CIRCULAR TO MASTER NO. O 9 DATE SUBJECT: Revision to Cargo Operation Manual Oil Tanker & Company Form

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CIRCULAR TO MASTER NO. O 9 DATE 01.06.17 APPLICABLE TO OIL TANKER VESSELS SUBJECT: Revision to Cargo Operation Manual Oil Tanker & Company Form Please note the following revision to the Cargo Operation Manual Oil Tanker & Company Form: Cargo Operation Manual Oil Tanker 1. SECTION 3 3.1.8 OPERATION OF VALVES PAGE 6 3 rd Paragraph add below as last text: Manual hydraulic pump should be kept stand-by in pump-room and at manifold for emergency use and all crew to be trained in its use. 3.2.2 VOYAGE ORDERS & CARGO STOWAGE PLAN PAGE 12 5 th Paragraph: On oil tankers generally tanks are loaded to maximum 98% volume. At no time vessel shall cross this maximum barrier replace with Nominated cargo quantity against available volume basis maximum temperature expected. Maximum stow shall not exceed 97.8% by volume of the tank capacity 2. SECTION 4 4.1 GENERAL PAGE 4 Add new section 4.1.4 Dealing with Emergencies in Terminal Dealing with emergencies in terminal 1. Stop cargo transfer operation and raise general alarm. 2. Inform the terminal that all operations are ceased and follow the Contingency plan of the terminal for the applicable type of emergency. 3. Prepare engines for immediate use. 4. Carry out notification to head office, Owners, Charterers and other parties as per Contingency notification procedure. 1

5. Evaluate whether safety of the vessel is endangered and prepare to case off from the terminal or follow evacuation plan, as per terminal instructions. 4.2.3 LOADING PRECAUTIONS PAGE 5 New add section - 4.2.3.1 Cargo Topping up precautions To include following topping up precautions. - Senior deck officer must be present in CCR, well before commencing top-up. - Reduce cargo loading rate to pre-agreed cargo topping up rate. - Restrict number of cargo tanks to be topped up simultaneously, and topping up more than one cargo tank should be avoided. - In addition to close monitoring of remote gauges, such readout should be compared with local independent monitoring such as UTI and/or MMC tapes. - Monitoring of Topped-up cargo tanks, post top-up, should be recorded in Port Log or Hourly Record. 3. SECTION 4 4.5.1 DISCHARGING PRECAUTIONS PAGE 8 Add this word as last paragraph: For Homogeneous cargo discharge, lower the tank levels to below 95% before commencing full discharge. 4. SECTION 5 5.6.4 LOADED PASSAGE PAGE 7 Replace with as below: It is important to maintain a positive pressure in cargo tanks and pressure should never be allowed to fall below 100 mmwg when in an inert condition. Oxygen content shall be checked atleast two times a week and records maintained onboard. Following safety checks should be carried out on daily basis except when weather conditions render it too dangerous to go onto deck; 2

a. Oxygen content of cargo tanks are to be measured atleast twice a week. b. Check the water level in water loops installed in pipework for gas, water or pressure transducers, to prevent the backflow of hydrocarbon gases into gas-safe spaces. c. In cold weather, ensure that the arrangements to prevent the freezing of sealing water in the deck seals, pressure/ vacuum breakers etc. are in order. d. Tank low pressure alarms should be tested at an interval not exceeding one week. 5.9 PURGING PAGE 12 First paragraph - 1.4% replace with 2%. 5. SECTION 11 11.2.1 CARGO TANK OPENINGS AND OTHER FITTINGS PAGE 4 Point 4 replace as below: 4. Pressurize tank using compressed air or inert gas. 11.2.2 CARGO PIPELINES AND VALVES TEST PAGE 5 1 st Paragraph replace as below: Cargo pipelines and valves should be pressure tested hydrostatically to 100% of their rated working pressure (MAWP) and be marked with the date of test and the pressure. Tests are to be carried out once in Twelve (12) months. The head office is to be informed if the duration extending beyond Twelve months. Furthermore, cargo pipelines and valves should be hydrostatically tested to 1.5 times their rated working pressure (MAWP) at least twice within any five year period. 6. SECTION 12 12.6.3 DISCHARGE OF HOMOGENEOUS CARGOES (PARALLEL PUMPING) PAGE 6 Replace existing guidance with below; 3

