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1/27
Art Montemayor Process Specification Sheets March 12, 2003
Rev. 0
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The accurate and complete preparation of Specification Sheets is one of the most (if not THE most)
important capabilities that a Chemical, Process, or Project Engineer should acquire very early in his/her
career.
does not have the time available to do all that must be done in order to resolve day-to-day problems.
That is why engineers are required to lead and supervise those around them in order to assure an
organized team-effort in resolving problems. To this end, engineers use communications skills (both
oral and written) as well as language, psychology, and interpersonal skills to inform and lead other
team members to a successful resolution.
At the very basic foundation of problem solving is the successful communications of the required
capital equipment required to resolve engineering problems. An engineer is unable to resolve a problem
if he/she is unable to successfully describe it in detail to the "stake holders" in a project. The ability toreceive constructive and cost-effective help and supply from parties involved in the project is directly
related to the timely and accurate description of the supply needed to resolve a problem.
Specification sheets are the indicated tools that are relied upon by engineers to convey an accurate
and detailed description of their needs and expected supply. These Specification sheets not only serve
to identify the required supply, they also serve to organize and structure the knowldege of the owner's
engineers as to the criticality and strategic importance of the supply. They force the Owner to comply
with the classic business rule: Emptor Caveat - buyer beware.
It is a basic business principle and law that the responsibility of defining the specific need for a supply
of goods or materials lies directly with the purchaser (or Owner). If you don't know what you need or don't
know how to describe what you need, you will never resolve your own problems. The Specification Sheetdescribes to others not only what you identify as your specific needs, it also documents them and
communicates this information to all interested parties.
A large part of the problem in preparing accurate Spec Sheets is that the lead engineers (who often are the
most experienced and knowledgeable) are not the ones that prepare the Spec Sheets. It falls upon the
Process and Project engineers to prepare them and many times these individuals have to be trained and
instructed on how to describe and specify equipment that they are only superficially familiar with. Therefore,
good Spec Sheets should be easy and simply to prepare, with a minimum of detail knowledge required.
Art's Centrifugal Blower
Art's Orifice Meter
Art's Coriolis Meter
Art's Ultrasonic Meter
Art's .
Art's Mass Meter
Art's Turbine Meter
Art's Vortex Meter
Art's Magnetic Meter
Specification Sheets Included in This WorkBook
An engineer is a problem solver, pure and simple. However, one cannot simply solve problems by
directly applying ones own efforts and time. In the industrial and competitive world, an engineer simply
Art's API 650 Storage Tank
Art's Centrifugal Pump
Art's Air-Cooled Exchanger
Art's Shell & Tube Exchanger
Art's Plate & Frame Heat Exchanger
Art's Process Vessel
Art's Control Valve
Page 1 of 27FileName: 166794456.xls.ms_office
WorkSheet: Introduction
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Art Montemayor Process Specification Sheets March 12, 2003
Rev. 0
I have arranged and organized the Spec Sheets found in this WorkBook in a manner that they should be
rather easy and intuitive for young engineers to prepare. A maximum use is made of drop-down list boxes
in order to facilitate the required information to engineers who are unaware of the various feature choices
available or much less how to describe them or spell them correctly. This method also "standardizes"
a variety of choices and does not leave it up to the individual to select whatever he/she thinks is required.
This method also allows the Spec Sheet to impose Corporate standards and pre-selected features without
wasting manpower to check their correct usage.
The utilization of an electronic spreadsheet such as Excel makes it easy for project documentation to be
safely stored, modified, and transmitted with a minimum of manpower. Engineers can generate and process
the documentation without further engineering assistance.
Additionally, the inherent calculation features of a spreadsheet are utilized to the maximum in allowing for
involved calculated information to be self-generated by the spreadsheet automatically. The spreadsheets
can be protected by the used/author for assurance that data will not be revised without prior knowledge.
The need to have calculations and related documentation readily available and filed due to legalities (such
as OSHA requirements on safety relief valve calculations and specifications) makes the spreadsheet a
natural tool for these requirements.
The utilization of Check boxes and Option buttons also give versatility and compactness to these Spec
Sheets, allowing the user to store more details and data in them. I have endeavored to limit the size of the
Spec Sheet to one page and design them around the need for communications of Process data for:
1. Documenting the results of calculations and other equipment details;
2. Preparing data and information for procurement inquiries (RFQs - Request of Quotes);
3. Obtaining Supplier information as related to a specific specification;
4. Preparing information that enters the Operations and Maintenance Manuals of a Unit;
5. Transmitting information regarding Unit equipment to other parties.
These Spec Sheets should be continuously revised and improved as spreadsheet technology improves or
is upgraded.
I will continue to work on and add additional Spec Sheets to this WorkBook in order to achieve as complete
a set of Spec Sheets as I can attain within the framework of available time.
Page 2 of 27FileName: 166794456.xls.ms_office
WorkSheet: Introduction
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Art Montemayor Spec Sheet Log March 12, 2003
Rev: 0Index of Process/Mechanical Data Sheet and Specification Forms
Equipment Type go-by draft* complete* debugged issuable** accepted
Control Valves Pressure Relief Valves
Orifice Plates
Centrifugal Pump Calculation Sheet PSV Selection Criteria
* in Excel spreadsheet format ** write-protected
InstrumentSpecifications
DataSheets,
Calculations(not
specs.)
Page 4 of 27
FileName: 166794456.xls.ms_office
WorkSheet: Spec Sheet Index 2
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Sheet 1 of 1
ng s n ts
1
2
3
4
5
6
7
8
9
10
11
12
13 Ft14
15 Ft16
17
18
19
2021
22
23
24
25
26
27
28
29
30 F
31
32
33
34 F
35 F
36
37
38
39
40
41
42
43
44
4546
47
48 %
49 lb lb
50
51
52
Rev Date Description By Chk. Rev Date Description By Chk.
STORAGE TANK SPECIFICATION
Stress Relieve ? Yes
Plot Plan No. :P&ID No.
psig
oz/in.2Set @
Shell Manway
Flush Cleanout MW
CONSTRUCTION/FABRICATION
SumpInternals (attach separate sheet, as req'd):
Design Wind Velocity
Design Specifications:
No
Paint Spec.Fireproofing ? Yes
F. F.
85Radiograph Inspection Req'd ? YesHot
API 650 LATEST EDITION
in.
