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Refinery & Petrochemical Integration- An IOCL Perspective

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Refinery & Petrochemical Integration- An IOCL Perspective Presented by : Brij Behari Chief General Manager(Technical) Indian Oil Corporation Ltd Refinery Olefins Aromatics
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Page 1: Refinery & Petrochemical Integration- An IOCL Perspective

Refinery & Petrochemical Integration-

An IOCL Perspective

Presented by :

Brij Behari

Chief General Manager(Technical)

Indian Oil Corporation Ltd

Refinery

Olefins

Aromatics

Page 2: Refinery & Petrochemical Integration- An IOCL Perspective

Source: Argus

Volatility in Crude Oil Prices

104.81

86.65

53.49

107.63

87.40

53.99

105.62

86.83

53.63

25.00

35.00

45.00

55.00

65.00

75.00

85.00

95.00

105.00

115.00

AP

R'1

4

JUN

'14

AU

G'1

4

OC

T'1

4

DEC

'14

FEB

'15

AP

R'1

5

JUN

'15

AU

G'1

5

OC

T'1

5

DEC

'15

FEB

'16

AP

R'1

6

JUN

'16

AU

G'1

6

OC

T'1

6

DEC

'16

FEB

'17

13

AP

R'1

7

Dubai+Oman BRENT(DATED) Indian Basket

Page 3: Refinery & Petrochemical Integration- An IOCL Perspective

Integration reduces Risk

The integrated downstream supply chain provides more options and inherent flexibility to optimize not only crude-mix but also each stream of entire supply chain to fetch higher value depending upon prevailing supply demand situation and pricing in domestic and international market.

Page 4: Refinery & Petrochemical Integration- An IOCL Perspective

Petrochemicals have proven to be financially attractive for the multinational integrated oil majors

Page 5: Refinery & Petrochemical Integration- An IOCL Perspective

Value Addition through Integration

14% 11%

70%

85%77%

0%

10%

20%

30%

40%

50%

60%

70%

80%

90%

Crude Refining Linera AlkylBenzene

Paraxylene/PTA Naphtha Cracker TotalPetrochemicals

Typical Value addition over the cost of raw material (%)

Page 6: Refinery & Petrochemical Integration- An IOCL Perspective

Value Addition

Petrochemical offer one of the highest value additions in manufacturing sector

Source: Report of the Sub-group on Petrochemicals for the 12th 5-yr Plan

Page 7: Refinery & Petrochemical Integration- An IOCL Perspective

Kerosene

PropyleneCracked LPG

Refinery

Naphtha

Gasoline

Fertilizer

Power Plant

EthylenePropylene C4’s

N-Paraffins

Fuel

Aromatic Naphtha

Paraffinic Naphtha

Fuel

Options for PetroChemicals

Page 8: Refinery & Petrochemical Integration- An IOCL Perspective

IOCL Experience

Page 9: Refinery & Petrochemical Integration- An IOCL Perspective

9

Panipat Naphtha Cracker

Source: IOCL

Page 10: Refinery & Petrochemical Integration- An IOCL Perspective

Key Integration Drivers / Push & Pull FactorsPush Factors:

1. Low demand growth globally for refined products with hybrid and energy efficient vehicles

2. Transition from Fossil Fuels to Renewables

3. Carbon Foot-Print minimization

4. Low refinery capacity utilization globally.

Pull Factors

1. Low cost Feed: Surplus Naphtha feedstock availability-Low transportation Cost. More consumption of RLNG and sparing of Naphtha.

2. Leveraging Refinery Intermediate streams as advantage feed to Petrochemical complex

3. Blending of Petrochemical By-Products into refinery fuel products leading to lower cost of conversion

4. Utilities: Significant Cost reduction in Shared Utilities & Infrastructure

5. Shared Services: Engineering, Maint., Procurement, Laboratory, HSE, Security, HR, Admin, IS etc.

> Higher Cash Margins

Page 11: Refinery & Petrochemical Integration- An IOCL Perspective

Key Integration Drivers…cont’d

> Using existing strengths in refining, marketing & supply chain

> More flexibility in reprocessing, storing and transporting off specification products

> Energy savings in well-integrated hydrocarbon processes

> Feedstock flexibility to capitalize on available low cost crude oils and intermediates

> Independence of feed stocks and supply security.

