an osmotically pumped heat pipe 10 shown in fig1 includes a solution reservoir assembly 12 including an evaporator , a solvent reservoir assembly 14 coupled to solution assembly 12 by a membrane assembly 16 and a mixing manifold 18 , a condenser assembly 20 , and tubing interconnecting the assemblies in a closed circuit . heat is inserted into the system at solution reservoir assembly 12 , as denoted by the symbol &# 34 ; q &# 34 ; whose arrow is directed toward the evaporator of assembly 12 . heat is removed from the system at condenser assembly 20 as denoted by heat symbol &# 34 ; q &# 34 ; whose arrow points away from the condenser assembly . solution is communicated between solution reservoir assembly 12 and solvent reservoir assembly 14 by concentric tubing comprising a solution transport tube 22 and a solution transfer tube 24 , the purpose for which will be shortly discussed . intercommunication between assemblies 12 and 14 is also effected by a path passing through condenser assembly 20 including a vapor transport tube 26 and condensate transport tubing 28 . solution reservoir assembly 12 includes a solution reservoir 30 bounded by top and bottom reservoir end caps 32 and 34 . vapor transport tube 26 communicates with reservoir 30 through end cap 32 and a vapor port tube 36 . a valve 38 is coupled to tube 36 for insertion of additional solution , if needed , through supply pipe 40 . heat input to solution reservoir assembly 12 may be effected by a plurality of conventional heat pipes inserted through heater well holes 42 in solution reservoir 30 . insertion or removal of solvent from solvent reservoir 14 may be effected through valves 44 and solvent inlet tubes 46 . in normal operation of heat pipe 10 , valves 38 and 44 are closed . reference is now directed to fig2 and 5 for a detailed description of solvent reservoir assembly 14 , membrane assembly 16 and mixing manifold assembly 18 . solvent reservoir assembly 14 includes a solvent reservoir 50 closed at one end by a cap 52 and open at its other end at a reservoir flange 54 . extending from the solvent reservoir are a pair of tubes 56 and 58 , both being interconnected with tube 28 . tube 58 transports solvent to and from reservoir 50 while tube 56 primarily transports gases or vapors , particularly vapors of solvent , to and from the solvent reservoir . as such , tubes 56 and 58 define full &# 34 ; on &# 34 ; or full &# 34 ; off &# 34 ; limits of heat transfer , respectively when the level of solvent in reservoir 50 is at tube 56 or at tube 58 . supported by and within solvent reservoir 50 is membrane assembly 16 , which comprises a plurality of perforated support tubing 60 coupled together by a membrane flange 62 . perforated support tubing 60 preferably comprises a plurality of perforated tubes ; however , a single tube may be employed if the largest possible solvent permeable membrane is not needed . such a solvent permeable membrane is depicted as comprising a membrane 64 , for example , of cellulose acetate . such membrane material is configured as tubing which fits closely within the interior of each perforated tube . solvent reservoir assembly 14 is closed by mixing manifold assembly 18 at its flange 66 . flanges 54 , 62 and 66 are secured together such as by a combination of cap screws , lock washers and nuts 68 . sealing between the flanges is effected such as by copper ring gaskets 70 . osmotically pumped heat pipe 10 , as described to this point , is capable of being fully operational to meet the present invention &# 39 ; s desired object of providing a self - equalizing control mechanism in that the pumping rate in the heat pipe is controlled by the membrane surface area inside reservoir 50 which is capable of being wetted by solvent . the solvent , designated by indicium 72 ( see fig5 ), is permitted to wet as much of membrane 64 as is determined by the level 74 of solvent in its reservoir . during rise or drop of the solvent level , gas or vapor escapes from or is drawn into the reservoir as it is filled with or emptied of the solvent . solvent reservoir 50 and solution reservoir 30 are designed to hold approximately the same volume of fluid , with only sufficient solvent placed in the heat pipe to come up to the top of vent tube 56 . there is enough solution in the entire system to fill the solution reservoir completely . when heat is applied thereto , the solution is distilled and the solvent vapor passes through tube 26 to condenser 20 to form a condensate which falls and joins with the remainder of solvent 72 . the solvent wets the backside of membrane 64 and osmotic pumping begins through the membrane . as more heat is applied to the evaporation section of solution reservoir 30 , the solvent fills solvent reservoir 50 to wet more area of the membrane . the maximum power of the heat pipe is reached when the solvent has filled its reservoir 50 . as heat power requirements drop , less solvent vapor is produced by solution reservoir 30 so that there is less condensate formed to resupply reservoir 50 for osmotic pumping through membrance 64 . as a consequence , level 74 drops until a balance exits between the formation of solvent vapor and a level of condensed solvent in reservoir 50 . in order to insure that heat pipe 10 operates to its fullest capacity , the teachings of co - pending patent application serial no . 106 , 984 , filed herewith and entitled &# 34 ; passive flow mixing device for osmotically pumped heat pipes &# 34 ; by algerd basiulis and charles p . minning , is used . the invention described therein describes a means by which the flow rate of the heat pipe is improved by providing a circulation current in the column existing between the solvent and solution reservoirs . specifically , better mixing occurs when the upward flow of a lean solvent - solute mixture is separated from the downward flow of heavier , more concentrated solution so that the richer solution would sweep away the concentration of solvent on the solution side of the membrane . this mixing concept is incorporated in the present invention by use of solution transport tube 22 and solution transfer tube 24 extending between solvent and solution reservoirs 50 and 30 . specifically , solution transfer tube 24 is placed within solution transport tube 22 and terminates at a solution mixing flange 80 . the solution mixing flange is supported in mixing manifold assembly 18 by attachment to an envelope 82 ; thus , solution transfer tube 24 communicates within a solvent collecting space 84 . also extending from solution mixing flange 80 is solution mixing tubing 86 comprising a plurality of tubes which respectively extend within the tubes of perforated support tubing 60 and face inwardly of membrane tubing 64 . solution mixing tubing 86 communicates with the heavier solution of the rich solute - solvent mixture and transport tube 22 . accordingly , the heavier solution moves downwardly through transport tube 22 and into solution mixing tubing 86 within perforated support tubing 60 . since solvent 72 is moving through membrane tubing 64 by the process of osmotic pumping , the lighter solvent moves into the space between tubing 86 and membrane tubes 64 and then upward into collection space 84 where it dilutes the solution therein for movement upward through solution transfer tube 24 into solution reservoir 30 . if the desirable use of convection currents effected by concentric tubes 22 and 24 is not needed , vent tube 56 may be extended from one or more cylindrical membranes through tube 22 , and past the evaporator and surface of the solution in reservoir 30 . in effect , inner pipe 24 would become a vent communicating with solvent space 84 on the solvent side of the membrane . in an experiment to test the validity of the inventive concept , a single cylindrical membrane tube was fitted within a solvent reservoir , and the solution column , using only a single solution path rather than convection current producing tubes 22 and 24 , was filled with a 1 . 0 molal solution of water and sucrose . distilled water was poured inside the solvent reservoir . a heater at the solution reservoir was turned on and adjusted until the power just matched the flow rate through the solvent permeable membrane . at a maximum evaporator temperature of 100 ° c ., the maximum power was 24 watts , as depicted in fig4 . then the heater power was reduced to 23 watts . since less water was being evaporated at that power level , the solvent or water level fell slighty within the solvent reservoir until the pumping rate matched the power input . fig4 shows this relationship where , as the power input is reduced , the area of membrane wetted by the solvent is also reduced , thus proving out the concept of the present invention . although the invention has been described with reference to particular embodiments thereof , it should be realized that various changes and modifications may be made therein without departing from the spirit and scope of the invention .