LVT Key reference projects for Plant Upgradation L/O/G/O

LVT Key reference projects for Plant Upgradation L/O/G/O

LVT Key reference plant/kilns upgrade jobs Client Project Name Country Detail CMS Plant upgrading to 2800 TPD Malaysia Turnkey Contract for plant upgrading from 2100 TPD to 2800 TPD (Actual achieve is 2880 TPD) NSCI Plant upgrading to 4000 TPD, Bahau Plant Malaysia EP Contract for kiln upgrading from 3600 TPD to 4000 TPD (Actual achieve is 4300 TPD) NSCI Kiln upgrading to 2750 TPD, Perlis Plant Malaysia EP Contract for kiln upgrading from 1900 TPD to 2750 TPD (Actual achieve is 2850 TPD) Power Cement (Al Abbas Cement) 2 Plants upgrading to 1000 TPD and 1800 TPD Pakistan EP Contract for plant upgrading from 500 TPD to 1000 TPD and 1000 to 1800 TPD Cemex 2 Kilns upgrading to 1000TPD Thailand EP Contract for plant upgrading to 1000 TPD Hanil Kiln upgrading to 4800 TPD Korea Engineering supply for kiln upgrading 4800 TPD Apiai Kiln upgrading to 2850 TPD Brazil EP Contract for plant upgrading from 2200 TPD to 2850 TPD Bodoquena Kiln upgrading to 1900 TPD Brazil EP Contract for plant upgrading to 1900 TPD Hoang Mai Kiln upgrading to 4500 TPD Vietnam EP Contract for kiln upgrading to 4500 TPD Chinfon 2 Plants upgrading to 4800 TPD and 5000 TPD Vietnam Engineering supply for kiln upgrading to 4500 TPD and 5000 TPD

LVT Key reference Nozzle ring upgrade jobs Client Project Name Country Detail APODI Nozzle ring upgrading Brazil Engineering supply for Nozzle ring upgrading for Raw Vertical Mill from 290 tph to 320 tph Holcim Nozzle ring upgrading (Vietnam Plant) Vietnam Engineering supply for Nozzle ring upgrading for Raw Vertical Mill from 347 tph to 375 tph Viacha Nozzle ring upgrading Bolivia Engineering supply for Nozzle ring upgrading for Raw Vertical Mill from 155 tph to 180 tph Holcim Nozzle ring upgrading (Lugait Plant) Philippines Engineering supply for Nozzle ring upgrading for Raw Vertical Mill from 305 tph to 320 tph

LVT Key reference LV Classifier for Semi Finish Grinding System Client Project Name Country Detail TPIPL LV Classifier for semifinish grinding upgradation Thailand EP Contract for cement mill upgrading from 220 tph to 257 tph

LVT Key reference plant/kilns upgrade jobs

CMS, Malaysia Plant upgrading to 2800 TPD Client Name: Cahya Mata Sarawak, Malaysia LVT Role: Turnkey EPC Contract for plant upgrading from 2,100 TPD to 2,800 TPD (Actual achieve is 2,880 TPD) Project period: 2011-2013 Job carried out : Plant Modification to achieve guarantee capacity 2,800 TPD with New vertical raw mill and new vertical coal mill 1) Raw Mill New raw mill grinding circuit of brand new vertical mill LVT/C- Hope (VRMR36.4) with LVT Classifier by normally VRMR36.4 can achieve 200 TPH but when operate with LVT Classifier the mill can achieve up to 230 TPH. New hot gas handling system for new raw mill department New Feeding system New bucket elevator for silo feeding.

2) Pre heater: Top stage 4 cyclones replaced with 2 new LVT spiral roof cyclones to reduce the pressure drop and improve the collection efficiency. 2 nd and 3 rd stage cyclones increased height of cyclone roof to reduce pressure drop in the preheater by increasing of cyclone inlet area 5 th stage modified inlet cyclone. Extension of calciner to increases the retention time and full combustion Installation of dispersion box at all stages of cyclones except cyclone no.5. This will ensure the effective heat transfer between hot gas and raw meal. Kiln inlet seal replaced with pneumatic type to arrest the false air leakage 3) Gas handling department: Existing ESP modified the electrical parts for support extra flow and clinker dust from cooler after increase clinker production as well as reduction of dust emission. Installation of new mechanical parts for ESP system for support the new gas flow. New kiln dust transportation transported to existing bucket elevator.

