Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion Introduction

Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion In 2008, Philippines purchased almost worth of SBR. $60 billion

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion Styrene Butadiene Water Buffer Coagulation Agent Shortstop Agent Chain Transfer Agent Emulsifier RAW MATERIALS

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion PROCESSES SOLUTION STYRENE BUTADIENE RUBBER batch and continuous operation high performance tire applications EMULSION STYRENE BUTADIENE RUBBER continuous operation used under mild reaction conditions COLD ESBR - 4  C HOT ESBR - 50  C

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion E-SBR PROPERTIES excellent abrasion resistance crack resistance water resistance USES decreases the rolling resistance of tires improves the green strength of natural rubber Note: The green strength of an elastomer is its resistance to deformation and fracture before vulcanization

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion Main Families of E-SBR Hot Nonpigmented Rubber (1002 to 1028) Cold Nonpigmented Rubber (1500 to 1573) Cold Oil Master Batch (1700 to 1779) Cold Oil – Black Master Batch (1601 to 1622 and 1805 to 1849) Emulsion Resin – Rubber Master Batch and High-Styrene Reinforcement Polymers (1900 To 1960)

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion E-SBR 1500 good extrusion behavior superior compound properties exceptional resistance to cutting, tearing and abrasion Applications: tires, tread rubber, and molded and extruded mechanical goods

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion Market Study

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion E-SBR

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion Global Market 3,286,677 4,571,201 8,201,902 $23,144.3 Billion

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion Global Market $23,144.3 Billion Booming Automotive Car Industry China India Japan Korea

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion Local Market

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion Local Market

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion Market Production Forecast

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion Market Competition NaturalSynthetic Rubber Tree 5 to 30 years Present but insufficient Chemicals 8 to 12 hours Present but imported Substitute for Natural Rubber

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion Market Competition COMPETITORS Art-Chem Ind'l Sales Corp. Bayer Phils. Inc. Behn Meyer Phils. Inc. Brenntag Ingredients, Inc. Connell Brothers Co. Pilipinas, Inc. DKSH Philippines Himmel Industries, Inc. Jebsen & Jessen Chemicals Trans World Trading Co., Inc. Uni-Dravo Commercial Knottical Power Energy Corporation Mitsui & Co. (Asia Pacific) Pte. Ltd. Manila Branch Nuevochem Specialties, Inc. (NSI) Phoenix Petroleum Philippines, Inc. Shiraishi Calcium Kaishia Ltd. Solid State Multi-Products Corp. Legaspi Imports-Exports Sytengco Enterprises Corp.

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion Target Market ProductManufacturer Tires Auto/Truck Motorcycle/Bicycle Goodyear Philippines, Inc. MSF Tire and Rubber, Inc. Johnson Mfg. Company, Inc. Manhattan Rubber and Plastics Manufacturing First Solid Rubber Industries Materials of Rubber Manila Rubber Corporation Power Synthetic Rubber Manufacturing Corporation Marcelo Tire and Rubber Corporation Laguna Rubber Company, Inc. Articles of Rubber Latex Products Company Eventflo Philippines, Inc. Pioneer Elastic Thread Corporation Mitsubishi Belting Philippines Corporation Transworld Rubber Industrial Mfg. Corporation Rubber FootwearFilcon Mfg. Corporation New Olympian Rubber Products Company Paramount Vinyl Products Company

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion STYRENE BUTADIENE LATEX SHORTSTOP WATER EMULSIFIER FESO 4 EDTA DODECYL MERCAPTAN CUMENE HYDROPEROXIDE MIXING TANK

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion LATEX PRESSURE FLASH COLUMN VACUUM FLASH COLUMN BLOWDOWN TANK BUTADIENE- FREE LATEX RECYCLED BUTADIENE

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion LATEX BLEND TANK COAGULATION TANK H 2 SO 4 Solution NaCl Solution STRIPPING COLUMN STEAM MONOMER- FREE LATEX BUTADIENE-FREE LATEX RECYCLED STYENE LATEX CRUMBS BRINE ACID SLURRY