1
OPERATING/DESIGN DATA
oz/in.2
NOZZLES/CONNECTIONS
0.7900Sp. Gr. : Size RatingQty
4"
8"
3/4"
3/4"
4"
2"
F. F.
F. F.
R. F.
API
48"x48"
1"
10"
150#
8"
30"
Shell & Bottom
Roof L. J.
R. F.
R. F.
F. F.
L. J.
API
L. J.
R. F.
K
Operating Design
P
M
H
Emergency Vacuum Design ?
METALLURGY
Remarks
Service :
Location :
Model :
Unit :
F
G
BarrelsFeet 11,191
Sloped
PID115-EPF-01-112A1
32.00
Bottom Floor Type:
Manufacturer :
1952.000
Fluid Stored : CRUDE OIL
0.50
Flash Point (Closed Cup) :
150#
Mark
A
0
Remarks
Project No.
Service
Cone
50.00
Nominal Volume :
For Inquiry ArtM
1. Items marked with an asterisk (*) to be completed by Vendor/Fabricator.
2. Fixed cone roof with internal floating roof.
Appr.
Mixer Manway
Vapor Pressure @ Max. Operating Temperature psia
Two
CA, in.
----Minimum Fluid Temperature
(Hydro)test Pressure expressed in Psig
0.0.3
Fill Nozzle
Sample Tap
Stilling Vent
Temperature Indicator
Outlet Nozzle
Positive Pressure
Yes
Material
200
-25
Component
150#
150#
Maximum Fluid Temperature
Roof Nozzle
N1
N2
Water Draw Nozzle
Top Center Vent
0.1250
0.1250
for:
57370 Normalized
Normalized
APILining/Coating 1Spare
D
Others:
mph100Thickness :
150#
150#
Face
Feet
5.5
Sample Tap
I
J
L
1
1
1
2
2
1
1
1
1
1
Design Engineer : Art Montemayor
T-400 & T-405Equipment No. :
No. Req'd :
Other Ref. Dwg No. :
CRUDE OIL Storage
Galveston, Texas Kirwin
1
1
Mfr Ref. No. :
24"
24"
6"
Roof Manway
E
This Tank Service is considered: Cyclic
Roof Type :
Shell Diameter : 50.00 Shell Height : 32.00
Approvals
125#
125#
125#
150#
150#
150#
150#
150#
Negative Pressure
150#
150#
API
API
16 Grade 5
0.00
1.00 2.00
Appr.
Tank Insulation ?
Insulation Type:
Code (as appl.):
EmptyTank Weight Full of Water
Seismic Zone 3
Montemayor,Inc.
Rev.
No.
48" X 48"FLUSH
CLEANOUT
F
A
MP G
K
D
E
L
E
H
N2N1 J I
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Sheet 1 of 1
Montemayor Corporation
1
2
3
4 Specification Engr:
5
6
7 %
8 psig (Norm.) psig (Max.) HP HP
9 Disch. Pressure psig (Norm.) psig (Max.) ft ft
10 Differential Pressure psi Diff. Head (TDH) ft gpm Cont. Thermal
11 Temperature, Normal F Max. F fps
12 @ PT @ Max. Temp. CW CCW
13 ft
14 cP cSt SSU Indoors X Outdoors ft ASL
15 F Max. F Min.
16 % psig @ F Max.
17 psig, Min. @ F Max.
18 Liquid is Flammable Toxic Other: v Ph Hz
19 Contains Chlorides H2S Other: II A
2021
22
23 in.
24
25 Case Mount'g CL Foot Brckt Vert. (Type)
26 Split Axial Radial Volute Single Radial Diffuser
27 Case MAWP * psig @ * F Hydrotest @ * psig
28 Connections Vent Drain Gauge Steam Jkt
29 Impeller Open Closed Special
30 Diameter: Rated * in. Max. * in. Min. * in. Case Impeller
31 Mount Betw. Brgs. Overhung Type Diameter in.; Clearance in.
32 Bearings Radial Thrust Int'stge Bush'gs, Diam. * in.; Cl'rnce in.
33 Lube Ring Oil Flood Oil Mist Flinger Pressure
34 Cplg. Mfr Model Approx. Wt., Pump & Base lb
35 Driver Half Mounted By Pump Mfr Driver Mfr Motor Wt. * lb Turbine Wt. lb
36 Seal Mech. Packing Auxiliary Mech. Packing Baseplate Dimensions (in.)
37 Seal Mfr. Type Model Baseplate No. ANSI API
38 Mfr Code API Code
39 Jacketed Box Other API 610
40 Gland Tap Quench Drain Flush Vent ANSI B73.1 B73.2
41 Customer Specs:
42 CW Plan Total CW Req'd No
43 CW Piping Mat'ls : for44 Packing Cooling Injection gpm @ psig Shop Inspection Req'd
45 API Seal Flush Plan SS CS Tubing Pipe Hydrostatic Test Req'd Witness46 SF Fluid : gpm @ psig Box psig Performance Test Req'd Witness
47 Auxiliary Seal Plan SS CS Tubing Pipe NPSH Test Req'd Witness
48 Auxiliary Seal Flush/Quench Fluid Internal Insp'n After Test Req'd Witness
49 Seal Flush Piping Threaded Socket Weld Flanged Other: Req'd Witness
50
51
52
Rev Date Description By Chk. Appr. Rev Date Description By Chk. Appr.
Sight FI ?gpm
Corrosion/Erosion Caused By:
Solids Present
16.7
Specific Gravity 0.854 0.839
190120
Vapor Press. @ PT psia6.87Viscosity @ PT
Suction Pressure 14.7NPSH Req'd @ Impeller CL * @ TOC *
Rotation (viewed from Cplg end)
14Location
* Hydr. Eff'y **@ Max. Impeller *
Manufacturer's Proposal Curve No.
Rated Brake Power *
Min. Flow Req'd *Suction Specific Speed *
*RPM No. Stages
Size Distribution
Concentration
Drip Pan
Wear Rings
Sleeve(s)
Ambient Temp. 100 10
Elev. 97
3 60
Wear Rings
Applicable Specifications
Weights and Dimensions
Internal Wear Parts
Epoxy Grout, etc.
Impeller
Shaft
Baseplate
Inspection and Tests
Corr. Allow.
