Document jBQ5J1rgdpkmoEDz95rmDmw2R

ADDENDUM TO THE OPERATING MANUAL FLUID CATALYTIC CRACKING UNIT PLANT 3B TEXACO INC. PUGET SOUND PLANT ESTIMATE 3910 BECHTEL INCORPORATED HOUSTON, TEXAS 1973 I WA-TEX 000864 TAPLE OF CONTENTS \ WA-TEX 000865 TABLE OF CONTENTS 1. Genera 1 Desc ript t on A. Introduction B. Basis of Design General C. Description ofAdditions $ Modifications Reactor Feed HeatSection 2. Control Features A. Principal Control Features B. Reactor Feed Heat Section C. Emergency Box Cooler 3. Preparation for Operation A. Introduction B. Drying the Reactor ChargeHeater h. Startup Procedure A. Introduction B. Steam Purge and TightnessTest C. Pressure With Fuel Gas D. Introduce Oil 5. Operating Variables A. Introduction B. Reactor Charge Heater Firing C. Heater Sootblowers D. Emergency Cooler Page No. I 1 ] I | 1 3 3 3 it 5 5 5 8 8 8 8 3 10 ]0 10 10 12 { WA-TEX 000866 6. Shutting Down Procedure A. Introduction 8. Heater Decoking 7. Appendix 7.1 Process and Utility Diagram 7.2 Vessel Drawings 7.3 Combustion Equipment 7 A Heat Exchangers 7.5 Pump Data and Curves 7.6 Instrument Data 13 13 13 WA-TEX 000867 1. GENERAL DESCRIPTION S.,*.**-.Tl- -->'- T-- JUVK.W*.-* 1 WA-TEX 000868 I - GENERAL DESCRIPTION A. INTRODUCTION This addendum to the Operating Manual for the Fluid Catalytic Cracking Unit at the Puget Sound Works of TEXACO Inc., Anacortes, Washington, covers the revamp of the FCC Unit. The principal new equipment for this revamp Is: Reactor Charge Heater Emergency Box Cooler Fresh Feed Pumps B. BASIS OF DESIGN . General The process design of the FCCU section is based on feeding 30,000 BPSO of hot fresh feed to the charge drum and feed preheat exchangers. Some 6,000 BPSD of hot intermediate recycle, gas oil are combined with the fresh feed for a total heater charge of 36,000 BPSD, The heater is designed for 750^ outlet temperature. The emergency box cooler is designed for 36,000 BPSD and 200F outlet temperature. Process flow conditions for the preheat section are shown on process flow diagram 3"RA_*f0. C. DESCRIPTION OF ADDITIONS AND MODIFICATIONS TO THE UNIT This section describes only additions and significant modifications to the FCC Unit. Reference should be made to the Operating Manual for the FCC Unit for a description of the existing facilities. Reactor Feed Heat Section (Reference PFD '3-RA-iiO) Hot gas oil from the Cxude Unit and Deasphalting Unit and/or cooi feed from storage are charged through the existing light gas oil-reactor feed exchanger, 3B-E4, and the existing slurry quench-reactor, feed exchanger, 3B-E5 AB. This stream is combined with the hot recycle gas oil and the combined stream is heated in the new reactor charge heater, 3B-F3. The preheated combined stream flows to the reactor feed riser. A new emergency box cooler is provided. Activation of the pushbutton, or low pressure drop across the spent or regenerated catalyst slide valve, will cause the valve in the line to the feed riser to close, the valve in the 1 WA-TEX 000869 oil line to the emergency box cooler, 3B-E40, to open, and the valve In the service water to the emergency box cooler, 3B-E*fO, to open. Hot reactor feed will be diverted from the feed riser, through the emergency box cooler, 3B-E*iO, and the cooled reactor feed flows either to the hot charge drum, 3B-C23, via 3L1C-62VB, or to storage via line 3B-0-1. 2 | WA-TEX 000870 CONTROL FEATURES ____________ . _________ _ / ->1 WA-TEX 000871 . - CONTROL FEATURES A. PRINCIPAL CONTROL FEATURES This section describes only additions and slgnlfcant modifications to the FCC Unit controls. Reference should be made to the Operating Manual for the FCC Unit for a description of existing controls. Reactor Feed Heat Section (Reference P$ID 3"RA-!i!) The fresh feed flow controller, 3FRC-30, and the recycle feed flow con trollers, 3FRC-11 and 3FRC-302, are left In place. Since a flow controll er, 3FIC-600, Is provided for the combined fresh feed and recycle streams, the flow controller for the fresh feed stream, or one of the recycle feed streams, must be taken out of service and the related control valve or bypass valve placed In the full open position. The fresh feed flow con troller, 3FRC-30, is, preferably, taken out of service as there is no danger of "starving" the combined fresh feed and recycle feed flow con troller, 3F1C-600, with the fresh feed flow controller out of service. Total feed to the feed riser is controlled upstream of the reactor charge heater, 3B-F3, by a master controller, 3FIC-600. The master controller, 3FIC-60Q, makes equal distribution of the charge to the six coils of the reactor charge heater, 3B-F3, by setting uniform rates on the individual coil flow controllers, 3FFIC-620, 3FFIC-621, 3FFIC-6.OI, 3FFIC-602, 3FFIC-603, and 3FFIC-604. Each heater coil is provided with a low flow switch, 3FSL-620, 3FSL-621, 3FSL-601, 3FSL-602, 3FSL-603, and 3FLS-604. Low flow through any heater coll will actuate common low flow alarm 3FAL-624. A further sustained reduction in flow through any heater coil will cause the fuel supply to the heater to shut off. A momentary reduction in flow through a heater coil will not cause the fuel supply to the heater to shut off, due to the action of time delay relay 3FY-622. Bypass switches 3FHS-620, 3FHS-621, 3FHS-601, 3FHS-602, 3FHS-603, and 3FHS-604 are pro vided to inhibit the heater fuel shutoff function of each low Flow switch. A selector switch, 3FHS-623, allows the flow through.any one heater coll to be recorded, 3FR-623. The combined oil oultet temperature from the reactor charge heater, 3&~F3, is on temperature control, 3TIC-302, by adjustment of the amount of fuel oil or fuel gas to the burners. A selector switch, 3US-606, provides a convenient means of firing fuel oil or fuel gas, or both. In this latter case, one fuel control valve, JPV-ih] or 3FV-606, is remotely positioned by a hand controller, 3H1C-606, to set a constant firing rate, while the other fuel control valve Is automatically positioned by the temperature controller, 3TIC-302, to trim thefirlng operation as required. 3 WA-TEX 000872 In Che event of a'power failure* the reactor charge heater outlet temper ature transmitter, 3TJ-302,. will be powered by batteries. If the batteries should fall or weaken, the output signal from the temperature transmitter, ' 3TT-302, will be low and high heater firing could result. A low tempera ture switch, 3TSL-302, Is provided to prevent this occurrence. If the out put signal from the temperature transmitter, 3TT-302, Is low, the low temperature switch, 3TSL-302, causes the output signal from the temperature controller, 3TIC-302, to be replaced by the output signal from the hand controller, 3HIC-302. With proper setting of the hand controller, 3HIC-302, high heater firing Is avoided. Emergency Box Cooler Low pressure drop across the spent catalyst slide valve, PdCL-JlfA, or low pressure drop across the regenerator catalyst slide valve, PdCL-l4B, or activation of the pushbutton will (1) close the riser Inlet valve, 3PdCL-lAVM, (2) close the recycle gas oil valve, 3FRC-1I, (3) close the slurry recycle valve 3FRC-302, (if) open the emergency box cooler process Inlet valve, 3PdCV-MtVB, (5) open the emergency box cooler water Inlet valve, 3PdCL-lAVM, (6) open the fresh feed pump discharge bypass yalve, 3PdCL--1AVH, to the blow down drum, (7) close the spent catalyst slide valves, 3PdCL-l4VF and 3PdCL-lAVG, (8) close the regenerated catalyst slide valves, 3PdCL-lIfVC and 3PdCL-lAVD, (9) open emergency steam valve, 3fdCL-l^VE, and (10) close slurry quench reactor feed exchangers temperature control valve 3PdCL-l4VK. A light cycly oil line is provided that ties In just downstream of the emergency box cooler process Inlet line block valve, 3PdCV-l4VB, to permit flushing of the emergency box cooler, BB-E^fO, when not in use. Flow of light cycle oil through this line is limited by a restricting orifice, 3F0-60B. k 1 WA-TEX 000873 ! \ffc-TEX 000874 3 - PREPARATIONS FOR OPERATIONS A. INTRODUCTION This section describes only those preparations for operations that are necessitated by the addition of the reactor charge heater, 3B-F3. Refer ence should be made to the Operating Manual for the FCCU for a general description of preparations for operations. B. DRYING THE REACTOR CHARGE HEATER The masonry In all heaters, firebrick, or refractory linings, must be dried by slow heating. Damage from cracking and expansion strains will occur If damp settings are heated too rapidly. The vendor's recommended drying procedure should be followed. An alternate procedure Is given below: 1. Check that the fuel gas system has been purged, and that it is blinded or otherwise secured against leakage of gas into the heater. Remove blinds in the gas supply header just prior to lighting burners. If natural gas is avail able, it should be used to dry out the heater. If fuel gas Is not available, fuel oil will be fired to dry out the heater. The fuel oil system must be thor oughly cleaned and charged with fuel oil. The fuel oil circulation should be established. Fuel oil temperature should be approximately 280F. 2. Break flanges at the oil coll outlets, venting them to atmosphere, or otherwise provide means for venting steam from the coils to the atmosphere. 3. Blowdown condensate drains on atomizing steam lines, snuffing steam lines, and coil steam lines. h. Purge the heater firebox with steam for at least 15 minutes, to eliminate all combustible gas from the fire box. The damper and air registers should be wide open. A steam plume should be readily noticeable from the top of the stack. 5. Light an alternate pattern of burners. During the drying period, rapid changes in temperature or highly localized temperature must be avoided. The lowest possible burner 5 I WA-TEX 000875 flame and maximum number of burners should be used for better heat ^distribution, while obtaining the desired temperature7 The burners should be alternated at hourly Intervals, for uniform heat distribution, and the performance of all burners should be verified. The purpose of the dryout Is to eliminate water from the furnace masonry. It follows that maximum ventila tion should be provided. The stack dampers should be fully open. All registers of unfired burners should be fully open. 6. During the drying period, the heater arch temperature Is used as the point of regulation. Raise the heater temperature at 50 to 75F per hour to 500F. Maintain at 500F for 2k hours. Increase the temperature at 50 to 75F per hour to 750F, Maintain at 750F for 2k hours. Increase the temperature at 50 to 75F per hour to 1000 F. At near 500F, steam should be carefully Introduced into the colls. Steam should not be introduced into the colls, particularly in vertically Installed colls, until temper atures have progressed above the steam condensation tem perature* Introduction of steam into cold coils will cause considerable "water hammer". The most accurate Indication of readiness of a furnace for operation Is the shell temperature. When the fires are started In a new furnace, the moisture of the outer surface of the refractory evaporates into the combustion gases, but much of the moisture held deeper In the refractory Is driven back Into the insulation next to the shell. During this period, the furnace shell remains cold. Then, as heat den sity In the combustion chamber Is increased, the lining heats through and the moisture frm the insulation begins to evaporate. This causes the furnace shell to heat up by the generation of steam on the adjacent insulation. When this moisture has been thoroughly evaporated, however, the shell temperature will again fall. If the operator keeps some progressive account of the shell temperature, he will note this rise and fall during the drying out process, and when the shell temperature has decreased to the rated casing temperature, the furnace can be considered ready for operation. 