Document 8wDBEQZe6oKOzXw2knndQkjZ
PLAINTIFF'S EXHIBIT
ij
WA-TEX 001864
. JOB -CONTENT
PLANT;
Puget Sound
DEPARTMENTS
RP&S-Docks~Raeks
CLASSIFICATION? Assistant Pumper
Page 1 TRAINEES
A.*. BASIC TRAINING
DATE
1* Principles of Operation - Proportioneers
Automatic Blender - Model FB-2
2. Principles of Operation - "Loss-In-Weight"
Tetraethyl Lead Blender
B. ON-THE-JOB TRAININS
1. Blend Gasolines - In-Line Method
2. Blend Middle Distillate - In-Line Method
3. Blend Avjet Fuels - In-Line Method
4,, Draw Samples from Blqnd Header
5. Draw Samples from Automatic Sampler
6. Take Gauges by Remote Control Console
7 Records and Reports
8. Dye Mixes
9,, petrox to Dock.-
10of Operate LPG Dryers and Heaters
11o Filter - LPG Coalescer
12. Filters - Salt
13^ Filters - Product
l4,, Dock Line Relief
NOTE: Assistant Pumper is also required to perform all items listed on the Job Content of the Pumper Helper A and B*
Employe Qualified:
Date
Signed
. NAME Foreman
j WA-TEX 001865
JOB BREAKDOWN
A-l
PLANTS DEPARTMENTS CLASSIFICATIONS
OPERATIONS
Pugt Sound
RP&S-Docks-Racks Assistant Pumper A-l Principles of Operation - Proportioneers Continuous Automatic Blender Model PB-2
IMPORTANT STEPS
KEY POINTS
1. Major Items 2. Design 3,, Items of Equipment
Description of Equip raenfc Blender Control Panels
The "blender consists of control panels, meters and supervisory devices and is designed to reduce batch compounding operations to a completely automatic process,,
The design of the blender provides for exact pre-setting and control of the component and additive ratios, together with means for quickly adjusting total rate to production requirements without affecting percentage relationship of the respective ingredients,.
The complete blending system Includes the following items of equipments
a) Master Control Panel bl Component Panels c) Batch Control
Id) Component Pumps e) Component Meters f) Component Control Valves g) Valve Pilots h) Tally Meter 1) Additive Systems J) Air Supply k) Electrical Supply
Note; Minor variations in master and component panels for service in gasoline or distillate blenders will be found. The detailed descriptions will apply equally to both, although items will be discussed on the gasoline blenders which will not be found on the distillate blenders,
(a) Master Control Panel has the follow ing equipment;
| WA-TEX 001866
PLANT; DEPARTMENT; CLASSIFICATION.;
OPERATION;
-JOB BREAKDOWN
A-l Cont
Page 2
Puget Sound
RP&S-Docks-Racks
Assistant Pumper
A-l Principles of Operation - Proportioneers
Continuous Automatic Blender Model FB-2
imporTan*F5teps
KEY POINTS
(1) Drive Motor - is connected direct to an infinitely variable stepless Integrator adjustable from zero to maximum.
(2) Rate Setting Handwheel - permits selection of blend rates0 The adjustment is made through a handwheel which can be set to a 3figure reading. Should it be found that certain oils cannot be brought to component panels at desired rates or certain formula-
'tions require percentages of com ponents not Initially considered, the blender can be slowed down to accommodate these conditions.
(b) Master Switch - Rotary is a multi position switch with the following settings; (1) "Off" - disconnects all power and supervisory control circuits,, (2) "Test" - Energizes the master drive motor and also illuminates the "Drive" green light at.the head of the panel. This ppsltion permits selection and adjustment of component panels. All panel test runs are made when the master switch is on "Test" position. (3) "Reset" - Permits resetting totalizers to zero after a test has been made. If the blender Is correct, the master switch can then be turned to the next position. (4) "Blend" - At this point, all con trol valves are opened at the same time to the manifold and finished stock passes to the tally meter.
(o) Indicating Lights and Switches across the top of the panel are a series cf lights and switches including;
I WA-TEX 001867
PLANT: DEPARTMENT: CLASSIFICATION: OPERATION:
JOB BREAKDOWN
A-l Cone
Page 3
Puget Sound
RP&S-Docks-Racks
Assistant Pumper
A-Jl Principles of Operation - Proportioneers
Continuous Automatic Blender Model PB-2
IMPORTANT STEPS
KEY POINTS
(1) "Drive" light is illuminated when .
blender is on.
(2) "Test" (red light) is Illuminated
when elector switch is in "Test"
position.
(3) "Blend" (green light) is illuminated
wKerTselector switch is in "Blend"
position.
. (4) Limit Reset Button is used to return
blender to operating condition after
limit switch has stopped operation.
(5) TEL Run (Light Green) Is Illuminated
when TE& blender is operating.
(6) TEL Ready Light (red) Is illuminated
prior to start of TEL blender opera
tion and after TEL blender has been
tested.
(7) TEL selector switch is used to acti
vate TEL blender.
(8) Dye Light (green) Is Illuminated
when dye additive unit is on,
(9) Bell Cutout Button is used to stop'_
alarm bell from ringing after being
activated by limit switches.
(10) Sampler Light (green) IS illuminated
when sampler is operating.
.
(11) Sampler switch is used to activate*:
sampler.
.(12) Batch Reset Button is used to clear
batch totalizer after completion of
batch or blend,
(13) Dye Pump Switch is used to start dye
pump to supply dye solution to blend
(14) Eductor Pump Switch is used to start
eductor pump for TEL blender.
(d) Batch Counter (1) Five setting knobs are provided to set batches up to as F^t&gh as
99,990 bbls. (2) An odometer section, resettable to
zero after each batch, totalizes the flow during the run.
WA-TEX 001868
PTtANfT11
DEPARTMENTS CLASSIFICATIONS
OPERATION."
JOB BREAKDOWN
A-l Cont
Page 4
Puget Sound
RP&S-Docks-Racks
Assistant pumper
A-l Principles of Operation - Proportioneers
Continuous Automatic Blender Model PB-2
IMPORTANT STEPS* 1 2 3 4 * * * * * * *
KEY POINTS
---------------- ---------- ------ ----- ----------- r
(e) Totalizers - Several are provided, j
(1) Dye - actuated by impulse switch oh
dye additive unit.
j
(2) TEL Reset - actuated by switch on
TEL blender drive, is used to indi
cate amount of TEL added during a
run.
(3) TEL - Non-Reset - actuated in
parallel with reset totalizer, gives
an accumulative total of TEL.
(4) Gasoline - consisting of a reset and
non-reset section, gives a continuous
reading of the finished product thru
tally venturi.
(f) Component Panels - controls are as follow
(1) Selector Switch - This has two
positions for on-off control.
(2) Air Controller - The controller is of
the anticipatory type with adjustment
for sensitivity and automatic reset.
(3) Totalizer - This i'g^of the manual
reset type with six figure wheels.
All totalizers are interconnected
with the drive shaft so that they
will stop when the master panel
switeh is turned to "off." Totalizer!
will show figures last reported unti:
manually reset.
(4) Variable Speed Integrator - The prin-
cipie or the integrator is that of a
cam driven connecting rod on the
input shaft imparting motion to a
connecting link which actuates an
over-riding clutch driving the out
put shaft, A secondary link shifts
the position of the connecting link
in relation to the driving cam,
changing the length of its stroke
through a range from zero to maximum
thereby changing the speed of the
output shaft accordingly.
WA-TEX 001869
PTAKPl*
DEPARTMENTS CLASSIFICATIONS OPERATION:
.TOR BREAKDOWN
A-l Cont.
Page 5
Puget Sound
RP&S-Docks-Racks
Assistant Pumper
A-l Principles of Operation - Proportloneers
Continuous Automatic Blender Model PB-2
IMPORTANT STEPS
KEY POINTS
(&) Ratio Adjustment for each component -
.. This dial is connected to the secondary
Integrator,
(h) Differential - The computer is a purely
mechanical device through which is con
nected the control meter to make It
follow the leading speed of the drive,'
This Is accomplished through the appli
cation of a differential gear assembly,,
(i) Indicating Lights - One green of the two
!3ats at the fop" of panel indicates
that the blender is running automatically
and this light goes off if there is a
component or equipment failure. The
second light, red, is an indication that
high or low pressure is on the system,
(j) Receiver - In the base of the panel is
a receiver selsyn which operates In
response to the selsyn transmitter on
the meter located on the blending com
ponent pad,
(k) Pump Panel - Pump control panel is pro
vided as a central location for pump
switches which ares
(1) Pump Run Light - Green
(2) Pump tine-Dp Light - Red
.