GlandInt'l Ctg/Lining
CONSTRUCTION
SITE CONDITIONS
Materials
Electrical Power 220/440
NPSH Available
CW Supply
CW Return
RF
Liquid Pumped Crab JuiceCapacity @ PT, Normal gpm400 Rated gpm500
150#
150#1" Case/Trim (API Class)
Casing
0 For Inquiry
Size Rating
Suction
Discharge 3"
170
2. See Motor Data, Sheet 2 of 2.
1. Items marked with an asterisk (*) to be completed by Vendor.
9-Oct-02
Facing Location
Remarks
Area Classification: Class Div. Group 1
Nozzles
FF
A. Montemayor
Mfr Ref. No. * No. Req'd One
OPERATING CONDITIONS, EACH PUMP PERFORMANCE
Plot Plan No. PLT-03-0000PID-01-0000
Model **Manufacturer
P&ID No.
CENTRIFUGAL PUMP SPECIFICATION(English Units)
Project No.
P-37
1234567
Service
Location P.O. No.
Equipment No.Crab Juice Transfer Pump
Galveston, Texas Unit Balinese Room
*
* *
*
*
*
Auxiliary Piping
Stainless Steel tubing & piping
77.7
63.0
90
XYZDEFABC
Rev.
No.M
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1 of 1
Corporation
1
2
3 Mfr Ref. No.
4 Draft Type: No. of Bays
5 Btu/h F Surface/Unit, Finned ft2; Bare Tube ft
2
6
7
8
9 Fluid Name
10 Total Fluid Entering lb/h
11
12 Temperature F
13 Vapor lb/h
14 Mol. Wt.
15 Liquid lb/h
16 lb/h
17 Mol. Wt.
18 Steam lb/h
19 Water lb/h
20 Fluid Vaporized or Condensed lb/h Velocity X Max. Min. fps
21 Steam Condensed lb/h
22 Liquid Specific Gravity
23
24 Air Quantity, Total lb/h scfm Plant Altitude ft Above Sea Level
25 Air Quantity per Fan lb/h scfm Temperature In (Design Dry Bulb) F
26 Velocity X Max. Min. Temperature Out F
27 Face Velocity std fps Mass Velocity (Net Free Area) lb/hft2 Min. Design Ambient Temp. F
28
29 F
30
31
32
33 Arrangement: Two in.
34 Bundles in Series Parallel 40 ft
35 Bays in Series Parallel Gasket Material in.36 Bundle Frame:
37 No. Size Rating Facing
38
39
40 in. in.
41 Louvers Auto Manual F
42
43
44
45
46
47 ft
48 HP
49 fps50 % Auto-Variable % v Ph Hz
51 Yes No
52 Air Failure Control Action: Fan Pitch Min. Max. Lockup Louvers Open Close Lockup
53 Vibration Switches Req'd? Yes No Chemical Cleaning, etc.
54 Weight - Bundle lb Shipping Weight lb
55
56
57
Rev Date Description By Chk. Appr. Rev Date Description By Chk. Appr.
in.
Code Requirements: ASME Sec. VIII, Para. 1 (1992)
Structural Mounting
Surface Preparation Temperature
**
Length :
Pitch : Rot. Square1.25
Plug Material
Effective MTD
Other Ref. Dwg No.
Viscosity, Liquid
Viscosity, Vapor
Latent Heat
Btu/fthF
Btu/fthF
cP
Forced
PERFORMANCE DATA - TUBE SIDE
Size
Btu/lbF
Btu/lbF
Welded
50
Pattern
Corrosion Allowance
No. of Passes Slope in./ft
0.125
Seamless
OD 1-1/2" 18Gage, B.W.G. :
Material :
Material :
Pressure
Type :Inlet
Outlet
Fins/inch
Transfer Rate, Ext'd Surface :
150
Non-Condensables
PERFORMANCE DATA - AIR SIDE
Bare Tube - Service :
Lethal Service?
Specific Heat, Vapor
Thermal Cond., Liq.
Btu/lb
One
OD
psig psig
Miscellaneous Connections
Size
Location
Process Vapor Condenser
Model
Service
* *
Unit
Manufacturer
250
100,000,000
Type
Heat Duty
Cedar Rapids, Iowa Furfural P.O. No.
1234567Project No.
No. Req'd*
No
Specific Heat, Liquid
cP
Fabrication Type :
Tube Sheet Joint :
No./Bundle :
Tubes
Fins
Low-Finned
316 Stainless SteelType
No. per Bay Material 316 Stainless SteelTube Rows
MECHANICAL EQUIPMENT
Type :TypeMfr/Model No.
Driver Speed Reducer Fan
RPM
Tip SpeedPitch Adj.
No./Bay HP/Fan
Pitch Angle
Blade Mat'l
Enclosure
HP/Driver RPM
ABC DEF27-Nov-020 For Inquiry XYZ
Remarks 1. Items marked with an asterisk (*) to be completed by Vendor.
AIR-COOLED EXCHANGER SPECIFICATION(English Units)
Mfr/Model No.
No./BayNo./Bay
Mfr/Model No.
Btu/ft2hF
Inlet Outlet
Plot Area *
Steam Coil?
AGMA Rating
Power Ratio :Support : Structure
Sheet
Des. Temp.
Stock Thk.
Gear box
Clean :
External - Over SideAir Recirculation Control :
Diameter
Equipment No.
Plot Plan No.P&ID No.
Btu/ft2hF Btu/ft
2hF
DP, Clean (Allow./Calc.)
Pour/Freeze Point
Dew/Bubble Point F
F
psi
Min. Fouling Resistance ft2hF/Btu
Operating Pressure, Inlet psig
In Out
Thermal Cond., Vap.
Section
CONSTRUCTION AND MATERIALS
Test PressureDesign Pressure Design Temperature
Header
Rev.
No.Montemayor
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Sheet 1 of 1
Corporation
1
2
3
4 Horiz. Vert. Connected in Series Parallel
5 ft2 Gross Eff. Surface/Shell * ft2 Gross Eff.
6
7 PERFORMANCE OF ONE UNIT8
9
10
11
12 Liquid lb/h
13 Steam lb/h
14 Non-Condensables lb/h
15 Fluid Vaporized or Condensed lb/h
16 Steam Condensed lb/h
17 F
18
19 Viscosity
20 Vapor Molecular Weight
21 Specific Heat
22 Thermal Conductivity
23 Latent Heat
24 Operating Pressure, Inlet
25 Velocity Max. Min.
26 psi
27
28
29 Btu/ft2hF . Btu/ft
2hF .