- Incase of parallel operation of Framo pumps there is a risk of back-flow of cargo into the incoming pump. - The incoming pump should have the hydraulic pressure higher than the running pump (normally 20 bars). This adjusted subsequently to get the desired flow rate from each tank. - The level of the tanks should be below alarm level (95%) so that any back-flow can be detected. - Pump capacity should be controlled by the pump hydraulic pressure, not by throttling the cargo discharge valve or any other valve in cargo piping system. - Generally, we recommend to run as many pumps in parallel as practical, at a reduced hydraulic pressure, rather than just a few pumps at maximum hydraulic pressure. - Monitor the ullage very closely of the incoming tank till it is confirmed that the level is dropping. - If the RPM of the pump is reduced below the parallel pump, part of the cargo from the pump with higher RPM will flow into the pump with lower RPM. Company Form 1. TKR 16 Cargo Operation Plan Page 4 - Inclusion of Topping off-rate m3/hr Kindly acknowledge this revision and bring the contents of same to the attention of all staff. Capt. Mayank Mishra General Manager Enclosure: TKR 16 Cargo Operation Plan Rev. 4 Jun / 17 4

CARGO OPERATION PLAN (As per 33 CFR 155.750) Vessel :- Voy / Date :- Port :- Berth :- 1. Cargo Information (*) LOADING / DISCHARGING Parcel Charterers / Shipper Stowage Tank B/L Figure Ship Figure Loading Port Unloading Port SG or Density Loading Temperature Deg C Deg C Deg C Voy:- Deg C MT MT Voy:- Deg C MT MT Voy:- Deg C MT MT Heat Requirement Disch:- Deg C Disch:- Deg C Disch:- Deg C Limitation :- Limitation :- Limitation :- Heat Adjacent Tank Max deg C Max deg C Max deg C Cooling Requirement N2 Requirement Yes / No mmhg % Yes / No mmhg % Yes / No mmhg % Pressure in Tank Oxygen Content Pollution Category ( X, Y, Z or OS) Ship Type (II, III or NA) Pre-wash Requirements YES / NO YES / NO YES / NO Viscosity at Discharge mpas @ Deg C mpas @ Deg C mpas @ Deg C Temperature Flash Point Deg C Deg C Deg C Boiling Point / Freezing Point Deg C Deg C Deg C Melting Point Deg C Deg C Deg C Vapour Density Vapour Pressure mmhg at Deg C mmhg at Deg C mmhg at Deg C Flammable Limit to % to % to % Extinguishing Agent Cargo Solubility Tank Filling Limits % % % Coating Compatibility PPE to be used (*) If more than 3 parcels are being worked at this port, prepare another form (TKR-16) for same. TKR-16 Page 1 of 12 REV 4 06/17

2. Hazards Involved in handing of Cargo :- Parcel 1 Parcel 2 Parcel 3 Safety (If Exposed) Parcel 1 Parcel 2 Parcel 3 Skin Contact Eye Contact Inhalation Ingestion Instructions for Safe Handling of Cargo :- Avoid exposure to gas, Stand on windward side while ullaging and sampling. TKR-16 Page 2 of 12 REV 4 06/17

Emergency Procedure for Spillage :- 1. Emergency Notification as per port specific Port Contact List. 2. Follow Vessel Response Plan and SOPEP/SMPEP manual. 3. Cargo specific procedures if any, to be mentioned below, Parcel Parcel 1 Parcel 2 Parcel 3 Emergency Spillage Procedure 3. Tank-wise Quantity to be Loaded or Discharged : Tank Number Quantity in m 3 Quantity(MT) Ullage Volume % Expected Transfer Time TKR-16 Page 3 of 12 REV 4 06/17

4. Order of Loading/Discharging : a) Parcel 1 :- b) Parcel 2 :- c) Parcel 3 :- Checks to be carried out prior Loading/Discharging :- Max allowable Loading/Discharging Rate :- m 3 /hr Topping off-rate m 3 /hr In case of Discharging, pump auto trip settings :- a. Over Heat Trip :- Pump Casing deg C / Pump Bearing deg C b. Over Speed Trip :- RPM c. Over Pressure Trip :- kg/cm 2 TKR-16 Page 4 of 12 REV 4 06/17

