Loop heat pipe (LHP) is a robust thermal transfer device for cooling electronic components . Figure 1 shows the schematic of LHP. A LHP consists of one evaporator (Evap), one vapor line (VL), one condenser (Cond), one liquid line (LL), one compensation chamber (CC) and one primary wick (PW).
Figure 1.Schematic of LHP.
The LHP employed the capillary force which generates in the porous structure to drive the inner working fluid. With the circulation and phase change of working fluid, the heat can be transported from evaporator (receiving heat from operating machine) to condenser (dissipating heat to outside, which is often embedded into radiator).Compared with conventional heat transfer device, LHP is free of electricity and can transfer more heat with longer distance. With its merits, the LHP has been applied in several spaceships . Multiple loop heat pipe (MLHP) is a kind of LHP which has multiple evaporators and multiple condensers, it has been demonstrated in the year 1997 . The mathematical models has been established in the year 2004, 2005  .
The MLHP has not been utilized as a thermal control device for spaceships because the operating characteristics have not been totally confirmed. According to the literature, the related research is rare. Only one experiment on investigation was developed in America . This research aims to demonstrate and figure out the operating performance of MLHP. In this research, firstly, a MLHP with two evaporators and two condensers for space demonstration was designed and fabricated. Then the thermal vacuum test was carried out to figure out the operating performance of MLHP with working fluid ammonia under the case that both evaporators were heated/one evaporator was heated and bothradiators were operated with the same heat load. The tests to confirm the performance of flow regulator (FR, a device to regulate the mass flow rate at each condenser side in the case that the temperature difference exists between two radiators. with ultra-high weight molecular (UHWM) polyethylene porous structure were also conducted under the case that both evaporators were employed with the constant heat load and one condenser was heated by flexible heater. The tests to demonstrate the startup behavior at low heat load (5W) with preheating were carried out under the case that one evaporator was heated with 5W and each radiator was heated with 60W to keep warm.
2. Operating Principle of Multiple Loop Heat Pipe
Figure 2 shows the schematic of MLHP. Compared with LHP, MLHP has two operating patterns. The Figure 2(a) shows the case that two evaporators are heated. In this case, the MLHP operates like LHP, the heat was absorbed from working machine to evaporators, then the evaporation happens and the vapor was generated. The vapor flows through the vapor line then condenses in the condenser and dissipates the heat to outside. Finally, the condensed working fluid flows back to evaporator, replenishing the evaporation volume. Since the MLHP has several evaporators, it can cool several heat sources or a heat source with large footprint. Figure 2(b) shows the case that one evaporator is heated. In this case, the flowing direction of working fluid in the unemployed evaporator is inversed, making the un-employed evaporator work as a condenser. In this way, the operating evaporator can provide the heat to unemployed evaporator, keeping the unemployed evaporator warm. The MLHP has two condensers. Therefore, compared with LHP, MLHP can operate in the case that one radiator`s temperature is too high to diffuse the heat, by diffusing the heat through the other radiator In this case, the flow regulator becomes necessary.
Figure 3 shows the schematic of flow regulator, there is a porous structure in flow regulator, the porous structure can only permit liquid to flow through. Therefore, the uncondensed vapor which flows through the high temperature condenser side is blocked and diverted to low temperature side. In this way, more working fluid can flow through the low temperature condenser side, making the low temperature condenser fully utilized and reducing the temperature of returning liquid, which can make the whole loop operate at lower temperature. Equation (1) shows the flow regulator’s operating condition.
Figure 2. Schematic of MLHP. (a) Both evaporators are employed; (b) One evaporator is employed.
Figure 3. Schematic of flow regulator.
The presents the capillary force of the porous structure, the presents the pressure loss from the diverging point of common vapor line to the confluence of common liquid line (except the pressure loss which is generated when working fluid flows through the flow regulator) and the presents the pressure loss generated by porous structure in flow regulator.
3. Multiple Loop Heat Pipe Equipment and Test Conditions
Table 1 presents the configurations of MLHP, the MLHP is designed to transport 260 W in total (130 W/eva- porator) for 1.5 m. The primary wick was made of stainless steel and the flow regulator’s porous structure was made of UHWM polyethylene. In the thermal vacuum test, the MLHP was wrapped with Multi-layer insulation (MLI) material except the radiation side of radiator. Each condenser was embedded into the radiator in order to enhance the heat diffusing ability. Both radiators were painted black with Z306 flat black to improve the emissivity. The flexible heaters with the size of 30 cm × 30 cm were pasted on the center each radiator to keep the radiator warm when MLHP operated at low temperature and to simulate the heat from sunlight.
Figure 4 shows the position of thermocouples (TC) and Figure 5 presents the photo of MLHP. In this experiment, the ammonia was applied as working fluid, 53 thermocouples were employed to measure the temperature of MLHP equipment. The thermal vacuum chamber was kept under −180˚C and 10−5 Pa.
Table 2 shows the experiment conditions. The heat loads with each evaporator and radiator are shown respect tively. The test 1 was conducted to demonstrate the operation of MLHP and measure the largest heat transport capability figure out the heat transfer ability of MLHP with the working fluid ammonia. The test 2 was carried out to confirm the heat transfer ability of each evaporator and demonstrate the heat exchange between two evaporators. The test 3 was conducted to demonstrate the operation of flow regulator with UHMW polyethylene. The test 4 was carried out to demonstrate the startup behavior of MLHP at low heat load with preheating. The tests were stopped when the MLHP reached its capillary limit or the temperature of any component rose above 70˚C.
Figure 4. Thermocouples’ position.
Table 1. Configurations of MLHP.
Table 2. Experimental conditions.
Figure 5. Photo of MLHP.
4. Test Result
4.1. Test Result of Case 1
Figure 6 shows the steady state behavior of MLHP under the condition that two evaporators were heated and two condensers were operated without heat loads. The x-axis shows the heat loads and the y-axis presents the temperature of evaporator and compensation chamber at each heat load. Judging from the Figure 6, the MLHP can transport 240 W in total (120W/evaporator) for 1.5 m. Therefore, the operation of MLHP was demonstrated. The calculations was done in the case that two evaporators’ temperature were 100/100 W, 110/110 W, 120/120 W. It can be inferred that the calculations agrees well with the test results. The MLHP’s heat transport ability was not attainted the designing goals (130/130W). The reason is that with the rising of heat loads, the temperature rose and deteriorated the adhesives between heat blocks and evaporators. When the heat loads rose to 130/130 W, the heat block1’s temperature rose above 200˚C and the evaporator 1’s temperature rose above 70˚C, then the experiment was stopped. According to the test result, the thermal conductance between evaporator1 and heat block1 at 80/80 W, 100/100 W, 110/110 W and 120/120 W were 884 W/˚C, 818 W/˚C, 831 W/˚C, 609 W/˚C, respectively. Therefore, it can be found that when the heat loads rose to 120/120W, the adhesive strength of adhesives began to deteriorate. To avoid this problem, in the future research, the adhesives which can tolerate high temperature will be utilized.
4.2. Test Result of Case 2
Figure 7 shows the steady state performance of MLHP under the condition that only evaporator 2 was heated. The x-axis shows the heat load, the left y-axis presents the temperature of evaporator and compensation chamber at each heat load and the right y-axis presents the heat loads at two radiators which were used to keep warm. Because of the deterioration of adhesive at high temperature, the experiment was continued until the heat load at evaporator 2 side rose to 120W. The calculations on the temperature of each evaporator and compensation chamber were conducted respectively. Judging from the Figure 7, it can be found that the temperature of evaporator and compensation chamber was well predicted. In the calculations, the MLI was supposed to insulate the heat totally between MLHP and thermal vacuum ambience. However, there existed the radiation to outside actually. As the result, the unemployed evaporator needs the heat from employed evaporator to keep warm. The heat exchange volume can be evaluated through Equation (2). The presents the temperature at the inlet of unemployed evaporator (Thermocouple 9), the presents the average temperature of unemployed evaporator. The denominator at the right side of the equal sign presents the heat resistance from the porous structure to the inner wall of evaporator and the heat resistance between the evaporator case. The presents the thermal transfer coefficient between the stainless steel primary wick to the inner wall of evaporator.
Figure 6. Temperature at steady state of test 1.
Figure 7. Temperature at steady state of test 2.
According to the Equation (2), assuming that the was 350 W/ , the heat exchange amount was about 3 W when the heat load on evaporator 2 varied from 60 W to 120 W. The heat exchange amount will rise if the MLI at unemployed evaporator is removed. The test that only evaporator 1 was heated showed the same operating characteristics unless the largest heat transfer value became to 80W because of the deterioration of adhesives.
