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Retro-Commissioning Plan
for the
Jack E. Brown Chemical Engineering Building
(Bldg. 0386)
Submitted to:
Office of Energy Management
Physical Plant Department
Texas A&M University
Prepared by:
Energy Systems Laboratory
December 10, 2008
ii
EXECUTIVE SUMMARY
A Retro-Commissioning (RC) assessment was conducted at the Jack E. Brown Chemical Engineering
Building (0386#) after it was identified as a good candidate for RC during the pre-retro-commissioning
phase. The Jack E. Brown Chemical Engineering Building is a seven-story building with a total
conditioned area of 205,000 square feet consisting of laboratories, classrooms, offices, and server rooms.
It is located on the main campus of the Texas A&M University in College Station, Texas. The HVAC
system consists of 37 Air Handling Units (AHUs) with a total design maximum supply flow of 393,600
cfm, including 23 single duct variable air volume (SDVAV) AHUs, 13 single duct single zone (SDSZ)
AHUs, and 1 multi-zone constant air volume (MZCAV) AHU. The building exhaust system is
comprised of 33 exhaust fans. The major exhaust system in the building is for the lab tracking system.
The building HVAC system is DDC controlled and powered by the Siemens Apogee system.
The purpose of the assessment was to further identify comfort and energy efficiency improvement
opportunities in this building especially focusing on its HVAC system. Basic building information has
been collected and field investigations have been conducted at selected AHUs and terminal boxes. This
report documents the resultant findings and recommendations.
Retro-Commissioning (RC) Opportunities:
1. Implement OCC/UN-OCC schedule and optimize the ventilation rate for lab areas
2. Implement cold deck temperature setpoint reset for all VAV AHUs and MZCAV A34
3. Implement OCC/UN-OCC schedule on the AHUs serving non-lab areas
4. Implement static pressure setpoint reset for all VAV AHUs
5. Optimize the temperature and humidity control for the SDSZ AHUs
6. Optimize the min flow setting and day/night mode control for fan power boxes
7. Implement space temperature dead band control for lab areas
8. Improve OA damper control if applicable
9. Optimize preheat temperature setpoint if applicable
10. Improve the differential pressure (DP) setpoint reset control for the ChW and HHW pumping
systems
Maintenance Opportunities
1. Verify and calibrate flow stations, CO2 sensors, room temperature sensors, and other control points.
2. Check and adjust HHW manual valves as needed.
3. Perform necessary maintenance on the filters and valves for all AHUs and boxes.
The baseline Energy Use Index (EUI) was 432.8 kBtu/ft2/year and the Energy Cost Index (ECI) was
$8.8730/ft2/year. It is estimated that implementation of the RC process would result in the energy
savings of 6,700 MMBtu/yr in ChW, 4,200 MMBtu/yr in HHW, and 182,600 kWh/yr in electricity, for
an estimated annual energy cost savings of $190,000. The cost savings was based on a rate of
$14.775/MMBtu for ChW, $17.374/MMBtu for HHW, and $0.117/kWh for electricity. The total cost of
implementing the RC process is roughly estimated at $80,000, making it a 0.4 years simple payback.
iii
ACKNOWLEDGEMENTS
The retro-commissioning (RC) initial assessment process detailed in this report was performed by the
Energy Systems Laboratory (ESL) under the direction of, and with the assistance of the Office of
Energy Management (OEM) at Texas A&M University. For information concerning OEM, please contact
Homer L. Bruner, Jr. at (979) 862-2794. For additional information regarding the information in this report
or the overall Continuous Commissioning® program at ESL, please contact Song Deng at (979) 862-1234.
The lead RC investigator for this building was Cory Toole, EIT.
iv
DISCLAIMER
This report was prepared by the Energy Systems Laboratory (ESL) of the Texas Engineering
Experiment Station (TEES) under contract to Sandia National Laboratory. Neither the ESL or TEES or
any of their employees, makes any warranty, express or implied, or assumes any legal liability or
responsibility for the accuracy, completeness, or usefulness of any information, apparatus, product, or
process disclosed, or represents that its use would not infringe on privately-owned rights.
Reference herein to any specific commercial product, process or service by trade name, trademark,
manufacturer or otherwise, does not necessarily constitute or imply its endorsement, recommendation or
favoring by the ESL or TEES or any agency thereof. The views and opinions of the authors expressed
herein do not necessarily state or reflect those of the ESL or TEES or any agency thereof.
v
TABLE OF CONTENTS
EXECUTIVE SUMMARY ........................................................................................................................ ii
ACKNOWLEDGEMENTS ....................................................................................................................... iii
DISCLAIMER ........................................................................................................................................... iv
TABLE OF CONTENTS .............................................................................................................................v
LIST OF FIGURES .................................................................................................................................. vii
LIST OF TABLES .................................................................................................................................... vii
BACKGROUND .........................................................................................................................................1
SITE DESCRIPTION ..................................................................................................................................1
General Facility Description ....................................................................................................................1
General HVAC System Description ........................................................................................................2
PERFORMANCE BASELINES .................................................................................................................4
Energy Baseline .......................................................................................................................................4
Indoor Environment Baseline ..................................................................................................................7
Building Pressurization ............................................................................................................................9
FINDINGS AND OPPORTUNITTIES .......................................................................................................9
Pumping System ....................................................................................................................................10
Air-Handling Units ................................................................................................................................11
Terminal Boxes ......................................................................................................................................16
Exhaust System ......................................................................................................................................18
Lighting System .....................................................................................................................................19
CONCLUSIONS........................................................................................................................................19
APPENDIX A: As-Built Design Information............................................................................................21
APPENDIX B: Field Measurement Records .............................................................................................24
vi
vii
LIST OF FIGURES
Figure 1. Jack E. Brown Chemical Building ............................................................................................. 1
Figure 2. Building location. ....................................................................................................................... 1
Figure 3. Room layout for floor 3/4/5/6/7 .................................................................................................. 2
Figure 4. Time series for Jack E. Brown Chemical Building (#0386) ....................................................... 5
Figure 5. Electricity vs. outside air dry-bulb temperature .......................................................................... 6
Figure 6. Chilled water vs. outside air dry-bulb temperature ..................................................................... 6
Figure 7. Hot water vs. outside air dry-bulb temperature ........................................................................... 7
Figure 8. Indoor thermal environment baseline in PMV chart ................................................................... 9
Figure 9. HHW pumping system control .................................................................................................. 11
Figure 10. AHU system setup ................................................................................................................... 12
Figure 11. AHU1-1 OA damper operation ............................................................................................... 14
Figure 12. AHU4-3 preheat temperature control ...................................................................................... 15
Figure 13. Terminal box serving the server room..................................................................................... 16
Figure 14. Current min/max flow settings for fan powered boxes ........................................................... 17
Figure 15. Lab tracking system ................................................................................................................. 18
LIST OF TABLES
Table 1. Room function for each floor........................................................................................................ 2
Table 2. Summary of Annual Energy Use, based on the Baseline Period .................................................. 7
Table 3. Indoor environment baseline measurements................................................................................ 8
Table 4. List of RC measures with estimated savings and priority .......................................................... 10
Table 5. Savings estimated for electricity, ChW and HHW ..................................................................... 20
1
BACKGROUND
The Energy Systems Laboratory has been under contract with the Physical Plant at Texas A&M
University since 1997 to perform retro-commissioning on selected campus buildings. This process
involves a systematic study of building performance to identify cost effective methods to improve
safety, comfort, and energy efficiency within the building. During the time period since this began,
more than 70 buildings have been commissioned, resulting in millions of dollars of energy savings to
Texas A&M University.