30 CONSTRUCTION AND MATERIALS
31 SHELL SIDE TUBE SIDE Sketch (Bundle, Nozzle Orientation)
32 Design Pressure psig
33 Test Pressure psig
34 Design Temperature F
35 Number of Passes per Shell
36 In37 Out
38 Intermediate
39 Tubes: Type Number OD in. BWG or in. X Min. Av. Wall
40 Tube Length in. Tube Pitch in. Flow Pattern (circle one)
41 Shell: ID in. OD in. Tube-to-Tubesheet Joint :
42 Baffles - Cross: Type Spacing in. % Cut on X Diam. Area
43 Baffles - Long: Perm. Removable Seal Type: Bypass Seal:
44 rv2: Inlet Nozzle * lb/ftsec Bundle Entrance lb/ftsec Bundle Exit lb/ftsec
45 Expansion Joint? Yes X No Type: Impingement Protection? X Yes No
46
47 Tubes
48 Shell
49 Shell Cover
50 Channel51 Channel Cover
52 Fltg Head Cover
53
Stress Relieved (Mark "SR') and/or Radiographed (Mark 'XR') Parts User Spec.:
54 Code Requirements: ASME Sec. VIII, Para. 1 (1992) Stamp? X Yes No TEMA Class:
55 Weights: Shell lb Filled with Water lb Bundle lb
56
57
58
Date Description By Chk. Appr. Rev Date Description By Chk. Appr.
*
* *
**
Carbon Steel
Carbon Steel
Carbon Steel
Carbon SteelCarbon Steel
Stnless Steel
None
0.0625None
NoneNone
16
Rolled and welded
0.062514 BWG Min
* * *
*
*
0.9375
0.75
Btu/lbF
Btu/hftF
Btu/lb
cP
psig
fps
0
Rev
Remarks: 1. Items marked with an asterisk (*) to be completed by Vendor.
Fouling Resistance
Pressure Drop, Clean (Allow./Calc.)
*
Transfer Rate, Service *
Heat Exchanged Btu/h
ft2hF/Btu
Log MTD (Corrected) * FLog MTD (Uncorrected) F
None
None0.125
0.125NoneNone
Cross BafflesLong Baffle
Gaskets
*
**
**
Floating Tubesheet
Fixed Tubesheet
Tube Supports
Site: Km 8, Avda. Venezuela; Lima, PeruMfr Ref. No.
Carbon Steel
(English Units)
Density, Specific Gravity
Temperature
lb/hTotal Fluid Entering
Fluid Allocation
Fluid Circulated
Service:
Manufacturer:
P&ID No.:
Carbon Steel
Carbon Steel
PART MATERIAL THK, in. C.A., in. PART MATERIAL
Carbon Steel
Carbon Steel
Stnless Steel
Vapor (In/Out) lb/h
THK, in. C.A., in.
Transfer Rate, Clean
Equipment No.
SHELL SIDE
Surface/Unit: *Other Ref. Dwg No.Plot Plan No.
Shells/Unit
SHELL & TUBE HEAT EXCHANGER SPECIFICATION
Project No.
*
Unit German Huanuco P.O. No.
Model
TUBE SIDE
*TEMA Size, Type:
No. Req'd
One
Lean MEA Solution Cooler
*
*
For Purchase
ConnectionsSize & Rating
Rev.
No.
Montemayor
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Sheet 1 of 1
Corporation
1
2
3
4
5
6 Position Horizontal X Vertical
7 Shell Diameter ID X OD ft-in. 8'-0" 8'-0"
8 Shell Length TL-TL X S-S ft-in. 9'-6" 9'-6"
9 Internal Pressure psig 0 0
10 Temperature (Min/Norm/Max) F Amb. Amb.
11 Nominal Volume 3,000 gal Total Volume 4,900 gal
12 Fluid Contained Aqueous Amine Sol'ns Specific Gravity 1.0 Note 4
13 Vapor Pressure @ Max. Ambient Temperature 0.95 psia
14 Process Contaminants
15 Service is X Cyclic Lethal Other
16
17
18 Shell & Heads
19 Internals X Weld-in
20 Remov.21 Supports
22
23
24 Des. Press. @ Top psig Ext. Des. Press. psig
25 System PSV Set @ psig; located @
26 Des. Temperature F Minimum Temp. F
27 Vessel Support(s) Skirt X Legs Lugs Saddles
28 Height (Btm of Horiz. or BTL of Vert.) ft Above Grade
29 Fireproofing Other
30 X Insulation X H C PP Thickness in.
31 Design Codes: ASME Section VIII (1992); no stamp req'd
32 Post-Weld Heat Treatment for:
33 X Radiograph 85 % Inspection Req'd? X Yes No34
35 Mark Service Qty Size Rating Facing
36 1
37 1
38 1
39 1
40 1
41 1 Specify Operating Levels Above Btm or BTL
42 1
43 1 LCH
44 1 HLL
45 1 LAH
46 1 NLL
47 1 LAL
48 1 LLL
49 1 LCL
50 1
51 1 Weights: Vessel Only lb Internals lb
52 Operating Weight lb Full of Water lb
53
54
55
Chk. Appr.
DEF XYZ
*
*
N/A5
top of vessel
100 -20
*
PROCESS VESSEL SPECIFICATION(English Units)
RF
Light (Future)
Sight Glass (Future)
Spare 4"
4. Nozzle 'E': Tube Turn 12" T-Bolt hinged closure.
1. Items marked with an asterisk (*) to be completed by Vendor.Remarks:
Chk. Appr.Date Description By
0
Rev
For Inquiry
DescriptionDate
30-Sep-00
1"
2. Ref. set of detail dwgs for existing V - 41 (circa 1969). 3. Agitator supplied by Owner; conn. details on ref. dwgs.
Rev By
ArtM
300 lb
300 lb RF
Liquid Inlet w/Dip Tube
Liquid Inlet w/Dip Tube
N2 Pad
Vent
Fill Connection (Note 4)
Agit'r Opn'g w/Reinf. Pad (Note 3)
Manhole w/Davit
Relief Valve
Level Indicator (DP Cell)
N
O
P
Level Indicator (Equal. Conn.)
Liquid Inlet
Temp. Indicator
Pump Suction
H
Q
J
K
L
M
B
C
D
E
F
G
Unit
Model
Plot Plan No. Other Ref. Dwg No.PLT-03-2049
A
Equipment No.
P.O. No.
No. Req'd
Project No.
V - 41
* OneMfr Ref. No.
Site:
Manufacturer
Service:
P&ID No. PID-01-2084
Belle Glade, Florida
Filter Feed Tank
Furfural
**
304SS
304SS Baffles, Dip Tubes,
0.0625
0.0625
NoneNone
Vortex Breaker
Note 2
PROCESS (OPERATING) DATA VESSEL SKETCH
RemarksCA, in.MaterialComponent
NOZZLES/CONNECTIONS
MECHANICAL DESIGN
304SSCarbon Steel
LJ
1" 300 lb RF
Top Bottom
METALLURGY
2" 150 lb RF
1"
1"
1"
1"
1" 300 lb
1"
3"
3"
4"
6"
2"
2"
4"
300 lb
300 lb
300 lb
300 lb
300 lb
300 lb
RF
RF
RF
RF
300 lb
300 lb
300 lb
300 lb
300 lb
300 lb
RF
LJ
RF
RF
LJ
RF
RF
RF
K
Montemayor
Rev.
No.
Standard DisplacerRanges are:
14"24"
32"45"
Special DesignOver 45"
9'-6"S-S
8'-0" OD
1
1
HA
O
PB D
FC E
L
J
M
N
G
6'-11"
Vortex Breaker4Legs(min.)
Baffle(4 req'd)
DipTube(2req'd,
Nozz
les'A'&'B')
Q
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1
2
3
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7
8 oF9
10
11
12
13
14
15
16
17
18
19
20 in. in. in.
21
22
23
24 End Connections (Size, Rating, Facing)
25 Bonnet Type Number of Ports
26 Lube
27
28
29
30
31
32
33
34
35 Size
36
37
38
39
40
41
42
43
44
45
46 Type Quantity
47
48
49
50
51 Set Press.
52
53 I 1 II 1 III 2
54
55
56
57
58
Valve Percent Open
Upstream Pressure @ Flow
Downstream Pressure @ Flow
N.A.
200 265 350
500
4.268
psig
350
500
Four
1" 1500# Ring-jointRF 1"
Montemayor Corporation
Fluid Name Phase(s)
psig
F-01-24112" 300AA-5238-457 1" 1500AA-5238-460
N.A.
Unit
InstrumentFormNo.
psi Closed
Packing MaterialPacking Type
VALVE SELECTION, FLOW CHARACTERISTICS
Manufacturer Valtek
Molded V-Ring
cPCritical Press., PC Op'g Viscosity, m
7 psi
lb/ft3
Actual CV @ % Open
Two
psi
Standard Two Cooling Fin
RF 150#
Under
Recycle Gas Vap SCFM
150 180 350
7.0
Over
Bal. in.
Mod. Parabolic
AutomaticValves
300#
316ss
316ss
25%
Fluid Density at Inlet T&P, Flow 0.2708
Maximum Closed DP Fail Position
Trim Characteristic
Closed
Under
100%
LinerBonnet/Body
Lube & Isolating Valve (check)
Extended
2"
Da
te
12-Ma
r-00
Min. Req'd Press.
Spring Action Handwheel Pos., Orient.
Eff. Area, in.2 Service
Max. Allow. Press.
Manufacturer Model
Rev.0
Description By Chk.
SG @ Op. T
Estimate InquiryP.O. No.
PCV G 2ndF-01-2411
Tequila Conmemorativa
350
SCFM2-PhRecycle Gas
C - G - 02 & C - G - 03
150 290
MATERIALS
Molded V-Ring Graphite Impreg.
N.A. psia 0.013
500 500
495 495 495 495
50% 90%
Model Valtek
Rev Date Description By
Cage/Guide Stem
200 265 350 350
N.A.
psia cP0.012
4.268
995 995 995 995
1000 1000
0.6082
Liq. SG @ 60oF Vapor MW
Norm. Max. Capacity
1000 1000
cPpsia
Liq gpm
Open
Flow Units
Temp., Min. Operating Max.
Flow, Min.
Assoc. Equip./Service
Perros Bravos, N. L.
C - G - 02 & C - G - 03
PCV G 1st
Location
Tag Number
P&ID Number
Line Number
INSTRUMENT SPECIFICATION - CONTROL VALVES(English Units)
1Sheet 1
1937Project No.
Valve CV @ Flow (Calculated)
Increases
SWITCHES
Appr.
psig
Rev DateChk.
psig
Double-actingSingle-acting
Appr.
psigpsig
POSITIONER
Diaphragm, pneumatic
Open Top, Left-hand
Modulating Modulating On-off
316ss
316ss
Diaphragm, pneumatic
ACTUATOR
Plug/Ball/Disk Seat/Seat Ring
Type Hydraulic Piston
psigRated Travel @Travel starts @
Avail. Air Supply Press., Max. Min. psig
None
Manufacturer Model
Type
Manufacturer
Check Other By-passGauges
CamSignal incr. output to Actuator
Group B
Filter
Manufacturer Model
SPECIALS/ACCESSORIES/TESTS
Class GroupAGroup Div.Div. Class
Actuation Points
psig Filter Gauge
AIR SET
Model
psig
Square Root
psig
Other (check)
Mechanical
psigpsig
psig
psigpsig
Decreases Square Root
Gauges
ANSI/FCI Leak ClassHydro Pressure
Open
Contacts/Rating
Electrical Area Classification (if appl.) Class
Increases Linear
psig Filter Gauge
Trim Size
Proximity
in.Unbal.
in.
Bal./Unbal. Body Size Port Size
SERVICE CONDITIONS
in.Stroke in.
Linear Equal %
Bal.
Flow Direction
in.
in. in. in.
The Recycle Gas working fluid is a binary mixture of 15% vol NH3 + 85% vol H2 (60 % wt NH3 + 40 % wt H2)
Two control valves are required for each of the two services.
Remarks
Other
psig Class II
psig
psig
Close Top, Right-hand
psig psig
psig
psig
psig Class III
Braided Graphite
Class Ipsig
CDiv.
Graphite Impreg.
