Amendment 3_Attachment 3 - FEL2 Distillation Column Information Package Revision 2.pdf

To: National Laboratory of the Rockies (NLR) Procurement and Subcontract Vendors

From:

Date: 12/10/2025

Subject: Process Design Basis – FEL II – IBRF Pilot Plant Revamp – Distillation Column

Unit Operation: Distillation Column

Feed Rate(s): 1.0 BBL/DAY from Hydrotreater of oxygen free C18 Alkanes

Assumptions:

• The unit is designed to operate with a maximum of 1 BPD production, and processing rates are likely to be lower.

• Control valve dP = 25 psi, when it is NOT a pressure control valve

• All electrical components must be NRTL certified. If they are not, they must be field verified.

o If additional cost is necessary to complete this task, please include the cost in the bid.

• One-line drawings are not complete and need to be done as the detailed engineering.

• Relief valve sizing is not complete and is considered a deliverable of detailed engineering.

• It is expected that the bid includes detailed design cost if necessary.

• Standard conditions are 60 deg F and 12 psia on South Table Mountain Campus

• Cooling water supply is available at 24 deg C (approx. 75 deg F) at approximately 50 psig

• BBL/DAY = 42 gal/day

Process Design Basis:

Un-stabilized distillate from the hydrotreater low pressure flash drum is fed to the top of the distillation column. The column has a reboiler on the bottom to supply heat for vaporization. The top of the column has a partial condenser to condense light end hydrocarbons formed in the process. The condenser will also cool the molecules too light to condense at the operating pressure. The overhead receiver can separate vapor, light organic phase and a water phase. The light organic phase can be refluxed back into the tower if necessary. The bottoms product is stabilized distillate for fuel consumption.

A small sump vessel has been added to the distillation column to act as the reboiler. The sump vessel should be mounted at the same elevation as the bottom of the column (bottom tangent lines of the vessels aligned). A two-zone clamshell heater is to be used as the reboiler heat source. The sump is not to be packed, internally.

The internals of the column will be designed so that they can be removed and changed frequently.

The design for the stripper of the hydrotreater used 0.16” 316 SS random packing and a height equivalent theoretical plate (HETP) of 1 ft per stage. The HETP of the packing will change with each system using this distillation column and will need to be included in the engineering study before each different experiment. The bottoms sump should be sized for a minimum five-minute hold up time. The vessel spec sheet and drawing will reflect the desired sizes. The pressure drop with the current hydrotreater model is approximately 0.2” psig, which is normal for this height of a column.

The overhead condenser is sized using the pilot plant cooling water supply of 75 deg F and 50 psig.

The overhead receiver should be sized for five minutes of holdup and surge time at a minimum. The vessel may be larger to accommodate the instrumentation needed for level and pressure control.

The vessel specification sheet and vessel drawing will reflect the needed dimensions. The organic level indication is to be a dP level and the water boot level is to be a float level that is top mounted.

The stripper bottoms stream is stabilized distillate that can be used as a finished product or proceed downstream to an isomerization unit if necessary. The bottoms stream will need to be cooled with an air cooler and trim cooler. The air cooler hot air is to be vented outdoors and will be fed into a header provided within the pilot plant.

The distillation column operating pressure is 20 psig. The maximum allowable pressure of this equipment will be 150 psig for the tower, condenser, and overhead receiver. The bottoms temperature does reach 685 deg F to vaporize the distillate for mass transfer. If the bottoms product is temperature sensitive and cannot be as high as 685 deg F, the distillation column will be rated for full vacuum, and a vacuum pump or ejector could be added to the overhead to accomplish this mode of operation. The P&ID reflects this connection. The ejector or vacuum pump is a separate equipment module, but it would be appropriate to use in tandem with this module.

Another option would be to inject live steam into the bottom of the tower to strip the light end material from the distillate product. This tower design does not currently allow for that capability.

The distillation column mass balance tables reflect the stripping operation necessary for hydroprocessing upstream. There is little to no overhead liquid, hydrocarbon or aqueous. This tower does, however, need to be flexible with operation so that it can make clean cuts and operate with temperature sensitive feeds. The temperature sensitive feeds will need a vacuum system, which is NOT a part of this bid. The tie point to the system is on the P&ID and should be included. The specification sheets for the overhead receiver, reflux and aqueous pumps show more flow than what the mass balance indicates. This is because they are oversized for more reflux if needed, or for a distillation where an aqueous overhead product is present, which is likely. The line lists have two cases per line for the P&ID 2300.D.002 because the stripper has very little flow, and when reflux is necessary, the flow is significantly higher.

This process will need to be controlled via a programmable logic controller (PLC) using a human machine interface (HMI). Currently the facility uses Opto 22 but is open to other hardware options.

Allen Bradley would be the preferred alternate. The facility HMIs are on Dell Computers located within the central control room of the pilot plant.

Additional Considerations

• Additional detailed engineering including but not limited to the following items needs to be included in this bid.

o Details regarding specific equipment selection o Relief valve sizing o Control valve selection o Equipment layout, particularly for taller items and maintenance needs o Rotating equipment selection o Finalized specification sheets o Electrical one-line drawings o Control hardware selection o PHA outcomes

• This package includes:

instrumentation specification sheets vessel specification sheets heat exchanger specification sheets pump and compressor specification sheets blower specification sheet piping and instrumentation diagrams (P&IDs) heat and material balance equipment lists instrumentation list o The process hazard analysis (PHA/HAZOP) has not been completed on this design.

This will be completed with NLR before construction begins.

• All pumps need to be mounted so that any NPSH requirements are met at start up conditions – meaning low to no levels.

• Maintenance access is required for rotating equipment and reactors. Cooling water exchangers need to be able to be removed periodically for cleaning.

• The equipment may be mounted on multiple structures if that helps ease construction. The pilot plant is divided into bays and are approximately 10 ft by 15 ft and 20 – 23 ft tall. The center of the building is taller than the outer perimeter.

• All product tanks are to be provided by the customer, NLR.

Material Balance Tables

Feeds Description Mass Flow, lb/day Density, lb/ft3 Volumetric

Flow, SCF/H or

GPD

Hydroprocessor Rx Effluent

294.2 5.943 46.578 GPD

GPD – gallons per day (24 hours at standard conditions); SCF – standard cubic foot; lb – pound mass

Products Description Mass Flow, lb/day Density, lb/ft3 Volumetric

Flow, SCF/H or

GPD

Offgas Vent 16.88 0.2137 6.8 SCFH Light Organic Product 0.00 47.62 0 GPD Aqueous Product 0.00 62.00 0 GPD Bottoms Product 277.3 48.07 42.42 GPD

GPD – gallons per day (24 hours at standard conditions); SCF – standard cubic foot; lb – pound mass; LPFD – low pressure flash drum

Utility Usage Utility Amount Necessary Note 1 Note 2 Cooling Water 0.213 gpm Pump/Compressor Motor Electrical Needs

2.32 Wh = 0.00232

kWh Brake Horsepower

Low Pressure Steam Usage

None regularly Would need some for decontamination

Clamshell Heater Electrical Needs

4420 BTU/hr

All utility needs will be met by NREL.