S3) Test Button
(5) Pump. Selector Switch
(l) Component Meter
The meter is of a positive displace
ment type, located on the discharge
of each component pump. The meter
Is equipped with a 3alsyn transmittei
for operation of the component con
trols in back of the control panel
in Control Room,
(m) Component Control Valve
(1) This valve is a~ 2-way diaphragm
motor operated valve with plug so
arranged that with air on the
diaphragm, the liquid will pass
thru and into the blend manifold.
When no pressure (air) is on the
diaphragm, no flow may pass thru
the valve.
j WA-TEX 001870
PTAWF0
DEPARTMENTS CLASSIFICATIONS OPERATION;
JOB BREAKDOWN
A-l Con*.
Page 6
Puget Sound
RP&S-Dooks-Racks
Assistant Pumper
A-l Principles of Operation - Proportioneers
Continuous Automatic Blender Model PB-2
IMPORTANT STEPS
KEY POINTS
(n) Valve Pilot
'
Tl) This valve is a 3-part solenoid 1
o^rated and diverts the flow of '
air according to the valve position
which is determined by the solenoid.
. The valve operates from the on-off
and Limit switches on the component
panel.
(o) Tally Meter - The tally meter is a
venturi nozzle installed down stream
of the blend manifold and is used to
meter the total blend and to provide
a differential for operating a trans
mitter. This transmitter operates a
gasoline totalizer on the master panel
and also actuates the TEL blender.
WA-TEX 001871
JOB BREAKDOWN
A-2
PLANTS
DEPARTMENTS CLASSIFICATIONS
OPERATIONS
Puget Sound RP&S-Daeks-Racks
Assistant Pumper A-2 Principles of Operation - "Loss-In-Weight"
Tetraethyl Lead Blender
IMPORTANT STEPS
-
1. General Information..
KEY POINTS
The "Loss-In-Weight" Tetraethyl Lead Blendhr Is a complete unit for the continuous auto matic blending of TEL fluid to untreated gasoline In any dosage to a required maximum per gallon, despite variations In rate of flow of the gasoline being treated or blended
The Installation includes complete safety 1 devices to insure accurate treatment and apfe handling throughout every step of the blendir process. Here at Puget Sound Plant there are
two (2) complete "Loss-In-Weight" T2A blendei One for the blending of Premium gasoline and the other for the blending of Regular gasslir
2. Important Items of Equipment
(a) Differential Producer
(1) The differential producer oonsists of a restriction in the line which causes: a difference in pressure between the inlel and the throat.
(2) The differential pressure operates the chronoflo transmitter. A venturi tube is the differential producer.
(b) Transmitter
(l) The chronoflo transmitter consists essentially of a synchronous motordriven cam, a rocker bar and magnet, and a cam shoe and its arm. The whole
mechanism is housed In a case to which are attached the mercury wells.
(c) Seals
(l) The seals contain the liquid transfer medium and are interposed between the
main line and the mercury wells to prevent the blend line gasoline frorai
finding Its ways into the wells.
(d) Scale Beam Assembly
(1) The "Loss-In-Weight11 control scale consists of a double beam scale having a capacity of 60,000 pounds on each beam. To the upper beam has been
added a constant pitch, high accuracypoise screw running Its entire length.
WA-TEX 001872
PLANT? DEPARTMENT? CLASSIFICATION?
OPERATION?
JOB- BREAKDOWN
A-2 Cont
Page 2
Puget Sound
RP&S-Docks-Racks
Assistant Pumper
A-2 Principles of Operation - "Loss-In-Weight"
Tetraethyl Lead Blender
IMPORTANT STEPS
KEY POINTS
The movable poise on this beam has
built into it a split nut operated by
a "T" handle to engage the screw so
that as the screw is rotated, the
poise will be retracted toward the in
board end. The lower beam also has a
movable poise with an additional small
balancing scale and vernier to enable
the operator to bring the scale into
exact balance with the weigh tank,
*
(2) A magnifying glass and scale enable the
operator to check the beam for proper
level position,
(3) A vernier dial* graduated in 100 parts
is provided and the ssaie can be read
in one-pound increments.
(4) The poise screw drive mechanism is
mounted on the cabinet shelf and con
sists of a small motor coupled to a
variable speed transmission to a
parallel shaft speed reducer which, in'
turn is coupled to an air operated
clutch. The output of the clutch is
connected through change gears to the
input of a second parallel shaft
reducer.
(5) The outboard end of the scale beam is
connected by means of an overthrow link
to an air controller mounted in the
scale cabinet. The air controller con
sists of three principal units? a
baffle movement unit, a sensitivity ad
justment unit and an automatic reset uni'
(6) Just below the doors on the cabinet are
mounted six switches. These switches ar<
(a) Master switch which energizes the
complete cabinet.
(b) Switch 1 which energizes the circuit;
to the vacuum and air pressure swltc;
(c) Switch 2 which energizes the high-lo'
alarm circuits.
(d) Switch 3 which energizes the chronof
transmitter circuits.
WA-TEX 001873
PLANT: DEPARTMENT: CLASSIFICATIONS
OPERATIONS
JOB BREAKDOWN
A-2 Cont
Page 3
Puget Sound
RP&S-Docks-Raeks
Assistant Pumper
A-2 Principles of Operation - "Loss-In-Weight"
Tetraethyl Lead Blender
| IMPORTANT STEPS
KHf POINTS
(e) Switch 4 which energises the drive motor*
(f) Switch 5 which energises the clutch circuits.
(g) Switch 6 which is used in wash operations when loading the TEL tank to bypass the automatic shutoff ac tion of the control valve* (we do not use this switch, because TEL
tank cars unloaded here are returned to DuPont without washing with gasoline*) (7) At the head of the control cabinet there are six lights:
a) Panel Energised b) Vacuum
(e) TEL Fluid Control Valve
(f) Gasoline Totalizer
(g) TEL Totalizer
Ic) Control Air d) High Beam ei Gaao Rate f) Low Beam
(a) This valve Is a normally-closed, diaphragm motor operated valve with charac terized plug and seat so arranged that air pressure is required to open it.
(a) This vtoatlvaelizweirl,l mopoeunrateted oson athpaltateheaftlow othfeTEleL fftluhiadndwsiidlle veomf &thlneactatbhienerte, qiusire( d aramteo.tor driven double counter, one of which may be reset at the beginning of a blend* The counters indicate the amount of gasoline passing through the venturi nozzle*
(a) The two TEL totalizers mounted on the same plate as the gasoline totalizers are mechanical counters chain driven from the poise screw drive* One. totalizer is eight figures for a cumu lative total and the other is a six figure reset type for batch indication.
I WA-TEX 001874
PLAKTs DEPARTMENTS
CLASSIFICATIONS OPERATIONS
JOB m-LR/i^OvW
Puget Sound RP&S-Docks-Racks Assistant Pumper A-2 Principles of Operation Tetraethyl Lead Blender
A-2 Cant.. Page 4
"Loss-In-Weight"
IMPORTANT STEPS
KEY POINTS
(h) Solenoid Pilot Valve
., .(i) Vacuum Switch
3. Other Items of Equipment
(a) This valve is a small three-way valve mounted in the piping manifold on top of the diaphragm TEL control valve. Energized, this pilot valve permits air to enter the diaphragm chamber from the air controller. De-energized, the dia phragm chamber Is exhausted to atmospher causing the control valve to shut. The action of the solenoid valve is con-., trolled from the vacuum switch. When the eductor pulls a sufficient vacuum, contacts in the vacuum switch close, energizing the solenoid.
(a) The vacuum switch consists of an explosion-proof normally open Micro switch with an actuating bellows which holds the switch contacts closed except when there Is a vacuum of 6" or more of mercury in the TEL line. This vacuum range is adjustable.
(b) The vacuum switch is normally closed when system is operating, but if vacuum falls, the switch will open and the pilot valve will cause the TEL valve to close.
There are a number of other items of equipment tied into the TEL Blender that the operator should acquaint himself with dur ing training and operation of the Blender. Details of such items can be found in Proportioneers, Inc. Booklet, "Loss-InWeight Tetraethyl Lead Blender."
| WA-TEX 001875
JOB BREAKDOWN
B-l
PLANT?
DEPARTMENT? CLASSIFICATION! OPERATION!
Puget Sound
RP&S-Docks-Racks Assistant Pumper B-l Blend Gasolines - In-Line Method (Premium or Regular)
IMPORTANT STEPS
KEY POINTS
1. General Information
2. Receive Blend Order PSP-2
3. Check Component Stocks Available
A. Check Stock In Finished Tank
5. Line Up Component Tankage
6. Line Up Finished Product Tank
Each important step and key point Is shown separately in the following breakdown, but It does not mean that the operator is re stricted to take each step in order shown. The operator can save much time by partly or completely lining up for several Impor tant Steps at the same time, especially at the beginning of the blend, because so many of the blender functions are tied together.