The Jack E. Brown Chemical Engineering Building was selected as a potential building for retro-
commissioning. An initial assessment was conducted in October 2008, and results suggested that this
building would be a good candidate for retro-commissioning. A more in-depth assessment was then
performed to further identify potential areas for building improvement. The results of this assessment
are presented in this report.
SITE DESCRIPTION
General Facility Description
Figure 1. Jack E. Brown Chemical Building Figure 2. Building location.
The Jack E. Brown Chemical Engineering Building was constructed in 2004 and is located on the main
campus of the Texas A&M University in College Station, Texas. The building has seven floors with a
total conditioned area of 205,000 square feet and consists primarily of laboratories, and offices and
classroom. The major room function for each floor is listed in Table 1 and the room layout for the 3rd
floor to the 7th
floor is shown in Figure 3 . It is generally occupied on weekdays from 7:30 AM to 5:30
PM, but also has some occupancy later in the evening and on weekends.
2
Figure 3. Room layout for floor 3/4/5/6/7
Table 1. Room function for each floor
Floor # Major function
1 Classrooms, computer and study rooms
2 Chemical Engineering offices
3/4/6 Chemical labs (interior) and office (exterior)
5 BL2 labs (interior) and office (exterior)
7 Clean rooms(interior) and offices (exterior)
General HVAC System Description
Mechanical
The chilled water (ChW) system in the building utilizes two identical pumps, each 125 hp and supplying
3,000 gpm, serving the main building and one small pump serving the server rooms, with VFDs under
EMCS control. The building piping system is of the variable flow type with two-way piping. The
heating hot water (HHW) system in the building utilizes two identical pumps, each 50 hp and supplying
1,070 gpm, with VFDs under EMCS control. A summary of the building pumping information is shown
in Table A - 1 in the Appendix.
The HVAC system in the building consists of 37 AHUs with a total design maximum supply flow of
393,600 cfm, including 23 SDVAV AHUs, 13 SDSZ AHUs, and 1 MZCAV AHU. Among the 23 VAV
AHUs, 9 AHUs are 100% outside air units (OAHUs) with a total design outside air flow of 157,125 cfm.
Table A - 2 in the Appendix provides an overview of the AHUs in the building, with their design
information. The building contains 240 terminal boxes with DDC control. Of the boxes, 112 are parallel
fan powered boxes, 25 are series fan powered boxes, 57 are in-line variable air volume reheat boxes
serving the labs, and 46 are variable air volume boxes without fan and reheat. The building exhaust
system is comprised of 40 exhaust fans without VFD and 2 exhaust fans with VFDs. The total design
maximum exhaust flow is about 212,960 cfm. Table A - 23 in the Appendix provides an overview of the
Laboratories
3
exhaust fans in the building, with their design information. The major exhaust system in the building is
for the lab tracking system.
Controls
The building HVAC system is DDC controlled and powered by the Siemens Apogee system.
At the time of the RCP investigation, the ChW and HHW pumps were run using the lead/lag control
scheme. The ChW/HHW pumping and the related building return valves were controlled to maintain the
minimum of three end loop differential pressures (DP) at its setpoint. The ChW end loop DP setpoint
was reset to maintain the ChW valves of AHU712 and AHU713 between 80%-90% open. The HHW
end loop DP setpoint was reset to maintain the secondary HHW return temperature between 120°F -
130°F. The small server ChW pumping system was controlled to maintain the DP of the end server loop
at 5 psi.
All AHUs ran 24/7 continuously. The ChW valves for the SDVAV AHUs were controlled to
maintain the cold deck temperature at constant set points from 53°F-56°F, whereas the pre-heat
valves were controlled to maintain the hot deck temperature at constant set points from 50°F -
56°F. The set points are shown in Table A - 3 Exhaust Fans Design Information
MARK Design CFM SP INCH WC MOTOR HP
EF-1-1 3,500 1.5 2
EF-1-2 6,200 1.75 5
EF-1-3 4,920 0.7 1 1/2
EF-1-4 1,200 1.5 3/4
EF-4-1 1,330 2.25 1
EF-4-2 785 3.75 1 1/2
EF-4-3 2,100 3.75 2
EF-4-4 1,330 2.25 1
EF-4-5 1,330 2.25 1
EF-4-6 1,380 2.5 1 1/2
EF-4-7 785 3.75 1 1/2
EF-4-8 1,330 2.25 1
EF-4-9 8,500 4 10
EF-4-10 8,500 4.25 15
EF-4-11 8,500 4.25 15
EF-4-12 880 0.625 1/4
EF-4-13 9,000 3.5 15
EF-5-1 8,500 4 10
EF-5-2 8,500 4 10
EF-5-3 8,500 4 10
EF-5-4 8,500 4 10
EF-5-5 785 3.75 1 1/2
EF-6-1 8,500 3.75 10
4
EF-6-2 9,750 3.75 15
EF-6-3 8,500 4 10
EF-6-4 11,000 3.75 15
EF-6-5 9,800 3.5 10
EF-7-1 3,500 2.5 3
EF-7-2 5,900 3.75 7 1/2
EF-7-3 4,035 2.5 3
EF-7-4 440 0.35 1/8
EF-7-5 7,200 2.75 7 1/2
EF-7-6 4,400 3.25 5
EF-7-7 2,665 2.25 2
EF-7-8 750 0.75 1/4
GRH-1 2,710 0.04 -
GRH-2 2,710 0.04 -
SFP-1 5,000 1 3
SFP-2 5,000 1 3
OAI-1 6,745 0.1 -
EF-3-1 9,000 4.6 15
EF-3-2 9,000 4.6 15
Total 212,960 241
Table A - 4. The supply fan speeds for SDVAV AHUs were modulated to maintain the static pressure at
constant set points, which could be from 0.75 inch WC to 3.50 inch WC. The outside air dampers for the
majority of non-OAHU VAV units were modulated to maintain the design OA flow whereas the outside
air dampers for AHU1-1 and AHU1-2 were modulated to maintain the maximum room CO2 level at
1,000 ppm.
The ChW and HHW control valves for most of SDSZ AHUs serving the 7th
floor were couple controlled
to maintain the space temperature at 67°F when the associated space relative humidity was less than
50%. When the space relative humidity was higher than 55%, the ChW control valves were controlled to
maintain the cold deck temperature at 53°F and the HHW control valves were controlled to maintain the
space temperature at their set points. The ChW control valves for MZCAV were modulated to maintain
the cold deck temperature at a constant set point of 53°F and the HHW control valves were controlled to
maintain the space temperature at 72°F.
