Question: Submit online. For this homework, you will use either Excel or EES to simulate the system, calculating pipe pressure loss and fitting pressure loss. You

Submit online. For this homework, you will use either Excel or EES to simulate the system,
calculating pipe pressure loss and fitting pressure loss. You will also simulate the system to estimate
flow rates in the components.
Creeping bentgrass is used for putting greens on premier courses. Bentgrass is a cool climate grass,
and we are at the southern edge of where it can grow. In recent years, some golf courses have
installed ?1 "greens cooling systems" that circulate chilled water in tubing beneath the greens' surface
to improve the grass quality. As far as I know, these systems have used custom air-to-water chillers
air-to-water heat pumps. It may also be desirable to provide turf heating under some conditions,
so a reversible heat pump may be favored over a chiller
Such a system is being installed for Karsten Creek. Rather than using air-to-water heat pumps, which
can be noisy and inefficient, water-to-water heat pumps are being used. Closed-loop ground-source
heat pump systems are being installed for each putting green. The system (shown in Figure 1) has
the following proposed components on the source-side. (For this homework, we won't consider the
load-side - the tubing that cools the greens.)
For this homework, we will consider a "laboratory-scale" system that could be used for experiments
and model validation. Rather than conditioning a full-size putting green, we will design a system
that could be used with a smaller putting green -25'40'-1000ft2
Water-to-water heat pump. For this homework, we are using a ClimateMaster Tranquility ?
Water-to-Water heat pump, model TMW060. This is expected to be able to condition about
4000 sq . ft . of greens - this would be one of multiple systems used to condition the greens.
The proposed design flow rate is 15 GPM; the heat pump entering fluid temperature on the
about 95F.[Note the TMW060 performance data on page 18 of the submittal set PDF is for
water. As shown on page 33, the pressure drop with 20% methanol is 15.4% higher than for
water
Working fluid. 20% methanol antifreeze is being used. You may assume a mean fluid
temperature of 95F35C
Boreholes. The original plan was to drill two 600 feet boreholes with 114" U-tubes, but
instead we ended up with the closer (to the heat pump) borehole being 500' deep and the
farther borehole being 700' deep.
Connecting piping. Figure 2 shows a layout for the piping. The dimensions are: x=30';B=25',
zt=5'. The horizontal connecting piping between the heat pump and the first borehole is 2''
SDR-11 HDPE. The horizontal connecting piping between the first and second boreholes is 1
14"SDR-11 HDPE
Circulating pump(s) To be selected
To receive full credit on this assignment, you must: (1) Number each section exactly matching the
numbering below, and present everything for that section in the section. Do not put figures at the
end of the document; do not use appendices. Everything for each section has to be presented in
that section. (2) Provide sufficient (but brief) narrative of how you arrived at each solution, showing
work as needed. It should be possible for the person grading your assignment to quickly ascertain
your methodology without reading your mind. (3) present your work legibly - if your handwriting is
not considerably neater than Dr. Spitler's you should do it all in Word and Excel! Any scanned work
has to be clearly readable.
Develop a simple model for the heat pump pressure loss. Explain your model and
prepare a plot showing the model behavior and the manufacturer's data points,
corrected for the actual methanol concentration.
Find the K values for the fittings and summarize in a table. I've labeled the fittings
that you will include in Table 3. In the table, show the fitting code, diameter, K value
and design flow rate. (Fitting codes are "E1","U2", etc. For T1 and T2, please
indicate straight or branch, e.g."T1-branch".) We will consider elbows, tees, and U-
bends. Reducers and expanders are needed, but their head loss is very small, so we
will neglect them. You may assume the tees are 1114?" diameter and the
reducers/expanders are on the heat pump side of the tees.
Determine the required head of a pump that will give a total flow of 15 GPM
Select a Taco circulating pump from Fig. 3. For purposes of this assignment, you
should select a minimally oversized pump. It is likely that no available pump wi
meet the design requirements. In this case, select the pump
Submit online. For this homework, you will use

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