NATIONAL RENEWABLE ENERGY LABORATORY

National Renewable Energy Laboratory

15013 Denver West Parkway

Golden, CO 80401

Operated for the US Department of Energy by

The Alliance for Sustainable Energy, LLC

AutoCAD SHX Text Trim Cooler MOC: Tubes & Shell 316 SS MAWP: Shell - 150 psig @ 650 deg F Tubes: 100 psig @ 150 deg F

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AutoCAD SHX Text Note 2 - Bottom sump to have clamshell heater with 2 heating zones.

AutoCAD SHX Text Note 3 - Bottom sump to be installed at the same elevation as the bottom of the column.

AutoCAD SHX Text Note 4 - The internals of the distillation column is packed with 0.16" 316SS Pro Pak

15013 Denver West Parkway

Golden, CO 80401

Operated for the US Department of Energy by

The Alliance for Sustainable Energy, LLC

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12/11/25

15013 Denver West Parkway

Golden, CO 80401

Operated for the US Department of Energy by

The Alliance for Sustainable Energy, LLC

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Note 2 - Sample stations can include vendor packages if all functionality is present.

of

REV

316SS

316SS

316SS

316SS

316SS

316SS

316SS

316SS

2300.D.002

2300.D.002

2300.D.001

2300.D.001

P&ID Page Number

2300.D.001

2300.D.001

2300.D.001

2300.D.001

2300.D.001

316SS

316SS

Materials of Construction

316SS

316SS

316SS

316SS

2300.D.001

2300.D.001

2300.D.001

2300.D.001

LegalDisclaimer Version 2 4/7/2004

AZ Equipment List Piping System.xls

316SS106.8 50 0.2449 0.009504 1/2" 0.035

1/2"-PF-001100-316SS

H2S, H2, C1 - C5 material 421.9 -- 421.9 170 SCFH 2300.D.001

Condenser Outlet (Case 2) 30 SCFH & 3.85 gph 100 50 13.33 Mixed Phase 3/8"

Tower Vapor Outlet (Case 2)

Condenser Outlet (Case 1 - Stripping Operation)

3/8"-PF-002100-316SS

H2S, H2, C1 - C5 material 421.9 371.162 50.73

99.8 25 0.2449 0.009504 3/8" 0.035

3/8"-PF-002100-316SS

H2S, H2, C1 - C5 material 17.6 -- 17.6 6.8 SCFH

0.035

0.035Reflux to Tower Inlet (Case 2 - High Reflux & Higher Pressure Operation)

0.71 gph 100 50-75 28.22 0.0781 1/4" 2300.D.001 & 2300.D.002

1/4"-PF-002116-316SS

Overhead Naphtha 71 71 --

316SS

316SS

Bottoms Product to Storage (Outlet of 2300-E-003) 1.76 gph 100 0 48.07 2.968 1/4"

Reflux to Tower Inlet (Case 1 - Stripping Operation) 1/4" 0.035 2300.D.001 & 2300.D.002100 25 -- --

1/4"-PF-002116-316SS

Light End Hydrocarbon

(C3/C4/C5) 0 0 --

2300-E-002 Outlet

1/4"-PF-001109-316SS

Jet Fuel 277.4 277.3 --

175 5 46.26 1.511 1/4" 0.035

1/4"-PF-001108-316SS

Jet Fuel 277.3 277.3 -- 1.76 gph

0.035

0.0352300-LCV-001 Outlet to Bottoms Air Cooler 5 SCFH & 1.26 gph 651 15 2.155 Mixed Phase 1/4"

1/4"-PF-001111-316SS

Jet Fuel 277.3 198.1 79.24

2300-LCV-001 Inlet 1.76 gph 681.6 40 31.82 0.1544 1/4"

Bypass around 2300-LCV-001 (normally no flow - the listed is maximum) 1/4" 0.035681.6 40 31.82 0.1544

1/4"-PF-001107-316SS

Jet Fuel 277.3 277.3 -- 1.76 gph

Pump Spillback (normally no flow - the listed is maximum)

1/4"-PF-001106-316SS

Jet Fuel 277.3 277.3 --

681.6 40 31.82 0.1544 3/8" 0.035

3/8"-PF-001105-316SS

Jet Fuel 277.3 277.3 -- 1.76 gph

0.035

Pump Outlet 2300.D.0011.76 gph 681.6 40 31.82 0.1544 3/8"

Product from Bottoms Sump to Pump

3/8"-PF-001104-316SS

Jet Fuel 277.3 277.3 --

681.6 27 31.8 0.1544 3/8" 0.035

3/8"-PF-001103-316SS

Jet Fuel 277.3 277.3 -- 1.76 gph

0.035

0.035Reboiler Return 17.46 SCFH 681 27 0.8994 0.007725 1/2"

1/2"-PF-001101-316SS

Vaporized Jet Fuel and

Light Ends 265 -- 265

Tower Vapor to Condenser Inlet (Case 1 - Stripping Operation) 6.8 SCFH 106.8 25 0.2449 0.009504 3/8"

Tower Bottoms to Reboiler 1/2" 0.035475 27 38.23 0.3075

1/2"-PF-001102-316SS

Jet Fuel 542.3 542.3 -- 3.47 gph

Tower Vapor Outlet (Case 1 - Stripping Operation)

3/8"-PF-001110-316SS

H2S, H2, C1 - C5 material 17.6 -- 17.6

106.8 25 0.2449 0.009504 1/2" 0.035

1/2"-PF-001100-316SS

H2S, H2, C1 - C5 material 17.6 -- 17.6 6.8 SCFH

0.035 inches ft/sec psi/100 ftlb/day lb/day lb/day gph/scfh °F psig

PRESSURE DROP

DESCRIPTION

Total Liquid Vapour Temperature Pressure Density

ITEM NUMBER

FLUID

MASS FLOWS VOLUMETRIC

FLOWRATE

FLUID CONDITIONS NOMINAL

Viscosity OD Thickness Velocity lb/ft3 cP inch

EQUIPMENT LIST Project: IBRF Revitalization - Distillation Unit Site: STM - IBRF

DocumentNumber

National Laboratory of the Rockies PRIMARY PIPING SYSTEMS Project No.: Revision: Date: 12/9/2025

Client:

By: Chk'd: Appr'd:

National Laboratory of the Rockies Page

LegalDisclaimer Version 2 4/7/2004

AZ Equipment List Piping System.xls

2300.D.002 316SSLight Liquid Product to Level Control Valve 2300-LCV-004 (Case 1) 100.9 50 47.62 2.398 1/4" 0.035

1/4"-PF-002111-316SS

C3-C5 Hydrocarbons -- -- -- --

2300.D.002 316SSBypass around 2300-FCV-005 (Normally no flow - Case 2) 100.9 100 28.22 0.0783 1/4" 0.035

1/4"-PF-002115-316SS

C3-C5 Hydrocarbons 71 71 -- 0.71 gph

2300.D.002 316SSBypass around 2300-FCV-005 (Normally no flow - Case 1) 100.9 50 47.62 2.398 1/4" 0.035

1/4"-PF-002115-316SS

C3-C5 Hydrocarbons -- -- -- --

2300.D.002 316SSReflux to flow control valve 2300-FCV-005 (Case 2) 100.9 100 28.22 0.0783 1/4" 0.035

1/4"-PF-002114-316SS

C3-C5 Hydrocarbons 71 71 -- 0.71 gph

2300.D.002 316SSReflux to flow control valve 2300-FCV-005 (Case 1) 100.9 50 47.62 2.398 1/4" 0.035

1/4"-PF-002114-316SS

C3-C5 Hydrocarbons -- -- -- --

2300.D.002 316SS2300-P-002 Pump Outlet (Case 2) 100 100 28.17 0.0783 1/2" 0.035

1/2"-PF-002110-316SS

C3-C5 Hydrocarbons 371.2 371.2 -- 3.71 gph

2300.D.002 316SS2300-P-002 Pump Outlet (Case 1) 100 50 47.62 2.398 1/2" 0.035

1/2"-PF-002110-316SS

C3-C5 Hydrocarbons 0 0 -- 0 gph

2300.D.002 316SSHydrocarbon liquid outlet from 2300-V-001 (Case 2) 100 50 28.17 0.0783 1/2" 0.035

1/2"-PF-002105-316SS

C3-C5 Hydrocarbons 371.2 371.2 -- 3.71 gph

2300.D.002 316SSHydrocarbon liquid outlet from 2300-V-001 (Case 1) 100 25 47.62 2.398 1/2" 0.035

1/2"-PF-002105-316SS

C3-C5 Hydrocarbons 0 0 -- 0 gph

2300.D.002 316SSVent to thermal oxidizer (Case 2) 100 25 2.746 0.01257 1/4" 0.035

1/4"-PV-002103-316SS

H2S, H2, C1 - C5 material 50.7 -- 50.7 30 SCFH

2300.D.002 316SSVent to thermal oxidizer (Case 1) 100 0 0.0793 0.00926 1/4" 0.035

1/4"-PV-002103-316SS

H2S, H2, C1 - C5 material 17.6 -- 17.6 6.8 SCFH

2300.D.002 316SSBypass around 2300-PCV-002 (normally no flow) 100 25 - 50 0.2137 0.00937 1/4" 0.035

1/4"-PV-002102-316SS

H2S, H2, C1 - C5 material 17 - 50 -- 17-50 6.8 SCFH - 30

SCFH

2300.D.002 316SSVapor Outlet to 2300-PCV-002 (Case 2) 100 50 2.746 0.01257 1/4" 0.035

1/4"-PV-002101-316SS

H2S, H2, C1 - C5 material 50.73 -- 50.73 30 SCFH

2300.D.002 316SSVapor Outlet to 2300-PCV-002 (Case 1 - Stripping Operation) 100 25 0.2137 0.00937 1/4" 0.035

1/4"-PV-002101-316SS

H2S, H2, C1 - C5 material 17.6 -- 17.6 6.8 SCFH

316SSDependent on relief case

Dependent on relief case 150 1/2"

1/4"

1/2"-PV-002104-316SS

H2S, H2, C1 - C5 material Dependent on relief case

Relief valve outlet for 2300-PSV-001

0.035

2300.D.002

0.035 2300.D.002

316SSTower Vapor to Condenser Inlet (Case 2)

1/4"-PV-002116-316SS

H2S, H2, C1 - C5 material 17 - 422 -- 17 - 55

50 0.2449 0.009504 3/8" 0.035

2300.D.002 316SS6.8 SCFH - 30

SCFH 100 5 mm HgTie-in to future vacuum system (no flow for any case in this basis) ft/sec psi/100 ft

3/8"-PF-001110-316SS

H2S, H2, C1 - C5 material 421.9 -- 421.9 170 SCFH 106.8 lb/day lb/day gph/scfh °F psig lb/ft3 cP inch inches

PRESSURE DROP

P&ID Page Number Materials of Construction

DESCRIPTION

Total Liquid Vapour Temperature Pressure

ITEM NUMBER

FLUID

MASS FLOWS VOLUMETRIC

FLOWRATE

FLUID CONDITIONS NOMINAL

Density Viscosity OD Thickness Velocity lb/day

EQUIPMENT LIST Project: IBRF Revitalization - Distillation Unit Site: STM - IBRF

DocumentNumber

National Laboratory of the Rockies PRIMARY PIPING SYSTEMS Project No.: Revision: Date: 12/9/2025

Client:

LegalDisclaimer Version 2 4/7/2004

AZ Equipment List Piping System.xls

2300.D.002 316SS 0Aqueous Phase Product to Storage (Case 2) 100 5 62.1 0.6815 1/4" 0.035

1/4"-PD-002109-316SS

Water with trace hydrocarbon 200.16 200.16 -- 1 gph

2300.D.002 316SS 0Aqueous Phase Product to Storage (Case 1) 100 5 62.1 0.6815 1/4" 0.035

1/4"-PD-002109-316SS

Water with trace hydrocarbon -- -- -- --

2300.D.002 316SS 0Level Control Valve 2300-LCV-003 Bypass (Normally no flow - Case 2) 100 75 62.1 0.6815 1/4" 0.035

1/4"-PD-002108-316SS

Water with trace hydrocarbon 200.16 200.16 -- 1 gph

2300.D.002 316SS 0Level Control Valve 2300-LCV-003 Bypass (Normally no flow - Case 1) 100 50 62.1 0.6815 1/4" 0.035

1/4"-PD-002108-316SS

Water with trace hydrocarbon -- -- -- --

2300.D.002 316SS 0Waterboot Pump Outlet to 2300-LCV-003 (Case 1) 100 75 62.1 0.6815 1/4" 0.035

1/4"-PD-002107-316SS

Water with trace hydrocarbon 200.16 200.16 -- 1 gph

2300.D.002 316SS 0Waterboot Pump Outlet to 2300-LCV-003 (Case 1) 100 50 62.1 0.6815 1/4" 0.035

1/4"-PD-002107-316SS

Water with trace hydrocarbon -- -- -- --

2300.D.002 316SS 0Waterboot Outlet from 2300-V-001 to pump (Case 2) 100 50 62.1 0.6815 1/2" 0.035

1/2"-PD-002106-316SS

Water with trace hydrocarbon 200.16 200.16 -- 1 gph

2300.D.002 316SS 0Waterboot Outlet from 2300-V-001 to pump (Case 1) 100 25 62.1 0.68 1/2" 0.035

1/2"-PD-002106-316SS

Water with trace hydrocarbon -- -- -- --

2300.D.002 316SS 0Overhead light liquid product to storage (Case 2) 100.9 50 28.22 0.0781 1/4" 0.035

1/4"-PF-002113-316SS

C3-C5 Hydrocarbons 300 300 -- 3 gph

2300.D.002 316SS 0Overhead light liquid product to storage (Case 1) 100.9 50 47.62 2.398 1/4" 0.035

1/4"-PF-002113-316SS

C3-C5 Hydrocarbons -- -- -- --

316SS 03 gph 100.9 50 28.22 0.0781 1/4"

1/4"

1/4"-PF-002112-316SS

C3-C5 Hydrocarbons 300 300 --Bypass around 2300-LCV-004 (normally no flow - Case 2)

0.035

2300.D.002

0.035 2300.D.002

316SS 0Light Liquid Product to Level Control Valve 2300-LCV-004 (Case 2)

1/4"-PF-002112-316SS

C3-C5 Hydrocarbons -- -- --

50 28.22 0.0781 1/4" 0.035

2300.D.002 316SS 0-- 100.9 50 47.62 2.398Bypass around 2300-LCV-004 (normally no flow - Case 1) ft/sec psi/100 ft

1/4"-PF-002111-316SS

C3-C5 Hydrocarbons 300 300 -- 3 gph 100.9 lb/day lb/day gph/scfh °F psig lb/ft3 cP inch inches

PRESSURE DROP

P&ID Page Number Materials of Construction

DESCRIPTION

Total Liquid Vapour Temperature Pressure

ITEM NUMBER

FLUID

MASS FLOWS VOLUMETRIC

FLOWRATE

FLUID CONDITIONS NOMINAL

Density Viscosity OD Thickness Velocity lb/day

EQUIPMENT LIST Project: IBRF Revitalization - Distillation Unit Site: STM - IBRF

DocumentNumber

National Laboratory of the Rockies PRIMARY PIPING SYSTEMS Project No.: Revision: Date: 12/4/2025

Client:

DocumentNumber

PRIMARY PIPING SYSTEMS Project No.: Hydroprocessing & Stripper Revision: 0 Date: LastIssueDate Client: National Renewable Energy Laboratory Page 1 3

INSTRUMENTATION LIST Project: IBRF Revitalization - Equipment Site: Integrated BioRefinery Faciltiy By:

ITEM NUMBER

FLUID & STATE

MASS FLOWS VOLUMETRIC

FLOWRATE

FLUID CONDITIONS Pressure Remarks

Max psig psig psig P&ID Page

Chk'd: Appr'd:

DESCRIPTION

Minimum Normal Maximum Temperature Cp/Cv Density M.W. Viscosity Normal Min

Flow Rate (lb/day)

Flow Rate (lb/day)

Flow Rate (lb/day)

Flow Rate (SCF/h or BBL/Day)

Operating Temperature (F)

Cp/Cv Density (lb/cu ft)

Molecular Weight

Dynamic viscosity

FV

2300.D.001 Pressure transducer

0-- 110 1.147 0.245 39.11 0.0095

2300-TE-009 Light End Material - Hydrogen, CO, CO2, Methane - Pentane (vapor)

-- -- --Stripper Column Overhead Temperature

75 25

75 25

2300-PT-001 Light End Material - Hydrogen, CO, CO2, Methane - Pentane (vapor)

-- -- --Stripper Column Overhead Pressure

FV

2300.D.001 Thermocouple (Type K)

0-- 110 1.147 0.245 39.11 0.0095

25 FV

2300.D.002 Thermocouple (Type K)

0Stripper Column Condenser Outlet Temperature 100 1.067 0.214 39.11 0.0094 75

2300-TE-010 Light End Material - Hydrogen, CO, CO2, Methane - Pentane (mixed)

25 FV

2300.D.002 Thermocouple (Type K)

0Stripper Overhead Receiver Temperature 100 1.605 47.62 224.5 2.398 75

2300-TE-0014 Light End Material - Hydrogen, CO, CO2, Methane - Pentane (mixed)

20 FV

2300.D.002 Pressure transducer

0Stripper Overhead Receiver Pressure 100 1.147 0.214 39.11 0.0094 75

2300-PI-002 Light End Material - Hydrogen, CO, CO2, Methane - Pentane (mixed)

20 FV

2300.D.002 With actuator and positioner (want to be able to see the position readout on the SCADA) 0Stripper Overhead Pressure Control Valve 100 1.147 0.214 39.11 0.0094 75 2300-PCV-002 Light End Material -

Hydrogen, CO, CO2, Methane & Ethane (vapor)

5 16.88 65 6.8

20 FV

2300.D.002 Coriolis meter

0Overhead Vapor Flow 100 1.147 0.214 39.11 0.0094 75

2300-FIT-002 Light End Material - Hydrogen, CO, CO2, Methane & Ethane (vapor)

5 16.88 65 6.8

20 FV

2300.D.002 Pressure transducer

0Stripper Vapor Battery Limits Pressure 100 1.147 0.214 39.11 0.0094 75

2300-PI-003 Light End Material - Hydrogen, CO, CO2, Methane & Ethane (vapor)

20 FV

2300.D.002 Thermocouple (Type K)

0Stripper Vapor Battery Limits Temperature 100 1.147 0.214 39.11 0.0094 75

2300-TE-011 Light End Material - Hydrogen, CO, CO2, Methane & Ethane (vapor)

20 FV

2300.D.002 dP level instrument

0Stripper Overhead Receiver Organic Level 100 1.605 47.62 224.5 2.398 75

2300-LT-004 Light End Material - Propane - Pentane (liquid) -- -- -- --

20 FV

2300.D.002 With actuator and positioner (want to be able to see the position readout on the SCADA) 0Stripper Overhead Receiver Organic Level Control Valve 100 1.605 47.62 224.5 2.398 75

2300-LCV-004 Light End Material - Propane - Pentane (liquid) 0 57 400 2.12

20 FV

2300.D.002 dP level instrument

0Stripper Overhead Receiver Aqueous Level 100 1.024 62.1 18.02 0.682 75

2300-LT-003 Light End Material - water (liquid) -- -- -- --

20 FV

2300.D.002 With actuator and positioner (want to be able to see the position readout on the SCADA) 0Stripper Overhead Receiver Aqueous Level Control Valve 100 1.024 62.1 18.02 0.682 75

2300-LCV-003 Light End Material - water (liquid) 0 0 0.2 0.0005

20 FV

2300.D.002 Turbine meter

0Stripper Reflux Flow 100 1.605 47.62 224.5 2.398 75

2300-FIT-005 Light End Material - Propane - Pentane (liquid) 0 50 400 2.12

20 FV

2300.D.002 With actuator and positioner (want to be able to see the position readout on the SCADA) 0Stripper Reflux Flow Control Valve 100 1.605 47.62 224.5 2.398 75

2300-FCV-005 Light End Material - Propane - Pentane (liquid) 0 50 400 2.12

20 FV

2300.D.002 Something similar to Ashcroft pressure gauge

0Stripper Overhead Pump Outlet Pressure 100 1.605 47.62 224.5 2.398 50

2300-PG-007 Light End Material - Propane - Pentane (liquid) -- -- -- --

LegalDisclaimer Version 2 4/7/2004

AZ Equipment List Piping System.xls

20 FV

2300.D.002 Something similar to Ashcroft pressure gauge

0Stripper Overhead Aqueous Pump Outlet Pressure 100 1.024 62.1 18.02 0.682 50

2300-PG-006 Light End Material - water (liquid) -- -- -- --

LegalDisclaimer Version 2 4/7/2004

AZ Equipment List Piping System.xls

25 FV

2300.D.001 Thermocouple (Type K)

0Stripper Column Internal Temperature 300 1.102 0.9 59 0.0095 75 2300-TE-002 Reactor Effluent (mixed)

25 FV

2300.D.001 Thermocouple (Type K)

0Stripper Column Internal Temperature 150 1.147 0.245 39.11 0.0095 75 2300-TE-001 Reactor Effluent (mixed)

2300.D.001 Clamshell control 0Stripper Column Sump Clamshell Heater Zone 2 Temperature Controller

2300-TC-002 Not seeing process (on reactor) -- -- -- --

2300.D.001 Clamshell control 0Stripper Column Sump Clamshell Heater Zone 1 Temperature Controller

2300-TC-001 Not seeing process (on reactor) -- -- -- --

25 FV

2300.D.001 Differential pressure transducer

0Stripper Column delta pressure 100 - 700 0.214 - 31.80

39.11 - 251.7

0.0077 -

0.154 75

2300-dPT-001 Reactor Effluent (mixed)

25 FV

2300.D.001 Thermocouple (Type K)

0Stripper Column Sump Outlet Temperature 682 1.026 0.8994 239.9 0.007725 75 2300-TE-006 Reactor Effluent (mixed)

5 FV

2300.D.001 Pressure transducer

0Stripper Bottoms Battery Limit Pressure 100 1.233 31.8 251.7 0.154 90

2300-PI-004 Stabilized SAF (liquid)

5 FV

2300.D.001 Thermocouple (Type K)

0Stripper Bottoms Battery Limit Temperature 100 1.233 31.8 251.7 0.154 90

2300-TE-008 Stabilized SAF (liquid)

40 FV

2300.D.001 With actuator and positioner (want to be able to see the position readout on the SCADA) 0Stripper Bottoms Level Control Valve 681 1.226 31.8 251.7 0.154 90

2300-LCV-001 Stabilized SAF (liquid)

125 277 400 1.01

40 FV

2300.D.001 dP level instrument

0Stripper Bottoms Level 681 1.226 31.8 251.7 0.154 90

2300-LIT-001 Stabilized SAF (liquid)

40 FV

2300.D.001 Something similar to Ashcroft pressure gauge

0Stripper Bottoms Air Cooler Inlet Pressure 650 1.006 31.8 251.7 0.154 90

2300-PG-008 Stabilized SAF (liquid)

40 FV

2300.D.001 Coriolis meter

0Stripper Bottoms Flow 681 1.226 31.8 251.7 0.154 90

2300-FIT-001 Stabilized SAF (liquid)

125 277 400 1.01

40 FV

2300.D.001 Something similar to Ashcroft pressure gauge

0Stripper Bottoms Pump Discharge Pressure 681 1.596 31.8 251.7 0.154 90

2300-PG-005 Stabilized SAF (liquid)

20 FV

2300.D.002 Thermocouple (Type K)

0Stripper Overhead Organic Battery Limit Temperature 100 1.596 28.17 41.8 0.078 75

2300-TE-013 Light End Material - Propane - Pentane (liquid) -- -- -- --

20 FV

2300.D.002 Coriolis meter

0Stripper Overhead Organic Product Flow 100 1.596 28.17 41.8 0.078 75

2300-FIT-004 Light End Material - Propane - Pentane (liquid) 100 250 400 2.1

FV

2300.D.002 Thermocouple (Type K)

0-- 100 1.025 62.1 18.02 0.682

2300-TE-012 Water (liquid)

-- -- --Stripper Overhead Aqueous Battery Limit Temperature

75 20

75 20

2300-FIT-003 Water (liquid)

0 0.1 0.2Stripper Overhead Aqueous Product Flow FV

2300.D.002 Coriolis meter

00.0005 100 1.025 62.1 18.02 0.682

Chk'd: Appr'd:

DESCRIPTION

Minimum Normal Maximum Temperature Cp/Cv Density M.W. Viscosity Normal Min

Flow Rate (lb/day)

Flow Rate (lb/day)

Flow Rate (lb/day)

Flow Rate (SCF/h or BBL/Day)

Operating Temperature (F)

Cp/Cv Density (lb/cu ft)

Molecular Weight

Dynamic viscosity

ITEM NUMBER

FLUID & STATE

MASS FLOWS VOLUMETRIC

FLOWRATE

FLUID CONDITIONS Pressure Remarks

Max psig psig psig P&ID Page

DocumentNumber

PRIMARY PIPING SYSTEMS Project No.: Hydroprocessing & Stripper Revision: 0 Date: LastIssueDate Client: National Renewable Energy Laboratory Page 2 3

INSTRUMENTATION LIST Project: IBRF Revitalization - Equipment Site: Integrated BioRefinery Faciltiy By:

DocumentNumber

PRIMARY PIPING SYSTEMS Project No.: Hydroprocessing & Stripper Revision: 0 Date: LastIssueDate Client: National Renewable Energy Laboratory Page 3 3

INSTRUMENTATION LIST Project: IBRF Revitalization - Equipment Site: Integrated BioRefinery Faciltiy By:

ITEM NUMBER

FLUID & STATE

MASS FLOWS VOLUMETRIC

FLOWRATE

FLUID CONDITIONS Pressure Remarks

Max psig psig psig P&ID Page

Chk'd: Appr'd:

DESCRIPTION

Minimum Normal Maximum Temperature Cp/Cv Density M.W. Viscosity Normal Min

Flow Rate (lb/day)

Flow Rate (lb/day)

Flow Rate (lb/day)

Flow Rate (SCF/h or BBL/Day)

Operating Temperature (F)

Cp/Cv Density (lb/cu ft)

Molecular Weight

Dynamic viscosity

FV

2300.D.001 Thermocouple (Type K)

0-- 500 1.025 20 150 0.01

2300-TE-004 Reactor Effluent (mixed)

-- -- --Stripper Column Internal Temperature

75 25

75 25

2300-TE-003 Reactor Effluent (mixed)

-- -- --Stripper Column Internal Temperature

FV

2300.D.001 Thermocouple (Type K)

0-- 682 1.012 25 200 0.1

25 FV

2300.D.001 Thermocouple (Type K)

0Stripper Column Sump Temperature 682 1.012 38.23 245.8 0.3075 75

2300-TE-005 Reactor Effluent (mixed)

25 FV

2300.D.001 Thermocouple (Type K)

0Stripper Bottoms Fin Fan Outlet Temperature 175 1.256 46.26 251.7 1.511 75

2300-TE-007 Reactor Effluent (liquid)

50 15

Standard Detail Drawing

Pressure gauge Cooling water supply pressure for 2300-E-001 75 1.0 62.27 18.09 0.913 70

2300-PG-008 Water (liquid)

500 2237 3500 11.25 gph

35 5

Standard Detail Drawing

Pressure gauge Cooling water return pressure for 2300-E-001 110 1.03 61.87 18.02 0.6139 55

2300-PG-009 Water (liquid)

500 2237 3500 11.25 gph

50 15

Standard Detail Drawing

Pressure gauge Cooling water supply pressure for 2300-E-003 75 1.0 62.27 18.09 0.913 70

2300-PG-010 Water (liquid)

100 310 500 1.56 gph

35 5

Standard Detail Drawing

Pressure gauge Cooling water return pressure for 2300-E-003 110 1.03 61.87 18.02 0.6139 55

2300-PG-011 Water (liquid)

100 310 500 1.56 gph

50 15

Standard Detail Drawing

Rotameter for cooling water flow monitoring Rotameter for 2300-E-001 cooling water flow 75 1.0 62.27 18.09 0.913 70

2300-FG-001 Water (liquid)

500 2237 3500 11.25 gph

50 15

Standard Detail Drawing

Rotameter for cooling water flow monitoring Rotameter for 2300-E-003 for cooling water flow 75 1.0 62.27 18.09 0.913 70

2300-FG-003 Water (liquid)

100 310 500 1.56 gph

LegalDisclaimer Version 2 4/7/2004

AZ Equipment List Piping System.xls

Area/Unit: of

1 Case: Governing Case: 0

2 Supplier: Applicable To: 0

3 Mfr.: Ref. P&ID: 0

4 Model No.: Serial No.: 0

5 0

7 Item Number 0

8 Service 0

9 Preliminary Line Size 0

10 Fluid Type 0

11 Fluid State 0

12 Normal Vapour Flow 0

13 Normal Liquid Flow 0

14 Maximum Flow 0

15 Minimum Flow 0

16 Molecular Weight 0

17 Specific Gravity @ Flow Conditions 0

18 Inlet Density 0

19 Liquid Vapour Pressure 0

20 Valve Type 0

21 Inlet Connection 0

22 Outlet Connection 0

23 Vapour Cp/Cv @ Flow Conditions 0

24 Normal Operating Temperature 0

25 Upstream Pressure at Normal Flow 0

26 Downstream Pressure at Normal Flow 0

27 Upstream Pressure at Maximum Flow 0

28 Downstream Pressure at Maximum Flow 0

29 Upstream Pressure at Minimum Flow 0

30 Downstream Pressure at Minimum Flow 0

31 Maximum Control Valve Pressure Drop 0

32 Sizing Coefficient, Normal 0

33 Sizing Coefficient, Maximum 0

34 Sizing Coefficient, Minimum 0

35 Tight Shut 0

36 Air Failure 0

37 Remarks

42 0

LegalDisclaimer Version 2 4/7/2004

AZ Equipment List Instruments.xls

Remarks:

Linear valve characteristics

Max Inlet Pressure - 150 psig Max Inlet Temp - 750 deg F

Remarks:

Linear valve characteristics

Max Inlet Pressure - 150 psig Max Inlet Temp - 300 deg F

Remarks:

Linear valve characteristics

Max Inlet Pressure - 150 psig Max Inlet Temp - 300 deg F

Remarks:

Linear valve characteristics

Max Inlet Pressure - 150 psig Max Inlet Temp - 300 deg F

Remarks:

Linear valve characteristics

Max Inlet Pressure - 150 psig Max Inlet Temp - 300 deg F

REMARKS

ANSI Class IV ANSI Class IV ANSI Class IV ANSI Class IV ANSI Class IV Fail Closed Fail Open Fail Closed Fail Closed Fail Open

0.0094 0.0084 0.00048 0.016 0.0018

0.0015 0.0019 0.00012 0.0018 0.0002

Cv 0.0037 0.0039 0.00026 0.0047 0.00052 psi 40 17 17 15 15 psig 10 3 3 5 5 psig 50 20 20 20 20 psig 20 10 10 5 5 psig 35 20 20 20 20 psig 15 5 5 5 5 psig 40 20 20 20 20

0.0039 deg F 682 100 100 100

CL 300 NPT CL 150 NPT CL 150 NPT CL 150 NPT CL 150 NPT

CL 300 NPT CL 150 NPT CL 150 NPT CL 150 NPT CL 150 NPT

Globe Globe Ball Globe Globe psia 27 0.95 20 20 lb/ft3 32 0.215 62.7 31.5 31.5

251.70 39.11 18.02 41.8 41.80

0.51 0.99 0.5 0.5 lb/hr 2.657 0.162 0.25 3.2 0.358 lb/hr 0.713 lb/hr lb/hr 10.61 0.637 0.75 12.5 1.416 Flow Rate (kgInlet / Outlet 5.3 lb/hr 0.5 lb/hr 6.5 lb/hr