6 . WA-TEX 000876 The 100Q*F temperature may be maintained for a few hours* and then gradually.reduced at not more than 75F per hour. When the heater has cooled to about 35QF, the steam to the colls may be discontinued. The burners may be extin guished at about 300F, and further cooling continued by natural draft. 7. Upon completion of drying, the heater coils should be drained, blown out, and flanged up. Everything Is left In readiness for process operation. 8. After cooling of the heater, the masonry and Internals should be Inspected, and repairs made If Indicated. 7 j WA-TEX 000877 V' I" I WA-TEX 000878 U > STARTUP PROCEDURE A. INTRODUCTION The procedure given here Is for initial startup of the reactor charge heater, 3B-F3, and commissioning of the emergency cooler, 3B-El(0, with the existing FCCU In operation. Feed to the FCCU Is flowing through the reactor charge heater bypass line. Reference should be made to the Operating Manual for the FCCU for a description of the startup procedure for the existing FCCU. It Is assumed the reactor charge heater, 3B-F3, and the emergency cooler, 3B-E40, have been made ready for operation as described in the preceding Section III. It is assumed that all utilities are available and ready for service. The reactor charge heater, 3B-F3, and the emergency cooler, SB-E^O, are steam-purged, tightness-tested, and pressured with fuel gas. Reactor charge heater burners are lit on low fire. Oil is gradually diverted from the reactor charge heater bypass line through the reactor charge heater to the reactor riser. When all the oil is flowing through the heater, the feed rate and operating conditions should be adjusted to desired operating levels B. STEAM PURGE AND TIGHTNESS-TEST Introduce steam through the steamout connection at line 3B-0-20l|-10" and through the steamout connections ateach reactor charge heater pass. Purge through the reactor charge heater, 3B-F3, and the emergency cooler, 3B--E^iO. Vent steam and air at all high point vents. Drain condensate at all low point drains. When the system has been thoroughly purged, close vents and drains and tightness-test the system by gradually increas ing the pressure to 100 psig with steam. C. PRESSURE WITH FUEL GAS After a successful tightness test, reduce the steam pressure to about 15 psig. Make a temporary connection and pressure the system to about 25 psig with fuel gas while all steam to the system is discontinued. Drain steam condensate from all low point drains. Make sure that all steam condensate is drained, as hot oil Is to be Introduced Into the system. D. INTRODUCE OIL The emergency cooler, 3B-Elt0, Is flushed with light cycle oil. The emer gency dump system Is not put into service at this time. Valving should be arranged such that if relief valve 3PSV-127A operates. It can discharge to storage. 8 WA-TEX 000879 Light a few burners In the reactor charge heater, 3B-F3, and bring the flue gas temperature at"the arch to about 300F. With the master heater flow controller, 3FIC-600, on manual control and the heater pass flow control valves closed, slowly open the block valve in line 36-0-20^-10" and admit oil to the heater Inlet header. At this point, it should be recognized that hot oil Is introduced Into a wet system. The hot oil should be brought In slowly, and with caution. It must be remembered that a volume of water will expand to about I600~volumes of.steam when vaporized at 212F and at atmospheric pressure. This vaporization takes place with violent force and, when in a closed place, is capable of causing physical damage to piping and equipment. With the Individual pass flow controllers on manual control, slowly admit oil through the heater passes, one pass at a time, to the block valve in the heater discharge header, 3B-0-213-10". Open the block valve in line, 3B-0-215-8", to the emergency cooler and permit the hot oil to flow through the emergency cooler, through the jump over from the emergency cooler dis charge line to the emergency tankage (slops) header. After the system is free of water, close the block valve in line, 3B-0-215-8", to the emergency cooler and the block valve In the heater feed line, 3B-0-204-10". Open the block valve In the heater discharge line, 3B-0-219-6", and the block valve In the line to the emergency cooler and permit hot oil to back through the heater discharge Hhe and the emergency cooler to the slops header. After the heater discharge line Is free of water, close the block valve in the jump over line to the slops header and Isolate the emergency cooler. Close the Individual pass flow control valves. With the individual pass flow controllers receiving their set point from master flow controller 3FIC-600, and with master flow controller 3FIC-600 on manual control, slowly start oil flow through the reactor charge heater, 3B-F3, while reducing flow through the reactor charge heater by pass. Light additional burners and adjust firing as required to maintain the oil temperature to the reactor riser. Commission the emergency dump system to the emergency cooler, 3B-E^0. When all of the oil is passing through the reactor charge heater, 3B-F3, and the heater bypass is closed, place the heater outlet temperature controller, 3TIC-302, and the heater master flow controller, 3F1C-600, on automatic control. Note that when the heater master flow controller Is on automatic control, the fresh feed flow controller, 3FRC-30, or one of the recycle feed flow controllers, 3FRC-11 or 3FRC-302, must be taken out of service with the respective control valve or bypass valve In the open position. Adjust feed and recycle flow rates and operating conditions as directed by supervision. 9 WA-TEX 000880 ;` p ^ttr3~hrt-~7&rS` ' Ir^lcK-tT: 5. OPERATING VARIABLES WA-TEX 000881 i} - OPERATING VARIABLES A, INTRODUCTION Reference should be made to the Operating Manual for the FCCU for a des cription of the operating variables. The following discussion Is limited to the reactor charge heater, 3&-P3* B. REACTOR CHARGE HEATER FIRING Control the combined pass outlet temperature of the heater with tempera ture controller 3TIC-302, This controller resets the pressure controller regulating the fuel gas supply to the gas burners of the heater, or resets the flow controller regulating the fuel oil supply to the fuel oil burners of the heater. During reduced firing rates, it may be necessary to take burners out of service to maintain the design burner fuel gas pressure to avoid burner backfiring. Maintain the burner air and firebox pressure to obtain clear burner flame and the design excess air In the flue gasses. Burner firing must be even, so that there is no flame impingement on the tubes or furnace walls. Flame Impingement will cause localized hot spots, and coking or tube failure can result. Visual inspection of the tubes for hot spots must be done routinely, several times per shift. C. HEATER SOOTBLOWERS Electrically-driven rotary sootblowers are provided In the convection sec tion of the reactor charge heater, 3B-F3, for cleaning the extended surface tubes during oil firing operations. Steam Is used as the blowing medium. The sootblowers should be operated every 8 hours, or on Indication of higher stack gas temperature, when oil Is being fired. The sootblowers can be operated automatic-sequential or manually. The sootblowers are conveniently operated from the Vulcan EC-15 automatic-sequential controller. Automatic-Sequential Operation 1. Place the start-run-stop (S-R-S) selector switch In the stop position. 2. Mace the toggle switches In the up (auto) position. 3. Place the steam supply selector switch in the auto position. The steam supply valve, 3PV-658, will open. The adjustable time delay (15 min utes maximum) for .Warmup will run out before blower operation will be gin. High pressure switch 3PSH-658, downstream of the steam supply valve, must be satisfied before the sootblowers will sequence. IQ WA-TEX 000882 4. Place the start-run-stop (S-R-S) selector switch in the start position and hold momentarily, then release. The blowers will then operate in sequence. 5. On completion of the sootblowing cycle, the unit will shut down. Place the steam supply switch in the close position. Open the circuit breaker to remove power supply to the controller. Individual Manual Operation The sootblowers can be operated individually in any sequence from the Vulcan EC-15 automatic-sequential controller or from the sootblower location. 1. Perform steps 1 through 3 of the automatic-sequential operation pro cedure, or place the steam supply selector switch in the open position. 2. Manual operation of a sootblower from the controller is accomplished by depressing the three-way toggle switch for the desired sootblower. Blowing will stop when the selected blower completes its cycle, 3. Manual operation of a sootblower at the sootblbwer location is accom plished by operation of the pushbutton in the sootblower housing. 4. After manual operation, return the steam supply selector switch to the off position. Automatic-Sequential Controller In addition to the control and switching functions described above, the Vulcan EC-15 automatic-sequential controller has the following features: 1. A light labeled "CO" to indicate that the controller Is operating. 2. A light labeled "LV" to Indicate that power has been lost. 3. A light labeled "RF" to indicate that a sootblower has failed to rotate. 4. A light labeled "LHP'* to indicate that the steam header has not come up to pressure. 5. A light for each sootblower to indicate operation of that sootblower. 6. An ammeter to indicate the power consumption of the operating sootblower.. 11 ! WA-TEX 000883 D. EMERGENCY COOLER Valving In the piping to arid from the emergency cooler Is arranged such that oil can freely flow through the cooler to storage in the event emer gency valve 3PdCV-l4VB opens. During periods of cold weather, steam should be utilized to prevent freezing of water in the cooler. 1Z ( WA-TEX 000884 | 6. SHUTDOWN 1 PROCEDURE WA-TEX 000885 6 - SHUTTING PPWM PROCEDURE A. INTRODUCTION Reference should be made to the Operating Manual for the FCCU for a des cription of shutting down procedures. The following discussion Is limited to the reactor charge heater, 3B-F3, and the emergency cooler, 3B-E40. During normal shutdowns, firing of the reactor charge heater Is reduced as feed rate Is reduced and then discontinued. The heater Is steamed out in conjunction with the remainder of the FCCU. A procedure for heater decoking is given at the end of this section. During an emergency shutdown, firing of the reactor charge heater, 3B-F3, may be stopped by operation of emergency shutdown-switch 3HS-601. Oil feed may be diverted from the reactor riser to the emergency cooler, 3B-E4Q, by operation of the emergency pushbutton. B. HEATER DECOKING The FCCU need not necessarily be taken out of service for heater decoking. The FCCU can be returned to the operating mode that was used before the reactor charge heater was installed. The reactor charge heater can then be Isolated, purged with steam and decoked as described in the following paragraphs. After heater decoking, the heater is returned to service by the procedures given tn Section k.- Means are provided for steam-air decoking the tubes in the 3B-F3 reactor charge heater. The typical decoking manifolds are shown on P&ID 3"RA-4l. Internal coke deposition may be removed from heater tubes by steam-air decoking. This is accomplished in two consecutive operations. The spall ing operation is removal of coke by cracking and fragmentizing the coke by external heating of the tubes, and blowing the loosened coke from the colls The burning operation is removal of coke by controlled combustion, (i.e., burning,) of coke with air in the presence of steam, which carries the pro ducts of combustion from the coils. The decoking procedure is described in four steps: Preparation Coke Spa 11ing Coke Burning Cleanup Preparation 1. The tubes are steamed free of oil. In the normal manner, at shutdown. 