(a) Read Blend Order carefully. (b) Determine product to blend and finished
tank number and total amount of blend, (c-) Determine component tankage, percentages
and quantities of each to use. (d) Note amount of TEL, dye and additives
to be used. (e) Note any other information on Blend
Order such as sampling and special line-ups.
(al) Gauge each component tank using console. (b) Record gauges on Form R-61A - Daily Oil
Report, also time and Blend number.
(a) Gauge tank to be blended into using console and record opening on R-6lA.
Open component tankage to be used on each blend line suction to Blending Manifold.
(a) Check blend line valves closed on tankage not to be blended into on same system.
(b) Open regular blend nozzle on tank to be blended. Shipping line or suction to be closed on tank receiving blend.
j WA-TEX 001876
PLANT;
DEPARTMENT* CLASSIFICATION; OPERATION;
JOB BREAKDOWN
B-l Page 2
Puget Sound
RP&S-Docks-Racks
Assistant- Pumper
B-l Blend Gasolines - In-Line Method
(Fremitim or Regular)
IMPORTANT STEPS
KEY POINTS
7. Conduct Test Run an Blender
8. Line-Up Component Pump Manifold
Select component panels to he used. Turn master switch from ''off" to "test" position. (e) Set master handwheel between 200,0 and 300,0 approximately with MASTER DRIVE RUNNING. Never adjust Master RanRwKee1 unTeg3~~Mas^r^r'ive'~is"running^ M
(ej Make component handwheel settings, using
percentages as shown on Blending Order from calibration curve. (f) Zero all totalizers with switches in "off" position, (g) Clear batch counter register to zero, by pushing reset button St% master control panel. (h) Set batch counter at 100 bbls. (I) Turn master switch from "reset" to "test". This will start the master drive. When the batch counter has registered 100 bbls. the board will automatically shutdown, (1) Read totalizers on each component panel in use. (k) Determine if amounts registered on each component totalizer check the percentages as shown on the Blend Order. If componenpanels check /or - 0.3$, they will be considered ready for blending. (l) Re-run test run if percentages are greater than / or - Q.3$o (ra) Set rust inhibitor timer for required amount; per 1,000 barrels as shown on Blend Order,
(a) Open suction cn all component pumps to be used and check all other interconnecting lines on suction closed.
(b) Open discharge of each component pump to be used into the Blend Header.
(c) Check discharge valves closed into Blend Header on those component pumps which may not be used on blend,
; WA-TEX 001877
PLANT: DEPARTMENT: CLASSIFICATIONS
OPERATIONS
JOB BREAKDOWN
B-l
Page 3
Puget Sound
RP&S-Docks-Racks
Assistant Pumper
B-l Blend Gasolines - In-Line Method
(Premium or Regular)
IMPORTANT STEPS
9,, Set-Up Dye Circulation
10. Line Up Automatic Sampler
11. Line Up RYP Machine 19. Line Up Rust Inhibi
tor Pump
KEY POINTS
(d) Open bleeder on each pump to be sure pumprcasing is flooded with product.
(e) Check all pump switches to be used in the "auto" position and check switches in "off" position on pumps not to be used
(f) Check air "on" to control regulating valves.
(g.) Check air "on" to back pressure regulating valve in Blend Header,,
(h) Take opening meter readings on each com ponent pump to be used. Record on Form PSP-19.
Ci} Check pump lubrication. U; Open the flow and mercury pot valves on
the c-hronoflo. (k) Check for leaks such as strainer and
meter housings.
{&.) Check Dye tank valves "open.11 Cb) Open suction and discharge on pump. (.) Check pump switch in "auto" position.
(a) Drain sampler of any previous product. (b) Close drain valve on sampler and fill
to overflowing with fresh water. (c) Make sure the sight glass shows full. (d) Close overflow valves on sampler and
close off water supply. (a) Open water displacement valve near
bottom of sampler on side. (f) Open suction to sample pump off blend
line. (g.) Open discharge (excess) from pump int.o
blend line. (h) Check pump switch In "auto" position.
(a) Note: When suction and discharge lined up to automatic sampler,, this also XineB up suction and discharge to RYP machine.
(a) Check suction on Rust Inhibitor storage tank open.
(b) Open suction and discharge on pump into blend header.
; WA-TEX 001878
JOB BREAKDOWN
PLANT; DEPARTMENTS CLASSIFICATIONS OPERATION;
Puget Sound RP&3-Doc ka-Racks Assistant Pumper
B-l Blend Gasolines (Premium or Regular)
B-l Page 4
In-Line Method
IMPORTANT STEPS
KEJT POINTS
(c; Open 1" block valve cn additive dis charge on vertical bank running to blend header.
13. Line Up TEL Eductor (a) Open suction and discharge valves on
System
vertical bank "to" and "from" blend header.
(b) Check suction valve from Tank #30 closed
on Eductor Pump and also 1" DMD valve '
closed.
(0) Open suction and discharge blend valves
on pump*
d) Check pump switch, in auto position,
ie) Check pump lubrication,
f) open valves 9 and 10 on Properfcioneers
Eductor system.
(g) Open Eductor By-Pass Valve one-third.
(h) Open Valve fip.
(i) Take opening reading on weigh scales -
upper and lower and small beam and
record weight on Blend Order,. B/P
Operations sheet and Log Book.
(l) Turn all cabinet switches to "on"
position except the wash blend switch -
which will be in the "Blend" position,
(k) Set TEL vernier in cabinet, with drive
shaft running, to same setting as shown
on Blend Order.
14. Set Up Component
(a) Start Dye pump by turning switch to "on"
and Master Panels
position on master panel.
to Start Blend
(b) Zero batch counter with master switch
in "reset" position.
(?) Set batch counter for required barrels
of total blend.
(d) Zero all totalizers cn component panels.
(e) Set- air controller pointers to control
"position" on each component panel, by
turning clutch so that screw on
assembly reads "4 o'clock."
(f) Turn panel selector switches to "on"
position of each component panel to
be used.
| WA-TEX 001879
t
PLANT; DEPARTMENT; CLASSIFICATION; OPERATIONS
JOB BREAKDOWN
Puget Sound RP&S-Docks-Raoks Assistant Pumper B-l Blend Gasolines - In-Line Method (Premium or Regular)
B-l Page 5
IMPORTANT STEFS
KEY POINTS
(g) Turn pump selector- switches to ''on" position cf each component pump to be used.
(h) Zero TEL, gasoline rate and Dye total izers on master panel.
(i) Turn selector switches to "on" position for TEL selector and TEL pump switch.
(j) Turn master switch from "reset" to "blend" -- at this time component products will start discharging Into blend header.
(k) Adjust master handwheel setting to 200.0 Man.. This will be at low rate and will tend to eliminate any undue surge on controllers and ehronoflo.
(l) Open No. 1 valve on top of TEL weigh tank. TEL should start entering blend.
(ra) Check all air controllers on board and see that- they are lining out.
(n) Check all pump suction and discharge pressures.
(o) Check by-pass on TEL Eductor and adjust to proper vacuum - 10 to 15 Inches.
(p) Run blend and check out all controllers, rates, etc. By this time, blend header should be cleared of any product from previous blend.
(q) Start rust inhibitor pump and RVP machine.
(r) Turn sampler selector switch to "on" position. Note.-. At this time, blend should be running normal, if alarm sounds and trouble is experienced, determine nature and correct. Souse cf the trouble spots to look for: Plugged strainer Meter not- turning Improper line-up TEL not entering blend due to vacuum switch not functioning properly, insufficient vacuum and ehronoflo not- putting out proper signal to TEL cabinet and loss of suction on Butane booster pump especially In summer.I
I WA-TEX 001880 I
\
PLANTS
DEPARTMENT; CLASSIFICATION; OPERATION:
JOB BREAKDOWN
B-I
" "*
Page 6
Puget Sound
RF&S-Docks-Racks
Assistant Pumper
B-l Blend Gasolines - In-Line Method
(Premium or Regular)
IMPORTANT STEFS
' ~~
KEY POINTS
(a) Start to Increase master handwheel setting, not to exceed 1200 bph with blend running normal, when TEL is required * On blends not requiring TEL, open master handwheel as high as controls on each component will allow,
ft) Note sample requirements on Blend Order. (uj Adjust blend component percentages as
advised to meet required specifications. (v) Read totalizers, batch counter, TEL
scale, RVP recorder, gauge component and blending tank every 4 hoars while blend
is in progress and record on Form PSP-19. From these readings it can be determined if components are being correctly blended on a percentage basts. (v) Blend to completion. When batch counter and register show the same figures, the blender will shutdown automatically but
will not stop pumps. (r) Turn master switch from "blend" to "off." (y) Push stop button Butane booster pump -
control on console. (z) Stop rust inhibitor pump. (aa) Stop RTF machine. (bhj Turn all switches on master and component-
panels to "off" position. (go) Close off blending, eductor pump and dye
pump manifolds. (dd) Close off component tankage. (ee) Close off blend line on finished tank if
not necessary to recirculate. (ff) Take closing readings on meters,
totalizers, TEL weigh scale and record
on PSP-19 and Blend Order FSF-S. (gg) Close gauge component, dye, rust inhibitor
and shipping tanks and record on Form
R-61A. (hh; Record totalizer re'tdlngs cxv R~6lA when
blending at 5>;00 A.M. stock and when blend completed,
! WA-TEX 001881
PIANTs
DEPARTMENTS CLASSIFICATIONS OPERATIONS
JOB BREAKDOWN
E-i
Puget Sound RP&S-Docks-Racka
Assistant Pumper B-2 Blend Middle Distillate - In-Line Method (448 Diesel - 454 Diesel and 431 Burner Oil)
IMPORTANT STEFS
KEY POINTS
10 General Information Each Important Step and Key Point is shown separately in the following breakdown, but
it does not mean that the operator is re stricted to take each step in the order
shown. The operator can save much time by partly or completely lining up for several Important Steps at the same time, especially at the beginning of the Blend, because so many of the blender functions are tied to gether.
