Chapter 6 Final Stripping Work
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1 Chapter 6 Final Stripping Work Procedure for implementing final stripping work Final stripping work should be implemented according to the procedure described below. 1. Final stripping and discharging work(p6-2 to P6-5) The stripping pump is used for final stripping. Efforts should be made to thoroughly strip pumps, lines and equipment used for discharging including slop tanks so that discharging is complete in all respects and the discharging efficiency is improved. There are two methods for final stripping and discharging, as given below. 1) Direct discharging method while stripping 2) Collection of oil first in the slop tank and then discharging 2. Disposal of oil remaining after discharging is completed (P6-6 to P6-9) A very small quantity of oil that could not be discharged used the stripping pump finally remains in the lines. After discharging is completed, this remaining oil should be drained to the cargo tank and disposed of. After disposal of the remaining oil, the liquid-sealed condition should be eliminated to prevent damage to the lines and valves. 2002/10 (Ver.1) (Discharging)6-1
2 1. Final stripping and discharging method 1.1 Final stripping and discharging using the stripping pump Pumps and lines finally used should be stripped using the stripping pump. Two discharging methods are available using the stripping pump, as described below. 1) Direct discharging while stripping (Short time is required) 2) Collection of oil first in the slop tank and then discharging it (Longer time is required) The time required by the stripping pump for stripping and discharging is about 30 minutes to 1 hour. The oil in the riser line should be allowed to remain until the end so that it can be used for "priming" the stripping pump. This is "a method of stripping oil sequentially from low locations to high locations." Here, the method of directly discharging the stripped oil is described. If however, there are terminals such as SPM where inclusion of gases is unavoidable (refer to "4. Gas purging of lines" on P2-26 of the "Discharging Section") or if there is uneasiness in directly discharging the cargo, then a firm decision should be made to adopt the method mentioned in 2). A bird's eye view plan of the pump room should be referred to so that relationships between lines can be thoroughly understood before stripping the pump room Direct discharging method while stripping (refer to "Fig. D-6-1 Line Diagram" on P2-35 of the "Documents Section.") The procedure given below for direct discharging while stripping should be implemented. 1) Make preparations for starting the stripping pump. Since a request has been made for preparations (at least one hour before the operation), at this stage, the steam pipes have been warmed up, and only the pump room side has to be drained. 2) Perform valve lineup in parallel with the preparations, such as draining out the stripping pump. 3) Valve lineup Crossover valve V331 (V332, V333 may be opened) Open Direct filling valve V311 (V312, V313 may be opened) Open Deck master valve V321 (V322, V323 may be opened) Open Crossover gas intake valve V388,V389 Open 4) Stripping of the No. 1 tank main line Stripping pump suction line V185,V188,V161,V164 Open 5) Discuss with the terminal and perform valve lineup of the stripping pump discharge line (port side manifold used). Stripping pump delivery line V168, V166, V352, V348, V344 Open Ensure open the delivery valve before operating the stripping pump. 6) If no head presuure is observed in the suction of the stripping pump, use the oil remaining in the riser of the No. 1 line for priming the pump. This means that all unused valves should be temporarily closed. 2002/10 (Ver.1) (Discharging)6-2
3 a) Stripping line valve V161 Close Pump delivery drain valve V521, V525 Open b) Prime the stripping pump. No. 1 pump delivery valve V113 Slightly open c) Test run the stripping pump locally at low speed. If there is no abnormality, shift to the CCR to operate the pump. (The stripping pump can be operated locally from the pump room.) The response to operate the pump may be slightly delayed since air is used for the control signal. Therefore take care not to turn the manual loader (manual setting device) excessively. The manual loader is a controller used to control the capacity manually when the stripping pump is operated remotely. If the manual loader is turned clockwise, the speed increases; if turned counterclockwise, the speed decreases and the pump stops. d) Confirm that the stripping pump is operating normally and then close V.113, V.521 and V ) With V.161 open, start stripping