The document outlines new requirements for oil record books effective January 1st, 2007. Key changes include:
1. Requiring the quantity of oil residues retained on board to be recorded weekly.
2. Clarifying items under procedures for collection and disposal of oil residues and bilge water.
3. Deleting item 19 from the section on automatic discharge overboard or disposal of bilge water, and renumbering subsequent items.
4. Adding an optional section on additional operational procedures and general remarks.
location and identification for defect, grinding then welding build up according to repair procedure ,then flushing .
*step by step fabrication and NDE activities.
location and identification for defect, grinding then welding build up according to repair procedure ,then flushing .
*step by step fabrication and NDE activities.
Presentation is about the repair welding not procedure also discussed the certain conditions where repair is necessary, it also include the welding procedure, Marking of repair. And the causes behind the occurance of repair, and various NDT techniques suitable to detect the welding defect.
This manual covers the basic guidelines and minimum requirements for
periodic inspection of heat exchangers used in petroleum refinery.
Locations to be inspected, inspection tools, frequency of inspection &
testing, locations prone to deterioration and causes, corrosion
mitigation, inspection and testing procedures have been specified in
the manual.
Documentation of observations & history of heat exchangers,
inspection checklist and recommended practices have also been
included.
Heat exchanging equipment is used for heating or cooling a fluid.
Individual heat transfer equipment is named as per its function.
Cooler
A cooler cools the process fluid, using water or air, with no change of
phase.
Chiller
A chiller uses a refrigerant to cool process fluid to a temperature below
that obtainable with water.
Condenser
A condenser condenses a vapour or mixture of vapours using water or
air.
Exchanger
An exchanger performs two functions in that it heats a cold process
fluid by recovering heat from a hot fluid, which it cools. None of the
transferred heat is lost.
Static and Fatigue Analysis of Pressure Vessel as per ASME CodesUtsav Patel
The problem statement is to design a pressure vessel working as an adsorber in a chemical plant. Design data calculated as per ASME BPVC Section VIII/Division I and it analyzed as per ASME BPVC Section VIII/Division II. You can trust this data.
If you need any help regarding this, contact me via LinkedIn.
Group case study on Pressure Vessel Safety.Basis of the presentation was The Great Molasses Flood of 1919.Includes solution of three mathematical problems,causes of pressure vessel failure,recommended shapes of vessels and conclusion of case study.
Introduction to stress corrosion cracking and nace material requirementsMahendra Prabhu S
Corrosion is one of the major areas of interest for Design / plant operator and maintenance personnel to keep the plant in good shape. The understanding of corrosion mechanism is important for the design engineers to tackle this problem by choosing right metallurgy / manufacturing methods and Inspection techniques. This presentation gives an overview about Sulfide stress corrosion in refining environment and the NACE MR0103 employed to control this phenomena.
Presentation is about the repair welding not procedure also discussed the certain conditions where repair is necessary, it also include the welding procedure, Marking of repair. And the causes behind the occurance of repair, and various NDT techniques suitable to detect the welding defect.
This manual covers the basic guidelines and minimum requirements for
periodic inspection of heat exchangers used in petroleum refinery.
Locations to be inspected, inspection tools, frequency of inspection &
testing, locations prone to deterioration and causes, corrosion
mitigation, inspection and testing procedures have been specified in
the manual.
Documentation of observations & history of heat exchangers,
inspection checklist and recommended practices have also been
included.
Heat exchanging equipment is used for heating or cooling a fluid.
Individual heat transfer equipment is named as per its function.
Cooler
A cooler cools the process fluid, using water or air, with no change of
phase.
Chiller
A chiller uses a refrigerant to cool process fluid to a temperature below
that obtainable with water.
Condenser
A condenser condenses a vapour or mixture of vapours using water or
air.
Exchanger
An exchanger performs two functions in that it heats a cold process
fluid by recovering heat from a hot fluid, which it cools. None of the
transferred heat is lost.
Static and Fatigue Analysis of Pressure Vessel as per ASME CodesUtsav Patel
The problem statement is to design a pressure vessel working as an adsorber in a chemical plant. Design data calculated as per ASME BPVC Section VIII/Division I and it analyzed as per ASME BPVC Section VIII/Division II. You can trust this data.
If you need any help regarding this, contact me via LinkedIn.
Group case study on Pressure Vessel Safety.Basis of the presentation was The Great Molasses Flood of 1919.Includes solution of three mathematical problems,causes of pressure vessel failure,recommended shapes of vessels and conclusion of case study.