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion WASHING TANK ROTARY VACUUM FILTER ROTARY VACUUM FILTER CRUMBS WATER CRUMBS

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion CRUMBS CRUMB RUBBER PRESSER DRYER ESBR

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion Styrene Butadiene Water kg/hr kg/hr kg/hr Emulsion Tank kg/ hr solution

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion Polymerization Reactors 60% conversion Recipe for SBR Emulsion Polymerization Butadiene = kg Styrene = kg Water = kg Emulsifier = kg Dodecyl mercaptan = kg Cumene hydroperoxide = kg FeSO 4 = kg EDTA = kg kg Latex

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion Distillation System Latex Emulsion Feed kg of unreacted butadiene kg unreacted styrene kg latex 99.7% Butadiene Recovery Butadiene Recovered D = kg Butadiene-Free Latex La = kg

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion Stripping Tower 80% Styrene Recovery Lb = kg xb = Steam Vb = kg Va = kg ya = La = kg xa = Butadiene-Free Latex Latex (with remaining styrene)

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion Latex Blend Tank kg 21% latex solution kg latex kg water

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion Coagulation Tank F = kg dry solids Wa4 = 5.41 kg water /kg dry solid kg water kg 21% by weight latex solution kg water from latex blend tank kg 3.6% by weight H2SO4 solution kg 15.8% by weight NaCl solution

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion Rotary Vacuum Screen F = kg dry solids/hr Wa2 = kg water /kg dry solid kg water F = kg dry solids Wa4 = 5.41 kg water/kg dry solid kg water Wa5 = kg water /kg dry solid kg water

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion Washing Tank F = kg dry solids Wa1 = kg water /kg dry solid 1984 kg water F = kg dry solid Wa2 = kg water /kg dry solid kg water Wa3 = kg water /kg dry solid 1909 kg water

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion Rotary Vacuum Screen F = kg dry solids Wr = kg water /kg dry solid kg water F = kg dry solids Wa1 = kg water /kg dry solid 1984 kg water Wa1s = kg water /kg dry solid 1786 kg water

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion Crumb Rubber Presser F = kg dry solids W1 = kg water /kg dry solid kg water F = kg dry solids Wr = kg water /kg dry solid kg water Wwc = 1 kg water /kg dry solid kg water

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion Dryer 93 ° F = kg dry solids W1 = kg water/kg dry solid kg water F = kg dry solids/hr W2 = kg water /kg dry solid kg liquid

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion Energy Balance

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion Mixing Tank Water = kg Emulsifier = kg Dodecyl mercaptan = kg Cumene hydroperoxide = kg FeSO 4 = kg EDTA = kg Water = kg Emulsifier = kg Dodecyl mercaptan = kg Cumene hydroperoxide = kg FeSO 4 = kg EDTA = kg 50.5 kW kJ/kg

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion Polymerization Reactor Q = 12,000 Btu/hr

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion Distillation Column Latex Emulsion Feed kg of unreacted butadiene kg unreacted styrene kg latex Butadiene Recovered D = kg Butadiene-Free Latex La = kg Q T = kJ/hr Q T = kJ/hr

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion Stripping Column La = kg xa = Butadiene-Free Latex Lb = kg xb = Latex (with remaining styrene) Steam Vb = kg Va = kg ya = Q T = kJ/hr

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion Latex Blend Tank kg 21% polymer solution 43.2 kW kJ/kg

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion Coagulation Tank kW kJ/kg kg 21% by weight latex solution kg water from latex blend tank kg 3.6% by weight H2SO4 solution kg 15.8% by weight NaCl solution F = kg dry solids Wa4 = 5.41 kg liquid/kg dry solid kg liquid

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion First Rotary Vacuum Filter W s =46, J/kg P = 0.11 kW F = kg dry solids Wa4 = 5.41 kg liquid/kg dry solid kg liquid F = kg dry solids/hr Wa2 = kg liquid/kg dry solid kg liquid Wa5 = kg liquid/kg dry solid kg liquid

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion Washing Tank F = kg dry solid Wa2 = kg liquid/kg dry solid kg liquid F = kg dry solids Wa1 = kg liquid/kg dry solid 1984 kg liquid Wa3 = kg liquid/kg dry solid 1909 kg liquid W s = KJ/kg P= 11.5 kW