4.3. Test Result of Case 3
Figure 8 shows the temperature profile of the MLHP under the condition that the heat loads at both evaporators’ side were kept at 40/40W and the radiator 1 was heated. Figure 9 shows the detailed temperature profile of thermocouples those were pasted near flow regulator. The x-axis shows the time, the left y-axis shows the temperature and the right y-axis presents the heat load at two radiators. The steady state temperature of the entrance and exit of each flow regulator (FR1: TC29, TC30; FR2: TC31, TC32) and the steady state temperature of the liquid line`s confluence (TC 35) with the variation of heat load at radiator 2 was shown at Table 3.
Figure 8. Temperature profile of test 3 (MLHP).
Figure 9. Temperature profile of test 3 (FR).
Table 3. Steady state temperature of flow regulator component.
Judging from the Table 3, when the heat load at radiator 1 was 40W, the temperature of liquid line confluence was close to the FR1, which shows that the all the vapor was condensed in the condenser. When the heat load kept rising, the temperature of liquid line`s confluence began to close to the FR2, which indicated the flow regulator 1 operated and prevented the high temperature vapor, which makes more and more working fluid flows through the unpowered radiator. Since the temperature of liquid line’s confluence was not risen sharply and was kept close to the FR2’s temperature, the operating characteristics of FR in this MLHP was demonstrated. From the calculation, in the case that the heat load on the radiator 2 was 160 W, the pressure loss from the diverging point of vapor line to the confluence of liquid line was 4047 Pa. The contact angle at the FR 1 was 75.6˚, which can be calculated by Equation (3).
In the case that the radiator 2 was heated, the FR2 was operated in the same method. However, the FR2 can only tolerate 100 W heat load which was supplied to radiator2. One of the probable reason is that the sealability between the FR2’s porous structure and the inner wall of FR2 was not good.
4.4. Test Result of Case 4
When the temperature difference between evaporator and compensation chamber reaches a certain value (superheat), the bubble generates into the evaporator and the MLHP begins to operate. It is difficult for a MLHP to start up at low heat load because the heat leak from the evaporator to compensation chamber is high, which makes the superheat cannot be attained. To improve the startup behavior at low heat load, the compensation chamber was preheated to change the distribution of working fluid, which can transport the liquid from compensation chamber to the core of primary wick and reduce the heat leak. Figure 10 shows the temperature profile of the MLHP under the condition that the MLHP started at low heat load (5 W) at evaporator2without preheating at compensation chamber 2. The x-axis shows the time while y-axis presents the temperature. Figure 11 shows the temperature profile of the MLHP under the condition that the MLHP started at low heat load (5 W) at evaporator2 with preheating at compensation chamber 2. The x-axis shows the time while left y-axis presents the temperature. The right y-axis shows the heat load of preheating. The test without preheating was continued 20 minutes. In the test period, the temperature of vapor line did not increase, therefore, the MLHP cannot startup. While in the case with preheating compensation chamber at 2W for 4 minutes, the MLHP started up 5 minutes later when the temperature of vapor line2 began to increase. The vapor reached the inlet of condenser1 31 minutes later from the startup. The MLHP operated in steady state at 50 minutes after the startup. Therefore, the startup behavior at 5W was demonstrated with preheating on compensation chamber. The preheating experiment at evaporator1 and compensation chamber1 was carried out too and showed the same result with the preheating experiment at evaporator2 and compensation chamber 2.
In this research, the operating characteristic of MLHP under thermal vacuum condition was experimentally investigated. In the case that both evaporators were employed, the MLHP was demonstrated and can operate stably, transporting 240 W in total for 1.5 m. In the case that one evaporator was employed, the heat exchange be-
Figure 10. Temperature profile of test 4 (without preheated).
Figure 11. Temperature profile of test 4 (preheated).
tween two evaporators was confirmed. The tests with the temperature difference between two radiators were conducted and the working performance of flow regulators were evaluated. The startup behavior at low heat load with preheating compensation chamber was demonstrated.
This research is partially supported by H. Ogawa, S. Okazaki from ISAS, H. Nagai from TOHOKU University. The author would like to express his sincere thanks to them.
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