Case study: Ground source heat pump system upgrade
Ground source water is one of the fastest growing applications of renewable energy in North America. Cold Spring Harbor Laboratories upgraded its Alfred D. Hershey Building with a direct expansion split unitary system.
Designers and managers of commercial buildings face increased demands to improve energy efficiency to reduce energy consumption, driven by local and state energy codes and standards like ASHRAE Standard 90.1 and ASHRAE Standard 189.1, and guidelines from the U.S. Green Building Council.
For example, Cold Spring Harbor Laboratories is a private, nonprofit research/education institute dedicated to exploring molecular biology and genetics to improve diagnosis and treatment of cancer. This world-famous biomedical research campus on the north shore of Long Island, New York, is committed to energy efficiency measurement in all facilities throughout its campuses, guided by the New York City Energy Conservation Code and New York state codes. The Alfred D. Hershey Building on one of the campuses of Cold Spring Harbor Laboratories is the home of microscope imaging and 3-D rendering and image analysis. Hershey Laboratory—rededicated in June 2012—required a major improvement in its HVAC system.
The main goal of the upgrade was to provide improved temperature and humidity control and to reduce energy consumption of the condenser refrigeration units by at least 30% annually.
Open ground source loop
In 2009, the institution decided to move forward with an ambitious HVAC system upgrade in the form of a direct expansion (DX) split unitary system for cooling and heating the interior space of the laboratory.
A ground source heat pump system was selected to upgrade the HVAC with ground source condenser water because the lab did not allow for an unattractive cooling tower and because this system can achieve much greater energy efficiency than a DX split system.
These water source heat pump systems are efficient at transferring heat, when used in conjunction with a plate and frame heat exchanger that maintains a very small temperature difference between the ground loop and building loop. Water source heat pumps recover excess heat from the building’s interior and move it to the building’s perimeter. They are also quite suitable for New York, whose aquifers produce a lot of water.
An open loop ground source water system is also known as a “pump and dump” system. With an open loop system, the groundwater is pulled up from one supply well (the “pump” well) and pumped through a plate and frame heat exchanger, then it is pumped back to the “dump” injection well. See Figures 2 and 3 for a diagram of the mechanical room and schematic description of the open loop system.
Design and optimization
A plate and frame heat exchanger offers high thermal performance because the corrugated pattern is pressed into each plate to produce highly turbulent fluid flows; this also allow specification of a very small approach temperature (as low as 1 to 5 F), which is sometimes useful in a ground source water application.
Described below is a three-step algorithm to properly select, design, and optimize the heat exchanger to achieve the best value of the ground source water temperature variation. It is based on the authors’ experiences from past projects in both the U.S. and Canada.
Step 1: To select a heat exchanger, the engineer must know five of the six parameters:
- Heater capacity
- Temperatures on the hot side (in or out)
- Temperatures on the cold side (in or out)
- Flow rate on the cold side and/or hot side
Based on five known parameters, calculate the capacity and surface area required for transferring heat to the media using the following equations:
Q = U x A x LMTD
Q = gpm x 500 x P x C x CF x ∆T
Q = heat load (capacity) in Btu/hr
U = overall heat transfer coefficient in Btu/Hr/sq ft/F
A = heat transfer area in sq ft
LMTD = logarithmic mean temperature difference in F
gpm = flow rate in gallons per minute
P = specific gravity
C = specific heat in Btu/lb F
CF = fluid correction factor to take into account changing specific gravity and specific heat
∆T = fluid temperature rise in F
The value for the LMTD is strongly influenced by the direction of the media flow. The most effective configuration is a counter flow configuration in which fluids flow in opposite directions.
The LMTD can be calculated using the difference between the incoming and outgoing temperatures of the two fluids (the hot water side and the cool water side) according to the following equation:
∆T = T1 – t2 temperature on the hot side end
∆t = T2-t1 temperature on the cold side end
The number of transfer units (NTU) is a dimensionless value that characterizes the performance of a heat transfer based on the LMTD and the temperature change occurring in the unit.
The importance of the NTU value lies in the fact that heat exchangers are capable of generating a given NTU for each fluid, and this value is dependent upon their specific plate construction.
The pressure drop through the plate depends on type of the corrugation, which can be predicted using the following equation:
If NTU > 3 (long angle corrugation patterns). Those plates have the highest heat transfer rate and highest pressure drop.
If NTU ≤ 3 (short angle corrugation patterns). Those plates have lowest heat transfer rate and lowest pressure drop.
Select the small heat exchanger model capable of handling the flow, surface area, and NTU for the winter conditions and summer conditions of the ground source water.
Step 2: Compare the surface areas calculated in step 1, equation 3, for winter conditions and summer conditions. Choose the model with the largest surface area between the two seasons (for instance, winter conditions).
Step 3: Using the heat exchanger model selected (winter heat exchanger) in step 2, simulate the flow and temperature of the smallest surface area (summer condition) on the heat exchanger model with the largest surface area (winter heat exchanger).
Based on our experiences, an acceptable deviation of the inlet and outlet temperatures of the heat exchanger is approximately +/- 3 F. If the inlet and outlet temperatures are close to the acceptable value, a solution has been achieved; otherwise, repeat step 1 and continue until a solution can be reached that is closer to the deviation point.
Most plate manufactures typically use 30 F angles for short angle patterns and 60 F angles for long angle patterns in forming the plate corrugation.