2025-07-25 Mennen Sports Center_Compressor Replacement_Project Manual_ 071425.pdf
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- Attached to
- Replacement of Screw Compressors for Chiller Package #1 and #2 State and local contract opportunity
- Solicitation number
- 85-25
- Issued by
- Morris County, New Jersey
About this file
This project manual, prepared by B32 Engineering Group, Inc., details refrigeration system improvements for the Mennen Sports Arena in Morristown, New Jersey. The project involves replacing two existing FES GEA Model 195 GME screw compressors with two owner-furnished GEA 195GMXE screw compressors in the facility's two chiller packages. The comprehensive scope of work includes removing and salvaging the existing compressors, installing new compressors, removing and replacing the entire refrigerant oil charge (estimated at 75 gallons per compressor), replacing liquid line refrigerant filter driers, performing pressure and vacuum testing, and conducting laser alignment of each compressor and motor. The project is scheduled for implementation in July 2025, with specific requirements for contractor qualifications, including successful installation of at least two industrial-grade refrigeration systems within the past five years.
The project manual specifies detailed technical requirements, including compliance with various state and national codes such as ASHRAE/ANSI 15 Safety Code for Mechanical Refrigeration, ASME B31.5 Refrigeration Pressure Piping Code, and relevant state building, electrical, and mechanical codes. The contractor must follow strict guidelines for refrigerant handling, adhering to Section 608 of the Clean Air Act of 1990, and must provide documentation of refrigerant recovery, including technician certifications and equipment verifications. The project also requires the contractor to maintain one chiller package operational at all times during the improvements, with a one-year warranty on materials and labor. The owner will separately handle the removal of existing GEA Mico control panels and installation of new GEA Omni control panels, with a GEA representative providing direct supervision during the compressor installation and startup.
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| File | Type | Posted |
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| 2025-07-25 RFB 95-25_Replacement of Screw Compressors at MSA_Bid Document.pdf | ||
| 2025-07-25 NJ Prevailing Wage rate Determination-morris-7-8-25.pdf | ||
| 2025-07-25 RFB 95-25_ Replacement of Screw Compressors at MSA_Advertisement.pdf |
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Mennen Sports Arena
Refrigeration System Improvements
Morristown, NJ
PROJECT MANUAL
July 14, 2025
B32 Project No. 900-25-601
B32 Engineering Group, Inc.
2211 O’Neil Road Hudson, Wisconsin 54016 www.b32eng.com
Ph: (651) 256-3090 Fax: (715) 808-0842 http://www.b32eng.com/
Mennen Sports Center Refrigeration General Requirements Project No. 900-25-601, © 2025 B32 Engineering Group, Inc. All Rights Reserved 13 1811-1
SECTION 13 18 11
REFRIGERATION GENERAL REQUIREMENTS
PART 1 - GENERAL
1.01 SECTION INCLUDES
A. Quality assurance - prequalification criteria.
B. General project description
C. Submittal and project closeout requirements.
D. Electrical requirements.
E. Demolition work.
1.02 QUALITY ASSURANCE
A. Contractors wishing to bid/quote on this project must submit, with their bid, the following prequalification criteria.
To demonstrate the qualifications to perform the Work, the Refrigeration Contractor shall submit the information requested below with their Bid. Refrigeration Contractor is defined as the contractor responsible for completing all Division 13 work. Subcontractors performing the work identified below shall also meet the qualifications. Qualification document submitted by the low bidder will be evaluated after the bid opening to determine if the Refrigeration Contractor meets these qualifications.
1. As evidence and assurance of the contractor’s ability to perform the work and support the Owner’s system with service, the contractor installing the new screw compressors must have successfully installed new industrial grade refrigeration systems and/or replaced industrial grade screw compressors (100 Tons or greater) on a minimum of two (2) industrial grade refrigeration systems within the past five (5) years.
Submit information on each project. Submittal shall be on company letterhead, signed by an authorized representative of the company and include project description, portion of project completed by the company, location, construction cost, owner's name, owner's representative, phone number and completion date of work.
B. Contractors wishing to bid on this project shall perform an on-site investigation prior to submitting a bid for the project. Contractor shall field verify all equipment and materials that will be affected by the work of this project and report any concerns to the Engineer at least ten
(10) business days prior to the bid opening date.
1.03 PROJECT SCHEDULE / PHASING:
A. See Division 0 and Division 1 documents for project schedule and phasing.
B. Improvements to the two chiller packages will occur at different times. One chiller package must remain operational at all times.
1.04 GENERAL PROJECT DESCRIPTION
A. The following is a general description of the project and may not include all materials and labor required or covered elsewhere in the contract documents.
a. Remove, store and reinstall existing R22 refrigerant as necessary for work to be completed.
Project No. 900-25-601, © 2025 B32 Engineering Group, Inc. All Rights Reserved 13 1811-2
b. Remove, dispose and replace the entire charge of refrigerant oil (estimated oil charge per compressor = 75 gallons). Furnish and install all oil and coalescer filters.
c. Remove and replace liquid line refrigerant filter driers on each package. (8 total).
Model #: Copeland / Emerson H100 or equal.
d. Remove and salvage (2) two existing FES GEA Model 195 GME screw compressors and turn over to owner. Disconnect all piping, valves, electrical, controls, etc. as necessary.
e. Install (2) two owner furnished barre GEA 195GMXE screw compressors.
Reconnect all piping, valves, electrical, etc. as necessary.
f. Perform pressure and vacuum testing each package.
g. Perform laser alignment of each compressor and motor.
h. Furnish and install (1) one pipe hanger on suction pipe of compressor #2.
B. The following is a general description of the work being performed by the owner or by the compressor manufacturer directly via a separate contract.
a. Removal of the existing GEA Mico control panels.
b. Installation and startup of the new GEA Omni control panels.
c. A representative from GEA will be on site to provide direct supervision and consultation overseeing the installation and startup of the new compressors.
1.05 RELATED SECTIONS
A. Division 0, Division 1, General and Supplementary Conditions.
B. Section 131812 - Refrigeration System Improvements.
C. APPENDIX A – Existing Compressor Package Information
D. APPENDIX B – New Compressor Information
E. APPENDIX C– Compressor Retrofit Instructions/Information
1.06 REFERENCES
A. ASHRAE/ANSI - 15 Safety Code for Mechanical Refrigeration.
B. ASME B31.5 - Refrigeration Pressure Piping Code.
C. International/State Fire Code.
D. International/State Building Code.
E. International/State Mechanical Code.
1.07 CODES AND STANDARDS
A. All parts of the project shall be performed in accordance with the most recent version of the following codes and standards and all amendments:
1. State Building Codes.
2. State Electrical Codes.
3. State Mechanical Codes.
4. National Fire Protection Association Codes.
5. ANSI/ASHRAE 15 -Safety Code for Mechanical Refrigeration.
Project No. 900-25-601, © 2025 B32 Engineering Group, Inc. All Rights Reserved 13 1811-3
6. ASHRAE 34-Number Designations and Safety Classification of Refrigerants .
7. OSHA.
8. American Standard Code for Pressure Piping ASA B31.1.
9. American Standard Code for Refrigeration Piping ASA B31.
10. American Standard Code for Pressure Vessels.
1.08 SUBMITTALS
A. See General Conditions, Division 0 and additional requirements below.
A. Shopdrawings and Submittals:
1. The Contractor’s approval stamp is required on all submittals and indicates that the Contractor has reviewed all materials and has a completed understanding of the specifications and requirements. Contractor shall clearly mark all deviations from the contract documents on all submittals.
2. Shop Drawings. All submittals shall conform to the requirements the General Conditions and these specifications.
3. Submit each item/material/equipment in a separate submittal and clearly labeled as follows using specification section, article and title.
a. For example: Rink Piping, Title: Polyethylene Rink Pipe, Submittal No.