The lab tracking system was controlled to maintain a negative pressure relative to the hallway by using
the offset flow method. The offset flow set points for most of the labs were overridden at 152 cfm.
PERFORMANCE BASELINES
Energy Baseline
The baseline period chosen was from 9/1/2007 through 8/31/2008. Figure 4 shows the outside air dry-
bulb temperature and the time series plots for the consumptions of Electricity, CHW, and HHW using
5
daily data. Figure 5 - Figure 7 show the consumption as it relates to the average daily outdoor dry bulb
temperature during the baseline period.
Figure 4. Time series for Jack E. Brown Chemical Building (#0386)
6
Figure 5. Electricity vs. outside air dry-bulb temperature
Figure 6. Chilled water vs. outside air dry-bulb temperature
7
Figure 7. Hot water vs. outside air dry-bulb temperature
It was found that from the HHW chart that there was about 25 MMBtu/day of reheat in the building
even during very hot outdoor air temperatures. While a laboratory building may require more reheat
than a typical office or classroom building because of larger ventilation requirements, the consumption
levels still indicate some potential for HHW savings through improvements in control and maintenance.
The baseline energy usage for the building is summarized in Table 2. The baseline Energy Use Index
was 432.8 kBtu/ft2/yr and the Energy Cost Index (ECI) was $8.873 /ft2/year. The annual energy cost
was $1,818,970.
Table 2. Summary of Annual Energy Use, based on the Baseline Period
Annual Use Unit Cost Energy Cost Baseline Period
ELE 34.7479 (kWh/ft2/yr) 0.117 ($/kWh) 4.0655 ($/ft2/yr) 9/1/07 to 8/31/08
CHW 250.8 (kBtu/ft2/yr) 14.775 ($/MMBtu) 3.7062 ($/ft2/yr) 9/1/07 to 8/31/08
HHW 63.4 (kBtu/ft2/yr) 17.374 ($/MMBtu) 1.1014 ($/ft2/yr) 9/1/07 to 8/31/08
Indoor Environment Baseline
Indoor Environment measurements, including dry-bulb and black ball temperatures, relative humidity,
and CO2 level, were taken at various locations throughout the building on Oct 23, 2008. At the time of
measurement, the outside air temperature was about 59°F-62°F and the relative humidity was about
37%-44%. The measurement results are shown in Table 3. Based on the results, a thermal comfort
evaluation was conducted by using the predicted mean vote (PMV) index method. The PMV index
8
predicts the mean response of a large group of people according to the ASHRAE thermal sensation scale
from -3 (cold) to +3 (hot).
The thermal comfort indexes based on the PMV method revealed that most of the sample points (13 out
of 16) were within acceptable thermal condition (-0.5<PMV<0.5), as shown in Figure 8. 3 points fell
outside the acceptable thermal condition but still were close to the acceptable boundary. In addition,
based on the conversation with the building proctor, hot/cold complaints were received in some rooms,
which would be addressed as a part of final retro-commissioning. The spot check results also showed
that all of CO2 levels were below 600 ppm, which indicated the potential of reducing OA intake in non-
lab areas.
Table 3. Indoor environment baseline measurements
Room # Room Function
Dry Bulb
Temperature
(ºF)
Relative
Humidity
(%)
Mean Radiant
Temperature
(ºF)
PMV* CO2
(ppm)
100 Floor Lobby 71.3 38.9% 69.88 -0.580 525
254 Office 72.3 38.5% 71.73 -0.385 550
200 Floor Hallway 70.8 37.9% 71.65 -0.504 505
200A
(Near stairs) Floor Hallway 74.9 33.6% 74.76
-0.021 515
330 Lab 75.1 32.7% 75.10 0.011 480
335 Office 71.1 37.0% 71.95 -0.467 475
341 Office 72.1 35.3% 72.38 -0.375 533
400
(Near Zachry) Floor Hallway 70.3 31.5% 82.98
0.167 425
413 Office 73 33.7% 73.28 -0.259 506
206 Lab 71.8 30.7% 72.22 -0.435 430
500
(Near Zachry) Floor Hallway 75.5 27.8% 82.47
0.518 450
532 Office 72.7 33.7% 73.55 -0.262 585
529 Lab 71.6 31.1% 72.87 -0.403 460
600
(Near Zachry) Floor Hallway 70.2 32.7% 72.89
-0.495 490
630 Lab 73.1 30.3% 73.66 -0.246 470
626 Office 71.1 33.5% 73.08 -0.412 550
Notes: *The PMV calculation was based on the assumptions below:
Metabolic rate: 1.2met
Clothing level: 0.70clo
Air velocity: 20fpm
9
Figure 8. Indoor thermal environment baseline in PMV chart
Building Pressurization
Pressure measurements were conducted to determine the baseline building pressurization relative to the
outside on Oct 24, 2008. The measurements were taken at the front and the back entrances of the
building. The measurement results showed that the building was positively pressurized relative to the
outside at the two entrances. The front entrance pressurization relative to the outside was about +0.020
inch water column and the back entrance pressurization relative to the outside was about +0.016 inch
water column, which were acceptable building pressurization values.
FINDINGS AND OPPORTUNITTIES
Since the building was built in 2004, the overall condition of the HVAC equipment was good. However,
a number of potential control problems and opportunities in the building were discovered. The major RC
opportunities are summarized in Table 4, with their priorities. The priorities are based on their potential
benefit as well as ease of implementation.
It is estimated that implementation of all of the RC measures would save approximately $190,000 per
year, based on utility rates of $14.775/MMBtu for ChW, $17.374/MMBtu for HHW, and $0.117/kWh
for electricity. The cost of implementing the retro-commissioning process is roughly estimated at
$80,000, for a simple payback period of around 0.4 years. The brief description and explanations of the
RC opportunities developed for each subsystem during the RCP phase are provided following the table.
-3.0
-2.5
-2.0
-1.5
-1.0
-0.5
0.0
0.5
1.0
1.5
2.0
2.5
3.0
Pre
dic
ted
Mea
n V
ote
(P
MV
)
Measured Points
Cold
Hot
Comfort Zone
10
Table 4. List of RC measures with estimated savings and priority
Priority
# Sub-system Brief RC Measure Description
Est. Savings
($/yr)
1 Exhaust &
Terminal Box
Implement OCC/UN-OCC schedule and optimize the
ventilation rate for lab areas $ 50,000
2 AHU Implement cold deck temperature setpoint reset for all
VAV AHUs and MZCAV A34 $ 48,000
3 AHU Implement OCC/UN-OCC schedule on the AHUs
serving non-lab areas $ 15,000
4 AHU Implement static pressure setpoint reset for all VAV
AHUs $ 14,000
5 AHU Optimize the temperature and humidity control for the
SDSZ AHUs $ 13,000
6 Terminal Box Optimize the min flow setting and day/night mode
control for fan power boxes $ 13,000
7 Terminal Box Implement space temperature dead band control for lab
areas $ 13,000
8 AHU Improve OA damper control if applicable $ 11,000
9 AHU Optimize preheat temperature setpoint if applicable $ 6,000
10 Pumping Improve the DP setpoint reset control for the ChW and
HHW pumping systems $ 4,500
Pumping System
ChW system
The ChW system in the building utilizes two identical ChW pumps, with VFDs under EMCS control,
and operates on a lead/lag schedule. The ChW pumping and the related building return valve were
controlled to maintain the minimum of three end loop DPs at its setpoint. The ChW end loop DP
setpoint was reset from 6 psi to 20 psi to maintain the ChW valves of AHU712 and AHU713 between
80%-90% open.
