Abstract: A geothermal heat exchange unit, which can be placed in ground or in water, having a hollow sleeve about which a helical winding of thermally conductive tubing is wound and a return length of thermally conductive tubing along the central axis of the sleeve separated from the inner wall of the sleeve by thermal insulating material. The heat exchange unit may be housed within a thermally conductive case with a thermally conductive material filling the gap between the inner wall of the case and the thermally conductive tubing surrounding the sleeve of the heat exchange unit. The thermally conductive case may have at least one set of helical fins which act as threads for ground insertion assistance. The heat exchange units may be combined to form greater lengths and be combined in series or parallel connection for greater efficiency.

Abstract: A plurality of each of said heat-exchanger coils each having a different winding diameter are provided between a header in the inlet side provided in an inlet tube and a header in the outlet side provided in the outlet tube so that the two headers are communicated to each other, and also a group of heat-exchanger coils each surrounded by another heat-exchanger coil having a larger diameter as compared to that of the former is provided.

Abstract: A non-adiabatic vapor-liquid contact device is disclosed which achieves high heat transfer effectiveness without sacrificing mass transfer effictiveness. Referring to FIG. 2, a helical coil of crested tubing 84 is contained within the annualr space between shrouds 82 and 83. Liquid flows downward through the annulus, and vapor flows countercurrently upward. The mass exchanging fluids pass through the space between tube crests and the shroud, achieving very effective mixing. Heat transfer fluid is flowed through the tubing via connections 87 and 88.

Abstract: A refrigeration and heating system in which an absorber (97), condenser (100) and recuperator are placed (107) in a single module (270) and are provided with tube-in-tube or tube-in-cylinder construction with fluted inner tubes. A general purpose, divided-flow, tube-in-cylinder, heat transfer device (400) is used to reduce the pressure drop in the circulating fluid.

Abstract: An improved refrigerant evaporator which uses a plurality of circuits to maximize inner and outer surface areas and cross-feed refrigerant to quickly and uniformly remove heat from static solutions within a containment tank. Refrigerant is equally fed to a plurality of individual circuits 20 from a common inlet manifold 2 located at one side of the coil. Individual circuits 20 alternately incorporate, and do not incorporate, crossover members 23 to carry the incoming refrigerant to the each side of the evaporator such that it simultaneously flows inward from both sides. Individual circuits 20 are additionally arranged such that all which are contained within an evaporator are of identical length thus making the invention particularly well suited for use with non-azeotrope refrigerants. Further, the device does not immerse joints or connections in the cooled medium and performs well in corrosion environments.

Abstract: The invention is concerned with a heat-exchanger for arrangement behind the combustion chamber of a heating boiler. The heat-exchanger comprises water-carrying and gas-carrying interior chambers separated from one another by walls extending in parallel and being spirally coiled about a filling member and sealed against one another by bent edges.

Abstract: A housing is provided for an air conditioning condenser of the type providing a fan creating an upward path of air movement through the housing, a heat exchange coil having and inlet and an outlet for connection to a source of hot refrigerant in a refrigerant loop and means for spraying water on the coil. The housing is made of rotomolded plastic and comprises a base, a plurality of identical walls and a top. The base and top are rotocast as a single piece and then cut horizontally with a saw to provide the two pieces. The base includes a U-shaped foot arranged to receive fork lift tines and oriented so the fork lift does not damage the inlet and outlet to the heat exchange coils.

Abstract: It is used to reheat a secondary fluid such as pool water or sea water. It comprises a body provided with an inlet for the secondary fluid to be reheated and an outlet for the reheated fluid, a sleeve inside the body, a coil in which the primary fluid circulates and which is housed inside the annular space between the body and the sleeve and outside of which the water to be reheated passes. The body (1) and the sleeve (8) are made of a plastic-based material, either reinforced or not, and the coil (10) is made of titanium.