2. The appropriate decoking manifold arrangement Is connected to the coils 13 WA-TEX 000886 h. Verify that all tube hangers and guides are present and in good con dition; if not, repair or replace as required before proceeding with decoking operations. 5. Verify that plant air, steam, and service water are available to the manifold. Spalling 1. Establish service water flows as quench water to the quench drum, 3B-Cl0. 2. The burners shall be lighted with nonluminous flames, if possible. It is advantageous to light the fires during the afternoon, so that the burning portion of the decoking operation can take place at night when red spots on the tubes can more easily be detected. Operate with a minimum amount of excess air, so as to reduce external tube oxida tion. 3. Establish steam flow through the coils. Initially, a high flow rate should be maintained to flush oil that may still be deposited on the coke. The rate will be decreased during coke spalling to prevent erosion by coke particles. it. Increase the bridgewall temperature at a rate of approximately 300F per hour to U00-1150F, with a maximum temperature of 1300F. 5. Increase steam flow through tha coll being decoked to produce a mass velocity of 18 pounds/square foot/second. 6. If spalling has not started at the above temperature, the following steps will be taken until spalling does start: a. Reverse the flow through the coil. b. Alternately decrease and increase steam flow. c. Lower flue gas temperature by 100-200*F. d. Add a small amount of air, for not more than 5 minutes, then be sure to close off the air. 7. The rate of spalling is determined by observing the quenched effluent. Spalling rate ts Judged by appearance of quench water stream. a. Light grey - containing soot or fine coke particles,. b. Dark grey to black - containing increased size and quantity of coke. 1& i WA-TEX 000887 8. When heavy spalling starts, decrease steam flow to prevent erosion. The amount of stearii flow rate is dependent on operator's judgment; the pressure in coll inlet and observation of the effluent is the guide. As effluent darkens, steam flow is decreased and Inlet pressure observed. As effluent becomes lighter, steam flow is increased and the observed inlet pressure may be a guide for flow . adjustment. High velocity may produce fine dust. This is deter mined by reducing steam flow for 10 to 15 minutes and observing the effluent. Should find dust continue, further reduce the steam flow to make sure the dust Is not produced by high velocity. 9. Continue spalling operation until assured that spalling has stopped. Burning 1. Reduce the radiant section flue gas outlet temperature about 50-1QOF. 2. Reduce the steam flew/ to produce a rate of 5650 LB/HR. 3. Gradually Introduce air to the colls at a quantity equal to one-tenth of the weight of the steam, i.e., 5650 LB/HR. Observe the appearance of the tubes. Do not permit the tubes* temperature to exceed I250-13O0F., i.e., dark red color. Decrease air flow, If necessary, to avoid high temperature. With a good coke burning operation, the progress of the burn can be observed by tube color. As the burning coke in the tube progresses, the tube temperature, hence red color, also progresses. Do not allow the tubes to attain a cherry red color. If the tempera ture rises, decrease the air flow. A. After about one hour of burning, the flow is reversed. If coke burn is heavy. It Is advisable to periodically increase the steam flow for short periods, to avoid plugging. 5. The effluent is observed throughout the burning operation. The appear ance of the effluent during spalling and burning indicates the progress. a. Greyish-milky Is the appearance before and after decoking. b. Light grey appearance indicates fine soot particles. c. Dark grey to black Indicates larger particle size and greater volume of coke. ' d. A reddish-brown color appears during coke burning and blowing out period. _ 15 WA-TEX 000888 6. When coke burning ts completed, the reddish-brown color disappears and decoking is completed. Cleanup ' L. Upon completion of coke burning, discontinue air flow. 2. Temporarily increase the steam flow to full line pressure. Hold for a few minutes, and then reverse In direction. Repeat this three or four times, to remove all loose ash and scale. 3. Maintain low steam flow and decrease firing at approximately 500F per hour rate, as indicated by radiant section outlet flue gas. When radiant tube metal temperature has dropped to 500F, stop steam flow. 4. At 400-450F radiant section outlet flue gas temperature, discontinue firing. Follow plant safety practices in discontinuing heater firing. Discontinue steam to tubes. 5. Flush the tubes thoroughly with service water. A hydrostatic test of the tubes may be made following the water flush. 6. Upon completion of the water wash, the tubes are dried. Re-estabilsh the air flow to remove water. Relight several burners to bring the radiant section flue gas temperature to around 400F. 7. Intermittently discontinue water quench and observe the blowoff line effluent, in this manner, it may be determined when coil is dry. 8. After completion of drying, discontinue heater firing. Follow the plant safety practices in discontinuing the heater firing. Stop air flow. 9. Disconnnect the decoking manifold from the heater colls. Replace the removable normal crossovers and swingout spools. Also turn the Figure 8 blinds to normal. The heater is made ready for normal service. 16 WA-TEX 000889 7. APPENDIX .... ' WA-TEX 000890 7. APPENDIX 7.1 Process and Utility Diagrams 7.2 Vessel Drawings 7.3 Combustion Equipment T.k Heat Exchangers 7.5 Pump Data and Curves 7.6 Instrument Data j WA-TEX 000891 WA-TEX 000892 TABLE OF CONTENTS SECTION 7.1 PROCESS AND UTILITY DIAGRAMS P&l D Reactor-Regenerator Section FCC Unit PSID Fractionation Section FCC Unit P&ID, Utility Water System FCCU S GRU PSID, Utility Stm. Cond. S Boiler Feed Water FCCU S GRU PSID, Utility Blowdown, Pumpout S Emergency Cooling FCCU s GRU PSID, utility Pit, Inst 6 Aeration Air, Fuel Oil & Gas FCCU S GRU Plot Plan FCCU 6 GRU Process Flow Diagram FCCU Unit Reactor Feed Heat and Emergency Cooling P&ID Feed Preheat FCCU Plot Plan FCCU Heater and Emergency Cooler Utility Usage Diagram FCCU Flag Flow Diagram FCCU Electrical Diagram FCCU - Single Line Diagram 3-RA-4 3-RA-5 3-RA-8 3-RA-9 3-RA-10 3-RA-1I 3-RA-1k 3-RA-AO 3-RA-iil 3-RA-42 3-RA-43 3-RA-44 3-AP-24 j WA-TEX 000893 ? 77T ;;V:'V'"*-* -iSFH P t HEW HUMilAS . .... is.. . we tit : loo* <410. AA *AT* VAIYT" -- ................................................... SIS 1 ttOO* ttlt. M> 4X11 YAVVA nri _ . ST4-U 1 tOOMCBI. 7.1. tl VALVI.Vt.JIkVntMEITtH Ho 9bO*WU NICK PLANS* Al''Q.r, a>e->i fcll'T* , IPO^HM.I.OATI vi4VAYv*.f..Ct\W IU t*..Bm Ul. !UN,iM.(Ntt ninw^mut. III M?. )M**ug.,.i<iui vtivi.Xi>'ii.>u.nieMo, .. >00*MtK.C.i.OAII VAlW.ttL'Hr. >. 1119 OS SB. ioo*EU*..t-*.6m vim.ti'ir, imoxx. ------ * Vobl 3ao*s.*vYT>AiN>i `Hu-i.f. loS r_T1 11 . LCGCMO soV.P. JPIPINa SV7HTI01 Jl . . *Tt,VALvft tf >-A)-" CHS6K VAbVH* aVOVR V<UNA. TSPBS*S!t?m" & Vxv| WM lUU MAS in imiV -X. ^mtSBLVALV* tctmnnjus 9 iium --X- cpwTRot valve (Hhc uaipyiuvtvn vmnriLiPYAtvi 0* HRRTIsaURlT <TIAM , A AIR. * 1C PSTAIV 'A* r^s?-- tnw w J P*|l4 L ivtai mit 10LS o LOCAL NAUHTIP TXANIMlYm UA*L Pmr.TAP H 80AI0 MftunTPQ TrRSAAKNVlMSSIttIFWRtTCDP k**RP ntmnUtt(iw.(Ht wrtttinmAiiLiui swmm*. HTTiUtr. ISA* ( uStCATiHS -*JUN*MtrT*l . IT"-- n*MT HOMMI A-- iHit 1VULNT IDtMTISICATJOM IWS7*UM*M| HOMHt INSTS'XLMCMT IDENTIFICATION ipr 1770 TI <41941 ilo+rt* HitPw im txrsuiiou 4Snlf Uk'kJi. .. whip <*v mi lUtHiiY'imH niHumntHgutt V4AU7 aIIImtIY*7TISH PUmimtVft'ltUH . 3oo*Jh.u- om v<wt.ut>`*MP.xtACUMw* **. ALLlHfTRUMBUtS APS COP)S IH Aeoft4MC* WITH |., A, TAMPAAfit tXClPT AS HOTIA line idEMTiFtCation BECHTEL ' tOOSS- fWACO Mr. 39>0 ----------'// / lit a.fy-fr-o- ^ SVMSOLS / EXISTING ' HEW REWOVt RELOCA.T* . .. .: hot used * o hot aimove; OCHOTES ftt*ni HUM0ISS - '. NOTES - REVISIONS Of MAJM 6Y5TCM& AAS OE^tfiHAT^ $Y THi SYMBOLS SHOWN ADOvS, MNM REVISIONS AR CIRCLED AMO IWCt-S* A , [ TRiAWCUtAR REVISE Aa.fe. . PjPiNG SERVICE SPfrCtFieATWU POA M(w/ [ LIKES 13 IN ACCORDANCE WITH 6CM$ J-2CBAfiUT . UNC HUMBER SUfFlKE* FOR INS^LATlOH oh NEW LINES AR IDENTIFIED A* POUOW*: PP* PERSONNEL PROTECTION l ( CC COLO CONSERVATION PttC- PARTIAL HEAT CONSERVATION 1 I RHC fW.L HEAT tONBERAVAtlcN / OOTTG** SGTPECARMATlTNRfrACTEfVDPtPATyftE CONTROL {\ Nt > NO INSULATION ' . REPLACE EXISTING O'UhE TO INLET A`PlStOH OPERATE VAVVe, 3PdCLl*fiWITH HEVI $CR PIPE 4/VAV4t&ft)CLtt.im, ExtSTlHB VAVY? SPdCL-M.V& WILL BtL mTALUD IH EMERGENCV COOUSA INLET UNE. SEE OWG, 3-RA*4l A, . push button ca low rwssuRE drop SISNAL AtftOSS THe SPENT CATALYST Ok CATA#$ }*L`Ot VALVE WAV AUTOMATICALLY j CLOSE INLCT VMVt TO RISER AND WILL PERFORM The FOLLOWIN'* ACTICHS $0WH ON owe*. 3<ftV4lt CHH PROCESS VALVE to fiMft6Sx&Y COOLER, OPEN -WATER VAlvS 19 EMERGENCY COOLER, CLOSE THE &WXXT REtTCLE CONTROL VALVE $ CLOSE RECYCLE A3 OIL TO 3B-F3 AT SFRC-i|. ^ I oooss. 'Oft >lta ua U 164 Ml 1>9 i* 4.* m 664 662 66T 611 fc<*7*U tu LlV*7-4l UGEND ITEM NUMBERS ACM BO BlAUvm PIPt 36*BtlCATie GTtlL PIPEVWAVL (AO'scro. mcbdu iyp vwm mvt ISO*B6fcO BtBUte ATl VAlVE WO'VW. r.l GAY* VAVVB lWbtMtOtK KkltUtlf VOttt 01 BO**l60 tv. GATt YAlV*.Xi,'CiF..>M4CXt.TE& (60-M.C.&. C.7. 0*72 V*Wt.&.`JL7.IWMU.TX.6 4 1*0* *t*0. fr4.0*72 VAVV4.KIP.MB.tlfO*!41 <0 kCOMLOO. 0.4,0*72 V*W4.<&,***. OUMI X2 |60*7L6A9fi>|*.J(M0 GATt VALV6 1 T J. 166*7140, C.2.0AT2 VAVV6.4CtF,7*C 90> 100*7166. (OUCKMO..OA16 VALVI.OIM. ret 600**660.7 4 614W47P VAfcVt.J*7. PU9 940 >IO**VOD. G9..UJB. HUB.&.'X,.W* OUt. 907 154**140. t.4., VUB.'PtOi.^CtX.. CtAt OUt. mot oos BOO^FVBP.C. -Y- 18*14W.STP.F, 1406 '4V0 iJOl IAM7V2 COOVt* Pit tWG *O.OVl$A IJC'ALSO 26U.6V7Tt7| IkPAHlIDU JOlUT.XfrX. IEQEMD --DO-- WVcMM/W . mtfo... --J*** --J-- PtPJUG SYMBOLS OAU VAIVi -- VPUTJClt AlulfrUtt ftlOftt V41VI -^3- Ptuo ceeu 6HUK VUvl HiKO COUrtMrVVUC > ttAMNIk *.4 TSRTSfSS: 7UI76IU7 trtlJUtt BBHttoV VtVVt imutvtiVKOsrtiirB 410.1/a linuetoriu ^L_ AVOU VJIVI -A- COMtAOV TALVt JL suMtuuf ciuiavvyt Hip uneimUvoKiMM _J 41*117 vnri iuou dnraetviui 4i9*At4M>vuiierav s Q feTma'iwjiw* INSTftUMEM tttAl ugUDTID (0*60 M5U-TW 70iHni viwi I*. ^ - wmwUJMT tiftUNi B746VA ttAM Slwtt SYMBOLS ' /iw t*A*!vma Biwti umiiamuiTtei Bifflwr1 HtCTOiCM. LUfi {APiUAtr rviiHa iw i eiiuT uAJlili /S7i\-- u$rsuiu? .&iHfmcATiew \Si_^/--- ifauw Ntfutu IWSTRUW6UT IDEUTIfICATJOM ` Alt tto74yU|Mf ** COM! Mt ACCOHOAMCl W>T* .. A. TAvO**6 U6t7 ABMO140. 702 fttVAV* tlPIU T &W4. N4. EOtA'4. T *>tg 206*7 k.lMCGt OIAMITI* 774V6 RUA FlAUOt 4902 UUE- IOUTl*lCAnOU 7*IN6AU.^J vn --7 III U.UHl9l9MV*i9. , rpA(p t9t, 9W) fcHATJKtf* y *e.ctMwPtib . ft&M'C.ATt $ hPSTh0Ut5H>P-TCifD'mNHOVTMi^MbO^v MOT&6 civi^.on* major wsrfcu* am i '9ftn&tlP bY rut SYMfcPL* SMOW* A&DYfc- UHUpft aevr4iPN> AM |fcCL$0 AND JHCUlDfe A TAiAMOUU^ MAftfc, ' PH**!* *R.v6* 4Ecpatiom^ rex uiw UN&5 *R$ V ft640ROAMi& VrttH 6EU4 J*C0 TS0V& 7 | Vine NO. $UPPl7tB PDR ifcpVVATION PN NtW ,,1V/B4peepAMApPflzOv^ltnpY<utinp?rttuD,i6PaZva*>TrOtrc(UrtipDhWB.: 1 Pu PARTIAL MtAt ADU6tavAY|ph Auc Ryu. UtAY e6U$&LVMtStt ' p4i7c p*tpU&S>Ai rTmiatctfoem$pc>rfcm*uuLcAkTeoeputepL. upiw-Vt.ATJDU " rv 04Vi6i9H4icfowJTf*O*CUftoOvft v*OfNwft,Pmft(fMttArrUcti*ftrrbMftNOPT Oft fttO,VJK.ftWo. Cfc.Y*,v<Vf .<bvvot VAUV. IV wvu. AUYOVkXT\CVA.