4) Kiln: Increase kiln speed to 4.5 rpm for reduce volumetric loading from higher kiln capacity to keep kiln filling percentage when increase the production by changing gear box and new AC drive motor. Kiln main burner replaced with high momentum burner After modification, kiln can achieve the capacity up to 2,850 TPD with free CaO of clinker less than 1%. 5) Cooler: Added fixed inlet at the cooler starting portion with new cooler air fans in order to get maximum heat recuperation. Replace 1 st grate of cooler by LV cooler with relocation of cooling air fan Clinker transportation machine was modified for support the new upgrading capacity.

6) New Vertical Mill with LV Classifier for Coal grinding New coal grinding circuit Installation of Beijing power Vertical millfor fine coal preparation, Mill-ZGM80G with LVT Classifier by when operate with LVT Classifier the mill can achieve the capacity up to 20.6 TPH. New hot gas handling for new coal mill department New feeding system for raw coal New coal feeder for calciner firing.

Vertical Mill with LV Classifier Rotation direction LV Pocket (Guide vane) Rotor Centrifugal force Drag force Gravity force COARSE FINE

CMS, Malaysia Plant upgrading to 2800 TPD Guaranteed and PGT figure : Description Guarantee PGT Kiln (TPD) 2800 2846 Raw Mill (TPH) 230 232 Coal Mill (TPH) 18.5 20.6

CMS, Malaysia Plant upgrading to 2800 TPD

NSCI, Bahau Plant Plant upgrading to 4000 TPD Client Name: Negeri Sembilan Cement Industries Sdn. Bhd., Malaysia LVT Role: EP Contract for plant upgrading from 3600 TPD to 4000 TPD (Actual achieve is 4300 TPD) Project period: 2007-2008 Main objective : To increase the plant capacity from 3,600 to 4,000 TPD and reduce plant power consumption

Job carried out : Modifications to achieve guarantee capacity 4,000 TPD 1) New LVT top cyclones NSCI, Bahau Plant Plant upgrading to 4000 TPD The LVT top cyclones will improve the efficiency and decrease the pressure drop of the preheater. 2) Enlarge inlet area to 2 nd stage cyclone The inlet area to the 2 nd stage is increased by lifting the roof in order to decrease the inlet velocity and thereby the pressure loss.

3) LVT design dispersion box for all stages New effective dispersion boxes are required to disperse the material properly when the velocity on cyclone riser pipes increases. This will ensure the effective heat transfer between hot gas and raw meal. 4) Extension of calciner NSCI, Bahau Plant Plant upgrading to 4000 TPD To increase the retention time and better burning of fuel in the calciner 5) New inlet and triangular cut in bottom stage cyclone The inlet modified according to the calciner modification. The new inlet will have a positive effect on the coating tendencies in this inlet. A triangular cut is made to the bottom stage cyclone in order to improve the cyclone efficiency and decrease the specific heat consumption.

6) Water spray in down comer The water spray system is designed to reduce the temperature of the gases leaving the preheater by 50 C, which will increase the ID-fan capacity. This water spray system will work as a secondary cooling tower as well. 7) New ID-fan and motor NSCI, Bahau Plant Plant upgrading to 4000 TPD It is necessary to install a new ID-fan with a higher flow and pressure rating than the existing. 8) New filter fan and motor parallel to existing ESP Fan A new parallel filter fan installed parallel to existing ESP fan. This will facilitate to exhaust the additional kiln gases after the upgrading to 4000 tpd.

NSCI, Bahau Plant Plant upgrading to 4000 TPD 9) GCT modification The gas conditioning tower modified with new water spray system to achieve 160 Deg.C gas temperature as the outlet. 10) Clinker transport Installed the new transportation for support material flow after kiln upgrade to 4,000 TPD.