Loading / Discharging Operation :- During transfer operations, The terminal and vessel will monitor the cargo transfer rate to verify it does not exceed the agreed max. allowable cargo rate and exchange cargo figures received / transferred. Any additional information to be listed below :- Topping Up / Stripping / Shutdown Procedure :- 5. Transfer Piping Arrangement :- (Manifold Jumper Connection etc) a. Attach Manifold Diagram to this plan, neatly showing various cargo hoses/jumper connections. b. Vessel s cargo transfer piping diagram including the location of each valve, pump and its control device, vents are posted in the Cargo Control Room. c. The locations of the shutoff valves or other isolation devices are posted in the Cargo Control Room. d. Procedure for operating the Emergency Shutdown and Communication e. The emergency trips are located in the following places :- 1. 2. 3. 4. 5. TKR-16 Page 5 of 12 REV 4 06/17

6. Ballasting / De-ballasting Plan :- (Please prepare ship specific Ballast Tank Lay-out) Order of Ballasting / Deballasting Operation :- 7. Vapour Emission System :- a. The maximum allowable transfer rate for the current operation b. The initial transfer rate for the current operation c. Venting Capacity :- PV Breaker (Pressure side setting) d. Venting Capacity :- PV Breaker (Vacuum side setting) e. Venting Capacity :- High Velocity Vents (Pressure side) f. Venting Capacity :- High Velocity Vents (Vacuum side) g. In case vessel is provided with independent tank pressure sensor, Alarm Pressure settings are mmhg Pressure side and mmhg on Vacuum side. h. Vapour Line Connection :- YES / NO i. A table or graph of transfer rates/pressure drop calculations :- Data is readily available in Vapour Recovery Operation Manual located in CCR. Inerted Vessel Non Inerted Vessel VRL (Inerted Vessel) VRL (Non Inerted Vessel) Guidance Note on Pressure Sensor Alarm Settings High Pressure Settings Low Pressure Settings 10% above the normal actuation settings of Pressure Valve Not more than 90% of the normal actuation settings of Pressure Valve Above Zero (Tank should never be allowed to fall below Zero) 10% above the normal actuation settings of Vacuum Valve Not less than 100 mmwg or (0.144 PSI) Not less than lowest Vacuum Valve setting TKR-16 Page 6 of 12 REV 4 06/17

8. Watch Arrangement :- Time Location Title and Name Remarks 00:00 to 06:00 and 12:00 to 18:00 06:00 to 12:00 And 18:00 to 24:00 CCR Manifold On Deck CCR Manifold On Deck Total Number of persons required during transfer : persons (including deck/engine room staff) Chief Officer :- He will be overall in-charge of cargo transfer operation. He will coordinate with the loading master, Determine loading/discharging rate as per pre-cargo conference with shore. Will discuss and decide Emergency Stop Procedures and method of communication. He will test emergency stops and High/Overflow alarms. Duty Officer :- He will execute cargo operation as instructed by chief officer. He will check list and trim of the vessel and correct as required. He will keep chief officer informed of any deviation observed to the cargo transfer procedure. He will carry out repeated checks as mentioned in Ship-Shore Safety Checklist. He will hourly monitor cargo transfer rate, stresses and record accordingly. Deck Duty Personnel :- They will assist Chief Officer and Duty officer in executing cargo transfer. They will assist surveyor in taking a sample and ullaging. They will rig required SOPEP/FFA equipment as required for the cargo transfer. Will attend manifold, tend gangway and moorings regularly. They will set up cargo/ballast lines under duty officers supervision. TKR-16 Page 7 of 12 REV 4 06/17