It was found that the ChW DP setpoint was reset at the lower limit (6 psi); in the meanwhile, the ChW
valves of AHU712 and AHU713 were less than 70% open in Oct 13, 2008. It indicates the possibility of
improving the secondary DP setpoint reset control.
It is estimated that this measure would result in energy savings of 13,000 kWh/yr in electricity, for an
estimated annual cost savings of $1,500.
11
HHW system
The HHW system in the building utilizes two identical HHW pumps, with VFDs under EMCS control,
and operates on a lead/lag schedule. The HHW pumping and the related building return valve was
controlled to maintain the minimum of three end loop DPs at its setpoint. The HHW end loop DP
setpoint was reset from 10 psi to 20 psi to maintain the secondary HHW return temperature between
120°F -130°F.
It was found that all of the hot water manual valves for the AHUs and reheat boxes were partially open
and the HHW DP setpoint was reset at 20 psi at the time of investigation, as shown in Figure 9. Since
the DP sensors were almost at the loop end, and normally the design DP for AHU HHW coil was less
than 4 psi, it was unnecessary to provide as high as 20 psi DP at the end loop. This indicates the
potential of improving the secondary DP setpoint reset control. In addition, the HHW manual valve
being partial-open indicates the possibility for HHW loop balancing optimization.
It is estimated that this measure would result in energy savings of 26,000 kWh/yr in electricity, for an
estimated annual cost savings of $3,000.
Figure 9. HHW pumping system control
Air-Handling Units
The HVAC system in the building consists of 37 AHUs, including 9 VAV OAHUs, 14 SDVAV AHUs,
13 SDSZ AHUs, and 1 multi-zone CAV AHU. Based on the design, about 80% of outside air flow for
12
the OAHUs serves the interior labs directly and the rest of outside air flow is supplied to other AHUs
serving other non-lab areas. The AHU system setup is shown in
Figure 10.
Figure 10. AHU system setup
During the initial assessment process, air-side and water-side measurements were performed on 6 AHUs
(2 VAV OAHU, 3 SDVAV AHU and 1 multi-zone CAV AHU). Measurement results are shown in
Appendix B. The existing control strategies for all of the AHUs were reviewed. The major potential
problems and opportunities are as follows:
1) Implement cold deck temperature setpoint reset for all VAV AHUs and MZCAV A34
The ChW control valves for all of the VAV AHUs (including 9 OAHUs) and MZCAV A34 were
controlled to maintain the cold deck temperature at constant set points ranging from 53°F-56°F. The
constant cold deck set points, as shown in Table A - 4, could cause unnecessary simultaneous cooling
and heating.
It is recommended that an optimal reset schedule be implemented for the cold deck temperature set
points. For instance, an optimal reset schedule based on a combination of dew point and reheat valve
positions could be implemented for the OAHUs and a reset schedule based on reheat valve positions
could be implemented for the non-OAHUs.
It is estimated that this measure would result in energy savings of 1,510 MMBtu/yr in ChW and 1,510
MMBtu/yr in HHW, for an estimated annual cost savings of $48,000.
2) Implement OCC/UN-OCC schedule on the AHUs serving non-lab areas
At the time of the RCP investigation, all AHUs, even the AHUs serving non-lab areas, i.e. offices and
classrooms, run 24/7 continuously. Typically, it is not necessary for the AHUs serving non-lab areas to
run continuously and a kind of shutdown/setback schedule could be implemented on these AHUs.
It is recommended that the room’s function, schedule, and thermal requirement be further investigated as
a part of final retro-commissioning. As one consideration, an OCC/UN-OCC schedule based on the
combination of the terminal boxes day/night mode and time schedule could be implemented on the
AHUs serving non-lab areas.
OAHU SDVAV
Lab terminal box
Non-lab SDVAV
13
It is estimated that this measure would result in energy savings of 860 MMBtu/yr in ChW, 200
MMBtu/yr in HHW, and -6,000 kWh/yr in electricity. Despite the electricity penalty from high fan
speeds at startup, it is estimated that this measure will result in a cost savings of $15,000 per year.
3) Implement static pressure setpoint reset for all VAV AHUs
The supply fan speeds for all VAV AHUs were modulated to maintain the static pressure at the
associated constant setpoint separately. The static pressure set points at the time of the RCP
investigation are shown in Table A - 4. It was found that some constant static pressure set points were
set as high as 3.5 inch WC, which was close to the maximum safe operation pressure for typical AHU
ducts. The high static constant pressure set points also could cause the terminal box dampers always
partially closed, which was proved by the fact that all terminal box dampers for AHU1-1 and AHU1-2
were less than 70% open in Oct 21, 2008. The partial damper positions indicated unnecessarily high
static pressure set points. It is recommended that a demand-based static pressure set point reset schedule
be considered to save fan energy consumption.
It is estimated that this measure would result in energy savings of 123,000 kWh/yr in electricity, for an
estimated annual cost savings of $14,000.
4) Optimize the temperature and humidity control for the SDSZ AHUs
All the SDSZ AHUs in this building serve the clean room in the 7th
floor. Based on the existing control
programming, the ChW and HHW control valves for most of SDSZ AHUs serving the 7th
floor were
couple controlled to maintain the space temperature at 67 °F when the associated space relative humidity
was less than 50%. When the space relative humidity was higher than 55%, the ChW control valves
were controlled to maintain the cold deck temperature at 53 °F and the HHW control valves were
controlled to maintain the space temperature at 67 °F.
It seems that the existing control programming intends to dehumidify the space air by controlling the
cold deck temperature at 53°F. However, the related dew point temperature is only about 50°F when the
space temperature and relative humidity are 67 °F and 55% separately. This indicates the potential of
optimizing the relative humidity set point. In addition, the hard constant temperature setpoint indicates
the possibility of optimizing temperature control by implementing temperature dead band schedule. It is
recommended that a survey of thermal environment requirement for the clean rooms be conducted to
determine the optimal set points.
It is estimated that this measure would result in energy savings of 410 MMBtu/yr in ChW and 410
MMBtu/yr in HHW, for an estimated annual cost savings of $13,000.