2. Receive. Blend Order (a) Read Blend Order carefully.
Form PSP-2
(b) Determine product to blend, finished
tank number and total amount of blend.
(o) Determine component tankage, percentages
and quantities of each to use.
Note amount of Rust Inhibitor or other
additives to be used.
(e) Note any other information on Blend
Order such as sampling and special
line ups.
3 = Check Component Stocks Available
Gauge each component tank using console. Record gauges, time and blend number on Daily Oil Report - Form R-61A.
4. Check Stock In Finished Tank
<) Gauge tank to be blended into using console and record opening on R-61A.
Line Up Component Tankage
(a) Open component tankage to be used on each blend line suction to Blending Manifold.
Line Up Finished Product Tank
(a) Check blend line valves "closed" on tankage not to be blended into on same system. Notes At- present there is only
one tank for each grade of middle distil late and each grade has its own separate blend line, however, in the future our finished storage may change whereby two tanks could be on same blend line.
i WA-TEX 001882
PLANTS DEPARTMENTS CLASSIFICATION s
OPERATION:
JOB BREAKDOWN
B- Page 2
Puget Sound
RP&S-Docks-Racks
Assistant Pumper
B-2 Blend Middle Distillate - In-Line Method
(448 Diesel - 454 Diesel and 431 Burner Oil)
IMPORTANT STEPS
7, Conduct Teat-Run on Blender
REST POINTS
(b) Open regular blend nozzle cn tank to be blended, if gauge is below J'0" with jet nozzle closed,
(c) Open jet blend nozzle on tank to be blended if gauge is more than 7'0" with regular nozzle closed. Note: The suction or shipping line valve is to be left open on 448 Diesel and 431 Burner Oil while blending into this tank age unless otherwise advised, as we blend and ship these two products at the same time . When blending 454 Diesel, the suction valve is to be closed cn this tankage as nc shipments are made until tank c-kehed by Laboratory,
(a) Select component panels to be used, (b) Turn master switch from "off" to "test"
position, l,c) Adjust master handwheel between 200,0
and 300.0 approximately, lock in wheel with master drive running -- never ad just master^ Handwheel liinTess master"' drive IS"runnXHgT id) Turn mas5erswTtch from "test" to "reset". (e} Make component handwheel settings, using percentages as shown on the Blend Order from calibration curve and lock in hand wheels, (f) Zero all totalizers with switches in "off" position, (g) Clear Batch Counter Register to zero, by pushing reset button on master con trol panel. (hj Set Batch Counter at 100 barrels. {ij Turn master switch from "reset" to "test.1 This will start the master drive. When the register on the Batch Counter Regis ter reads 100 barrels, the board will automatically shut down.
j WA-TEX 001883
PLANTs DEPARTMENTS CLASSIFICATION: OPERATIONS
JOB BREAKDOWN
B-2 Page 3
Puget Sound
RP&S-Docks-Racks
Assistant Pumper
B-2 Blend Middle Distillate - In-Line Method
(448 Diesel - 4^4 Diesel and 431 Burner Oil)
IMPORTANT STEPS
8. Line-Up Component Pump Manifold
9. Line-Up Rust Inhibitor Pump
KEY POINTS* (l)
(J) Read totalizers on each component panel in use.
(k) Determine if amounts registered on each component totalizer check the percentages, as shown on the Blend Order. If compo nents check /'or - 0.3$, they will be considered ready for blending.
(l) Re-run test run If percentages are greater than / or - 0.3# as shown on Blend Order.
(m) Set Rust Inhibitor timer for required amount per 1^.000 barrels as shown on Blend Order.
(a) Open suction on all component pumps to be used and check all other Interconnect ing lines on suction closed,
(h) Open discharge of each component pump to be used into the Blend Header.
(e) Check discharge valves closed into Blend Header on those component pumps which may not be used during blend.
(d) Open bleeder on each pump* to be sure casing la flooded with product.
(e) Check all pump switches to be used in "auto" position and check switches in "off" position on pumps not to be used.
(f) Check air "on" to control regulating valves,
(g) Take opening meter readings on discharge of each component pump to be used and record on Form PSP-19.
!h) Check pump lubrication. (iji Check for leaks, such as, strainer and
meter housings, (j) Check all pump bleeders closed.
(a) Check suction on Rust Inhibitor storage tank open.
(b) Open suction and discharge on pump into Blend Header.
! WA-TEX 001884
PLANTS DEPARTMENTS CLASSIFICATION: OPERATION:
JOB BREAKDOWN
B-2
Page 4
Puget Sound
RP&S-Doc ka ~Rac ka
Assistant Pumper
B-2 Blend Middle Distillate - In-Line Method
(448 Diesel - 4p4 Diesel and 431 Burner Oil)
IMPORTANT STEPS
KEY POINTS
10. LineUp Salt Filter (a) Open bottom drawcff to sewer on salt filter Just long enough to check for
`free water and draw off If necessary. (b) Check inlet and outlet valves open on
salt filter. Note: When blending Diesel* use the West filter and when blending Burner Oil, use the East filter, (c) Open Blend Line Header valve and close bypass at East end steel walkway in blending component area. (d) Check all run down lines closed on discharge of Salt Filter Header* with run down valve open on line to tank that Is to be blended on East end steel walkway.
11. Set Up Component and Master Panels
to Start Blend
(a) Zero batch counter register with master switch In "reset" position.
(b) Set batch counter for required barrels of total blend,.
(c) Zero all totalizers on component panels. (d; Set air controller pointers to control
"position" on each component panel* by turning clutch so that screw on assembly reads "4 o'clock." (e) Turn panel selector switches to "op
position of each component panel to be used. (f) Turn pump selector switches to "on" position of each component pump to be
used. (g) Turn master switch from "reset" to
"blend" at this time component products will start discharging into Blend Header. fh) Start Rust Inhibitor pump.
(I) Adjust master handwheel setting at 200.0 maximum. This will be at low rate and
will tend to eliminate any undue surge on transmitters and controllers. (J) Check all air controllers on board, and see that: they are lining out.
WA-TEX 001885
PLANT: DEPARTMENTS CLASSIFICATION: OPERATION:
JOB BREAKDOWN
B-S
Page 5
Puget Sound
RP&S-Docks-Racks
Assistant Pumper
B~2 Blend Middle Distillate - In-Line Method
(448 Diesel - 454 Diesel and 431 Burner Oil)
IMPORTANT STEPS
KEY POINTS
(k) Check all pump suction and discharge pressures and check meter counters (registers) to determine if they are turning properly,
(l) Increase master handwheel setting to maximum that will allow each pump to stay in control on proper percentage basis, Note: At this time, blend should be run ning normal. If alarm sounds and trouble is experienced, determine nature and correct. Some of the trouble spots to
look for: Plugged Strainer
Meter not turning Improper line-up (m) Check sample requirements on Blend Order and follow through. Note: Automatic sampler is installed on Middle Distillate Blend Header, but it is not used. All required blended samples are taken in 1-qt. sample bottles directly off Blend Header after product has passed thru Salt Filter, (n) Adjust blend component percentages as advised to meet required specifications. (o) Read totalizers, batch counter, gauge component and blending tank every 4 hours while blend is in progress and record on Form. PSP-19. From these readings, it can be determined if components are being correctly blended on a percentage basis. (p) Blend to completion. When Batch Counter and register show the same figures, the Blender will shutdown automatically, but component pumps will continue to run. (q) Turn master switch from "blend" to "off." This will stop component pumps. (r) Stop R.ust Inhibitor Pump. ($) Turn all switches on master and component panels to "off" position. ft) Close component pump manifolds. (u) Close off blend line on finished tank if not required to recirculate.