the No. 1 tank main line. Make sure that the number of strokes is in the range of 25 to 30 (about 160 to 200 m 3 /h). If the quantity of remaining oil is very small, it is more efficient to use a smaller number of strokes. The stroke rate rises steeply when gas is included, the discharge pressure reduces, and the steam chest pressure also reduces. At this stage, the stripping of the No. 1 tank main line is complete. Close the valves in this line. 8) Stripping of TCP Valves associated with V512, V511, V145, V524, V577, V578, V525 Open TCP line 9) Stripping the No. 1 pump Valves associated with No. 1 pump V521, V571, V572, V525 Open Open the delivery valve V113 of the No. 1 pump slowly and start stripping. In this case, a large head from the riser acts. 10) Other lines After the suction of the stripping pump approaches zero, strip the common line, eductor, TCP line and other pump room pipelines simultaneously. The slop tank should also be stripped, but practically no oil remains in the slop tank in a double hull tanker ship. 11) If gas is drawn in during the condition mentioned above, the stripping and discharging operations are completed. Confirmation of the dryness of the all cargo tanks should be obtained from terminal representative Collection of oil first in the slop tank and then discharging (refer to "Fig. D-6-2 Line Diagram" on P2-36 of the "Documents Section.") At terminals that prohibit entry of gas in submarine pipelines such as those of SPM, the final stripping of lines, pumps and other equipment should be carried out by gathering the liquid first in the slop tank and then discharging it all at once from the slop tank. In this case, the stripping pump has to be stopped the moment gas inclusion occurs and discharging should be terminated. This method is easy for priming the pump also, and there is not much cause for concern related to gas inclusion. Thus, it is a safe and sound method. The oil is gathered first in the slop tank, and the gathered oil is discharged through the MARPOL line. Only the differences between this method and the direct discharging method are mentioned here. 2002/10 (Ver.1) (Discharging)6-3
4 1) Gathering tank (assuming this is the port side slop tank) Recover the oil stripped from all lines, pumps, riser and deck lines in the slop tank. 2) Stripping sequence Strip oil from a low location to a high location. 3) Valve lineup Recover all the stripped oil in the port side slop tank. Valves associated with MARPOL V166, V352 Confirm closure line Stripping pump suction line V164 Open Stripping pump delivery line valve V168, V167, V183 Open 4) When gas is drawn in, change the priming line of the stripping pump and the suction line from the pump, use the oil accumulated in the slop tank and carry out the priming work. a) Suction line valve V161, V163, V525 Confirm closure Valve lineup from SLOP to V162, V164, V168, V167, V183 Open SLOP b) Operate the stripping pump. c) When the stripping pump operation is restored, close the slop tank valve, open the suction valve on the stripping tank side to be stripped and re-start the stripping operation. Slop tank valve V162 Close 5) Final discharging from the slop tank Pump the oil to shore through the MARPOL line. a) Notify the terminal about the final discharging operation and make preparations for discharging the oil to shore through the No. 1 manifold. b) Valve lineup Stripping pump suction valve V162, V164 Open Valves associated with V168, V166, V352, V348, V344 Open MARPOL line c) Final discharging Start the stripping pump and carry out final discharging. d) Completion of discharging A short while after the float in the slop tank touches the base point, gas will be drawn in. The discharging is completed at the point the gas starts being drawn into the suction line. At the same time, confirmation of the dryness of all cargo tanks should be obtained from terminal representative. 6) Stopping the stripping pump The stripping pump should be stopped immediately after gas inclusion is detected. Oil may remain in the delivery line, but this oil can be used as oil for priming the stripping pump when "tank stripping" is to be performed during the outward voyage. Accordingly, oil is left as-is in this discharge line with countermeasure for the liquid-sealed condition to be eliminated. 1.2 Precautions during operation of the stripping pump Click here to view video 044.mp4 Open the delivery valve and start the stripping pump. This means that it may not only open the pump delivery valve but it need to line up the delivery side properly. If the discharge valve is closed by mistake during the pump operation, the discharge pressure will rise abruptly and the relief valve will 2002/10 (Ver.1) (Discharging)6-4