131813.2.05.001
B. Progress Schedule. Submit progress schedule before project begins.
C. Test Reports. Submit one (1) electronic copy of test reports to the Engineer when specified.
D. Certifications. Submit one (1) electronic copy of certifications to the Engineer when specified.
1.09 WARRANTY/GUARANTY
A. In addition to the standard manufacturer's warranty on all equipment and materials, the contractor shall provide a standard one-year materials and labor warranty on all work performed for this project.
B. Warranty of the new compressors will be owned by the owner.
1.10 PRODUCT DELIVERY, STORAGE AND HANDLING REQUIREMENTS
A. Transport, handle, store and protect products in accordance with manufacturer's recommendations. Secure products at all times.
B. Store products with seals and labels intact and legible.
C. Store products in a secure environment at all times.
D. Provide adequate labor to handle products and prevent damage.
E. All damaged materials and equipment will be rejected.
PART 2 - PRODUCTS
2.01 ELECTRICAL
A. See requirements in Section 131812 - Refrigeration System Improvements
Project No. 900-25-601, © 2025 B32 Engineering Group, Inc. All Rights Reserved 13 1811-4
PART 3 - EXECUTION
3.01 CONSTRUCTION UTILITIES AND FACILITIES
A. Unless specified elsewhere, all temporary utilities and facilities required to complete the project shall be the responsibility of the contractor and costs for these utilities and facilities shall be incidental to the project costs.
3.02 NOTIFICATIONS OF WORK
A. The Contractor shall notify the Engineer, a minimum of seven (7) business days, prior to the following phases of the work:
1. Start of demolition.
2. Start and completion of all pressure tests.
3. Start up of Refrigeration Package
3.03 INSPECTIONS
A. See Section 1.04 of this specification for requirements regarding re-inspection of uncompleted or unsatisfactory work.
3.04 DEMOLITION
A. The Contractor is responsible for all demolition and disposal of the items associated with the scope of work (and all related piping, valves, supports, electrical, control systems).
B. The following items shall be salvaged and turned over to the owner.
1. (2) Two existing FES GEA Model 195 GME screw compressors.
C. Drain fluids from all systems as necessary prior to starting demolition.
1. Primary refrigerant (R-22).
a. Contractor shall pump down and store existing R-22 refrigerant to each chiller’s receiver as much as possible. Any remaining refrigerant shall be removed, stored and reinstalled.
b. The reclamation and recovery of all refrigerants must meet the requirements outlined in Section 608 of the Clean Air Act of 1990. Contractors who recover systems containing refrigerant are required to carry a Pollution Liability Insurance Policy. The following project documentation is required. Copies of the documentation shall be submitted to the Owner.
1) Approved reclamation contractors include Rapid Recovery (952.297.2011), Hudson Technologies (845.512.6012), or equal.
2) Recovery technicians EPA certification
3) Recovery equipment certification
4) Date of service
5) Location of service (site name & address)
6) Make, model and serial number of systems
7) Type and quantity of refrigerant
8) Comments or concerns about condition of existing system or parts of systems.
9) Signed certificate of abatement certifying the following:
10) An EPA certified technician was used to perform the service and complete EPA documentation as required by the EPA - Clean Air Act.
11) EPA Certified and ARI Certified equipment was used to recover the refrigerant.
Project No. 900-25-601, © 2025 B32 Engineering Group, Inc. All Rights Reserved 13 1811-5
12) The systems were recovered to EPA required levels.
13) Recovered refrigerants were transported to an EPA certified reclamation facility.
D. Disconnect all electrical systems prior to starting demolition. Coordinate utility service outages with the Owner, Engineer and utility company since the main facility may still be in use.
Provide temporary wiring and connections to maintain existing systems in service during construction. When work must be performed on energized equipment or circuits use personnel experienced in such operations. In particular, all security and safety systems must be maintained in operation at all times as required by the Owner and local officials. This includes security and safety lighting.
E. All mechanical equipment, piping, valves, electrical systems and other items related to the refrigeration or ice system resulting from required demolition shall be removed and disposed of off-site by the unless specifically designated to be salvaged.
F. All disposals shall occur off-site and shall be performed in accordance with applicable authorities having jurisdiction.
G. PROTECTION: The Contractor shall be responsible for covering all electrical systems, control systems, sensitive equipment, scoreboards, bleacher system, doorways, HVAC intakes, and other areas adjacent to areas where demolition will take place with polyethylene sheeting prior to the start of demolition.
H. VENTILATION: The Contractor shall be responsible for providing proper ventilation in the arena during construction of the project and to prevent unwanted vapors or odors from reaching other parts of the facility.
3.05 CLEANING, PAINTING AND RESTORATION
A. Contractor shall be responsible for cleaning the immediate construction area where work or demolition is conducted and the mechanical rooms where work is being performed.
B. Clean all equipment and piping to original condition after project has been completed.
C. Touch up all equipment paint, using paint provided by the manufacturer, after the installation is complete.
D. All piping, valves, and other items related to the ice system resulting from required demolition shall be removed and disposed of off-site by the contractor unless specifically designated to be salvaged.
3.06 COORDINATION OF WORK
A. The contractor shall be responsible for coordinating all work in Division 13 – Refrigeration. The contractor shall also work closely with the owner and other subcontractors on the project and help coordinate all associated work.
3.07 PERMITS
A. The contractor shall apply for and obtain all permits required to construct the project at no additional cost to the Owner unless specified otherwise.
END OF SECTION
Mennen Sports Center Refrigeration System Improvements Project No. 900-25-601, © 2025 B32 Engineering Group, Inc. All Rights Reserved 13 18 12-1
SECTION 13 18 12
REFRIGERATION SYSTEM IMPROVEMENTS
PART 1 - GENERAL
1.01 SECTION INCLUDES
1. General system description, design criteria and control criteria.
1.02 RELATED SECTIONS
1. Division 0, Division 1, General and Supplementary Conditions.
2. Section 131811 - Refrigeration General Requirements.
3. APPENDIX A – Existing Compressor Package Information
4. APPENDIX B – New Compressor Information
5. APPENDIX C– Compressor Retrofit Instructions/Information
1.03 SUBMITTALS
1. Shop Drawings. All submittals shall conform to the requirements of the General Conditions and these specifications.
1.04 WARRANTY/GUARANTY
1. As required in Section 131811 - Refrigeration General Requirements and as follows:
1. The contractor shall warranty workmanship performed as part of this project for 1 year.
2. Warranty of the new compressors will be owned by the owner.
1.05 PRODUCT DELIVERY, STORAGE AND HANDLING REQUIREMENTS
1. As required in Section 131811 - Refrigeration General Requirements.
PART 2 - PRODUCTS
2.01 BARE SCREW COMPRESSOR REPLACEMENT / RETROFIT
A. General Description of Work:
1. In general, the scope of work involves providing all labor and materials necessary to replace the bare screw compressors on two existing screw compressor packages including but not limited to:
a. Remove, store and reinstall existing R22 refrigerant as necessary for work to be completed.
b. Remove, dispose and replace the entire charge of refrigerant oil (estimated oil charge per compressor = 75 gallons). Furnish and install all oil and coalescer filters.
c. Remove and replace liquid line refrigerant filter driers on each package. (8 total).
Model #: Copeland / Emerson H100 or equal.
Project No. 900-25-601, © 2025 B32 Engineering Group, Inc. All Rights Reserved 13 18 12-2
d. Remove and salvage (2) two existing FES GEA Model 195 GME screw compressors and turn over to owner. Disconnect all piping, valves, electrical, controls, etc. as necessary.
e. Install (2) two owner furnished barre GEA 195GMXE screw compressors.
