ASHRAE OR-16-C044-2016 In-Situ Testing of Shallow Depth Helical Heat Exchangers for Ground Source Heat Pump Systems.pdf
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1、 Francisco Javier Alvarez-Revenga is a Masters Student in the Department of Mechanical they are marked as 10, 11 and 12 in Figure 2. A trench was dug to collect all the pipes and lead them towards the mechanical room, which is located in the northeastern corner of the house print, in the basement. C
2、onsequently, there is approximately 128 ft (39 m) of horizontal runs, which were insulated with closed-cell foam insulation. Figure 2 Location of the geothermal boreholes at the residence. Boreholes marked as 1, 2, 3 and 4 correspond to the location of the deep vertical probes and 10, 11 and 12 repr
3、esent the location of the three helical heat exchangers Local soil formation conditions were determined through well logs and ground thermal response tests at the time of the building construction. According to the well log reports, the soil corresponding to the helical bores was classified as moder
4、ately plastic and sticky clay (CL). The conductivity test for the deep boreholes showed a thermal conductivity of 1.26 Btu/(hrftF) (2.18 W/(mK). Temperature sensors were located on the pipes just after they entered the mechanical room in order to measure the entering water temperature (EWT) and the
5、leaving water temperature (LWT). Data was acquired at 30 second intervals. A weather station was installed at the test site to collect outdoor conditions during the study. Some outdoor conditions were determined by using data from the National Oceanic and Atmospheric Administration databases (NOAA 2
6、015). Global horizontal solar radiation was retrieved from average hourly statistics provided by energy modeling software for the Gallatin Field weather station location, near Bozeman, MT (EnergyPlus 2015). Field Testing In-situ tests were performed during both heating and cooling seasons. The heati
7、ng and cooling mode tests spanned over 5 days (February 9th to 14th, 2015) and 3 days (August 2nd to 5th, 2014) respectively. During the heating mode test, the GSHP was initially switched on so it would take care of the heating load of the building using its own internal controls. The residence has
8、comprehensive building automation systems that allow the user to control the systems in a very flexible manner. These control sequences were configured in such way that the GSHP maintained a given setpoint in the 120 gal (450 L) buffer tank. From the buffer tank, a secondary loop connects the differ
9、ent building zones. In this case, a radiant floor heating (RFH) system was used to heat up the building spaces. This control strategy resulted in the system cycling and providing intermittent heating pulses. To explore the long term performance of the heat exchanger, a steady heat load was applied t
10、o the system, in a similar process to that of a formation thermal conductivity test (ASHRAE 2011). In order to achieve this, the digital control system was set to provide a steady supply of energy to the building. This control strategy leads to the system working constantly (compressors continually
11、running). The GSHP energy output was estimated based on the temperature of the ground being as steady as possible within reasonable ranges to ensure the loads could be sustained for long periods of time. The cooling mode test had a similar approach, but in this case only the steady state situation w
12、as explored. Conditions and parameters during the tests are summarized in Table 1. Table 1. Parameters During The Tests Description Value (SI Units) Value (I-P Units) Geothermal Fluid Total Mass Flow Rate in Loop (Heating Test Cooling Test) 0.63 0.57 kg/s 4990 4514 lbm/hr Specific Heat 4061.2 J/(kgK
13、) 0.97 Btu/(lbmF) Thermal Conductivity 0.48 W/(mK) 0.28 Btu/(hrftF) Kinematic Viscosity 2.710-6 m2/s 2.910-5 ft2/s Density 1023.9 kg/m3 63.92 lbm/ft3 Layout and Geometry of Heat Exchanger Type of Probe Helical Number of Probes 3 Spacing 3.4 m 11 ft Depth of installation 1.8 m 6 ft Length of Probe 3.
14、7 m 12 ft Diameter of Borehole 0.46 m 18 in Diameter of Helix 0.38 m 15 in Pitch between Turns 0.11 m 4.3 in Total Length of Pipe 40 m 131 ft Material of Pipe PEXa Inside Diameter 22.2 mm 0.875 in Outside Diameter 28.6 mm 1.125 in Density of Material 940 kg/m3 58.68 lbm/ft3 Thermal Conductivity of M
15、aterial 0.41 W/(mK) 0.24 Btu/(hrftF) Thermal Properties of the Ground Estimated Thermal Conductivity 2.18 W/(mK) 1.26 Btu/(hrftF) Estimated Specific Heat Capacity 1275.6 J/(kgK) 0.305 Btu/(lbmF) Estimated Density 1760 kg/m3 110 lbm/ft3 Backfilling Material Native Soil (No grout) Climate Data of Loca
16、tion Location Bozeman, MT Air Temperature From On-Site Data Acquisition System Solar Radiation From EnergyPlus Database Annual Mean Temperature 7C 44.6F Annual Variation (Semi-amplitude) 12.2C 21.9F The Model The independently developed CaRM numerical simulation tool was used. The CaRM simulation to
17、ol is based on the electrical analogy, where the domain (comprised of ground, grouting material and ground heat exchanger) is discretized with thermal capacitances and thermal resistances that link the thermal nodes (see Figure 3). Then, for each thermal node the heat balance equation is written, ob
18、taining a linear system with as many equations as unknown temperatures. The CaRM simulation tool has been highly improved from the first release reported in De Carli et al. (2010). In this study, the current version of this simulation tool (Zarrella and De Carli 2013) was used. The approaches define
19、d in this model account for the axial heat transfer (within both the ground and grouting material), the effect of surface conditions, convection, and short- and long-wave radiation heat transfer. These new features make it possible to investigate even short length borehole heat exchangers. The model
20、 can also be used for short-term analysis because the thermal capacitance of the borehole heat exchanger (both the grouting material and the heat carrier fluid) is considered. The actual geometry of the helical pipe (pipes length and pitch between turns) is modeled (see Figure 3-B). The details of t
21、he model are described in the reference (Zarrella and De Carli 2013). Figure 3 Approach of CaRM: A) overall approach, B) particular of helical pipe modeling (CaRM-He) Results Experimental Results Measured entering water temperature (EWT) and leaving water temperature (LWT) were plotted together with
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