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion Second Rotary Vacuum Filter W s =110, J/kg P=0.43 kWC F = kg dry solids Wa1 = kg liquid/kg dry solid 1984 kg liquid F = kg dry solids Wr = kg liquid/kg dry solid kg liquid Wa1s = kg liquid/kg dry solid 1786 kg liquid

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion Crumb Presser F = kg dry solids W1 = kg liquid/kg dry solid kg liquid F = kg dry solids Wr = kg liquid/kg dry solid kg liquid

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion Dryer F = kg dry solids W1 = kg liquid/kg dry solid kg liquid F = kg dry solids/hr W2 = kg liquid/kg dry solid kg liquid P= kW

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion Pumps PumpDescriptionPower Required 1Pump from Water Storage Tank to Mixing Tank P = 0.05 kW 2Pump from Mixing Tank to Polymerization Reactors P = 0.04 kW 3Pump from Reactor to Distillation Column P =0.07 kW 4Pump to the Stripping ColumnP = 0.06 kW 5Pump to the Rotary Vacuum FilterP = 0.13 kW 6Pump for the water in the washing tank P = 0.29 kW 7Pump to the washing tankP = 0.03 kW

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion Heater in the Drier EquipmentPower Required Heater42.76 kW

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion Utility Requirements

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion UtilityDescriptionAmount Deionized water Supplied in the mixing tank Kg/hr Steam supplied in the stripping column Kg/hr Water Supplied in the washing tanks 1909 Kg/hr Air Air supplied in the drier 2285 kg dry air/hr Electricity For all the equipment kW

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion Equipment Design & Material Selection

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion CONTINUOUS STIRRED POLYMERIZATION TANK REACTOR

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion CONTINUOUS STIRRED POLYMERIZATION TANK REACTOR HEURISTICS: 3 equally distanced baffles for better mixing 4-Blade Turbine Agitator

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion SPECIFICATION SHEET EquipmentContinuous Stirred Tank Reactor Number of CSTR8 CSTRs in Series Design Temperature35 °C Design Pressure4.201 atm OrientationVertical ShapeCylindrical with flat top and ellipsoidal bottom Material304 Stainless Steel Tank Diameter m Tank Height m Ellipsoidal Head Length m Cylindrical Wall Thickness mm Flat Head Top Thickness22.63 mm Ellipsoidal Head Bottom Thickness4.378 mm First Inlet Pipe3” Sch 40 Steel Pipe Second Inlet Pipe3” Sch 40 Steel Pipe Third Inlet Pipe3” Sch 40 Steel Pipe Exit Pipe3” Sch 40 Steel Pipe Pump TypeCentrifugal Pumps (all) % Polymerization (Total)60% Residence Time60 minutes (each)

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion CONTINUOUS STIRRED POLYMERIZATION TANK REACTOR Mixer Agitator Type4-Blade Turbine Agitator Number of Impeller1 Impeller Impeller diameter m Distance of impeller from the tank bottom m Baffles Number of baffles3 Baffles Height of a single baffle m Width of a single baffle m Thickness of single baffle5 mm Offset from the bottom of the tank m

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion DISTILLATION COLUMN Wankat, 2011

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion DISTILLATION COLUMN Flash TankVacuum Tank Diameter1.693 m1.051 m Total length5.075 m3.152 m Percentage recovery75.0%99.7% Maximum allowable working pressure psi30.13 psi Maximum allowable working temperature ˚F ˚F Maximum allowable working stress lb/in Material of constructionCarbon steel, A285 Gr A Shell thickness4.610 mm3.229 mm Head thickness9.684 mm5.625 mm Welded joint efficiency 1 (fully radiographed, single welded butt joint) Corrosion allowance2 mm Inlet nozzle1.210 m0.687 m

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion STRIPPING TOWER Sinnot, R.&Towler, G. (2005). Chemical Engineering Design. Oxford: Elsevier Butterworth-Heinemann.