Introduction to stress corrosion cracking and nace material requirementsMahendra Prabhu S
Corrosion is one of the major areas of interest for Design / plant operator and maintenance personnel to keep the plant in good shape. The understanding of corrosion mechanism is important for the design engineers to tackle this problem by choosing right metallurgy / manufacturing methods and Inspection techniques. This presentation gives an overview about Sulfide stress corrosion in refining environment and the NACE MR0103 employed to control this phenomena.
SUPER SAFETY SERVICES provide both single gas and multigas monitors for personal monitoring and portable safety applications providing protection against a wide range of industrial gas hazards.
Gas Detector-compact portable gas detector with a large LCD. It can monitor CO, H2S, O2 and combustible gas simultaneously. The instrument features two instant alarms
OSHA and the NFPA have specific guidance and safeguards that must be followed when performing hot work operations. This can most readily be achieved by instituting a hot work permit program/system at your facility or within your community. This slideshare provides an overview of the hot work process and considerations. This presentation is based on the requirements found in NFPA 1:41 and NFPA 51B.
Citation by KPMG-SCLC (Supply Chain Leadership Council) on awarding India's first ever Cold Chain Personality Award, December 2010. For Individual Excellence in Food Business in an Emerging Landscape and works related to street hawkers, innovation and thought leadership
Presented at World Conference Cold chain - Thaifex 2013. Opportunity and Challenges in emerging markets, case study India. Cold chain development, the need and the success in hand. Market prospects for cold chain in emerging markets with focus on India.
Why worry about Organised Retail (or FDI in retail). It can bring organisation and promote economic co-operation and development but will require a shift in current day mindsets.
by Capt. Pawanexh Kohli on the shooting incident off Kerala (India), involving the Italian tanker MT Enrica Lexie and fishing boat St. Antony - Feb 2012
Free Trade Zone in Uttar Pradesh India
A cover feature column, Logistics Times, India's largest Free Trade and Warehousing zone. The future of India's supply chain network.
Humanitarian Logistics (2012)- importance of supply cells when planning for disasters. Create lifeboats round population centres to cater supplies for different types of disaster situations. Only deploying man power is insufficient mitigation. Emergency management must include associated pre-emptive stock and supply management - Synergy with existing cold chain capacities.
Interview with ICE Magazine (of GCCA) on cold chain scenario in April 11. The future prospects of cold chain in India, on being awarded cold chain personality of the year, on the bottlenecks to development of cold chain
1. CHANGES TO OIL RECORD BOOK (EFFECTIVE 01/JAN/2007)
(Go through the Rules yourself – errors and omissions likely)
New Print Marked in Red -- explanatory remarks in Blue
(A) Ballasting or cleaning of oil fuel tanks
1. Identity of tank(s) ballasted.
2. Whether cleaned since they last contained oil and, if not, type of oil previously carried.
3. Cleaning process:
.1 position of ship and time at the start and completion of cleaning;
.2 identify tank(s) in which one or another method has been employed (rinsing through,
steaming, cleaning with chemicals; type and quantity of chemicals used, in m³);
.3 identity of tank(s) into which cleaning water was transferred.
4. Ballasting:
.1 position of ship and time at start and end of ballasting;
.2 quantity of ballast if tanks are not cleaned, in m³.
(B) Discharge of dirty ballast or cleaning water from oil fuel tanks referred to under Section (A)
5. Identity of tank(s).
6. Position of ship at start of discharge.
7. Position of ship on completion of discharge.
8. Ship’s speed(s) during discharge.
9. Method of discharge:
.1 through 15 ppm equipment
.2 to reception facilities.
10. Quantity discharged, in m3
(C) Collection and disposal of oil residues (sludge and other oil residues)
(Codes 11 - . 1, . 2 changed)
11. Collection of oil residues.
Quantities of oil residues (sludge and other oil residues) retained on board. The quantities should
be recorded weekly1 (means that the quantity must be recorded once a week even if the voyage
lasts more than one week).
.1 identity of tank(s) ………………………………
.2 capacity of tank(s) ……………………………… m3
.3 total quantity of retention………………………… m3
1
Only in tanks listed in item 3 of form A and B of the Supplement in the IOPP Certificate used for sludge.
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2. 12. Methods of disposal of residue.