Abstract: A heat exchanger element for exchanging heat between a fluid circulating in the element and a phase-change medium in a reservoir housing the element is formed of a plurality of spiral coils of flexible tubing disposed horizontally, one above the other, in a vertical stack. One end of each spiral coil is in communication with an inlet manifold and the opposite end is in communication with an outlet manifold. Preferably, the manifolds are disposed vertically, extending the height of the stack and side-by-side. Preferably, the manifolds are adjacent the outer periphery of the vertical stack of spiral coils. The spiral coils of the stack are wound alternatively clockwise and counterclockwise from a first radially outermost turn to a last radially innermost turn and arranged in pairs, one above the other. One spiral coil of each pair has the first radially outermost turn connected directly to the inlet manifold and the last radially innermost turn connected directly to the outlet manifold.

Abstract: The heat absorbing member formed by connecting the bottom portion of the inlet header (1) with that of the outlet header (2) through a heat absorbing tube installed so that the heat absorbing tube is located in a heating container (9). The heat absorbing tube (16) is comprised of a plurality of down tubes (3, 5) and down tubes (4, 6) all with lower ends closed and connected under the inlet header (1) and outlet header (2) respectively, and spiral tubes (7, 8) which connect to the bottom portion of the down tubes (3, 5) and to the top portion of the down tubes (4, 6), and wherein the spiral tubes (7, 8) are of the same length.

Abstract: The heat exchanger is made up of a shell having a coaxial tubular outer and inner wall with end plates attached thereto to enclose a tubular shell cavity provided with an inlet and outlet for a first fluid. Within the shell cavity is a spiral coil of tubing through which flows a second fluid. The coil is wound helically about the axis of the shell and sized to fit the inner and outer walls with limited radial clearance. The coils are axially spaced from one another to define a spiral flow path within the shell cavity for the fluids to first flow. The radial and axial clearance establish a spiral flow path and an axial flow path which are relatively sized to cause the first fluid to travel in a spiral motion, thereby enhancing heat transfer between the first and second fluids. Also, an enclosed central receiver, include communication with the shell cavity, may be formed within the inner tubular wall which serves as a fluid accumulator or reservoir.

Abstract: Prechilling the tap water with the cold waste water from an ice machine is achieved by using an insulated, elongated casing, which encloses a reservoir housing a heat exchanger made of a relatively long tubing of copper to provide a relatively long path of travel for the tap water. The heat exchanger is in the form of a coil followed by a substantially straight tube within and surrounded by the coil's turns. A hollow member, closed at one end, is spaced from the straight tube. The coil's turns surround the hollow member and the straight tube. Preferably, the hollow member is mounted over and is spaced from the straight tube to form there between an elongated chamber. In use, the tap water flows downwardly in the coil and upwardly through the straight tube. The cold waste water flows through the elongated chamber into the reservoir, thereby progressively and continuously increasing the temperature of the waste water and correspondingly decreasing the tap water's temperature.

Abstract: A refrigeration and heating system has been made in which improved efficiencies are obtained by placing helical concentric coils of at least two generators (80 and 81) and recuperators (86 and 95) on a common axis (232) with a heating unit (84) at the center and allowing the hot combustion gases (245) to circulate in serpentine fashion through separate concentric chambers containing the coils. Further efficiencies are obtained by placing an absorber (97), condenser (100) and recuperator (107) in a single module (270) and by using tube-in-tube or tube-in-cylinder construction with fluted inner tubes. A general purpose, divided-flow, tube-in-cylinder, heat-transfer device (400) is used to reduce the pressure drop in the circulating fluid.

Abstract: Spent surface finishing compound is filtered and cooled or heated for reuse in a machine finishing process. The spent finishing compound is filtered through a pleated polyester or polypropylene wound filter cartridge to remove particles of a predetermined size ranging from about 0.5 to 100 microns. The surface finishing compound circulates through an in-line, constant flow intercooler having a chamber for receiving and maintaining the finishing compound in a spiral circulation. The surface finishing compound circulates about cooling tubes positioned within the chamber. Heat is exchanged between the circulating water within the cooling tubes and the surface finishing compound.

