Document bOVdJz2ZZaGMLkL40BooraQnD
/
c
PART IX - ADDITIONS TO UNIT SERVICES POLYETHYLENE UNIT - PLANT 510 PROJECT 64-12 930-6548
PORT LAVACA, TEXAS NOVEMBER 10, 1964
017445
UNION CARBIDE CHEMICALS COMPANY
DATE
SHOP ORDER TRANSMITTAL H-10-64
SHEET
1 of 1
"project 930-6548 - Part DC -
additions to Unit Services
location poly "A" Expansion
DISTRIBUTION
J. F. Tamborello
D. F. Peyton
!. D. Adkison
D. L. Buchanan
J. H. Wieting
Brown & Root - See Rote
J. M. McBride
R. G. Ziefle
L. Wiley
f. Rogstad
J. J. Walthall
G. L. Funk
DRAWING N Vie ER
SHOP OROER
major subject issued for
ISSUE 8.M. NO.
Design Report
T RAN SM 1 TT AL NO .
transmittal
2
1 1 1 1 1 1 1
attachments
3 1 1 1 1 5
2
1
DESCRIPTION
SK-80517 SK-80523
930-6548
Design Report - High Pressure Polyethylene Plant Ho. 1 Expansion - Seadrlft Plant Part DC - Additions to Unit Services
Flow Sheet
Flov Sheet
A
^..
-Jr 1
v &F' O
M . 13
fK! ^
'*1 P. f'}' j-
if*? y
V
y
m it
017446
REMA rks
Please acknowledge receipt by signing copy of transmittal and returning to Jo Ann Goldman.
J. F. Tamborello
ISSUEO BY
J. F. Taaborello
issued by
Design Report High Pressure Polyethylene
Plant No. 1 Expansion Seadrift Plant
Part IX - Additions to Unit Services 930-65^8
Foreword
This section of the design report describes miscellaneous additions to unit services required in support of the polyethylene plant expansion. Unit services additions are to be issued with individual job numbers and added to this report as needs arise. This report initially contains.
Job I
Addition of Dowtherm Pump Cooling Water System
Job II
Revisions to North Reactor Panel Board
Job III
Air Conditioning of Reactor Console Area Bldg. 102
Job IV
Rearrange No. 3 Reciprocating Primary Pump Piping
017448 1
Job IV
Rearrange No. 3 Reciprocating Primary Pump Piping Sketch None
The existing reciprocating primary pumps Items 6036E-201 thru 203 are connected to ethylene inlet piping and intensifier suction piping in such a manner that pumps labeled 1 and 2 serve as spare primary pumps for the No. 1 plant and pump No. 3 serves as an isolated spare for the No. 2 plant. In this arrangement, production is curtailed when either primary pump 4 or 5 is out of service for repair because the capacities of the replacement reciprocating pump so piped is inadequate.
The purpose of this rearrangement of reciprocating primary pump piping is to connect the pump in parallel so that they operate together as an effective spare for either pump 1+ or 5-
This is a rearrangement of existing piping and all work to complete the job should be charged to 03711-9-26993*
1. Disconnect and blank the connection of No. 3 reciprocating primary pump to the No. 2 plant suction header 3" 6256-P-lOl. Reconnect No. 3 reciprocating primary pump suction to blanked off connection in No. 1 plant suction header V 603J4-P-IOI.
2. Disconnect and blank the connection of No. 3 reciprocating primary pump to the No. 2 plant primary pump discharge header 3" 6256 P-102. Reconnect No. 3 reciprocating pump discharge to blanked off connection in the No. 1 plant primary pump discharge header 6036 3" P-225.
3. Rearrangement of primary pump suction line should conform to piping specification No. 155*
4. Rearrangement of primary pump discharge piping should conform to piping specification No. 158.
5. The existing extensions of the No. 3 reciprocating primary pump piping to the No. 2 plant piping are sufficiently long to be reusable as material to reconnect the pump to No. 1 plant header. Plans should be made to complete the necessary pipe revisions during the all plant shutdown, which will be required as part of Project 64-12.
- 6a -
017449
N oiz.TH Pa n e l B o a r .d B l d g 102.
UNION CARBIDE CHEMICALS COMPANY
'roject 930-6548 - Part IX dditions to Unit Services location Poly "A" Expansion
distribution
J. F. Tamborello D. F. Peyton
. D. Adkison D. L. Buchanan J. H. Wieting Brown & Root - See Rote J. M. McBride R. G. Ziefle
GATE
SHOP ORDER TRANSMITTAL 11-10-04
5h E E T 1 Of 1
major subject Design Report
TRAN SMI T T A L NO .
ISSUED FOR
TRANSMI T T A L 2 1 1 1 1 1 1 1
ATTACHMENTS
3 1 1 1 1
5 2 1
Please acknowledge receipt by signing copy of transmittal and returning to Jo Ann Goldman.
017451
J. F. Tamborello
ISSUED BY
High Pressure Polyethylene Plant No. 1 Expansion - Seadrift Part IX - Addition to Unit Services. Also replace page 7
_ 01/452
J. F. Tanborello
Design Report High Pressure Polyethylene
Plant No. 1 Expansion Seadrift Plant
Part IX - Additions to Unit Services 930-65'1+8
Foreword
This section of the design report describes miscellaneous additions to unit services required in support of the polyethylene plant expansion. Unit services additions are to be issued with individual job numbers and added to this report as needs arise. This report initially contains.
Job I
Addition of Dowtherm Pump Cooling Water System
Job II
Revisions to North Reactor Panel Board
Job III Air Conditioning of Reactor Console Area Bldg. 102
-1-
y
017453
ISSUED BY
Design Report High Pressure Polyethylene
Plant Ho. 1 Expansion Seadrift Plant
Part IX - Additions to Unit Services 930-65^8
Foreword
This section of the design report describes miscellaneous additions to unit services required in support of the polyethylene plant expansion. Unit services additions are to be issued with individual job numbers and added to this report as needs arise. This report initially contains.
Job I
Addition of Dowtherm Pump Cooling Water System
Job II
Revisions to North Reactor Panel Board
Job III
Air Conditioning of Reactor Console Area Bldg. 102
Job IV
Rearrange No. 3 Reciprocating Primary Pump Piping
017455
1
Job IV
Rearrange No. 3 Reciprocating Primary Pump Piping Sketch None
The existing reciprocating primary pumps Items 6036E-201 thru 203 are connected to ethylene inlet piping and Intensifier suction piping in such a manner that pumps labeled 1 and 2 serve as spare primary pumps for the No. 1 plant and pump No. 3 serves as an isolated spare for the No. 2 plant. In this arrangement, production is curtailed when either primary pump 4 or 5 is out of service for repair because the capacities of the replacement reciprocating pump so piped is inadequate.
The purpose of this rearrangement of reciprocating primary pump piping is to connect the pump in parallel so that they operate together as an effective spare for either pump 4 or 5-
This is a rearrangement of existing piping and all work to complete the job should be charged to 03711-9-26993.
1. Disconnect and blank the connection of No. 3 reciprocating primary pump to the No. 2 plant suction header 3" 6256-P-lOl. Reconnect No. 3 reciprocating primary pump suction to blanked off connection in No. 1 plant suction header 4" 6034-P-101.
2. Disconnect and blank the connection of No. 3 reciprocating primary pump to the No. 2 plant primary pump discharge header 3" 6256 P-102. Reconnect No. 3 reciprocating pump discharge to blanked off connection in the No. 1 plant primary pump discharge header 6036 3" P-225.
