Abstract: An oil changing unit comprises a base having a disk configuration and forming a socket at a center thereof. The base further includes a manifold block thereunder and a first circular ridge formed on the base and surrounding said socket and a second circular ridge formed on a peripheral of the base. A first tube is securely assembled to the socket and having an orifice in a wall thereof. A first cylinder is attached to the first circular ridge and encloses the first tube therein. The first cylinder includes a first lid enveloped and secured onto the first tube and tightly sealing an upper end thereof such that the orifice of the first tube is located within the first cylinder. A second cylinder is attached to the second circular ridge and encloses the first tube therein and includes a second lid enveloped and secured onto the first tube and tightly sealing an upper end.

Abstract: A method and apparatus for controlling and isolating heat exchanger flows in a heat exchanger includes at least one isolation and flow direction control plate (40) having at least one fluid slot (45). The isolation and flow direction control plates (40, 41, 42) create a plurality of smaller heat exchangers 50 within a heat exchanger assembly (1). The isolation and flow direction control plates (40, 41, 42) permit fluid communication between the corresponding smaller heat exchangers (50) and individualized flow direction control over a shell side fluid flow between a shell side fluid inlet (11) and a shell side fluid outlet (12) of the heat exchanger assembly (1).

Abstract: The temperature distribution in a shell and tube type heat exchanger having an expansion joint is uniformized by improving the circulation efficiency of fluid in the shell side. The uniformization is attained by the heat exchanger having an invasion-preventing plate against the fluid in the shell side attached to the expansion joint installed around the periphery of the shell, and a method of catalytic gas phase oxidation reaction that uses the heat exchanger.

Abstract: A modified air heater gas inlet plenum for a tubular air heater which permits retrofit installation of additional flue gas environmental treatment equipment. A divider plate is located within the inlet plenum to subdivide it into first and second flue gas passages. The first flue gas passage created by the divider plate merely conveys the hot flue gas through the inlet plenum and into flues which convey the flue gas to the new equipment. Return flues convey the flue gas back to the second flue gas passage created in the inlet plenum which, in turn, conveys the flue gas into the tubular air heater heat exchanger tubes. By taking advantage of the large size of a conventional air heater gas inlet plenum, the first and second flue gas passages created by the divider plate still have sufficient cross sectional area so that acceptable flue gas velocities are preserved.

Abstract: An engine charge air cooler system including a charge air compressing system, a refrigerant cycling system, and a charge air cooling apparatus for transferring heat from the compressed charge air of the charge air compressing system to the refrigerant fluid of the refrigerant cycling system. The charge air cooling apparatus comprises a housing with a charge air passage for charge air moving through the housing. A plurality of fins are positioned in the charge air passage. A fluid tube is provided in the housing and passes through each of the fins in a plurality of locations. Preferably, the refrigerant compressor of the system is adapted to also compress a separate flow of refrigerant fluid for an air conditioning system of the vehicle in addition to the refrigerant fluid of the system of the invention. A heating element may be provided in the interior of the housing, and may be selectively heatable for preventing accumulated moisture from freezing in the interior of the housing in sub-freezing temperatures.

Abstract: A heat exchanger for an easily polymerizing substance-containing gas provided with a shell possessed of a heat-exchanging gas inlet and a heat-exchanging gas outlet and a heat-exchanging part adapted to circulate fluid introduced from outside the shell between the gas inlet and said gas outlet, which heat exchanger is characterized by being provided with a gas distributing plate between the gas inlet and the heat-exchanging part. The heat exchanger is characterized by the gas distributing plate having a cross-sectional area in the range of 1.0-10.0 times the cross-section of the gas inlet. When an easily polymerizing substance-containing gas contacts a structure, the gas is condensed on the contact surface of the structure and suffered to generate a polymer.

Abstract: A heat exchanger comprises a plurality of first heat exchange tubes extending through the exchanger, and through a plurality of laterally extending heat exchanger chambers, each chamber having at least one entry from a first chamber and at least one exit to a second axially adjacent chamber, and each chamber having a plurality of transverse interconnecting zones, each of which is defined by at least two of said tubes, and at least one first zone has an entry to said first chamber and at least one second zone, different from said first zone, has an exit to said second chamber. Also included is a vessel for mixing or distributing streams of a first fluid passing axially from an upstream to a downstream location, which comprises transverse baffles across said vessel in at least two successive rows, which rows of baffles define an open transverse chamber, the baffles in successive rows having a different spatial distribution across the vessel.