Abstract: A sub cooling condensate trap as an auxiliary unit for an air conditioning system, comprising a container having a heat exchange coil disposed therein and through which hot liquid refrigerant is passed, and water inlet and outlets in the container through which condensate water from the air conditioner condenser is passed countercurrently to the refrigerant, thereby sub cooling the refrigerant and increasing the power usage efficiency of the air conditioning system.

Abstract: A process and apparatus for enhancing in-tube heat transfer within a tubular member. A fluid is introduced into the tubular member and then directed in a downstream direction through a coil of the tubular member. The first coil defines a first coil axis. The fluid is further directed in the downstream direction through at least one downstream coil. Each downstream coil has a coil axis which is rotated at a coil switching angle, with respect to the coil axis of the immediately upstream coil. The fluid is maintained at a turbulent flow level within at least a portion of a coiled section of the tubular member. The fluid is then discharged from the tubular member.

Abstract: A radially fired water heating apparatus (10) having a plurality of stacked segments of multiple-loop, finned coiled tubing (58) separated by inner and outer support baffles (86, 88), all contained within a cylindrical baffle (20) which cooperates with the coiled tubing (58) and support baffles (86, 88) to direct combustion by-products into an annulus (24) promoting heat transfer to a countercurrent flow of inlet air, the water being supplied to and recovered from the stacked segments of coiled tubing (58) through inlet and outlet headers (54, 56) disposed outside cylindrical baffle (20) that can be selectively modified by installing or removing baffles (90, 92) for either single-pass or multiple-pass operation.

Abstract: The present invention relates broadly to methods for heating or cooling a media in a indirect heat exchanger. In a specific embodiment of the invention, the indirect heat exchanger is a shell and tube heat exchanger where the tube is coiled within the shell and the coiled tube includes baffles at least every third coil. The media is passed through the coiled tube and a coolant or heat source flows through the surrounding shell such that the coolant or heat source floods the entire shell. The baffles redirect the coolant or the heat source in such a way as to cause turbulent flow. This turbulent flow allows the heat transfer process to be conducted in a uniform and highly efficient manner.

Abstract: A heat exchange device includes a vessel having a top end and a bottom end, and having a first chamber located in the vessel and a second chamber located in the vessel and separated from the first chamber by a partition. An elongated tube for conveying liquid to be cooled is located in the second chamber and is arranged in a convolution. A port is connected to the first chamber for supplying coolant to that chamber, and a flow path extends between the first and second chambers for permitting fluid flow between the first and second chambers. The flow path is a space between the upper edge of the partition and the top end of the vessel, and the upper edge of the partition uniformly distributes coolant over the elongated tube. A port is located in the second chamber for evacuating coolant from the second chamber.

Abstract: A heat exchanger adapted to handle dusty hot waste gases including a vertically oriented shell through which the waste gases flow longitudinally downward. The shell contains a tube assembly of vertical tubes having external, longitudinal heat transfer fins with the tubes being connected for fluid flow and support of their upper and lower ends to a central vertical support/header assembly. This support/header assembly is a tube divided into an upper header, a lower header and a center support tube section.

Abstract: The high cost of fabricating heat exchangers having two fluid flow paths in countercurrent or cross current relation is minimized by utilizing an extrusion (14) wound upon itself with adjacent convolutions (16, 18, 20, 24) spaced at (26) and located within a housing (10). A baffle (56) or a seal (82, 84) are employed within the housing (10) to respectively define cross current or countercurrent heat exchangers. Alternatively, an extrusion such as a unitary extrusion (100) may contain plural flow paths (114, 120, 122) or an extrusion made up of two extrusions (150, 152) bonded together and having flow paths (162, 164) may be employed.

Abstract: The heat exchanger is made up of a shell having a coaxial tubular outer and inner wall with end plates attached thereto to enclose a tubular shell cavity provided with an inlet and outlet for a first fluid. Within the shell cavity is a spiral coil of tubing through which flows a second fluid. The coil is wound helically about the axis of the shell and sized to fit the inner and outer walls with limited radial clearance. The coils are axially spaced from one another to define a spiral flow path within the shell cavity for the fluids to first flow. The radial and axial clearance establish a spiral flow path and an axial flow path which are relatively sized to cause the first fluid to travel in a spiral motion, thereby enhancing heat transfer between the first and second fluids.