3. Rearrangement of primary pump suction line should conform to piping specification No. 155.
4. Rearrangement of primary pump discharge piping should conform to piping specification No. 158.
5- The existing extensions of the No. 3 reciprocating primary pump piping to the No. 2 plant piping are stifficiently long to be reusable as material to reconnect the pump to No. 1 plant header. Plans should be made to complete the necessary pipe revisions during the all plant shutdown, which will be required as part of Project 64-12.
- 6a -
017456
-7-
1 0 2BN ok.t h Pan el B o a (2_d
ldg
DESIGN REPORT HIGH PRESSURE POLYETHYLENE
PLANT NO. 1 EXPANSION SEADRIFT PLANT
PART IX - ADDITIONS TO UNIT SERVICES 930-65^8
Written by: J. F. Tamborello
ENGINEERING DEPARTMENT UNION CARBIDE CHEMICALS DIVISION
PORT LAVACA, TEXAS
NOVEMBER 10, 1964
017458
Design Report High Pressure Polyethylene
Plant No. 1 Expansion Seadrift Plant
Part IX - Additions to Unit Services 930-6548
Foreword
This section of the design report describes miscellaneous additions to unit services required in support of the polyethylene plant expansion. Unit services additions are to be issued with individual Job numbers and added to this report as needs arise. This report initially contains.
Job I
Addition of Dovtherm Pump Cooling Water System
Job II
Revisions to North Reactor Panel Board
Job III
Air Conditioning of Reactor Console Area Bldg. 102
Job TV
Rearrange No. 3 Reciprocating Primary Pump Piping
017459
1-
Job I
Closed Cooling Water Cycle for Dovtherm Pump Jackets & Bearing Housings
SK-80517
Existing plant cooling water piping servicing Dovtherm pump jacket and bearing housings is too small to handle additional Dovtherm pumps to be added as part of project 04-12. Additional services must be provided.
The closed cooling water system (Job i) will:
1. Provide adequate supply of cooling water to all Dovtherm pumps in Poly "A" area.
2. Eliminate the sewering of approximately 190 gpm of plant cooling water.
3. Provide a clean, salt free, cooling water avoiding the fouling of pump cooling jackets.
Job Description
(1) Extend existing No. 1 plant pelleter water cycle header 60V7W-907 and pelleter return water header 60hlW-76h, as shown on sketch with new V and 3" piping 65h8W-901, 902, 903 and 90k.
(2) Provide^ - 1
take off piping from each header 65^8W-902
and 903 Use
supply and return branch lines fmm tlru
11111,0 to each Dovtherm pump. Provide
valves No. 1 on each individual 3^" supply and return branch.
/= r ? - .
(3) All new piping is to be charged to 930-65^+8.
(M This job should be accomplished in the following sequence:
(a) Install header 65^8W-902 and all header valves in advance of the plant shut down.
(b) With 3" header valve (7) closed, supply cooling water tQ_ new Dovtherm pumps by connecting fire hose to valve vWjand temporarily sewering the water from the pump.
(c) When the final No. 1 plant reactor is shut down the rest of this syBtem as shown can be installed, and placed in service.
(d) Connect existing pumps to new cooling water headers as No. 2 plant reactors are shut down for routine purposes.
2 017460
(5) Remove and retire headers 6112W-763 and 764 under product
room floor. All work done to remove headers is to he charged
to 829"34.
' '`
(6) Heat exchangers 6047E-937 and 950 are to be left mounted on existing bases. New system is arranged so that a closed cooling water circuit is provided for Dovtherm pumps, utilizing pump 6047E-936A or 936b and one of the existing coolers.
-3-
017461
Description of Job II
SK-S0523
(1) Move existing instruments on north panel hoard, ' A,, which is adjacent to reactor console to accommodate the following:
(a) New panel mounted instrument switches and alarm lights for the return gas system additions on work order 930-65^5.
(b) Relocation of instruments on south panel, (B-, as described in Job III this report.
(c) Relocation of instruments from the Dovtherm instrument panel.
(2) Provide for future instrument additions which will be required by work order 930-6550.
(3) The cost to relocate all existing instruments is to be charged to 03711-9-26993-
(4) See SK 510-o5^8E-902 for location of new instruments on north panel board.
-h -
017462
Job III
Air Condition Reactor Console Area in northeast corner of Building No. 102. (Engineering of Job III is to be handled by the Seadrift Plant Engineering Group.)
SK-80523
Job Description
(1) Remove 2 instruments labeled "No. 1 Plant Primary Pump Discharge Pressure" and "High Pressure Pump Suction" from instrument panel B shown on SK-80523. Both of these instruments service the same pressure measurement. The former is a recorder and the latter is an indicating on off control actuating an alarm in the event of low pressure.
Combine the functions of both these instruments into one case and relocate the combined instrument to panel board C shown on SK-80523.
See Job II SK-930-5^5E-902 for new location on panel board C'.
(2) Remove two existing ventilating fans in east wall of console area and seal off wall to conform with existing architecture. Costs to remove fans and seal off wall opening is to be charged to 829-3^-' Ventilating fans are to be retired.
(3) Install new prefabricated insulating type walls shown as "new wall" on SK-80523.
(a) Provide 3 access doors in new wall as shown.
(b) Provide window in new south wall to view No. 5 reactor pressure gauge.
(c) West new wall to be solid to wainscoat height and glassed above wainscoat.
(d) New south wall in front of panel board ' b' to block and seal off door C .
(k) Make ceiling height uniform in area confined by new wall. Ceiling height to conform with existing ceiling height immediately above reactor console. Ceiling to be accoustic type.
(5) Provide florescent lighting on new ceiling of the type now located above existing reactor console.
-5-
017463
(6) Relocate unit header, conduit, switches and equipment at the direction of unit operating personnel as required to install new walls.
(7) Air condition the area confined by the new wall to provide temperatures at recognized comfort levels both in winter and in summer.
(8) All relocation of existing equipment to be charged to 03711-9-26993-
(9) Cost of all new installations to be charged to 930-65^8.
(10) Air conditioner to take Buction of make up air from the north roof east end of Building 102.
(11) Electric, water and steam services are to be provided. Service requirement will be determined when the air conditioner is sized.
-6-
017464
Job IV
Rearrange No. 3 Reciprocating Primary Pump Piping Sketch None
The existing reciprocating primary pumps Items 6036E-201 thru 203 are connected to ethylene inlet piping and intensifier suction piping in such a manner that pumps labeled 1 and 2 serve as spare primary pumps for the No. 1 plant and pump No. 3 serves as an isolated spare for the No, 2 plant. In this arrangement, production is curtailed when either primary pump 4 or 5 is out of service for repair because the capacities of the replacement reciprocating pump so piped is inadequate.
The purpose of this rearrangement of reciprocating primary pump piping is to connect the pump in parallel so that they operate together as an effective spare for either pump 4 or 5-
This is a rearrangement of existing piping and all work to complete the job should be charged to 03711-9-26993-
1. Disconnect and blank the connection of No. 3 reciprocating primary pump to the No. 2 plant suction header 3" 6256-P-lOl. Reconnect No. 3 reciprocating primary pump suction to blanked off connection in No. 1 plant suction header 4" 6034-P-101.
2. Disconnect and blank the connection of No. 3 reciprocating primary pump to the No. 2 plant primary pump discharge header 3" 6256 P-102. Reconnect No. 3 reciprocating pump discharge to blanked off connection in the No. 1 plant primary pump discharge header 6036 3" P-225.