, WA-TEX 001886
PLANT: DEPARTMENT: CLASSIFICATION: OPERATION;
JOB BREAKDOWN
B-2
Page 6
Puget Sound
RP&S"Docks-Raoks
Assistant Pumper
B-2 Blend Middle Distillate - In-Line Method
(448 Diesel - 454 Diesel and 431 Burner Oil)
IMPORTANT STEPS
KEY POINTS
(v) Take closing readings on meters and totalizers and record on PSP-19 and Blend Order PSP-2.
(w) Close gauge component rust inhibitor and finished tank and record on R-61A.
(x) Record totalizer readings on R-61A when blending at 5?00 A.M. stock and when blend completed.
Finished Blend Diesel - Burner.
j WA-TEX 001887
PLANTS DEPARTMENT; CLASSIFICATION; OPERATION;
JOB BREAKDOWN
B-3
Page 1
Puget Sound
RP&S-Docks-Raeks
Assistant Pumper
B-3 Blend AvJet- Fuels - In-Line Method
(AvJet and Burner Oil)
IMPORTANT STEPS
KEY POINTS
1 General Information Each Important Step and Key Point is shown separately in the following break-
down, but it does not mean that the operator is restricted to take each step in the order shown. The operator can save much time by partly or completely lining up for several Important Steps at the same time, especially at the begln-
* ning of the blend, because so many of the Blender functions are tied together.
2. Receive Blend Order (a) Read Blend Order carefully.
Form PSP-2
(b) Determine product to blend, finished
tank number and total amount of blend.
(c) Determine component tankage, percent
ages and quantities of each to use.
Note; AvJet Fuels are blended without
the addition of additives.
<d) Note any other information on Blend
Order such as sampling and special
line-ups.
3. Check Component Stocks
{a} Gauge each component tank to be used by console to determine if enough stock is available for blend.
(b) Record gauges, time and Blend Number on Daily Oil Report - Form R-61A.
4. Check Stock In Finished Tank
(a) Gaxige tank to be blended into using console and record opening on R-61A.
5. Line Up Component Tankage
(a) Open component tankage to be used on each blend line suction to Blending Manifold.
6. Line Up 5'inished Product Tank
(a) Check blend line valves closed on tankage not to be blended into on
same operation, Co) Open regular blend nozzle on tank to
be blended, if gauge is below 10*0" with Jet nozzle and shipping line . closed.
| WA-TEX 001888
PLANTS DEPARTMENTS CLASSIFICATIONS OPERATIONS
JOB BREAKDOWN
B-3
Page 2
Puget Sound
RP&S-Docka-Racks >
Assistant Pumper
B"3 Blend AvJet Fuels - In-Line Method
(Avjet and Burner Oil)
IMPORTANT STEPS
7. Conduct Test-Run . on Blender
KEY POINTS
(c) Open Jet blend nozzle on tank to be
blended If gauge is 10' O'1 or more
with regular nozzle and shipping
line closed# Notes No shipment of
Avjet
to be made while blending
into tankage, unless authorized.
Select component panels to be used. Turn master switch from "off" to "test" position# (c) Adjust master handwheel between 300#0 and 350.0 approximately and lock in wheel with Master Drive Running. Never adjust faster Randwheel unless blaster "Drive is running.
using percentages as shown on the Blend Order from calibration curve and lock in handwheels. Notes The Avjet Blender Board Is so adjusted that It can be set to run at 150$ if the com ponents to be blended will not over range the pumps and meters. The 150$ range will vary with each Blend Order, listing percent of each component. (f) Zero all totalizers with switches in "off" position. (g) Clear Batch Counter Register to zero, by pushing reset button on master control panel. (h) Set Batch Counter at 100 barrels. (l) Turn master switch from "reset" to "test." This will start the master drive. When the Batch Counter Regis ter reads 100 barrels, the board will automatically shut down. (j) Read totalizers on each component panel in use. (k) Determine if amounts registered on each component totalizer check the ' percentage as shown on Blend Order. If components check / or - 0.3$# they will be considered ready for blending#
WA-TEX 001889
PLANT?
DEPARTMENT? CLASSIFICATIONi OPERATION?
JOft BREAKDOWN
B-3
Page 3
Puget Sound
RP&S-Docks-Racks
Assistant Pumper
B-3 Blend Avjet Fuels - In-Line Method
(Avjet and Burner Oil)
IMPORTANT STEPS
8. Line-Up Component Pump Manifold
KEY POINTS
(1) Re-run test-run if percentages are greater than / or - 0,3# as shown on Blend order.
(a) Open suction on all component pumps to be used and check all other interconnecting lines on suction closed.
(b) Open discharge of each component pump to be-Jased into the Blend Header.
(c) Check discharge closed off blend header on product not to be blended and open discharge valve of blend header on product to be blended. Notej Avjet and Burner Oil discharge into a common Blend Header. Just beyond the Blend Header proper this manifold "ties" and Avjet runs to a separate run down line to tankage and Burner Oil runs to a separate run down line to tankage. The two block valves mentioned in item "c" are to be checked closely.
(d) Check discharge valves closed into Blend Header on those component pumps which may not be used during blend.
(e) Open bleeder on each pump to be sure casing is flooded with product.
(f) Check all pump switches to be used in "auto" position and check switches in "off" position on pumps not to be used.
(g) Check air "on" to control regulating valves.
(h) Take opening meter readings on dis charge of each component pump to be used and record on Form PSP-19 and PSP-2.
(i) Check pump lubrication. (j) Check for leaks, such as strainer
and meter housings.
! WA-TEX 001890
PLANTS DEPARTMENTS CLASSIFICATIONS OPERATION;
job
B-3 Page 4
Puget S.ound
RP&S-Docks-Racks
Assistant Pumper
B-3 Blend Avjet Fuels - In-Line Method
(Avjet and Burner Oil)
IMPORTANT STEPS
KEY POINTS (k) Check all pump bleeders closed.
9, Set Up Component . (a) Zero Batch Counter Register with
and Master Panelp
master switch in "reset" position,
to Start Blend
(b) Set Batph Counter for required
barrel*%^total blend.
(c) Zero all totalizers on component panels.
(d) Set air controller pointers to control "position" on each compon ent panel, by turning clutch so that screw on assembly reads "4 o'clock".
(e) Turn panel selector switches to "on" position of each component panel to be used.
(f) Turn pump selector switch to "on" position of eaoh component pump to
be used.
(g) Turn master switch from "reset" to "blend". At this time, component
products will start discharging Into Blend Header.
(h) On Burner Oil blends, line up Rust Inhibitor pump.
(i) Adjust master handwheel setting at 300.0 max. This will be at low rate and will tend to eliminate any undue surge on transmitters and
controllers. Blend rate not to exceed 400 bbls. per hour.
(J) Check all pump suction and discharge pressures and check meter counters (registers) to determine if they are
turning properly.
WA-TEX 001891
PLANTS DEPARTMENTS CLASSIFICATION? OPERATIONS
JOB BREAKDOWN
B-3
Page 5
Puget Sound
RP&S-Docks-Raoks
Assistant Pumper
B~3 Blend Avjet Fuels - In-Line Method
(Avjet and Burner Oil)
IMPORTANT STEPS
KEY POINTS
9. Set Up Component
and Master Panels to Start Blend (Continued)
(k) Increase master handwheel setting to max, that will allow each pump to stay in control on proper per centage basis. Note: At this time blend should be running normal. If alarm sounds and trouble is experi enced, determine nature and correct. Some of the trouble spots to look for ? Plugged strainer Meter not turning Improper Line-up
(l) Check sample requirements on Blend Order and follow through. Note; Automatic sampler is in stalled on Avjet Blend Header Line* but it is not used. At this writing, all required blended samples are taken in 1-qt. sample bottles directly off Blend Header.
(m) Adjust blend component percentages as advised to meet required speci fications .
(n) Read totalizers, batch counter, gauge component and blending tank every four hours while blend is in progress and record on Form PSP-19. From these readings it can be deter mined if components are being correctly blended on a percentage basis.
(o) Blend to completion. When batch counter and register show the same figures, the Blender will shut down automatically, but component pumps will continue to run.
(p) Turn master switch from "blend" to "off" position. This will stop component pumps.
WA-TEX 001892
PLANT*
DEPARTMENT: CLASSIFICATION s OPERATION?
JOB BREAKDOWN Page 6
Puget Sound RP&S-Docks-Racks
Assistant Pumper B-S Blend Avjet Fuels - In-Line Method (AtJet -ftid Burner Oil)
IMPORTANT STEPS
9* Set Up Component and Master Panels to Start Blend (Continued)
KEY POINTS
(q) Turn all switches on master and component panels to "off" position,
(r) Close component pump manifolds.
(s) Close off blend line on finished tank.