9. Arrival / Intermediate / Departure Drafts and Stress Calculations :- INITIAL ARRIVAL BERTH HRS COT ULLAGE VOL(m3) WBT SNDG(m) VOL M3 DRAFT 1P FPK FWD : 1S 1P AFT : 2P 1S TRIM 2P DEPTH / LOW 3S TIDE 4P 3S UKC 4S 4P SF/BM 5P 4S Fr No 5S 5P GM 6P 5S DISP 6P SL P SL S QTY OBQ XXXXXXX m3 QTY TO GO XXXXXX m3 TOTAL : STAGE 1 AFTER HRS COT ULLAGE VOL(m3) WBT SNDG(m) VOL M3 DRAFT 1P FPK FWD : 1S 1P AFT : 2P 1S TRIM 2P DEPTH / LOW 3S TIDE 4P 3S UKC 4S 4P SF/BM 5P 4S Fr No 5S 5P GM 6P 5S DISP 6P SL P SL S QTY OBQ XXXXXXX m3 QTY TO GO XXXXXX m3 TOTAL : TOTAL HRS : TKR-16 Page 8 of 12 REV 4 06/17

STAGE 2 AFTER HRS COT ULLAGE VOL(m3) WBT SNDG(m) VOL M3 DRAFT 1P FPK FWD : 1S 1P AFT : 2P 1S TRIM 2P DEPTH / LOW 3S TIDE 4P 3S UKC 4S 4P SF/BM 5P 4S Fr No 5S 5P GM 6P 5S DISP 6P SL P SL S QTY OBQ XXXXXXX m3 QTY TO GO XXXXXX m3 TOTAL : STAGE 3 AFTER HRS COT ULLAGE VOL(m3) WBT SNDG(m) VOL M3 DRAFT 1P FPK FWD : 1S 1P AFT : 2P 1S TRIM 2P DEPTH / LOW 3S TIDE 4P 3S UKC 4S 4P SF/BM 5P 4S Fr No 5S 5P GM 6P 5S DISP 6P SL P SL S QTY OBQ XXXXXXX m3 QTY TO GO XXXXXX m3 TOTAL : TKR-16 Page 9 of 12 REV 4 06/17

STAGE 4 AFTER HRS COT ULLAGE VOL(m3) WBT SNDG(m) VOL M3 DRAFT 1P FPK FWD : 1S 1P AFT : 2P 1S TRIM 2P DEPTH / LOW 3S TIDE 4P 3S UKC 4S 4P SF/BM 5P 4S Fr No 5S 5P GM 6P 5S DISP 6P SL P SL S QTY OBQ XXXXXXX m3 QTY TO GO XXXXXX m3 TOTAL : FINAL DEP HRS COT ULLAGE VOL(m3) WBT SNDG(m) VOL M3 DRAFT 1P FPK FWD : 1S 1P AFT : 2P 1S TRIM 2P DEPTH / LOW 3S TIDE 4P 3S UKC 4S 4P SF/BM 5P 4S Fr No 5S 5P GM 6P 5S DISP 6P SL P SL S QTY OBQ XXXXXXX m3 QTY TO GO XXXXXX m3 TOTAL : TKR-16 Page 10 of 12 REV 4 06/17

10. Safety Information / Requirements / Guidance Notes :- a. All crew members to be briefed about proper cargo handling procedures as required while handing cargo. All officers and crew members must read and familiarize themselves with MSDS of chemicals onboard. (See MSDS board) b. Carry out Pre-Arrival Checks as per checklist and ensure all items are in order. c. Gangway and moorings to be tended at regular interval. d. Keep eye wash and decontamination shower on for ready use. e. Ship-Shore checklist to be strictly complied with at all the times. Duty officers must carry out Repeated Checks as listed in Ship-Shore checklist at agreed interval and log down. f. No open sampling is allowed. Duty officer will accompany surveyor for gauging and sampling. g. Duty officer to calculate hourly cargo transfer rate/sf/bm and maintain a record of same in hourly rate log. h. PV valves to be monitored closely for their correct operation. i. Keep strict ISPS watch and comply with all company/port regulations. j. EMERGENCY NOTIFICATION INFORMATION :- Refer to Port Contact List which must be readily available on Bridge and CCR.. TKR-16 Page 11 of 12 REV 4 06/17

Approved by : Master Prepared by Chief Officer Read and Understood : Second Officer Cadet Pumpman AB Third Officer Cadet AB AB TKR-16 Page 12 of 12 REV 4 06/17