Abstract: A heat exchanger for transferring heat between an inner and outer medium with a tube bundle for transporting the inner medium. The tube bundle being a plurality of tubes forming concentric rings of tubes. The tubes have angular progressions and are corrugated their entire length; thus adjacent tubes can contact without fatally increasing mechanical tensions. A shell surrounds the tube bundle. An inner medium connector transports the inner medium to and from the tube bundle. An outer medium connector transports the outer medium to and from the shell; the outer medium flowing around the tube bundle inside the shell.

Abstract: A compact modular isothermal reactor for converting a feedstock such as methanol into a fuel usable in power generation systems, such as electrochemical fuel cells, is provided. The reactor includes a sealing plate, a baffle plate having heat transfer surfaces extending toward the sealing plate, and a housing having an interior substantially circumscribing the heat transfer surfaces The cooperating surfaces of the sealing plate, baffle plate, heat transfer surfaces and housing interior define a labyrinthine channel for containing a suitable quantity of solid catalyst and through which feedstock flows. The cooperating surfaces of a fluid flow plate and the baffle plate define a flow passage for carrying a thermal fluid. Heat is transferred from the thermal fluid to the feedstock by the heat transfer surfaces. In two alternative designs, thermally conductive pins extending from the baffle plate or a pair of spaced folded thermally conductive plates transfer heat to the interior of a catalyst containment vessel.

Abstract: The present invention pertains to a tubular heat exchanger for operation at high gas temperature and high pressures with heat exchanger tubes, which are coiled on the greater section of their linear extension. Further, the tube bottoms have tie rods, which brace the tube bottoms. The tie rods (3) of a graduated circle (1a, 1b) are connected at several points in the longitudinal direction by rings (5) into a cage. The tie rods (3) are flattened (3a) in the area of the rings (5). The tubes arranged on the adjacent graduated circle are connected to one another in the coiled area (2a) by means of angular plates (4) in pairs in the area of the rings (5). The connection to the angular plates (4) is such that, the tube form a hollow-cylinder-shaped tube cage. At least three guiding plates (6, 6a) are arranged in each area of uncoiled tubes (2b).

Abstract: A heat exchanger for cooling superheated steam with water, yielding saturated steam. The heat exchanger consists of U-shaped pipes (4) that the superheated steam flows through. The pipes are accommodated in a jacket (1) provided with intakes (10 & 11) and outlets (12 & 13) for the evaporating water. The pipes have their ends secured in a slab of tubes. The slab demarcates a chamber that is separated by a partition into an intake compartment (17) with an intake (14) and an outlet compartment (18) with an outlet (15).

Abstract: Disclosed is an improved heat exchanger whose flow rate and heat exchange rate are so improved that it may quickly respond to any demand in a very efficient way. This heat exchanger comprises a tank in which a first fluid may be circulated, this tank having an inlet port and an outlet port for the first fluid, and at least one heat conductive tubular element located within the tank, and in which a second fluid may be circulated in order to exchange heat with the first fluid within the tank, this at least one heat conductive element having ends leading outside the tank. A fluid injector is operatively connected to at least on one of the ports of the tank to generate turbulences and prevent the formation of dead spots within the tank. This injector is preferably in the shape of a loop and provided with a plurality of perforations, the loop extending in a plane parallel to and near one end of the tank.

Abstract: A heat recovery system with a heat exchanger and a mixing valve. A drain trap includes a heat exchanger with an inner coiled tube, baffle plate, wastewater inlet, wastewater outlet, cold water inlet, and preheated water outlet. Wastewater enters the drain trap through the wastewater inlet, is slowed and spread by the baffle plate, and passes downward to the wastewater outlet. Cold water enters the inner tube through the cold water inlet and flows generally upward, taking on heat from the wastewater. This preheated water is fed to the mixing valve, which includes a flexible yoke to which are attached an adjustable steel rod, two stationary zinc rods, and a pivoting arm. The free end of the arm forms a pad which rests against a valve seat. The rods and pivoting arm expand or contract as the temperature of the incoming preheated water changes. The zinc rods expand more than the steel rod, flexing the yoke and rotating the pivoting arm.

