Jetty Information Booklet

Transcription

1 Page 1 of 15 JETTY INFORMATION BOOKLET Revison Name Change Date Signature 1 S.Chatterjee Section 2.3,2.7,2.8,2.9,2.10, Aug 10 Action Name Title Date Signature Preparation S.Chatterjee Operations Manager 14 June 09 Approval Paul Shynett Jr Terminal Manager All rights reserved. This document has been prepared for internal use on Oiltanking facilities only. It is the user s obligation to comply with all applicable laws and regulations. No warranty is made, either expressed or implied.

2 Page 2 of 15 Jetty Information Booklet Content 1 Foreword 2 Terminal Regulations 3 Jetty Information and Acceptance Criteria 4 Mooring Arrangements 5 Shore Connections 6 Jetty Emergency Action Plan

3 Page 3 of Foreword The Jetty Information Booklet (JIB) has been compiled for your information and guidance. It contains the relevant terminal regulations and information essential for safe and efficient operations while your vessel is alongside at Oiltanking Odfjell Terminal Oman (OOTO). It will be updated as necessary to reflect recent changes. We would appreciate your full co-operation during your stay at our terminal, in particular on matters concerning health, safety, security and environmental protection. You are requested to comply with the relevant recommendations and guidelines contained in the latest edition of the International Safety Guide for Oil Tankers and Terminal, and the relevant requirements of the latest version of SIP Rules and Regulations for Port Area. Please do not hesitate to contact our Operations Superintendant or the Terminal Manager in his absence, for the latest version of JIB or on any query you may still have after reading this booklet or regarding other items not included in it. They may be contacted at GSM: (+968) and (+968) respectively. The Terminal Management, Oiltanking Odfjell Terminals & Co LLC

4 Page 4 of Terminal Regulations 2.1 Moorings The Master shall ensure that his vessel is adequately moored alongside. Please refer to Section 4 on mooring arrangements. 2.2 Cargo Transfer Operations The vessel shall adhere strictly to the safety and pollution prevention guidelines laid down in the latest edition (5 th ) of the ISGOTT. 2.3 Clean Ballast and readiness to commence operation There is no dirty ballast/slop reception facility at the terminal. Vessels for loading are to arrive with clean ballast and cargo tanks ready to receive nominated cargoes. This specifically includes tests like wall wash which should be done prior to vessel berthing alongside. 2.4 Tank Cleaning/Gas-Freeing Cleaning or gas freeing of tanks alongside is not permitted. 2.5 Inert Gas System If fitted, the inert gas system of the vessel, including alarms, meters and recorder for oxygen content and pressure of inert gas supply shall be fully operational and in use. 2.6 Readiness to Move Your ship must be ready to move under its own power at short notice in the event of any emergency. 2.7 Wind Velocities At wind speeds of 18m/s or 35 Knots the loading /discharge operation will be stopped and MLA disconnected. At a wind speed forecast of 26m/s or 50 Knots the tanker shall normally leave the berth for open sea.

5 Page 5 of Over the Tide Cargo operations Over the tide cargo operations are not allowed at OOTO s berths. 2.9 Double banking Double banking operations (direct transfer from ship to ship) is allowed at berth AA2 and A. For any manipulation of goods which is to take place between the ship and any other vessel, prior permission from OOTO is required. Even if OOTO has allowed such transfer, it willtake place under the masters responsibility and for account and risk of the master and owner of the ship and not to the account of OOTO Communication When alongside the communication between ship and shore will be through Terminal UHF set Channel 2. In case of failure in communication on terminal UHF set then alternate communication will be established on VHF channel 13. In case of complete failure in communication defined by failure of either ship or shore representative to respond to radio communication (radio check or normal operations) within five successive calls or five minutes whichever is less then the operations to be immediately suspended and to be resumed only on reestablishment of communication Escape Routes and Emergency equipment Refer to OOTO Terminal Information Booklet HSSE Policy OOTO is committed to the safe and efficient operation of its facilities. Its goal is to prevent all accidents, injuries and occupational illness and to protect the environment. Towards this end, OOTO HSSE rules and regulations will be strictly enforced. - No Smoking Allowed on the Jetties. Smoking on vessels to be allowed in designated areas, which will be marked, by the vessel. - All operations to comply with closed loading as per ISGOTT. - Vessel operations will be stopped in the event an unsafe practice is observed.