Liquid Gaseous Liquid Liquid Liquid

Flow Rate (kgInlet / Outlet 0.32

0.25 inches

Kerosene/Jet Fuel Offgas Water Naphtha Hydrocarbon Naptha Hydrocarbon

Heavy Product Overhead Product Overhead Aqu. Prod Overhead Liq Prod Reflux

0.25 inches 0.25 inches 0.25 inches 0.25 inches

OPERATING CONDITIONS

2300-LCV-001 2300-PCV-002 2300-LCV-003 2300-LCV-004 2300-FCV-005

Site: South Table Mountain - IBRF

Service: Please see each valve's service No. Req.: 1 of ea

Client: National Renewable Energy Laboratory

Project: Distillation Column Manufacturer

Appr'd:

Type: Design Design

INSTRUMENT PROCESS SAP No.: Inquiry No.:

SPECIFICATION By: Chk'd:

8/28/2025

Distillation Column - IBRF Page 1 1

Proc. No.: P.O. No.:

Item No.: 2300-LCV-001/003/004; 2300-PCV-002; 2300-FCV-005 Project No.: Revision: 0 Date:

6 Fluid 7 Corrosive 8 Sour Service 9 Flow Min Norm. Max. Units

10 Pressure Min Norm. Max. Units 11 Temperature Min Norm. Max. Units 12 Design Pressure 13 Design Temperature 19 Size 20 To 25 Trace Size 32 Min Max. Units 37 Area Classification 48 Client Reference Item

Date No. Revision Approver 7/21/2024 0 Original

Serial Number Weight

Dwg No:

Material Code Notes:

Engineer INSTRUMENT SPECIFICATION Flow Meter

Sheet:

Would like a local readout Power Supply Consumption 24 V DC

Purchase

Manufacturer Model

Requisition No

Accessories

Measuring Cable Length Special Cable Length Mounting Kit Cable Glands

Electrical Connections Prefer 24V DC power Output Signal Load 4-20 mATransmitter

Location Mounting Field Mounted or Integral (either is acceptable) Calibration Range To

Surge Protection Device Electrical Protection Class Protocol HART preferred, but not wireless

Other Output Signal

Meter Materials Process Connections Conection Material Swagelok 316 SS Measuring Element

Meter

Meter Type Coriolis Rating Facing 1/4"

Tracing Winterization is not necessary Rating Facing

450 lb/day Housing Stainless steel or Aluminum Electrical Connections Prefer 24V DC power Accuracy Manufacturer standard

Instrument Range 0

Conductivity 0.04387 BTU/hr-ft-deg F

Density @ normal Viscosity @ normal 31.8 lb/cu ft 0.154 cP Molecular Weight cp/cv 251.7 1.01

FV 40 90 psig 250 681 750 deg F

Line dP Meter dP Allowed 1 psi / 100 ft 3 psi

No No 125 277 400 lb/day

Operating Conditions

Phase State Aviation Fuel (Hydrocarbon) Liquid Abrasive No No

Special Conditions

Min. Max. FV 150 psig Min. Max. 32 deg F 825 deg F

PS14

Line Size Line Internal Diameter 1/4" Type of Flow Meter Coriolis

General Data

Tag Number P&ID No. 2300-FIT-001 2300.D.001 Service Stripper Bottoms Product Line No. Piping Class 1/4"-PF-001106-PS14

6 Fluid 7 Corrosive 8 Sour Service 9 Flow Min Norm. Max. Units

10 Pressure Min Norm. Max. Units 11 Temperature Min Norm. Max. Units 12 Design Pressure 13 Design Temperature 19 Size 20 To 25 Trace Size 32 Min Max. Units 37 Area Classification 48 Client Reference Item

Date No. Revision Approver 7/21/2024 0 Original

Serial Number Weight

Dwg No:

Material Code Notes:

Engineer INSTRUMENT SPECIFICATION Flow Meter

Sheet:

Would like a local readout Power Supply Consumption 24 V DC

Purchase

Manufacturer Model

Requisition No

Accessories

Measuring Cable Length Special Cable Length Mounting Kit Cable Glands

Electrical Connections Prefer 24V DC power Output Signal Load 4-20 mATransmitter

Location Mounting Field Mounted or Integral (either is acceptable) Calibration Range To

Surge Protection Device Electrical Protection Class Protocol HART preferred, but not wireless

Other Output Signal

Meter Materials Process Connections Conection Material Swagelok 316 SS Measuring Element

Meter

Meter Type Coriolis Rating Facing 1/4"

Tracing Winterization is not necessary Rating Facing

75 lb/day Housing Stainless steel or Aluminum Electrical Connections Prefer 24V DC power Accuracy Manufacturer standard

Instrument Range 0

Conductivity 0.01373 BTU/hr-ft-deg F

Density @ normal Viscosity @ normal 0.214 lb/cu ft 0.0094 cP Molecular Weight cp/cv 39.11 1.147

FV 20 75 psig 45 100 250 deg F

Line dP Meter dP Allowed 1 psi / 100 ft 3 psi

Yes No 5 16.88 65 lb/day

Operating Conditions

Phase State Light End Hydrocarbon Gaseous Abrasive Yes No

Special Conditions

Min. Max. FV 150 psig Min. Max. 32 deg F 300 deg F

PS14

Line Size Line Internal Diameter 1/4" Type of Flow Meter Coriolis

General Data

Tag Number P&ID No. 2300-FIT-002 2300.D.002 Service Stripper Overhead Vapor Product Flow Line No. Piping Class 1/4"-PV-002101-PS14

6 Fluid 7 Corrosive 8 Sour Service 9 Flow Min Norm. Max. Units

10 Pressure Min Norm. Max. Units 11 Temperature Min Norm. Max. Units 12 Design Pressure 13 Design Temperature 19 Size 20 To 25 Trace Size 32 Min Max. Units 37 Area Classification 48 Client Reference Item

Date No. Revision Approver 7/21/2024 0 Original

Serial Number Weight

Dwg No:

Material Code Notes:

Engineer INSTRUMENT SPECIFICATION Flow Meter

Sheet:

Would like a local readout Power Supply Consumption 24 V DC

Purchase

Manufacturer Model

Requisition No

Accessories

Measuring Cable Length Special Cable Length Mounting Kit Cable Glands

Electrical Connections Prefer 24V DC power Output Signal Load 4-20 mATransmitter

Location Mounting Field Mounted or Integral (either is acceptable) Calibration Range To

Surge Protection Device Electrical Protection Class Protocol HART preferred, but not wireless

Other Output Signal

Meter Materials Process Connections Conection Material 316 SS Measuring Element

Meter

Meter Type Coriolis Rating Facing 1/4"

Tracing Winterization is not necessary Rating Facing

1 lb/day Housing Stainless steel or Aluminum Electrical Connections Prefer 24V DC power Accuracy Manufacturer standard

