The country's second refinery, the Barauni Refinery, was commissioned in July 1964 , with a refining capacity of 1 million metric tonnes per annum (MMTPA) to process Assam (Naharkatiya) crude oil. In 2002, the refinery capacity was revamped to 6.0 MMTPA, with secondary processing facilities such as the Hydrogen Generation Unit (HGU-1), Residue Fluidized Catalytic Cracker Unit (RFCCU), and Sulphur Recovery Unit (SRU) as part of technological advancements.
Indian Oil Corporation Limited has awarded iFluids Engineering to carry out SIL Verification for the identified SIF loops & Preparation of Safety Requirement Specification SRS for Barauni Refinery.
SIL Verification study is the process of calculating the average probability of failure on demand (or the probability of failure per hour) and architectural constraints for a safety function design to see if it meets the required SIL.
Software Requirements Specification (SRS) is a document that describes what the software will do and how it should perform.
The software to be used is exSILentia.
Project to be completed within 6 months from the date of site Handover
GAIL (India) Limited awarded iFluids Engineering to carry out Quantitative and Qualitative Risk Assessment (QRA) study for their 278 km long Cross country Pipeline in Cauvery Basin. The scope of study is to systematically identify the potential hazards associated with GAIL pipelines, respective terminals and SV stations through risk assessment methodologies.
Brief on Client and the Location-specific details
GAIL (India) Limited was incorporated in August 1984 as a Central Public Sector Undertaking (PSU) under the Ministry of Petroleum & Natural Gas. It is the largest state-owned natural gas processing & distribution company.
Pipeline Specification details and what it transports
LIST OF STATION/INSTALLATIONS (RISK ANALYSIS) AT CB PIPE LINE NETWORK
|Sl No||Station Name||Location||Gas Supplier Name|
|1||NANNILAM GCS||NANNILAM GCS||ONGC|
|2||KAMALAPURAM GCS||KAMALAPURAM GCS||ONGC|
|3||ADIYAKKAMANGALAM GCS||ADIYAKKAMANGALAM GCS||ONGC|
|4||TIRUVARUR EPS||TIRUVARUR EPS||ONGC|
|5||NARIMANAM GCS||NARIMANAM GCS||ONGC|
|6||NALLUR EPS||NALLUR EPS||ONGC|
|7||KUTHALAM GCS||KUTHALAM GCS||ONGC|
|8||AKM – MEMATHUR||AKM – MEMATHUR||ONGC & HOEC|
|9||RAMNAD (VALANTHARAVAI) GCS||RAMNAD (VALANTHARAVAI) GCS||ONGC|
|10||BHUVANAGIRI GAS DESPATCH TERMINAL - ONGCL||BHUVANAGIRI GAS DESPATCH TERMINAL - ONGCL||ONGC|
|Sl No||Station Name||Location||Maintenance Base|
|Sl No||RT/CT||Maintenance Base|
|1||CHENNAI PETROLEUM CORPORATION||Narimanam|
|2||KIRAN SILICATE (P) LTD||Narimanam|
|3||NANNILAM SILICATE (P) LTD||Narimanam|
|4||EZHIL CHEMICALS (P) LTD||Narimanam|
|5||SUNDRISE SILICATE (P) LTD||Narimanam|
|6||MADRAS CHEMICALS (BOOTH)||Narimanam|
|7||REENA SILICATE IND. (P) LTD||Narimanam|
|8||SREE JAYADEVI INDUSTRIES||Narimanam|
|9||PREM CHEMICAL INDUSTRIES||Narimanam|
|10||PONDY CHEM (P) LTD||Narimanam|
|12||HENKEL SPIC INDIA LTD||Narimanam|
|14||KOTHAVARI SUGARS & CHEM. LTD||Narimanam|
|16||BOSS PROFILES LIMITED||Narimanam|
|17||REGENCY CERAMICS LIMITED||Narimanam|
|18||SOUNDARARAJA COTTON MILLS||Narimanam|
|21||GODREJ SARA LEE, TIRUNALLAR||Narimanam|
|22||ADITYA FERRO ALLOYS||Narimanam|
|26||GODREJ SARA LEE, NEDUNGADU||Narimanam|
|28||PONDICHERRY POWER CORP. LTD||Narimanam|
|35||SOUTH INDIA EDIBLE OIL PVT.LTD||Adiyakamangalam|
|42||KAVERI GAS POWER||Kuthalam|
|46||ARKAY ENERGY (RAMESWARAM)||Ramnad|
|47||SAI REGENCY POWER CORP.||Ramnad|
|48||NEYCER TERMINAL (VADALUR)||Bhuvanagiri|
What is Quantitative Risk Assessment?