\.n ClDftU VALVE 70 tMEftOEWOV COOLER CLOSE t)Al&YVMifc 70 ftvOtA \Vj tyNfc. t>*ftK**.OPCvi EMEft&EViftV eooLft.ft WAtan, VAyvft^ Cud^E. WP.'buj'W rsAvCaa. com- *r&o\_ VMM*. AMO CVOMl ftECMCVft <4\V, to A.T *7TRC,-V. I (U-tmitOI)--CM-U-K FIPtHQ 9YM50LS Pitt KOaEJUCK jwrftluwt'tm TAtift' pftiMKtW* rdvttA? uqoOOBdvuDWM* tUMOUMKUT tTMaoTt n UtAUY MftMjffO iklSTQUtUMT iPnifiTlUTiOM -->uf momma IDtMTfMHTIOtt |/-tUTfcUWHJ HtiUMtl Dm ioiijVi gt?at totT* 4--(!<.>>.firT fjpiKo (>. (6Kw'ru> VIMl lQIALUUHttR T*.aC*Cn.SuiamvrUaOtmltime.n)fttJ fUvir UBU^(CHTU) v>hisjU wuyA$EwttVmICftC. PSMOUAttoU fiqiHKiHt* WMLB Piah wtng nR.v)c'twAua~ PIW IHa-Uqm: loo*,e*t..h cbfcfc iubwmcrtin f.f..c,v gam HO* tOttAUftTAHtt ( eecHiet^toow TEXACO 54T. MlO SYMBOLS CXlMtHft mew R|M6v| RELOCATE N01 U5EO(OdH07 REMOVE) DtNOOV fit'tN HVMOCft) MOTES REVISION) OF MWOft SYSTEM) ARC DEStOHAteO OT THE SYMBOLS SHOWN KbOVfi. U1H0H OeVtSiOUS Art CIRCLED AMD IUCUUOS A TmAHOgLAR REVlSfOR MARK* . 1. Piping service specificatiom? for HEW ImES ARE IN ACCORPANCt WITH OEMS J 2Do TABLE 5. t(Nt HUMfttft SUrptXES FOR INSOUTttH ARE IPEMTIFIEO k% FOLLOWS: , PERSONNEL PROTECTIOti COLD C0M$ERVA1toM PARIIM, MfA CONSERVATION FULL MEAT CONSERVATION OPERATlMfi TeMPCRAIOtte COMtROL STEAM IRACEP HO IH2ULATI0H LIRE" VoKfltlPicAYioN ' Sfilf | | --INSIHMIOH A SIZE | IIOOUlwIMTS l-KOMttk [TStXlJAIVCtOCtPtMlHCwOlIKfAfttAWlfjfHlAt i O t. demotes tie-in numbers . DEMOTES PIPING. EOUH3MEMT+ " INSTRUMENTS ADDED OH C-IIHD, 1 ............ BtfEttlMCE CB4WIU01 FBJCtiSPt) o.ftUtloa l atciutBitiow icr.r(.u J.S4.* POOtlSTPti.o.tQicnouJiiou stcTfou.rc.6u. )>!> pooc&tt*ii.o,,w*tit witm $tqi*(muo nctiau.rtAJj gtll$Fl O..CoM?gtHi6M 9tCtlOU.es,MntOKUUiT c-nl-fr PttOCUSP<r.o.Aboft?iio ttdisu eA9Bit0u'UHiT *.04.T Pooe.Pip.pt*nHUTioMHiaMw<,5t<!vCwt:ecovvn P80l p.tl.p.wn VfATU MIUMIN1 MCIIOH.CCCAl 9AX*7 uotto F 0 0, CO. Wilt 3KT1PH.FCCO )>U>lt F0t* PCbAtCATALVOt *TOBAC0Ct; KC.C.U- >*IA1V rtto^fiue BOMtouc &fttfVTCfc tccx3yu,wAittj: oyo. J1-QA4 riafi PCOTC'CTIOH OYtBftU. 59.R*.| Sleains>Roer ir*ain O * nciim covounon UttfUMOMO IHI TXXAI COMPACT UTILITY P1PIUQ ClMSTftUMSMt OUORAM y/ATtd SYSTEM FCCU 4 049 RECOVERY UUIT 2525 3^RA-8I*1 I: S*R J0 H. CMHIO OWp K CIB N& PJ*1-0 A itstotATud TIU-Ih iv-ivotu/vt no w & s -A 7*V A $ iHfe AK*r>v.v. BEVir-COW'EQ DAAWIVG 3>AA*I08 REY.O cr ,JC -- Jf ik *V A ISSUED (OR COMSTRUCIIOH \ k )fe w A St npn^ncD to Jca mawap U5UID f6R APPROVAL <1 SK SB Im (HI ***** A At j* N A* suit i Mnnn BECHTEL HOVSIOH UTILITY PjPlH* ^INSTRUMENT DjACRAM WATER SYSTEM rceu ( cas recovery uhit mturn a Htto HfActm- Oft 3-RA-B* I2A WA-TEX 000896 i s-r o6b n c-rnio n zjws skt w*03-i-oa WA-TBX 000897 5E33> .LtSSIJO P1PIUC iTMitoi-l 4PICTU11 Ut rntfaulim iiutieCl UUL U0UUTXD >mo uouurio fciCHJit IOOP* SYMBOLS MW#'** .,, . (-A-&-A- l-O-O-O-O- EXISTING WEH BfcMOVfc BfcLOtAJfe NOT USfcO UXACO fcPT. 3*10 A 0 DENOTES tlfc'lN NOM&fcttS imtauMtxn ipujiiucxthhi & - film uo. - tti*MuMir ipiuwrtjmu - umtimmt u. tmliptuTi* titfioiT L_ ww mrmcmu trot ituusa, ittamviti eifiisuifjou flint until (u.aj iuhi ue- (8Kwm) lint tut ssavict pwomtioh utpukibbph).uauip ipoe i mi gi> PY Oil OAVAPOft.CATALYST PttfltlfY >r tttnu tiPtit4iri.nu>wAWt w WW1 W4TU ' pipiijo bpbci cic4ti o m~ :Voq.>.6ni, c. 'tj <ciq, mow. na*o.f. iflftriliJS.- 6J>*S J.6MM. yf cwt, AUtWAVa >,<< Sa* ee*w. auw*. S'- MOTfcS BfcVIStOW5 OF MMO? SYSTfeWSABS Ofc*lGMttEp| OY THE &YM&OU5 SWOPiU ^&OVE,MlNOB ntVlSlONS AJZt CIRCLED AK1D JMCWUDt A 7CIAWC.lN.Att CttVl&JOU MAttlt. PIPING SfeDVItt SfC<FIC*TtON* POC MW LIMES ARt H ACCOffDANCE WITH <3tM 4 CDS ume MUM&ee suppixts foc insula*?tow Attt ^IDENTIFIED A FOLLOWS! PP Ct m tUt Ore ST HI PiBSONfJfeU PCOTfcCT^ON COLD COMSfeOVATION PADTIAL HEAT CON6&BVATOW FULL Mft&r COWSEttVATIOM OP60ATIMG TEMPfe/ZATOBE CONTCOl &7&AM TILACErO KlO ISOLATION \ L<N IDENTIFICATION r? IA->L INSULATION AwUfc miz ITtKACO-* TfXJ IfQUlWHfNIS . HXACO MASS SMI UMUft StSVICL SNClMCAltON ITEM NUM&tllB &*1t VAiyi, jlHi jIMJ yMT>'.ii>JOlWT.Wrt* n-.nwmi H 1>T_ )*>U M.r4 Wl m* n* ~v y *., tAI*<V itnft> >uw un iwmitH jmt Vu. o DCNOTEG DENOTES PiMKG, EQUIPMENT I m^rWwSEMT* ADDED OH C*IUlO ttBgiatwci 6tiimn6i` muu * up iucmucpiwp mimic caiotm vt >utr?uatwtM.|to-.ftfwitMimj nut ittt<tBuwip<pima fmt wmrn. cm,uncim PSt4AUP.>imHioiJ3ICi iti guovmuw mem g,u.p.amncntr. gm at<o/ftt w pjcchu.uc. otn,t raumio m% w momy-ww HK.AIi.P.'Mil.l QMtfit, W<T>T|/CM.nBKPVlV Utit ' misTu* ouo/>uwmVw in. >.Uft.Lu<i6Ujtiawncun6tmi4 luttr uq,^ USl;B i.gl.g ORAWMO STATUS $t isMttiu // tovitLPAK csr. AtVlSKC) nfc HTtMAU 5***C erat*. it* p*k t^an tw. ut w I'M > 6v 'U) &v. >..>.m1o=rs'4!")p"a...v4.t.. ......J. 4? * & u fk s Mvvsit ?1 E S*"s* fticrnn cokPOiunoH 1AM HMKMOO S^taMtorar MOO___I-- iffMTO II M NM6 Twlffl* -MHT' PMCT fowl WCWTH* TlXA* COMPANY um.nr Pfdus tiujiftuHiur uuon/tu &iwoow. poupout (.imiogeuct toouuo nmD arnYuc muma uwir 2525 3-RA~i0lH S*R JOR. H*. C'MIIO OtfG. NO. ttilS AHT. J 5 A A 4 \ h JSo:ioum`^yT?4orr HK * Ox M & jc*tt | MtuMt HUM 74. > i>r s BECHTEL RESSBI TEXACO INC. TUOIT SPUMD NAHT UTILITY PIPING ^ INSTRUHEHT MAGftAU BLOWDOWN, PUHPOUT,^ MftCeNCY COOLING UUlt> CATALYTIC CRACKING UNIT Mcmi. hcw ituutn* >* 3-RA-IO 7A WA-TEX 000898 ion#iapvimt 4ig I0Q mm on t*w tu L*V UT. MiV JL LEGIMP ______ , .......... PiPWft OATI vnvt tncHcu ftuuo CUlOt ilLti r |tptaA? toncw^; WUJUtWWiWrW.-ntMgOl niif. yjuvt 4 uwy vawi mm umity mrioi wnnua.iifoM>tt iffiamB*SYMBi U(4i MttmtIO tMWMIfTW SA0 UfttftW j m MMHHA7ICH mVlU msra.ettuKOtuuftl Tiiafi^uMs^f ipm^ftciTToTT ,,ftMT WUHft .mioumuT MM*i*4ndw -iMjiooutur yuwiia ..uw tpcunncinou" - L----- f0tM WICIHC1WCU UUI JlOlAt uuustft ,, --------,. HniVwii <fc ilflVjet Fiugiuiion] ...........--., PUUT UWIWOKVJU) ______ UUI 9IU SgQVICt PtflltWATtOlj** fLAHT Alft, IHStftWtW AW < AtRATION Al*. rtttCwtOm 0A> ....... -1 - T/m.m PIPIU6 SPUmClTtOU Jj.M& | [* HW/0<Tlu6,itt/ watt. AUftW. j8^o iiio^B.R.^ ij'on," coaa him. zm. w> o.rea<K&. y ctma. uloyi $616 >QQ* R.P. 6ME6. Xo COQg.moW, f Jyit~T im*hqh. ITEM NUM&CClS7" znosssssLW^mH.'WWi'iSliSSWftV AT' m* ri&'o.c.&. am m.vt.waj. mnao. l.m, oau vaml o DENOTES m-m NUWBE* DENOTES P1PIM, EQUIPMENT 4 JHSTftUMENTS ADDED OH GrtlllO, titUXtl . 1009* StfM&PL* sxiatmo * Dm etw{jvt RetttiMe not uno* vo hot ftRWove Ttfc'lNWMMft* & leyinpx of wxjoz btstews au oe*l#KAttp CrV THE SVMfrpLiJ (SHOWN A&OV6, KiiHO*. ft.CVl4<C>rJ t*,t <5tEdtEt> '. AJ JWCkHPfc A TRlAU6iULA&ttftv1$ia>* MAK^. t. PiPlU4 6tftV(^9 r&<tPIAHPN to* N|W . UHEA ii Kue*ptod& vofM O&NS AA J*lDr ?A*U t, S. uwl Muwpta $u*itt6 4Oft IMEttl/kfloH AftE IDEHJIP?f7 A PotLC>W5> PP PftSOHMV P(t<9T&ftfsoH CC COLO C0N4(LVAT|0M PHD PARTIALM4AT COHSCftvAIIOhf FMC OTC >*t FUlU HEAT C0N4aVATIOH * OPtMTH6 TeuAfRATUHe COMtfcoU . M6AM TSLAfiftO `/ ttriiS' 3ssaai [`MSJ1'"I?IHS-3' __ iDiAllON tfoyiUMtHU noMK* s1IiExAvCicOt AreciHCMAAf7iOHhIATL WA-TEX 000899 ftEFEfiEN&E PaAWUGS^ >w>tm p.tii>.mmtftwiamiM ntr..r^.e.u.. VHUIY M LD.iftttK aYnW_F.C.C,l>. ljiiurr M LoTyu, ;wcn tooth mo watia F-t.c.0. WUTY P.I tp..a6ittgyw j pwpout fj^cvT" [ipnptoo<twmpP, it^c.gwmoiuw*tsHwaio. wf.c..c.ucx..Ww,dtt,uW VwPtt?* wirtsi mrnTinwr *c&ia |u o> y>>rey> i ft;* pmftwft iiyv pt^Pftu>mwi ttwi7WBicf.matc.wir UTmtV CWftlBUHW Stearns'Roger , -- WMHW* , O .. , KCHTtt COlPOJtWOH . WtlUWtM Itt* IfXAt COMMHT PUWtMWtWMID U71UTT PIPm0^1STQUtm DU6QAM PUHT, IWC5UWEWT i, AERAtlOM Al3 FUEL Oil ( OAft fccu4gj5 aieomY UUtT ' Imcwpm.jiva .II |.TkrxttwT-cua-rr ,I 2525 3-RA-Iit* s-k-dub h-c-iiiiu bw&.N.. eseis fttviitro itfe nmxt\wto0m4r9w,rcc*wMo". actifimnn * nW J5SUE0 fORCOltSlftOCTlOH % n aF M ssifsziSIS*5' \ (Ml &< BECHTEL HOVlfCW gSH TEXACO INC. . niOIT I0UH. HAM. UTILITY PIPING &'INST DIAGRAM PUT, INST & AERATION AIR FUEL OIL 8. GAS FCCU & GAS RECOVERY UNIT !U. WCfV nuaRT* mK 3-RA-ll MAJ H mcD^xBtx-iCzzDmm D*Cf Tfk^RmcUxrSivASffOeCNTUTtMrS*CaClWATKHD,SiSAKTrTATJ9SRCXSIPttAUsfrtaMlMt-tU-.A-'n-YmO-i*vi h _53?B'>CCDT 5B-8IO WSWAgaAbWsfhiTtWteK. MT*wrMA*aTu^tBreRsNrrTBaAdOtWtCmwSTwEpspPT*fOCtfChMi Mo*tpBm(bm EQUIPMENT LIST PLANTS- -4B Cl aedossso pu**MAMizfta - 4AbtyCe'Sa I 4&N<8I COLUMN' ' IZT. ~j)C6UfcAWJ?E& COLUMN ` `", 46 *e* 5Pu*rrfeB column . *" ` " 4B-C.B * OfTlAh* COAJDBnBATS PWLA.T <46*Cb 4B-CT 1 i2MnTOtaSTTAAgQS"B~6ilPPAOROATOTOOH`. '_^___,,_ WATER DSmepf POT' ' ____ 46-0/5 99*017 CAT>U3r RNB RORPnt 3 ' M'OIA RRItGA1cN-tEcRnAT0R: : ... si-os'. *.hrELAiMLXBaCHaUT.DRUL * " 33D6*G-cTm7 MS-btS'CtlTO McsSocEBonAwrB.LpoOTaoavAileiMreRNrILBoBUkuJWummP.oC"o.W--mN\kD\bR%UfiMt./M-.-. ^.l_aMUft-KA.ggr_______ 1 DOCTOR SOLUTION MIXING TANK frp-fcl I tA3 c5ErtPWa330n i oASGQttrxtsBon AyTcncootiy /Aw*pOUnawOmVi^^'o'iNOCADLNTTAWN) K ' tr 1 "ASoowghc^ oh. cooler r--I A&*tK5i*ftfyg.jf wiicoqim" .3MDi'Ctr2t ODHDttnbatc. storagb PH03FHAT7J-NUXINO- . i>\ AL-Lla-c-7 I tew pcc qjKPwwvgatcggugg^ V^t"4ftId" I ittCfrCTWN&E* OIL KIOILW#' coMwmsaoR ume ou. mAkeup . J4P*gEIPA_AB tar-d*-n- -nwet ovehheao coHwwtyiRa 0E6UTANI2B0 OCBOlLStf _ 3J>`RZ aa-ft4a&a**z*#a<* .MjimuMKtB (tuaux srm.tum.' FtPuRRwEESnIMHraTFeuUBiHDDeUlFfDsROnErKEtEX.eCAnhTAtRUNRO. AR.." . LMTi*SwJTrM*EE*U*ffToEuC: tAoSsOteLiCtO Oi.LiE'R . 44&&*Ci1i5a 4tt&. 44B0.-CII&I7 6tto ifujfea &M.towcMa finarn saw ftpLirtett otgotuno WAVY ftt GABO COOLER * u4W f& oAfo ctioi&h `"7"! 5tlACi CCUDt.OAS COMA T03 imhbitbr drum Mtknn I ' "aSDB-B-cSi"T" PtOfttACLn`O0fFMWTOERXBCOHTATHOAMESRCOOCBR. 46- _ib JiEAVV FGC gASGLtUC AP1CR. COOlCR 4S-E19 Ain ^TACC'tafOeUfiR^EtUMERTlffEira *36-132 Q"3SSE'BC.--KCDAiDEtS 'WnWsCfTt'B^T^M'r9e.*BzPoTD7ErXiuH.AEKiBcweRiiNjiiw: wWA.WST'BSWrwKTrCmni e.CeOjoOoLXSo* m.1lel ii 1 .'.-:. OC.ElWEHCy CDOLM CAL1 "T . AB*2tt<liA 3JIM*I1M>AI(SD rtUHE OIL BLilWft*SO' OUIL. jCCCOOCOOOLLLOWKKUB4X3I-XT+ lil XTH) *1.r 5B5*5FI^" A6I0AHMEA1TLCGRR ... . 6D&50 nRsH-.rcEo * * 1 V3.6bi^-oU-UeiSszaAaA J0FwqJru4lnu1xnMrnmfbfaclttDnt.a5WtJou.TA.sCBrHdl!Rta-n(fmx3ti!AxfWin^iWxusTOmpwa*w5rBeR*-Eai4Z!Tlj.* . iauaii-`5BSS UCOMrrM<OFNAOSjAOARILIt tSB-M 4JMt<_yT_J , RECYCLE AAS OIL ...... 41cr< 84 A' 54f.Bfi6-6.41CA JQ'GTA 4J>*0O. (a 44-fBi*`O6ial^l *`44SQ5^jl|A' (^h& [aB'CIS* !i4.6-A66tO<0l)O9A lAe6a5n.Q5gPOTWHG.Em6nfrlrggac5oPoAtJREIPLcip_c. COMdMeOwN S.P2AljRoEwte&fcGoTotjpf &cfleffbMacKMBiouSreEAu7uiHAig.TQrooEBpQloIKLoEnpEorALQPA'ffg-- COMMON SPARE. FOR OIO-4GII j| aPLITTCR BOTTOM^ *! COMMON. GPAftC FOR_o___j4_& so_; N* I CAUSTtG'ctHCmJ^lfr h*5 caustic cvfteuLxru*& wiwtor aiEMO iHJECTipH(pn<yoFrd . tCNOHMJBPIRICERSSCOIRRCTUULBAST,INCGOUP*C SlftHE 1 a^tuTaA BTTgMUATC^ WB CTL^PBgiCr.. T~ 2fe9m .a3Bin-Gw1iAI SOUR WATER t SPARE ' / *' "Vi'AftTJuE'rwBXTjMsKyemrrtautrpSr.icidNfede;<dspare cowmoti seNO.iiimXaB+Si !<B*GZI1ZIa` DCBUTAWIZGR RtFiUxGGPAREj ] corrosion inhibitor injection " cQRRosi'ofi iNUisnoR^KijECTipy DOCTOR SOLUTION ifottfiftK Lffra caustic1 cm&uL*rwa- AB-gEfe Mt 4- CAUSTIC CTBCUIATIHS oB^RnK JYA1TIEEAD3IEtH3TCT 5Tn>m1SMKE LUBE CtL * 1_ sJPtEawHl*of .MWSAESTAESWJUATlMEMRMSTSOAPEIWERmRXERALUFXlUn. ' iM.i_6_.Mft_' `VATLftlHjECTiftW fto iia-fcjt Mi CJCCTORA t CONOEHSIfes___ T'jaSPpaSaSr" _sjaas*--C-arMiol. . rScLcOiPnO6IwL.t'*"W)"5''P'wra*i5r: T APHHDcVmHwwAmTeEiUnfjceUcQtXinoonN. T..r.:.*.*.Y. PHOSPHATE IMIRCriOSL . .L. 3SBB'E-BHBt?fUSAa 'ulurnbse oeiLiCaiiw^rArs^tatiai'KsH`XAiSX. ..:*f`'' 1ST, STAftg GAS COMPfOASaX 4gB.-gK1^Br fWiHfeaC HP. STA&g. OAS COMPfCBOSOR iEaRstSN^mfopfmi^fCrciCMHrioiLHCcftvRb^tl~m ~SUTANe KEFWgeWggWKPffiseR sibfnfoA lvbj^. oil ienme. ces*ke) ......*SB-2IA. CO BOILER WASH WATER * : *81>MS SRfOENlMrS. RKTURN - ' NOTE t ALL HOftCUNTAL VE6EL3- ARE LOCATED TO SEAM-UMB. OTt-OPVgfiSgt. DOUR GAS. ICO. DRUM PUMPOUT L6B.-M-I * B8B4-Kkal JUKBJECTDED i COHDEKSHRET * .lMU-APITN AAIRIR BBLLOWWKERR ,1 wk*13a 'JTHKE0 DRAFT PAN ( BJAjIE ` 3-Ti ELEVATOR (r.C.C.TEUCTm) . a3aofai-*e-ctiaais* : JPoOhCnUsoHnefircOotfwARAGPE DfttIM 4&>K1A tf%0. POT - jRSB^'i^3^V!Widi;eii .m.o.w.n....... . 01* *JII__ .. -.... -i. r*** Utctfto puma> m, tiotwrep* * iMAtt rVtO`-0*}lWWi T z BECHTEL CORPORATION V5I iAH rbutoieo IIi | ?S THt TEXAS COMPANY CA3*tX>TeCrfP7p,MC0QMOi>POmlV43NLT't>ALSSXV0CUJ0. JVS5:'tdlLb.