Gauge
By-pass Gauges
Pneumatic
By-pass
Side, Left-hand
M
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Corporation
1
2
3
4
5
6 Manufacturer's Proposal Curve No.
7 Service is Continuous Intermittent for hrs/day Centrifugal Axial Vane
8 lb/h or SCFM No. Stages 1 Efficiency %
9 Capacity, Design lb/h or SCFM Inlet Size/Rating Top Bottom Side
10 Inlet Pressure in. WC Inlet Temp. F Disch. Size/Rating Top Bottom Side
11 Disch. Pressure in. WC Disch. Temp. F Case Design Press. psig; Design Temp. F
12 Gas Mol. Wt. Compr. (Z) at Inlet Relief Valve No. Located @
13 Cp/Cv at Inlet By Mfr By Customer Set @
14 Corrosion/Erosion Caused By Rotation (viewed from Cplg end) CW CCW
15 Dust Present? No Yes ; Name Packing, Type: No. of Rings
16 Concentration gr/ft3 Size Range m Mech. Seal, Type: Mfr by
17 Solids are Abrasive Explosive Sticky
18 Other (specify)
19 Type: Mfr to Furnish Mount
20 Location Indoors x Outdoors Elev. 97 ft ASL Direct Indirect: V-Belt Gear 21 Ambient Temp. F Max. F Min. Single Variable Speed HP RPM
22 Max. Relative Humidity Other v Ph Hz Enclosure
23 Electrical Area Classification NEMA Service Factor
24
25
26
27 Cast Iron Aluminum Steel Ball Steel V-Belt
28 Steel Alloy Steel 316SS Sleeve Static Conductor
29 Aluminum Cast Steel Roller Guard
30 316SS 316SS Sparkproof
31
32
33 Flexible Oil Stellited Bronze Bronze Seal
34 Fast/Falk Grease 420SS Cast Iron Cast Iron Bearing
35 Guard None Steel Steel None
36 Sparkproof None
37
38 Common Baseplate and Driver by Mfr? Yes No Baseplate Mat'l Cast Iron Fabricated Steel
39 Baseplate Dimensions Approx. Wt., Blower & Base lb lb
40
41
42
43
44
4546
47
48
49
50
51
52
Rev Date Description By Chk. Appr. Rev Date Description By Chk. Appr.
0 27-Dec-96 For Inquiry ABC DEF XYZ
CENTRIFUGAL FAN, BLOWER SPECIFICATION(English Units)
Gears V-Belt Drive
No. Req'd One
P.O. No.
Bearing Lubrication Shaft Sleeve Lantern Ring
Driver
SITE CONDITIONS
MECHANICAL DETAILS AND MATERIALS OF CONSTRUCTION
Driver Wt.
Water Cooling
PROCESS CONTROL SKETCH (Incl. Scope of Supply
Coupling(s)
Capacity, Normal
Type
Case Rotor(s) Shaft Bearings
Other Ref. Dwg No.
RPM 3600
Packing Gland
Gas Handled :
Plot Plan No. PLT-03-0000OPERATING CONDITIONS PERFORMANCE
*Manufacturer
P&ID No. PID-01-0000
* Model * Mfr Ref. No.
Project No.
Service Political Hot AirSite: Kingston, Jamaica Unit Alf Newton
CF - 100
1234567
Equipment No.
Montemayor
Rev.
No.
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1
2
3
4
5
6
7
8
9
10
11
12
13
14 Quality (%) or Superheat (F)
15 N Y N Y N Y
16
17 N Y N Y N Y
18
1920
21
22
23
24
25 in. in. in. in. in. in.
26
27
28
29
30
31
32 Vent (top) Drain (btm) Vent (top) Drain (btm) Vent (top) Drain (btm)
33
34
35
36
37
38
39
40
41 Gr Div Gr Div Gr Div
42
43 Hi Lo Fault Hi Lo Fault Hi Lo Fault
44
45
46
47
48
49
50
51
Rev Date Description By Chk. Appr. Rev Date Description By Chk. Appr.
Fluid Density @ STP
Compress. FactorMol. Wt. CP/CV
Date
5-May-99
Plate
F
langes
Sheet
(English Units)FLOWMETER SPECIFICATION, ORIFICE PLATE
MontemayorProject No.
El Gallinero, Nuevo Leon Huevos Rancios *Location Unit P.O. No.
Tag Number
P&ID Number
Line Number
Service or Associated Equipment
cP
psig
gpm lb/min
Fluid Name and Phase (l, v, g or 2 )
Flow, Min. Nominal Max. units
Temp., Min. Nominal Max.
Press., Min. Nominal Max.
Air or Gas Bubbles; Name
SSUViscosity, Min. Nominal
Size Range
Pipe Diameter Schedule
Units
Vent, Drain, Other?
Meter Type
DP @ Max. Flow: Allow./Calc. *
Other:
Manufacturer Model
feet
ClassClass
Other:
feet
Special Requirements:
feet
Min. Range
Area Classification Class
Switches/Alarms
Other:Totalizer (check)
Cable Distance (Transducer to Console)
Units
Housing Requirements
1. Items marked by an asterisk (*) to be completed by Vendor/Mfr.Remarks
Other:
Rev.
0
InstrumentFormNo.
b = d/D
Material
SERVICE CONDITIONS
METER SELECTION, MEASUREMENT PARAMETERS
INSTALLATION, INTERFACE SPECIFICATIONS
Bore Diam., d Thickness
Location
Design Std
Size Range
@ Op'g T&P
Max.
% by volume
% by weight
Flanges & Taps: Supply by
Tap Size
Plate Type Material
Bore Sized for
Rating
Ring Type (if appl.) Material
MaterialFlange Type
Pipe ID, D
Suspended Solids; Name
Manufacturer Model
Liner Material Insulation Thk, Type
ORIFICE PLATE AND FLANGE SPECIFICATIONS
Output Units
UnitsStatic
Chart or Scale Range Chart Multiplier
Range: Diff. (Dry)
Seal Sp. Gr. @ 60F
F F
psig
F
psig
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1
2
3
4
5
6
7
8
9
10
11
12
13 N Y N Y N Y
14
15 N Y N Y N Y
16
17
1819
20
21
22
23 F F F
24
25
26
27
28 % % %
29
30
31
32
33
34 II Gr Div 2 II Gr Div 1 III Gr Div 1
35
36 Hi Lo Fault Hi Lo Fault Hi Lo Fault
37
38
39
40
41
42
43
44
45
46
47
48
Rev Date Description By Chk. Appr. Rev Date Description By Chk. Appr.
Op'g T&PSTPFluid Density @
RFConn. Size Type Face WN 125# FF
* psig *
Full Scale% of
% of Full Scale
A
1" 1" SW
Material, Wetted Parts Gaskets, Rings
300# FF
lb/ft
Liq
Material
Max.
% by volume
% by weight
Flow Acc'y @ Min./ Nom.