NSCI, Bahau Plant Plant upgrading to 4000 TPD

NSCI, Bahau Plant Plant upgrading to 4000 TPD

NSCI, Perlis Plant Kiln upgrading to 2750 TPD Client Name: Negeri Sembilan Cement Industries Sdn. Bhd., Malaysia LVT Role: EP Contract for kiln upgrading from 1900 TPD to 2750 TPD (Actual achieve is 2850 TPD) Project period: 2008-2009 Main objective : To increase the plant capacity from 1,900 to 2,750 TPD and reduce plant power consumption

NSCI, Perlis Plant Kiln upgrading to 2750 TPD Job carried out : 1) Pre-heater Cyclone modification Installation of new top LVT cyclone. To install new dispersion boxes for improve heat exchange efficiency Top part of downcomer duct modified. Enlarge and extend calciner to increase retention time. Modified tertiary air duct and connect to the calciner Kiln hood modification for reducing of hot cooler dust injection issue which cause severely injured New coal feeding system for calciner firing

2) Kiln gas dedusting Installation of new main baghouse for upgrade capacity (former is ESP) 3) New Kiln motor, VVVF and Gear box Installed a new motor and gear box for new kiln speed. 4) Clinker Cooler modification New fixed inlet (7 rows 8 plate wide) and 2 new fixed inlet cooler fan for increase heat recuperation. 5) Cooler cooler ESP extenstion Extend one more field for existing ESP for additional amount of cooler waste gas and reduce dust emission 6) Kiln feed system New bucket elevator for kiln feed system

NSCI, Perlis Plant Kiln upgrading to 2750 TPD

Power cement, Pakistan 2 Plants upgrading to 1000 TPD and 1800 TPD Client Name: Al Abbas Cement, Pakistan LVT Role: EP Contract for plant upgrading from 500 TPD to 1000 TPD and 1000 to 1800 TPD (Actual achieve are 1,236 and 1,891 TPD) Project period: 2005-2007 Main objective: To increase 2 plants capacity from 500 TPD to 1000 TPD and 1000 TPD to 1800 TPD Job carried out : 1) Vertical Mill for raw material grinding Installed new transportation equipment for support upgrading capacity.

1) Vertical Mill for raw material grinding (cont.) Power cement, Pakistan 2 Kilns upgrading to 1000 TPD and 1800 TPD Installed new raw vertical roller mill(lm32.4 with LVT Classifier, normally this mill size can achieve the capacity below 200 TPH but when operate with LVT Classifier can achieve the capacity up to 216 TPH) 2) New kiln feed system Installed new kiln feed transportation machine for support upgrading capacity.

3) Preheater system and clinker cooler modification Installed the LVT top cyclones for improve the efficiency and decrease the pressure drop of the preheater. New kiln gear reducer for new kiln speed. Tertiary Air Duct, clinker cooler, and fan system and dust collecting system was modified. 4) Clinker storage and new cement grinding system Power cement, Pakistan 2 Kilns upgrading to 1000 TPD and 1800 TPD Installed the new clinker storage and transportation for increasing the stock capacity. Installed the new cement vertical mill system and modified the existing cement ball mill by optimize ball charge and installed the LVT Classifier system.

Power cement, Pakistan 2 Kilns upgrading to 1000 TPD and 1800 TPD 5) New cement packing system Installed the new packing plant system for support new upgrading capacity. 6) Coal grinding system modification Installed the new coal vertical roller mill system (Raymond Mill) with LV Classifier for support new upgrading kiln system.

Cemex, Thailand 2 Kilns upgrading to 1200 TPD Client Name: CEMEX Thailand LVT Role: EP Contract for kiln upgrading from 900 TPD and 1200 TPD Project period: 2003-2004 Main objective: To increase the plant capacity from 900 to 1,200 TPD

Job carried out : Cemex, Thailand 2 Kilns upgrading to 1200 TPD New top stage cyclones Top cyclones preheater will be replaced to the new LVT cyclones (without refractory) for improving the efficiency. It can be improved by installing a cylindrical part at the body of the cyclone. LVT suggest modifying the complete inlet duct section to the top stage cyclones to LVT new design, to avoid the present ducting pinch point at the cyclone inlets, where caking on tendency on the roof has been observed. This will also reduce the pressure drop over the top cyclone stage. The new cylindrical cyclone part will also call for installation of an extra downcomer part.

Cemex, Thailand 2 Kilns upgrading to 1200 TPD Modification of the 4 stage cyclone Expand the riser duct after Pre-calciner and Enlarge the riser part of the Pre-calciner A small but not unimportant improvement can be done in the riser part of the calciner. The expansion of the riser part was done on the front side (towards the kiln) and on the right side (seen from the kiln). The start of the riser expansion to the sides has been done nearly horizontal, which has created shelves and areas for possible turbulence resulting in downwards flow and undesired material dropping directly to the kiln (along the walls). New preheater ID Fan & Motor

Cemex, Thailand 2 Kilns upgrading to 1200 TPD New top stage cyclones without refractory Modification of the 4 th stage cyclone Expand the riser duct after Pre-calciner Enlarge the riser part of the Pre-calciner New preheater ID Fan & Motor

Cemex, Thailand 2 Kilns upgrading to 1200 TPD Guaranteed figure : Description Present Pass Guaranteed (FAC*) Production (TPD) 900 1200 *Final Acceptance Certification

Hanil Cement (Danyang plant ), Korea Kiln No.5upgrading to 4800 TPD Client Name: Hanil Cement (Danyang plant), Korea LVT Role: Engineering Service for kiln upgrading Project period: November 2008 April 2009 Main objective: To increase the kiln capacity from 4,320 to 4,800 TPD and increasing the waste firing upto 20% In year 2008, Hanil cement at Danyang plant would like to upgrade plant capacity and they consult with LVT. After LVT team investigation, the LVT suggest that the Danyang plant can be upgraded to 4800 tpd from 4320 TPD as per the measured during pretest.

Hanil Cement (Danyang plant ), Korea Kiln No.5upgrading to 4800 TPD The operation by following the existing main equipment In-Line Calciner (ILC) 5-stage preheater with swirl chamber Kiln 4.57 x 67 m, slope 4 % Kiln drive motor 522 kw Fuller grate cooler (CIS-CFG-RFT) Pillard kiln main burner

Hanil Cement (Danyang plant ), Korea Kiln No.5upgrading to 4800 TPD Job carried out : 1) Cyclone Preheater The 4 existing top cyclones will be replaced by completely new LV Cyclones to reduce the pressure loss and to improve the top cyclone efficiency. This will lead to a bit higher pressure drop over the new LVT top stage cyclones. The cyclones are foreseen installed with 114 mm castable

Hanil Cement (Danyang plant ), Korea Kiln No.5upgrading to 4800 TPD 2) Extension of the ILC calciner with New TAD inlet and new LVT mixing chamber Hanil is firing approx. 20 % of waste fuel to the calciner. This leads to operational problems and CO formation in the calciner. Hanil possesses at the same time a strong desire to increase the waste firing to 30 %.

Hanil Cement (Danyang plant ), Korea Kiln No.5upgrading to 4800 TPD Extension of the ILC calciner LVT therefore suggests extending the existing calciner with a new square duct. The result in the largest possible extension of the calciner gas retention time, which is crucial for the satisfying completion of the combustion of the waste fuel fired in the calciner. The calciner a gas retention time of approx. 4.6 seconds is achieved (at 4800 TPD)

Hanil Cement (Danyang plant ), Korea Kiln No.5upgrading to 4800 TPD New TAD inlet and new mixing chamber Installing a new LVT mixing chamber and a modified TAD inlet to the new mixing chamber. The reason is that the existing swirl chamber is much too large (low gas velocity) and do not facilitate a proper mixing of the calciner fuel (waste) and the combustion air. The result is the observed CO problems out of the calciner. With the new LVT mixing chamber we improve the start conditions for the combustion of the calciner fuel (waste), and we are convinced that it shall be possible to increase the %-waste fired from the existing 20 % even at the increased clinker production level to 4800 TPD.

Hanil Cement (Danyang plant ), Korea Kiln No.5upgrading to 4800 TPD 3) New LVT material flap gates Installation of new LVT material flap gates to minimize the amount of heat transfer bypass gas flows in the preheater. Any amount of hot gas bypassing the heat transfer process stages leads to an increase in the kiln system heat consumption and to increased temperature profile and hereby to increased pressure drop and increased fan power consumptions 4) Modified inlets to the two bottom stage (C5) cyclones Modification of the inlets to the two cyclone stage number 5 cyclones to minimize dust settlement and build up in these areas.

Hanil Cement (Danyang plant ), Korea Kiln No.5upgrading to 4800 TPD 5) Material spreader boxes (distribution boxes) The existing spreader boxes (distribution boxes) in the preheater are suggested replaced by new and more efficient spreader boxes of LVT design

Hanil Cement (Danyang plant ), Korea Kiln No.5upgrading to 4800 TPD Over all for modification

Hanil Cement (Danyang plant ), Korea Kiln No.5upgrading to 4800 TPD Guaranteed figure : Description Present (Sep.07) Present (Sep.08) Pass Guaranteed (FAC*) Production (TPD) 4,461 4,320 (+) 4,800 (#) Heat cons. (kcal/kg) 657** 710 (+) 657** Specify power consumption (kwh/t), kiln drive 1.75 2.08 (+) 1.75 Waste firing in calciner (%) Approx.20** Approx.13 (+) 20 at 4,800 TPD *Final Acceptance Certification **The heat consumption figure does not include (not constant) the combustibles added in the raw mix.

Hanil Cement (Danyang plant ), Korea Kiln No.5upgrading to 4800 TPD

APIAI, Brazil Kiln upgrading from 2200 TPD to 2850 TPD Client Name : APIAI Brazil (Intercement group) LVT Role: EP Contract for plant upgrading from 2200 TPD to 2850 TPD Project period: 2009-2011 Main objective : To increase the plant capacity from 2200 to 2850 TPD Job carried out 1) Kiln-Preheater section modification The homogenizing silo replaced aeration system. The kiln feeding added by new rotary feeder and belt weigh feeder together with a new FULLER pump and blowers.

APIAI, Brazil Kiln upgrading from 2200 TPD to 2850 TPD 1) Kiln-Preheater section modification (cont.) The kiln equipped with new four cyclones at top stage and 2 nd stage pre heater. The installation of LVT cyclone improved the efficiency of the collection efficiency, decrease the pressure drop of the preheater Modified inlet and new outlet of six cyclones at 3 rd, 4 th and 5 th stage to decrease the inlet velocity and thereby the pressure loss. This will ensure the effective heat transfer between hot gas and raw meal. Installed the new calciner placed inline on top of the kiln. The retention time in the calciner will be about 2.5 s. The installation of the calciner made the retention time and better burning of fuel in the calciner.

APIAI, Brazil Kiln upgrading from 2200 TPD to 2850 TPD 1) Kiln-Preheater section modification (cont.) The kiln shortened corresponding to the new lay out of the pre heater, and a new kiln inlet seal was installed A new ID fan with 15% reserve on the flow and 30% reserve on the pressure was installed. The gas conditioning tower was installed. Hot gases from the ID fan was cooled in a conditioning tower to app. 200 dg. C, and at the location of the existing ESP a new bag filter was installed. The existing housing of the ESP can be re-used. For the de-dusting a new fan has been included. To make the cooler more efficient a new fixed inlet was installed with a surface area of approximately 6 sqm. together with a new cooling fan and the renovation of Grate 1.

APIAI, Brazil Kiln upgrading from 2200 TPD to 2850 TPD 2) New vertical mill for petcoke grinding To install vertical mill (Ube mill) with LV classifier with gas handling system for petcoke grinding To install new feeding system to vertical mill To install fine petcoke feeding to kiln system 3) Cement mill classifier To install LV Classifier for existing cement mill system

APIAI, Brazil Kiln upgrading from 2200 TPD to 2850 TPD

APIAI, Brazil Kiln upgrading from 2200 TPD to 2850 TPD

Bodoquena, Brazil Kiln upgrading to 1,900 TPD Client Name: Bodoquena, Brazil (Intercement Group) LVT Role: EP contract for Plant upgrading to 1,900 TPD Project period: 2009-2010 Main objective : To increase the kiln capacity from 1,500 to 1,900 TPD Job carried out : 1) Kiln-Preheater section modification Change new ID fan to higher efficiency and bigger capacity Fixed inlet of the cooler and modification of first grate Extension of calciner to increase retention time, modification of triangular cut of 3nd and 4 th cyclones, increase roof height of bottom cyclone and dividing gate Addition BF for additional preheater waste gas to handle additional preheater waste gas

Bodoquena, Brazil Kiln upgrading to 1,900 TPD 2) Coal mill modification to LV-MODE Modification of the Classifier to an LV-type and an adjustment of the velocity profile in the mill so that the materials are accelerated to the classifier avoiding static classification in the mill body With concept to control the entire flow of both material and air in the mill to be able to reduce the internal circulation of material in the mill By modifying vertical mill to LV-MODE an increase in production of 18%, with a consequent power saving is possible 3) Cement mill modification The gases from separator outlet shall go to LV cyclone to reduce dust load before bag filter inlet

Bodoquena, Brazil Kiln-Preheater section modification

Bodoquena, Brazil Kiln-Preheater section modification

Bodoquena, Brazil Kiln-Preheater section modification

Bodoquena, Brazil Kiln-Preheater section modification Guaranteed and expected figure : Description Guaranteed Obtained (*PAC) Clinker production (TPD) 1,900 2,032.4

Bodoquena, Brazil Cement Mill Modification with LV-cyclone

Bodoquena, Brazil Mill modification with LV-cyclone

Bodoquena, Brazil Mill modification with LV Cyclone Guaranteed and expected figure : Description Present Obtained (*PAC) Cement production (TPH) @Blaine 3065 cm2/g 107.57 123.3

Bodoquena, Brazil Coal mill modification to LV-MODE

Bodoquena, Brazil Coal mill modification to LV-MODE Guaranteed and expected figure : Description Present Guaranteed Fine coal production (TPH) 11 13 %Residue @90µm 2.5 2.5 HGI (Min.) Pet coke 35 35 HGI (Min.) Coal 55 55

Hoang Mai, Vietnam Kiln upgrading to 4500 TPD Client Name: Hong Mai, Vietnam LVT Role: EP contract for Kiln upgrading to 4500 TPD Project period: 2005-2007 Main objective : To increase the kiln capacity from 4,100 to 4,500 TPD Job Carried out : 1) Kiln-Preheater section modification New LVT top cyclones to improve the efficiency and decrease the pressure drop of the preheater A triangular cut at the inlet to bottom stage cyclones to improve the collecting efficiency of the bottom stage cyclones by leading the gas and material away from the immersion tube Extension of calciner to increase retention time Addition filter fan (parallel existing fan) to handle the additional smoke gases

Hoang Mai, Vietnam Kiln upgrading to 4500 TPD 2) Raw mill MPS5000B modification with LV Classifier The modification of the Classifier to an LV-type and an adjustment of the velocity profile in the mill so that the materials are accelerated to the classifier avoiding static classification in the mill body With concept to control the velocity of the air any point in the mill body from above the rollers. This system effectively separates the transport of the material rejected by the classifier from the air transport of material to the classifier By increasing the efficiency of the entire classification process in the mill it is possible to reduce the specific power consumption of mill and fan

Hoang Mai, Vietnam Kiln-Preheater section modification

Hoang Mai, Vietnam Kiln-Preheater section modification

Hoang Mai, Vietnam Kiln-Preheater section modification Guaranteed and expected figure : Description Present Guaranteed Achieved Clinker production (TPD) Heat consumption (kcal/kg) P preheater (mbar) 4,150-4,200 4,500 4,580 800 N/A 775 73 N/A 75

Hoang Mai, Vietnam Raw mill modification with LV Classifier

Hoang Mai, Vietnam Raw mill modification with LV Classifier Guaranteed and expected figure : Description Present Expected Raw meal production (TPH) 320-325 360 %Residue @90µm 12 <12 Mill Specific power consumption (kwh/t) Mill fan Specific power consumption (kwh/t) Total Specific power consumption (kwh/t) 8.6 8.5 6.6 5.0 15.2 14 P fan (mmwg) 900 850 Fan flow (m3/h) 630,000 590,000

Chinfon, Vietnam Kiln No.1 upgrading to 4,800 TPD Client Name: Chinfon, Vietnam LVT Role: Engineering supply for Kiln No.1 upgrading to 4,800 TPD Project period: 2003-2005 Job Carried out : 1) Kiln upgrade to 4,800 TPH Modification top cyclone to be LV cyclones to improve the efficiency and decrease the pressure drop of the preheater Addition EP fan 2) Coal mill modification with LV Classifier

Chinfon, Vietnam Kiln No.2 upgrading to 5,000 TPD Client Name: Chinfon, Vietnam LVT Role: Engineering supply for Kiln No.2 upgrading to 5,000 TPD Project period: July, 2009-2010 Job Carried out : 1) Kiln No.2 upgrade to 5,000 TPH Modification top cyclone to be LV cyclones to improve the efficiency and decrease the pressure drop of the preheater Addition EP fan (parallel existing fan) Modification kiln feed bucket elevators by increasing speed Installation new burner 2) Modification of LV Classifier by install LV-Pocket Modification of LV Classifier for Raw mill No.2 (UM40.4) Modification of LV Classifier for Coal mill (UM26.3) Modification of LV Classifier for Cement mill (UM46.2+2)