Instrument Range 0

Conductivity 0.3623 BTU/hr-ft-deg F

Density @ normal Viscosity @ normal 62.1 lb/cu ft 0.682 cP Molecular Weight cp/cv 18.02 1.024

FV 20 75 psig 32 100 300 deg F

Line dP Meter dP Allowed 1 psi / 100 ft 3 psi

Yes No 0 0.1 0.2 lb/day

Operating Conditions

Phase State Sour Water Liquid Abrasive Yes No

Special Conditions

Min. Max. FV 150 psig Min. Max. 32 deg F 300 deg F

PS14

Line Size Line Internal Diameter 1/4" Type of Flow Meter Coriolis

General Data

Tag Number P&ID No. 2300-FIT-003 2300.D.002 Service Stripper Overhead Aqueous Phase Product Line No. Piping Class 1/4"-PD-002107-PS14

6 Fluid 7 Corrosive 8 Sour Service 9 Flow Min Norm. Max. Units

10 Pressure Min Norm. Max. Units 11 Temperature Min Norm. Max. Units 12 Design Pressure 13 Design Temperature 19 Size 20 To 25 Trace Size 32 Min Max. Units 37 Area Classification 48 Client Reference Item

Date No. Revision Approver 7/21/2024 0 Original

Serial Number Weight

Dwg No:

Material Code Notes:

Engineer INSTRUMENT SPECIFICATION Flow Meter

Sheet:

Would like a local readout Power Supply Consumption 24 V DC

Purchase

Manufacturer Model

Requisition No

Accessories

Measuring Cable Length Special Cable Length Mounting Kit Cable Glands

Electrical Connections Prefer 24V DC power Output Signal Load 4-20 mATransmitter

Location Mounting Field Mounted or Integral (either is acceptable) Calibration Range To

Surge Protection Device Electrical Protection Class Protocol HART preferred, but not wireless

Other Output Signal

Meter Materials Process Connections Conection Material Swagelok 316 SS Measuring Element

Meter

Meter Type Coriolis Rating Facing 1/4"

Tracing Winterization is not necessary Rating Facing

225 lb/day Housing Stainless steel or Aluminum Electrical Connections Prefer 24V DC power Accuracy Manufacturer standard

Instrument Range 0

Conductivity 0.04963 BTU/hr-ft-deg F

Density @ normal Viscosity @ normal 28.17 lb/cu ft 0.078 cP Molecular Weight cp/cv 41.8 1.605

FV 20 75 psig 32 100 300 deg F

Line dP Meter dP Allowed 1 psi / 100 ft 3 psi

Yes No 100 250 200 lb/day

Operating Conditions

Phase State Naphtha Liquid Abrasive No No

Special Conditions

Min. Max. FV 150 psig Min. Max. 32 deg F 300 deg F

PS14

Line Size Line Internal Diameter 1/4" Type of Flow Meter Coriolis

General Data

Tag Number P&ID No. 2300-FIT-004 2300.D.002 Service Stripper Overhead Organic Product (Naphtha Range) Line No. Piping Class 1/4"-PF-002111-PS14

6 Fluid 7 Corrosive 8 Sour Service 9 Flow Min Norm. Max. Units

10 Pressure Min Norm. Max. Units 11 Temperature Min Norm. Max. Units 12 Design Pressure 13 Design Temperature 19 Size 20 To 25 Trace Size 32 Min Max. Units 37 Area Classification 48 Client Reference Item

Date No. Revision Approver 7/21/2024 0 Original

Serial Number Weight

Dwg No:

Material Code Notes:

Engineer INSTRUMENT SPECIFICATION Flow Meter

Sheet:

Would like a local readout Power Supply Consumption 24 V DC

Purchase

Manufacturer Model

Requisition No

Accessories

Measuring Cable Length Special Cable Length Mounting Kit Cable Glands

Electrical Connections Prefer 24V DC power Output Signal Load 4-20 mATransmitter

Location Mounting Field Mounted or Integral (either is acceptable) Calibration Range To

Surge Protection Device Electrical Protection Class Protocol HART preferred, but not wireless

Other Output Signal

Meter Materials Process Connections Conection Material Swagelok 316 SS Measuring Element

Meter

Meter Type Turbine Rating Facing 3/8"

Tracing Winterization is not necessary Rating Facing

450 lb/day Housing Stainless steel or Aluminum Electrical Connections Prefer 24V DC power Accuracy Manufacturer standard

Instrument Range 0

Conductivity 0.04963 BTU/hr-ft-deg F

Density @ normal Viscosity @ normal 47.62 lb/cu ft 2.398 cP Molecular Weight cp/cv 224.5 1.605

FV 20 75 psig 32 100 175 deg F

Line dP Meter dP Allowed 1 psi / 100 ft 2 psi

Yes No 0 50 400 lb/day

Operating Conditions

Phase State Naphtha (hydrocarbon) Liquid Abrasive No No

Special Conditions

Min. Max. FV 150 psig Min. Max. 32 deg F 300 deg F

PS14

Line Size Line Internal Diameter 3/8" Type of Flow Meter Turbine

General Data

Tag Number P&ID No. 2300-FIT-005 2300.D.002 Service Stripper Overhead Reflux Flow Line No. Piping Class 3/8"-PF-002114-PS14

6 Fluid 7 Corrosive 8 Sour Service 9 Flow Min Norm. Max. Units

10 Pressure Min Norm. Max. Units 11 Temperature Min Norm. Max. Units 12 Design Pressure 13 Design Temperature 14 Density @ Min T Norm T Max T Units lb/cu ft 25 Rating 32 Min Max. Units 37 Area Classification 48 Client Reference Item

Date No. Revision Approver 8/21/2025 A

Engineer INSTRUMENT SPECIFICATION Level Transmitter

Sheet:

Dwg No:

Weight Material Code

Notes:

Purchase

Manufacturer Model

Requisition No Serial Number

Accessories

Measuring Cable Length 12m Special Cable Length Mounting Kit

Power Supply Consumption 24VDC from panel 2.4W max Surge Protection Device n/a (spec. to explosion-proof) 250 mA fast-acting fuse in panel n/a Cable Glands 1/2" NPT cable gland

Electrical Protection Class Cl. I, Div. 2 Group B (not necessary if this adds 10x the cost) Protocol HART

Electrical Connections 2- or 3-wire (Power, signal, common) Output Signal 4-20[ mA Other Output Signal n/a

1/2" NPT

Housing

Location Mounting Field Mounted or Integral (either is acceptable) Calibration Range 0 To 60 in H2O

Air Pressure n/a

Connections Process Connection Type Connection Material Remote-sealed flanges SST Measuring Element Hydraulic membrane Connection Size

NEMA 4X/IP69 24VDC 100 mA

SS316

Differential in Inches 12 No of…