5) Improve OA damper control if applicable
Based on the existing PPCL programming, the outside air dampers for the majority of non-OAHU VAV
units were modulated to maintain the design OA flow, which was about 10%-30% of the associated max
total air flow. Since all non-OAHU VAV units don’t have return air dampers in the return air ducts and
the outside air ducts are far smaller than the return air duct size, these AHUs can’t fully use 100% OA to
implement the full economizer control. Whereas it was also found that most of the OA dampers for these
14
non-OAHU VAV units were 50%-70% open to maintain the OA flow set points, which indicated the
possibility of improving OA dampers control by partial economizer implementation.
In addition, since the OA flow sensors were critical to damper control, a total of 7 OA flow sensors were
sample checked during the retro-commissioning. It was found that 2 flow sensors were off by 20%
(field measurements were higher than Apogee readings), and 2 flow sensors had failed, which caused
the related OA dampers to fully open. Therefore, the actual OA flow almost was twice of the flow set
points. It is recommended that all of the OA flow sensors be checked and calibrated.
For AHU1-1 and AHU1-2, the outside air dampers were modulated to maintain the maximum CO2 level
in some rooms at 1,000 ppm. However, it was found that all five CO2 sensors investigated were out of
calibration (Apogee reading: 1,300-1,400 ppm; Field measured: 600-800 ppm), which drove the OA
dampers of AHU1-1 and AHU1-2 to full open, as shown in Figure 11. It is recommended that all CO2
sensors be verified and calibrated. Also, the OA damper control for AHU1-1 and AHU1-2 could be
improved by the partial economizer implementation.
It is estimated that this measure would result in energy savings of 720 MMBtu/yr in ChW and 40
MMBtu/yr in HHW, for an estimated annual cost savings of $11,000.
Figure 11. AHU1-1 OA damper operation
6) Optimize preheat temperature setpoint if applicable
15
The pre-heat control valves were controlled to maintain the hot deck temperature at the associated
constant set points separately. The preheat temperature set points at the time of the RCP investigation
are shown in Table A - 4.
As can be seen from the table that some of the preheat temperature set points were very close or even
higher than the associated cold deck temperature set points, which could cause unnecessary
simultaneous cooling and heating. For example, as shown in Figure 12, it was found that the preheat
temperature setpoint for AHU4-3 was 53°F whereas the cold deck temperature setpoint was 50°F, which
caused both the pre-heat valve and the ChW valve to be over 10% open when the outside air temperature
was about 51°F on Nov. 16, 2008. This indicates that the preheat temperature set point could be
optimized to avoid the un-necessary simultaneous cooling and heating.
It is estimated that this measure would result in energy savings of 190 MMBtu/yr in ChW and 190
MMBtu/yr in HHW, for an estimated annual cost savings of $6,000.
Figure 12. AHU4-3 preheat temperature control
7) Improve server room unit control
The server room on the first floor is served by a separate ChW pumping system and an individual unit
besides a fan powered box of AHU1-1. The ChW valve for the dedicated AHU in the server room was
modulated to maintain the return air temperature at 72°F. Since the sensed return air temperature reading
was 78°F on November 11, 2008, it was found that the ChW valve was fully open, and the unit
discharge air temperature and the server inlet air temperature were about 54°F and 66°F separately.
However, since the temperature distribution for the server room could be different dramatically, the
ASHRAE class 1 design standards recommend that the dedicated unit for the server rooms be controlled
16
to maintain the server inlet air temperature at 68°F to 77°F instead of using the average return air
temperature. This indicated the potential of improving the ChW valve control for the dedicated unit.
It was also observed that the sensed server space temperature was about 67°F, and in the same time, the
reheat valve of the fan power box was fully open, as shown in Figure 13, which indicated the potential
of improving the reheat valve control for the terminal box.
It is estimated that this measure would result in energy savings of 80 MMBtu/yr in ChW and 10
MMBtu/yr in HHW, for an estimated cost savings of $1,500 per year.
Figure 13. Terminal box serving the server room
Terminal Boxes
The building contains 240 terminal boxes with DDC control, the majority of which are equipped with
reheat coils. 8 terminal boxes were selected as samples to be investigated in the field during the initial
assessment process. The investigation results are summarized in Table B - 1 and Table B - 2. It was
found that one of the reheat valves was leaking by and four flow sensors and three room temperature
sensors were out of calibration. It is recommended that all flow sensors and room temperature sensors be
checked and calibrated as needed.
In addition, about 100 terminal boxes were investigated on Apogee during the RCP investigation. These
sample investigations revealed some potential opportunities to save energy as outlined below.
17
1) Optimize the min flow setting and day/night mode control for fan power boxes
At the time of RCP investigation, it was found that the flow settings for almost all the sample boxes
were kept as same as the design flow settings, and that the design minimum air flow set points for
almost all fan powered boxes serving the non-lab areas, as shown in Figure 14, were over 30% of the
related maximum air flow set points, which caused many fan power boxes to operate in heating mode.
This indicates the potential of optimizing the min flow settings for these boxes.
Figure 14. Current min/max flow settings for fan powered boxes
In addition, it was also found that the fan powered boxes serving the non-lab areas had night/day
operation mode at the time of RCP investigation, whereas many boxes were overridden at day mode.
These boxes and the related areas served by the boxes need to be addressed and the box day/night mode
control schedule could be considered if applicable.
It is estimated that this measure would result in energy savings of 360 MMBtu/yr in ChW and 360
MMBtu/yr in HHW, for an estimated annual cost savings of $13,000.
2) Implement space temperature dead band control for lab areas
It was observed that most of the lab space temperature set points were overridden at 75°F for some
reason, and that most space temperature sensor locations were close to the door. Since the labs were
negative relative to the hallway, the cooler air from the hallway may “fool” the lab temperature sensors,
which could be one of the reasons causing the box reheat valve open. A temperature dead band control
would relieve the reheat valve partial-open issue besides achieving the energy benefit from the lower
0%
10%
20%
30%
40%
50%
60%
0 10 20 30 40 50 60 70 80 90 100 110 120 130 140 150
Cu
rren
t B
ox
Min
/ M
ax
Flo
w S
etti
ng
s
Fan Powered Boxes
18
heating set points. It is recommended that a full survey of lab function and thermal requirement be
conducted, and that a temperature dead band control be implemented.
It is estimated that this measure would result in energy savings of 750 MMBtu/yr in HHW, for an
estimated annual cost savings of $13,000 per year.
Exhaust System
The building exhaust system is comprised of numerous exhaust fans. The major exhaust system is for
the lab tracking system. Each floor from the 3rd
to 7th
floor has between 8 and 16 lab suites, and each lab
suite is equipped with a DDC tracking system and designed to maintain a negative pressure in each lab
relative to the hallway by the offset method. Each lab suite has flow stations on the general exhaust flow,
the fume hoods exhaust flow, and the total supply flow as shown in Figure 15.
The fume hoods exhaust have maximum and minimum flow settings and the each has a flow controller
that maintains a constant face velocity until the maximum or minimum flow condition occurs. The
general exhaust air damper is controlled to maintain the general exhaust air set point, which is
determined to pressurize the lab based on the supply air flow required for temperature control, the
supply air minimum setpoint and the fume hoods exhaust. A controller on the main supply duct
regulates the supply flow to be a fixed value less than the total exhaust flow from the lab suite.