Reconnect all piping, valves, electrical, etc. as necessary.
f. Perform pressure and vacuum testing each package.
g. Perform laser alignment of each compressor and motor.
h. Furnish and install (1) pipe hanger on suction pipe of compressor #2.
2. The following is a general description of the work being performed by the owner or by the compressor manufacturer directly via a separate contract.
a. Removal of the existing GEA Mico control panels.
b. Installation and startup of the new GEA Omni control panels.
c. A representative from GEA will be on site to provide direct supervision and consultation overseeing the installation and startup of the new compressors.
B. Existing Compressor Information:
Model No. GEA 195GME
Design Conditions: 163 Tons @ 5F SST and 105F Condensing
VI: Fixed VI
Refrigerant: R-22
Type of Cooling: Liquid Injection
Application: High Stage
Economizer: DX
Motor: 300 HP TEFC Standard Efficiency
See “Appendix A” for additional information on existing compressors.
C. Replacement Compressor Information: (Furnished by owner)
Model No. GEA 195GMX
Design Conditions: 163 Tons @ 5F SST and 105F Condensing
VI: Fixed VI
Refrigerant: R-22
Type of Cooling: Liquid Injection
Application: High Stage
Economizer: DX
Motor: Existing
See “Appendix B” for additional information on replacement compressors.
D. Retrofit Instructions:
1. See “Appendix C” for replacement and retrofit provided by compressor manufacture.
E. Startup / Commissioning Requirements:
Project No. 900-25-601, © 2025 B32 Engineering Group, Inc. All Rights Reserved 13 18 12-3
1. The refrigeration system shall not be started until all local and state governing authorities have inspected and provided written approval for all systems related to, and including the refrigeration, piping, controls, ventilation, ice equipment room and building and all other related systems; and all alarms and controls have been thoroughly tested for all conditions and modes of operations.
2. Provide documentation of all piping pressures tests and vacuum tests on systems. All tests shall be witnessed by Owner or Owner’s representatives.
3. Provide professional motor laser alignment service on each compressor/motor. Provide report showing as-found and as-left results.
4. Provide a technician for a minimum of eight (8) hours to completely check the operation of the refrigeration system and equipment and all associated systems and equipment during start up. Provide documentation and certification from trained technician with completed, detailed, check list.
5. After the system has been fully inspected and tested and charged with refrigerant, the contractor shall assist the owner and GEA controls contractor start-up services for the chiller package.
F. Follow-Up Service: The Contractor shall provide the following follow-up services, at minimum.
The cost of these services shall be incidental.
1. Clean suction strainers/filters per manufacturer’s recommendations.
2. Replace oil filters 200 hours after start-up or per manufacturer's recommendations, whichever is sooner.
3. Provide an oil analysis 500 hours after initial start-up or per manufacturer's recommendations, whichever is sooner.
2.02 TESTING OF PIPING SYSTEMS
1. All testing shall be witnessed by the Owner Representative. Provide advanced notification to the Owner and Engineer as specified in Section 131811 - Refrigeration General Requirements.
2. All piping shall be tested prior to insulating. Isolate all equipment and any other devices that may be damaged by the pressure test. Testing procedures shall meet all code requirements.
3. Testing Requirements:
1. Steel Refrigerant Pipe (Primary refrigerant system):
a. Pressure Test: All refrigeration piping systems shall be pressure tested at the pressures stated in the table below with nitrogen gas for 24 hours with no pressure drop. The pressure shall then be lowered to 200 psig and maintained until system is ready to be charged. The test shall not begin until the Contractor is confident all water and contaminants are removed from the system. The Owner or Owner’s representative shall witness the test.
Refrigerant Pressure (psig)
R-22 Verify with Manuf.
b. Vacuum Dehydration: After the piping has been tested, a vacuum pump of adequate size shall be connected to the associated piping and allowed or run continuously until a vacuum reading of at least 500 microns (29.882 in. vacuum) or lower is obtained. This test must be maintained with the pump valved off for at least thirty (30) minutes. Provide an absolute pressure gauge for monitoring and use per the manufacturer’s recommendations. The Engineer shall witness the test.
Project No. 900-25-601, © 2025 B32 Engineering Group, Inc. All Rights Reserved 13 18 12-4
2. Gauges used for pressure tests must be designed for pressures greater than the test pressure. For example, a 100-psi gauge cannot be used for a 100-psi test. The scale on the gauge must be the next increment up from 100 psi.
2.03 CHARGING OF SYSTEMS
1. Primary Refrigerant Systems: After all pressure tests and vacuum dehydration testing has passed, the system shall then be fully charged with the existing R-22 refrigerant.
2.04 PIPE HANGERS AND SUPPORTS
1. Approved Manufacturers: Anvil International, Crane, Red Head, or equal.
2. Provide a complete pipe support system including hangers, supports, brackets, guides and anchors even if not specifically shown on the drawings. All supports shall conform to the latest requirements of ASME Code for Pressure Piping B31.1 and MSS Standard Practice SP-58, SP-69, SP-89 and SP-90.
3. Pipe hangers shall be capable of supporting the pipe in all conditions of operation without transferring excessive stress to the pipe.
4. Supports shall fit adequately over insulation. Provide 12 gage pipe saddles and inserts of high-density block insulation.
5. Supports shall not be connected to factory provided framework for equipment.
6. Support all piping in such a manner as to prevent all vibration and vertical or horizontal movement.
2.05 EQUIPMENT INSTALLATION
1. All equipment shall be installed according to the manufacturer's requirements.
2.06 ELECTRICAL
1. Contractor shall follow all OSHA and Code requirements for locking out and tagging out of equipment being affected by scope of work.
2.07 CLEANING
1. After project completion thoroughly clean all equipment and piping systems affected by work.
END OF SECTION
Mennen Sports Center APPENDIX A Project No. 900-25-601, © 2022 B32 Engineering Group, Inc. All Rights Reserved
APPENDIX A – EXISTING COMPRESSOR PACKAGE INFORMATION
PHOTO OF CHILLER PACKAGE #1 LABEL PHOTO OF CHILLER PACKAGE #2 LABEL
PHOTO OF CHILLER PACKAGE #1 COMPRESSOR NAMEPLATE PHOTO OF CHILLER PACKAGE #2 COMPRESSOR NAMEPLATE
OVERALL PHOTO OF CHILLER PACKAGE #2
PHOTO SHOWING LOCATION OF NEW SUCTION PIPE HANGER ON
CHILLER PACKAGE #2
Model N - 195GM R-22 High Stage Liq Inj
Screw Rating
OPERATING DATA - Condition 1 Evaporator Condenser
Evap Temperature 5.0 °F Cond / Inter Temperature 105.0 °F
Evap Pressure 42.87 psia Cond / Inter Pressure 225.38 psia
Superheat (Useful) 0.0 °F Subcooling at Condenser 0.0 °F
Superheat (Non-Useful) 0.0 °F Condenser Capacity 2829.2 MBH
Suction Discharge Suction Line Loss 0.0 psi Discharge Line Loss 0.0 psi
Package Suction Loss - psi Package Discharge Loss - psi
Saturated Suction Pressure 42.9 psia Discharge Pressure 225.4 psia
Suction Stop Valve Size - Discharge Stop Valve Size -
Suction Temperature 5.0 °F Disch. Temp (100% / min) 150.0/150.0 °F
Mass Flow 415.7 lb/min Mass Flow 581.5 lb/min
Volume Flow 518.8 ft³/m Volume Flow 162.9 ft³/m
Theoretical Swept Volume 618.3 ft³/m Min Cond Temp - °F
ECONOMIZER
Type DX Economized (By
Others) Econ Approach Temp (ΔT Eco) 10.0 °F
Econ Vessel Temp 28.8 °F Econ Mass Flow 123.0 lb/min
Econ Vessel Pressure 68.02 psia Econ Capacity 41.1 TR
Econ Line Loss 0.00 psi Sideload Mass Flow 0.0 lb/min
Econ Package Loss 10.00 psi Sideload Capacity 0.0 TR
PERFORMANCE DATA
Compressor Performance Motor
Capacity 174.0 TR Voltage - V/PH/Hz
Power 291.4 BHP Motor Size - HP
Performance Factor 1.67 BHP/TR Frame Size -
Speed 3550 RPM Efficiency - %
Percent of Full Load 100 % Full Load Amps - A
Vi - Fixed 3.6 Starting Type -
Starting Torque 133.5 lb-ft
OIL COOLING DATA
Oil Cooling Type Liq. Inj. - IntelliSOC Oil Cooling Medium R-22
Oil Supply Temp 150.0 °F Min Liq Inj Feed Pressure 110.2 psia
Functional Oil Flow 10.1 GPM Liq Inj Mass Flow (100%) 42.7 lb/min
Injection Oil Flow 5.0 GPM Liq Inj Capacity (100%) 17.3 TR
Total Oil Flow 15.09 GPM Liq Inj Mass Flow (min) 52.9 lb/min
Oil Type FES #2 (65 gal) Liq Inj Capacity (min) 21.5 TR
Oil Pump Size -
PROJECT DATA
Project Name: Reference:
Customer Name: New Contact Prepared By: Adam Thorson
Proposal Number: Date: 6/27/2025
Tolerance on compressor performance is +/-5% per ARI 510. The information contained in this program is subject to change without notice. GEA reserves the right to final verification of all ratings results.