(t) Take closing readings on meters and totalizers and record on PSP-19 and Blend Order Form PSP-2.
(u) Close gauge component and finished tankage and record on Form R-61A.
(v) Record totalizer readings on R-61A when blending at 5:00 A.M. stock and when blend completed.
! WA-TEX 001893
JOB BREAKDOWN
PLANTS
Puget Sound
DEPARTMENT:
RP&S-Docks
CLASSIFICATIONS Assistant Pumper
OPERATION?
B-4 Draw Samples from Blend Header
B-4 Page 1
IMPORTANT STEPS
KEY POINTS
1. General Information (a) Blend line samples are drawn from a sample header located east of the
sample hut on 100 ft. pipeway at
Blending Pljaat,
2. Sampling
(a) Clear sample lines by running to drain.
(b) Sample hose should be inserted to . . the bottom of sample bottle,
(c) Draw sample slowly.
(d) If sample lines are so equipped, use rubber stopper. This prevents most vapors from escaping from
sample bottle.
(e) Put cork or stopper In bottle immediately.
3. Component Pump Sampling
(a) Each component pump is equipped with a 1/4" sample connection.
(b) Take samples slowly.
(c) Cork bottle immediately.
4. Bomb Samples
(a) Are taken from Butane component pumps upon request.
(b) A 1/4" sample connection is in stalled on each pump. Sample bombs
may be screwed directly to fitting
or a flex hose may be used.
(c) Bomb should be In an upright position, venting at top.
(d) Open both valves on bomb.
(e) Open line valves slowly.
! WA-TEX 001894
JOB BREAKDOWN
PLANTS DEPARTMENTS CLASSIFICATION s
OPERATION:
Puget Sound RP&S-Docks
Assistant Pumper B~4 Draw Sables from Blend Header
B-4 Page 2
uiiiiwLiiwiMMin * ' m "i nmiMtrr
IMPORTANT STEPS
KEI POINTS
4.. Bomb Samples (Continued)
(f) When liquid butane appears from top of bomb, close top valve first, then bottom bomb valve,,
(g) Close line valve and remove sample bomb slowly.
WA-TEX 001895
JOB BREAKDOWN
B-
PLANT;; DBF-' tTMENTs CIA- 3IFICATXON; OPE ATIONs
Puget sound Plant
RP&S"Docks
Assistant Pumper B~5 Draw Samples from Automatic Sampler
IMPORTANT STEPS
1, Line Up Automatic Sampler - S/C and P/C Blends
KEY POINTS
(a) Drain Sampler.
(t>) Pill Sampler to overflowing with fresh water.
(c) Close overflow valve, sight glass valve, and water supply.
(d) Open water displacement valve.
(e) Make sure sight glass shows full.
(f) Open suction and discharge valves to the blend line.
2. Start Sampler
(a) Follow instructions on blend order for starting of sampler and when samples are to be drawn, usually when sampler is full or once per
shifti 5 AM, 1 PM, and 9 PM.
3, Draw Sample
(a) Close water displacement valves on side of sampler.
(b) Open vent.
(c) Slowly add water to sampler.
(d) Open valve on top of sight glass to plastic hose.
(e) Clear water from line. Then in sert hose to the bottom of sample bottle, using attached rubber stopper to contain vapors in sample.
(f) Take required number of samples.
(g) Put stopper In sample bottles immediately.
4* Refill Sampler
(a) Increase water flow and overflow with water.
(b) Follow line up procedures.
. WA-TEX 001896
PLANT: DEPARTMENT: CLASSIFICATION $
OPERATIONS
JOB BREAKDOWN
B-6
Page 1
Puget Sound
RP&S-Docks
Assistant Pumper
B-6 Take Gauges by Remote Control Console
IMPORTANT STEPS
KEJT POINTS
1. General Information (a) Most all of our tanks are equipped with a float operated level gauge,
with a ground reading gauge on the side of the tank, A transmitter
on the ground reading gauge trans mits the product level to the con sole located in the Blending Plant Control Room, This is referred to as the VAREC gauge. Two thermome
ters are on most tanks. One for local dial reading, the other is used for transmitting the tempera ture to the console in the same
manner as gauges.
2. Tank Gauging
(a) Dial desired tank number - slowly.
(b) In approximately 6 to 8 seconds, tank number and tank gauge will show in console window.
(c) Gauge will remain for approximately 10 seconds, then clear. Notes Reset button may be used to clear gauge from console if desired. If wrong tank Is dialed - wait until digital pulse code has completed its cycle before using reset button.
3. Tank Temperature
(a) Dial desired tank.
(b) Wait for gauge to appear.
(c) Press temperature button.
(d) Pulse code will cyele as in gauging and tank number and temperature will appear in console window. Reset button - Follow instructions on gauging procedures.
WA-TEX 001897
PIANTs DEPARTMENTS
CLASSIFICATIONS OPERATIONS
JOB BREAKDOWN
B-6
Page 2
Puget Sound
RP&S-Docks
Assistant Pumper
B-6 Take Gauges by Remote Control Console
IMPORTANT STEPS
KEY POINTS
4. Scan Operation
(a) The tank farm Is divided into three
General Information
areaso Tankage in any given area
is shown in R-295 A, with a few ex
ceptions. Area selector switch is
located to the left of tank dial*
Scan will begin with first tank in
the selected area. It will give
tank gauge, then temperature and
then go on to the next tank gauge
and temperature, etc., through the
entire group of tanks in that area.
5. Start Scan ...
(a) Select area to be scanned.
(b) Press "Scan Start" button.
6. Stop Scan
(a) While a gauge or temperature is showing on console window, press "Scan Stop" button. Console will continue to scan selected area until "Stop Scan" button is pushed.
WA-TEX 001898
JOB BREAKDOWN
PLANT? DEPARTMENT;
CLASSIFICATION? OPERATION?
Puget Sound RP&S-Docks Assistant Pumper B-7 Records and Reports
B-7 Page 1
IMPORTANT STEPS
KEY POINTS
R-295-A - Gauges and Pumping Record
1* General Information (a) R-295-A is to be made out daily. Original and four copies. Gauges are to be taken at 8-hour inter vals - 5 AM, 1 PM, 9 PM. Stock gauges are to be taken on moving tanks as close to 5 AM as possible. Standing tanks can be gauged and
temperatures taken before this time.
2f. Gauge Tanka-.- 5 AM
(a) Dial desired tank.
(b) Record gauge and temperature on R-295-A.
(o') Check gauge with previous gauges to make certain tank is gaining or losing as operations warrant. A standing tank should only change due to temperature change.
Any unusual product movement should be noted. If necessary, the Varec should be checked on the tank and a hand tape gauge may be required.
(d) If hand tape gauge or Varec gauge is recorded on R-295-A, such should be identified by an (h) or (V) after the gauge.
3. BSSsW or Water Gauge (a) Are entered on R-295 the first of each month and carried forward each
day until a new gauge is taken.
(b) Water gauges are taken by hand tape, and must be entered in the "Black Band Book." Before a change can be
made on R-295-A, the time and date must be entered in the "Black Hand
Book."
| WA-TEX 001899
JOB BREAKDOWN
PLANT:
DEPARTMENT: CLASSIFICATION: OPERATIONS
Puget Sound
RP&S-Docks Assistant Pumper B-7 Records and Reports
B-7 Page 2
IMPORTANT STEPS
KEY POINTS
4. Temperatures
(a) Are recorded on R-295-A at 5 AM.
(b) Crude tank temperatures are recorded at 5AM, 1 PM and 9 PM. At various times, requests will be made to re cord temperatures of other tanks at gauging time,
5. "To" and "From" Columns
(a) These columns will indicate flow of product "to" or "from".tankage and where.
(b) When a change is made in tankage lineup, the time should be noted in these columns.
6. Disposition of R-295-A Form and
Copies
(a) Original to Stock & Shipping Dept,
(b) 2 carbon copies to Shift Foreman's Office,
(c) 1 carbon copy to RP&S Office.
(d) 1 carbon copy to Blending Plant file.
7. Notify TJhits of Tank Gauges
(a) Dally - After 5 AM gauging has been completed, phone the VPS, FCCU, HTU and Alky. Give them the 5 AM tank
gauges they require.
R-61-A - Daily Oil Report
8. General Information
(a) R-61-A is to be made out with Original and two copies. We usually
make out three sets to cover the following work in the RP&S Dept.: 1. Blending 2. Shipping
3= Transfers.
Original to Stock Dept., 1 copy to RP&S Office, and 1 copy to Blending
Plant file.
WA-TEX 001900
JOB BREAKDOWN
PLANTS DEPARTMENTS CLASSIFICATIONS OPERATIONS
Puget Sound RP&S-Docks
Assistant Pumper B-7 Records and Reports
B-7 Page 3
IMPORTANT STEPS
KEY POINTS
R-6I-A - Dally Oil Report (Continued)
9. Blending R-61-A
(a) Enter starting blends. In left column, list component tanks and additive tanks. Show opening gauges and temperatures. Show finished product tank In right column. Indicate blend number, gauge, temperature, and time blend started.