Figure 15. Lab tracking system
1) Implement OCC/UNOCC schedule and optimize the ventilation rate for lab areas
19
It was found that all lab boxes and general exhaust dampers were overridden at OCC mode, and the
ventilation rate for most of labs was about 9-12 outside air change per hour (ACH). However, the design
minimum required ventilation rate was 8 ACH during the occupied time and 4 ACH during the un-
occupied time. This indicates the possibilities of implementing OCC/UNOCC schedule and optimizing
the ventilation rate for lab areas. It is recommended that a full survey of labs schedule and ventilation
requirement be conducted, and that lowering the minimum supply and general exhaust flow setting on
occupied and unoccupied modes be considered as one option to optimize the ventilation rate for lab
areas.
In addition, based on the sample investigation results (see in Table B - 2), it was found that 6 out of 17
flow stations were off-calibrated and 1 flow station was failed, which could cause unsafe lab conditions
and waste energy. It is recommended that all of the flow stations be checked and calibrated.
It is estimated that this measure would result in energy savings of 2,530 MMBtu/yr in ChW and 760
MMBtu/yr in HHW, for an estimated annual cost savings of $50,000 per year.
Lighting System
It was observed that almost half of the exterior hallway lights near the windows were on during the
daytime at the time of investigation. It is totally not necessary for the windows day-lighting, which
indicates the potential of improved lighting control.
It is recommended that the hallway lighting control be improved by implementing time schedule. It is
estimated that this measure would result in electricity savings of 9,000 kWh/yr, for an estimated annual
cost savings of $1,000.
CONCLUSIONS
A preliminary evaluation has identified the Jack E. Brown Chemical Engineering building as a good
candidate for retro-commissioning, and a more in-depth assessment has targeted potential areas for
improvement. It is believed that the measures that have been proposed will save on energy costs, in
addition to improving comfort in the building. The major Retro-Commissioning and maintenance
opportunities are listed below:
Retro-Commissioning (RC) Opportunities:
1. Implement OCC/UN-OCC schedule and optimize the ventilation rate for lab areas
2. Implement cold deck temperature setpoint reset for all VAV AHUs and MZCAV A34
3. Implement OCC/UN-OCC schedule on the AHUs serving non-lab areas
4. Implement static pressure setpoint reset for all VAV AHUs
5. Optimize the temperature and humidity control for the SDSZ AHUs
6. Optimize the min flow setting and day/night mode control for fan power boxes
7. Implement space temperature dead band control for lab areas
8. Improve OA damper control if applicable
9. Optimize preheat temperature setpoint if applicable
10. Improve the DP setpoint reset control for the ChW and HHW pumping systems
20
Maintenance Opportunities
1. Verify and calibrate flow station, CO2 sensors, room temperature sensors, and other control points.
2. Check and adjust HHW manual valves as needed.
3. Perform necessary maintenance on the filters and valves for all AHUs and boxes.
It is expected that implementation of the RC process in this facility will yield avoided energy
consumption of 6,700 MMBtu/yr in ChW, 4,300 MMBtu/yr in HHW, and 182,600 kWh/yr in electricity,
for an estimated avoided cost of $190,000 per year, in addition to comfort improvements. The detail
savings estimated for electricity, ChW and HHW are listed in Table 5. The cost of implementing the
retro-commissioning process is roughly estimated at $80,000, which would result in a payback period of
0.4 years.
Table 5. Savings estimated for electricity, ChW and HHW
Items Unit Cost
Pre-RC Estimated Post-RC Estimated Savings
Annual Use Annual Use Annual Use Savings Energy Cost
Savings
Savings
Percentage
ELE 0.117
($/kWh)
34.7479
(kWh/ft2/yr)
33.8572 (kWh/ft2/yr) 0.8907 (kWh/ft2/yr)
0.1042
($/ft2/yr)
3%
CHW 14.775
($/MMBtu)
250.8
(kBtu/ft2/yr)
218.4 (kBtu/ft2/yr) 32.5 (kBtu/ft2/yr)
0.4800
($/ft2/yr)
13%
HHW 17.374
($/MMBtu)
63.4
(kBtu/ft2/yr)
42.8 (kBtu/ft2/yr) 20.6 (kBtu/ft2/yr)
0.3585
($/ft2/yr)
33%
21
APPENDIX A: AS-BUILT DESIGN INFORMATION
Table A - 1 CHW and HHW Pumping Information
CHW System HHW System
Number of pumps 2 2
Pump control source Apogee Apogee
Pump speed control VFD VFD
Pump speed control method DP DP
Bldg Valve control method DP DP
Control valve type DDC DDC
Nameplate GPM 3000 1070
Nameplate Head (ft) 115 110
Nameplate HP 125 50
Table A - 2 AHUs Design Information
AHU# AHU Type Area Served Total Supply Air
(CFM)
Outside Air
(CFM)
Motor
(HP)
A11 SDVAV 1st FLR 18,350 4,020 20
A12 SDVAV 1st FLR 11,120 6,745 15
A31 SDVAV 2rd FLR 9,180 1,500 10
A32 SDVAV & OAHU 2&3rd FLR 25,000 25,000 40
A33 SDVAV 2rd FLR 11,700 1,815 15
