1. 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

2. 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

3. 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

4. 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

5. 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

6. 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

7. 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

8. 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

9. 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

10. 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)

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 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

12. 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

13. 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

14. 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

15. 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

16. 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

17. 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

18. 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

19. 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

20. 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.

21. 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

22. 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

23. 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

24. 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

25. 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

26. 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

27. 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

28. 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

29. 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

30. 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 42.019 kg/hr 126.057 kg/hr 302.536 kg/hr Emulsion Tank 470.612 kg/ hr solution

31. 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 = 159.478 kg Styrene = 53.159 kg Water = 382.747 kg Emulsifier = 10.632 kg Dodecyl mercaptan = 0.425 kg Cumene hydroperoxide = 0.361 kg FeSO 4 = 0.036 kg EDTA = 0.128 kg 364.18 kg Latex

32. 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 63.791 kg of unreacted butadiene 21.264 kg unreacted styrene 364.18 kg latex 99.7% Butadiene Recovery Butadiene Recovered D = 63.791 kg Butadiene-Free Latex La = 385.444 kg

33. 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 = 368.443 kg xb = 0.012 Steam Vb = 116.95 kg Va = 133.961 kg ya = 0.127 La = 385.444 kg xa = 0.055 Butadiene-Free Latex Latex (with remaining styrene)

34. 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 287.87 kg 21% latex solution 364.18 kg latex 29.856 kg water

35. 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 = 138.889 kg dry solids Wa4 = 5.41 kg water /kg dry solid 751.839 kg water 364.18 kg 21% by weight latex solution 29.856 kg water from latex blend tank 375.252 kg 3.6% by weight H2SO4 solution 120.99 kg 15.8% by weight NaCl solution

36. 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 = 138.889 kg dry solids/hr Wa2 = 0.541 kg water /kg dry solid 75.139 kg water F = 138.889 kg dry solids Wa4 = 5.41 kg water/kg dry solid 751.839 kg water Wa5 = 4.869 kg water /kg dry solid 676.251 kg water

37. 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 = 138.889 kg dry solids Wa1 = 14.286 kg water /kg dry solid 1984 kg water F = 138.889 kg dry solid Wa2 = 0.541 kg water /kg dry solid 75.139 kg water Wa3 = 13.745 kg water /kg dry solid 1909 kg water

38. 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 = 138.889 kg dry solids Wr = 1.429 kg water /kg dry solid 198.413 kg water F = 138.889 kg dry solids Wa1 = 14.286 kg water /kg dry solid 1984 kg water Wa1s = 12.857 kg water /kg dry solid 1786 kg water

39. 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 = 138.889 kg dry solids W1 = 0.421 kg water /kg dry solid 59.524 kg water F = 138.889 kg dry solids Wr = 1.429 kg water /kg dry solid 198.413 kg water Wwc = 1 kg water /kg dry solid 138.889 kg water

40. 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 = 138.889 kg dry solids W1 = 0.421 kg water/kg dry solid 59.524 kg water F = 138.889 kg dry solids/hr W2 = 0.005 kg water /kg dry solid 0.698 kg liquid

41. 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

42. 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 = 302.536 kg Emulsifier = 8.404 kg Dodecyl mercaptan = 0.336 kg Cumene hydroperoxide = 0.286 kg FeSO 4 = 0.029 kg EDTA = 0.101 kg Water = 302.536 kg Emulsifier = 8.404 kg Dodecyl mercaptan = 0.336 kg Cumene hydroperoxide = 0.286 kg FeSO 4 = 0.029 kg EDTA = 0.101 kg 50.5 kW 378.93 kJ/kg

43. 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

44. 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 63.791 kg of unreacted butadiene 21.264 kg unreacted styrene 364.18 kg latex Butadiene Recovered D = 63.791 kg Butadiene-Free Latex La = 385.444 kg Q T = 17746.33 kJ/hr Q T = 630.028 kJ/hr

45. 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 = 385.444 kg xa = 0.055 Butadiene-Free Latex Lb = 368.443 kg xb = 0.012 Latex (with remaining styrene) Steam Vb = 116.95 kg Va = 133.961 kg ya = 0.127 Q T = 5893.08 kJ/hr

46. 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 287.87 kg 21% polymer solution 43.2 kW 540.24 kJ/kg

47. 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 66.71 kW 174.598 kJ/kg 364.18 kg 21% by weight latex solution 29.856 kg water from latex blend tank 375.252 kg 3.6% by weight H2SO4 solution 120.99 kg 15.8% by weight NaCl solution F = 138.889 kg dry solids Wa4 = 5.41 kg liquid/kg dry solid 751.839 kg liquid

48. 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 =46,395.87 J/kg P = 0.11 kW F = 138.889 kg dry solids Wa4 = 5.41 kg liquid/kg dry solid 751.839 kg liquid F = 138.889 kg dry solids/hr Wa2 = 0.541 kg liquid/kg dry solid 75.139 kg liquid Wa5 = 4.869 kg liquid/kg dry solid 676.251 kg liquid

49. 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 = 138.889 kg dry solid Wa2 = 0.541 kg liquid/kg dry solid 75.139 kg liquid F = 138.889 kg dry solids Wa1 = 14.286 kg liquid/kg dry solid 1984 kg liquid Wa3 = 13.745 kg liquid/kg dry solid 1909 kg liquid W s = 19.50 KJ/kg P= 11.5 kW

50. 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 =110,576.96 J/kg P=0.43 kWC F = 138.889 kg dry solids Wa1 = 14.286 kg liquid/kg dry solid 1984 kg liquid F = 138.889 kg dry solids Wr = 1.429 kg liquid/kg dry solid 198.413 kg liquid Wa1s = 12.857 kg liquid/kg dry solid 1786 kg liquid

51. 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 = 138.889 kg dry solids W1 = 0.421 kg liquid/kg dry solid 59.524 kg liquid F = 138.889 kg dry solids Wr = 1.429 kg liquid/kg dry solid 198.413 kg liquid

52. 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 = 138.889 kg dry solids W1 = 0.421 kg liquid/kg dry solid 59.524 kg liquid F = 138.889 kg dry solids/hr W2 = 0.005 kg liquid/kg dry solid 0.698 kg liquid P=13.738 kW

53. 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

54. 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

55. 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

56. 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 302.536 Kg/hr Steam supplied in the stripping column 92.422 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 equipment233.618 kW

57. 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

58. 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

59. 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

60. 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 Diameter1.06114 m Tank Height0.79585 m Ellipsoidal Head Length0.26528 m Cylindrical Wall Thickness10.632 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)

61. 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 diameter0.35371 m Distance of impeller from the tank bottom 0.35371 m Baffles Number of baffles3 Baffles Height of a single baffle0.88428 m Width of a single baffle0.088428 m Thickness of single baffle5 mm Offset from the bottom of the tank 0.177 m

62. 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

63. 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

64. 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 39.70 psi30.13 psi Maximum allowable working temperature 61.394 ˚F-9.274 ˚F Maximum allowable working stress 12 900 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

65. 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.

66. 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 0.3487 atm Operating Temperature70 o C Design Pressure2.0494 atm Design Temperature97.78 o C Thickness of shell2.418 mm Column headEllipsoidal Head Thickness of head2.418 mm Material of ConstructionCarbon Steel

67. 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 0.005 m Tray Spacing6 in Downcomer Area0.009 m Active Area0.055 meters Hole Area0.006 meters Percent Flooding80% Material of Construction Carbon Steel

68. 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.

69. 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

70. 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) 890.7282122.889 Filter Cake (kg/hr) 214.028337.293 Pressure drop (kPa) 50 Caking time (sec) 15 Total surface area of the drum (m 2 ) 1.7561.781 Radius of the drum (m) 0.7480.753 Filtration Area (m 2 ) 0.9370.957 Thickness of the cake (m) 0.0370.024 the distance of axis of rotation to the slurry surface (m) 0.5 Number of revolutions (RPM) 11

71. 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 - 600 ft/min. Lengths:widths= 20:3 m Over 1 ton/hr of feed http://www.globalspec.com/SpecSearch/SearchForm/processing_equipment/materials_processing_equipment/process_dryers

72. 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 138.889 kg/hr Water Evaporation 58.826 kg H 2 O/hr Minimum Residual Moisture 0.5% Belt Speed 0.027 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

73. 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

74. 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

75. 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

76. 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

77. 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

78. 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

79. 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

80. 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

81. 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

82. 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 46 469 745.64

83. 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 15 507 934.31

84. 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 77 986 548.57

85. 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 8 225 100.00 Direct Supervisory and Clerical Labor Cost = Php 6 600 00.00

86. 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 94 977 806.44 Gross Sales = Php 102 576 030.95

87. 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

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 BREAK EVEN POINT SELLING PRICE (BEP SP ) Total Product Cost = PhP 94,977,806.44 Annual Production Rate = 1,420,999.20 kg/year

89. 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

90. 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

91. 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

92. 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 = 1,420,999.20 kg/year

93. 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

94. 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

95. 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 13,064,434.35 Net Present Value: PhP 68,586,171.67 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.

96. 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

97. 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

98. 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.

99. 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

100. 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

101. 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

102. 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

103. 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.

104. 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.

105. 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.

106. 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.

107. 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.

108. 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.

109. 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.

110. 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.

111. 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.

112. 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.

113. 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.

114. 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.

115. 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.

116. 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

117. 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

118. 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

119. 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

120. 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

121. 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

122. 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

123. 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

124. 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

125. 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

126. 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

127. 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

128. 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

129. 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

130. 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

131. 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

132. 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

133. 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

134. 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 83.55 per kg Return of Investment: 30.45% > MARR = 12 % Annual Equivalent: PhP 13,064,434.35 Net Present Value: PhP 68,586,171.67 Internal Rate of Return: 34% > 12% (MARR) Payback Period: 2.18 years

135. 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.

136. 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!