pumps and gas-moving equipment
DESCRIPTION
PUMPS AND GAS-MOVING EQUIPMENT. Pumps. Positive-displacement pump s : reciprocating pump (piston, membrane) rotary pump (gear, vane, screw). Centrifugal pumps: radial-flow pump (centrifugal) axial-flow pump (propeller). Centrifugal pumpPropeller pump. 1 – impeller 2 – diffuser. - PowerPoint PPT PresentationTRANSCRIPT
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PUMPS AND GAS-MOVING PUMPS AND GAS-MOVING EQUIPMENT EQUIPMENT
PumpsPumpsPositive-displacement pumps: reciprocating pump (piston, membrane)
rotary pump (gear, vane, screw)
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Centrifugal pumps: radial-flow pump (centrifugal)
axial-flow pump (propeller)
Centrifugal pump Propeller pump
1 – impeller2 – diffuser
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Basic parameters of pumps
flow-rate of pumping liquid [m3·s-1] (discharge)
mechanical energy added to fluid by pump e (Y) [J·kg-1]
V
02
1
2
121
2122
22
21
21 eeghgh
ppuu z
brake power of pump Pp [W]
YV
Pp
efficiency of liquid pumping
electric power input Pe [W]
m
pe
PP
total mechanical efficiency
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Typical shape of pump characteristics
Positive-displacement pump
pt VnV
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Centrifugal pumps
Centrifugal pump Propeller pump
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Suction lift of pumps – NPSH
If the pressure on the liquid in the suction line drops below the vapor pressure p´´, some of the liquid flashes into vapor – rise of cavitation. Than no liquid can be drawn into pump, and vibration can occur.
To avoid flashes of vapour or cavitation, the pressure at the inlet of the pump must be greater than this vapor pressure and exceed it by a value termed the Net Positive Net Positive Suction Head – NPSH (Suction Head – NPSH (ΔΔppss)).
zsss
ss e
ugh
pp
2
221
ssss pppu
2
22
ss Yp
ss hgp VfhYp sss ,,
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Determination of duty point of pump
Duty point of pump is obtained as intersection of system characteristic (pipe and local resistance, filters, heat exchangers) with pump characteristic.
zehhgpp
e
1212
system characteristics
pump characteristic
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Parallel and series connection of pumps
=
common characteristic
common characteristic
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EXAMPLE:EXAMPLE: Design of basic parameters of pump Design of basic parameters of pump
Water with temperature 80°C ( = 971,8 kg•m-3 a = 0,355 mPa•s) is pumping from storage tank with atmospheric pressure into heat exchanger with pressure atmospheric 100 kPa. Length of suction pipe is 15 m, total length of delivery pipe is 55 m. Suction and delivery pipes are made from slightly corroded steel tubes with outside diameter 76 mm and thickness of wall 3 mm (average roughness of pipe wall kav = 0.3 mm). Choose suitable pump with give discharge of water about 300 l•min-1. Determine duty point of pump and check suction lift of pump.
7m
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Selection of pump type
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Determination of system (pipe) characteristic
V [l·min -1 ] 25 50 100 150 200 250 300 350
Re 2,08E+04 4,14E+04 8,23E+04 1,25E+05 1,66E+05 2,08E+05 2,47E+05 2,91E+05l 0,0347 0,0323 0,0308 0,0303 0,0300 0,0298 0,0297 0,0296
H p [m] 16,51 16,57 16,78 17,14 17,64 18,27 19,05 19,96
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Determination of duty point of pump
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Gas-moving machineryGas-moving machinery
Compression ratio p2 /p1: Fans (small value of CR 1, incompressible flow)
Compressors (greater value of CR)
Blowers (atmospherics suction pressure, CR < 3)
Vacuum pumps – equipment for gases removal from closed spaces
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Positive-displacement compressors
Piston compressor Screw compressor
Rotary piston compressor
Liquid ring vacuum pump
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Dynamic compressors
Two-stage radial turbocompressor Axial turbocompressor
Jet ejector
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Compressor duty cycle
Vz – cylinder capacity (displacement)
Vs – suction volume
V0 – clearance space
Ve – volume of clearance space expansion
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Basic parameters of compressors
brake power of compressor P [W]
mechanical energy work e (Y) [J·kg-1]
cadadPP /
8.05.0 madcad
adiabatic efficiency
mechanical efficiency
/dd peadiabatic process: p·v =
const
polytrophic process: n
11
1
1
2
1
1
p
ppead
11
1
1
2111
p
pVpVemeP adadad
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theoretical capacity of single cylinder and action compressor [kg·s-1]
transport efficiency d
capacity of compressor [kg·s-1]
gases expansion from clearance space –
volumetric efficiency pressure losses in suction
tm
nLSm gt
ntšod
leakages
gases heating at suction
The main effect – volumetric efficiency
95,075,0 ntš
z
eoz
z
so V
VVV
V
V
m
dtt
d mmm
m
o = 0 critical CR p2/p1, all sucked gas is compressed into clearance space
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heating during compression
n
p
p
T
T1
1
1
2
1
2
M
TRvpvp n const.,
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EXAMPLE:EXAMPLE: Basic parameters of piston compressor Basic parameters of piston compressor
Single-stage double-action piston compressor with speed 180 rpm is used for compression of air with temperature 20°C from atmospherics pressure to 0.4 MPa. Inside diameter of cylinder is 200 mm and piston stroke is 250 mm. Suppose polytrophic compression with exponent 1.2.Determine:
1) capacity of compressor (transport efficiency ηd = 0.8)2) temperature of discharge air3) power consumption of compressor (adiabatic efficiency ηcad = 0.6)