A34 MZCAV 1rd FLR Hallway 17,940 2,200 25
A35 SDVAV 3rd FLR 7,500 1,500 10
A36 SDVAV 3rd FLR 12,500 1,500 15
A41 SDVAV 4th FLR 7,500 1,700 10
A42 SDVAV & OAHU 4th FLR 21,000 21,000 30
A43 SDVAV & OAHU 4th FLR 21,000 21,000 30
A44 SDVAV 4th FLR 5,500 1,700 7.5
A51 SDVAV 5th FLR 7,500 1,700 10
A52 SDVAV & OAHU 5th FLR 21,000 21,000 30
A53 SDVAV & OAHU 5th FLR 21,000 21,000 30
A54 SDVAV 5th FLR 5,500 1,700 7.5
A61 SDVAV 6th FLR 7,500 1,000 10
A62 SDVAV & OAHU 6th FLR 25,000 25,000 40
A63 SDVAV & OAHU 6th FLR 25,000 25,000 40
A64 SDVAV 6th FLR 5,500 1,000 7.5
A71 SDSZ 729 6,000 - 7.5
A72 SDSZ 730 2,300 - 3
A73 SDSZ 736 2,000 - 3
A74 SDSZ 737 2,250 - 3
A75 SDSZ 731 8,000 - 7.5
A76 SDSZ 716A 2,925 - 3
22
A77 SDSZ 716B 3,500 - 5
A78 SDSZ 716C 3,700 - 5
A79 SDSZ 716D 2,200 - 3
A710 SDSZ 706 2,700 - 5
A711 SDSZ 716E 3,900 - 5
A712 SDVAV & OAHU EE O/A 12,965 12,965 20
A713 SDVAV & OAHU CHEME O/A 16,270 16,270 25
A714 SDVAV OFFICES 4,500 875 7.5
A715 SDVAV OFFICES 11,000 1,000 15
A716 SDSZ 733 21,000 - 10
A717 SDSZ 735 2,100 - 3
Total - - 393,600 218,190 533
Table A - 3 Exhaust Fans Design Information
MARK Design CFM SP INCH WC MOTOR HP
EF-1-1 3,500 1.5 2
EF-1-2 6,200 1.75 5
EF-1-3 4,920 0.7 1 1/2
EF-1-4 1,200 1.5 3/4
EF-4-1 1,330 2.25 1
EF-4-2 785 3.75 1 1/2
EF-4-3 2,100 3.75 2
EF-4-4 1,330 2.25 1
EF-4-5 1,330 2.25 1
EF-4-6 1,380 2.5 1 1/2
EF-4-7 785 3.75 1 1/2
EF-4-8 1,330 2.25 1
EF-4-9 8,500 4 10
EF-4-10 8,500 4.25 15
EF-4-11 8,500 4.25 15
EF-4-12 880 0.625 1/4
EF-4-13 9,000 3.5 15
EF-5-1 8,500 4 10
EF-5-2 8,500 4 10
EF-5-3 8,500 4 10
EF-5-4 8,500 4 10
EF-5-5 785 3.75 1 1/2
EF-6-1 8,500 3.75 10
EF-6-2 9,750 3.75 15
EF-6-3 8,500 4 10
EF-6-4 11,000 3.75 15
EF-6-5 9,800 3.5 10
23
EF-7-1 3,500 2.5 3
EF-7-2 5,900 3.75 7 1/2
EF-7-3 4,035 2.5 3
EF-7-4 440 0.35 1/8
EF-7-5 7,200 2.75 7 1/2
EF-7-6 4,400 3.25 5
EF-7-7 2,665 2.25 2
EF-7-8 750 0.75 1/4
GRH-1 2,710 0.04 -
GRH-2 2,710 0.04 -
SFP-1 5,000 1 3
SFP-2 5,000 1 3
OAI-1 6,745 0.1 -
EF-3-1 9,000 4.6 15
EF-3-2 9,000 4.6 15
Total 212,960 241
Table A - 4 AHUs temperature and pressure set point at the time of RCP
AHU#
Preheat Temp.
Setpoint
Cold Deck Temp.
Setpoint
Static Pressure
Setpoint
°F °F Inch WG
A11 52 56 3.10
A12 45 50 1.00
A31 - 56 2.75
A32 55 56 3.50
A33 - 56 2.50
A34 - 53 -
A35 - 56 1.25
A36 - 56 2.00
A41 - 56 2.50
A42 56.5 56.5 1.65
A43 53 50 2.25
A44 - 56 1.65
A51 - 56 2.00
A52 53 56 1.35
A53 53 56 2.35
A54 - 56 1.30
A61 - 56 2.00
A62 53 56 1.25
A63 55 52 1.70
A64 - 56 1.50
A714 55 55 0.75
A715 55 55 2.00
24
APPENDIX B: FIELD MEASUREMENT RECORDS
Table B - 1 Fan power boxes field measurement records
Box
#
Box
Type
RM
Served
Apogee
Reading
(CFM)
Flow
Measured
(CFM) Damper Reheat
Valve
Fan
Motor Filter
Thermostat Notes
Max. Min. Max. Min. Apogee Field
FCV
1-10
Fan
powered
constant
Study
room 113 864 268 915 265 Good Good Good x 75.3 73.5
No
return
opening
FCV
2-1
Fan
powered
constant
Library
244 770 220 725 217 Good
Valve
works;
No
water
flow
Good x 75.5 73.9
FVV
2-13
Fan
powered
Variable
Volume
Office
246 652 220 860 283 Good Good Good Clean 75 73.3
FCV
1-5
Fan
powered
constant
Classroom
106 1680 570 1870 640 Good
Leaking
by Good x 71.3 69.9
Table B - 2 Laboratories field investigation records
Room
#
Supply Flow (CFM) General Exhaust
Flow (CFM)
Fume Hood 1
Flow (CFM)
Fume Hood 2
Flow (CFM) Notes
Box# Apogee Field Apogee Field Apogee Field Apogee Field
330 LS 3-2 1020 1175 665 945 250 313 240 255
Room very negative;
Hall air coming around
space
431 LS 4-
11 1360 1540 80 255
1400
(240) 307
240
(1400) 1545
Fume hood 1&2 flow
sensor crossed on
Apogee
512 LS 5-6 1030 1095 700 915 235 308 240 302
Manual reheat valve
25% open; Supply
Temp 87.6F (reheat
valve full open)
631 LS 6-
11 1080 1130 570 615 405 308 240 520
Reheat Valve 50%
open; Supply Temp
80.6F
25
WATER LOOP INFORMATION Service: □ CHW □ HW
Supply
Return
P2
Secondary
Return Temp.Primary
Return Pressure
Secondary
Supply PressurePrimary
Supply PressureP1
Secondary
Supply Temp.
DP1 DP2 DP3
RP1 RP2 RP3
LOOP SIDE MEASUREMENTS
LOCATION TEMPERATURE PRESSURE
COMENTS Apogee Field Apogee Field
Primary Supply
43.3 72.61 72.5
Primary Return
59.5 82.0 66.5 Off calibration
Secondary Supply
42.17 43.3 80.5
Secondary Supply 1
54.98 59.4 Off calibration
Secondary Supply 2
57.41 56.9
Secondary Supply 3
52.86 52.3
Differential Pressure 1
23.33 24.4
Differential Pressure 2
19.12 21.1
Differential Pressure 3
14.98 16.30
PUMPS AND VALVE POSITIONS:
# 1 VFD Running: □ Yes Speed 30 Hz
# 2 VFD Running: □ No Speed -
Return VALVE
POSITION 100% open COMMENTS: CONDITION Good
VALVE POSITION COMMENTS:
CONDITION
FIELD FINDING: DP sensors on 6
th floor
Pressure sensor on 6th
floor, it is supply pressure
26
WATER LOOP INFORMATION Service: □ CHW □ HW
Supply
Return
P2
Secondary
Return Temp.Primary
Return Pressure
Secondary
Supply PressurePrimary
Supply PressureP1
Secondary
Supply Temp.