RTSelect Version 14.4.5 Printed: 6/27/2025 1:55:58 PM
Engineering Data Sheet
G - Series Compressor Package Micro III Control Panel
FES Job No.: 04230041 Page 1 of 5 Form: E-169 Revision: E Effective: 12-02
JOB NUMBER: 04230041
MODEL NUMBER: 195GME
PROGRAM PART NUMBER: 726-00416M-001 – 270 psig HPCO
ENCLOSURE: NEMA 4
AC LINE FREQUENCY: 60 Hz.
UNITS: I-P
LANGUAGE: ENGLISH
ENVIRONMENT: NON-HAZARDOUS
CAPACITY CONTROL: PRESSURE
FES Job No.: 04230041 Page 2 of 5 Form: E-169
Effective: 12-02
DIPSWITCH SETTINGS
DIPSWITCH FUNCTION SWITCH POSITION
SW6 #1, #2 ComMENT Network Baud Rate OPEN, OPEN [2.5 Mbs]
SW6 #3 Normal / Service Mode OPEN [Normal]
SW6 #4 Not Used
SW6 #5 Keypad Lockout Mode CLOSED [Lockout all keys]
SW6 #6 Power Fail Reset Enable / Disable OPEN [Disable]
SW6 #7 Not Used
NOTE: PLEASE REFER TO MICROPROCESSOR III INSTRUCTION MANUAL FOR
PARAMETER & DIPSWITCH EXPLANATIONS AND DETAILS.
FES Job No.: 04230041 Page 3 of 5 Form: E-169
Effective: 12-02
OPERATING PARAMETERS
Parameter Recommended Settings
Suction Pressure Suction 1 Pressure Setpoint 28.2 psig Suction 1 Pressure Upper 37.7 psig Suction 1 Pressure Lower 20.1 psig Suction 1 Pressure Proportional Band 4.0 psi Suction 1 Pressure Dead Band 0.5 psi Suction 2 Pressure Setpoint 28.2 psig Suction 2 Pressure Upper 37.7 psig Suction 2 Pressure Lower 20.1 psig Suction 2 Pressure Proportional Band 4.0 psi Suction 2 Pressure Dead Band 0.5 psi Low Suction Pressure 0=Shutdown / 1=Cycle 0 Process Temperature Process 1 Temperature Setpoint 0.0 °F Process 1 Temperature Upper 0.0 °F Process 1 Temperature Lower 0.0 °F Process 1 Temperature Proportional Band 0.0 °F Process 1 Temperature Dead Band 0.0 °F Process 2 Temperature Setpoint 0.0 °F Process 2 Temperature Upper 0.0 °F Process 2 Temperature Lower 0.0 °F Process 2 Temperature Proportional Band 0.0 °F Process 2 Temperature Dead Band 0.0 °F Low Process Temperature 0=Shutdown / 1=Cycle 0 Process Temperature Control Low Suction 0.0 psig Process Temperature Control Proportional Band 0.0 psig Process Temperature Control Load Adjust 0.0 psig Compressor Motor Motor Current Upper (FLA X SF) 372.6 A Motor Current Lower (FLA X SF X 0.85) 316.7 A Motor Current Dead Band (Nom. 10% FLA) 32.4 A Anti-Recycle Period 20 min Accumulated Compressor Runtime 0.0 hrs Motor Current CT Ratio 600 :5 Inlet Oil Oil Filter Pressure Drop Maximum 15.0 psid Inlet Oil Temperature Upper 150.0 °F Inlet Oil Temperature Lower 95.0 °F
FES Job No.: 04230041 Page 4 of 5 Form: E-169
Effective: 12-02
OPERATING PARAMETERS (cont’d)
Parameter Recommended Settings
Oil Separator Oil Separator Heater Setpoint 115.0 °F Oil Separator Temperature Upper 225.0 °F Oil Separator Temperature Lower 75.0 °F Discharge Discharge Pressure Maximum 270.0 psig Discharge Pressure Proportional Band 10.0 psi Discharge Temperature Upper 225.0 °F Control Control Mode 0=Pressure / 1=Tempreature / 2=Digital Input 0 Control Point 0=Digital Input / 1=Point #1 / 2=Point #2 1 Capacity Load / Unload Period 4.0 s Slide Valve Position Minimum 0.0 % Load Limit 0=None / 1=Pulse / 2=Set Point / 3=Slide Valve 0 Economizer Economizer Solenoid On Above % 40.0 % Economizer Solenoid Off Below % 40.0 % Slide Valve Slide Valve Output #1 ON Position 0.0 % Slide Valve Output #1 OFF Position 0.0 % Slide Valve Output #2 ON Position 0.0 % Slide Valve Output #2 OFF Position 0.0 % Power Failure Reset Reset to Mode? 1=Local / 2=Remote 1 Delay Before Power Fail Reset 10.0 s Abort Power Fail Reset After 600.0 s Power Monitoring Demand Metering Ratio (CT)(Voltage)(.7)(1.732)/1000 334.6 kW Kilo Watt Hour Sampling Period 5 min Kilo Watt Hours Consumed 0.0 kWh Historical Data Short Term Sampling Period 2.0 s Long Term Sampling Period 10 min Reset Short Term Trend (0=No / 1=Yes) 0 Reset Long Term Trend (0=No / 1=Yes) 0 Real Time Clock Hour (0-23) Minute (0-59) Second (0-59) Day of Week (1=Sun / 7=Sat) Month (1-12) Day of Month (1-31) Year (00-99)
FES Job No.: 04230041 Page 5 of 5 Form: E-169
Effective: 12-02
OPERATING PARAMETERS (cont’d)
Parameter Recommended Settings
Units Temperature 0=°C / 1=°F 1 Pressure 0=kg/cm2 / 1=kPa / 2=psi / 3=Bar 2 Reset Memory Reset Memory (0=No / 1=Yes) 0
ALARM PARAMETERS
Suction Pressure Suction 1 Pressure Upper 35.7 psig Suction 1 Pressure Lower 21.6 psig Suction 2 Pressure Upper 35.7 psig Suction 2 Pressure Lower 21.6 psig Process Temperature Process 1 Temperature Upper 0.0 °F Process 1 Temperature Lower 0.0 °F Process 2 Temperature Upper 0.0 °F Process 2 Temperature Lower 0.0 °F Process Temperature Control Low Suction 0.0 psig Compressor Motor Motor Current Upper (FLA X S.F. X 0.99) 368.8 A Inlet Oil Oil Filter Pressure Drop Maximum 10.0 psi Inlet Oil Temperature Upper 145.0 °F Inlet Oil Temperature Lower 102.0 °F Oil Separator Oil Separator Temperature Upper 210.0 °F Oil Separator Temperature Lower 102.0 °F Discharge Discharge Pressure Maximum 250.0 psig Discharge Temperature Upper 210.0 °F
GM Series Compressor Package
FES Job No.: 04230041 Page 1 of 6 Form: E-176 Revision: W Effective: 03-04
JOB NUMBER: 04230041
JOB NAME: MENNEN ARENA
LOCATION: MORRISTOWN, NJ
DATE: MAY 28, 2004
REVISION:
PROJECT ENGINEER: PAUL WAPLINGER/pw
MODEL: 195GME
REFRIGERANT: R-22
TYPE OF COOLING: LIQUID INJECTION
APPLICATION: HIGH STAGE – FIXED VI
TYPE OF CONTROL: MICRO III
OPERATING CONDITIONS:
SAT. SUCTION TEMPERATURE 5.0 °F
SAT. SUCTION PRESSURE 28.2 psig
SAT. ECON. SUCTION TEMPERATURE 30.1 °F
SAT. ECON. SUCTION PRESSURE 55.0 psig
SAT. DISCHARGE TEMPERATURE 105.0 °F
SAT. DISCHARGE PRESSURE 210.8 psig
PACKAGE RATINGS:
CAPACITY 162.0 Tons
POWER 287.0 BHP
Ratings are for the complete package including losses for FES supplied suction and discharge stop valves. Stop valves supplied by others may have losses slightly greater or less than those used in the calculation.