6 Page 6 of 15 Our facility is in compliance with the ISPS Code. Therefore you are requested to comply with the following terminal security regulations: - Only OOTO authorized personnel are allowed access into the terminal. - Unless permitted by the Terminal Management, no persons are allowed on the jetty. - Delivery of provisions, stores or equipment to ship alongside the jetty is permitted on a case to case basis with prior approval from the Terminal Manager. - Except for authorized crafts, no boat, launch or other craft may approach the jetty or vessel secured thereto without the prior approval of the Terminal Management.

7 Page 7 of Jetty Information & Acceptance Criteria Berths C1A & C1B (for ORPC) Max/Min Dwt 107,000/1,000 Max Displacement 137,500 MT Max/Min LOA 268/61 m Max Beam 43m Max Draft m Max berthing speed 0.10 m/sec Max berthing angle 6 deg Max manifold height at HHW 20.4/12.8*m Min manifold height at LLW 2.0/1.5*m Depth alongside m CD Notes: 1. A min UKC of 0.5m is required for vessel alongside. 2. * Applicable for LPG & Propylene L/arms. Min/max distances between manifold flange and shipside:1.5/3.5 m. Min/max distances between manifolds:1.3/1.5 m. 3. Fuel Oil, LPG and Propylene are not available on C1B. 4. HHWL = +3.4m CD; LLWL = 0.0m CD. 5. Berths C1A & C1B are mostly dedicated for SRC. 6. All ships will berth Bow Out alongside all berths. Berth AA1 Max/Min DWT 70,000/4,000 Max Displacement 94,000 MT Max/Min LOA 220/96 m Max Beam 35m Max Draft m Max berthing speed 0.10 m/sec Max berthing angle 10 deg Max manifold height at HHW 20 m Min manifold height at LLW 1m Max manifold height at HHW (LPG) 15 m Min manifold height at LLW (LPG) 1.5 m Depth alongside m CD

8 Page 8 of 15 Berth AA2 Max/Min DWT 70,000/ 4,000 Max/Min DWT for Methanol MLA 50,000/10,000 Max Displacement 94,000 MT Max/Min LOA 220/96 m Max Beam 35m Max Draft m Max berthing speed 0.10 m/sec Max berthing angle 10 deg Max manifold height at HHW (for Methanol) 15.1 m Min manifold height at LLW (for Methanol) 02.5 m Max manifold height at HHW (for Others) 20 m Min manifold height at LLW (for Others) 1 m Depth alongside m CD Berth A Max/Min DWT 110,000/1,000 Max Displacement 146,300 MT Max/Min LOA 260/60 m Max Beam 42 m Max Draft m Max berthing speed 0.10 m/sec Max berthing angle 6 deg Max manifold height at HHW 20 m Min manifold height at LLW 1m Depth alongside m CD

9 Page 9 of Mooring Arrangements Ships alongside shall be securely moored at all times. The required minimum numbers of mooring lines for each category of vessels are indicated in the following table: DWT of Vessel Mooring Lines and below 2 breast & 2 springs fore and aft Between head/stern lines; 2 breast & 2 springs fore and aft Between head/stern lines; 2 breast & 2 springs fore and aft Above 40,000 4 head/stern lines; 2 breast & 2 springs fore and aft Notes: Mooring lines shall be secured to proper self-stowing winches, mooring bitts or bollards onboard. Mixed mooring is not permitted. Whenever possible, springs and breast lines shall be of wires. All wires shall be attached with nylon tails not exceeding 11 metres in length. Automatic self-tensioning winches must not be left in automatic self-tensioning mode on completion of mooring. Emergency towing wires shall be in place both forward and aft of the vessel. Mooring watch shall be maintained to ensure that moorings are properly tended. Reference: OCIMF publication Effective Mooring.