DP1 DP2 DP3
RP1 RP2 RP3
LOOP SIDE MEASUREMENTS
LOCATION TEMPERATURE PRESSURE
COMENTS Apogee Field Apogee Field
Primary Supply
126.5 73.75 50.0
Primary Return
103.5 9.58 39.3
Secondary Supply
128.8 126.8 59.6
Secondary Return 1
x X
Secondary Return 2
X x
Secondary Return 3
x x
Differential Pressure 1
19.4 20.1
Differential Pressure 2
20.07 20.4
Differential Pressure 3
20.41 19.58
PUMPS AND VALVE POSITIONS:
# 1 □ VFD Running: □ Yes Speed 27 Hz
# 2 □ VFD Running: □ No Speed
Return VALVE
POSITION 100% open COMMENTS: CONDITION Good
VALVE POSITION COMMENTS:
CONDITION
FIELD FINDING: DP sensors on 6
th floor
27
AHU Information AHU: 1-1 Type: Single-Zone
Area Served: Computer rooms and offices
H
C
1 5 6 74
2 RA
OA
C
C
3
AIR-SIDE MEASUREMENTS
POSITION FLOW (CFM) TEMP (°F) S.P. (in WG) Notes
# Descrip Apog. Field Apog. Field Apog. Field
1 OA 3150 3370 66.1 -0.44
OA damper 100% open
VFD 83%
2 RA 9700 71.3 -0.45
3 Mixed Air 69.7 -0.40
4 After Filter -0.74
5 Preheat 69.8 69.8 -0.81
6
After
CHW 55.9 56.1 -1.16
7 Discharge 58.1 3.1 2.02
WATER-SIDE MEASUREMENTS
LOCATION
VALVE PRESSURE(100% VAVLE OPEN)
NO/NC Range Position Leaking By? Before Strainer After
Strainer Before Valve After Valve
HHW - 100% No 62 53.8 51
CHW - 100% 69.3 64.4 63.1
DAMPER OPERATION
LOCATION
DAMPER
NO/NC Range Current
Position
Min
Position
OA N/C DDC 100%
RA No
Damper
28
AHU Information AHU: 1-2 Type: Single-Zone
Area Served: Classrooms
H
C
1 5 6 74
2 RA
OA
C
C
3
AIR-SIDE MEASUREMENTS
POSITION FLOW (CFM) TEMP (°F) S.P. (in WG) Notes
# Descrip Apog. Field Apog. Field Apog. Field
1 OA 2062 2460 62.1 -0.086
CHW 32% VFD = 60% - 65%
2 RA 71.1 -0.08
3 Mixed Air -0.086
4 After Filter 68.4 -0.12
5 Preheat 65.8 68.7 -0.125
6 After CHW 48.9 48.2 -0.27
7 Discharge 5600 49.6 1.0 1.05
VFD
WATER-SIDE MEASUREMENTS
LOCATION
VALVE PRESSURE(100% VAVLE OPEN)
NO/NC Range Position Leaking
By? Before
Strainer After
Strainer Before Valve
After Valve
HHW N/O DDC 100% open No 58.5 59.7 57.5 49.3
CHW N/O DDC 100% open no 65.0 66.3 63.2 61.2
DAMPER OPERATION
LOCATION DAMPER
NO/NC Range Current Position Min Position
OA N/C DDC 100% open
RA No Damper
FIELD FINDING:
29
AHU Information AHU: 3-4 Type: Multi-zone Bypass
Area Served: Hallway
C
CC
C
C
H
C
H
1
2 3
4
5 6
7 8
RA
OA
Zone 1
Zone 2
AIR-SIDE MEASUREMENTS
POSITION FLOW (CFM) TEMP (°F) S.P. (in WG) Notes
# Descrip Apog. Field Apog. Field Apog. Field
1 Mixed Air 70.1 -0.43
2 After Filter 70.1 -0.46
3 After Fan 70.7 1.13
4 After CHW 52.5 53.1 2.8
5 Z2 Before HW 57.1 1.59
6 Z2 Discharge 59.5 56.5 0.234
7 Z1 Before HW 54.3 0.38
8 Z1 Discharge 54.3 54.2 0.40
VFD
WATER-SIDE MEASUREMENTS
LOCATION
VALVE PRESSURE(100% VAVLE OPEN)
NO/NC Range Position Leaking
By? Before Strainer
After Strainer
Before Valve
After Valve
HHW
CHW
DAMPER OPERATION
LOCATION
DAMPER
NO/NC Range Current Position
Min Position
OA
RA
FIELD FINDING:
30
AHU Information AHU: 4-3 Type: Single-Zone OAHU
Area Served: Labs
C
C
1 4 53
OA
2
C
H
AIR-SIDE MEASUREMENTS
POSITION FLOW (CFM) TEMP (°F) S.P. (in WG) Notes
# Descrip Apog. Field Apog. Field Apog. Field
1 -0.033
OA filter dirty
2 71.0 -0.043
3 71.7 71.3 -0.172
4 52.2 52.5 -0.520
5 52.8 2.24 2.17
VFD
WATER-SIDE MEASUREMENTS
LOCATION
VALVE PRESSURE(100% VAVLE OPEN)
NO/NC Range Position Leaking
By? Before Strainer
After Strainer
Before Valve
After Valve
PHW N/C 43.2 34.2 33
CHW 50.5 47.9 46.9
HHW
DAMPER OPERATION
LOCATION
DAMPER
NO/NC Range Current Position
Min Position
OA 100%
RA
FIELD FINDING:
31
AHU Information AHU: 4-4 Type: Single-Zone AHU
Area Served: Labs
1 5 6 74
2 RA
OA
C
C
3
AIR-SIDE MEASUREMENTS
POSITION FLOW (CFM) TEMP (°F) S.P. (in WG) Notes
# Descrip Apog. Field Apog. Field Apog. Field
1 OA 3980 54.3 -0.109
2 RA 54.5 -0.006
3 Mixed Air -0.050
4 After Filter 54.3 -0.100
5
6 After CHW 53.3 54.9 -0.274
7 Discharge 3530 55.8 1.65 1.675
VFD 60.3% 36.1 Hz
WATER-SIDE MEASUREMENTS
LOCATION
VALVE PRESSURE(100% VAVLE OPEN)
NO/NC Range Position Leaking
By? Before Strainer
After Strainer
Before Valve
After Valve
CHW 52 48.8 46.9
DAMPER OPERATION
LOCATION
DAMPER
NO/NC Range Current Position
Min Position
OA
RA
FIELD FINDING:
32
AHU Information AHU: 6-2 Type: Single-Zone OAHU
Area Served: Labs
C
C
1 4 53
OA
2
C
H
AIR-SIDE MEASUREMENTS
POSITION FLOW (CFM) TEMP (°F) S.P. (in WG) Notes
# Descrip Apog. Field Apog. Field Apog. Field
1 OA 76.8 -0.05
VFD 43 Hz Apogee – 48.9% OA filter dirty
2 After Filter -0.33
3 Preheat 75.3 75.6 -0.41
4 After CHW 55.9 57.8 -1.0
5 Discharge 59.3 1.23 1.27
VFD
WATER-SIDE MEASUREMENTS
LOCATION
VALVE PRESSURE(100% VAVLE OPEN)
NO/NC Range Position Leaking
By? Before Strainer
After Strainer
Before Valve
After Valve
PHW 35.2 31.5 29.3
CHW N/C 25 22.5 22.5
DAMPER OPERATION
LOCATION DAMPER
NO/NC Range Current Position Min Position
OA 100% open
RA
FIELD FINDING: