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What should the holder do if the Holder department ceases to exist?
What should the holder do if the Holder department ceases to exist?
The holder shall return the controlled copy to the Head of Department (HOD).
What happens after a total of 20 revisions or a major change in process to the manual?
What happens after a total of 20 revisions or a major change in process to the manual?
The manual will be re-issued, and the revision numbers of all chapters will reset to 00.
What is the document number and revision number of the operating manual?
What is the document number and revision number of the operating manual?
The document number is OPT/01/KHDS/01 and the revision number is 02.
What major amendment was noted on the amendment sheet regarding control valve hunting?
What major amendment was noted on the amendment sheet regarding control valve hunting?
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What specific valve set points were changed according to the amendments?
What specific valve set points were changed according to the amendments?
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When was the last amendment date recorded in the document?
When was the last amendment date recorded in the document?
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What kind of policy was updated in the last amendment?
What kind of policy was updated in the last amendment?
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What is covered in section 6.5 of the operating manual?
What is covered in section 6.5 of the operating manual?
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What are the two types of shutdowns mentioned in section 7.1?
What are the two types of shutdowns mentioned in section 7.1?
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What is the purpose of the reaction section leak test in section 5.4?
What is the purpose of the reaction section leak test in section 5.4?
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What is the focus of section 5.6 in the operating manual?
What is the focus of section 5.6 in the operating manual?
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In section 7.2, what is necessary for restarting the unit after a shutdown?
In section 7.2, what is necessary for restarting the unit after a shutdown?
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What does section 6.1 summarize in the operating manual?
What does section 6.1 summarize in the operating manual?
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What is the first step in the chronology of start-up operations as per section 5.2?
What is the first step in the chronology of start-up operations as per section 5.2?
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What does section 5.7 involve regarding the stripper and naphtha stabilizer?
What does section 5.7 involve regarding the stripper and naphtha stabilizer?
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What is emphasized in section 6.4 regarding the reaction section?
What is emphasized in section 6.4 regarding the reaction section?
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What is the maximum allowable value of sulphur content in hydrotreated kerosene according to the specifications?
What is the maximum allowable value of sulphur content in hydrotreated kerosene according to the specifications?
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What is the specific gravity specification for hydrotreated kerosene and how does it compare with the provided cases?
What is the specific gravity specification for hydrotreated kerosene and how does it compare with the provided cases?
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According to the specifications, what is the freezing point limit for hydrotreated kerosene?
According to the specifications, what is the freezing point limit for hydrotreated kerosene?
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In the specifications, what is the maximum volume percentage for total aromatics in hydrotreated kerosene?
In the specifications, what is the maximum volume percentage for total aromatics in hydrotreated kerosene?
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What is the ASTM D86 boiling point specification for hydrotreated kerosene at the 50% volume point?
What is the ASTM D86 boiling point specification for hydrotreated kerosene at the 50% volume point?
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What is the designed on-stream factor for the unit in hours per annum?
What is the designed on-stream factor for the unit in hours per annum?
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What is the minimum operating cycle recommended for the unit?
What is the minimum operating cycle recommended for the unit?
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How many days of design feedstock can the unit process in three years?
How many days of design feedstock can the unit process in three years?
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At what percentage of design capacity can the unit operate while maintaining on-specification products?
At what percentage of design capacity can the unit operate while maintaining on-specification products?
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What is the design flow rate for the KHDS feed in TPH?
What is the design flow rate for the KHDS feed in TPH?
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How long can the unit ideally operate continuously at 100% capacity?
How long can the unit ideally operate continuously at 100% capacity?
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What should be the condition of products produced when the unit operates at turndown capacity?
What should be the condition of products produced when the unit operates at turndown capacity?
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What document outlines the operating manual for the Kerosene Hydrodesulfurization unit?
What document outlines the operating manual for the Kerosene Hydrodesulfurization unit?
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What is the purpose of the design and engineering practices advised for the unit?
What is the purpose of the design and engineering practices advised for the unit?
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When was the last revision date noted for the operating manual of the unit?
When was the last revision date noted for the operating manual of the unit?
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What is the purpose of the operating manual for the Kerosene Hydrodesulphurization unit?
What is the purpose of the operating manual for the Kerosene Hydrodesulphurization unit?