5 activate. If the relief valve does not activate, the pump may be damaged. Therefore, adequate precautions are needed to ensure that the relief valve works properly. 1) Operation of the stripping pump When the stroke of the stripping pump is slow and large, it indicates that the pump is operating steadily. Under such conditions, if excessive negative pressure is not acting on the suction side and both discharge pressure and steam chest pressure are adequate for discharging the liquid, then this state of operation should be maintained. 2) Delay in the discharging time The stripping pump has adequate capacity to cope with small air inclusions. If the pump is operated with excessively small strokes fearing gas inclusion, the discharging time may be prolonged. 3) Large gas inclusion The stroke rate of the pump increases abruptly when a large amount of gas is drawn in. This condition can be identified from the drop in discharge pressure, steam chest pressure and zero suction pressure indicated by the various gauges. Reduce the stroke rate using the manual loader, and re-start the operation gently from the stopped position. If the pump is allowed to operate with rapid strokes, the piston stroke (travel) becomes shorter and the dry running phenomenon occurs, which has adverse effects on the pump. 4) Restoring the operation of the stripping pump The fastest method to restoring the operation of the stripping pump is to prime it using oil with a head. Generally, the oil in the riser is used for priming the pump. 5) Load and steam chest pressure The speed of the pump is expressed as the number of strokes per minute since the stripping pump is a reciprocating pump (piston pump). Even if the manual loader is used at the same position, when the suction pressure is strong, the number of strokes becomes small (large load at the same steam amount). Conversely, when the suction pressure goes from negative to near zero pressure (small load at the same steam amount), the number of strokes increases. In ships where the steam chest pressure can be read in the CCR, if this pressure is carefully monitored, it can be observed that the steam chest pressure is high when the load is large, and it decreases when the load becomes small. Thus, one can be judge whether a load is being applied or not on the pump from the CCR. 6) Others If oil is to be discharged using the MARPOL line, the No. 3 manifold is generally designed as the main manifold for the discharging. If manifold No. 1, 2 and 4 are assumed to be used for discharging, then a blank plate should be inserted in the No. 3 line. Thus, during the final discharging using the No. 1 manifold described until now, when oil passing through the No. 3 manifold line is stopped leaking outside by the blank plate at the end of the manifold. The frequency of usage of the manifold is high and the flange surface is likely to be damaged. Therefore, the flange surface and the condition of the gasket (renewed if necessary) should be adequately checked considering the discharging mode mentioned above. 2002/10 (Ver.1) (Discharging)6-5
6 2. Disposal of oil remaining after the discharging is completed Click here to view video 045.mp4 All the oil remaining in the deck lines should be drained to the tank and disposed of. The disposal of oil remaining at various locations is described below. 2.1 Draining the MARPOL line The method of eliminating the liquid-sealed condition in the MARPOL line is given below. 1) Handling of valves in the MARPOL line (when measures against liquid-sealed condition are implemented in the port side slop tank) Valves associated with MARPOL line V344, V348, V352 Close Valve lineup for draining remaining oil to V166, V167, V183 Open slop tank 2) Remaining oil Oil remains in the stripping line and also enters the No. 1 eductor through V Disposal of oil remaining in the Chiksan arm on the outer side of the gate valve 1) Confirming that the gate valve is fully open Confirm that the gate valve is fully closed when the discharging of oil with the pump is completed. 2) Drip line Although valve positions have been confirmed each time a different operation is performed, check that all the drip valves and the equalizer valves are fully closed. 3) Gas intake valve In principle, even if the gate valve is closed when it has been fully opened, no problem in particular will occur but it should be kept fully closed until necessary valve operation for the preparation of navigation has been completed. 