>JCbtf->tl4O-.nx; AA'iS.^ft'Kl.rfAgXAAfi'CU, n* won sound worn PLOT PLAN 4ft-tU,4S<,II |46.etLAPD* &PM*A4 1 Si IRUID CAT CRACKER < CA3 KCQVTCY UWS te^rCnftfcwwc^-Nwei'TPOpM m ii(__*__&_._4__t_UitMn ^SiLiiAmu-itt `rmCHLfrflKtKAAlOfcKMOusrvixNtm?. mvasiKJVT <,iW--B------ft 252S JbBflSM 5 A mrri Hi UMA!TSD PWAPfe Hi p i1 1 l65pD fioft CPKKT&CPOR np5ENpTPBOETSAfPAPPAvC8M3QUT. " n1 'U1 iUsuis-- . E Xr Bf ft 'OkuM w5jqnmn |4 *# BECHTEL Iie^H TEXACO INC. S5 *mf29&* WJBtr SOUND KANT ` PLOT PLAW ' FLUID CATCEACKK4SAS KCCVERYUNIT KOm - K3ff hilf 3-RA-I4 m WA-TEX 000900 -C SERVICE WATER CIZ> TO STORAGE DR P()CL I4A8B !LZZ> H--------------- > -tZZ> TO FEED RISER TO LIGHT CAS OIL PRODUCT COOLERS TO FRACTIONATOR NOTES. L THIS FC(NEW1 CONTROLS TOTAL FLOW BY RESETTING INDIVIDUAL HEATER COIL FLOW CONTROLLERS (NEW) NORMAL OPERATION WITH 250 B/H ICCO RECYCLE AND NO HCCO RECYCLE. ALTERNATE CASE WITH 250 B^l HCGO RECYCLE AND NO ICCO RECYCLE. 3.PUSHBUTTON OR LOW IRE DROP SIGNAL ACROSS THE SPENT OR REGENERATED CATADSL SUCK *" AUtwvmcAuy eras \alves in lines to EMERGENCY COOLER ANO CL0SE8 INLET VALVE TO RISER. THE EXISTING VALVE AT THE RISER WILL BE RELOCATED AS THE EMERGENCY COOLER VALVE AND A NEW VALVE WILL BE INSTALLED AT THE RISER. 4. NORMAL OPERATION-HOT rfitiO PROM CRUDE AND DEASPHALTING UNITS. ALTERNATE' OPERATION- COLD FEED FROM STORAGE. 5. STREAM ? PROPERTIES ARE FROM TEXACO TEST RUN. 6. STREAM 8 PROPERTIES ARE FROM TEXACO'S NEW DESIGN. . SYMBOLS ......... -........... existiNo tVMWV HEW REMOVE RELOCATE 0 0 0 0 0 not USED DO NOT REMOVE 7\<jf7Xt' *ieflac i i i 4 ) WA-TEX 000901 A, PIPING S'. -tm- GATE VALVE (SEE MOTE 2) GLOBE VALVE , ---- -ASb CHECK VALVE BUTTERFLY VALVE -- ANGLE VALVE -Ph- gggE SAFETY a ' BAU.-VALVEJ T WflHAHV Ptiocew UHS ntonmet PtIEUMATTC INSTRUMENT LIRE m&ruNE' VTYPE STRAINER CONE TYPE STRAINER C&5TOR SIAITOOWN BLIP OR MAINTENANCE BUND ' UTILITY LEGEND -------;----r~"------------- AP PLANT AIR AS STARTING AIR 00tf SEWER- OILY WATER Of gas refinery fuel Ip INSTRUMENT air supply Of OIL FUEL HI TO FLARE DRUM S250 250* STEAM S40 AO* STEAM StSSO E50" STEAM CONDENSATE Wf WATER-SERVICE OPERATIONAL T OR SPECTACLE BLIND OPEN DRAIN HUB FOR COMPLETE LIST OP INSTRUMENT SYMBOLS, REFER,TO TEXACO 3TAHDAR0 DRAWINGKIB'ITBP, J*-7d*. AMO 13-1791 NOTES LOCATE TOGETHER. HEATER OECOKlNG SEE DETAIL X OT'PUai DUTTON ORLOW PRESSURE DROP SIGNAL ACCROSS THE SPENT CATALYST OR REGENERATOR CATALYST SUOE VALVE WILL AUTOMATICALLY OPEN VALVE TO EMER6ENCY COOLER, CLOSE INLET VALVE TO RISER SHOWN ON DWG. 3-RA-A, OPEN EMERGENCY! COOLER WATER SHUTOFF VALVE, CLOSE THE SLURRY RECYCLE CONTROL VALVE ANO CLOSE RECYCLE <3A5 oil to ajs-jF9 atsprc-ii, _ RS3SfEB(BfmG^crRi^TSLEr valve 3 PE CL 14VB AS CLOSE TO TEE AS POSSIBLE, PIPE PROM TEE TO VALVE TO BE 9 CR 5. CAN USE EXISTING TURBINE 3B-GTIA C. ADJUSTABLE ORIFICE IN PNEUMATIC LINE TO EFFECT SLOW OPENINB ANO CL03ING OF VALVE 3PJ CL I4V-M. 7. ANGLE OF INTERSECTION SHOULD BE 4B OR LESS 8. REPLACE EXI3TIN0 FCC INLET PIPINP WITH BCR IPE I BECHTEL - I0O9S TEXACO EST. -30)0 O-O-O O" SYMBOLS EXISTING NEW REMOVE RELOCATE NOT USED LDO NOT remove; DENOTES TIE-IN NUMBERS NOTES - IgA REVISIONS OF MAJOR SYSTEMS ARE DESIGNATED I / BY THE SYMBOLS SHOWN ABOVE. MINOR ` (revisions are circled and include a ! triangular revision mark. ;I6./Plpm& SERVICE SPECIFICATIONS FpR Nevy Junes are in accordance with sems U-SDB TABLE 7. 17.] LINE NUMBER SUFFIXES FOR INSULATION 'ARE IDENTIFIED AS FOLLOWS* PP PERSONNEL PROTECTION CC COLO CONSERVATION PHC PARTIAL HEAT' CONSERVATION FHC FULL HEAT CONSERVATION OTC ' ST Nl OPERATIN& TEMPERATURE CONTROL STEAM TRACED ' NO INSULATION A LINE IDENTIFICATION INSULATION KltW REQUIREMENTS , .TEXACO PIPING MATERIAL mUMMR SERVICE SPECIFICATION -More 4 70. 3B-: - T3T 3S-.iT-1 3B-.7-L 3B-S.TM1 3S-:,7-5t . 3B-J7-LW 3B- -usx-lrt SFTM9'9"9 Mrwwr 0B0CllT7ON REVISIONS 10. LINE NUMBER SUFFIXES FOR INSULATION ARE IDENTIFIED AS FOLLOWS: PP - PERSONNEL PROTECTION - CO - OOLO CONSERVATION PHC - PARTIAL HEAT CONSERVATION . FHC - FULL HEAT CONSERVATION ' OTC - OPERATING TEMPERATURECONTROL ST - STEAM TRACED 0 INSULATED HI - NO INSULATION II UNLESS OTHERWISE SPECIFIED,THE VALVE SELECTION SHALL BE BY THE CONTRACTOR OEMS, ` E REFER TO OEMS J-IO, PARA.BI3 FOR TEXACO'S PHILOSOPHY WITH REGARDS TO BLINDS TO BE SUPPLIED BY THE CONTRACTOR. PARTICULAR ATTENTION SHOULD BE GIVEN TO THE MODIFICATION OF PARA.SI3.1 WHICH COVERS SHUTDOWN BLINDS. 13, RELIEF VALVES 3-PSV.74ft75 REQUIRE 'P' SEE ORIFICE 14. TRANSFER LINE PRESSURE DROP MUST BE CHECKED BY CONTRACTOR AFTER HEATER SELECTION HAS SEEN MADE NOTICE w<W*<S!*f&Wuwt eayuiji*SSS5wlo*4lob'ahp*?*!?'T>,tA*oS*El2t/Yk TEXACO me. ENGINEERING DEPARTMENT HOUSTON, TtXAS ENGINEERING FLOW DIAGRAM FEED PREHEAT FLUID CATALYTIC CRACKING UNIT nmrHJH) tmetmrr HUMUAAWIO tuow *tca*9 i 3-RA-4I A,;--- I.C A % JOU UWS* tt-Q-ZtSodA vi-il 'KeviiUD fPISUL.lWCKNBLi' LINES i*v?n. NOT*AlPQEP`OT**7P ^u-A0SU9 IN*. 4HIC*US' A fTZK> CHAN&Bp 3P3PV*WY-H, AA AettTO JW&-/4V/S a 'Elwslb pk"pjj<S 3sAAr.litL.Rww. -ta a Vviiew F- CU%. VMl>Yi\ `fy,. Rev^A fl.V5V4bir\> PU<t> pwtt A REVISED PER DRAWING A zm 3-AA-T41 - REV. O HI. *C A A 7* A ISSUED FOR CONSTRUCTION 28m<> 3ib&Efifc&iVr *9 to COOMS^<4S W CMfiTr HTIW M'/I0671 ML 0M llnWUM > ataut HOWS ( OEBIKID BECHTEL HOUSTON TA. >* %th %Tff- p *V WJ ft T<*if, u fir % *a $ % jc * tAl ifT ft rt sst u*r*n.. TEXACO INC. PUGET SOUND PLANT PROCESS PIPING &1NST. DIAGRAM FEED PREHEAT FLUID CATALYTIC CRACKING UNIT V ) * rnicscn- SRW 3-RA-4I WA-TEX 000902 EQUIPMENT LIST 38*&40 EMERGENCY COOLER ' S8-F3 , REACTOR CHAROE HEATER N 3B-C40 QUENCH DRUM i <? WA-TEX 000903 ter BBSST -------- TEXACO me. [TEXACO] engineering department (TEXACC HoDttOH, TEXAS DEIHITEL a tem% ino. PLOT PLAN rccu HEATER a EMERGENCY COOLER WOET tOUHD ftAHT PLOT PLAN . ; FCCU HEATER $ EMERGENCY COOLEHl nuxANxDttA4tiORib ,. . . TAAQHa RECORD EKTCRXS 3-AA*4 1 IWHIIl- TcufaoT- 3919 m3"*RA"42' 6" iMAij seat 1--* BLOWERS 3&-P3 16.46 1 LEGEND 1 2 | / - nonmL operation fww 3 WATER on FUEL GAS, g-normal operatton f/rwo heater on fuel on., ' 3- SPAKE FRESH PESO PUMP ' OPERATING, C temp -r OESIGN-OECOK/Ntt OPERATION ACL FIGURES /At tOOO */HR. EXCEPT AS t/OTEP ' 5Z> OECOXWG WNIFOLD 3&<F3 -Oit.i) 230'F 2.0 t 2.01 'GGOKtbJG WUM P j __/oov 1&-CAQ > A <4 Aj {39URP FOR INFORMATION faA ISSUED FOR BMSW M* bum HhUm X HJL & h n rtt. ft * DU 6ft u. $Un**. tCAtE 1 flismsw " ORAM BECHTEL > tiguwpN INC. NIQET SOUND KANT UTILITY USAGE DIAGRAM FCCU UNIT ` PLANT 30 timtt- vox tixAcom- to 3-RA-4 3 IA WA-TEX 000904 IfL (otesv^T n| NFLOW . ' j Ji i drainage DITCH JL SERVICE WATER TO STORAGE FROM PUSHBUTTON OR PdCL WARD (NOTE 3) I (NOTE 3) /7\ ............ w LIGHT CAS OIL Of flPSD 6400 TO FEED RISER TO UCIIT CAS OIL PRODUCT COOLERS 3* TO FRACTIONATOR -v SLURRY -TO CAS RECOVERY -S UNIT RESOILCR D * NOTEit - l THIS FCINEW) CONTROLS TOTAL FLOW BY RESETTING WQWIWAL HEATER COIL FLOW'CONTROLLERMNSW) . . NORMAL OPERATION WITH Z50 B/H ICOO RECYCLE AM) NO HCCO RECYCLE. ALTERNATE CASE WITH 250 B/H .HCGO RECYCLE ANO NO ICOO RECYCLE. ' * 3. PUSHBUTTON OR LOW PRESSURE PROP SIGNAL ACROSS THE SPENT OR RECEWHfttD CATAWSt SUE WJTOMWlCAUY CffiNSNAtYES iHtMS TO fl..f.f..i...E...&.. tCrYiNSCOVOALWERE AND CLOSES INLET VALVE TO RISER. AT THE RISER WILL BE RELOCATED AS THE EM..E..R..G...E..N..C...Y.....C..O...O..L..E...R...V...A..L..V..E. AJ NO A HEW VALVE WILL BE INSTALLED AT THE RISER. . ` < NORMAL OPERATION-HOT FEED FROM CRUDE AHb OEA9PHALT1NO UNITS. ALTERNATE OPERATION- QOLP FEED FROM STORAGE. 9. STREAM 7 PROPERTIES ARE FROM TEXACO TEST RUN. ' 6.STREAM * PROPERTIES ARE FROM TEXACtfS NEW DESIGN. TVTl LOCATED ON LCGO STftmft OUTLET WA-TEX 000905 A A A 0 A tSk "Hi m. m SCAIE /$$VP FOR. % ICl ISSUED FOR APPROVAL Iff tl . ft5 >* 04A dm K. JMs | 0BJBXSD BMW BEOHTEi TEXACO INC, fUCfcT SOUND PLANT FLAG flow DIAGRAM REACTOR FEED HEAT AND EMERGENCY COOLING FCC UNIT HM. * rtUlU* WW4 uutow- Mi* *1M. 3-RA-44 tH+. IA WA-TEX 0009Q6 .... -- 1 "'--r- ,TTfr- 7.2 VESSEL DRAWINGS' i i WA-TEX 000907 .r-cia-j TABLE OF CONTENTS SECTION 7*2 VESSEL DRAWINGS Decoking Quench Drum - 3B-C4D 3-DC-AO i I WA-TEX 000908 $ZE D I WA-TEX 000910 TABLE OF CONTENTS SECTION 7*3 COMBUSTION EQUIPMENT Data Sheet for 3B-F3 3B-F3 General Arrangement Combination 011 and Gas Burner V. P. 10095-F-01 -HAC-ltO-S V.P.IQ095-F-01-MAC-67-2 I WA-TEX 000911 t This draw ing and (he design it covers are the property of 8ECH1 fcL. They are merely loaned and on the borrow er's express agreem ent th a t in e y w ill n o t be reproduced, copied loaned, exhibited, or used except in the lim ited way and private use perm itted by any w ritte n consent given by the lender to the borrower. FIRED HEATER DATA SHEET Customer tei^ccl me, ManutacmiierJ^TFR. WttEJEFE-SlC o ft P Locution PUCiET Se>Q>iP . PuKhlT....... ................ Unit FC.CU KXPKMS1QN Service RekCTOr , Ch.A. _BliKT-------- Equip. Noi.JkR.=_F3 .... Raq.No___ JO_pS>5,,'. F-OI ItamNo_______ .... %.--, .... . Number Required . ____ C?..bl-------------------------------- Total Duty par Heater. MM Btu par Hr Absorbed---------- _____ Typa___ y. &i,q _____ .. - ' Heatar Section PROCESS DESIGN CONDITIONS ......................................... ................................................................................... R^lfe^T Com Vc.~no4 ' Service ........................................................................................................................... * Heat Absorption. MM Btu par Hr.............................................................................. SsL'Q- Fluid ......................................................................................................................... .. .ftifetSLAlLk. ' Flow Rate. Lb par Hr.......................... .................................................. .................................&3&+SJU_______ Flow.Rate. BPD .............................................................. ........................................... ............. ............................................ * Pressure Drop, pei (Allowable)........................................................................................... ^,0 ( Pressure Drop, psi ICalculatad) .. .ft !-&AN. ....................................... ..........1 &.Z-AQ---------- * Average Flux Density. Btu par Hr par Sq Ft (Allow*ble)/tCalculat*d)..........................I^QOO/j'ZQQO Maximum Flux Density, Btu par Hr car Sq Ft (AI!oweble)/(Ca!culatad)..................... .............. ---4---------------- -Z Velocity Limitation ............................................................... ......................................................................... . --------Maximum Inside Film Temperature. Deg F lAltowsbiel/ICalculated)............. ........... .....- -Z__________ Fouling Factor.................................................................. .......................... ............. .. ................. ., Corrosion or Erosion Characteristics...................................................... .............................. --------------------------------- . Inlet Conditions `Temparatuie. Deg F........................................................................................................... ...........SJ2J------------ * Pressure, (psiaj. (psig).................................... ..................................................................... ..............70 (O 'Liquid Flow. Lb per Hr ......................................................................................................... ... ------------------------------------ `Vapor Flow, Lb per Hr ............................................................................................... 