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Reliance Industries Limited Financial Presentation

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Reliance Industries Limited - PowerPoint PPT Presentation

Reliance Industries Limited

Ril has achieved high capacity utilisation rates despite weak demand conditions ... high capacity utilisation rates of 107% leading to 14% volume growth from 12.6 ... – powerpoint ppt presentation.

• Strong operational and financial performance achieved in continuing adverse industry environment
• General economic slowdown in India and globally led to weak demand conditions for several of Reliances products
• Focus on high operating rates, specialities, productivity gains, integration and reduction in financial costs have contributed to continued profit growth
• Increase in overall uncertainty in view of the recent global developments
• Global petrochemical margins under pressure during H1
• Leading international petrochemicals companies in US, Europe and Asia have reported weak performances
• Historically low product prices - currently trading 20-50 below 10 year averages
• Uncertain future outlook for margins in view of
• - global demand slowdown
• - continued volatility in feedstock prices
• Capacity utilisation 104
• Production volumes 5.7 mn. tonnes, up 9
• Domestic sales 88 of total sales
• Exports US 328 mn. (Rs.1,569 crores)
• Market shares polyester 53
• intermediates 78
• polymers 50
• H1 Financial Performance
• Lower raw material prices
• Greater focus on speciality products, contributing to higher margins
• Continued focus on cost, productivity and efficiency
• Interest cost savings, owing to prepayment and refinancing
• H1 FY 2001-02 FY 2000-01
• OPM 19.2 17.4
• NPM 14.9 13.2
• ROE 19.6 18.1
• ROCE 18.4 18.0
• EPS - Rs. () 25.1 (0.52) 22.8 (0.49)
• Cash EPS - Rs() 40.6 (0.85) 38.1(0.83)
• excluding FX gains
• H1 FY 2001-02
• EPS - Rs. () 33.6 (0.70)
• Debt Equity 0.72 0.72
• Gearing 44 41
• Interest Cover 3.7x 3.3x
• Total Debt/Cash Flow 2.0x 1.8x
• Reliance is by far the largest exporter in India - manufactured exports of US 1.08 billion (Rs. 5,150 crores) in the first half
• The current exports represent 120 times growth over the annual exports of Rs. 86 crores (US 25 million) just 5 years ago
• Individually too, RIL and RPL are Indias top 2 exporters - still only 12 of RILs and 21 of RPLs sales come from exports
• RILs manufactured exports were US 328 mn (Rs. 1,569 crores) in the first half
• RIL exports products to over 90 countries, including to the most quality conscious customers globally
• Business Review
• RIL is Indias largest private sector EP operator in India, with total acreage of over 175,000 square kms
• Well balanced EP portfolio comprising 25 onshore and offshore, deep and shallow water blocks
• Exploration work progressing well - drilling of first well likely next year
• Exploration capex expected to be Rs. 1,500 - 2,000 crores (US 300 - 400 million) over next 3 years
• Demand slowdown in H1 due to seasonal factors, Diwali timing, inventory drawdown, and lower demand from apparels segment
• Reliance is responding by creating new markets for speciality grades and growing high potential segments
• Increasing focus on polyester grades finding application in segments with higher growth potential such as home furnishings, automobiles, and industrial textiles
• Polyester demand in India likely to grow at double digit rates over the long term - CARG of 15 over last 10 years
• Polymers demand has shown further strong growth of 15 during the first half - on top of 11 growth in FY 2000-01
• Higher relative industry production growth reflects the impact of new industry capacities operating at fuller rates during H1
• Healthy demand growth for RILs polymers during H1
• Demand from high growth user industries like telecom, packaging, food and beverages, consumer durables
• Domestic demand / supply balance is progressively improving with healthy growth
• Reliance Petroleum
• LPG and gasoline continue to register strong demand growth
• Negative growth rates for middle distillates
• RPLs high operating rates despite the domestic demand slowdown reflect
• Integration with groups downstream operations
• Ability to tap exports markets
• Flexibility of product slate
• High capacity utilisation rates of 107 leading to 14 volume growth from 12.6 to 14.4 million tonnes
• Improved product mix to take advantage of niche opportunities
• Import tariff rationalisation in October, 2000, as well as in March and April, 2001, leading to higher effective import tariff differentials
• Stability of earnings through risk management
• Advantageous price setting mechanism for export cargoes
• Ongoing productivity gains and cost reductions