4) The explanations below are given assuming that the Chiksan arm is connected to No. 1, 2 and 4 manifolds. Generally, oil is drained out and the remaining oil is disposed of from all lines except for the No. 1 line which is used finally. Open the outer drip valve and the drip master valve while communicating with the terminal. Outer drip valve and drip master valve V342, V344, V346, V362 Open The oil remaining in the Chiksan arm on shore is drained out to 3P with this valve lineup. However, if the equalizer valve is opened, the oil can be drained out faster. Equalizer valve V370, V378, V372, V374 Open 5) Disconnecting the Chiksan arm Before disconnecting the Chiksan arm, fully close the drip valve, the drip master valve and the equalizer valve. Place a drip pan of the half-cut drum at the connection of the Chiksan arm and then start the disconnecting work. 6) Inserting the blank plate of the manifold After disconnecting the Chiksan arm, check the flange surface, gate valve and the seat surface, perform simple cleaning, and then immediately insert the blank plate of the manifold to complete preparations for the voyage condition. All work other than disconnecting the Chiksan arm should be performed by the ship independently. 2002/10 (Ver.1) (Discharging)6-6
7 2.3 Draining out the oil remaining in the manifold cross line (Refer to "Fig. D-6-3 Line Diagram" on P2-37 of the "Documents Section.") 1) Open the port side inner drip valve and the master drip valve. Port side inner drip valve and V354, V356, V358, V360, V362 Open master drip valve 2) Open the crossover valve. Crossover valve V331, V332, V333 Open 3) Open the gas intake valve. Crossover gas intake valve V388, V389 Open 4) Open the valve on the starboard side after draining the manifold cross line on the port side. Finally, fully open the inner/outer drip valves and the master drip valve on both port and starboard sides. The equalizer valve may be open or closed, but when this line is used it should always be open. 5) Open the direct filling valve and the deck master valve. Direct filling valve V311, V312, V313 Open Deck master valve V321, V322, V323 Open 2.4 Draining out the oil remaining in the small diameter shore delivery pipeline 1) MARPOL line Valves associated with MARPOL line V352, V348 Open 2) The oil in the pump room should be drained out to the port side slop tank, as mentioned earlier, and the liquid-sealed condition should be eliminated. 2002/10 (Ver.1) (Discharging)6-7
8 3. Valve position at completion of discharging (Refer to "Fig. D-6-4 Line Diagram" on P2-38 and "Fig. D-6-5 Line Diagram" on P2-39 in the "Documents Section.) The valve should be opened with the main aim of eliminating the liquid-sealed condition of the line. The valve positions when discharging is completed (including COW line) are as given below. 1) Valves associated with the manifold Gate valve V302,V304,V306,V308,V301,V303,V305,V307 Close Crossover valve V331,V332,V333 Open Inner drip valve V354,V356,V358,V360,V353,V355,V357,V359 Open Outer drip valve V342,V344,V346,V348,V341,V343,V345,V347 Open Master drip valve V362,V361 Equalizer valve V370,V378,V372,V374,V376,V369,V377,V371, V373,V375 Open Open 2) Deck master valve V321,V322,V323 Open 3) Deck main line gas intake valve V381,V382,V383,V385,V386 Open or closed 4) Direct filling valve V311,V312,V313 Open 5) COW line Gas intake valve V M-3,V703 Open Drip valve V M-38,738 Open The COW sub main valve/cow machine valve should be opened after leaving the discharging port. 6) Tank main line All tank valves Close Line segregation valve V281,V282,V283,V284 *1. *1. Should be double shut or single shut. 7) Tank stripping line All tank valves Close Line segregation valve V285,V286 *2. *2. Connect the stripping line and main line, fill gas from the tank in this line to obtain positive 2002/10 (Ver.1) (Discharging)6-8
9 8) Pump room pressure and then close the line. Double shut should be changed to single shut. No. 1, 2, 3 and TCP suction valve V112,V122,V132,V143 Close No. 1, 2, 3 and TCP delivery valve V113,V123,V133,V145 Close Common line valve V151,V152,V153,V154 Close Stripping pump suction/delivery valve V164, V168 Open or close Stripping pump discharge line valve V166, V167, V183 Open Tank cleaning heater bypass valve V512 Open 2002/10 (Ver.1) (Discharging)6-9
10 Line Diagram Title Page D-6-1 Discharging - while final stripping 2-11 D-6-2 Discharging - after collection of oil 2-12 D-6-3 Draining - manifold cross line 2-13 D-6-4 Valve position at completion of discharging (1/2) 2-14 D-6-5 Valve position at completion of discharging (2/2) /10 (Ver.1) (Discharging)6-10
11 2002/10 (Ver.1) (Discharging)6-11
12 2002/10 (Ver.1) (Discharging)6-12
13 2002/10 (Ver.1) (Discharging)6-13
14 2002/10 (Ver.1) (Discharging)6-14
15 2002/10 (Ver.1) (Discharging)6-15
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