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K iln Start-up Procedures  Presentation & Instructor Notes  Operator Development Kiln Control Best Practices
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174105579-Start-Up-Procedures.pdf

Apr 14, 2018

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Page 1: 174105579-Start-Up-Procedures.pdf

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K i ln Start-up Procedu res Presentat ion & Instructor Notes 

Operator DevelopmentKiln Control Best Practices

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Pyro-processing: Kiln Control 4

Kiln Start-up Procedures

Learning Objectives

At the end of this session you should be:

fami l iar with the start-up BP 

able to l ist the major steps invo lved 

name the requ ired pro cess ind icators 

able to explain the cus tom izat ion dif ferences w ith 

you r plants SOPs 

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End-users: Production Operators/technicians

Content: Checks p r ior to start-up 

Kiln preheat preparat ion: Bu rner pip e, Refractory 

Kiln Preheat schedu le:  Parameters to monitor 

Tire Creep

Turning schedule

Start-up Process data sheet

Kiln lining preheat schedule Feeding raw m ix 

What to do in c ase of deviat ions 

Start-up Pos t-aud it 

Kiln Start-up Procedures

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Pyro-processing: Kiln Control 6

Pre Start-up Checks

Dry run & complete check sheets

Feed Sys tem 

Cooler & Clinker Handl ing 

ID fan 

Coal Conveying System 

Ki ln Baghouse ESP 

Pre-heat sy stem 

Pre-heater tour 

Bu rner Pipe al ignment 

Common & auxi l iary equipment 

Check sheets should include room for comments

& assigned responsibility

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Sample:

Pre Start-up Checks

Feed System

recirculat ion mode & cal ibrate 

if no recirculation ... run briefly check operation, leaks

run dust evacuat ion (e levators, screws & pumps) 

Cooler & clinker handling

run cooler dr ives & inspect for loose grates 

check cooler alignment while running

run for 12 hours (mechanical integrity)

Breaker, fans, con veying equ ipment 

alignment, motor direction, automation & full motion

operation & seal of all Plattco valves

calibration of all pressure transmitters

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Kiln Preheat Prep

Burner pipe alignment

exact ly w here is th e pipe in relat ion to the ki ln 

laser al ignm ent measu red in 3 places 

Refractory preparation manage the ins tallat ion o f refractory ,

proper installation is key to longevity

fo l low p rocedu re for preheat ing to maximize br ick l i fe 

Burner pipe lining

pou red castable mus t cure 24 hrs before remov ing 

forms or at temp t ing bake-out 

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Burner Pipe Lining Preheat Schedule

Four inch refractory lining

50

100

150

200 200 200 200 200

250

300

350

400

450

500

550

600 600 600 600 600

0

100

200

300

400

500

600

700

1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20

Temperature C

bake-out - adjust per inch of refractory

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Kiln Preheat Schedule

Determined Prior to Start-up

10-14 process parameters should be recorded l ist di f fers for precalciner & long ki lns 

Example list (incomplete) oxygen 

back -end, BZ temperatures 

tyre creep, tyre & bear ing temperature 

hood pressure 

fuel con sumpt ion 

turn ing schedule 

Kiln shell temperature ( BZ) 

ESP/Baghouse 

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Kiln Start-up Process Data Sheet

Date: _________________ Time of Flame On:_________________ Preheat Schedule: -

 _____ Hours

 ___________________ Hour of the

Preheat

Tyre Creep

#1 Tyre

Tyre Creep

#2 tyre

Hour of the

Day

Chain Gas

Temp

Fuel Rate Feed End

Oxygen

Swirl Air 

Setting

Axial Air 

Setting

Feed End

Temp

I.D. Fan

Speed

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Tyre Creep Control

Minimum heating-up period

determ ined by the t ime required to s tabi l ize the 

temperatur e difference, hence the clearance 

shel l heats up faster than tyre 

Tyre #2 is critical

too rapid heat ing w i l l constr ic t ki ln shel l 

resul t in permanent shel l deform ation 

excessive tyre sl ip after no rmal temp. regained 

Creep should be monitored at regular intervals i f low, heat ing shou ld be slowed 

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Pyro-processing: Kiln Control 14

Turning Schedule

Ensures slow, uniform heating of the kiln and

refractory

increase in temperature over t ime 

allows for the expansion of refractory and s hel l 

br ick remains in p lace and shel l expands uni form ly 

along its long itudinal axis 

Too Slow

overheat ing o f refracto ry and shel l 

shell & refractory damage (e.g. “duck - nesting” ) 

Too Fast

longer preheat t imes du e to poo r heat transfer 

potent ia l br ick spiral ing 

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Pyro-processing: Kiln Control 15

Turning Schedule Example

KILN TURNING PROCEDURE WITH 

AUXILIARY DRIVE 

UP TO 120 C KEEP THE KILN STOPPED

120 C TO 210 C TURN 90 TO 120 EVERY 45 MINUTES

210 C TO 450

 C TURN 90

 TO 120

 EVERY 30 MINUTES

450 C TO 600 C TURN 90 TO 120 EVERY 15 MINUTES

600 C TO 750 C TURN 90 TO 120 EVERY 10 MINUTES

750 C UP TO FEEDING CONTINUOUS TURNING

Reference temperature (Lower

stage)

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Pyro-processing: Kiln Control 16

Kiln Preheat Schedule

Major & short shutdown

0

100

200

300

400

500

600

700

800

900

1000

0 3 6 9 12 15 18 21 24 27 30 33 36 39 42

HEATING-UP GRAPH FOR ROTARY CEMENT KILNS

   K   i   l  n  e  x   i   t  g  a  s   t  e  m  p  e  r  a   t  u  r  e  a   t   i  n   l  e   t  a  r  e  a

Heating-up Time, hours

º

{START OF MATERIAL FEED ACCORDING TO

{KILN TYPE AND OPERATING PROCESS

1300*

1200*

900*

600*

300*

curve 1:

Limited

repairs

30-35 C/h

curve 2:

Complete

relining

20-25 C/h

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Pyro-processing: Kiln Control 17

Kiln Preheat Schedule - Detailed

stepped to inclu de two holdin g patterns (300, 550 C) 

allows refractor to “catch- up” with gas temperature 

24 HOUR PREHEAT SCHEDULE

0

100

200

300

400

500

600

700

800

900

1000

1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28HOURS

   T   E   M   P   E   R   A   T   U   R   E

0.0

5.0

10.0

15.0

20.0

25.0

   O   X   Y   G   E   N STG 4 TEMP

STG 1 TEMP

STG1 OXYGEN

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Pyro-processing: Kiln Control 18

Feeding of Raw Material

Raw material feed “ON” 

when burning zone is ready 

Start of feed and arrival in sintering (burning) zone is

critical to tyre creep

fue l supply m ust be increased 

com pensate for heat absorb ed by raw mater ial 

Close attention to tyre slip

i f sl ip ceases, coun ter measures m us t be taken 

Limited feed may be introduced prior to optimaltemperature to assist coating

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Pyro-processing: Kiln Control 20

Start-up Post Audit

Analyze deviations from the planned schedule to

continuously improve operational performance

produ ct ion coo rdinator , ki ln coach & operators 

ident i fy reason s for deviat ion s 

make jo int recommendat ions 

correct SOPs and circu late among al l operators 

Develop a table of variances and explanations

Use our collective knowledge & experience to

become the world’s best cement producer!