Rev.
Date
SERVICE CONDITIONS
InstrumentFormNo.
Special Requirements:
Area Classification Class
Output Units Housing Requirements
Other:
4 to 20 mA
Switches/AlarmsOther:
feet
Other:
NEMA-4X
Remarks
Totalizer (check)
Cable Distance (Transducer to Console) feet
UnitsMin. Range
feet
1. Items marked by an asterisk (*) to be completed by Vendor/Mfr.
Class C
% of Reading
INSTALLATION, INTERFACE SPECIFICATIONS
Class B
* g/cc *
% of Full Scale
* * *
* * * %
*
*
* * *
150#2" SO
% of Reading
psi
psig *
* * * fps*
* * * %
% of Reading
* g/cc *
** * psi
fps
* * *
* *
* g/cc *
* * * %
* * * fps
* * *
psi
psig **
* * *
Density Accuracy
Velocity @ Min. Nominal Max. Flow
NRe @ Min. Nominal Max. Flow
Max. Flow
Model
Meter MAWP Max. Allow. Temp.
DP @ Min. Nominal Max. Flow
Rating
Liner Material Insulation Type, Thk None None
Manufacturer
FLOWMETER SELECTION, MEASUREMENT PARAMETERS
* *
Air or Gas Bubbles; Name
Size Range
Suspended Solids; Name
Size Range
Pipe Diameter Schedule
A-Swt " Hot
Viscosity, Min. Nominal
1"
Temp., Min. Nominal Max.
Press., Min. Nominal Max.
Fluid Name (l, v, g or 2 )
Flow, Min. Nominal Max. units
cSt
lb/gal
lb/min
F
psig
SSU
Gas
g/cc
F
cP
psig
gph
Vap
psig
gpm
F
Tag Number
P&ID Number
Line Number
Service or Associated Equipment
Project No.
Chiclayo, Peru Cayalti *Location Unit P.O. No.
Pulse NEMA-7 Digital NEMA-12
Sheet
(English Units)FLOWMETER SPECIFICATION, CORIOLIS
Montemayor
0
5-May-
99
Required Accuracy
Required RepeatabilityOther:
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1
2
3
4
5
6
7
8
9
10
11
12
13 N Y N Y N Y
14
15 N Y N Y N Y
16
17
1819
20
21
22
23 F F F
24
25
26
27
28 % % %
29
30
31
32
33 I Gr Div 2 II Gr Div 1 III Gr Div 1
34
35
36 Hi Lo Fault Hi Lo Fault Hi Lo Fault
37
38
39
40
41
42
43
44
45
46
47
48
Rev Date Description By Chk. Appr. Rev Date Description By Chk. Appr.
Material
@ Op'g T&P
Max.
% by volume
% by weight
FLOWMETER SELECTION, MEASUREMENT PARAMETERS
SERVICE CONDITIONS
Date
5-May-9
9
Rev.
0
InstrumentFormNo.
Special Requirements:
1. Items marked by an asterisk (*) to be completed by Vendor/Mfr.Remarks
NEMA-4
Digital
Other:
feet
NEMA-7
Pulse
Other:
feet
Totalizer (check)
Cable Distance (Transducer to Console)
UnitsMin. Range
feet
AlarmsOther:
Class CArea Classification Class
NEMA-4X
4 to 20 mA
Housing Requirements
Output Units
% of
BA
% of
%
g/cc
fps
psi
psig
% of
%
g/cc
% of
fps
psi
psig
Full Scale% of
% of Reading
INSTALLATION, INTERFACE SPECIFICATIONS
Class
* g/cc *
* * * %
* * fps
* * *
psig **
Density Accuracy
Required Accuracy
Required Repeatability
Other:
psi* * *
*
NRe @ Min. Nominal Max. Flow
Flow Acc'y @ Min./ Nom. Max. Flow
Velocity @ Min. Nominal Max. Flow
Liner Material Insulation Type, Thk
Manufacturer Model
Max. Allow. Temp.
* *
None Hot
Size Range
Pipe Diameter Schedule
Air or Gas Bubbles; Name
Size Range
Suspended Solids; Name
None None
Nominal Max.
A-Swt
Fluid Density @ STP
Viscosity, Min. Nominal
Fluid Name (l, v, g or 2 )
Flow, Min. Nominal Max. units
1"
Temp., Min. Nominal Max.
Press., Min.
lb/ft3
cP
psig
gpmoF
lb/ft3
cP
psig
gpmoF
cP
psig
lb/ft3
gpmoF
Tag Number
P&ID Number
Line Number
Assoc. Equip./Service
Caracas, Venezuela Rbt. Humphries *Location Unit P.O. No.
FLOWMETER SPECIFICATION, MASS(English Units)Montemayor
Project No.
Sheet
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21/27
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No.
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22/27
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Corporation
1
2
3
4
5
6
7
8
9
10
11
12
13 N Y N Y N Y
14
15 N Y N Y N Y
16
17
18
19
20
21
22
23 F F F
24
25
26
27
28 % % %
29
30
31
32
33 II Gr Div 2 I Gr Div 1 I Gr Div 1
34
35
36 Hi Lo Fault Hi Lo Fault Hi Lo Fault
37
38
39
40
41
42
43
44
45
46
47
48
Rev Date Description By Chk. Appr. Rev Date Description By Chk. Appr.
FLOWMETER SPECIFICATION, TURBINE(English Units)Montemayor
Project No.
Sheet
Arica, Chile Air Products *Location Unit P.O. No.
Tag Number
P&ID Number
Line Number
Assoc. Equip./Service
oF
gpm
cP
psig
gpm
lb/ft3
psig
lb/ft3
cP
gpmoF
cP
oF
psig
lb/ft3
Fluid Name (l, v, g or 2 )
Flow, Min. Nominal Max. units
Temp., Min. Nominal Max.
Press., Min. Nominal Max.
Fluid Density @ STP
Viscosity, Min. Nominal
Air or Gas Bubbles; Name
Size Range
Suspended Solids; Name
Size Range
Pipe Diameter Schedule
* *
Liner Material Insulation Type, Thk
Manufacturer Model
Nominal Max. Flow
NRe @ Min. Nominal Max. Flow
Max. Allow. Temp.