Abstract: In a heat exchanger fueled by a metal-corroding heating gas, the use of a replaceable aluminum plug component which, because of its chemical affinity, corrodes first to thereby obviate the corroding of other non-replaceable metal components, to thereby contribute to eliminating malfunctioning due to corrosion. The construction of the plug also contributes to the heat transferring efficiency of the heat exchanger.

Abstract: The barrel assembly of the heat exchanger is manufactured with abutment joints between the housing and the headers thereof, and is clamped together along the axis of the assembly by a rod extending through the respective headers, and the housing, parallel to the axis, so that the housing is not vulnerable to "blowing its ends" when under pressure. The housing is also free draining at the discharge header when relieved of pressure, and this combination of features is made possible in part by the use of an insertable fluid flow cartridge for the housing which provides the tubing for one of the fluids and baffling for the other fluid when the latter fluid is circulated through the housing.

Abstract: A cross-flow heat exchanger comprising according to a preferred embodiment a shell formed of two concentric cylinders providing an annular space. A number of tubes and baffles are arranged in the annular space such that one fluid flows through the tubes in a helical fashion in the annular space and the second heat exchange fluid flows in a counter helical path in such annular space across the tubes, constrained by the baffles in such annular space. In another embodiment cross-flow is also achieved using spirally shaped tubes and spirally shaped baffles.

Abstract: This invention relates to an improved method of manufacturing a heat exchanger element. In a second aspect the invention concerns a heat exchanger element itself. In the third aspect the invention concerns a reservoir suitable for housing the heat exchanger element to form a heat exchanger. The element is manufactured by extruding polyethylene tubes and winding them into spiral coils. Each coil is located along the length of a rigid horizontal spacer bar in order to maintain even spacing of the coil. The element comprises a stack of coils which are not restrained against vertical movement. The element also comprises a cylindrical void through the center.

Abstract: In a shell and tube boiler for use, in particular, in a liquid-metal-cooled fast-breeder nuclear reactor, the shell is formed as two vertical side-by-side units joined at their upper ends by a chamber. This "folding" of the unit considerably shortens the overall height of the boiler. Each tube is formed in two sections, each comprising a vertical limb with a curved portion at its upper end. The sections are joined by welding together the ends of the curved portions. This reduces the tube lengths which must be manufactured and transported to the site. In use of the boiler, the liquid sodium level in the chamber is maintained below the level of the tube welds. The chamber region above the sodium level may be filled with a blanket gas, such as argon.

Abstract: An evaporation heat exchanger having at least one active circulating circuit for a coolant liquid to be cooled, is constructed for removing heat in a spacecraft under a gravity-free operating condition and under different acceleration conditions. For this purpose, a housing encloses an evaporating space provided with at least one inlet valve for controlling the admission of a medium to be evaporated. The produced vapor or steam is discharged through a respective port. A plurality of cooling tubes interconnected in a meandering shape form a number of tube panels in which the individual tubes are arranged in a zig-zagging pattern to form respective flow passages for the medium to be evaporated. The individual tubes extend in parallel to each other and perpendicularly to the flow direction of the medium to be evaporated, while the meandering configuration is forming the zig-zag pattern.

Abstract: A cooler for particle-laden gases in a coal-gasification plant, with an upright nest of hot-gas tubes that coil around the cooler's longitudinal axis inside its jacket and with a pipe for supplying a coolant inside the nest of tubes. The cooler has a ceramic-lined or liquid-cooled distributing head (1) with a central gas intake (2) at the top and with several diffusor-like gas outlets (3) at the bottom that open into the nest (4) of tubes and several gas outlets (5) below the nest. The hot-gas tubes are suspended from the coolant-supply pipe (v) on claws (7). The pipe has at least one intake (8) for the descending coolant and rests on a support (9) on the base (11) of the cooler or on supports (10) against the inner surface of the cooler. The mixture of steam and water ascending among the tubes is extracted through at least one outlet (14) on the jacket (12) of the cooler.