3. Rearrangement of primary pump suction line should conform to piping specification No. 155-
4. Rearrangement of primary pump discharge piping should conform to piping specification No. 158.
5. The existing extensions of the No. 3 reciprocating primary pump piping to the No. 2 plant piping are sufficiently long to be reusable as material to reconnect the pump to No. 1 plant header. Plans should be made to complete the necessary pipe revisions during the all plant shutdown, which will be required as part of Project 64-12.
- 6a -
017465
0 2N o r t h Pa n e l B o a r _d B ldg ( .
Line List (Line Numbers Refer to SK-8051T)
All Line Numbers are Preceded by 65^8
Line No. Size
W-901
4"
W-902
3"
W-903
3"
W-90k
k"
Spec. 1 1 1 1
From Exist 6" 6047W-907 W-901 Dovtherm Pumps W-903
W-905
W-906 W-907 W-908
2" 1
1 1/2" 1 1 1/2" 1 1 1/2" 1
Existing 60J4-7W-907 6"
W-905 Dovtherm Pumps
Dovtherm Cooler
To W-902 Dovtherm Pumps W-90k Existing 6041W-764 Exist 60U0W-601
Dovtherm Cooler Sump 60V7E-936 Sump 60L7E-936
Material Handled Remarks Water Water Water Water
Water
Water Water
-8 -
ENGINEERING DEPARTMENT UNION CARBIDE CHEMICALS
p(-lf fi
DESIGN REPORT ISOPROPANOL RECOVERY SYSTEM HIGH PRESSURE POLYETHYLENE UNIT
PLANT 510 930-6550
0
PORT LAVACA, TEXAS JANUARY 26, 1965
017472
UNION CARBIDE CHEMICALS COMPANY
DATE
SHOP ORDER TRANSMITTAL 1-26-65
SHEET
L of l
roject
930-6650 H.P.Poly
Isopropanol Recovery System
iocat on
Plant 510
_________________________ ^___________
I s T* I luriON
J. W. Warner ^
J. F. Tamborello
g tad ;yton
G. L. Funk
R. G. Ziefle J. J. WaLthalL J. H. Wietine D. L. Buchanan J. M. McBridg
major subject
ISSUED FOR
Design Report
TRANSM1TTAL NO .
TMNSMI TTU
ATTACHMENTS
J. C. Upchurch
DRAWING NUM8ER
SHOP ORDER ISSUE B.M. NO.
* DESCRIPTION
5K-80586
930-6550
Design Report Isopropanol Recovery System High Pressure Polyethylene Unit
Flow Diagram
EMARKS:
RM 51O- 30-97 A
017473
J. F. TamboreLLo
ISSUED BY
1.
%
DESIGN REPORT ISOPROPANOL RECOVERY SYSTEM HIGH PRESSURE POLYETHYLENE UNIT
SEADRIFT PLANT
930-6550
Written by:
D. L, Buchanan J. F. Tambor eLLo J. C. Upchurch J. L. Warner
Engineering Department Union Carbide Chemicals Division
Port Lavaca, Texas January 26, 1965
017474
Design Report
Isopropanol Recovery System High Pressure Polyethylene Unit
Seadrift Plant
930-6550
F orew ord This report specifies the design of a system for continuous recovery
of isopropanol from a mixture of isopropanol and oils. Standard distillation methods are used to recover isopropanol of a quality reuseable in the poly ethylene process.
This report contains: Equipment List Safety Valve Schedule Pressure Gage Schedule Equipment Specifications Instrument Specifications Equipment to be Insulated Piping to be insulated Line List Flow Diagram SK-80586
017475
Equipment List SK-80586
6550E-100 - EXISTING OIL POT
An existing vessel which serves to vent dissolved gases from an accumu late polyethylene oil and isopropanol from No. 2 oil column bases. Service of this vessel will not be changed by this work order, however, it is to be equipped with automatic liquid level controls.
Normal tank operating pressure Tank size - diameter
length Tank details shown on Dwg. Original Item Number Property Number
30 psig 48" 10'-6" 937 -A -6136 6256E -1005 6392-642
6550E -101 6550E-10I-1 6550E-101A 6550E-101B 6550E -101C 6550E-101D 6550E-101E 6550E-10IF
LIQUID LEVEL INDICATOR CONTROLLER TRANSMITTER CONTROLLED VALVE PRESSURE SWITCH PRESSURE SWITCH ALARM LIGHT (HI LEVEL) ALARM LIGHT (LO LEVEL)
To control the liquid level in Item 6550E-100 by controlling the amount of liquid released by differential pressure to tank 6550E-102. Existing alarm horn to sound and alarm lights 101E and 101F to light when either the tank level is high or low. Control instrument and alarm lights to be located in control room of No. 1 Gas Separation.
Instrument Flow Range
. 2 to 12 gpm
Normal Tank Level Low Level Alarm High Level Alarm
22" liquid - 17" H2O 7" H20
27" H20
Label Instrument See Instrument Specifications
"No. 2 Oil Clm. Oil Pot L. L.' SK-5I0-6550-101
017476
-2-
6550E-102
EXISTING TANK
To serve as a feed and surge tank for Isopropanol Recovery Column 655QE-IQ6. This tank is now in caustic service but is to be made available for this work order by 2-1-65. No alterations to this tank are required, but tank is to be cleaned and inspected before use in new service.
Nominal Capacity
10,000 gallons
Size - Diameter
96"
Length
34'-10"
Tank Details Shown on Dwg. General Welding - S/O 4450B
Original Item Number Property Number
GRA-104 6392-352
6550E-102B - ORIFICE FLANGES
To be installed in 3" vent line P-102 from tank 6550E-102 to flare header for possible future measurement of vent gas flow. No orifice plate is to be provided. Orifice flange to be specified by instrument engineer.
6550E-103 6550E-103-1 6550E -103-2 6550E-103A 6550E-103B 6550E-103C 6550E-103D
LIQUID LEVEL INDICATOR LIQUID LEVEL INDICATOR LIQUID LEVEL CONTROLLER TRANSMITTER CONTROLLED VALVE PRESSURE SWITCH ALARM LIGHT
To indicate and control the liquid level in isopropanol feed and surge tank 6550E-102 by controlling the amount pumped to the isopropanol recovery column 6550E-106.
Items 6550E-I03 and I03D are to be located on the control panel of the No. I Gas Separation Unit.
Item 6550E-I03-I to be located on the north instrument panel near the Polyethylene "A" reactor console.
Instrument and alarm light to be labeled:
"Iso Feed Tank L. L. "
Control Valve Flow Range Normal Tank Liquid Level High Level Alarm
See Instrument Specifications
-3-
017477
4 to 10 gpm 48" Liquid - 37" H20 78" Liquid - 60" H2O
SK-510-6550-10 3
6550E-I04 6550E -104A
FEED PUMP MOTOR
To pump P. E. oils - isopropanol mixture from tank 6550E-102 to isopropanoL recovery column 6550E-106.
Pump to be started and stopped from its field location.
See specifications page 15.
Item
Property No.
6550E-104 (Pump) 6550E-104A (Motor)
6306-1465 6213-19 67
6550E-I04C - ORIFICE FLANGES 6550E -104D - RESTRICTION ORIFICE
To provide for a continuous recycled flow from pump 6550E-104 to feed tank 6550E-102. Recycle flow to prevent pump overheating and provide flows more suitable to pump characteristics.
Flow Orifice Differential Location
12 gpm 28 psi P-107
6550E-I05
- FILTER
To remove non abrasive particles from feed to distillation column 6550E-106. Use surplus filter (Property Number 6311-128).
