HPHE |
Yau et al., 2015 [136] |
HPHE with 2, 4, 6, and 8 numbers of rows were tested. The coil face velocity was 2 m/s and the return air temperature was at 24 °C. The results of the HPHE were recorded for one week. |
The results showed that a total amount of 2885 kWh can be saved yearly; this amount can be raised to 7023 kWh per year if eight-rows HPHX was used. The volumetric flow rate is increased, and a higher amount of energy recovery is expected as the face velocity is increased, but this results in a higher-pressure drop in the coil, which decreases the effectiveness. |
Firouzfar et al., 2011 [137] |
HPHE is placed in two streams of fresh air (32–40 °C) and return air (26 °C) in AC. Ratios of mass flow rates 1, 1.5, and 2.3 were tested to observe heat transfer and change in the temperature of fresh air. |
The heat transfer and effectiveness rate of both the condenser and evaporator sections were raised to 48%. |
Sanaye et al., 2014 [138] |
A HPHE, made from copper with water as working fluid and wick structure of 10 sheets of the 100-mesh bronze screen, is placed horizontally to recover heat from the exhaust air, in heating mode, and transfers it to the cold inlet fresh air; whereas, in cooling mode, it pre-cools the hot inlet fresh air. |
The optimal point is with the effectiveness of 0.774 and a total cost of $1474, with a return period of about 2.5 years. |
Ahmadzadehtalatapeh, 2013 [139] |
TRNSYS software was used to study the hourly influence of HPHE on HVAC. Eight-row HPHE was added with an average of 22.4 °C indoor temperature and 54.5% indoor air relative humidity (RH). |
The results revealed that by reheating and pre-cooling, a total amount of 236.9 MWh energy could be saved yearly. This amount results in saving $24,572 annually. |
THE |
Firouzfar et al., 2011 [137] |
3-row THE was investigated which consists of 48 wickless heat pipes organized in 6-row. |
The cooling capability for the system was improved by 20 to 32.7%. In an evaporator and condenser, the equal value of air face velocities should be avoided. |
Guoyuan Ma et al., 2013 [140] |
THE is used in an AC system for outlet air heat recovery in a shopping mall in Beijing. |
The results show that the seasonal temp effectiveness (STE) is 66.08% in winter and 55.43% in summer. |
Jouhara et al., 2018 [92] |
Wraparound loop heat pipes (WLHP), are thermosiphons which are used commercially. It depends on gravity to return the condensed liquid. HP filled with R134a and water were investigated at two different air velocities: 2.56 m/s and 2.6 m/s. |
The results show that the effectiveness declines with the rise of air velocity. The effectiveness of the HP filled with water varied from 20.14% to 19.61%, whereas it varied from 13.76% to 13.25% when it is filled with R134a. This means water HP was 46 to 48%, which is greater than R134a. |
Vanyasreet al., 2017 [141] |
Thermosiphon of an outer diameter of 16 mm, and 570 mm long is used with a working fluid de-ionized water. Different flow rates are set in the test 10 mL/s, 15 mL/s, and 20 mL/s for various heat inputs of 155 W, 200 W, 250 W, and 300 W and different inclinations 30°, 45°, and 90°. |
A comparison was done on the results obtained, and it was concluded that in thermosiphon, 45° is more efficient than other inclinations when de-ionized water is used as a working fluid. |
PHP/OHP |
Mahajan et al., 2017 [142] |
OHP consists of multiple finned OHP, organized in a staggered way (to increase the heat transfer). Typical HVAC is studied at 60.96 × 45.72 cm2. The ducted air streams have a constant volumetric flow rate of 1.18 m3/s opposite to each other. The outdoor temperature is assumed to vary between −8 °C and 48.9 °C. |
The results show that the OHP system is energy and cost-effective since a reduction of total average consumption was observed, around 16% yearly. OHP can save, annually, more than $2500 in cities that have continental (warm to hot summer and severe cold winter) climatic conditions |
Supirattanakul et al., 2011 [143] |
Copper tubes closed-loop (CLOHP) was used with a diameter of 2.03 mm. Indoor design temperature varies between 20 and 27 °C with 50% RH. R134a, R22, and R502 refrigerants were used as working fluids. |
When R134a was used as the working fluid, heat flux increased to 5.19 kW/m2 at a temperature of 27 °C. The CLOHP/CV resulted in an increase in the surface area and the heat capacity of the base fluid. |
Govinda Mahajan et al., 2015 [144] |
OHP-HE was studied with a 70% fill ratio of n-pentane. The performance of OHP was compared with the empty tube, i.e., at vacuum pressure having the same overall dimension. |
The results indicate that OHP can recover up to 240 W of heat from the waste exhaust air stream, with a low-pressure drop of almost 62 Pa in the cold air stream. The heat transfer rate with 70% n-pentane is two times that of the evacuated OHP. |
Pachghare, 2016 [101] |
Closed loop pulsating heat pipe (CLPHP) consists of 10 turns of copper tubes of ID = 2.0 mm and OD = 3.6 mm. The evaporator, condenser, and adiabatic sections have a length of 50 mm. Different working fluids are used as methanol, R-134a, and water. |
With R134a working fluid, PHP indicates, at all orientations, better thermal performance than water and methanol. When using water as a working fluid, PHP shows a negligible inclination angle effect, whereas, with methanol, a significant effect is detected since the better thermal performance was observed in a vertical position than the horizontal one. |
Chawane et al., 2013 [70] |
PHP performance is compared by using three different working fluids: ammonia, water, and acetone. |
Water-filled devices showed higher performance as compared to R-123 and ethanol in a vertical orientation. Ammonia shows desirable characteristics for heat transfer, as it has a high freezing point. |
Patil et al., 2016 [71] |
OHP experiment was done in three different conditions: window, indoor, and outdoor. The working fluid used has a boiling point around 25 °C to deliver a suitable temperature. |
The power consumption obtained is around 109 W (less than one ceiling fan). Outlet air temperature and humidity cannot be controlled, due to the inability to control the mass flow rate of the refrigerant. |
Barua et al., 2011 [145] |
Mathematical models of falls in temperature in the condenser section were established concerning time for different diameters D and lengths L of the pipes of the evaporator sections. |
Temperatures decline exponentially. For a fixed D, the temperature drop depends on the length of the evaporator. For a fixed L, the temperature reduces faster for the smaller diameter of the pipe. |
Runaround coil |
J. Wallin et al., 2012 [61] |
A summary on increasing the performance of transferring energy through run-around coil ventilation HRS. Studies have also investigated the methods to improve heat pump units by decreasing the energy used; this was done by conducting a modified design of a three-stage heat pump to the system the heat recovery rate per year which was obtained in Stockholm. |
The Annual HR rate was improved from 47% to 66%. The system shows considerable and affordable results, for the three-stage heat pump design, the payback period was 5.7 years, for the variable heat pump capacity design 6.2 years. |
R. Zaengerle, 2012 [95] |
Integrated system of energy recovery with cooling and heating devices of runaround coil studied in cold climates. |
This system is very valuable to recover energy in cold climates, and, thus, decreasing the power of the fan. |