1 Liquid. (Deg API) (Sp Or at 60 F)........................................................................... ZS.4 'Vapor. Molecular Weight.................................................................................................. ....................... ` Liquid Viscosity. Cp........................................................................... ............................................Q_5-4*. Outlet Conditions; ' temperature, Deg Is . ' Pressuie. (psig) * Liquid Flow. Lb per Hr .. . . ,, * Vapor Flow. Lb per Hr .. .. . * Liquid. 10*9 API) (Sp Gr at 60 F) 'Vapor. Molecular Weight * Liquid Viscosity, Cp ....................................... .................................................................... 75Q 52 473^71 O.R-4. _________ Remarks and Special Requirements; * 1, Distillation Data or Composition Attached....................................... ...................... . ............ ,, 2 SaLutts Pee&'EiUitc >*0** C.M.c.outa.-r\e>M& Skau. Klo-r TAvig. C ate pit Fog STtortc. Wtati Berv/sEM Hekt-er 1mu.et. Ou-rugT Items Te Designated Te t Fills* It ly l)tr t, &>. p, 4QQ * F 2*V*-n OftMtgbA. 4^ 4-Kt VL l^idSb Fok /Sh. Fob. Ho DATE OMOIN RjtacwKfce Foil CpM1sTR.VC.TioM...... . REVlttONS 75LTA-t "V& y za~ Mi W/?...... / CM* . JOB Ha IOO >S DXJyeiwGHo REV OS- 3* F-1 *L WA-TEX 000912 sain t Co MECHANICAL DESIGN CONDITIONS General Plot limitations * Tube limitations 'Required Drawings Structural Design Data: Wind Load_______________ ' List ol Applicable Standards or Specifications: t. 2. Coil Design " -Heater Section:RA.PIA'Fa'r ' Slack Umitenona Other Umitaliona SelemT* 7eler 3. 4. KrTtscWKSMT C.OHVeCTIOH _ ' Service ............................................................. ....:...................................... .... Design Pressure, psig .......................................................................................... Design Fluid Temperature. DegF .................................................................. Corrosion Allowance: Tube*__ _-- Fitting*....................... ........................................... ,.. Hydrostatic Test Pressure, psig ........................................................................... Number of Pssses/Tube* per pas*................................................................... Overall Tube Length. Ft........................................................................................ Effective Tube Length, Ft .......................... .............................................. Bare Tubes: Number ............................ ................................................ .. Total Exposed Surface. Sq Ft........................ *.................... Extended Surface Tube*: Number .......................... ...................... .................. Total Exposed Surface, Sq. Ft..................................................... Tube Spacing. Center to Canter, In. (Staggered! (In One!........................... Tube Center to Furnace Wall, In. Min............ .................................................. Stress Believe.......... ............................................................................................... Weld Inspection Requirements..*-Bay or Other 1...................................... Psocs.sa 150 750 1 -- ........ ................... >'&* .......... 550 U /IS* A / 11 . 3 3'- C6 341- Ca 2.7C=> IGs1- O is. 4.,(2sO 551 54*- li.ooo Cb Ysa - 141 Ha.* S, ' Yks -- t Oia a/o Tubes Vertical or Horizontal ...................................................................................... ......................... 'Tube Material (ASTM Specification and Grade)................................. .............................. Outside Diameter .In ........................................................................................... .................. Wall Thickness. (Minimum) (Average). In........................................................................... Maximum Tube Wall Temperature. Deg F tCataulatedVIDetign)................................. Inside Rim Coefficient (Calculated) (Based on Outside Surface) ................................... t Design Basis for Tube WeH Thickness................................................. ................................ Description of Extended Surface: . ' Type .................................................. ................................................................................... . Fin or Srad'Materiel ........................................ :.............................................................. Fin orStud Dimensions :.. HmdrHX. .* ................. Fin or SBBt Spacing , .......................... ,..................... . Maximum Fin or Stud Temperature........................................ .................................... Extension Ratio.................. ................................i.......................................................... .. Vert ' Hori?. . /CV2QO &R.T-P) 4.5 0,2&>S _______ /qpQ/^OO Cl a MS t-4- 1M7 ~_____ -- n%c.i-s> --_______ \ * O > \ OS --______________ a --___________ M, A*. Plug-Typo Headers Manufacturer end Type............................ .... ` Material (ASTM Specification and Grade) Nominal Rating............................................. _* Location .......................................'................. 'Weldedor Roiled................. ......................... Return Bends Manufacturer arid Type................................. 'Material IASTM Specification and Grade)., Nominal Rating or Schedule------........ 'Location.......... ................ ................................ tHLO V/cuacp Rgftjtm B-guta q%cg-i%Mo .......: .......... Ts Surr Tu e.Es -- FteS-Rox l4es.og.aL 3>q"< tsvl. 0 I WA-TEX 000913 S"- MECHANICAL DESIGN CONDITIONS (CONTO) ' Coil Design (COnt'd) ' Heater Section ,.................................................................. .....................................................L tgA.PI A.t4T_. C^vecriOM -son**............................................................. :...............................;----------------- _______________________ Terminal* . Manufacturer and Typo............ 1....................................................................................... r .......... ... Material lASTM Specification and Grade) ........................................................................ ................................................ A m.JLs, Nominal Rating ...,.................................................................................................................. J._ Location ................... .......................................................................................................................OoTStog. H-S. Welded or Rolled........................ .............................................................................................. --Mgjr-Pgi.P:------------ Flange: Site end Rating lQ^ E.P. Location........... " MB Note l' Strew Group To Complet* Noale Movement: ............ :........... . 'Direction... External Noale Load................... Direction... `Pipe Load Supported By Heater .. Special Support Bracket* Required Comment* --................. .................. . --------- - R.F. Crossover* Welded or Flanged............................................. ......................................................... .. ----------------------- Z_ * Pipe Materiel (ATSM Specification end Grede).................................................................. ,hZT..9..-frf3..T P. Pipe Site end WH Thkrfmes*............ ......................................... ......................................... 4-.S,* l.,Oi.Z<^LilK ------------- Z. Location .................................................................................................................................... .^SRMAL-------------Z. Flange Rating ........................ ..................................................................................... ............. ... . ................. ....................... Tube Support* Ends, Top.DsIlsmi " 4 47 TP.U. Material ................................................ ...............................................................................fee. Thickness ........................................................................................... ................................ .............. ----------------------. Type and Thickness of Insulation........................................ ......................................... .................. ZZ-------------- -. i ------ ------------- -- -- . Insulation Reinforcement................. ......................................................................... ......... . ........................ . ..--..... - .. .TM Intermediate: ' Materiel ............ .............. ...................................;.............................................................. ................................................. A^47.T.PI.t Spacing. Ft........................................... ......................................................... .................... .......................................... .--- --1^--1" 3 _ . _ . Type and Thickness of Coating ...................................................... Guides: Location................................................................. ........................ .. --...... ....................... --. .--.......................... .5.5? XT.S..tft----------- , .. ------- ' MM.......................................................................................................................... ........... ... Notes--------------- -------------------------------------------------------------------------------------------- ---------------- :----------------- TM~--------------_ ------------------ - --- l) RftDlANT OdTLETS fkRg Ta 4taovJPc.p. .. . ` __________ H iC SfE FORM 376C Ofi.- 'i-PH E*rr 7 (& ; WA-TEX 000914 r MECHANICAL DESIGN CONDITIONS (CONTD) Head*/ Bow '. tnrJtk>n'-Ce>v3Vg.g.~noJ> &&g.riovi------- UMri*, Ct.R6,B.H g-rgfeu .. Thickness-_____ 'Lfe . --.. Insulation: muradai OA.fe'TA^&L.S i US/____ l- ^ H'**--.-- .......... .Thickness------ ------- ------------- . a--w--w, n.---i c \tt ^ ^Tg.gu CtAi^m \-twl'< Fa>4d.\4^i Are Header Boa Door* Bolted or Hinged?. --... ...............------ ............ ............ -- ........................ . j Burners _ Manufacturer and Type. JoWH . C>ot\fe__ *QtU ** ^ Location__________ RcMot^t-nr Floor___________________________________________ Size and Type of Pit"** ~ Ca ~ **Pe.R.SiIRH8.K. -Sb*. 24: -Humber. 1 Heat Bel*#** per Burner at Design Encase Air and Draft (MM 8tu per hour) tin,**i I^OOO^OOO Minimum___ ..llPPEUSP. P.., Minimum Distance Burner Certerite* to Tribe Centeriin*:. , Hmininr^ ' Ce>'~Q \A\^-_________________,, .... .-...... Vertical-- ___ Msaimum-.i^P/^PQj.QQ.Q. H> As>> . Setting*! iw*' ;< , Exposed Vertical Wads: Wall Construction- Outside Casing: Thickness. /--dp Tieback Design and Material- Support' Material- Method of Fastening Tiebeck* to Structure. . Hoi-Fee* Temperature: Design. 4- .Materia). -Calculated- . Outside Temperature!. ...... --.Spacing.... Shielded Vertical Wans: ` ' . . '* ] ThicknessJS ~Hot-Fpe*Temperature: pe*gnJ^OOO_.--------------------------------------------------------------------------- CaicuUtedijLQQJ Wait Construction___CcA.^X.ftsH ---- -------------------------------------------:---------- ,--------- Outside Casing: Thicknesa___--________ ljlA:____ ________________ Materiel.1? Tiebeck Design and Materially R^.3--, S> --OutsWe Temperetitre---------------^------------------------------------SpacingJ-... . L ,,*---------- --- Support- Materiel:--;--,,--.......................-- J"c* ............ ........................ .....................................--------------------------- :----------- : ,, Metbod-of Fastening Tiebeeks to Smieiut*!--r..:.`_\Sajsi?miPi 1 H.fH------------!