Make Type
Flow (Maximum) See Specifications
Cuno Auto Klean No-AK-234
Type EGLF-4-8 10 gpm Surplus Item Record F7-58
017478
-4-
6550E-106 6550E -106A
DISTILLATION COLUMN TRAYS
r
i
To separate isopropanol from a mixture of isopropanol and polyethylene oils. Except for materials of construction column design and auxiliary equip ment to be suitable for future recovery of acetaldehyde. Substitution of materials or coatings are to be used in the event acetaldehyde is to be recovered.
Performance Information
F eed
Feed Rate Feed Temperature Base Temperature Head Temperature Head Pressure Normal
Design Column Differential Make Quality
Reflux Ratio Tails Composition Recovery Efficiency
96% Isopropanol 4% P. E. Oils Some Water and light Hydrocarbons
4 to 8 gpm 35C Normal 120C Normal 100C Normal 15 psig 50 psig 45" Minimum, 50" Maximum Isopropanol and <. 5% H2O and v. 3% Oils 1:1 50% Isopropanol - 50% Oils 90% Minimum
Construction Information
Size No. Trays and Spacing Type Trays Tray Capacity Feed Point Make
Head Cut Kettle Capacity Design Wind Load Materials of Construction
30" ID 531 -6" High 30 - 12" Valve See BM-15893 9th Tray Normal, 5th Tray Alternate 25th Tray Normal, 21st Tray
Alternate Thief Top Tray 370 gallons 30 Lbs /in. ^
Steel
See Specifications SK-654169-81-4
Property Number
6471-1012.
-5- 017479
6550E-106B
CALANDRIA
One external calandria for column 6550E-I06.
Head Load Heat Exchange Area
L, 680,000 BTUs/Hr 165 Sq Ft.
Material
Operating Pressure Design Pressure Flow Operating Temperature
Shell 75# Steam
Approx 70#/in. 2 " 150#/in.2
1850#/Hr.
T ubes 50% Isopropanol 50% Oils 17#/in.2 75#/in. 2
120C
See Specification SK-564169-81-2
Property Number
6376-1824
6550E-L06B-2 - STEAM TRAP
Make Model Type Connections, Size, in.
Type Operating Pressure, Max. psig Design Pressure Condensate, Lb/hr Differential Pressure, Psi, Min. Orifice Size
-Strong
Inverted Bucket
-4 i/a*--
/ If
Screwed
75 psig
150 psig
Min. 3, 700
25
o ir
The condensate load specified is the continuous discharge capacity of the trap.
6550E-106B-3 - STRAINER
Size Pressure Rat ing, Psig Min. Body Material
Screen Material
1-1/2" 150 Cast Iron
STD
Case iron strainers will have threaded end connections. Screen perfora tions wiLL be 1/32 in. , approximately. Screen material specified as "Standard" will be either brass, monel, or stainless steel.
017480
-6-
6550E -L06C
INTERNAL CONDENSER
/
U Bend, internal total condenser to be located in top head of column 6550E-106.
Heat load Heat exchange area
2, 165, 000 BTU/hr. 240 sq. ft.
Material Temperature in (Approx.) Temperature Out Design Pressure Flow (Max.) Sub Cooling To: C
Tube Side
Outside of Tubes
Cooling Water Isopropanol
30"C
100C Vapor
45C
Approx. 50C Liquid
50 psi
160 gpm (Approx) 6, 000#/hr
50C
See Detailed Specifications SK-564169-81-3
Property No.
6376-1825
6550E-107 6550E -107 -1 6550E-107A 6550E -107B 6550E-107C
PRESSURE INDICATOR PRESSURE CONTROLLER PRESSURE TRANSMITTER CONTROLLED VALVE CONTROLLED VALVE
One instrument system to control the pressure in Distillation Column 6550E-106 by venting column to atmosphere or by making up hydrogen methane gas.
Indicating controller to be mounted on north instrument panel near polyethylene "A" reactor console.
Control Instruments to be labeled:
"Iso Clm Pressure"
See Instrument Specifications SK-5I0-6550-107
6550E-108
- PRODUCT COOLER
017481
To sub cool refined isopropanol from.the 25th or 2lst tray of recovery column 6550E-106 by heat exchange with plant cooling water.
Performance Information Material Quantity, Max. Temperature inlet
Outlet Operating Pressure Design Pressure Design Pressure Drop Heat Transferred Materials of Construction
See Specification SK 564169-81-1
Tubes
Shell
Water
Isopropanol
24 gpm
4, 100#/hr
30 C
lOO^C
45C
50C
30 psig
15 psig
75 psig
75 psig
4.6 psi
0.24 psi
292,000 BTUs/hr 292, OOOBTUs/hr
Steel
Steel
Property Number
6376-1826
6550E-109 6550E-I09-I 6550E-L09A 6550E-109A-I 6550E-109B 6550E-109C 6550E -109D
- FLOW AND DIFFERENTIAL RECORDER (Two Pen) - FLOW CONTROLLER - TRANSMITTER (Product Make) - TRANSMITTER (Column Differential) - PRESSURE SELECTOR - ORIFICE FLANGES - ORIFICE PLATE
To record the column differential and flow of make from isopropanol recovery column 6550E-106. Controller shall override the column feed valve 6550E-103B when make rates become excessive (at 8 gpm).
The two pen recorder controller shall be located on north instrument panel near the Polyethylene "A" reactor console.
Controller to be labeled: "Iso Colm Diff. and Make".
Make Flow Range Feed Flow Override Setting Clm Differential
Units for Flow Conversion Graph
4 to 10 gpm 8 gpm 45" H2O Min. 50" H2O Max. GPH
See Instrument Specifications SK-5I0-6550-I09
6550E-U0
- FLOW RECORDER (Two Pen)
6550E-U0-1 - FLOW CONTROLLER
655OE-U0A
- RATIO CONTROLLER
6550E-U0B - TRANSMITTER (Feed Flow)
6550E-110C
- TRANSMITTER (Steam Flow)
6550E-H0D, llOD-l - ORIFICE FLANGES
6550E-U0E, 110E-1 - ORIFICE PLATES
6550E-U0F - CONTROLLED VALVE
To record the flow of feed to column 6550E-I06 and steam to calandria 655QE-106B. Controller to control the flow of steam in selected ratio to the flow of feed to the column.
Feed Flow Range Steam Flow
Units for Conversion Graphs Steam Flow Feed Flow
4. 0 to 10. 0 gpm 1850#/hr at 8.0 gpm feed flow
#/hr GPH
See Instrument Specification SK-510-6550-U0 -8-
0 7 7482
6550E -111 6550E-U1-1 6550E-U1A 6550E-U1B 6550E-IUC 6550E-ULD 6550E-IIIE 6550E-U1F 6550E-111G
TEMPERATURE RECORDER (Two Pen) TEMPERATURE CONTROLLER TRANSMITTER (Head Temperature) TRANSMITTER (Base Temperature) THERMO WELL THERMO WELL CONTROLLED VALVE CONTROLLED VALVE SELECTOR SWITCH
To record the temperature in the head of isopropanol recovery column 6550E-106.
To record and control the temperature in the base of the isopropanol recovery column by controlling the flow of isopropanol make from the column to either of the make tanks 6550E-114 or 115. Control instrument and switch to direct flow to either of the make tanks to be located on the north instrument panel near the polyethylene nA" reactor console.
Make Instrument flow Range Normal Head Temperature Normal Base Temperature
0 to 10 gpm 100C 120#C
See Instrument Specifications SK-510-6550-111
6550E-112 6550E-U2-1 6550E-II2A
- LIQUID LEVEL RECORDER - LIQUID LEVEL CONTROLLER - TRANSMITTER
To control the liquid level in the base of the isopropanol recovery column by controlling the amount pumped from the column base by variable capacity pump 6550E-U3.
