2. Standards and Codes
API STD 617
Centrifugal Compressors for Petroleum, Chemical, and Gas Industry Services
API STD 619
Rotary Compressors for Petroleum, Petrochemical, and Gas Industry Services
API STD 618
Reciprocating Compressors for Petroleum, Chemical, and Gas Industry Services
API STD 681
Liquid Ring Vacuum Compressors for Petroleum, Chemical
4. Main Types Of Compressors
HIGH LOW
V. HIGH
NO NO
YES
LOW HIGH V. HIGH
YES NO NO
Pressure P
Flow Rate Q
S .R .V
Efficiency
Maint. cost
Pulsation
Surging
Positive D.P. Centrifugal Axial Flow
V. HIGH LOW LOW
LOW MEDIUM V. HIGH
NO YES YES
6. 29 August 2023
6
Different Types of Compressors
Disadvantages
Advantages
Type
Centrifugal
Axial
-
Positive
displacement
- Wide operating range
- Low maintenance
- High reliability
- Unstable at low flow
- Moderate efficiency
- High efficiency
- High speed capability
- Higher flow for a given
size
- Low pressure ratio per stage
- Narrow flow range
- Fragile and expensive blading
- Pressure ratio
capability not affected
by gas properties
- Good efficiencies at low
specific speed
- Limited capacity
- High weight to capacity ratio
- Higher maintenance requirements
Introduces vibrations into the
system
- Bigger foundation requirements
23. 23
General aspects
1- A Complete spare balanced rotor to be ideally
stored in ware house
2- Compressor will be equipped with a complete
surge control system.
3- It is advisable to use dry gas mechanical seal
system instead of wet mechanical seal one.
30. It is the flow back of gases from the outlet of the
Last stage of the compressor towards the suction and
return again to discharge
SURGE PHENOMEN
IN OUT
31. • FLOW-RATE IS NOT ENOUGH
• GAS PROPERTY
• FLATENESS OF P.C. AT LOW Q
• COMPRESSOR PERFORMANCE
Why
SURGE PHENOMEN
32. • FLOW-RATE
IS NOT ENOUGH
• GAS PROPERTY
This will happen at
starting and shutdown,
also at abnormal conditions.
Gas is compressible but liquid is not.
33. • FLATENESS OF P.C. AT LOW Q
• COMPRESSOR PERFORMANCE
Centrifugal and Axial compressors are pumping
gas continuously but reciprocating is not.
Gas pressure has the same energy at
horizontal portions of the performance curve
41. 1- BY PASS WITH ANTI - SURGE VALVE
ANTI-SURGE METHODS
2 –BLOW OFF VALVE
THIS METHODS IS COMMONLY
USED FOR GAS COMPRESSORS
THIS METHODS IS COMONLY
USED FOR AIR COMPRESSORS
42. 42
1- BY PASS WITH ANTI - SURGE VALVE
P,T
FT
UIC
FY
COMRESSOR
COOLER
ANTI-SURGE
VALVE WILL
OPEN
ANTI-SURGE METHODS
IN CASE OF
COMPRESSOR
SURGING
43. 43
6000 M
3
COMRESSOR
10000 M
3
4000 M
3 4000 M
3
6000 M
3
P,T
FT
UIC
FY
COOLER
ANTI-SURGE
VALVE
FY = TRANSDUCER
UIC = ANTI- SURGE INTEGRATED CONTROLER
1- BY PASS WITH ANTI - SURGE VALVE
44. 44
BY PASS WITH ANTI - SURGE VALVE
GRAPHICALLY
A
H
p C
Q M³/ hr
B
SURGE CONTROL LINE
RECYCLE TRIP LINE
SURGE LIMIT LINE
45. 45
2 –BLOW OFF VALVE
FY = TRANSDUCER
UIC = ANTI- SURGE INTEGRATED CONTROLLER
BLOW
OFF
VALVE
Air
3
6000 M
P,T
F
T
UIC
FY
AIR
COMRESSOR
10000 M
3
46. 46
2 – BLOW OFF VALVE
A
B
GRAPHICALLY
Q M ³/ hr
Hp
B1
47. 47
IN CASE OF GAS TURBINE
AIR COMPRESSOR SURGE
BLEED VALVE WILL OPEN
COMPRESSOR TURBINE
BLEED VALVE
51. 29 August 2023 51
Reciprocating Compressors properties
• Lower Power Density
• Low Speed (300–1800 rpm)
• Generally used in low volumetric rate applications
(< 500 acfm [850 m3/h] )
• Higher maintenance
• Unaffected by changes in gas properties (MW, T)
• Most common driver – gas engine, electric motor
• Pulsating flow/vibration
52. 29 August 2023 52
Crosshead
Stuffing
Box
Packing
Discharge
Valves
Suction
Valves
Piston
Distance
Piece
Con-rod
Crank
Piston
Rod
Wiper
Rings
Reciprocating Compressors construction
53. Multi stage reciprocating compressor
ACCUMILLATOR
PULSATION
DAMPENER
GAS
GAS
COOLER
SCRUBBER
SCRUBBER
ACCUMILLATOR
PULSATION
DAMPENER
1St
2nd
53
58. 29 August 2023 58
Manual Operated Clearance
There is a clearance existed in the cylinder head.