Abstract: A heat exchanger for heating washer fluid supplied to motor vehicle windshield washer nozzles simultaneously with diesel oil supplied to the diesel engine of the vehicle is disclosed. Engine coolant heats a tank containing separate coils through which the washer fluid and diesel oil circulates.

Abstract: For selectively satisfying a basic cooling demand or a cooling demand which is an integral multiple of said basic cooling demand, the apparatus can be assembled from components selected from a plurality of sets of such components. For satisfying the basic cooling demand the apparatus comprises a single cooler-filter unit. One set of components consists of a plurality of said cooler-filter units. Another set of components consists of mounting blocks, which are to be mounted in a reservoir and adapted to communicate with cooler-filter units provided on the outside of a wall defining said reservoir. Another set consists of manifold blocks, each of which is adapted to be connected between the port members of cooler-filter units and a mounting block and to which each cooler-filter unit is hydraulically connected by means of a transverse supply passage section and a transverse return passage section.

Abstract: A tube matrix for a heat exchanger is connected between two spaced ducts for conveying a fluid from one duct to the other. The tube matrix has a plurality of spaced heat exchange tubes whose ends are secured to the ducts and which have a generally S-shape between the ducts. At the points of lateral offset and at the intermediate point therebetween, spaces are provided for keeping adjacent tubes in spaced relation from one another. Each loop of the S-shape tube is formed with two successive sections each of which includes two segments of opposite curvature such that in all there are eight segments which make up the tube. Preferably, the tube is a one piece member and the shape is formed by bending the tube. At each of the points where the tubes are secured and are connected by the spacers, tangents to the tubes extend parallel to one another.

Abstract: A multiple tube heat exchanger formed from a number of elbow members which when combined form a "U" shaped jacket, an elongate tubular section connected to the ends of the U-shaped jacket, a number of heat conductive U-shaped tubular members mounted in the jacket, a tube sheet mounted on the ends of said tubular members and tubular sections and a number of baffles for supporting the tubular members in a spaced relation from said tubular sections.

Abstract: An evaporative condenser having a cylindrical fiberglass housing which provides a circumferential air flow across a plurality of concentrically oriented spiral condensing coils. The planar spiral coils are generated through the compression of a conical winding of tubing formed about a multi-tiered platform, to form an evenly-spaced spiral condensing coil. Each layer of tubing is affixed to a plurality of radial braces, which provide the evaporative coils with sufficient structural integrity to be individually employed. A method and apparatus for producing spiral coils having uniform spacing between adjacent revolutions.

Abstract: A header for a tube-in-tube heat exchanger is formed in a single piece such that the manifold plate in one end thereof is integrally formed with the header body. Such a design eliminates the process of brazing the manifold plate into the header body, thus substantially simplifying the assembly process. In order to accommodate thinner walled tubes and a thinner manifold plate, reinforcing sleeves are placed around the inner tubes ends and are brazed in place in the manifold plate openings.

Abstract: Heat transfer equipment is provided having a chamber adapted to contain a bed of free-flowing granular material and a plurality of spirally wound cylindrical tube coils nested together which extend concentrically around a centrally positioned tube collector. Each tube coil is wound on a cylindrical surface having an axis coinciding with the longitudinal axis of the chamber. The tubes at least at the top end of the chamber emerge from the coil and remain on the cylindrical surface as they extend in a direction substantially parallel to the longitudinal axis. The tubes then bend about 90.degree. and extend radially toward the longitudinal axis and connect to the centrally positioned tube collector. In the radial run, the tubes from different tube coils overlap one another on the top of the coils and extend radially over substantially the same outer surface of the tube coils. A retaining device adapted to be removed in sections is positioned below the tubes in the chamber.