• High complexity - Ability to process heavy and sour varieties of crude oil
• Superior product slate - leading to higher value addition per barrel
• Ability to optimise product mix in response to market conditions
• Favourable location and access to world class infrastructure - leading to lower freight/logistics costs
• World class risk management techniques employed to hedge margins
• Q2 FY2001-02 Q2 FY2000-01
• OPM 9.31 9.34
• NPM 4.86 4.47
• ROE 17.7 23.2
• Annualised EPS - Rs. () 3.34 (0.07) 3.13 (0.07)
• Annualised CEPS - Rs. () 4.90 (0.10) 4.50 (0.10)
• H1 FY2001-02 H1 FY2000-01
• OPM 9.8 9.8
• NPM 5.0 4.7
• ROE 19.5 20.9
• Annualised CEPS - Rs. () 4.90 (0.10) 4.51 (0.10)
• H1 FY2001-02 FY2000-01
• Debt Equity 0.83 0.83
• Gearing 45.1 43.9
• Interest Cover 3.26 2.98
• Total Debt / Cash Flow 2.26 2.95
• RPL is Indias largest exporter with exports of US 1,375 mn (Rs. 6,410 crores) in FY 2001
• H1 exports of RPLs products have increased 67 to US 759 mn (Rs. 3,581crores)
• RPL exported 3.6 million tonnes of products during H1 - Gasoline, HSD, and naphtha were the largest items of exports
• RPLs products have been exported to 14 countries, including to the most quality conscious customers globally
• Capacity increase possible through debottlenceking at marginal cost - capital cost advantage will be further enhanced
• Investments in pipeline infrastructure - will result in smooth evacuation of products and enhanced cost competitiveness
• Evaluating a multi-pronged strategy to enter the business of retail marketing of controlled products in India
• - potential joint ventures and alliances
• - acquisitions of marketing and distribution assets (participating in disinvestment of government owned oil PSU IBP)
• - development of its own distribution and marketing infrastructure
• 54 growth in GSM based cellular subscriber base over last six months as compared to industry growth rate of 34
• Subscriber base has crossed 300,000 mark with services in 118 cities across 15 states
• Leading market shares in most circles
• Pre-paid services account for over 90 of cellular revenues low risk strategy
• Strength of Reliance Mobile brand and expertise in building retail consumer franchise demonstrated
• Won the Kolkata GSM license for Rs. 78 crores (US 16 million) under the fourth cellular license bidding
• Presence in Kolkata circle to offer synergy in operations and marketing efforts in the entire Eastern region
• Acquisition of Kolkata circle to enable superior roaming facilities throughout the region
• Roll out plans being finalised
• National footprint with licences signed for providing fixed line services in 18 circles
• Fixed line licences also enable tapping of mobile segment through WLL services in addition to existing GSM business
• First company to receive National Long Distance (NLD) LOI
• Work on 60,000 route kms, world class IP backbone on schedule project on target for completion by end 2002
• Participating in process for disinvestment of VSNL, Indias monopoly international long distance carrier - ILD services to be opened up to private sector in April, 2002
• Reliance Infocom to be the holding company for all infocom and related businesses of Reliance group
• Reliance Infocom to invest up to Rs. 25,000 crores (US 5 bn) over the next 5 years
• Project proposed to be financed with 21 debtequity
• RIL is the lead investor with 45 equity stake
• Our consistent and transparent policy regarding share buyback
• Rs. 303 not an automatic trigger for buyback
• Share price decline part of global market meltdown
• RIL shares have been outperforming Sensex and other leading stocks over all time frames
• Buyback not a mechanism for providing exit to short term traders / speculators / operators
• Investment of cash flows directed towards highest return investments
• Consistent focus on value creation as operating managers
• Through margin improvement focus on productivity improvements and higher margin products
• Through capital efficiency stretching and sweating existing assets, focus on high returns investment for future growth
• Through financial efficiency - continuous innovation to lower financial costs and reduce the cost of capital
• RIL is on track to deliver more than 11 million tonnes in production volume in the current financial year
• RIL has reported good performance in a very difficult industry environment, reflecting the strength of its cost and market positions, and the success of its business strategies
• Global petrochemicals margins are likely to remain under pressure, owing to the world-wide slowdown in demand
• RILs future investments in oil and gas and infocom are likely to generate attractive returns in the medium to long term

