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Hagen-Poiseuille law Hagen-Rubens relation, between electrical and optical constants, Hall Taylor, N S, Halogenated hydrocarbons: Handley and Heggs equation for fixed bed pressure drop, Hankinson and Thomson method, for liquid density: Hardening (precipative) of stainless steels, Hardwick, R, Harris, D, Hausen equation for developing laminar flow, Hays, G F Headers in shell-and-tube heat exchangers, Heads, in heat exchangers: Heat and mass transfer: Heat exchanger design, introduction, Heat exchangers: Heat of vaporisation (see Enthalpy of vaporisation), of pure substances Heat pipes: Heat pumping, relation to heat exchanger network design, Heat storage (see Regenerators and thermal energy storage) entropy generation in, Heat transfer: Heat transfer coefficient: Heat transfer media, Heat transfer salt, Heat transfer regimes: Heat of vaporization, Heated cavity reflectometer, Heating media, for reboilers, Heavy water, physical properties of, Heggs, P J, Helical coils of circular cross section: Helical coils of rectangular cross section, Helical inserts, for enhancement of heat transfer in boiling, Helium: Helmholtz reciprocity principle, in radiative heat transfer, Henry, J A R, Henry-Fauske model, for critical two-phase flow, Henry's law, for partial pressure, Heptadecane: Heptadecene: Heptane: 1-Heptanol: 1-Heptene: Herman, K W, Hermes, C L L, Heterogeneous conveyance in horizontal pipes, Heterogeneous nucleation in boiling, Hewitt, G F Hexachloroethane (Refrigerant 116): Hexacyclopentane, superheated vapor properties, Hexadecane: Hexadecene: 1,5-Hexadiene: Hexagonal cells, in free convection, Hexamethylbenzene: Hexane: Hexanoic acid: 1-Hexanol: 1-Hexene: Hexylbenzene: Hexylcyclohexane: Hexylcyclopentane, Hicks equation, for fixed-bed pressure drop, High pressure closures, ASME VIII code guidance for, High-chrome steels, thermal and mechanical properties, High-finned tubes, correlations for single-phase heat transfer in flow over, Hills, P D Hohlraum cavity, Holdup, in liquid-liquid flow, Holland, guide to national practice for mechanical design of heat exchangers, Homogeneous condensation (fog formation), Homogeneous model: Homogeneous nucleation: Honeycombs: Hopkins, D, Horizontal condensers: Horizontal cylinders: Horizontal layers, of fluid, free convection heat transfer in, Horizontal pipes: Horizontal shell-side evaporator, Horizontal surfaces: Horizontal thermosiphon reboilers: Horizontal tube-side evaporator, Horizontal tubes: Hottel's rule, in absorption of radiation by gases, Hsu criterion, for onset of nucleate boiling, Hybrid cooling towers, Hydraulic conveyance: Hydraulic expansion, of tubes into tube sheets in shell-and-tube heat exchangers, Hydraulic turbine, lost work in, Hydraulic resistance, in flow of supercritical fluids, Hydraulically smooth surface, Hydrazine: Hydrocarbons: Hydrodynamic entrance length, in single-phase flow in ducts, Hydrogen: Hydrogen bromide: Hydrogen chloride: Hydrogen cyanide: Hydrogen fluoride: Hydrogen iodide: Hydrogen peroxide: Hydrogen sulfide: Hydrostatic testing of shell-and-tube heat exchangers, Hysteresis:
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Two-Phase Loop with Capillary Pump

DOI 10.1615/hedhme.a.000318

3.10.9 Two-phase loop with capillary pump

A. Introduction

The Two-Phase Loop with Capillary Pump (Figure 1) is a passive heat transfer device and is a form of heat pipe. Phase change take place in the regions of heat input (evaporation) and heat rejection (condensation). Thermal energy is transferred in latent form by vapor and condensed liquid is returned back by action of capillary forces (a unique characteristic of a heat pipe). The distinguishing characteristics of the Two Phase Loop with Capillary Pump are the placement of a capillary structure only in the evaporator and the presence of separated channels for vapor and liquid. There are no counter flows of vapor and liquid as in the classical heat pipes but only unidirectional flows in a closed loop. The separation of the vapor and liquid flows allows a significant reduction of the viscous pressure losses in the shielded (adiabatic) section (smooth wall tubing is usually used as the channels), and the elimination of entrainment of liquid by vapor, in comparison with classical heat pipes. The placement of the capillary pump in the evaporator allows the use of micron-size porous structures, which are capable of developing a very high capillary head. Sintered metal powder capillary pumps manufactured in the Institute of Thermal Physics (Ekaterinburg, Russia) are shown on Figure 2. The normal effective pore radii of such capillary pumps for Two Phase Loops are in the range 0.520 microns.

Figure 1 Functional schematic of two-phase loops with capillary pump

Figure 2 Sintered metal capillary pumps for Two-Phase Loops

The heat transfer in the evaporator can be organized in two ways: (1) the traditional way, where liquid evaporates from outer wick surface (Philips and Grove, 2003) (Figure 1a) and (2) by evaporation from an "inverted meniscus" where heat and mass flows in the wick have opposite directions (Figure 1b and c). The second approach is used in the great majority of the evaporators in todays Two-Phase Loops with Capillary Pumps. The phenomenon of "inverted meniscus" evaporation was considered in detail by Philips and Grove (2003) and Khrustalev and Faghri (1996). To reduce the wick hydraulic resistance (to minimize the flow path of the of liquid in the porous structure) a central core is usually inserted into the capillary pump (Figure 1c). However, an evaporator without a central core (Figure 1b) also has certain advantages such as preventing undesirable boiling in the wick body and the possibility to design compact flat evaporators for high-pressure working fluids (Philips and Grove, 2003). Due to their specific features, Two-Phase Loops with Capillary Pumps are more flexible and can transfer much higher heat fluxes over much longer distances than classical heat pipes. The Loops are capable of effective operation against gravity (up to several meters) or other body forces [one of the first names for such devices was "anti-gravitational heat pipe" (Philips and Grove, 2003)]. Because the heat pipe is a precursor and close cousin of the Two-Phase Loop with Capillary Pump it is logical to call this class of devices "heat loops" for consistency (Philips and Grove, 2003).

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