------------------------ T---'---------------------:---------- ---- - Thickness.!C=>- Arch rrm>w^4nr __________ __ Hot-F*** Temperature; Detign_jL2^3j2----- .,,Calcul*ted-,,-------- C k-$TA.BU.Sj l~, V4.S/i ... I r.2...4r..------------------------------------ ---------- Outside Casing: TtOrtin^. ' " X/jS* [----------Material Tiebedt Design and Materia*.?... VC'.krJ.^ ^SO N. ^T-S.gt-. , Outside Temperature^.^.Q.0.. ,^Q,.4:--------------------- -.Spacing.-------------- _ - Support. Material;--1, .................................... ........... ................ ...............................................;-------------------- ----------- - Method of Fastening Tiebaeks to Structures-------- NaJiiL01 N^rl--:------------------- i---------------------- i------ --- -------------------- -- .. . Floor: - . Thietin . .. Co. "' Hnt.F*g Temperature: Dwen 2000____ Catariated-------------- -- . - ' Floor Construction CrA.S.TAfi>.<-S j .L H ...... },, --------------------------------------------------------- --------------------- ............. ......... ........... Outside Casing:. Tt'U-e---^ ^ P................ Mjrimtwn Fhwr Eteuarion------- __--------------------- ------, --------- --------------MmeriaiC.AC.BoM 5~[*.SSt-_Qutsid Tmeimi 4 2 Oj3 ConvectionSections ; , _ 2is2.Q.Q_. Thickness S>iDesign Hct-Feee Terrpr*hu*-- .................................................. .. Construction______ C.A>ST~A.8>t-.S. ^ (_ M.\A t> Ar MlX...... ... . Outside Casing: ttut-- ' _________M*leriet^4.&S3bi-SESSW-_._0ut*>de Tamperatom htC $Ff fQAM 37*0 WA-TEX 000915 MECHANICAL DESIGN CONDITIONS (CONTD) Saltings {Corn'd) Tleback Design and Materiel yV~Cu.PS .. *?S-TTVp.1S__2>Q'4- Support Minwial ............. . --........ ............................... Method of Fastening Tiebocks to Structure..__ N\/S{--DIN^t .... - Internal Wet): ' Typl' ` Kl a>si Dimensions. Material. Slack Number .0>*| . CtLeia^aKt ^ ^Tbet. . * Self-Stipportingoe Bnyeri SS-LP SUPPQR*T *I nretionToP OP A,-3<b -jhMmnM ' ___________ - - - ' -- ^..Minimum Thick/* l'4~- t u Inside Metal Diameter C> Cs . xVT 4- - ^ Height At>OV (tfarle-A ^2. *- >-.... . Stank Ungth.l3--%-" 3. Lining; Mataria)1:' --..............................................................................................................................Thickness . .Typeof Material orReinforcemenu. Extent of lining ' .... ......._ ........ Dampers' , . ' ... Locotiori:.'Stack or Bottom Air Plenum ' ..--*.S*T AsC. _______ MafBrial./;Cfre7&Q*A tg-regu - VA >Aih ....... Multiple or Single teef.'- M uUTI PV-- Description of Provision for Operation from Grade____L.________ V/t hi C VA ............ ~ ____ HotDurts:Breechlng1Flues;and05Uactors-t-'r'-."r-"`: .; Material : OAK SaOhi '^TSSI---- ty. 1~HtC . . . -- . . , ` ASTM Rpeejfimtion 5^0' Sire Insulation; Type C.A*5*T~Ayfet-5.:.r FM I , ~2 , rd- M I X Thicknear ' TypeofAnrirnrtniTMmertel CA.RSPN ^TS.e.L CuM -t-IM*! F&HCIKIC, Size of Access Door into Breeching^________ SjoMte. '! w'- ^ wimm t. . Y * * Material-C-AyRStOhi _S~TSSL. />'4--rTtA 1 C VC *. A STM RpeniBeelinn ... ...... ' film ................ 'Miscellaneous' Overall Dimansions of Fnmwe-1-"- " ......... .... " ^ * v*1 . tf Cavj'J \>thrg.`t'^ T.\?A.Ci Ov>TL_GT~ ' Platforms?!Location - BoTT gA.CS --~ lsOOTSuaWgS -- 'DS&OXIhLgt CoMhl^-- 5 "'V- C \< ' ' . ' Width-Viul. ' '2. ~ Ce> ~ ' ' 3 *- O_______ '' "3 *- O 'Ct-gAv^ * Typenf Poor '* ly4 ** CHECKERED PtATE . ' <' '' ' ' Stairs; location......."{*0 BoTTQM RAO) AbiT* ' PlA.TFOK,f^ ' ____. ' Ladders: location 0 FkttVA rgftMSSTo 5ooTe>t^avJK. Pwh.TR W/ St&P-OFP'At RuO, FuATP 2.) 6ocTSLOV)g. R.tet-cr ' To Og-COXthACt C Qtiti 3u) 'pooTBUCVi^g R-bTcrTo `uTAOC PiUTC" Access Doors; Location and. Size._>x .P.o'oR ' ________ *2.') &TAatC ' Observation Doors; Location and-sire.)^ 'DoORCi *2^ putooR ^' Miscellaneous Connections (Number and Slzo):: . '.. ... ' . ' Draft______ V ~ ** ^ ^ ' `".Cp Flu* Gas <tmPu - I - ISD^RF " 4 , Temperature. _L ^"150^ RP l*>"& Rmnthering^ftoaro- Z.. ^ IFS> ~~ Ca ' Header Box Drain >*- IPS' t 'stack Drainl/?. ' *' l Coil Drains . ....... ' Tlther . . .......... _______________ i m-TEX 000916 . . . MECHANICAL DESIGN CONDITION* (COMTD) Painting and Galvanising B*qubmin Ugb.*T*-Sft. &? .t-- *----------..........................................................B.P3-7-------- PMMT t.B Mn.*, NhvJ. bKT, f To. FapeRAoL BfSG TT^P-gifayTYPE- II 2'*i PL^P-OKM^i. LA.aOF.g&, ^>TMRS \mo kiAWT TROt.TuRM.- ........... Akx.'JtKMise.cs. Per, ,~>f>.c S- *2.VA_________________ V) &tac:ic.-s>^ M.g.TM.u.1giso Qm Extse-ior. U*>iMct IhE fe.TCO UPiy^TsM ' Are Painter'* Trolley and Rail Induded? , . . Np.M-fcEatsnt of Tube.Htndiing Fedlitle*____________ MoUaT z . i&K nEsptosion Door*: Location and Slie_ . Special Equipment (Soot Biowart. Air Preheater*. Noiee Suppreeeora. Fens, Ctc.). *0 4- - Rotary SootblciWeri \ - W/ Automatic, ^omthou PA.t>ltki_ &i .1 - , 1 (, - .... r .,: /. ,. b> 1 - Not-s-tt;.._PLsKiUM ..... : . A~ ' r'` . ' A . . .. COMBUSTION DESIGN CONDITIONS . P,E--,^J-.. . . * "Type of FOai ......................... I.................... \\k............ ,.....................^AiJr-------- *2--------4. A5>. -- Excess Ak: Parcant ......... '...................................................................................................... ---------- ^ fa ...........~............3.9...,/?... Srls-QGuaranteed Efficiency,! Protect OHV) ISea Note)................................................... ..* ------------ -------- --...................... Calculated Effidtney. Percent ILHVK.......... ............... '....'............ ................................. ............... 1-------- i-s/---------------------------- ' Radiation Los*, Percent cf Heat Release (LHV)................................................ ............... -......................................... ......... . ` Rue Gat Temperature, Dag F,,- Leaving Radiant Section ......................... .. ,, >530-------------- ------- r,, .. '............. .- Rue Gas TermperSture, Dag P, Leaving Convection Section................... ...............^jLQ______ _________ ^5.j5i9l Rue Gat Mata Velocity Through Convection Section lb/Sp Ft/$*e............................. ...................4~...................... 'IS---------^:4P .. Draft at Bridge WaH. In. H O ?& P.45*. fil4 0-1 ' '___________ Draft at Burner*; In. H O . 1..................................................................................................... ' O-4-S .. '_ Ambient Air Temperature, Deg F,i.......................... .......................................................... ......................C=> ,Q . ....... ........... ....... ;-- * Altitude. Ft Above See- level-.. v. ............... ..................................................................... ...... :_____ -------------------------------------------------- J-L. . Calculated Heat Relee*#, MM Btu per Hr |LHV>................................................... .. ................... *?&%> ' ---------------------1 . Volumetric Heat Release, Btu per HrperCu Ft................................... ............. ...... .......--...................................................... Not*: A fuel saving ofMM Btupar hr wiHoffteta tt.COOtncreate in furnace coat {ererrtedl. ; .-. ... A tube side pressure decrease ofpsi will offset a $ 1.000 increase in furnace cost (erected)." ' o fuel characteristics On * Heating Vikw: HhV . IHV RS.F1N4CY FUE.U *. PsE.S,URe PSV< gtSSClFtC. Gg.bsVITV _ . fuel- Qu-................... Pressure psio Temp F API obavity Viscosity- ssu ^5 pt tuunisi. Pe.ft.cSMT t By V/t'i VTI2. - l.*T. boo 1*542 lo*jO-. Tfet ..IAax>....... ...IP-...... I-Q-3-S___ WoaM CsO : O.&B JiLHL' 47 --- 25o B10 \Z 'JB-iol ' 5 z so 1 150-170 ' _ .. 2oo 250 IO 2&<i-220 t2' ' Pott. TPctB-asottG-s. Aac. -Oostf.Am Op Cen-rcte-v- VauVB' --------- DS - 2-P-") l WA-TEX 000917 WA-TBX 000918 WA-TEX 000919 exchangers >4CweC^. _ WA-TEX 000920 i Data Sheet 3B-E40 TABLE OF CONTENTS SECTION l.k HEAT EXCHANGERS Emergency Cooler Emergency Cooler 3B-E*tO 3"DE~1 WA-TEX 000921 EXCHANGER SPECIFICATION SHEET 8 CUSTOMER AND , , PROJECT LOCATION TE.Vt.A.-0 \tU.. ,|.plant ' Ptu.e*r sovimp EXCHANGER REO- NO, E. -Q>\ SERVICE OF UNIT EtARXi.*4C.*V 3<M-taL SIZE TYPE CONNECTED IN SURFACE PER UNIT U OOO 44R SHELLS PER UNIT OV4C SERIES SURFACE PER SHELL PARALLEL `f'f Gft. PERFORM ANCE OF ONE UNIT 7 FLUID CIRCULATED TOTAL FLUID ENTERING 9 VAPOR 10 LIQUID II STEAM LSS/rtl BoiC S+Wtfe SIOE W^TtR. 1. too. 000 1 , , OOQ ............... TUBE SIOE on. 4-14,^71 4T3.WI ... WN-&0N0ENSJBLES _____ f FLUID Vttp'omZED "oft'cONOENSED . 14 STEAM CONDENSED 15 GRAVITY-LIQUID A** | IS | VISCOSITY-LIQUID f -" " .. 0 4. .a&isctv 17 MOLECULAR WEIGHT-VAPORS IS SF-EC'f'lC HEAT-LIQUIDS ?19 ..ATENT heat-VAPORS 20 j UMOf RATURE IN 2 I 4*t MPE RAtuRE OUT 22 } OPERATING PRESSURE PSIS 23 NUM 3ER OF PASSES i VELOCITY * i | PRESSURE DROP AlLOw/cauj J26 FO-Jl ING RESISTANCE MIN 27 50 (SCs in/* LTD/* *f *F FT /SEC # /SO IN. 7SO 250 Co &.8k 20 / 20 26 g HE AT EXCHANGED- BTU /HR 1^,0,000,000 M T.D. IWRWH> Z>ZS r29 TRANSFER RATE- SFRVICE SO CLEAN ACTUAL FOUUNP FACTOR 1 CONSTRUCTION 30 DESIGN PRESSURE P31 TEST PRESSURE */$O.IN #/S0. IN ISO 1515 32 jj DESIGN TEMPERATURE F 600 33 h tubes C-S. tv Cm B no 22>4- o o4.$ *w* ,0.2S'! JUS. length pitch L34 Shell 1.0. 0.0. THICKNESS 35 |' SHELL COVER FLOATING HEAD COVER i CHANNEL 1, TUBE SHEETS - STATIONARY C.S. Vft'THlC CHANNEL COVER FLOATING ' B T U / e tu /# *f -f FT/SEC */SQ IN P/ SO IN P/so IN *F &" 4 ,* n At BAFFLE - LONG TURE SUPPORTS GASKETS TYPE THICKNESS THICKNESS 42 M CONNECTIONS - SHELL - IN 43 N ____________ - CHANNEL-! N [CORROSION ALLOWANCE-SHELL SIDE CODE REQUIREMENTS WEIGHTS - EACH SHELL____ OUT OUT SUNOLE RATING RATING TUBE SIDE TCHA CLASS FULL OF WATER SPEC, g_~ NOTE INDICATE AFTER EACH PART WHETHER STRESS RELIEVED IS R) AND WHETHER RADIOGRAPHED I K-jT>~ - ?-M-RKS ~ FX. A.&OITtcm>A.U lnrowMAT'lOU &CC PHAkNAf I4Aa IQOTS-'S- Ofc. - I 4gf A 01 LAil-v-Ta~uihNLi& CowTtocTiow b>ha JO 6 NO DRWG NO. REV. pOj5 os-5*E-^ s a /s o iu v j oei-H wuoji WA-TEX 000922 I <ASA) WA-OJEX 000923 lilt* T-S'"PUMPS 1 WA-TEX 000924 I* TABLE OF CONTENTS SECTION 7*5 PUMP DATA AND CURVES Summary Table 7-5"! Data Sheets - AH Pumps Pump Curves - All Pumps I WA-TEX 000925 WA-TEX 000926 CENTRIFUGAL PUMP DATA SHEET APPLICABLE Td PROPOSALSO PURCHASE O AS BUILT O NOTE i) INDICATES INFORMATION TO IE COMPLETED BY PURCHASER; ' . BY MANUFACTURER JOB NO ^jSa^iTlTEM HO - d?Q/{j PURCHASE OBOEB N0-_J, -O Q> 9. S' " .<3* Q \ REQUISITION NO. 4JDCi.c\ S' -- ,0\.O\ INQUIRY NO, _ . . DATE__ .--_______ REVISION.. . (OR 'ftdxAoa/AfiO. UNIT. Pl.u/d C* ta^TjC C&^rr/AVG _______________ _ NO. BUMPS RED O ITEM NO.2ztJzjPL PROVIDED BY_ Ft)w?/?_P__l_S__Ampby F~J&t~G immZ&&56A PROVIDED BY-^kjW^/p4i_MT0 BY . P. _te.ua PUMP MfR SIZE AND vin ASJTsebial no. .7^3/ - fiS- ><3>/3//2 OPERATING CONDITIONS. EACH PUMP Liat)IO..jS O.S. 6PM It PT. NOR. J.Q.)3k___ RATED, .OISCH. PRESS. PStfi. PT. f. NOR. AtO MAX------- _---- SUCT. PRESS, PSIO MAX___ RATED. 3.4- SP OR nPT___ &'7&_________ OlFf.PRESS,*< VAP PRESS. It PT. PSIA_Z(^cf5____.O0IFIFF.f.HHEEAAD0. F.fTT__________ eLZiT VIS. II PT. Sw JxJjCL. NPSHA FT___ Q. Co&f? IZCT&D CORR/EROS CAUSED BY. .HYD. HP. CONSTRUCTION PERFORMANCE PROPOSAL CURVE NO JZZ7/-.Z. rpmJ&I5j2.-npshr iwateri *? 5^__ BHP mVOjLQS' wT.. MAX. BHP RATED IMP______ //.. 7. _......... MAX HEAD RATED IMP1&.&O.... MIN. CONTINUOUS GPM. // o ROTATION (VIEWED FROM CPUS m)ZCj\{ SHOP TESTS NOZZLES SUE RATING FACING LOCATION SUCTION DISCHARGE zS<3ezj 3co& 3oo# TOP..... CASE-MOUNT ^CENTERLINE QfOOT BRACKET OVERT |TYPE|_----- SPLIT AXIAL pjfwDJYPE VOLUTE OSGl Te6L O DIFFUSER PRESS MAXAlLOW.OSiSeZiL.PSIG . .