See Instrument Specifications SK-510-6550-H2.
-9- 017483
6550E-U3 6550E-113A
COLUMN BASE PUMP MOTOR
Positive displacement, reciprocating plunger pump with automatic remote speed or adjustable stroke to pump base liquid from isopropanol recovery column to Polyethylene Unit tank 6034E-125 or to the "Dirty Oil" tank at No. I Gas Separation
See Pump Specifications, page 23.
Item
Pump 6550E-U3 Motor 6550E-U3A
PropertyNumber
6306-1466 6213-1968
fr550E-U4 6550E-II5
- ISOPROPANOL MAKE AND STORAGE TANK
Type Nominal Capacity Operating Pressure Design Pressure
Horizontal Dished Head 10, 000 gallons 5 psig 50 psig
See Specifications Page 25.
Item Number
6550E-U4 6550E-U5
Property Number
6392-1126 6392-1127
6550E-U6, 117 6550E-1I6A, 117A 6550E-116B, U7B 6550E-U6C, U7C -
LIQUID LEVEL INDICATORS TRANSMITTERS PRESSURE SWITCH ALARM LIGHTS
To indicate the level in tank 6550E-114 and 115, respectively, sound existing alarm horn and high alarm lights in the event of hi-level.
See Instrument Specifications SK-510-6550-U6, 117
017484
-10-
655QE-U8 6550E -I18A
TRANSFER PUMP MOTOR
/'
To transfer refined isopropanol from tanks 6550E-U4 and 115 to an existing isopropanol feed tank.
Pump Capacity
100 gpm
See Specifications, page 26.
Item Number
Pump 6550E-118 Motor 6550E-U8A
Property Number
6306-1467 6213-1969
6550E-119 6550E-II9-1 6550E-119A 6550E-U9B 6550E-U9C
PRESSURE INDICATOR PRESSURE CONTROLLER TRANSMITTER CONTROLLED VALVE CONTROLLED VALVE
One instrument system to control the pressure in storage tanks 6550E-LI4 and 115 by venting tank pressure to atmosphere or by making up hydrogen methane gas.
Indicating Controller to be mounted on north instrument control panel near Polyethylene "A" reactor console.
Control instrument to be labeled "Iso Make Tank Pressure".
See Instrument Specifications SK-510-6550-II9
6550E-I20 - ROTOMETER
To measure the flow of water laden isopropanol drawn from the head of the isopropanol column 6550E-I06. To be field mounted.'
Flow Range
25 to 75 #/hr
See instrument Specifications SK-510-6550-120
017485
6550E-L21 6550E -121-1 6550E-12I-2
THERMO WELL (CooLing Water Supply) THERMO WELL (Cooling Water Return from 6550E-L08) THERMO WELL (Cooling Water Return from 6550E-106C)
For use with test thermometers.
122 - ORIFICE FLANGE For possible future measurement of cooling water flow to 6550E-106C. See Instrument Specifications SK-510-6550-I20.
-12-
017486
V-nJ
0 i
\X
IT,
N
3
i^
55 >
to O'
c\
^
to.
s.
5;
to
^
\ \j
>1 J
\
>0
w
^\>
<*/> Hfc
}
>>
*
?
s
s -l
%
I
$1
\ ^J
<s\ 03
1/ KJ
n;.
<r (n
017487
Safety Valve Schedule Flow Diagram 5K-80586
Item No.
Location
Size Type (1)
Set Connections
Pressure, psig , Inlet
Outlet
6550E-I02A
'6550E-102
6Q8 Crosby JO-25
60
150#RF
150#RF
6550E-106D 6550E-I06 6550E-L0bE ^ 6550E -106
3K4 (Crosby JO-25
55
3K4 ^Crosby JO-25^_^ 45
150#RF y^14C^RF
6550E -I06B-4 -- 6550E-I06B 1" (^Lunkenheimer I045^y82
6550E-108B
PP--1I1I44 P-113 6550E-II4
ID2 ( Crosby JO-25
y75 -
ID 2 4P6
Crosby JO-25 ^\ ifxU . A0r, Ec
Crosby JO-25
125 50
NPT I" i '/t_ S! t FH56RF
1" 150#RF
4" 150#RF
L50#RF c.
150#RF
NPT 1-1/4
2" 150#RF
2" 150#RF
6" 150#RF
6550E -115A
6550E-U5 4P6 Crosby JO-25
50
4" 150#RF
6" I50#RF
/ ''
1-/
(1) Suitable for operations at temperatures and pressures indicated by series number.
(2) For steam service - provide valve with lifting device.
-13-
017488
Pressure Gauge Schedule Flow Diagram 5K-80586
Item No. 6550E -102C 6550E -I04B 6550E-106F 6550E-106B-1 6550E-U3B 6550E -114B 6550E-115B 6550E-U8B
Location 6550E-102 P-105 6550E-106 MS-103 P-UO 6550E-114 6550E-1I5 P-120
Model US Gauge* 1525 1525 1525 1525 1525 1525 1525 1525
Material
Range
Tube
0-30
SS
0-60
ss
0-60
SS
0-100 ss
0-160 ss
0-60
ss
0-60
ss
0-60
ss
Coil Syphon Not Required Not Required Not Required Required Not Required Not Required Not Required Not Required
*Or equivalent.
L I i
c.
1)^-"T ^
1 . ,,
'
C-:' -
-
NV'
hi is (rf*
-- "d;
~7
-14-
017489
Page 1 of 2 Item No. E -104 & E-104A
SPECIFICATIONS FOR PUMP AND MOTOR ITEMS 930-6550E-10.4 and E-L04A
SCOPE
One centrifugal, electric driven pump is required for continuous outdoor hazardous area operation.
PERFORMANCE
V olume Total head Pressure, suction
discharge Speed
20 gpm 100' 5 psig normal 33 psig normal By manufacturer to suit NPSH conditions.
PUMPED FLUID
Material
Specific gravity V iscosity: T emperature:
Suspended solids: NPSH available
DRIVER
Mixture: 96% isopropanol, balance light hydrocarbon oil
0.77 (Ref. 20C water) Approximately 3 cp 958F Normal 120 F Maximum Not present In excess of 10 ft.
Eleccric motor to be HP, RPM, 3 phase, 60 cycle 440 volt, fully impregnated, void free, epoxy encapsulated with drip-proof chemical plant enclosure, with cast iron terminal box and Parkerized hex head cap screws. Suitable for Class I, Division IT locations. Ventilating fan shall be of spark-proof and corrosion-proof material. Air inlet opening shall have corrosion-proof screen covers, openings shall be small enough to prevent entry of 1/2" round rod. Internal metal surfaces of frame and enclosure are to be of non-corroding material or properly prepared and coated with epoxy base or approved equal paint. Nameplate shall be of corrosion-proof metal and bearings shall be double shielded.
HP/Speed
By manufacturer but size for maximum 20 gpm flow.
-15-
017490
Sheet 2 of 2 ITem No. E-104 & 104A
MECHANICAL DETAILS
Centrifugal., in-line mount, or horizontal, end suction. Closed impeller, solid shaft, oil lube, ball bearing, fitted with shaft seal.
Cast iron casing, cast iron impeller, steel shaft. Flanged connections 150# ASA, RF.
Shaft seal to be single, inside, unbalanced. Pump manufacturer shall quote Durametallic type ROTT in 316 SS as extra if not an O. E. M. standard. Preferred materials are Kalamate, #5 carbon and glass filled teflon.