FES Job No.: 04230041 Page 2 of 6 Form: E-176
Effective: 03-04
DRAWINGS
GENERAL ARRANGEMENT 04230041-01D
PIPING SCHEMATIC 010-02100D
ELEMENTARY CONTROL DIAGRAM 04230041-04D
CONNECTION DIAGRAM
LARGE I/O RACK 04230041-08D
FIELD & STARTER WIRING DIAGRAM 04230041-05D
OPTIONS DIAGRAM(S) SEE BELOW
DRAWING NO. OPTION
[ X ] 196-00101A Oil Cooling [ ] 196-00102A Remote Control & Sequence – Slave [ X ] 196-00103A Shutdown Status [ X ] 196-00104A Economizer/Subcooler Output [ X ] 196-00105A Auxiliary Alarm #1 [ X ] 196-00106A Alarm Status [ X ] 196-00107A Auxiliary Shutdown #2 [ X ] 196-00108A Oil Level [ ] 196-00109A Division 2 [ ] 196-00110A Panel Air Purge [ ] 196-00111A Compressor Start Isolation Relay [ ] 196-00112A Oil Pump Start Isolation Relay [ X ] 196-00113A Keypad Lockout [ X ] 196-00114A Process Temperature Probe with well (Shipped loose) [ ] 196-00115A 4-20mA Slide Valve [ ] 196-00116A 4-20mA Slide Valve and Motor Current [ X ] 196-00117A 2nd Oil Heater [ ] 196-00118A 3rd Oil Heater [ ] 196-00129A Variable Vi [ X ] 196-00130A External Oil Pump Note: Panel options marked with an “X” are shown on the Elementary Control Diagram, drawing number 04230041-04D.
FES Job No.: 04230041 Page 3 of 6 Form: E-176
Effective: 03-04
COMPRESSOR COMPONENTS
ITEM FES PART NO. QTY. DESCRIPTION/REMARKS
Compressor Model 195GM 1 Compressor Model N-2 390-004440-002 Serial No. N0520 Compressor Vi 3.6
Compressor Motor 3A434055-R01 1 HP 300 (Siemens) Frame 447TS Synchronous RPM 3600
FL RPM 3565
Enclosure ODP Volt/Ph/Hz 460/3/60
FLA 324
LRA 2200
SF 1.15
Serial No. F04TESP.19 2 DE Bearing 65BC03JP3 ODE Bearing 65BC03JP3 Furnished By FES Mounted By FES
Motor Starter 04230053-R01 1 Type Solid State (Benshaw) Current Transformer 600:5 Furnished By FES
Compressor Coupling 010-02092C-019 1 Motor Shaft Dia. 2-3/8" Series 52, Size 225
Suction Check Valve 390-004520-135 1 Integral to the Compressor
Suction Strainer Screen 390-004520-133 1 Integral to the Compressor
Suction Stop Valve 361-00430M-060 1 6" Globe, S.C., B.W.
Ship Loose
Discharge Check Valve 370-000100-000 1 4"
Discharge Stop Valve 361-00430M-040 1 4" Globe, S.C., B.W.
Mounted
Oil Separator 011-02187D-004 1 DWP (psig) 300 OD (in.) 24 WSL (in.) 120 National Board No. 13771
FES Job No.: 04230041 Page 4 of 6 Form: E-176
Effective: 03-04
OIL SYSTEM COMPONENTS
ITEM FES PART NO. QTY. DESCRIPTION/REMARKS
Coalescer 030-00613C-002 3 9½" OD x 17" Long
Manway Gasket 030-00085C-000 1
Oil Pump/Motor 290-009910-015 1 w/External Relief 1½ HP, 145TC Frame, TEFC
230-460/3/60, 1.15 S.F., 1725 RPM
FLA = 5.0-2.5
Serial No. 11777212
Oil Pump Shaft Seal 290-000820-000 1
Oil Pump Relief Valve 290-000920-000 1
Oil Differential Pressure 370-001700-000 1 ¾" Port Regulator
Oil Strainer 370-007595-100 1
Oil Filter Cartridge 130-000910-002 1
Main Oil Injection Metering Valve 360-003150-000 1 Check Valve 370-007540-075 1
Secondary Oil Return Line Combo Valve 370-005090-000 1 Shut-Off/Drain Valve 370-005130-000 1
Low Oil Level Float 745-001850-000 1 1FS Switch
LIQUID INJECTION COMPONENTS
Liquid Injection TX Valve 370-005000-025 1
Power Element 370-005050-000 1
Liquid Injection Solenoid 370-001070-000 1 7SOL Valve
Solenoid Coil 370-001860-000 1
Liquid Injection Strainer 370-001090-000 1
Liquid Injection Sight 030-001200-000 1 Glass
FES Job No.: 04230041 Page 5 of 6 Form: E-176
Effective: 03-04
LIQUID INJECTION COMPONENTS (cont'd)
ITEM FES PART NO. QTY. DESCRIPTION/REMARKS
Liquid Injection Pressure 370-000400-000 1 Reducing Valve
Needle Valve 370-000410-000 1
ECONOMIZER COMPONENTS
Back Pressure Regulator 370-003910-250 1 2½" Port w/Shut Off Solenoid – 10SOL
Solenoid Coil 370-007620-115 1
Check Valve 370-010150-250 1
Strainer 370-007590-250 1
Stop Valve 360-005360-200 2 2" Angle, S.C., S.W.