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion STRIPPING TOWER Column Design Column Height4.012 meters Column Diameter0.295 meters Tray Efficiency10% Theoretical Number of stages1 Actual Number of Stages10 Operating Pressure265 mm Hg or atm Operating Temperature70 o C Design Pressure atm Design Temperature97.78 o C Thickness of shell2.418 mm Column headEllipsoidal Head Thickness of head2.418 mm Material of ConstructionCarbon Steel

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion Tray Design Type of TraySieve Tray Weir Height0.5 in Weir Length0.056 meters Tray Thickness5 mm or m Tray Spacing6 in Downcomer Area0.009 m Active Area0.055 meters Hole Area0.006 meters Percent Flooding80% Material of Construction Carbon Steel

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion Rotary Vacuum Filter Tarleton,S. & Wakeman, R. (2006) Filter Media. Solid/Liquid Separation: Equipment Selection and Process Design. Elsevier. p. 88.

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion Rotary Vacuum Screen Heuristics:  P= Pressure drop,  P < 50 kPa t = Cake formation time, t <15 secs rotary vacuum filter speed = 0.2 – 1.0 rpm  t = time consumed of the drum to travel from one segment to another segment, 5 sec d = distance of axis of rotation, 0.5 m

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion Rotary Vacuum Screen First Rotary Vacuum FilterSecond Rotary Vacuum Filter Entering Sludge (kg/hr) Filter Cake (kg/hr) Pressure drop (kPa) 50 Caking time (sec) 15 Total surface area of the drum (m 2 ) Radius of the drum (m) Filtration Area (m 2 ) Thickness of the cake (m) the distance of axis of rotation to the slurry surface (m) 0.5 Number of revolutions (RPM) 11

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion Continuous Hot Air Conveyor Belt Dryer Heuristics: For 24 in wide belt carrying a 3000 ft 3 /hr run at speed 100 ft/min ft/min. Lengths:widths= 20:3 m Over 1 ton/hr of feed

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion Continuous Hot Air Conveyor Belt Dryer Capacity Feed Rate kg/hr Water Evaporation kg H 2 O/hr Minimum Residual Moisture 0.5% Belt Speed m/hr Heat Sources Hot Air 2,285 kg dry air/hr Dryer Dimensions Belt Width 0.9 m Length 6 m Area 5.4 m 2 Materials of Construction Conveyor Belt Stainless steel with high chromium content Dryer Enclosure Stainless steel

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion Storage Tank

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion Mixing Tank

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion Blowdown Tank

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion Washing Tank

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion Crumb rubber presser

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion OPTIMIZATION OF PIPES

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion TOTAL PRODUCT COST & TOTAL CAPITAL INVESTMENT

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion Over-all Raw Materials Cost = Php

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion Total Equipment Cost = Php

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion Total Capital Investment= Php

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion Operating Labor Cost = Php Direct Supervisory and Clerical Labor Cost = Php

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion Total Product Cost = Php Gross Sales = Php

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion MARKET SELLING PRICE & MEASURES OF PROFITABILITY

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion BREAK EVEN POINT SELLING PRICE (BEP SP ) Total Product Cost = PhP 94,977, Annual Production Rate = 1,420, kg/year

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion MARKET SELLING PRICE Current market selling price of imported ESBR for the year 2015: Rubber Statistical Bulletin, January to March 2016 edition

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion MARKET SELLING PRICE 25 % price mark up was added to BEP SP

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion MARKET SELLING PRICE

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion BREAK EVEN POINT SALES VOLUME (BEP SV ) Projected Production Rate = 1,420, kg/year

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion GROSS SALES

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion INCOME

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion Measures of Profitability Return of Investment: 30.45% > MARR = 12 % Annual Equivalent: PhP 13,064, Net Present Value: PhP 68,586, Internal Rate of Return: 34% > 12% (MARR) Payback Period: 2.18 years All present measures of profitability available gave a positive result in terms of profit therefore it is justifiable to proceed with the plant construction.

