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Showing posts with label power plant maintenance. Show all posts
Showing posts with label power plant maintenance. Show all posts

Comparison between Acetylene & LPG fuels for gas cutting operation

 


SL No.

Acetylene

LPG (Propane)

1

Highest flame temperature up to 3100 Deg C

Flame temperature up to 2800 Deg C

2

Flame speed up to 7.5 m/sec

Flame speed up to 3.3 m/sec

3

Most of the heat released is in inner cone

Most of the heat released is in outer cone

4

Higher flame GCV of inner cone (4500 kcal/M3)

Lower flame GCV of inner cone (2500 kcal/M3) as compared to acetylene

5

Stoichiometric air fuel ratio1.2:1 (Requires 2.5 to 3 Oxygen cylinders for burning one Acetylene cylinder)

Stoichiometric  air fuel ratio 4.3:1 (Requires 7 to 8 Oxygen cylinders for burning one LPG cylinder)

6

Can be used in gas welding, as acetylene when burning with air creates reducing zone that cleans the steel surface

Cannot be used in gas welding as it does not create reducing zone

7

Acetylene has Specific gravity 0.9 kg/m3, so if it leaks it will raise in air without harming much

Propane has Specific gravity 1.6 kg/m3, which is heavier than air. So if it leaks it will concentrate in deck level or any other closed/corner area

8

Acetylene requires less air for complete combustion

Propane requires more air for complete combustion, so there may be chances of formation of carbon monoxide (CO) in case of incomplete combustion. This incomplete combustion may result into poisoning of working area, as CO is poisonous gas

9

Can be used for cutting & welding applications in industry

Used only for domestic applications

Why do Bearings fail?

 Following are the 16- top listed reasons for bearing failure or damages

1-Lubrication:

Following are the 7 major reasons for bearing failures related to lubrication

1-Lack of lubrication

2-Less lubrication

3-Over lubrication

4-Contaminants in lubricants




5-Wrong method of lubrication

6-Poor quality of lubricants

7-Selection of wrong lubrication

8-Lubricant failure

2-Bearing clearance:

Bearings may fail if the clearance between rolling elements & race is too less & too more. Lesser bearings clearance than desired creates friction & temperature rise.

More bearing clearance creates vibrations

3-Operating the bearings at higher vibrations for long time:

Bearings can operate satisfactory at the vibrations range up to 5 mm/sec, vibrations more than this reduces the bearing life & eventually failure.

Operation range: 0.5 to 3 mm/sec

Alarm Range: 3 to 5mm/sec

Trip range: > 5mm/sec

High vibrations in machine or bearings are due to;

1-Axial vibrations due to misalignment

2-Horizontal vibrations due to imbalance in machine

3-Vertical vibrations are due to looseness in foundation bolts

4-Shaft run out

4-Operating the bearing at excessive loads:

Excessive load on bearings leads to premature fatigue, over loading creates other side problems like bearing overheating, damage to rolling elements.

Brinelling occurs when loads exceed the elastic limit of the ring material. Brinell marks show as indentations in the raceways which increase bearing vibration (noise]. Severe brinell marks can cause premature fatigue failure.

 


5-Overheating




Overheating & damage of the bearings is due to;

1-Lack of lubrication

2-Over lubrication

3-Improper cooling of bearings

4-Excessive loads

6-Smaller clearance between rolling elements & race

Operating the boilers at higher temperature (>90 deg C for ball bearings & sump cooling) will lead to annealing the races & rolling elements that, eventually fails the bearings.

7-Miss alignment

Running the equipments at misaligned condition creates vibrations & excessive loads on bearings in axial, vertical & horizontal directions that causes bearing failures.

Misalignment also leads into failure of couplings & equipments parts like seals, impellers, pulley etc

8-Frequent start & stops of machine

Leads to jerk load on bearings & leading to reduction of its life

9-Not following of equipment/machine SOP:

If machine SOP (standard operating procedure) is being not followed, then it could cause not only bearing failure but also machine other elements.

For example if pump is not started with discharge valve closed or not stopped without closing discharge valves, it could cause jerk loads on bearings & impellers. After some cycle it will reflect it effect on misalignment, vibrations etc

10-Reverse rotation of machine or reverse loading of bearing element:

Some machines & bearings are not recommended for reverse rotation.

For example: Boiler feed pumps & screw compressors are meant to rotate in only one direction

Also Angular contact ball bearings are meant to take load only in one direction

11-Corrosion in Bearings:

Red brown areas on balls, raceways, cages, or bands of ball bearings are symptoms of corrosion. This condition results from exposing the bearings to corrosive fluids or a corrosive atmosphere. The usual result is increased vibration followed by wear, with subsequent increase in radial clearance or loss of preload. In extreme cases. Corrosion can initiate early fatigue failures.

12-Loose & tight fittings of bearings:

Fitting of bearings loose on shaft or loose in housing leads to rotation of bearings outer race in housing, this causes rubbing & bearing damage.

As like loose fitting, very tight fit can also cause excessive load on rolling elements which eventually creates overheating & vibrations

13-Entry of water in bearings grease

14-Material or manufacturing defects in bearings cause bearing failure as soon as it is been installed.

15-Leakage current in VFD motor bearings lead to bearing failure




16-Carrying out welding near bearings or Plummer blocks without proper earthing can lead to flow of currents through bearings, which ultimately causes bearing failure


CHAIN CONVEYOR MAINTENANCE GUIDE


Read Powerplantandcalculations.com


Questions & answers on bearings


Clear steps for Boiler Safety valves major overhauling

 Boiler Safety valve major overhauling steps

  • Cleaning of safety valve
  • Complete dismantling of safety valve.
  • Cleaning, polishing & buffing of parts.
  • Thorough inspection of all parts.
  • Seat & disc lapping
  • Spindle run out (bend) checking
  • Spring checking for any abnormalities like crack, bend, reduced tension etc
  • Lapping of both disc & seat.
  • Inspection of upper & lower ring teeth for damage/crac
  • Measurement & re-assembly.
  • Inspection of discharge pipe connection. If there is telescopic discharge pipe, then ensure a gap of minimum 10 mm for thermal expansion.