*
Required Accuracy
Required Repeatability
Other:
Flow Acc'y @ Min./ Nom. Max. Flow
Density Accuracy
Velocity @ Min.
psig **
fps
* * *
*
* * *
psi*
INSTALLATION, INTERFACE SPECIFICATIONS
Class
* g/cc *
* * * %
Reading% of
% of Full Scale
psig **
fps
psi
* * * %
* g/cc *
% of
*
fps
psi
psig *
* * * %
% of
g/cc *
% of
% of
Area Classification Class
NEMA-4X
4 to 20 mA
AA
Housing Requirements
Output Units
Totalizer (check)
Cable Distance (Transducer to Console)
AlarmsOther:
Class C
UnitsMin. Range
feet
lb
Special Requirements:
NEMA-4
Pulse
Other:
NEMA-7
Pulse
Other:
US gal
feet
kg
feet
1. Items marked by an asterisk (*) to be completed by Vendor/Mfr.Remarks
Date
5-May-9
9
Rev.
0
InstrumentFormNo.
Material
@ Op'g T&P
Max.
% by volume
% by weight
FLOWMETER SELECTION, MEASUREMENT PARAMETERS
SERVICE CONDITIONS
*
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1
2
3
4
5
6
7
8
9
10
11
12
13 N Y N Y N Y
14
15 N Y N Y N Y
16
17
18
19
20
21
22
23 F F F
24
25
26
27
28 % % %
29
30
31
32
33 I Gr Div 1 II Gr Div 2 III Gr Div 2
34
35
36 Hi Lo Fault Hi Lo Fault Hi Lo Fault
37
38
39
40
41
42
43
44
45
46
47
48
Rev Date Description By Chk. Appr. Rev Date Description By Chk. Appr.
Material
@ Op'g T&P
Max.
% by volume
% by weight
FLOWMETER SELECTION, MEASUREMENT PARAMETERS
SERVICE CONDITIONS
Date
5-May-9
9
Rev.
0
InstrumentFormNo.
Special Requirements:
1. Items marked by an asterisk (*) to be completed by Vendor/Mfr.Remarks
NEMA-7
Digital
Other:
US gal
feet
NEMA-4
Pulse
Other:
kg
feet
Totalizer (check)
Cable Distance (Transducer to Console)
UnitsMin. Range
feet
lb
AlarmsOther:
Class CArea Classification Class
NEMA-12
4 to 20 mA
Housing Requirements
Output Units
% of
BA
% of
%
g/cc
fps
psi
psig
% of
%
g/cc
% of
fps
psi
psig
% of
% of
INSTALLATION, INTERFACE SPECIFICATIONS
Class
* g/cc *
* * * %
* * fps
* * *
psig **
Density Accuracy
Required Accuracy
Required Repeatability
Other:
psi* * *
*
NRe @ Min. Nominal Max. Flow
Flow Acc'y @ Min./ Nom. Max. Flow
Velocity @ Min. Nominal Max. Flow
Liner Material Insulation Type, Thk
Manufacturer Model
Max. Allow. Temp.
* *
Size Range
Pipe Diameter Schedule
Air or Gas Bubbles; Name
Size Range
Suspended Solids; Name
Nominal Max.
Fluid Density @ STP
Viscosity, Min. Nominal
Fluid Name (l, v, g or 2 )
Flow, Min. Nominal Max. units
Temp., Min. Nominal Max.
Press., Min.
lb/ft3
cP
psig
gpmoF
lb/ft3
cP
psig
gpmoF
cP
psig
lb/ft3
gpmoF
Tag Number
P&ID Number
Line Number
Assoc. Equip./Service
La Paz, Bolivia Pepe Mendietta *Location Unit P.O. No.
FLOWMETER SPECIFICATION, VORTEX(English Units)Montemayor
Project No.
Sheet
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25/27
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No.
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26/27
1 of
Corporation
1
2
3
4
5
6
7
8
9
10
11
12
13 N Y N Y N Y
14
15 N Y N Y N Y
16
17
1819
20
21
22
23 F F F
24
25
26
27
28 % % %
29
30
31
32
33 I Gr Div 1 II Gr Div 1 III Gr Div 2
34
35
36 Hi Lo Fault Hi Lo Fault Hi Lo Fault
37
38
39
40
41
42
43
44
45
46
47
48
Rev Date Description By Chk. Appr. Rev Date Description By Chk. Appr.
Sheet
*Location Unit P.O. No.
FLOWMETER SPECIFICATION, MAGNETIC(English Units)Montemayor
Project No.
Tag Number
P&ID Number
Line Number
Assoc. Equip./Service
Victoria, TX DuPont Nitric Acid
gpm
kPa
Liq
oC
lb/ft
cP
lb/min
oC
psia
lb/ft
SSU
lb/min
cSt
2-Ph
oC
atm
lb/ft
Fluid Name (l, v, g or 2 )
Flow, Min. Nominal Max. units
Gas
Temp., Min. Nominal Max.
Press., Min. Nominal Max.
Fluid Density @ STP
Viscosity, Min. Nominal
Air or Gas Bubbles; Name
Size Range
Suspended Solids; Name
Size Range
Pipe Diameter Schedule
* *
Liner Material Insulation Type, Thk
Manufacturer Model
Nominal Max. Flow
NRe @ Min. Nominal Max. Flow
Max. Allow. Temp.
*
Required Accuracy
Required Repeatability
Other:
Flow Acc'y @ Min./ Nom. Max. Flow
Density Accuracy
Velocity @ Min.
psig **
fps
* * *
*
* * *
psi*
INSTALLATION, INTERFACE SPECIFICATIONS
Class
* g/cc *
* * * %
Full Scale% of
% of Reading
psig **
Reading
fps
psi
Full Scale
%
g/cc
% of
*
fps
psi
psig *
%
% of
g/cc
% of Full Scale
% of
Area Classification Class
NEMA-4X
4 to 20 mA
BA
Housing Requirements
Output Units
Totalizer (check)
Cable Distance (Transducer to Console)
Reading
AlarmsOther:
Class C
UnitsMin. Range
feet
lb
Special Requirements:
NEMA-4
Digital
Other:
NEMA-7
Pulse
Other:
US gal
feet
kg
feet
1. Items marked by an asterisk (*) to be completed by Vendor/Mfr.Remarks
Date
5-May-99
Rev.
0
InstrumentFormNo.
Material
@ Op'g T&P
Max.
% by volume
% by weight
FLOWMETER SELECTION, MEASUREMENT PARAMETERS
SERVICE CONDITIONS
-
7/27/2019 Art's Process Spec Sheets
27/27
Rev.
No.