-16-
017491
auRPtas ccwtroi. aid disposal department
Union Carbide Chaaloala Company D1vieIon of
Union Carbide Corporation South Charloaton, boat Virginia
Oil Filter
Proparty No. 6311-128
Data of Mating 3/31/61*-
Claaalf&oatlont Surplua for Dlapoaal InetalledQ Not InetalledQT) Surplua - Bold ' InatalladQ Not Inatalladl i
Looatlon 510
Building 160 EE lU-3
Surplua It-- So, F7-58 Type of Property:
Oil Filter
Capacity (3# drop) 120 gps at 100 SSU 100 gpo at 300 SSU 61.2 gpo at 700 SSU 35.2 gpo at 2300 SSU
Equiv. Mesh 70 Free Area 63.2 Sq. In.
If Surplua for Dlapoaal, thla Proparty Item la available for tranafar within tha Chaaloala Coapany upon an "as la - wharo la" baala for a porlod of ona yaar fro* data of Hating.
DESCRIPTION
Oil Filters, Cuno, Auto-Kleen, NO-AK-23^, Type EDLF-1*--8, Manually Operated, Stainless Steel, Length 8", Spacing .008, Specify #12272-6.
Unit consists of four sumps and cartridges with a cannon-head.
Serial No. None.
First Class Condition.
CONDITION
Item No. 6257E-231C Former Service: Esstic Oil Service
Date of Purchase!
9/6l
Work Order:
017492
Estimated Repair Cost: --
930-6257
Original Cost: $452.
Transferred to Plant: Sold to: Sorapped:
DISPOSITION
Departmental Symbol: Value Received: Value Reeelved:
Upon disposition of this Item, Surplua Program Representative of Owning Plant will fill In above dlapoaltlon data and iauediately forward this sheet to R, S. Wright, Surplua Control and Disposal Department, South Charleaton, Waat Virginia.
f h9" * vrerip
1
I
aeaeeae <t>f.s
WORES..ENGINEERING DEPARTMENT
UNION CARBIDE CORPORATION CHEMICALS DIVISION Texas City. Texas
BILL OF MATERIAL
______________________________________ _______________ BM________ 15893ISSUE
1
G. NO. DATE \.TE ISSUED
(r if CHARGE
11/17/64PAGE 1 OF
93000-00-06550-600
AW
564169
j ISOPROPANOL RECOVERY SYSTEM - Seadrift, Texas
l DETAIL Valve Trays
Valve Trays in accordance with the following specifications: ITEM NO. 6550E-106
K 49315
Tray Specifications
Tray type: Number required: Tray diameter: Tray spacing: Materials of construction: Tray thickness: Maximum point load without
permanent deflection: Method of support and
peripheral seal:
Valve 30 To be specified by vendor To be specified by vendor Steel To be specified by vendor
250-lbs.
To be specified by vendor
Process Requirements
Trays to be designed for efficient performance over the range of the following conditions:
Top Maximum Minimum
Base Maximum Minimum
Vapor rate, #/hr. : Liquid rate, #/hr.: Vapor density, #/ft. Liquid density,#/ft. 5; Liquid viscosity, cp: Surface tension, Dynes/cm:
5480 2740
2740 1370 0. 244 44. 9 0. 35 15
7370 7750
3680 3870 0. 304 41.4 0. 28 15
- 19-
017494
120" tube le n g th
/ 8" 1 smell- ---------_______ i 0 STEEL
/
or welded
2 fuses- 64 .1
.Ik 6WC. SEAMLESS IfXKBXKXSX.
3 OUTLET CH^NEl-ZXUinUSI STEEL
4 StfURL LHifJNEL-STEEL
3 tcp tuce sheet-------------------.'muxximxxnss steel
6 BOTTOM TUSE SHEET''XMHBmUBSSiKS STEEL 7 outlet channel flange- steel
0 return channel flange-steel 9 SUPPORTS-STEEL
10 SHELL EXPANSION JOINT is NOT REQUIREO
Notes
64 - 1 1-1/4*"
'
CS ON ._AR PITCH
"R OUTER V TUBE LIMIT
A
1. Impingement plate required on the tube bundle opposite the 4" steam nozzle. Remove 2 or 3 tubes if necessary.
2. Heads with sharp re-entrance angles are not acceptable. Minor angles will be allowed according to customer's judgment.
3. Design, material, fabrication, and testing according to the ASME Code and TEMA Class C unless noted.
i
i
SCHEMATIC SECTION thru SHELL
I ....It T.MI Nit OUKTI
*
v- -- e
``LINN
CI.VCNSlONS ARE APPi-G X;MATE. .*'ANU.L ALTuhC' IS hiEPL.'w.E..E FC-I MCCH.`.-',.CAL ocsign.
FILLEO with WATERLOS-
ESTlMATEO WEIGHT,
FLANGED CONNECTION ORILLING-'W LS.ASA, SHELL SIDE; ISOLD ASA TuOE SICE.
TUGE SiOE SHELL SIOE
DECiCN
PRESSURE
7 5 PSI 1 50 PSI
3 50 -f 350 *f
-20 -
TEST PRESSURE
MYC.H0
PSI PSI
017495
,te., 6550E-106B
1
iw;;;/ *. r* .. CAnC.-'i a Catv,: . ', v*
: CCn?
Texas City, Texas
CALA.NCRIA
165 -a ft.
1
.... KCi.fif. 7 1
MECHANICAL SPECIFICATIONS
1 SHF LL - NONE REQUIRED.
or welded
tuseb 150 - U . V**_*0.01.1 ^ two. seamless inSMUB STEEL
4 TUBE SHEET- rfSUKS&ttSBMMAAkSTEEL, full face
CHANNEL FLANOC-STEEL
IHCUL FLAN9C- NON r UfaumED,
2 tube supports and 2 baffles 7 SAFFLEl/---------------------- * MMSi MFJBlESMSniWtilKVAmBdS STEEL
s spacers -- *oo. snanma steel t tieroos-------- *-------------- * o o aasmamis iTS steel
10 LONGITUDINAL OAFfLE- NONC. ItSTEEL SUFFOATS- NONE NEQUINEO.
It CHANNEL PARTITION- ,_
__*THICE MMMtMniBS STEEL
Notes
1. 6-pass tube bundle and channel.
2. Tube bundle to fit inside 24" schedule 20 pipe as vertical knock-down condenser.
i i
i
3. Choose tube pitch so that bundle fills the space provided.
4. Customer will furnish exact location of tube supports and baffles.
5 Connecting flange to 24" column will be TEMA
75 lb. class.
N0TS
017496
THIS EXCHANGER IS TO BE INSTALLED VERTICALLY IffiSSONSABC DIMENSIONS ARE APPROXIMATE. MANUFACTURER IS RESPONSIBLE TOR MECHANICAL OCSIGN. S&JCIWK SiJXlKS
sasLkoaKacxMKKxaExxxaxBiaRcimtxNinc KiiouuccsxsaxxjscAuusai steel. BUSMEBSEOBfiSBO, ESTlMATEO WEIGHT, FILLE0 WITH WATERLBS
I i i i
i
PIAN0C0 CONNECTION DftIUI NQ' MOBMtpMlUaDt; 73 10-ASATUBC SIDE
6. Design, material, fabrication and testing according to ASME Code and TEMA, Class C unless noted.
tube tiot
DESIGN 0C SIGN TEST PRESSURES
PRESSURE TEMP
HYDRO.