<5? <2. F. OHYDROTE$T_Z<Q?O-PSIG OWIT PERF SSwit HYORO ;s&hop INSPECTION OWIT NPSH (.TOISMANT AINSP AFTER TEST loOTHER -CONNECT ^VENT SfFRAm OGAOE^, /V> IMPELLEROIA ORATED 'CL OMAX _Zs3_,,`!K------ -- DTYP;jC*fiWZ- MOUNT D BETWEEN BR6S JflbVERHUNG WEAR- N6. OIAM./CLRNC. C?t C?2.C3_ REARINBS-TYPE: ntlAlllAI 2/4 i~ OTHRUSTA^- LUBE. ORIHO OIL OFLOOD OWL MIST ^LINGER DPRESSURE COUPLING OMRF___FPFj _____ O MODEL____ *?.- DRIVER HALF MTb BY- OPUMP MfR OORIVER MfR $} PURCHASER MATERIALS APt CASE/TRIM CLASSO-- fi>P--ZJ3! 1Cags* - Saas>PACKING. O MfR 1 TYPE___ ____ ________ _ OSIK/NO. OF RIN6J MECH. SEAL. O MFR A MODEL W ~ Cj? P__ APLCLASS. C001. n BASEPUTE. MFROCDE. J/EHTTCAL PUMPS AUXILIARY PIPING )P1OCW. PJPF PLAN__ __ OCU; OS.S, . QTUS1H6: OPIPE TOTAL COOLING WATER RED'D, 6PM. totIl . o SIGHT F.I. REQ'D- OPACXING COOLING INJECTION REDO; OTOfliLGPM OPSIG 3<$t. OSEAL FLUSH PIPE PLAN jL/r_j$CS. OSS OTUMNS tftmSCH&Q wsua OEXTERNAl SEAL FLUSH FLUID____ ' OGPMOPSIO.-------------------------------- OAUXIUARY SEAL PUN___________ OC.S. OSS O TUBING O P'"E. I -VOOAUX SEAL QUENCH f HID ftsTtn. Qa UP -A- Pig-UftC- C.H PuM P MfR. MOTOR DRIVER i HP _/^L5Z. RPM___1_ 30*00 ruut4 0^jjUS>mvKmust/ema < Z/h MFR. PC O BfARHKS 34LL -LUBE. | ( rvt >LsriJ?/ 7 !,,,-- c? .full LOAD AMPS___ 1/ ENC .7ZSv^ZTBHP RISE. C_cSi2-lOCXEO ROTOR AMPS, //a OVHS o VSS VERT. THRUST CAP. LISERVICE (ACTOR PIT OR SUMP OEPTHO......... .....................-- MIN. SUBMERGENCE REQ'O.O -. .... COLUMN PIPE HANGED THREADED LINE SHAFT OOPEN O ENCLOSED bugs oeowL____ _ Dune shah BRG LUBE OWATER OWL QGREASE HOAT A ROD l'YcS OSS ' BUZ . 'NONE FLOAT SWITCH D___________ .... _ PUMP THHUST. IB UP____ D DOWN _ . APPROX WT. PUMP A BASE_SLfi2.g5.CiL. MOTORS$3lZ. CLtuwihf. API STANDARD BIO GOVERNS UNLESS OTHERWISE NOTED. * I-U--J4 izwen fdvl tou trrtivcnou 2 /Mi V)5EDSAL PLUSH PlAH 4r f vf-tt-hi. /.-**/fifty? Et/KCHAStE n toll, hi TVr.d f?_ is GXjkta* . * *; NO DATE < v7 .... n \ 4 JOB NO DRAWING NO REV & 3I009S DS-39-&-1 SHEET.. ( OF.../L WA.-TEX 000927 CENTRIFUGAL PUMP DATA SHEET APPLICABLE TO; PROPOSALS O PURCHASE O AS WHIT O . M m.JtQ<%SITEM NO _ 3B- G> Z PUACHASE OAOEA NO_____ .. AEOUimONNO. . .. NOTE <; INDICATES INFORMATION TO U COMPLETED IT PURCHASER; BY MANUFACTURER FOA . MC "/:r SITE- INQUIAYNO_________ . . DATE____ - _____ _ REVISION MS3.0uAaL. UNIT. NOPUMPSIWO. -NO. MOTORS AEQO. JTEMHO- PAOVIDEOIY- NO. TURBINES AiffO-iITEM No3B-67'fr_ PAOVIDEDIY__________ PUMP MFH -CZfc/IXjfjQ____________ Sin ANC TTfE-4-" . X.C' AA_ _ MTD IT _ --MID 8Y_ . -SERIAL NO.. 7 419$ OPERATING CONDITIONN, EACH PUMP PERFORMANCE s/vw?<r imlim (lAS>Pt-n4 lg .....uscpmmptnoa Ca^D....hated . itXdtL.__________________ ______________ OISCH. PRESS.. PSI6 PT. F.NOR JLELQ MAX CeuSL.-- SUCT. PRESS, PSI6MAX______________ RATED-- QjJS.SP GA M PT____ ------------- OIFF. PRESS, PSI________ -SfeiJfe. VAP PRESS.HPT.PSIA_ VIS. M PT. SmCP-tiS. NPSHA. FT EHFF.HEAO.FT__________ -Llii- .ISL COAA/EAOS CAUSED IY. ___________________________________ -HYO. HP- PAOPOSALCUAVENO------------------------RPM 35 Si t?- NPSHA (WATER) IFE._33^jHP RATED--3jL MAX BUP RATED IMP 3 .. MAX. HEAO RATED IMP MIN, CONTINUOUS GPM_ CROTATION (VIEWED FROM CPLC END| C VsJ CONSTRUCTION SHOP TESTS NOZZLES SUCTION DISCHARGE SIZE (*" .... 4.- RATING ISO"** 2.50-1* FACING FP pp LOCATION td If* Top -SPLIT O AXIAL ttfRAO: TYPE VOLUTE DSGL 0OW. DIFFUSER PRESS DMAX ALLOW. .Gt<kiik.PSIG . . (gOS F. D HYDRO TEST _ PSIG CONNECT J&VENT (gffRAlN D6AGE yJU 1X2,IMPELLLLEERROIA ydRATED______ 7 ____ 0MAX------ TYPE:. MOUNT BETWEEN BAGS DWEAR.R6 WAM./CLRNC. &/UL .AfAAINGS TYPE (^RADIAL___ jSlTHWUST........................................ LUBE. RING OIL Of1000 OIL MIST OFLINSER OPRESSURE COUPLING tfi'MRF___ _______________________________ MODEL DRIVER HALF MTO BY OPUMPMFR O DRIVER MFR QPURCHASEA 7~i/'Xsfrr >' PACXING MFR* TYPE____ SIZE/NO. OF RINGS ? -- MECH SEAL MFR* MODEL- .API CUSS. CODE______________________ OMFROCOE____ Ohon-wit perf OWIT PERF C'IRON-WIT HVORO OWIT HYORG l "WSH fiEO O OWIT NPSH OSHOP INSPECTION LlDISMART IINSP AFTER TEST OOTHER MATERIALS API CASE/TRIM CLASSO- BASEPLATE . VERTICAL PUMPS AUXILIARY PIPING OCW PIPE PUN. -OCU: OSS, OTUBIN6: OPIPE- TOTAL COOUNG WATER RED'D. 8PM__________ O SIGHT F I RECTO-- OPACXIN6 COOLING NUECTION RED'O: TOTAL GPM PUG iTSUI FLUSH PIPE PUN__________ OtS. OSS. OTUMN6 OPIPE- L ^EXTERNAL SEAL ElUSH FLUID _ OEPM_______ OAUXILIARY SUL PUN______ . OCA OSS. OTUMNG OP"E- Oaux seal OUENCH FLUID- MOTOR DRIVER PSIG. PIT DR SUMP DEPTHO-- -.......... .... min. submergence reo'd ..................... COLUMN PIPE. FUNDED THREADED LINE SHAH DOPEN ENCLOSED IR8S. DBOWL______ DUNE SHAFT BUG. LUBE OWATER OOIL GREASE FLOAT*ROD OCS OSS ,'DRZ l'NONE FLOAT SWITCH O____________ -___________ PUMP THRUST. LB UP_______ OOOWN_____ HP _ . . -RPM___ -FRAME. --VQLTS/PHASE/CYCLES- MFR. ________ ..BEARINGS. ___ LURE_____________ TYPE ENC . ._ , -tNSUL____ -FULL LOAO AMPS. (.-TEMP RISE. C______ -tBCXEDROtOR AMPS. OVHS OYSS VERT THRUST CAP, II.. SERVICE FACTOR. APPROX WT. PUMP* BASEMOTOR .TURBINE- s WSTlNCrAPI STANDARO *10 GOVERN* UNLESS OTHERWISE NOTED 77) PUM?- <USTAU-L=b Nt=VLj I r\J lUHN/Er- DZ-NIFTL..__________________________________ _ V I'l1*14 /iSLMrli POU-CON&r. NO DATE JOB NO. DRAWING NO. REV. % 10095 DS-VG'2. 0 fSHEET /......... OF___ 1 WA-TEX 000928 CENTRIFUGAL PUMP DATA SHEET JDBNO.ifiQ&S.ITEMNO____3Bt_(s> PURCHASE ORDER NO........................................... _______ APPLICABLE ID: PROPOSALS O PURCHASEO AS BUILT O NOTE I VINDICATES INFORMATION TO K COMPLETED IT PURCHASER; BY MANUFACTURER REQUISITION NO.___ ... . mowAT NO--------- ----------------------- DATE_______ _____ ______ REVISION .. for" Ti3*A6"'}hi.C7'.~~ UNIT, F C...C..u.y VT ........ --~ SITE- -PUKP NO. PUMPS REQ'O. ' mhapmer -NO. MOTORS REOU- NO. TURBINES REQ'O. fi Aj AM________ .ITEM NO- PROVIDED BY. .MTDIY .. -JTW MQ.3&&IL3- PROVIDED BY------ ------------- -------------M---T--OIY. ., . SIZE ANOTYPE ^AfOMU Vi--M'S SERIAL NO . 3 2-0 &><&/& 7 OPRRATING CONDITION*. EACH PUMP IIOUIO BOCUi-___ - US. 6AM t PT. N0B..-2 3 ..WEB ..................... SS-T____________________ ____________ DISCH. PRESS.. PSIG-------- ----------------------- f.PT. NOR. -43SL.MAXSUCT, PRESS. PSI6 MAX---------------------------------------- RATED- JJ.. $P 6R mPT _______ WFf.PRESS.PSI__________ TjLjL L2___VAP PRESS. t PT. PSIA- 01FT. HEAO. FT JJLSL VIS. *t PT, tw_t.M3.CS.AP---------NPSHA. FT______ -IX CORR/IROS CAUSED BY .HYO.HP. CONfTRUCTION PERFORMANCE FROPOSAl CURVE NO_ _ _ _ _ _ _ _____ rpmXZj6bD__npshr (water) --27 EFF-3J______ SHPRAtD_/42.. MAX. BNP RATEO IMP_______ CIS. &MAX. HEAD RATED IMP_____ MIN. CONTINUOUS PPM -- ROTATION (VIEWED FROM CPL6 END|... fi.dW HOP TEST* NOZZLES SUCTION DISCHARGE . SIZE RATING J D*B 300 <T... 300* FACING RX J&3___ LOCATION EMD TOP OWIT Plfif OWIT HYDRO OWIT NPSH SPIIT O AXIAL GRAD: TYPE V01UTE GSGL j^DBl DIFFUSER .PRESS (UMAX. AUOW, ,3S._PSIG f. HYDRO TEST -J&S.O. .PSI6 CONNECT B VENT tj^RAIN OSAGE . jOMSMANT A INSP AFTER TEST lOOTHER *5 8 LLt-lXIMPELLER OIA RATEO____ I V ____ QMAX------- --------------- TYPElCj^j&fiC't' MOUNT O BETWEEN BR$S ftOVERHUNG Q WEAR. RG. (HAM./CLRNC. MATERIALS REARINGS-TYPE. DRADIAL. THRUST. API CASE/TMM CLASSO- LUBE. tjj RING OIL FLOOD DOILMIST DFLINGER > .!.$SUR COUPLING riMRF _____________ ___ MODEL.... .X$Q-- DRIVER HALF MTO BY: OPUMPMFJl OORIVERMFR OPUftCHASER PACKING: Q MFR A TYPEOSIZI/NO. OF RINGS. MECH. SEAL MFR A MODEL----------------------------------------- API CUSS. CODE-------- BASEPLATE. . QMFROCDE. VERTICAl PUMPB AUXILIARY PIPING OC.W PIPE PUN. -OCU: OSS.; OTUMN6: QPIPE- D TOTAL COOLING WATER REOD. SPM__________ . O SIGHT F.I. REDD. OPACKING COOLING INJECTION REQTJ, TOTAL 6PM DPSIG DSEAL FLUSH PIPE PUN. D C.S. OS.S. OTUIIN6 OPIPE- OEXTERNAl SUL FLUSH FLUID__________________ _ OGPM_______ OAUXIllARY SEAL PUN______ . QC.S. OS.S. OTUAIN6 OP"E- OAUX. SEAL QUENCH FLUID. HP MFR. . _____ TYPE. . . __ ENC . .. OVHS OVSS MOTOR DRIVER FRAME. 5..BEARINGS. .VOLTS/PHASE/CYCta. ___ LINE______________ -HRUL ________ FULL LOAD AMPS. _TEMPNSE.C_ _ _ _ _ _ ; JLDCXID ROTOR AMP*_________ VERT. THRUST CAP.. LA ; KRWCI FACTOR- OPSJG- |PIT OR SUMP 0EPTHO......................................- MIN. SUBMERGENCE REDO ... ........ COLUMN rtPE: D FLANGED QTHREADED LINE SHAFT O0PEN ENCLOSED mgs-. Growl______ dune shaft BRG LUBE GWATER DOU GGREASE FLOAT!ROD OCS OS,S ,~8RZ ONONE FLOAT SWITCH O PUMP THRUST. LB GUP. . GOOWN. APPRO*. WT. PUMP A BASE. MOTOR___________ . TURBINE. API STANOARO BIO GOVERNS UNLESS OTHERWISE NOTEO.(f) Ej\\ci'T(N Or PUMPr I N ~n;ZRINl?- pfttv^tgR.. P Nm \ u 03SIA2M> OCI ON MUQ* Hf p htbiy /S.c.LZPft POR. CDVJ.C.T. . NO. DATE ._ JOB NO. DRAWING NO. REV. 1009$ D5-3-6-3 o J- --lSHEET . ........OF ------------ WA-TEX 000929 .c k s o n *\y % 4 4 WA-TEX 000930 Byron Byron Z O u> o <: WA-TEX 000931 TABLE OF CONTENTS SECTION 7.6 INSTRUMENT DATA Summary Sheet - Relief Valves Summary Sheet - Restriction Orifice Summary Sheet - Flow Element Summary Sheet - Alarm 6 Shutdown Setting Control Valve Data Sheets Table 7.6-1 Table 7.6-2 Table 7.6-3 Table 7.6-4 ! WA-TEX 000933 Taq No. 3PSV-127A 3PSV-127B 3PSV-&30 3PSV-634 Service 3B-F3 3B-GT3 3B-GT2 Size 6" x 3" >1 3" x 4" 1-1/2" x 2-1/2" Set Press U4 PSIG M 300 PSIG &5 PSIG i I WA-TEX 000934 Tag No. 3F0-608 3FO-610 3F0-611 ' Service Lt. Cycle Oil Flushing Oil Fuel Oil .. Location 3B-0-218 AB-O-372 3B-0-228 TABLE 7.6-2 RESTRICTION ORIFICE SUMMARY SHEET PUNT 38 FCC Unit ANACORTES. WASHINGTON Line Size Orifice Size . Flow Pate 2" 2" 1-1/2" 0.433 0.433 0.23* 1* GPM i WA-TEX 000935 flow Element No. 3FE-60Q 3FE-601 3FE-602 3FE-603 3FE-604 3FE-607 3FE-620 3FE-621 Service 3B-F3 Feed II II Mn it n ii it Fuel Gas to 3B-F3 3B-F3 Feed <1 II Orifice Size 6.773 2.489 1) .n it 3.681 2.489 11 Line Size 10" Sch 40 4" Sch 80 II II 11 Meter Coefficient 300 BPH 40 BPH II ii it 6" Sch 40 4" Sch 80 It 20000 SCFH 40 BPH 11 WA-TEX 000936 .<# & &w vy yt - w c- WA-TEX 000937 B O bO45 *H CD 0.0CO lx. li. o oo -3* CO LTV ./^rv in 9 H rl * H 3 3r-4 O. 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CO cbmoi CO cbploa_cbmlo CO tO b bCO CO pcUo co i NONrtrOtNOPOVO'td'TONi \0 nO vD iD vO vD ID, beJuogSbccooiibccJooibccJoojbccJoojbccJooibJccooibJccooi NIp C\rI>J<Nf <\oMI 4tjN1) 3\N0I ir401l N\C0I ooo WA-TSX 000938 r\ i Sj SJ UJ * |.s Si IB fS?5 J! I i4 M . FORMNO,.MU>.l(l/EW FLUID INLET FEIO OUTLET PSIO MIN.|OftW.|MAX, MIN. OFtN: MAX. INLET TEMP. F lOPtR. MAX. OPEB. SP. QB. \um{f0Ct MOL.WT. ta'fwh flash OPEN. vise..p. CRIT. FREES. Pc VAPOR PRESET OPER. FLOW MIN. FLOW EIZINO FLOW MAX. FLOW FLOWtlNITf OP EIZINO OPEHUTOFP APMIN. Cv EIZINO AP A FLOW | MIN.Cv Cy.VALVE EELCCTEO FACTOR* SIZE PRESS. PATINO MATERIAL BONNET TYPE PACKING LUBRICATOR TYPE CONNECTION* CLAES SOLTE TYrE I MAT'L isol. valve 4o 3k. Am bdlL m lea ll Ss. JilL. JSL qZR 1ML LLksmfifloa zrL 3pp _____ .sWEtpAE JUL 4r- MSL MSl Km Z.7S S5 na. m. ZiT 6,pn\ ilk jS3L J2l Cl.?.3,4r 12 2bl$L>Z*L CnLQSS 3saH _ dL C.f Km m. fesf-ka yes J6&. , s5.r Tifi'iif. 1&. J ye 5 CHARACTER. NO. OP PORTS PLUG TYPE GUIDE TYPE TRIM SPEC. DPWttOsf FLOW: 0PBIS-CUWES ACTUATOR TYPE MOTIVE POWER {LINEAR / ROTARY [PRESS./VOLTAOEIPOS. ON POWER PAIL THBU5T OB TORQUE Rtfl. [ehUT OFp[qper! MAX. OUTPUT [MANUAL O'RIDE | POE. FEEDBACK TYPE POSITIONER OUTPUT SINGLE/DUAL INPUT SIGNAL BY-PASS SUPPLY PEIG GAUGES J&L leg 6 PSU <p.iT~ ft-l -IU BAEV aw -aP, r>C 40 l=il ie ua dsn dsi. jtep. J.^9, dsi. Higher mm i Pifeo M.R./P.O. NUMBER MANUFACTURER MODEL NO. P.& 1.0. NUMBER SERVICE JOt.JC 6*j A iC tStUl ttiHiAtS iAttiS ....... 'ies?-- 4-..ill. -V..& ^ lU4II MO. p-i AmQ-A -M? ^ a-/?A-/) , 3-gfi-4-< EEra&Ek*$$Ms _4__m_ntr-orut{rsAi.r yg^> _iiU?C. Oh^'7 **7 LINE SIZE - NO. SPEC 19" JI46 A J1174' -4."-AnA- INSTRUMENT TAG NO. mZ-M& HkX-liM3.pt-6S3 /g-ift.-rtsv/?gp tPixunl y,V 7 Vfclfe MnJ ISW SO PPVZ. ft) .* ftPa g DATE REVISION! ORIGIN R&C ENG. .iffACO ; iy,:j CONTROL VALVES ** \ *" \ ' JOB NO. Lr ^ *J. l ItiCJS DATA SHEET NUMBER os* n& REV. ( WA-TEX 000940 'X *