Chinfon, Vietnam Kiln No.2 upgrading to 5,000 TPD Guaranteed and expected figure : Description Present Guaranteed Clinker production (TPD) 4,300 > 5,000 *With Modification of LV Classifier for Raw mill No.2 and Coal mill Description Production (TPH) %Residue @90µm Specific power consumption (kwh/t) Raw mill No.2 Raw mill No.1 Same as Raw mill No.1 0.5 kwh/t less than Raw mill No.1 Coal mill (HGI 37) 15% more than UBE Guarantee Same as present N/A *Power consumption covering mill, classifier and fan(s) Cement mill 170 (@3600 cm2/g) N/A 0.5 kwh/t less than present

LVT Key reference Nozzle ring upgrade jobs For Vertical Mills

Nozzle Ring Upgrading Drawing section of mill

Nozzle Ring Upgrading Before After

Nozzle Ring Upgrading Existing LV modification

Nozzle Ring Upgrading Nozzle ring modification

Client Name: APODI, Brazil LVT Role: Engineering supply and supervision for Nozzle ring modification of Raw vertical mill Project period: 2015 Apodi, Brazil Raw mill UBE38.4 Main objective: Nozzle Ring Modification for upgrading vertical mill Nozzle ring Before After Capacity (tph) 290 320 Reject (tph) ~ 100 <20 Mill pressure diff. (mbar) - 12 Power saving (Kwh/t) - 0.5

Apodi, Brazil Raw mill UBE38.4

Client Name: Holcim, Vietnam LVT Role: Engineering supply and supervision for Nozzle ring modification of Raw vertical mill Project period: 2015 Holcim, Vietnam Raw mill LM46.4 Main objective: Nozzle Ring Modification for upgrading vertical mill Nozzle ring Before After Capacity (tph) 347 375 Reject (tph) ~ 100 <40 Mill pressure diff. (mbar) - 12 Power saving (Kwh/t) - -

Holcim, Vietnam Raw mill LM46.4

Client Name: Viacha Cement Plant, Bolivia LVT Role: Engineering supply and supervision for Nozzle ring modification of Raw vertical mill Project period: 2016 Viacha, Bolivia Raw mill ATOX32.5 Main objective: Nozzle Ring Modification for upgrading vertical mill, Additional Chute, Lowering the Dam Ring Nozzle ring Before After Capacity (tph) 155 180 Reject (tph) - - Mill pressure diff. (mbar) - - Power saving (kwh/t) - -

Viacha, Bolivia Raw mill ATOX32.5

Holcim, Philippines Raw mill LM48.4 Client Name: Holcim Lugait Plant, Philippines LVT Role: Engineering supply and supervision for Nozzle ring modification of Raw vertical mill Project period: 2016 Main objective: Nozzle Ring Modification for upgrading vertical mill, Lowering the Dam Ring Nozzle ring Before After Capacity (tph) 305 320 Reject (tph) >100 <40 Mill pressure diff. (mbar) - 2 Power saving (Kwh/t) - -

Holcim, Philippines Raw mill LM48.4

LVT Key reference LV Classifier for semi-finish grinding upgradation

TPIPL, Thailand Upgradation of Semi-Finish Grinding Client Name: TPI Polene PCL, Thailand LVT Role: Engineering, supply of equipment and erection for cement ball mill no.1 upgradation Project period: 2015-2016 Main objective: To improve the capacity of semi-finish grinding system by LV Classifier system

TPIPL, Thailand Upgradation of Semi-Finish Grinding Existing system consisting of roller press with 2x825kW (Polycom) and ball mill 4.8x14.5 m, 5400 kw. Job carried out : Installation of LV classifier for material outlet from roller press Installation of LV cyclone Installation of gas handling system of classifier circuit Nozzle ring Before After Capacity (TPH) 220 257.4 Blaine (cm2/g) 3785 3776 Sieve on 45 micron (%) 9.16 4.8

TPIPL, Thailand Upgradation of Semi-Finish Grinding

TPIPL, Thailand Upgradation of Semi-Finish Grinding Inlet chute Fluidizing bed system Guide plate

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