50 PSI 300 *f
PM
-21
item no 6550E- 106C {MmttPmG otPAATMtof
I j
1
CARBI0C B CARBON CHEMICALS C0RP J
jTEXAS CITY. TEXAS
HEAT EXCHANGER-MULTI-PASS- I
RETURN SEN0 2 4 0
SO FT. I
11- 27- II
jam
SK_ sfidi co-P1-T
92 - 5/[8`tubes on 13/16 'T.AIANGULAA AITCH
-f -
SCHEMATIC SECTION THAO SHELL
(MU
mmmmtm mmiivi
Notes
1. Single pass shell, 4-pass tube side. 2. Bend longest tube from 10 ft. length.
Make shell length to suit. 3. Baffle cut 20% of diameter. 4. Design, material, fabrication, and testing
according to ASME Code and TEMA Class C unless noted.
NOTfeS
tms exchanges is to ac installed nasnv hoaizontally. dimensions aae AAAAOXIMATE. MANUAACTUAEA IS AESAONSIBLE rrw MECHANICAL OESNSN. IHJUISHA nBzanmiuocnsiiKKuaHEisxBNCMnEaniisis steel, amsuiniv estimated weight, eilleo with watealbs.
alanoeo connection DNCLINBUSOLB. ASA, SHELL side; ISO lb. ASA TUBE Side
OESION 0E SION TEST AAESSUACS AAESSUAE TEMA HTQAO SSH
TUBE SICE 75 ABI 30 Of
AS! ]
StCLLtlOC 75 ASI 3 00*A
ASI I
-22-
017497
itemn 6550E-108
(MtiaciAiN* oiMATHtar CAABIDC B CAABON CHEMICALS CONA
Texas City, Texas
HEAT EXCHANCEA-MULTI'AASS*
aetoan bcno
75*o at
I* U
Sheet L of 2 Item No. E-U3 & E-IL3A
SPECIFICATIONS FOR PUMP AND MOTOR ITEMS 930--6550E-113 and E-II3A
SCOPE
One, variable capacity, electric driven pump is required for continuous outdoor hazardous area operation.
PERFORMANCE
Volume, GPH
25 to 75 normal 100 Maximum 0 Minimum
Pressure, psig Discharge
35 normal 125 maximum
Suction
18 normal 50 maximum
FLUID PUMPED
Temperature:
230F Normal 250F Maximum
C las sification:
Light hydrocarbon oil and isopropanol in 50-50% mixture, non-corrosive; no suspended solids.
Specific Gravity:
0. 77 @ temperature
Viscosity:
Approximately 8 cp @ temperature
N. P. S. H. Available:
10 Ft. , Minimum
-23-
017498
Sheet 2 of 2 Item No. E-IL3 & E-U3A
DRIVER
Electric motor to be HP, __________________RPM, 3 phase, 60 cycle 440 volt, fully impregnated, void free, epoxy encapsulated with drip-proof chemical plant enclosure, with cast iron terminal box and Parkerized hex head cap screws. Suitable for Class I, Division II locations. Ventilating fan shall be of spark-proof and corrosion-proof material. Air inlet opening shall have corrosion-proof screen covers, openings shall be small enough to prevent entry of 1/2" round rod. Internal material surfaces of frame and enclosure are to be of non-corroding material or properly prepared and coated with epoxy base or approved equal paint. Nameplate shall be of corrosion-proof metal and bearings shall be double shielded.
VARIABLE CAPACITY DEVICE
To be offered by pump manufacturer in constant speed input, variable stroke or constant stroke, variable input (sheave) speed. Include pneumatic control for continuous remote operation of capacity variation.
MATERIALS OF CONSTRUCTION
Manufacturer's recommendation
GUARANTEE:
Manufacturer's standard on time limit
TECHNICAL DETAILS
Five copies of the selected manufacturer's certified installation drawings, parts lists and operating instructions are to be a part of these speci fications and forwarded to Union Carbide Corporation, Chemicals Division, P. O. Box 186, Port Lavaca, Texas 77979; Attn: J. L. Warner. Questions on and information relating to these specifications may be similarity directed.
-24-
017499
SPECIFICATIONS FOR STORAGE TANK 6550E-L14, 115
to be added later
-25 -
017500
Sheet 1 of I Item 6550E-118 & LI8A
SPECIFICATIONS FOR PUMP AND MOTOR ITEMS 930-6550E-118 and 1I8A
SCOPE
One electric driven, centrifugal pump for transfer (intermittent) service in outdoor hazardous area operation.
PERFORMANCE
V olume Total Head Suction Pressure Discharge Pressure
100 gpm 100 ft. 7 psig 40 psig
PUMPED FLUID
Material Specific Gravity Viscosity Temperature NPSH Available
Refined Isopropanol 0.75 (Ref. to 20C water) 2. 4 cp 130 F in excess of 20'
DRIVER
Electric motor to be HP, _______________ RPM, 3 phase, 60 cycle 440 volt, fully impregnated, void free, epoxy encapsulated with drip-proof chemical plant enclosure, with cast iron terminal box and Parkerized hex head cap screws. Suitable for Class I, Division II locations. Ventilating fan shall be of spark-proof and corrosion-proof material. Air inlet opening shall have corrosion-proof screen covers, openings shall be small enough to prevent entry of 1/2" round rod. Internal metal surfaces of frame and enclosure are to be of non-corroding material or properly prepared and coated with epoxy base or approved equal paint. Nameplate shall be of corrosion-proof material and bearings shall be double shielded.
MECHANICAL DETAILS
017501
Centrifugal, in-line mount, or horizontal, end suction. Closed impeller, solid shaft, oil lube, ball bearing, fitted with shaft seal.
Cast iron casing, cast iron impeller, steel shaft. Flanged connections, 150# ASA, RF.
Shaft seal to be single, inside, unbalanced. Pump manufacturer shall quote Durametallic type ROTT in 316 SS as extra if not an O. E. M. standard. Preferred materials are Kalamate, #5 carbon and glass filled teflon.
-2 6-
UNION CARBIDE CHEMICALS COMPANY
PROJECT 930-0550 - H. P. Poly Isopropanol Recovery System
location
SHOP ORDER TRANSMITTAL
major subject Instrumentation Specifications
ISSUED for
DATE
Sheet
2-26-65
1 Of 1
transmi ttal no.
distribution
J. Warner
T V. JEaw'fatSrellO
T. Rogstad
D. F. Pevton
O- T- Funk
R. C. Ziefle
J- J. Walthall
T- R- Wieting D- T.. -RiifihRnan
T. M.
n t.. wipv:
J. C. Upchurch
OR AWING NUMBER
SHOP
ORDER
ISSUE B.M. NO.
TRANSM!TTAL
ATTACHMENTS
DESCRIPTION
SK-510 .6550-101 SK-510 -6550-103 SK-510 -6550-107 SK-510- 6550-109 SK-510- 6550-110 SK-510- -6 5 50-in SK-510- 6550-112 SK-510- 655O-II6 SK-510. 6550-119 SK-510- 6 5 50-120
-A
'str
017502
REMARKS:
Please insert these pages in your Design Report. Instrument Specification 3K-510-6550-117 referred to on Page 27 of design report was combined with SK-5IO-655O-II0 therefore -117 will not be issued. This completes all instrument specs. _________ D. L. Buchanan
ISSUED BV
FORM 510-30-97A
017503
017505
I
017506
017507
017508
%
017509
ICS.Dr- St 3,, 534 H7D
iTTM I ITKH
I'Hn
I iTia
1
jircN
I
116 I
116A
tool 00
COM *0
LI '
II
I | 117A COM NO
LT
|VI llfiB KI U7B - (
1 too* NO
,, (com m
! Press. Sv. 1 Press. Sv.
116C Lt.