(b) At 5 AM, record the blend panel reading for each component tank used in the blend. Record gauges
on additives injected. Show finished tank gauge and temperature,
(c) completed blends are to be handled the same as for 5 AM gauging.
10. In-Line Blending
(a) Starting - Same as starting regular
blend except log the opening component blend meter readings.
(b) Finish - Same as 5 AM gauging except log the closing component blend meter readings.
11. Shipping
(a) Record opening tank gauge and temperature. (If hand tape gauge
Is recorded. Identify as such.) For vessel being loaded, record time gauges are taken and time actual loading begins. Notify Truck Rack.
(b) Periodic check gauges are to be made on all tanks being shipped and this information Is to be
given to the point of delivery.
Only In this way can you determine rate of flow and establish loadingtime.
WA--TEX 001901
JOB BREAKDOWN
PLANT! DEPARTMENTS CLASSIFICATION:
OPERATION:
Puget Sound RP&S-Docks Assistant Pumper B-7 Records and Reports
B-7 ,
Page 4
IMPORTANT STEPS
KEY POINTS
R-61-A - Dally Oil Report (Continued)
11. Shipping (Continued)
(c) Closing--Record openings on every other line on the sheet. Closing gauges are to be recorded directly below opening gauges. Times are Important, l.e. gauging time, and shut down loading time.
12. TransMountain, Olympic Pipeline and Transfers
(d) 5 AM gauges are to be recorded daily. Should a vessel or barge finish loading before 8 AM, it is permissible to hold this R-61-A until shipment is completed. Enter closing gauges, and forward original to Stock Dept, before 8 AM.
(a) T/M and QPL are to be handled the same as shipping. Record opening and closing gauges.
(b) All transfers of products between tanks are to be recorded showing tank number, gauges, temperature, and times.
R-67-A - Texaco Inc. Receipt
13. General Information (a) To be filled out for deliveries of bunker fuel to shipB and spent caustic to N.W. Petrochemical Plant.
14. Ship Fueling
(a) Fill in heading, plus gravity, flash, and viscosity of this fuel.
(b) Record opening gauge, temperature, and gross barrels. Record closing gauge, temperature and gross barrels.
(c) When personnel are available in the Shipping Dept., they will compute the net barrels. At other times, . we must compute net barrels.
k-.J*
I WA-TEX 001902
JOB BREAKDOWN
PLANTS DEPARTMENTS CLASSIFICATIONS OPERATIONS
Puget Sound RP&S-Docks
Assistant Pumper B-7 Records and Reports
B-7 Page 5
IMPORTANT STEPS
KEY POINTS
R-67-A - Texaco Inc,, Receipt (Continued)
14. Ship Fueling (Continued.)
(d) Send all copies to the dock for Chief Engineer's signature and give him yellow copy. All other copies go to the Shipping Dept.
15. N0W0 Petrochemical
(a) Spent caustic transfers from Tank 303 to N.W. Petrochemical are covered by R-67-A. Fill in heading, opening and closing tank gauges, temperature and gross barrels,,
(b) All copies are to be sent to the Shipping Department.
WA-TEX 001903
JOB BREAKDOWN
PLANT! DEPARTMENT! CLASSIFICATION s
OPERATIONS
Puget Sound RP&3-Docks Assistant Pumper
B-8 Dye Mixes
IMPORTANT STEPS
B-8 Page 1
KE3T POINTS
1. General
(a) We are now using Ethyl Corporation^ Red-B liquid and yellow liquid dyes. The dyes come in 240 lb. barrels.
Refer to RP&S Additive Manual or Instructions on mix composition. , Dye mixes can be made while circu lating a dye tank, or It is more common to inject the dye while filling the dye tank with Hvy. Plat, or Lt. Plat. T.M.D. is also mixed in dye tanks to provide the amount of T.M.D. required in gasoline . blends.
2. Prepare to make Red (a) Gauge Tank 66 and record on R-61-A.
Dye Mix in Tank 66
Compute the amount of Hvy. Plat.
required to fill tank 66.
(b) Using Additive Instruction Manual, determine amount of red dye and T.M.D. to be used,
(c) Line up red dye pump, 24N-GM11, to take suction on Tank 30, Hvy. Platformate. Then discharge to Tank 66 through dye eductor in dye mix room.
3. Make Mix
(a) Start Pump.
(b) Check Tank 66 gauge for increase.
(c) Close eductor bypass valve in dye mix room.
(d) Weigh red dye barrel and determine the necessary closing scale weight.
(e) Slowly open valve to eductor hose; make sure you have a vacuum.
(f) Draw desired amount of dye by scale weight.
I WA-TEX 001904
JOB BREAKDOWN
PLANT; DEPARTMENT; CLASSIFICATION*. OPERATION:
Puget Sound RP&S-Docks Assistant Pumper B-8 Dye Mixes
B-8 Page 2
IMPORTANT STEPS
KEY POINTS
4. Adding T.M.D. to Mix (a) Weigh T.M.D. barrel and determine the closing scale weight.
(b) Open valve to eductor hose.
(c) Close valve when the desired amount of T.M.D. has been injected.
(d) Open eductor bypass valve.
5. Completing Mix
(a) Check Tank 66 gauge level. Fill tank to 23'-0". Watch closely, tank fills rapidly.
(b) Shut down pump.
(c) Close Tank 30, Hvy. Plat, suction to pump.
6. Record on R-61-A
7. Copper Dye to Tank 67
(d) Open Tank 66 to suction.
(e) Start pump for circulating to Tank 66. Mix for two hours.
(f) Catch 1-quart sample for color. Send to- the Laboratory properly tagged.
(a) Closing gauge of Tank 66.
(b) Number pounds red dye used.
(c) Number pounds T.M.D. used.
(d) Record same Information in Blend ing Plant dye mix log book.
(a) Use pump 24N-GM10 and Light Platformate Tank 24.
(b) Follow red dye procedure except we use both red and yellow dye to make copper color. Refer to Additive Instruction Book for "mix".
j WA-TEX 001905
#
JOB BREAKDOWN
PLANT: DEPARTMENT: CLASSIFICATION: OPERATION:
Puget Sound
RP&S-Docks Assistant Pumper B-8 Dye Mixes
IMPORTANT STEPS
B-8 Page 3
KEY POINTS
8. Yellow Dye to Tank 64
(a) Use red dye pump 24N-GM11 and Tank 30 Hvy. Plato
(b) Be sure to close valves on Tank 66 and pump valves to Tank 66, then open suction to Tank 64 and pump discharge to Tank 64.
(c) Pollow red dye procedure. Refer to Additive Instruction Book for "mix".
WA-TEX 001906
JOB BREAKDOWN
PLANT; DEPARTMENT; CLASSIFICATIONt OPERATION;
Puget Sound RP&S-Docks Assistant Pumper B-9 Petrox to Dock
B-9 Page 1
IMPORTANT STEPS
KE3T POINTS
1. General Information (a) Marine shipments of Fire Chief and Sky Chief gasoline accounts in
Alaska, Port Townsend and Port
Angeles require Petrox.
Small shipments are handled from the dock Petrox trailer. When large shipments are made, Petrox is in jected at the dock to treat the - gasoline which is already in the lines. The balance of the cargo is treated from the Blending Plant.
2. Prepare to Load. S/C (a) Determine the amount of Petrox to
with Petrox
be used. (Check Additive Instruc
tion Book.) Gauge tank and enter
gauge on R-61-A.
(b) Line up pump 24N-GM12 through S/C Petrox meter.
(c) Turn pump switch to automatic.
(d) Set meter stop. Meter injects 4 gallons Petrox for each gallon shown.
3,, Loading
(a) Start loading the ship or barge. The doekman will Inject approxi mately 788 gallons of Petrox from the trailer.
(b) Start Petrox pump and meter.
(c) Check frequently. Compare the Petrox Injection rate to the gasoline loading rate.
(d) Have all Petrox in the line before
the last 2800 bbls. of gasoline is pumped Into the dock line.
| WA-TEX 001907
JOB BREAKDOWN
PLANT: DEPARTMENT: CLASSIFICATION: OPERATION:
Puget Sound RP&S-Docks Assistant Pumper B-9 Petrox to Dock
B-9 Page 2
IMPORTANT STEPS
KEY POINTS
4. Finish Loading
5,, Load F/C with Petrox Added
(a) Shut down pump. Pump will not shut off automatically.
(b) Gauge Petrox tank and record the gauge on R-67-A.
(a) Determine the amount of Petrox to be used.