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion PLANT SITE LOCATION

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion Brgy. San Jose Sico, Batangas City Industrial Port City of CALABARZON 5 hectares of prime property 19 km away from Batangas City Port 25.6 km away from JG summit petrochemicals. SB Elastomers Inc. Plant Site Location

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion Near a stream which is connected to Calumpang River Water rates Php 61.50/cu.m. Fire station is 12 minutes away from the site Meralco power rates Php 9.86/kwh 17 minutes away from the site Plant Site Location SB Elastomers Inc.

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion Easy access on the main road (Gov. Antonio Carpio Road) Coldest month: January Hottest Month: May Low susceptibility to floods and landslides Average:1705 mm Lowest:14 mm (March) Highest:288 mm (July) Plant Site Location

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion Industrial Plant Layout

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion Manufacturing Plant Layout

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion Plant Safety HAZOP Analysis

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion Process Step Study Node Process Parameters Deviation (Guide Words) Possible Causes Possible Consequences Action Required Storage Tanks PumpFlow More The pump and or impeller size is wrong. There will be a possibility that the yield product will be reduced. Verify the pump and impeller size fitted. The set flow rate by the tanker man is too high. There is a potential of filling the tanks faster than the situation can be controlled. Installing flow rate indicators should be considered and terminal operators should be considered to provide an emergency shutdown if necessary. Less The tank level is low. There might be inadequate suction of the material. Alarm level for the storage tank should be installed with the proper level setting.

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion Process Step Study Node Process Parameters Deviation (Guide Words) Possible Causes Possible Consequences Action Required Mixing TankAgitatorsMixing No Stirrer motor malfunction. No mixing possible, accumulation of wasted raw materials. Interlock motor with feed line. Power Failure Feed continues accumulation of wasted raw materials. Feed valve automatically closes when there is power loss. More Power failure due to high motor speed. No mixing possible, accumulation of wasted raw materials. Replacement or maintenance.

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion Process StepStudy Node Process Parameters Deviation (Guide Words) Possible Causes Possible Consequences Action Required Polymerizati on Reactor (CSTR) AgitatorFlowNo Blockage in line. Decrease in production rate. Cleaning of lines. No raw materials in the storage tanks. Level control system. Feed pipe rupture. Maintenance of pipes. Supply pipe rupture. Valve is closed.Automatic valve. Pump is closed.Automatic pump. Problems in raw materials. Decrease in quality of product. Quality control of raw materials and products. Fouling in pipes. Maintenance of pipes.

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion Process StepStudy Node Process Parameters Deviation (Guide Words) Possible Causes Possible Consequences Action Required Polymerizati on Reactor (CSTR) AgitatorFlow More More amount of opening of valve. Explosions.Automatic valves. High recovery of styrene and butadiene. Lower temperature in feed to reactor. Check reactor conditions. Increase of styrene and butadiene to be recovered. Less Less amount of opening of valve. Low production rate.Automatic valves. Low recovery of styrene and butadiene. Higher temperature in feed to reactor. Temperature control at reactor feed preparation.

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion Process StepStudy Node Process Parameters Deviation (Guide Words) Possible Causes Possible Consequences Action Required Polymerizati on Reactor (CSTR) MotorSwitchNo Release spring failure. Accumulation of unreacted materials. Check what caused spring failure. The motor is malfunctioning. Interconnect with feed line. The power supplied failed. In power loss, the feed valve should fail close.

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion Process StepStudy Node Process Parameters Deviation (Guide Words) Possible Causes Possible Consequences Action Required Flash Distillation MotorOperateNo The motor is malfunctioning. There is a possibility of minimal butadiene recovery. A sound alarm should be installed to prevent losses in recovering butadiene. PipeFlow NoPipe is broken. There will be no desired product due to loss of feed. Inspection and maintenance should be scheduled. The specified product is not met. LowPipe is leaked. Material back flow. A check valve should be installed. Off-specification product.

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion Process Step Study Node Process Parameters Deviation (Guide Words) Possible Causes Possible Consequences Action Required Stripping Tower Valve Control No Control valve and controller failed to open. Off-specification product flows in excess. Flow alarm should be added. LowFalsely low reading. Flow to column of off-specification products in excess. For specific application an instrument should be installed.