10 Page 10 of Shore Connections Product Berth No. & Size of Loading Arms (L/Arm No.) Design Flow Rate Per MLA (cbm/hr) & Temp Naphtha C1A C1B 2 x 12 (6401/2) 2 x 12 (6412/13) 3,100 Temp 55 deg C Regular Gasoline C1A C1B 2 x 12 (6401/2) 2 x 12 (6412/13) 3,100 Temp 55 deg C Premium Gasoline C1A C1B Methanol (import) C1A C1B 2 x 12 (6401/2) 2 x 12 (6412/13) 1 x 12 (6402) 1 x 12 (6413) 3,100 Temp 55 deg C 1,272 Temp 55 deg C Gas Oil C1A C1B 2 x 12 (6403/4) 2 x 12 (6414/15) 2,862 Temp 55 deg C Aviation Fuel C1A C1B 2 x 12 (6403/4) 2 x 12 (6414/15) 2,862 Temp 55 deg C Fuel Oil C1A 1 x 12 (6405) 2,544 Temp 90 deg C Propylene: Liquid Vapour C1A 1 x 10 (6410) 1 x 8 (6411) 1,200 Temp 47 to 55 deg C LPG: Liquid Vapour C1A 1 x 10 (6406) 1 x 8 (6407) 1,200 Temp 28 to 55 deg C Methanol (Export) AA2 2 x 12 (501 A/B) 1,925 Temp 10 to 80 deg C

11 Page 11 of 15 Product Berth No. & Size of Loading Arms (L/Arm No.) LAB AA1 1 x 6 Hose 300 Design Flow Rate Per MLA (cbm/hr) & Temp Pure Petroleum Products Pure Petroleum Products Pure Petroleum Products AA1 2 x 12 (MLA AA1 1&2) AA2 2 x 12 (MLA AA2 1&2) A 2 x 12 (MLA A 1&2) 1925 Temp:10 to 80 deg C 1925 Temp:10 to 80 deg C 1925 Temp:10 to 80 deg C LPG AA1 1 X 8 Liquid 1 X 4 Vapour (Piggy back on liquid) (MLA AA1 LPG) Benzene AA1 1 X 10 Liquid 1 X 6 Vapour (Piggy back on liquid) (MLA AA1 BZ) Benzene AA2 1 X 10 Liquid 1 X 6 Vapour (Piggy back on liquid) (MLA AA2 BZ) Paraxylene AA1 2 X 12 (MLA AA1 PX 1 &2) Paraxylene AA2 2 X 12 (MLA AA2 PX 1 &2) Raffinate AA1 2 x 12 (MLA AA1 1&2) Raffinate AA2 2 x 12 (MLA AA2 1&2) Temp:10 to 80 deg C 1925 Temp:10 to 80 deg C

12 Page 12 of 15 Product Berth No. & Size of Loading Arms (L/Arm No.) LSRN AA1 2 x 12 (MLA AA1 1&2) LSRN AA2 2 x 12 (MLA AA2 1&2) Design Flow Rate Per MLA (cbm/hr) & Temp 1925 Temp:10 to 80 deg C 1925 Temp:10 to 80 deg C Heavy Aromatics AA1 1 X 6 hose 300 MDI AA1 1 X 6 hose, liquid 1 X 3 hose, Vapour 300 Note: 1) In jetty C1 A & B Loading arms for LPG & Propylene are fitted with Emergency Release System. 2) In jetty AA2 Methanol loading arms are fitted with Emergency Release System. 3) In jetty AA1 LPG loading arms are fitted with Emergency Release system. 4) Rating of MLA flange connection: ANSI 300 # for LPG & Propylene ANSI 150 # for others