Pressure Gauge 910-000850-000 1 2½" Dial; Range: 30.00" – 250 psig
CONTROLS AND INSTRUMENTATION
Valve Block 390-004260-137 1 Y1, Y2, Y3 & Y4 – Solenoids 4-Way Load/Unload S5, S6 & S7 – Metering Valves
Solenoid Coil 390-004260-139 4 Y1, Y2, Y3, & Y4 – Solenoids For Load/Unload Valve
Position Sensor 390-004200-A53 1 Capacity Control 4-20mA
Temperature Probes Separator Oil 715-00006A-001 1 1T Inlet Oil 715-00006A-000 1 2T Discharge 715-00006A-000 1 3T Suction 715-00006A-002 1 4T
Pressure Transducers Suction 745-001500-000 1 1TD, 0-100 psia Discharge 745-001510-000 1 2TD, 0-500 psig Inlet Oil 745-001510-000 1 3TD, 0-500 psig Oil Filter Inlet 745-001510-000 1 4TD, 0-500 psig
PACKAGE TRIM
Relief Valve 370-016990-300 2 300 psig (86.6 #/min of air)
Oil Heater 715-000050-000 2 NEMA 1 Volts 120 Watts 1200
FES Job No.: 04230041 Page 6 of 6 Form: E-176
Effective: 03-04
PACKAGE TRIM (cont’d)
ITEM FES PART NO. QTY. DESCRIPTION/REMARKS
Oil Separator Sight Glass 030-000720-000 3 2" Diameter
Electrical 1 Standard UL#BD-389908
Package Paint 560-001010-000 1 System 1 Standard FES Paint Dusty Gray
Oil Charge 560-000300-055 75 Gallons Type Alkyl Benzene Brand FES No. 2 Supplied By FES
Special Specification Sheet Short Form
Page 1 of 1 Form: E-1 Revision: F Effective: 01-03
Job Number: 04230041 Date: May 28, 2004 Job Name: Mennen Arena Project Eng./Eng. Ass’t: Paul W.
Location: Morristown, NJ Revision:
Model Number: 195GME Page 1 of 1
(Check Items That Are Applicable)
No Specials Required [ ]
CRN Required [ ]
CSA Nameplate Required [ ]
California X-Ray [ ]
Class ___, Group ___, Division ___ [ ]
Dual Oil Filters [ ]
Insulation/Heat Tracing [ ]
Mill Certs. [ ]
Oil Charge Not Required [ ]
Oil Charge Ship Loose [ ]
Process Temperature Probe w/well [ X ] Ship loose
Special Oil Heaters [ ]
Special Oil Pump Motor [ ]
Special Paint [ ]
Taiwan Code Required [ ]
People's Republic of China [ ]
Control Transformer [ ]
Customer Inspection Requirements
(See Attached)
Ship Loose Items, Specify: [ ]
Special Piping Specs., Specify: [ ]
Other, Specify: [ X ] Demister pad in oil separator. Enable Condenser Control for FAN #1, Fan Damper & Pump. Supply digital inputs for interlock feedback. Hot gas bypass control.
DX Chiller control with 2 ouputs for dual circuit evaporators. Interlock for glycol pump starter – permissive start. Remote start/stop input. Permissive input from glycol flow switch (switch by others).
Common alarm and shutdown outputs.
Copies to: Traffic Manager
Contracts Manager
Planner (one for each unit)
QA Inspector (one for each unit)
Electrical Leadman
Original to Contract File
G - Series Compressor Package Micro III Control Panel
FES Job No.: 04230042 Page 1 of 5 Form: E-169
Effective: 12-02
JOB NUMBER: 04230042
MODEL NUMBER: 195GME
PROGRAM PART NUMBER: 726-00416M-001 – 270 psig HPCO
ENCLOSURE: NEMA 4
AC LINE FREQUENCY: 60 Hz.
UNITS: I-P
LANGUAGE: ENGLISH
ENVIRONMENT: NON-HAZARDOUS
CAPACITY CONTROL: PRESSURE
FES Job No.: 04230042 Page 2 of 5 Form: E-169
Effective: 12-02
DIPSWITCH SETTINGS
DIPSWITCH FUNCTION SWITCH POSITION
SW6 #1, #2 ComMENT Network Baud Rate OPEN, OPEN [2.5 Mbs]
SW6 #3 Normal / Service Mode OPEN [Normal]
SW6 #4 Not Used
SW6 #5 Keypad Lockout Mode CLOSED [Lockout all keys]
SW6 #6 Power Fail Reset Enable / Disable OPEN [Disable]
SW6 #7 Not Used
NOTE: PLEASE REFER TO MICROPROCESSOR III INSTRUCTION MANUAL FOR
PARAMETER & DIPSWITCH EXPLANATIONS AND DETAILS.
FES Job No.: 04230042 Page 3 of 5 Form: E-169
Effective: 12-02
OPERATING PARAMETERS
Parameter Recommended Settings
Suction Pressure Suction 1 Pressure Setpoint 28.2 psig Suction 1 Pressure Upper 37.7 psig Suction 1 Pressure Lower 20.1 psig Suction 1 Pressure Proportional Band 4.0 psi Suction 1 Pressure Dead Band 0.5 psi Suction 2 Pressure Setpoint 28.2 psig Suction 2 Pressure Upper 37.7 psig Suction 2 Pressure Lower 20.1 psig Suction 2 Pressure Proportional Band 4.0 psi Suction 2 Pressure Dead Band 0.5 psi Low Suction Pressure 0=Shutdown / 1=Cycle 0 Process Temperature Process 1 Temperature Setpoint 0.0 °F Process 1 Temperature Upper 0.0 °F Process 1 Temperature Lower 0.0 °F Process 1 Temperature Proportional Band 0.0 °F Process 1 Temperature Dead Band 0.0 °F Process 2 Temperature Setpoint 0.0 °F Process 2 Temperature Upper 0.0 °F Process 2 Temperature Lower 0.0 °F Process 2 Temperature Proportional Band 0.0 °F Process 2 Temperature Dead Band 0.0 °F Low Process Temperature 0=Shutdown / 1=Cycle 0 Process Temperature Control Low Suction 0.0 psig Process Temperature Control Proportional Band 0.0 psig Process Temperature Control Load Adjust 0.0 psig Compressor Motor Motor Current Upper (FLA X SF) 372.6 A Motor Current Lower (FLA X SF X 0.85) 316.7 A Motor Current Dead Band (Nom. 10% FLA) 32.4 A Anti-Recycle Period 20 min Accumulated Compressor Runtime 0.0 hrs Motor Current CT Ratio 600 :5 Inlet Oil Oil Filter Pressure Drop Maximum 15.0 psid Inlet Oil Temperature Upper 150.0 °F Inlet Oil Temperature Lower 95.0 °F
FES Job No.: 04230042 Page 4 of 5 Form: E-169
Effective: 12-02
OPERATING PARAMETERS (cont’d)
Parameter Recommended Settings
Oil Separator Oil Separator Heater Setpoint 115.0 °F Oil Separator Temperature Upper 225.0 °F Oil Separator Temperature Lower 75.0 °F Discharge Discharge Pressure Maximum 270.0 psig Discharge Pressure Proportional Band 10.0 psi Discharge Temperature Upper 225.0 °F Control Control Mode 0=Pressure / 1=Tempreature / 2=Digital Input 0 Control Point 0=Digital Input / 1=Point #1 / 2=Point #2 1 Capacity Load / Unload Period 4.0 s Slide Valve Position Minimum 0.0 % Load Limit 0=None / 1=Pulse / 2=Set Point / 3=Slide Valve 0 Economizer Economizer Solenoid On Above % 40.0 % Economizer Solenoid Off Below % 40.0 % Slide Valve Slide Valve Output #1 ON Position 0.0 % Slide Valve Output #1 OFF Position 0.0 % Slide Valve Output #2 ON Position 0.0 % Slide Valve Output #2 OFF Position 0.0 % Power Failure Reset Reset to Mode? 1=Local / 2=Remote 1 Delay Before Power Fail Reset 10.0 s Abort Power Fail Reset After 600.0 s Power Monitoring Demand Metering Ratio (CT)(Voltage)(.7)(1.732)/1000 334.6 kW Kilo Watt Hour Sampling Period 5 min Kilo Watt Hours Consumed 0.0 kWh Historical Data Short Term Sampling Period 2.0 s Long Term Sampling Period 10 min Reset Short Term Trend (0=No / 1=Yes) 0 Reset Long Term Trend (0=No / 1=Yes) 0 Real Time Clock Hour (0-23) Minute (0-59) Second (0-59) Day of Week (1=Sun / 7=Sat) Month (1-12) Day of Month (1-31) Year (00-99)