Abstract: In such an exchanger, in which the blocks have fluid inlet openings in communication with the interior space of a supply box which runs alongside the block and communicates with at least one analogous box of an adjacent block to form a fluid supply line, in order to even out the distribution of fluid between the openings of the blocks, the supply line contains at least one grating (30) leaving perforations (301) and solid parts (302) which are distributed in such a way as to create pressure drops which are such that the flow velocities of the fluid in the inlet openings downstream of the grating have similar values.

Abstract: A heat exchanger includes a shell having an open end and a closed end and defining a shell cavity. A steam inlet is located adjacent the closed end and communicates with the shell cavity to allow steam to enter the shell cavity. A flange is coupled to the shell adjacent the open end. The flange includes a first passageway communicating with the shell cavity for receiving a tube bundle, and a second passageway communicating with the shell cavity to allow condensate to drain from the shell cavity. Preferably, the shell has a longitudinal axis and the second passageway has a longitudinal axis that is oriented substantially normal to the longitudinal axis of the shell. The second passageway is positioned in the flange to allow condensate to the drain from the shell cavity regardless of whether the heat exchanger is oriented vertically or horizontally.

Abstract: Parallel flat tubes are juxtaposed in a direction perpendicular to their greater axis, spaced from one another, the internal space of the tubes being divided by intercalary strips of a thermally conducting material into parallel first flowing channels as first flowing paths for a first fluid, a second fluid flowing through spaces between adjacent flat tubes.

Abstract: Heat exchanger provided with a housing having an inner wall, an inlet and an outlet for passing a first heat exchange medium through the housing. The housing furthermore has a core comprising a series of plate-shaped fins placed at least almost parallel to each other. Each fin is provided with pipe openings. A bundle of pipes is present for passing a second heat exchange medium, as well as a number of baffle plates, each baffle plate being provided with pipe openings. Each of the pipes extend through respective pipe openings of respective fins and respective baffle plates. Filling blocks are further provided, each having a bent base portion which has an outer surface. The bend of the base portion is such that the filling block closely abuts the inner wall of the housing. The filling block further has a rib projecting from the base portion to the centre of the housing when placed in the housing, which rib has a central slot. In said slot a respective baffle plate is accommodated.

Abstract: A multiple tube bundle heat exchanger includes axially opposite tube plates, a housing, and a plurality of tube bundles disposed between the tube plates. Each of the tube bundles is an independent tube bundle subassembly forming an integral unit having at least one heat exchanger tube with two axial tube ends. The subassembly is made from the exchanger tube and respective tube plates fastened to the two axial tube ends. The housing has a casing part defining a interior and having two axial housing ends with flanges, removable head pieces respectively disposed at the two axial housing ends to be fastened to the flanges, and partitions subdividing the interior into chambers. The number of chambers corresponds to a number of tube bundles. Each of the chambers receives one of the tube bundles. The tube plates and head pieces respectively form seals, and the tube plates delimit distributor, collecting, and/or transfer chambers formed in the head pieces.

Abstract: A heat transfer device, particularly an exhaust gas heat transfer device, having a tube bundle made of rectangular tubes for guiding the gas. A jacket surrounds the tube bundle; is used for guiding the liquid coolant and is equipped with a coolant inlet 17 and a coolant outlet 18. The rectangular tubes of the tube bundle 10 are provided with outwardly directed projections 22 which determine the distance of adjacent rectangular tubes with respect to one another and to the interior wall of the jacket 11.

Abstract: An improved heat exchanger includes a central chamber, preferably in the form of a tube, having a proximal end and a distal end. A return manifold is connected to the distal end of the central chamber. A plurality of tubes, which are preferably straight, are positioned around the central chamber. In one embodiment, two or more circumferential patterns of tubes, each at a different radius, are equally spaced around the central chamber. An exhaust manifold receives the tubes and includes an exhaust vent.

Abstract: A heat exchanger useful for preheating oxidizing gases in a combustion process includes a shell having an inlet and an outlet for the ingress and egress of a first heat exchange fluid, such as a flue gas or preheated air. A first tube manifold couples an inlet end-cap to the first end of the shell. The inlet end-cap has an inlet for receiving a second heat exchange fluid, such as an oxidizing gas. In one embodiment, a second manifold couples an outlet end-cap to the second end of the shell. The second manifold includes an outlet tube therein extending from the second manifold through an outlet opening in the outlet end-cap. A tube bundle is disposed within the shell for transporting the oxidizing gas through the heat exchanger and is coupled to the first and second tube manifolds. The outlet tube collects oxidizing gas flowing through the tube bundle for discharge to a combustion system.

Abstract: The temperature distribution in a shell and tube type heat exchanger having an expansion joint is uniformized by improving the circulation efficiency of fluid in the shell side. The uniformization is attained by the heat exchanger having an invasion-preventing plate against the fluid in the shell side attached to the expansion joint installed around the periphery of the shell, and a method of catalytic gas phase oxidation reaction that uses the heat exchanger.