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion Process Step Study Node Process Parameters Deviation (Guide Words) Possible Causes Possible Consequences Action Required Latex Blend Tank Agitator blade Speed Low The set speed for the conveyor is specified in a falsely slow speed. Uneven distributions of latex blend leading to inconsistent results. Check and adjust the speed of the agitator blade. More The set speed for the conveyor is specified in a falsely fast speed. Final product may become very viscous and cannot meet specifications. Check and adjust the speed of the agitator blade.

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion Process Step Study Node Process Parameters Deviation (Guide Words) Possible Causes Possible Consequences Action Required Emulsion Tank Stirrer Agitation No The motor of the stirrer is malfunctioning. There is the possibility of accumulation of unreacted materials. Interconnect with feed line. The power supplied failed. There is the possibility of accumulation of unreacted materials. In case of power loss, the feed valve should close. More The motor speed is high. There is the possibility of increasing the temperature during the process. Verify the motor speed.

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion Process StepStudy Node Process Parameters Deviation (Guide Words) Possible Causes Possible Consequences Action Required Rotary Filter Filter Drum Rotational Speed No Power failure. Process failure. Manual monitoring. Presence of foreign objects. LowMotor malfunction.Halting of operation. HighMotor malfunction. Over damping of solids/particles. Spillage of fluid and particles. Speed alarm. Drum Cleaning Pump Feed rate NoPump malfunction. Process failure. Manual monitoring. Accumulation of solids/particles on the surface of filter drum. HighPump malfunction.Over spilling. Installation of level sensors.

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion Process StepStudy Node Process Parameters Deviation (Guide Words) Possible Causes Possible Consequences Action Required Rotary Filter Scraper Conveyor Feed rateNo Loss of parts. Accumulation of solid particles on the conveyor. Manual monitoring. Motion malfunction.Over spilling. Vacuum Pump PressureLowPump malfunction. More powerful suction force that attracts particles on the filter drum. Installation of pressure transmitter and controller devices. Particles are harder to scrape. Manual monitoring. Inflation of filter drum.

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion Process StepStudy Node Process Parameters Deviation (Guide Words) Possible Causes Possible Consequences Action Required Rotary Filter Scraper Conveyor Feed rateNo Loss of parts. Accumulation of solid particles on the conveyor. Manual monitoring. Motion malfunction.Over spilling. Vacuum Pump PressureLowPump malfunction. More powerful suction force that attracts particles on the filter drum. Installation of pressure transmitter and controller devices. Particles are harder to scrape. Manual monitoring. Inflation of filter drum.

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion Process Step Study Node Process Parameters Deviation (Guide Words) Possible Causes Possible Consequences Action Required Dryer Conveyor Belt Speed More The set speed for the conveyor is specified in a falsely fast speed. Final product might not be dried to its specification. Inspection of speed. Low The set speed for the conveyor is specified in a falsely slow speed. Final product might be burnt and cannot meet its specification. Inspection of speed. Heater Temperatur e More The set temperature is falsely high. Final product might not be dried to its specification. Inspection of temperature. Low The set temperature is falsely low. Final product might be burnt and cannot meet its specification. Inspection of temperature.

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion Process Control Process and Instrumentation Diagram

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion SB Elastomers Inc. First E-SBR plant to enter the Philippine market Produces E-SBR Grade 1500 Located at Brgy. San Jose Sico, Batangas City, Philippines Has its own waste treatment facility Practices responsible manufacturing practices

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion SB Elastomers Inc. Selling Price = Php per kg Return of Investment: 30.45% > MARR = 12 % Annual Equivalent: PhP 13,064, Net Present Value: PhP 68,586, Internal Rate of Return: 34% > 12% (MARR) Payback Period: 2.18 years

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion Why invest on us? SB Elastomers Inc. is to be the pioneer E-SBR manufacturing plant in the Philippines. The company produces quality rubber products by Filipinos, for Filipinos. More than just a profitable investment, the company provides livelihood and economic growth for the country.

Introduction Review of Related Literature Market Study Process Flow Diagram Material Balance Energy Balance Equipment Design Optimization Economic Analysis Plant Layout and Location Plant Safety HAZOP Process Control Conclusion THANK YOU!