(b)- Gauge tank and record the opening gauge on R-61-A.-
(c) Line up pump 24N-GM25 through F/C Petrox meter.
(Balance of procedure same as S/C Petrox loading.)
O
i WA-TEX 001908
PLANTS
DEPARTMENT; CLASSIFICATION;
OPERATION;
JOB BREAKDOWN
Puget Sound RP&S-Docks Assistant Pumper B-10 Operate LPG Dryers and Heaters
B-10 Page 1
IMPORTANT STEPS
KE3f POINTS
1. General Information (a) There are no alarms to Indicate that an LPG dryer is spent or "wet". How ever, a dryer will normally last in excess of two weeks before regenera
tion is required. To insure constant production of dry LPG, the dryers will be switched every two weeks and the dryer taken out of service will be re generated, This schedule will also be governed by the availability of Cascade Natural Gas and the dryness of the LPG
In storage. Normal LPG' flow through a dryer is in the bottom and out the top,
2. Changing Dryers
(a) Open LPG inlet and outlet valves to the recently regenerated dryer.
(b) Close LPG inlet and outlet valves to the spent wet dryer.
3. Prepare Dryer for Regeneration
(a) Notify Alky-Poly that you will regenerate a dryer.
(b) Open a flow of Cascade Gas through the heater and into the top of the
dryer.
(c) Push liquid LPG out the bottom LPG valve into the dryer in service.
(d) Close the bottom LPG valve.
4. Start Regeneration
(a) Line up Cascade Gas flow from bottom of dryer back through cooler to fuel gas.
(b) Regulate gas flow to approximately 7 psi on gauge.
(c) Start water through the cooler.
(d) Turn on electric heater.
| W&-TEX 001909
JOB BREAKDOWN
PLANT; DEPARTMENT? CLASSIFICATION; OPERATION:
Puget Sound RP&S-Docks Assistant Pumper B-10 Operate LPG Dryers and Heaters
B-10 Page 2
IMPORTANT STEPS
KEY POINTS
4. Start Regeneration (Continued)
5. Regeneration Time
6. Regeneration Finished
(e) plug In recording instruments In B/P Control Room.
(f) Record starting,time and which dryer Is being regenerated in the log book.
(g) Notify Shift Foreman Cascade Gas is being used.
(a) 5 to 6 hours time is required to bring temperature up to 375-400 F.
(b) Regenerate for 16 hours at this temperature. (This may vary due to condition of dryer and allot ment of natural gas.) The heater is equipped with high temperature and low flow alarms.
(a) Turn off electricity to heater.
(b) When vessel cools to 100-125* the regeneration cycle is completed.
(c) Close all valves on the Cascade Natural Gas line up.
(d) Turn off water to cooler.
(e) Notify Shift Foreman that RP&S is through using Natural Gas.
! WA-TEX 001910
PLANTS
DEPARTMENTS CLASSIFICATION OPERATIONS
JOB BREAKDOWN
Puget Sound RP&S-Docks Assistant Pumper B-ll Filter - LFG Coalescer
B-Xl
IMPORTANT STEPS
KEY POINTS
1. General Information (a) Coalescers Fram-Warner Lewis located North of LPG Dryers and upstream from LPG Dryer.
2. Purpose
(a) Will collect excess water and impurities from wet LPG liquid
before flow enters LPG Dryer.
3. Daily Routine
(a) Coalescer is equipped with an automatic water drawoff. It should be checked each shift to determine if it Is working
properly. If frost forms on the vent or drain line this indicates the automatic water drawoff is not working properly. Water will have to be drained from the coalescer
manually until repairs are made on automatic water drawoff. The coalescer is also equipped with a high water level alarm.
j WA-TEX 001911
V.
PUNT: DEPARTMENT?
CLASSIFICATION; OPERATION;
JOB BREAKDOWN
Puget Sound RF&S-Docks Assistant Pumper B-12 Filters - Salt
B-12
IMPORTANT STEPS
KEY POINTS
1. General Information (a) After determining; that the Diesel Blend component pumps are routed through the salt filter in service.
line up Diesel header to finished tankage. The second salt filter is held in reserve.
2. Location
(a) Southeast corner of Blending Plant area.
3. Purpose .
(a) The salt removes moisture and cleans and brightens the finished product,.
A, Daily Routine
(a) Draw all water from bottom of filter once every shift.
WARNINGs BYPASS SALT FILTERS -
1. When circulating Diesel tanks.
2. Anytime blend line pressure exceeds 80 psig. The PRV relieves to the impounding basin North of Blending Plant.
WA-TEX 001912
JOB BREAKDOWN `
PLANT: DEPARTMENT: CLASSIFICATION: OPERATION:
Puget Sound RP&S-Docks Assistant Pumper B-13 Filters - Product
IMPORTANT STEPS
B-13 KEY POINTS
1. General Information (a) At the South end of the shipping manifold, filters are installed in the Fire Chief, Sky Chief, Burner Oil and 448 Diesel lines to the Truck Rack. The low lead
' gasoline filter Is located East of the Loading Rack* Two Avjet filters at the Dock are not in use.
2. Daily Routine
4
(a) Daily between 6 and 8 AM -
1. Check filters for water.
2. Check pressure drop across filter while loading a truck. Should pressure drop be in excess of 15 lbs. notify RP&S Foreman.
WA-TEX 001913
JOB BREAKDOWN
PLANT; DEPARTMENT; CLASSIFICATIONj OPERATION:
Puget Sound RP&S-Docks Assistant Pumper B-l4 Dock Line Relief
B-l4
IMPORTANT STEPS
KEY POINTS
1. General Information (a) When the dock finished product lines are not in active use, they are pressure relieved at the b/P through 1" crossovers to finished tankage Instead of relying on PRVs at the dock.
2. Location
(a) S/C and F/C relief lines are located on shipping manifold.
(b) Diesel, Burner Oil and Avjet re lief lines are located West of the component pumps in the 100 ft.
pipeway.
(c) Bunker Fuel Oil relives through the shipping pump back to tankage. The check valve Is removed on the shipping pump.
3. Operation
(a) Valves on relief lines are to be closed when shipping to dock.
(b) After each shipment is completed, open relief crossover. Dock Diesel lines can be relieved to either 448 or 454 Diesel tankage. Extreme oare must be taken to prevent products from being mixed.
(c) The block valves for all PRVs are sealed in the open position.
*3
I WA-TEX 001914
JOB CONTENT
PLANT:
Puget Sound
DEPARTMENT:
RP&S-Docka
CLASSIFICATION: pumper
Page 1 TRAINEE:
B0 ON THE JOB TRAINING
DATE
1. Responsible for RP&S Operations
2. Review Operations With Relief
3. Acknowledge and Acquaint Personnel With Operating Orders
4. Checjc Unit Operations
3. Check RP&S Equipment
6. Coordinate Activities of Shift Crew
7. Checjc Tank- Inventories
8* Maintain Operating Materials and Supplies
9. Maintain Safety Equipment
10. Direct Safe Work Performances
11. Cheo& Fire Equipment
12. Inspect and Approve Vessels and Equipment'for Repairs and Maintenance
a o Drain, Flush and Gas Free
b. Arrange for Gas Tests
c. prepare Safety Work Permit, R-241-A 7. *
d. Prepare Hot Work Permit, R-241
e. Direct Placement of Blinds
13>v Maintain.Records and Reports
a. Operating Log
b. Run Sheets
c. Repair List
NAME
WA--TEX 001915
JOB CONTENT
PLANT:
Puget Sound
DEPARTMENT:
RPfcS-Doeks
CLASSIFICATION: Pumper
Page 2 TRAINEE:
B. ON THE JOB TRAINING (CONT.)
14. Direct Clean Up and Housekeeping
15. Direct Running Maintenance
16 Coordinate unit Operations with
Other Units and Departments
1
17* Relieve Crew Members
18. Train and Direct Training of Crew Members.
19* Direct Emergency Procedures
DATE
NAME
Note: "
Pumper also required to perform all iteraB listed on the Job Contents of the Pumper Helper B* Pumper Helper A and Assistant Pumper.
Employe Qualified: Signed
Foreman
WA-TEX 001916
JOB CONTEST
PLANTS
Puget Sound
DEPARTMENT;
RP^S-Docks
CLASSIFICATION s Pumper
Page 2 TRAINEE:
Be ON THE JOB TRAINING (CONT,,)
14. Direct Clean Dp and Housekeeping
15. Direct Running Maintenance
16. Coordinate Unit Operations with Other Units and Departments
i
17. Relieve Cpew Members
18*- Train aijdf Direct Training of Crew . Members.
19. Direct Emergency Procedures
DATE
NAME
0
Note:
Pumper also required to perform all items listed on the Job Contents of the Pumper Helper B, Pumper Helper A and Assistant Pumper.
Employe Qualified: Signed:
Foreman
! WA-TEX 001917