ASSEMBLY STEPS.

1-After seat & disc lapping, place lower nozzle ring on seat & level both the faces






Questions & Answers on Safety valves

2-After leveling, turn the lower ring by 3 notches in clockwise direction.

For example if Safety valve’s operating pressure is 117 kg/cm2, then 117 kg/cm2/42.4 kg/cm2 = 2.75 Appx. 3 Nos i.e 42.4 kg/cm2 for every notch (For more details, refer manufacturing data)

 Then lock the lower ring by inserting lower set screw




3- Take measurement from seat top to guide (89-90mm)                                          

4-Then measure the length of upper ring (it should be same as seat top to body top) & place it into the body




5-Fit disc to spindle then place disc with disc holder & spindle into the body & lock it by set screw



6-Put a body on spindle & lock the spindle by split pins & adjust the lift ,to increase the lift , rotate the lift stop collar clockwise & to decrease the lift, rotate the collar in anticlockwise direction. For every one full rotation, 1.58 mm lift can be adjusted.



7-Then fit the lower spring washer & helical compression spring



8-Then fit upper washer & yoke assy. thrust bearing & spindle lock nuts 



Basic concepts of safety valves


BLOWDOWN ADJUSTMENT

To increase the blow down: Lower the upper ring by 7 notches for 1Kg/cm2

To decrease the blow down: Raise the upper ring by 7 notches/1 Kg/cm2

To reduce shimmering: Raise the lower ring by one notch up, if not adjusted again rise one notch up. This is allowable till ring levels seat top.

 

 Power plant Safety QnA

 Boiler calculations for Boiler exam operation engineer (BOE)

 Attemperation & related calculations

 

 


Turbine oil and transformer oil standard testing parameters

 

TURBINE OIL STANDARD PARAMETERS

OIL: Servo prime 46T

Testing frequency: Every 6 months

Sl No.

Oil Property

UOM

Test Method

Acceptable limits

1

Appearance

NA

Visual

Clear/yellow Viscous liquid

2

Colour

Hazen

ASTM D1500

< 2

3

Density

Kg/m3

IS 1448-P-16:1990

820-870

4

Flash Point

0C

ATM D 93

> 180

5

Kinematic Viscosity at 40 0C

Cst

ATM D 445-17a

43-48

6

Kinematic Viscosity at 100 0C

Cst

ATM D 445-17a

>6.7

7

Viscosity index

NA

ASTM D 2270

> 98

8

RPVOT (Revolving Presure Vessel Oxidation  Stabilty Test)

Minutes

ASTM D 2272

>25% (minimum)

9

Total acid number (TAN)

mg/KOH/g

ASTM D 974

<0.2

10

Elemental analysis (Metal like Fe,Cu,Cr,Al, Ni, Sn, Si etc wear analysis)

ppm

ASTM D 5185

< 20

11

Sediments

%

IS 1866:2000

<0.01

12

Moisture content

ppm

ASTM D 6304

<1000



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TRANSFORMER OIL STANDARD PARAMETERS

OIL: Transformer oil

Testing frequqency: 1 year

Sl No.

Oil Property

UOM

Test Method

Acceptable limits

1

Appearance

NA

Visual

Clear free from sediments & suspended matter

2

Density

Kg/m3

IS:1448(P:16)1990 (RA 2014)

890 max

3

Flash Point

0C

IS 1448(P:21)-2012/ATM D 93

>125

4

Pour point

0C

IS-1448 (P-10)

-6

5

Kinematic Viscosity at 27 0C

Cst

IS:1448(P:25)-1976 (RA 2007)

<27

6

Total acid number (TAN)

mg/KOH/g

S: 1448(P:2)-2007/ASTM D 974

<0.03

7

Sediments

%

IS 1866:2000

Should not be detective or <0.01

8

Moisture content

mg/kg

IS: 13567-1992 (RA 2008) /IEC-814/ASTM D 6304

<50

9

Breakdown voltage (Dielectric strength)

kv

IS: 6792-1992 (RA 2008)

40 kV

10

Tan Delta (Di–Electric Dissipation Factor) in absolute, at a Temp:900C

Degree

IS: 6262-1971 (RA 2011) 

<1

11

Resistivity (Specific Resistance) at 90 deg C

Ω-cm

IS: 6103-1971 (RA 2011) 


>35 X1012

12

Dissolved gas analysis

 

IS: 10593:2006
 &
9434-1992 
(RA 2008) or IEC 567

 

a

Methane (CH4)

ml/l

100-150 (oil life 4 to 10 years)

b

Ethylene (C2H4)

ml/l

15-200 (oil life 4 to 10 years)

c

Ethane (C2H6)

ml/l

100-150(oil life 4 to 10 years)

d

Acetylene(C2H2)

ml/l

30-50(oil life 4 to 10 years)

e

Carbon Monoxide(Co)

ml/l

400-500(oil life 4 to 10 years)

f

Carbon Dioxide (Co2)

ml/l

4000-5000(oil life 4 to 10 years)

g

Hydrogen (H2)

ml/l

200-300(oil life 4 to 10 years)

13

Interfacial Tension (IFT)

N/m

IS: 6104-1971 Ring Method (RA 2011)/ASTM D 971 

> 0.015


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