Ivi. iv . LDuELo
1
i.i s*
2
E-sC ' 2
hnU I 2 .d - ldS
i.2 - ia#
2
i c,ion t?____ 3 .
f3 -
IS
3
1
o-ioo u : * -
i -
J * a. c.
i * a. c.
4
t
2____________ ________________J______________1 _ . .
1
la_________! .1
f*t
Yea__________ .>
9
1
See Electrical .
~
i uS ss
! ' lit ss r^-:
P-:
-
* 3J-? 5
: 316 55 ! -
1 -
-
N1 Sean
lie SS
VLb SS j -
-
-
o Panel 1l5
, = Field 125
Field 125
: .
l' !"
ho . '
2 -* .* 2 2 i<2
J___ __
3
-'3
'<
u)
1 >3
. * 4 .4 It >4 | 14
*T
Ml*
Mt|
ra
rft
M* ft
Foxboro
Foxboro
Foxboro
Barksdale Barksdale
-|"'"llTC lll"*U6l> |l|r,*117D
| TEN
rm
1`TIM
i'ikTM Lt" ^ - PI
" PI
COOl *0
COM m
C404 44
See PI
J-
4m ft m
r*1
>0 -
2
>4
11) (2)
P-10A-CY
P-10.-CY '
5t
t 1.15#
:?
2
2
3- 3 - 3
3
3
* 0-100 u
0-100 0
4
4
4
41
1
4
ft
ft
- * -
ft
ft
7_ ? t 7
"" "T " ' BS
fc
fftt
ft t
>0 Field
0 Field
<9
10
10
'' 1 .1
2 *2 '2 <2 *2
3 3 >3 <3 <3
4 4 14
4
4
* ItM n*a era
l\ 5. Gauge U. S. Gauge
From 510 plant spares. Slope leads from transaitter to tap at least 3/U" per foot
MTV M
rs-
ItM tact m
sE^jfggf
SI
*t4T\n.
iit n. Contacts
Fefep ftMf
I MIC jll.Special
I55T |,r *"
UNIT
*
LOCATION . _i_
MQ -^550
FLOW BIAONAM 31 . 50566 [VISIONS
----------
-- - 1SOPROPAMOL MAKE ANT. STOSAr.F TAHKS LEVEL TmTCATTOK Aim 1TABM.
--------------
R- W>u*
niimllir-4 'jJ~
s.51g-ti5-U-
017510
017511
017512
Instrument Specifications SK-510-6550-101 SK-510-6550-10 3 SK-510-65 50-107 SK-510-6550-109 SK-510-6550-II0 SK-510-6550-IU SK-510 -6550 -112 SK-510-6550-U6(i#*f7 ' CH0' 1 SK-510 -6550 -119 SK-510-6550-120
added 13TE7T .t
-27-
77573
Equipment to be Insulated SK-80586
Item . 6550E-106 Column
6550E-106B Calandria 6550E -108" Cooler 6550E-U3 Pump
Normal Operating T emperature
Head - 1008C Base - 120 8C
Shell - l608C
Shell - 1008C
--*
lsO>
oo
Remarks
For personnel protection only For personnel protection only
-28-
017514
Piping to be Insulated SK-80586
Line No. P-109 Co-TD ~r' ' P-110 :> P-IL2 P-113 TP-U4^>i . _ _ ^ ji P-115 P-118
Normal Operating T emperature 130 C 130C 130C 130C
U0C 110C 120 C
MS-101 MS-102 MS-103 MS-104 SC-101 SC-102
175 C 175"C \1S9C 175C 150 C 150*C
Remarks For personnel protection only For personnel protection only For personnel protection only For personnel protection only For personnel protection only For personnel protection only Steam trace and insulate to prevent condensation .
-29-
017515
LINE LIST Line Numbers Refer to SK-80586 (All line numbers are proceeded by prefix 6550)
Line No. Size
Spec.
P-101 RS. 1-1/2
25A
P-102 Spas- 3"
25A
P-103
P-104
2"
25A
P-105 PS. 1-1/2"
25A
P-106 V'-"'- 1-1/2"
25A
P-107 iP'-'w l"
25A
P-108 Zp'--. 1-1/2"
25A
P-109
I"
25A
p-iio RF l". 1-1/2" 25A
p-iu 9.3 1-1/2"
25A
P-112 PS 1"
25A
P-113 F>n- I"
25A
P -114
1-1/2"
25A
P-115 ^pr. 1-1/2"
P-U6 ?r- 1-1/2"
25A 25A
P-117 SPr-'- 3/4"
25A
p.UgSpinA. 2"
25A
P-U9- 3" P-120 F9- 2"
25A 25A
From
To
6550E-100
6550E-L02
6550E-102
Flare Hdr
Not used
6550E-102 6550E-104
6550E-104 6550E-I06
P-105 P-105
6550E-102 6550E-102
P-105 6550E-106 6550E-U3 6550E-102 P-110 P-UO 6550E-I06 6550E-106 6550E-108 6550E-106
6550E-I06 6550E-U3 Dirty oil tank P-110 6034E-I25 P-109 6550E-108 P-U4
6550E-U4 k 115
P-109
6550E-106
Air
6550E-114, 115
6550E-U8
6550E-118
Is op Unloading Header
Material Handled
Is op - Oils
Hydrocarbon Gas
Isop - Oils
Isop - Oils E^ci
Isop - Oils
Isop - Oils
Isop - Oils Isop - Oils
Isop - Oils
Isop - Oils CS' Tak .
Isop - Oils *5;
f>.
Isop - Oils
Isopropanol
Isopropanol
. , pn-iw H'Z tv
Isopropanol
Isop - Water
Vent Gas
Isopropanol
Isopropanol (/'
-3 0-
017516
LINE LIST SK-80586 (Continued)
Line No. Size P-121 F^. 2"
P-122 I-1/2"
P-I24>oi_ 2" P-I25'P5 I" P-126 PS I"
Spec. 25A
25A 25A 53 53
From
To
P-120
Isop Feed Tank
Not Used
P-120
P-105
6550E-U4 & 115 Air
6268-P-I366
P-118
6268-P-I366
P-124
Material Handled
Isopropanol (S A***5
Isopropanol Vent Gas Methane ^ C*uw .
Methane
^4 v*w'
P'3^ 1 Lxoc71
p CC L ^ ---i1-' ',!?>' 0>-C!Llf --
ICIet (c-t - T* V Icb0
? L"wi r -- ):. JT MO;l cv pirv>.,; f>
< 1 G^f
-31 -
LINE LIST Line Numbers Refer to SK-50586 (All line numbers are preceded by prefix 6550)
Line No. Size Spec. From
MS -101 3" i|V-2
MS-103 4"
MS-102 MS-10 3 MS-104
!" 2 3", 2 ,^p'rpL I" P- 2
MS-101 MS-101 MS -101
To Isop System P-118 6550E-106B P-124
Material Handled
Remarks
75# Steam Use Seadrift Spec.------
75# Steam For Snuffing
75# Steam 75# Steam For Snuffing 1
>
SC-101 SC-102
2" pi
"2 2
6550E-106B Stm Cond Hdr Stm Condensate
MS-101
Stm Cond Hdr Stm Condensate
W-101 W -102 W -103 W -104 W -105 W -106
4" 1
6034W-118
4" JpwV. 1
6550E-106
1-1/2" l Sol-'--- W-101
1-1/2" 1
6550E-108
1/2" -
W-101
1/2" - PJ W -102
6550E-106 6034-119 6550E-108 W -102 Ground Ground
Water Water W ater Water Water Water
Use Cu Tubing ^ T?10 Use Cu Tubing ^
-32-
017518
rn
czd cm
PL_:
cm ocm
Q
cr; ct