13 Page 13 of Jetty Emergency Action Plan The purpose of this Jetty Emergency Action Plan (JEAP) is to provide our Operations Technicians and Masters of ships at OOT managed jetties with a plan of action to be taken in the event of an emergency at the jetty or aboard the ship. This JEAP covers incidents on the jetties and aboard ships while they are moored alongside or approaching the berths. Types of Emergency An emergency is a non-routine situation resulting from an accident that gives rise to a spill or a fire. Some of the emergency situations that may occur are: 1) Fire on the jetty/ship. 2) Chemical or hydrocarbon spill on the jetty/into surrounding water. 3) Ship colliding/grounding at jetty approaches. Action Plan for Handling Emergency Situations at the Jetty The person discovering an emergency situation aboard a ship or on the jetty shall sound the alarm and report it immediately to the responsible Officer of the ship and the Duty Shift Supervisor, who shall activate their respective Emergency Action Plans as appropriate. Duty Shift Supervisor is contactable by the UHF radio set (channel 1) provided by the terminal to all vessels alongside. 1) Fire on the Jetty/Ship Actions by the Terminal: - Sound the fire alarm. - Activate ESD switch to automatically stop loading pump and close valves. (only when loading vessels) - When unloading vessel, confirm that ship s pumps are stopped before initiating ESD. Note : Ensure that Vessels pump are stopped before pressing the ESD. Valve closure time is sec.

14 Page 14 of 15 - Activate water spray system on gangway tower and near loading arms as appropriate. - Activate elevated remote control water/foam monitor to fight the fire or cool jetty and cargo manifold area as appropriate. - Disconnect loading arms/hoses if safe after liaising with the ship s Officer. - When directed by the Harbour Master arrange for ship at adjacent jetty to unmoor and sail off. - Restrict vehicle entry into jetty area to emergency vehicles only. - Cordon off the affected area. - Request all vessels approaching the terminal to hold off. - Activate Terminal Emergency Action Plan Actions by the Ship: - Sound fire alarm. - Activate shipboard Emergency Action Plan. - Activate ship s fire-fighting system to fight fire and prevent fire from spreading. - Inform the Terminal, HMO and other parties in Emergency Contact List. - Stop all ventilation and close all openings. - Stop cargo pumps and close all valves when discharging. - When loading, close all valves after confirming terminal cargo pumps are stopped. - Rig pilot ladder or accommodation ladder on offshore side for rescue/evacuation purpose. - Direct fire fighting in cooperation with the terminal. - Standby to disconnect loading arms/hoses. - Put engines on standby. 2) Hydrocarbon/Chemical Spill on the Jetty/into Surrounding Water Actions by the Terminal: - Raise alarm. - Notify Harbour Master and other relevant parties in the List of External Party Contacts - Refer to MSDS for material spilled. - Identify the source and try to arrest further spillage if safe. - Use proper PPE.

15 Page 15 of 15 - Use absorbents and/or dispersants to clean up spillage on jetty as appropriate. - If source of spill is from the ship, assist ship s crew to disperse and/or contain spillage. - Activate Terminal Spill Response Plan. Actions by the Ship: - Investigate source of spillage. - Stop cargo operations when spillage is from the ship. - Raise the alarm. - Identify the source and arrest further spillage if safe. - Refer to MSDS for material spilled. - Use proper PPE. - Activate shipboard Spill Response Plan (SOPEP). - Notify the terminal, Harbour Master and other parties in the Emergency Contact List. - Seek assistance from the terminal to disperse and/or contain spillage as necessary. - Use absorbents and/or dispersants to clean up spillage on deck as appropriate. 3) Ship Colliding/Grounding at Jetty Approaches Actions by the Terminal: - Inform Terminal Manager. - Hold off berthing/unberthing of vessels at affected berths. - Notify Harbour Master. - Activate Terminal Emergency Action Plan as appropriate. Actions by the Ship: - Inform the Terminal via the pilot onboard. - Notify Harbour Master. - Activate shipboard Emergency Action Plan as appropriate. - Consult the pilot who is trained to handle marine emergencies.