FES Job No.: 04230042 Page 5 of 5 Form: E-169
Effective: 12-02
OPERATING PARAMETERS (cont’d)
Parameter Recommended Settings
Units Temperature 0=°C / 1=°F 1 Pressure 0=kg/cm2 / 1=kPa / 2=psi / 3=Bar 2 Reset Memory Reset Memory (0=No / 1=Yes) 0
ALARM PARAMETERS
Suction Pressure Suction 1 Pressure Upper 35.7 psig Suction 1 Pressure Lower 21.6 psig Suction 2 Pressure Upper 35.7 psig Suction 2 Pressure Lower 21.6 psig Process Temperature Process 1 Temperature Upper 0.0 °F Process 1 Temperature Lower 0.0 °F Process 2 Temperature Upper 0.0 °F Process 2 Temperature Lower 0.0 °F Process Temperature Control Low Suction 0.0 psig Compressor Motor Motor Current Upper (FLA X S.F. X 0.99) 368.8 A Inlet Oil Oil Filter Pressure Drop Maximum 10.0 psi Inlet Oil Temperature Upper 145.0 °F Inlet Oil Temperature Lower 102.0 °F Oil Separator Oil Separator Temperature Upper 210.0 °F Oil Separator Temperature Lower 102.0 °F Discharge Discharge Pressure Maximum 250.0 psig Discharge Temperature Upper 210.0 °F
GM Series Compressor Package
FES Job No.: 04230042 Page 1 of 6 Form: E-176
Effective: 03-04
JOB NUMBER: 04230042
JOB NAME: MENNEN ARENA
LOCATION: MORRISTOWN, NJ
DATE: MAY 28, 2004
REVISION:
PROJECT ENGINEER: PAUL WAPLINGER/pw
MODEL: 195GME
REFRIGERANT: R-22
TYPE OF COOLING: LIQUID INJECTION
APPLICATION: HIGH STAGE – FIXED VI
TYPE OF CONTROL: MICRO III
OPERATING CONDITIONS:
SAT. SUCTION TEMPERATURE 5.0 °F
SAT. SUCTION PRESSURE 28.2 psig
SAT. ECON. SUCTION TEMPERATURE 30.1 °F
SAT. ECON. SUCTION PRESSURE 55.0 psig
SAT. DISCHARGE TEMPERATURE 105.0 °F
SAT. DISCHARGE PRESSURE 210.8 psig
PACKAGE RATINGS:
CAPACITY 162.0 Tons
POWER 287.0 BHP
Ratings are for the complete package including losses for FES supplied suction and discharge stop valves. Stop valves supplied by others may have losses slightly greater or less than those used in the calculation.
FES Job No.: 04230042 Page 2 of 6 Form: E-176
Effective: 03-04
DRAWINGS
GENERAL ARRANGEMENT 04230041-01D
PIPING SCHEMATIC 010-02100D
ELEMENTARY CONTROL DIAGRAM 04230041-04D
CONNECTION DIAGRAM
LARGE I/O RACK 04230041-08D
FIELD & STARTER WIRING DIAGRAM 04230041-05D
OPTIONS DIAGRAM(S) SEE BELOW
DRAWING NO. OPTION
[ X ] 196-00101A Oil Cooling [ ] 196-00102A Remote Control & Sequence – Slave [ X ] 196-00103A Shutdown Status [ X ] 196-00104A Economizer/Subcooler Output [ X ] 196-00105A Auxiliary Alarm #1 [ X ] 196-00106A Alarm Status [ X ] 196-00107A Auxiliary Shutdown #2 [ X ] 196-00108A Oil Level [ ] 196-00109A Division 2 [ ] 196-00110A Panel Air Purge [ ] 196-00111A Compressor Start Isolation Relay [ ] 196-00112A Oil Pump Start Isolation Relay [ X ] 196-00113A Keypad Lockout [ X ] 196-00114A Process Temperature Probe with well (Shipped loose) [ ] 196-00115A 4-20mA Slide Valve [ ] 196-00116A 4-20mA Slide Valve and Motor Current [ X ] 196-00117A 2nd Oil Heater [ ] 196-00118A 3rd Oil Heater [ ] 196-00129A Variable Vi [ X ] 196-00130A External Oil Pump Note: Panel options marked with an “X” are shown on the Elementary Control Diagram, drawing number 04230041-04D.
FES Job No.: 04230042 Page 3 of 6 Form: E-176
Effective: 03-04
COMPRESSOR COMPONENTS
ITEM FES PART NO. QTY. DESCRIPTION/REMARKS
Compressor Model 195GM 1 Compressor Model N-2 390-004440-002 Serial No. N0531 Compressor Vi 3.6
Compressor Motor 3A434055-R01 1 HP 300 (Siemens) Frame 447TS Synchronous RPM 3600
FL RPM 3565
Enclosure ODP Volt/Ph/Hz 460/3/60
FLA 324
LRA 2200
SF 1.15
Serial No. F04TESP.19.1 DE Bearing BRG65BC03JP3 ODE Bearing BRG65BC03JP3 Furnished By FES Mounted By FES
Motor Starter 04230053-R01 1 Type Solid State (Benshaw) Current Transformer 600:5 Furnished By FES
Compressor Coupling 010-02092C-019 1 Motor Shaft Dia. 2-3/8" Series 52, Size 225
Suction Check Valve 390-004520-135 1 Integral to the Compressor
Suction Strainer Screen 390-004520-133 1 Integral to the Compressor
Suction Stop Valve 361-00430M-060 1 6" Globe, S.C., B.W.
Ship Loose
Discharge Check Valve 370-000100-000 1 4"
Discharge Stop Valve 361-00430M-040 1 4" Globe, S.C., B.W.
Mounted
Oil Separator 011-02187D-004 1 DWP (psig) 300 OD (in.) 24 WSL (in.) 120 National Board No. 13772
FES Job No.: 04230042 Page 4 of 6 Form: E-176
Effective: 03-04
OIL SYSTEM COMPONENTS
ITEM FES PART NO. QTY. DESCRIPTION/REMARKS
Coalescer 030-00613C-002 3 9½" OD x 17" Long
Manway Gasket 030-00085C-000 1
Oil Pump/Motor 290-009910-015 1 w/External Relief 1½ HP, 145TC Frame, TEFC
230-460/3/60, 1.15 S.F., 1725 RPM
FLA = 5.0-2.5
Serial No.
Oil Pump Shaft Seal 290-000820-000 1
Oil Pump Relief Valve 290-000920-000 1
Oil Differential Pressure 370-001700-000 1 ¾" Port Regulator
Oil Strainer 370-007595-100 1
Oil Filter Cartridge 130-000910-002 1
Main Oil Injection Metering Valve 360-003150-000 1 Check Valve 370-007540-075 1
Secondary Oil Return Line Combo Valve 370-005090-000 1 Shut-Off/Drain Valve 370-005130-000 1
Low Oil Level Float 745-001850-000 1 1FS Switch
LIQUID INJECTION COMPONENTS
Liquid Injection TX Valve 370-005000-025 1
Power Element 370-005050-000 1
Liquid Injection Solenoid 370-001070-000 1 7SOL Valve
Solenoid Coil 370-001860-000 1
Liquid Injection Strainer 370-001090-000 1
Liquid Injection Sight 030-001200-000 1 Glass
FES Job No.: 04230042 Page 5 of 6 Form: E-176
Effective: 03-04
LIQUID INJECTION COMPONENTS (cont'd)
ITEM FES PART NO. QTY. DESCRIPTION/REMARKS
Liquid Injection Pressure 370-000400-000 1 Reducing Valve
Needle Valve 370-000410-000 1
ECONOMIZER COMPONENTS
Back Pressure Regulator 370-003910-250 1 2½" Port w/Shut Off Solenoid – 10SOL
Solenoid Coil 370-007620-115 1
Check Valve 370-010150-250 1
Strainer 370-007590-250 1
Stop Valve 360-005360-200 2 2" Angle, S.C., S.W.
Pressure Gauge 910-000850-000 1 2½" Dial; Range: 30.00" – 250 psig
CONTROLS AND INSTRUMENTATION
Valve Block 390-004260-137 1 Y1, Y2, Y3 & Y4 – Solenoids 4-Way Load/Unload S5, S6 & S7 – Metering Valves
Solenoid Coil 390-004260-139 4 Y1, Y2, Y3, & Y4 – Solenoids For Load/Unload Valve
Position Sensor 390-004200-A53 1 Capacity Control 4-20mA
Temperature Probes Separator Oil 715-00006A-001 1 1T Inlet Oil 715-00006A-000 1 2T Discharge 715-00006A-000 1 3T Suction 715-00006A-002 1 4T
Pressure Transducers Suction 745-001500-000 1 1TD, 0-100 psia Discharge 745-001510-000 1 2TD, 0-500 psig Inlet Oil 745-001510-000 1 3TD, 0-500 psig Oil Filter Inlet 745-001510-000 1 4TD, 0-500 psig
PACKAGE TRIM
Relief Valve 370-016990-300 2 300 psig (86.6 #/min of air)
Oil Heater 715-000050-000 2 NEMA 1 Volts 120 Watts 1200
FES Job No.: 04230042 Page 6 of 6 Form: E-176
Effective: 03-04
PACKAGE TRIM (cont’d)
ITEM FES PART NO. QTY. DESCRIPTION/REMARKS
Oil Separator Sight Glass 030-000720-000 3 2" Diameter
Electrical 1 Standard UL#BD-389909
Package Paint 560-001010-000 1 System 1 Standard FES Paint Dusty Gray
Oil Charge 560-000300-055 75 Gallons Type Alkyl Benzene Brand FES No. 2 Supplied By FES
Special Specification Sheet Short Form
Page 1 of 1 Form: E-1 Revision: F Effective: 01-03
Job Number: 04230042 Date: May 28, 2004 Job Name: Mennen Arena Project Eng./Eng. Ass’t: Paul W.
Location: Morristown, NJ Revision:
Model Number: 195GME Page 1 of 1
(Check Items That Are Applicable)
No Specials Required [ ]
CRN Required [ ]
CSA Nameplate Required [ ]
California X-Ray [ ]
Class ___, Group ___, Division ___ [ ]
Dual Oil Filters [ ]
Insulation/Heat Tracing [ ]
Mill Certs. [ ]
Oil Charge Not Required [ ]
Oil Charge Ship Loose [ ]
Process Temperature Probe w/well [ X ] Ship loose
Special Oil Heaters [ ]
Special Oil Pump Motor [ ]
Special Paint [ ]
Taiwan Code Required [ ]
People's Republic of China [ ]
Control Transformer [ ]
Customer Inspection Requirements
(See Attached)
Ship Loose Items, Specify: [ ]
Special Piping Specs., Specify: [ ]
Other, Specify: [ X ] Demister pad in oil separator. Enable Condenser Control for FAN #1, Fan Damper & Pump. Supply digital inputs for interlock feedback. Hot gas bypass control.
DX Chiller control with 2 ouputs for dual circuit evaporators. Interlock for glycol pump starter – permissive start. Remote start/stop input. Permissive input from glycol flow switch (switch by others).
Common alarm and shutdown outputs.
Copies to: Traffic Manager
Contracts Manager
Planner (one for each unit)
QA Inspector (one for each unit)
Electrical Leadman
Original to Contract File
Mennen Sports Center APPENDIX B
APPENDIX B – NEW COMPRESSOR INFORMATION
Model NM - 195GMX R-22 High Stage Liq Inj
Screw Rating
OPERATING DATA - Condition 1 Evaporator Condenser
Evap Temperature 5.0 °F Cond / Inter Temperature 105.0 °F
Evap Pressure 42.87 psia Cond / Inter Pressure 225.38 psia
Superheat (Useful) 0.0 °F Subcooling at Condenser 0.0 °F
Superheat (Non-Useful) 0.0 °F Condenser Capacity 2869.2 MBH
Suction Discharge Suction Line Loss 0.0 psi Discharge Line Loss 0.0 psi
Package Suction Loss - psi Package Discharge Loss - psi
Saturated Suction Pressure 42.9 psia Discharge Pressure 225.4 psia
Suction Stop Valve Size - Discharge Stop Valve Size -
Suction Temperature 5.0 °F Disch. Temp (100% / min) 150.0/150.0 °F
Mass Flow 429.2 lb/min Mass Flow 589.6 lb/min
Volume Flow 535.6 ft³/m Volume Flow 165.2 ft³/m
Theoretical Swept Volume 618.3 ft³/m Min Cond Temp - °F
ECONOMIZER
Type DX Economized (By
Others) Econ Approach Temp (ΔT Eco) 10.0 °F
Econ Vessel Temp 31.8 °F Econ Mass Flow 120.7 lb/min
Econ Vessel Pressure 71.92 psia Econ Capacity 40.6 TR
Econ Line Loss 0.00 psi Sideload Mass Flow 0.0 lb/min
Econ Package Loss 10.00 psi Sideload Capacity 0.0 TR
PERFORMANCE DATA
Compressor Performance Motor
Capacity 177.8 TR Voltage - V/PH/Hz
Power 289.2 BHP Motor Size - HP
Performance Factor 1.63 BHP/TR Frame Size -
Speed 3550 RPM Efficiency - %
Percent of Full Load 100 % Full Load Amps - A
Vi - Fixed 3.6 Starting Type -
Starting Torque 132.6 lb-ft
OIL COOLING DATA
Oil Cooling Type Liq. Inj. - IntelliSOC Oil Cooling Medium R-22
Oil Supply Temp 150.0 °F Min Liq Inj Feed Pressure 98.4 psia
Functional Oil Flow 15.8 GPM Liq Inj Mass Flow (100%) 39.7 lb/min
Injection Oil Flow 7.9 GPM Liq Inj Capacity (100%) 16.1 TR
Total Oil Flow 23.67 GPM Liq Inj Mass Flow (min) 52.6 lb/min
Oil Type FES #2 (35 gal) Liq Inj Capacity (min) 21.4 TR
Oil Pump Size -
PROJECT DATA
Project Name: Reference:
Customer Name: New Contact Prepared By: Adam Thorson
Proposal Number: Date: 6/27/2025
Tolerance on compressor performance is +/-5% per ARI 510. The information contained in this program is subject to change without notice. GEA reserves the right to final verification of all ratings results.
RTSelect Version 14.4.5 Printed: 6/27/2025 1:54:10 PM
Mennen Sports Center APPENDIX C
APPENDIX C – COMPRESSOR RETROFIT INSTRUCTIONS/INFORMATION
October 12, 2015
Installation of a GMX compressor on a GM compressor package
Below is a basic overview of the retrofit requirements when replacing a GM compressor with a new GMX compressor. A GEA Engineer will review each compressor retrofit at time of order to determine exactly what package modifications are required to install the new GMX compressor.
GEA Scope of supply Included (as required)
• Drawing describing specific installation
• Bill of material
• Control panel program update
• Compressor
• Mounting feet
• Suction spacer plate
•…
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