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What does 'Management of Change' refer to in the context of this operating manual?
What does 'Management of Change' refer to in the context of this operating manual?
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How many pages are listed in the table of contents for the Kerosene Hydrodesulphurization operating manual?
How many pages are listed in the table of contents for the Kerosene Hydrodesulphurization operating manual?
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What is the issue date of the operating manual for the Kerosene Hydrodesulphurization unit?
What is the issue date of the operating manual for the Kerosene Hydrodesulphurization unit?
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Which annexure contains the format for panel engineer validation?
Which annexure contains the format for panel engineer validation?
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What is the revision number listed for the operating manual?
What is the revision number listed for the operating manual?
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What kind of recommendations may be included in Annexure B?
What kind of recommendations may be included in Annexure B?
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What does the abbreviation 'SIC' stand for in Annexure C?
What does the abbreviation 'SIC' stand for in Annexure C?
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What does the term 'operating manual' generally imply in industrial settings?
What does the term 'operating manual' generally imply in industrial settings?
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What is the significance of having separate formats for different engineers’ validations?
What is the significance of having separate formats for different engineers’ validations?
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Study Notes
Operating Manual Revisions and Procedures
- Revision Control: If there are 20 revisions or major process changes, the manual is re-issued, resetting all chapter revisions to 00.
- Holder Responsibility: If the Holder department ceases to exist, the controlled copy is returned to the HOD.
- Manual Information: The provided text is part of an operating manual for a Kerosene Hydrodesulphurization unit (OPT/01/KHDS/01), currently on Issue 02, Revision 02 (dated 01.07.2022 and 10.07.2023). The manual has many chapters and annexures.
Specific Amendments
- Amendment 1 (01/07/2022): New issue released after merger with BPCL. Included RO installation provisions.
- Amendment 2 (31/03/2023): Added isolation valve in makeup kerosene to avoid hunting of control valve, and further isolation valve in makeup Kerosene to ASA vessel line for batch preparation. Altered set points for UV valves (17UV1821A/B) from 70% to 40% opening and 30% to 20% closing.
- Amendment 3 (10/07/2023): Updated QEHS and Energy policies.
Operating Manual Contents (Examples)
- Table of Contents: Includes sections on start-up operations, pressurization, leak tests, catalyst treatment, capacity increasing, normal operation, process control, troubleshooting, and shutdown/restart procedures.
- Chapter 6 - Normal Operating Procedure: Details the normal unit operation, operating parameters summary, process control philosophy, operating parameter adjustments, troubleshooting, and alarm/trip settings.
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Chapter 7 - Normal Shutdown and Restart: Provides detailed procedures for shutdown, and also restarts for short-term and long-term shutdowns, maintenance, inspection, and catalyst unloading circumstances.
- Includes numerous specific restart instructions based on shutdown duration.
- Annexures: Include forms for panel engineer, area engineer, and SIC validations along with related recommendations.
- Management of Change: Included within the manual as a specific annexure.
Specific Equipment Operations (Examples)
- Positive Displacement Pumps: Start-up tasks include checking mechanical jobs, oil flushing, strainer check, alignment, verifying motor rotation, adjusting stroke, monitoring pump parameters, and handling dry-run and backflow avoidance by bleeding.
- Shutdown Procedures: Specific order for pumps, including steps to stop the pump, close valves, and drain liquid for maintenance (if necessary). Troubleshooting includes checking suction/discharge pressure issues and mechanical seal leakage.
Unit Design and Operation
- On-Stream Factor: The unit is designed for 8000 operating hours per year.
- Turnarounds: Minimum 3-year operating cycles between shutdowns.
- Turndown Capability: Can operate at 40% of design capacity for making products.
- Feed Specifications: Provides table about design flow rate (75.6 TPH) for product SR Kerosene.
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Product Specifications: Detailed product specification tables for hydrotreated kerosene, including specifications like:
- Specific gravity
- ASTM D86 vol% figures
- RVP, TVP
- Sulphur
- Freezing point
- Smoke point
- Color
- Cetane Index
- Total Aromatics
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Description
This quiz covers the revisions and specific amendments to the Operating Manual for the Kerosene Hydrodesulphurization unit. It includes details about revision control, holder responsibilities, and major amendments made since the last issue. Test your understanding of the procedural changes and their implications in the operation of the unit.