ft)
d = m.Var(value=0.008 , lb=0.0008 , name='d')
Pt = m.Var(value=1 , name='Pt')

# Intermediates
# Reynolds number
Rw = m.Intermediate(rho_w*V*Dpipe/mu,'Rw')

# Friction factor for water (fit empirical correlation)
y = m.Intermediate(m.log(Rw),'y')
fw = m.Intermediate(-1.5919e-4*y**3+5.5535e-3*y**2-6.8029e-2*y+0.31078,'fw')

# Dimensionless numbers to obtain drag coefficient
CdRp2 = m.Intermediate(4*g*rho_w*d**3*(gamma_L-rho_w)/(3*mu**2),'CdRp2')
x = m.Intermediate(m.log(CdRp2),'x')
Cd = m.Intermediate(m.exp(0.03420*x**2-0.98327*x+6.17176),'Cd')

# Slurry density
rho = m.Intermediate((1-c)*rho_w+c*gamma_L,'rho')

# Limestone specific gravity
S = m.Intermediate(gamma_L/rho_w,'S')

# Slurry friction factor
r = m.Intermediate(rho_w/rho,'r')
t = m.Intermediate(g*Dpipe*(S-1)/(V**2*m.sqrt(Cd)),'t')
f = m.Intermediate(fw*(r+150*c*r*t**1.5),'f')

# Pressure drop (lbf / ft^2)
dp = m.Intermediate(f*rho*L*V**2/(2*Dpipe*gc),'dp')

# Pipe cross-sectional area (ft^2)
Area = m.Intermediate(pi*Dpipe**2/4,'Area')

# Slurry flow rate (ft^3/sec)
Q = m.Intermediate(Area*V,'Q')

# Slurry mass flow rate (lbm/sec)
mdot = m.Intermediate(rho*Area*V,'mdot')

# Limestone mass flow rate (lbm/sec)
Q_L = m.Intermediate(Q*c,'Q_L') # ft^3/sec
mdot_L = m.Intermediate(gamma_L*Q_L,'mdot_L') # lbm/sec = (lbm/ft^3) * (ft^3/sec)

# Friction power loss (ft * lbf / sec)
Pf = m.Intermediate(dp*Q,'Pf')

# Grinding power (ft*lbf/sec)
Pg = m.Intermediate(218*W*(1/m.sqrt(d)-1/m.sqrt(a)),'Pg')

# Critical velocity
Vc = m.Intermediate((40*g*c*(S-1)*Dpipe/m.sqrt(Cd))**0.5,'Vc')

# Equations
# Total power (grinding + pumping)

# Mass flow of limestone

# Velocity must be greater than the critical velocity constraint


print('Optimal Power: ' + str(Pt[0]))