Quantitative Risk Assessment is a systematic approach to spot hazards, evaluate the danger & include appropriate measures to manage and mitigate risk for any work process or activity, In this method, the evaluated/estimated risk is quantified numerically.
What is Qualitative Risk Assessment?
Qualitative Risk Analysis involves identifying threats (or opportunities), how likely they're to happen, and therefore the potential impacts. Qualitative Risk Assessment is administered by Risk Index Method. In this method, the evaluated/estimated risk is described in words (Low, Medium and High as per the danger assessment criteria).
Risk Index Method
The risk factor is an important parameter that determines the ways to develop a Risk Assessment model, using either a data first or a frame first model. Since pipelines usually go across many regions whose conditions vary significantly, it is important to have a complete and universally accepted list of factors that can be used to build a risk assessment model. Risk assessment model parameters viz. Third-Party, Corrosion, Design, and Incorrect Operation would then be summed up and multiplied by the leaked impact (based on Product Hazard, Dispersion, Leak volume, and Receptors) shall be used for assessment of the pipeline integrity
Why Risk Assessment is carried out for pipelines?
Risk Assessment of the pipelines is conducted to identify the location-specific events or conditions, or combination of events and conditions that could lead to loss of pipeline integrity, and provides an understanding of the likelihood and consequences of these events.
This identification of location-specific risks were carried out in consultation with GAIL after analyzing the data like Pipeline routing drawings, mechanical data, CP (Cathodic Protection) data, construction details, historic leak /rupture data, O&M philosophy etc. Which was provided by GAIL. These risks shall be rated as Low, Medium and High as per the risk assessment criteria.
PNGRB guidelines represent 22 root causes for the threat to pipeline integrity. One of the cases reported by the operator is "unknown". The remaining 21 threats have been classified into three groups based on time dependency and further into nine categories of related failure types according to their nature and growth characteristic as shown below
Time Dependent threat
1. External Corrossion
2. Internal Corrosion
3. Stress Corrosion
4.Defective pipe seam
6. Defective pipe girth weld
7. Defective fabrication weld
8. Wrinkle bend or buckle
9. Stripped threads /broken pipe /coupling failure
10. Gasket O-ring failure
11. Control/relief equipment malfunction
12. Seal pump packing failure
Time Independent Threats
14.Damage inflicted by first, second or third party (instantaneous /immediate failure)
15. Previously damaged pipe (delayed failure mode)
17. Rat bites
18. Electric Arching 19. Weather related and outside force
20. Earth Movements
21. Incorrect operational procedure
Risk Assessment Methodology
The Risk Assessment Study includes the following steps:
How to evaluate the residual life to minimize failures and sustain pipeline operations.?
Following test methods as per OISD -SOP- Integrity assessment of Petroleum and Natural Gas Pipelines should be performed for pipelines crossing 25 years of design life to assess the health of the pipeline :
DNGVL PHAST SAFETI 8.22
The Recommendation is done as per the OISD Standards and best Engineering practices
Indian Oil Corporation Limited has awarded iFluids Engineering to carry "FIRE WATER ADEQUACY STUDY NETWORK AND ASSOCIATED FACILITIES AS PER OISD-STD-116 FOR BONGAIGAON REFINERY"
Bongaigaon Refinery is a petroleum refinery in Assam, India. It was commissioned on 20 February 1974 by the government of India.Refinery capacity was increased in 1995 to 2.35 million tonnes per year (51400 barrels per day of stream through expansion.
The study is performed for checking the adequacy of the existing fire, water network and identify their limitations while considering different combinations of the fire scenarios (as per OISD-STD-1116 ).
Existing facilities to be covered under this study are:
Upcoming new facilities to be cover under the study are:
Indian Oil Corporation Limited (IOCL) has awarded iFluids Engineering to carry out Safety Integrity Level (SIL) Assessment for the process units of Gujarat refinery. The Gujarat Oil Refinery is located at Koyali, Vadodara District in Gujarat. It is the second largest and one of the most complex refineries in India.
Gujarat Refinery has about 40 operating units with a present capacity of 13.7 MMT per year and is gearing up for further expansion across an area of 148 acres.The refinery was commissioned in the year 1965.
Below are the list of process units that will be covered under this study.