A piston rod complete with an adjustable nut is
connected to piston with packing to seal the
clearance volume in font of the compressor piston.
The more the clearance volume in font of the comp.
piston, The less the compressor flow rate.
No effect of the clearance volume in font of the
piston on the compressor discharge pressure.
1- VARIABLE CLEARANCE
62. 29 August 2023 62
Point g suction valves open
C = Clearance volume
C
v
b
a
c
g
Pd
Ps c1
M
EFFECT OF
CLEARANCE
VOLUME
At
Point a suction valves closed
Point b discharge valves open
Point c discharge valves closed
63. Compression ratio
Pressure ratio (ABSOLUTE)
Pd
P s
=
Volumetric efficiency =
Va g
V cylinder a M
a g
=
= V cylinder
Vb M
C
v
b a
c
g
Pd
Ps c1
M
b
b M
a M
=
64. 29 August 2023 64
C
v
Pd
Ps c1
M
b
a
c
Volumetric efficiency =
Va g
V cylinder a M
a g
=
g
65. 29 August 2023 65
C
v
Pd
Ps
M
b
a
c
g
Volumetric efficiency =
Va g
V cylinder a M
a g
=
66. 29 August 2023 66
v
Pd
Ps
M
C
a
b
c
g
Volumetric efficiency =
Va g
V cylinder a M
a g
=
67. 29 August 2023 67
If C Increased suction valves will open at ( g )
C
v
a
c
g
Pd
Ps
b
M
EV DECREASES
Q DECREASES
Volumetric efficiency =
Va g
V cylinder a M
a g
=
68. 29 August 2023 68
If C Decreased suction valves will open at
(g)
Q INCREASES
Volumetric efficiency =
Va g
V cylinder a M
a g
=
EV INCREASES
C
v
a
c
g
Pd
Ps
b
M
69. 29 August 2023 69
Compression ratio
Pressure ratio (ABSOLUTE)
Pd
P s
=
Volumetric efficiency =
Va g
V cylinder a M
a g
=
= V cylinder
Vb M
C
v
b a
c
g
Pd
Ps c1
M
b
b M
a M
=
70. 29 August 2023 70
• SUCTION VALVE UNLOADERS
There are an unloaders existed on suction valves of
the compressor and pneumatically operated
If the unloaders energized, the suction valves will
be opened.
If there are 4 suction valves and the unloaders are
energized for :
1- One suction valve (Capacity will be ¾ max. Q)
2- Two suction valve (Capacity will be ½ max. Q)
3- Three suction valve (Capacity will be ¼ max. Q)
4- Four suction valve (Capacity will be = 0 Q)
82. 29 August 2023 82
Rotor profile of the four ------lobe male and the six lobe female
83. 29 August 2023 83
Oil – flooding system for a rotary screw air compressor.
Oil injected to
compressor
compressor
Air Outlet
Dry Air
Hot Oil
Cold Oil