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Reliance Industries Limited

Sep 18, 2014

540 likes | 1.36k Views

Reliance Industries Limited. BUTADIENE EXTRACTION. Sanjay Rinke Dr.G.Padmavati,Vimal Shah,Nitin Pal. Agenda. BASF NMP Process – VMD JSR Acetonitrile Process – HMD Simulation of HMD Process - RTG. BASF NMP PROCESS RELIANCE INDUSTRIES LIMITED VADODARA MANUFACTURING UNIT.

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Reliance Industries Limited BUTADIENE EXTRACTION Sanjay Rinke Dr.G.Padmavati,Vimal Shah,Nitin Pal

Agenda • BASF NMP Process – VMD • JSR Acetonitrile Process – HMD • Simulation of HMD Process - RTG

BASF NMP PROCESS RELIANCE INDUSTRIES LIMITED VADODARA MANUFACTURING UNIT

RIL VMD BD UNIT-OVERVIEW

ADVANTAGES OF BASF NMP PROCESS • BASF Process commercialized since 1968 • Total BASF capacity more than 2000 KMT • High Yields • Higher Butadiene Purity • Ability to process wide variety of feed

ADVANTAGES OF BASF NMP PROCESScontd. • Non corrosive, Non Toxic solvent • Safe plant operation–No acetylene accumulation • Low Energy Consumption • High turndown ratio

FLOW DIAGRAM

BASF NMP PROCESS PERFORMS SEPARATION • Extractive Distillation Butenes, Butanes & C4 Acetylenes have B.P. close to 1,3 Butadiene. Separation is not possible by conventional distillation. However solubility of these components in NMP is very different from 1,3 Butadiene. Therefore separation by extraction distillation. • Conventional Distillation 1,2 Butadiene, Propyne & some C5 HC have high boiling point compared to 1,3 BD. Therefore separation by conventional distillation.

SEPARATION STEPS • Extractive distillation-1 (Separation of C4 Raffinate) • Extractive distillation-2 (Purification of Crude butadiene for separation of Ethyl Acetylene/ Vinyl Acetylene) • Degassing (Solvent Recovery & Removal of VA Stream) • Product Purification (For removal of traces of lighter & Heavier impurities)

PRODUCT QUALITY

RELIABILITY ISSUES • Popcorn formation & fouling in final column overhead condensers • Fouling in degasser column • Final Column PSV line rupture • Prime reason is oxygen initiated polymerization • Higher losses of solvent in acetylene washer wash water stream

MEASURES IMPLEMENTED • Nitriting of system with hot nitrite circulation and monitoring of NO3 conversions. • Oxygen level measurement from the vents of the receiver twice a week • Continuous venting from the condenser dome cover end. • Installation of one spare condenser and changing over at regular frequency of 80-90 days in Final Column • Installation of in line oxygen measurement from the vents (commissioned by Nov 07) • TBC dosing across the shell (at 5 locations) and in the vapor line to the condenser for oxygen scavenging.

JSR ACETONITRILE PROCESS RELIANCE INDUSTRIES LIMITED HAZIRA MANUFACTURING DIVISION

RIL HMD BD UNIT-OVERVIEW PRODUCT : 1,3-BUTADIENE (99.5% pure) CAPACITY : 140 KTA LICENSOR : JSR, Japan BASIC ENGINEERING : JSR, Japan DETAILED ENGINEERING : Toyo Engineering India YEAR OF COMMISSIONING : 2005 PLANT INSTALLATION TIME : 16 MONTHS Winner of International Project Management Award

Design Considerations • Designed to process the Mix C4 from In house Cracker Plant & Imported Mix-C4 • Case 1 : High severity operation - 1,3BD (54%) • Case 2 : Low severity operation - 1,3BD (44%) • BD recovery : Case1- 98% / Case2- 98.9% • Solvent used : Acetonitrile • Selectivity :VA>EA>1,2BD>MA>C5+> 1,3BD>cis-Butene>n- Butene> t- Butene>C3

Critical to Safety Operation • Build up of MA > 50 wt% explosive decomposition, alarm, TALO trip to purge the stream to flare • Build up EA + VA > 45 wt% explosive decomposition, alarm, low diluents flow trip • Build up of 1,2 BD > 50 wt% decomposition takes place.Temp cascade control with bottoms with drawl and hard wired alarm provided.

Butanes + Butenes Solvent Water Topping Column EDC No.1U C4 Feed BB Washer BD Washer Solvent + water Butadiene Product Water EDC No.1L Tailing Column Solvent Water + HCs EDC No.2 1,2BD + C5+ & 1,3BD (traces) C4s Acetylenes + B & B Solvent Stripper Water Washer Column Side Cut Column B & B Diluents Water + Solvent Lean Solvent Process Flow Diagram

C4 Hydrocarbon Balance

NO:1 EDC COLUMN (UPPER) ANALYER – 51002 FOR 1-3 BD & OTHERS E –5103 ANALYZER 510001 FOR 1-3 BD, EA, VA, & MA V –5101 Butane & Butene BB Washer C -5101

NO:1 EDC COLUMN (LOWER) ANALYZER – 51005 FOR MA & 1-2 BD C –5102

NO:2 EDC COLUMN ANALYZER – 51004 FOR MA,VA & EA C –5103

SOLVENT STRIPPER C –5104

SIDE CUT COLUMNSIDE CUT WASHER E –5110 E –5111 E –5112 V –5102 ANALYZER – 51003 FOR EA & VA C –5105 C –5106

V –5106 LP-FLARE OWS PH Analyzer ACN 62.52%, H2O 28.84%,ETOH 8.64% BB-W 94 Deg C TO E - 5112 E –5122 SCC-W CWS V –5110 E –5126 E –5121 V –5107 BB-W V-5105 TO C-5104 BOTTOM V-5104 V-5101 E –5124 E –5123 114 Deg C SOL. From SCC-W LP-Steam CAUSTIC V-5117 V-5109 C –5110

WATER CIRCULATION LOOP CWR TO V – 5118 LP - FLARE 8 MT/hr E – 5126 4 MT/hr CWS 30 25 TO E – 5112 V - 5110 13 MT/hr SCN 25 19 BB-W C - 5109 SSC-W C - 5106 V - 5106 BD-W C - 5111 25 E - 5121 A/B 21 1 1 FROM E-5112 FROM V-5101 1 FROM V-5104 SRC C - 5110 V-5101 Boot V-5104 Boot 1 V-5105 Boot 25 MT/hr

SOLVENT LOOP C - 5104 SDN TBC 88.6 Deg C E –5105 E –5106 E –5107 A/B E –5123 110 Deg C 97.3 Deg C 126 Deg C 138 Deg C FROM C - 5110 E –5115 E –5117 E –5114 50 Deg C E –5102 A/B E –5127 73 Deg C 70 Deg C 78 Deg C 58.7Deg C DENSITY ANALYZER TO C-5109 TO C - 5103 TO C - 5101

Process & Quality Control • Butadiene Process Controls and Quality Control systems are well established. • Strong on-line and off-line Quality control system is followed to ensure that customer gets the right material. • Logistics systems are designed to ensure on-time and reliable supplies. Proper tracking methodologies are set. • Fully equipped QC & QA set-up available. • All the parameters are checked for conformance to specification and certification is done through COA. Labs are accredited to ISO:17025:2005 • Well defined customer feedback/ complaint management procedures exists for improving QA systems.

SIMULATION OF ACETONITRILE PROCESS RELIANCE INDUSTRIES LIMITED CEPD GROUP-RTG VMD

Butanes + Butenes MA & other C4s Solvent Water Topping Column EDC No.1U C4 Feed BB Washer BD Washer Tear1 Butadiene Product Tear4 Water EDC No.1L Tailing Column Tear2 Solvent Water + HCs Solvent Tear3 EDC No.2 1,2BD + C5+ & 1,3BD (traces) C4s Acetylenes + B & B Solvent Stripper Water Solvent recovery column Washer Column Side Cut Column B & B Diluents Water + Solvent Lean Solvent Waste water Simulation of BD Process

Thermodynamics • Selection of VLE model is crucial for BD ED simulation • UNIFAC Activity coefficient model used for all columns • UNIFAC-LBY Activity coefficient model used for Topping column simulation • ASPEN Plus 10.2 version used for simulations • To use latest ASPEN plus v7.0 pure component properties are to be updated by user • NRTL, WILSON, UNIQUAC Activity coefficients are not supporting well

Comparison of Design and Simulation Temperatures RadFrac (rigorous distilaltion for two & three pahse fractionation) Aspen Plus module used for simulation

EDC-1 Upper Column Simulation Results U/B L/D Reflux ratio is provided as input for simulation

EDC-1 Upper Column Simulation Results Solvent D/V C4 Feed D/L Columns converged without any errors

EDC-1 Lower Column Simulation Results SC/V B/L 1-3 BD flow in bottom six trays is found to be very sensitive to temperature 2C difference in temperature results in major difference in BD flow.

Solvent Stripper Simulation Results D/V B/L

Solvent Stripper Simulation Results To C-5106 SC/V R/L 1,2-Buatdiene stripping observed to be difficult

EDC2 Column Simulation Results D/V B/L C5 heavier is considered as n-pentane in simulations

Tailing Column Simulation Results D/L SC/L B/L

Topping Column Simulation Results D Excellent matching between simulation & design values Thermodynamics: UNIFAC-LBY From BD washer top

Solvent Recovery Column Simulation Results D Simulation results and design results matched very well Opportunity for reflux ratio optimization observed B

Observations • ASPEN Plus RadFrac module is used for simulation of all the columns • Used default value for efficiency • Considered four tear streams from EDCU, EDCL, EDC2 & solvent stripper • EDC1U, tailing, topping & solvent recovery columns design reflux is provided as input • In solvent recovery column opportunity for reflux ratio optimization noticed • EDC1L Bottom 6 trays flow is found to be very sensitive to change in temperatures. 2ºC difference in temperature resulted in major difference in 1,3 BD flow

Conclusion • UNIFAC Thermodynamic activity coefficient model seems to simulate the process reasonably well • The simulations are to be done for the actual plant conditions to conclude the effectiveness of the UNIFAC model for the system & optimization

GROWTH IS LIFE THANK YOU

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Reliance Industries Ltd.

NSE: RELIANCE | BSE: 500325

2999.95 3.70 ( 0.12 %)

35.11% Gain from 52W Low

5.2M NSE+BSE Volume

NSE 23 Aug, 2024 3:31 PM (IST)

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Market Leader

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Net Profit Margin TTM %

Revenue Growth (TTM)

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Net Profit TTM Growth %

Below industry Median

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