Abstract: A laminated spiral heat exchanger (10) in accordance with the invention includes a heat conductive top laminate (30); a heat conductive bottom laminate (36), at least one spiral heat conductive laminate (42), the laminates being joined together to form a heat exchanger core; at least one spiral channel (18) disposed within at least one spiral laminate; a first fluid port (20) coupled to each spiral channel at a first radius with respect to a center of the spiral heat exchanger; and a second fluid port (24) coupled to each spiral channel at a second radius with respect to the center point of the spiral heat exchanger which is greater than the first radius.

Abstract: A heat exchanger unit comprises a plurality of heat exchangers of a construction in which a number of tubes are mounted on mounting plates, which additionally serve as manifolds, in a manner such that the tubes maintained in spaced relation while being twisted such that their axes conform to parts of helices.

Abstract: An apparatus 10 is provided for supplying a high-velocity flow of temperature regulated air 5 to the calender roll 90 of a paper making machine. Ambient air 1 is received into the plenum chamber 20 and distributed therefrom through a longitudinally elongated conduit means 30 which has an inlet 32 opening directly into the plenum chamber 20 and an outlet opening 36 along the other end thereof and defining therebetween a flow passageway 34. The outlet opening 36 is adapted to direct the air flow passing through the flow passageway 34 along the calender roll 90 in counter direction to the rotation of the calender roll 90. A series of spiral wound heating element coils 40 are disposed within the conduit means 30 at longitudinally spaced intervals along the length thereof to heat the air to a desired temperature by selectively powering the heating element coils 40.

Abstract: An apparatus for heating fuel, especially Diesel fuel and heating oil, that is to be supplied, for example, to a motor or oil burner. Disposed upstream of a fuel filter is a heat exchanger that heats the fuel line. To continuously heat fuel without supplemental energy consumption, the heat exchanger has warm coolant or liquid, for example from the engine, flow through it to heat it up. Disposed on the fuel filter is an electrical heating element that can directly heat the filter space or fuel contained in the filter housing. The heating element can be activated and deactivated in a controlled manner, for example manually, only when needed.

Abstract: A heat exchanger includes a plurality of generally planar spiral flow channels in a stacked, generally parallel array for accommodating a first fluid. Each spiral flow channel terminates in an inner end at an axial core area of the heat exchanger. Flow channels are sandwiched between the spiral flow channels for accommodating a second fluid in heat exchange relationship with the first fluid. Relatively rotatable tubes extend axially of the core area and have radial openings in axial registry with the inner ends of the spiral flow channels. Relative rotation of the tubes vary the overlapping relationship of the tube openings and thereby vary the flow to the spiral flow channels.

Abstract: A waste heat boiler for cooling partial oxidation crude gas comprises a pressure container, a crude gas-clean gas heat exchanger in the container, a tubular body formed as a tubular basket and arranged in the pressure container, the crude gas-clean gas heat exchanger being arranged inside the tubular basket, and heating surfaces associated with the crude gas-clean gas heat exchanger.

Abstract: A heat exchanger having an inlet duct for admission of a first fluid to be heated, an outlet duct for discharge of the first fluid after heating thereof, the ducts being arranged in substantially parallel relation, and an assembly of a plurality of heat exchanger tubes connected to the inlet and outlet ducts for receiving the first fluid from the inlet duct to convey the first fluid through the tubes for discharge into the outlet duct. The heat exchanger tubes are of U-shape each including a curved bend region in which reversal of direction of flow of the first fluid is effected. The assembly of heat exchanger tubes extends laterally of the ducts into the path of travel of a second fluid which flows around the tubes in a passage area to effect heat exchange with the first fluid in the tubes.

Abstract: A heat exchanger and heater of a tube type is provided for heating a liquid n a coiled type housing having an inlet and an outlet for liquid of various types. Hot materials in a gas flow are introduced into the system and a liquid is vaporized to heat the heat exchanger system. In a second embodiment of the shell type of heat exchanger and heater is used in the heating of the input liquid. The third embodiment of the heat exchanger and heater system utilizes a frusto-conical shell with a heat coil centrally located in the shell, while a fourth embodiment of the heat exchanger and heater utilizes a cylindrical coil for the liquid to be heated and a temperature sensor for sensing the temperature in the system at end point.