Page 12: Refinery & Petrochemical Integration- An IOCL Perspective

Value Addition by Return Streams to Refinery

> C4: After extracting Butadiene, balance Stream exported for added LPG Production

> C5-C6: routing to Refinery

Non-aromatic Streams shared with refinery for MS Maximization

Additional Naphtha Processing capability of Cracker(~ 7%)

Value addition: 35-40 million USD/yr

> C7-C8: for PX yield enhancement & MS Octane Boosting

C7-C8 is split into C7 & C8 (About 70:30 ratio).

Potential value addition: 5-10 million USD/yr.

12

Page 13: Refinery & Petrochemical Integration- An IOCL Perspective

Value Addition by Return Streams to Refinery…2

> C9+ for Enhancement of Diesel pool

Majority absortion in Diesel pool & partially to MS with Reformate sharing with Other refineries

Value addition: 4-5 million USD/year.

> PFO for -Low Sulphur Fuel Oil

Cutter Stock to maintain Low-Sulphur Specs in IFO

> Acid Gases ex NCU

Sharing of Refinery’s SRU infrastructure

Page 14: Refinery & Petrochemical Integration- An IOCL Perspective

Exploiting Low Cost Olefin stream from Refinery

> C2 Stream

Ethylene Maximization: Extracting C2 from FCC/Coker/Indalin Offgas

> C3 Stream

Maximizing Propylene from Captive Refinery’s FCC using advanced catalysts(ZSM-5)

Supplemental Propylene Generation from Coker LPG

Saturating Poly-Propylene capacity using Orphan Propylene from other Standalone Refinery

> Hydrogen Stream Sharing with Refinery

2-way sharing increases Operation flexibility

Page 15: Refinery & Petrochemical Integration- An IOCL Perspective

Aromatics-Refinery Integration

> Streams to Hydrogen Grid

Platformer – PSA Product hydrogen

Tatoray Separator Off Gas-CRU (80% H2)

> Streams to Diesel Pool

HA Colum Bottoms

Oxygen Stripper Net Overhead

NHT Stripper Overhead

Page 16: Refinery & Petrochemical Integration- An IOCL Perspective

Aromatics-Refinery Integration

> Streams to MS Pool

Reformate and Tatoray feed Tank ( C7/ C9 Str )

> Streams to LPG Pool

LPG from Platformer

> Streams to Naphtha Pool

SSU ( Shell Sulpholane unit ) Raffinate to Naphtha blending

> Future Streams

C9 Stream from PNC PGHU to PX-Feed Naphtha

Page 17: Refinery & Petrochemical Integration- An IOCL Perspective

> Cheap Ethylene from Gas Crackers

> Cheap Shale Gas Crackers switching Feed

> On-purpose Propylene technologies PDH, OCT, MTO

> Value Addition by Integration

> Liquid Streams(e.g Butadiene, Styrene etc)hold key to incremental profits

> Maximize Propylene potential

Naphtha Cracker Strengths

Challenges faced by Naphtha Crackers

Page 18: Refinery & Petrochemical Integration- An IOCL Perspective

Huge Olefin Deficit Capacity Additions

Page 19: Refinery & Petrochemical Integration- An IOCL Perspective

Way Ahead for IOCL

Expanding Existing PetChem Assets

• 800 to 1147 kta NCU revamp

• 300 to 425 kta MEG Revamp at Panipat

• 553 to 700 kta PTA revamp at Panipat Refinery

• 120 to 162 kta LAB revamp at KoyaliRefinery

• FCC-Indmax revamp(s) at Refinery locations

Greenfield PetChem Projects

• 680 kta PP Plant at Paradip

• 335 kta MEG Plant at Paradip

• Olefin Recovery from Refinery OffGas

• Oxo-Alcohol Complex based on 150 ktaButly Acrylate plant at Gujarat

• Styrene Recovery Project at Panipat

• Proposed PP at Barauni

• 60 MMT-West Coast Integrated Refinery & Petrochemical Complex

Page 20: Refinery & Petrochemical Integration- An IOCL Perspective

In conclusion

> Integrating Petrochemicals with Refineries offers attractive benefits Better realization from value added products

Mitigate the effects of volatile oil prices and highly competitive refining business.

Provides earnings Stability across the value chain

> Crackers esp. Naphtha Based provide opportunity to tap a host of high-value Liquid Streams

> The petrochemical Synergy with refinery is a win-win by way of Definite value addition for both refinery and petrochemical operations

Enhanced overall profitability of the complex

Page 21: Refinery & Petrochemical Integration- An IOCL Perspective

THANK YOU !


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