State quantity of oil residues disposed of, the tank(s) emptied and the quantity of contents
retained in m3:
.1 to reception facilities (identify port)2
.2 transferred to another (other) tank(s) (indicate tank(s) and the total content of tank(s))
.3 incinerated (indicate total time of operation);
.4 other method (state which).
(D) Non-automatic discharge overboard or disposal otherwise of bilge water which has
accumulated in machinery spaces
13. Quantity discharged or disposed of, in cubic metres.3
14. Time of discharge or disposal (starts and stop).
15. Method of discharge or disposal:
.1 through 15 ppm equipment (state position at start and end);
.2 to reception facilities (identify port) 2
.3 transfer to slop tank or holding tank (indicate tank(s); state the total quantity retained
in tank(s), in m3).
(E) Automatic discharge overboard or disposal othererwise of bilge water which has accumulated
in machinery spaces.
16. Time and position of ship at which the system has been put into automatic mode of operation for
discharge overboard.
17. Time when the system has been put into automatic mode of operation for transfer of bilge water
to holding tank (identify tank).
18. Time when the system was put into manual operation.
Item (E) 19 deleted. 19 carried forward to (F) and subsequent item numbers changed.
(F) Condition of the oil discharge monitoring and control system.
19. Time of system failure. (This used to be item 20)
20. Time when system has been made operational. (This used to be item 21)
21. Reasons for failure. (This used to be item 22)
(G) Accidental or other exceptional discharges of oil.
22. Time of occurrence (This used to be item 23)
23. Place or position of ship at time of occurrence. (This used to be item 24)
24. Approximate quantity and type of oil. (This used to be item 25)
25. Circumstances of discharge or escape, the reasons therefor and general remarks. (This used to be
item 26)
2
Ship’s masters should obtain from the operator of the reception facilities, which includes barges and tank trucks, a receipt or
certificate detailing the quantity of tank washings, dirty ballast, residues or oily mixtures transferred, together with the time
and date of the transfer. This receipt or certificate, if attached to the Oil Record Book Part I, may aid the master of the ship in
proving that his ship was not involved in an alleged pollution incident. The receipt or certificate should be kept together with
the Oil Record Book Part I.
3
In case of discharge or disposal of bilge water from holding tank(s), state identity and capacity of holding tank(s) and
quantity retained in holding tank.
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3. (H) Bunkering of fuel or bulk lubricating oil.
26. Bunkering: (This used to be item 27)
.1 Place of bunkering
.2 Time of bunkering
.3 Type and quantity of fuel oil and identity of tank(s) (state quantity added in tonnes and
total content of tank(s)).
.4 Type and quantity of lubricating oil and identity of tank(s) (state quantity added in
tonnes and total content of tank(s)).
All Items under (I) are Optional/Additional.
(I) Additional operational Procedures and general remarks
27. Cleaning / Steaming of oily - water separator.
.1 position of ship and time at start and completion of cleaning.
.2 identify the tank(s) in which one or another method has been employed (rinsing
through, steaming, cleaning with chemicals, type and quantity of chemicals used).
.3 identify tank(s) into which cleaning, water was transferred.
28. Changing cartridge / coalescer of oily - water separator.
.1 position of ship and time at the start and completion of changing.
.2 method of containing cartridge / coalescer in preparation for disposal to shore facility
(must be sealed and labeled properly).
29. Testing 15 ppm equipment
.1 time at which equipment was tested
.2 condition of equipment during the test.
30. Transfer of Oils within ship.
.1 from fuel storage tank (identity of tank) to fuel settling tank, quantity transferred (cubic
meters), number of transfers per day, mode of transfer (manual or automatic pump).
.2 from diesel storage tank (identity of tank) to diesel setting tank, quantity transferred
(cubic meters) number of transfer (manual or automatic pump).
3. from cylinder oil storage tank to measuring tank (if applicable), quantity transferred
(liters / number of transfers per day / mode of transfer (pump or gravity)).
.4 from main engine oil storage tank(s) lube oil service tank (identity of tanks ie. main
engine sump tank, Stern tube header tank, etc & quantity transferred (liters), mode of
transfer (pump, gravity, bucket)).
.5 from generator engine oil storage tank to lube oil service tank (identity of tank, ie G:E
engine sump tank, etc) quantity transferred (liters) mode of transfer (pump, gravity,
bucket).
.6 from 200 L drums (location / ex deck, forecastle, steering room. etc.) to lube oil
storage or service tank (identity of tank ex cylinder oil storage tank; E M lube oil
storage tank, etc) quantity transferred / mode of transfer (pump, gravity, bucket).
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