Abstract: A heat exchanger for use in a sulphuric acid manufacturing plant to effect heat transfer between desired gas streams selected from air, sulphur dioxide and sulphur trioxide. The exchanger provides for hot or cold split flow gas streams through the exchanger shell with either mixing or splitting into two or more streams to provide for reduced condensible material condensation, corrosion, metal thermal differential stress and capital equipment cost. A preferred exchanger is used in combination with a sulphur burning furnace to provide an improved preheater.

Abstract: A radial flow regenerative counter flow heat exchanger includes a) a shell; b) a plurality of large circular baffle plates aligned coaxially within the shell and extending to an inner wall of the shell, defining at least one circular hole therein; c) a plurality of small circular baffle plates aligned coaxially within the shell, and alternately spaced from and coaxially positioned relative to each of the large circular baffle plates; d) a plurality of symmetrically-arranged tubes positioned perpendicular to the small baffle plates and the large baffle plates forming at least one coaxial tube bundle extending through the small baffle plates and large baffle plates, wherein an inner radius of the innermost tube row of the tube bundle is larger than a radius of the circular hole in the large baffle plate and the outer radius of the outermost tube row is smaller than a radius of the small baffle plates, and wherein the small baffle plate defines at least one space outside the tube bundle, and e) a heat transfer c

Abstract: The present invention provides a vertical falling film shell and tube heat exchanger, where the falling film is formed on the exterior surface of the tubes. A distribution plate is provided below an upper tubesheet, and a sparger plate having sparger holes is provided between the upper tubesheet and the distribution plate. A plurality of vertical, parallel tubes pass through the distribution and sparger plates and are sealingly engaged with the upper tubesheet and the sparger plate. The distribution plate has oversized holes through which the tubes pass, an annular space being defined around each tube where the tube passes through the distribution plate. The first fluid passes one time through the tubes, and the second fluid is fed to the shell side as two streams, a liquid stream and a vapor stream. The liquid stream is introduced to the shell between the upper tubesheet and the sparger plate and drains downwardly onto the second distribution plate through the sparger holes.

Abstract: This heat recovering apparatus for a cogeneration system with an engine comprises a turbocharger driven by an exhaust gas, an energy recovering turbine provided on the downstream side of the turbocharger, and a heat exchanger provided on the downstream side of the energy recovering turbine. The energy recovering turbine comprises a gas turbine driven by an exhaust gas, and a steam turbine driven by steam occurring in the heat exchanger. The heat exchanger comprises a casing joined to an exhaust gas passage, oxidation resisting ceramic pipes, in which the water and steam flow, provided in the casing, and oxidation resisting ceramic porous members, through which an exhaust gas can pass, provided in the portions of the interior of the casing which are on the outer sides of the ceramic pipes.

Abstract: A steam generator tube support plate has passageways with inwardly extending lands. Two or more tubes extend through the passageways and are supported by the lands. The tube support plates are variably spaced to provide additional support near the tubesheet and in the distal bends of U-tube bundles. This design provides reduced clogging, pressure drops and tube vibrations.

Abstract: A heat exchange catalytic process and reactor of the shell-and-tube type having a plurality of tubes extending longitudinally through the shell from a tube fluid inlet region to a tube fluid outlet region and baffles extending transversely across the shell dividing the shell between said inlet and outlet regions into at least three heat exchange zones through which each tube passes in sequence in heat exchange with that zone. A shell fluid is passed through the heat exchange zones in heat exchange with the tube fluid passing through the tubes. Transfer passages are provided connencting the heat exchange zones and are disposed so that the shell fluid passes through the second zone before or after it has passed through both the first and third zones. A particulate catalyst is disposed in either the shell heat exchange zones or, preferably, the tubes.

Abstract: A method for manufacturing a ceramic shell-and tube type heat exchanger provided with fins includes the steps of: inserting heat transfer tubes of sintered tubular ceramic into throughholes of tubular plates of unsintered plate-like ceramic each having a plurality of the throughholes for fixing the heat transfer tubes inserted thereinto; standing the heat transfer tubes vertically to a floor surface; positioning the tubular plates at both the upper and lower end portions of the heat transfer tubes; disposing between the tubular plates many fin plates of unsintered ceramic so as to pile up the fin plates in the direction of a length of the heat transfer tubes, each of the fin plates including a thin plate having a plurality of throughholes for fixing the heat transfer tubes inserted thereinto, and protrusions formed on both edge portions of the thin plate; firing the components so as to unitarily join them by the utilization of differences of firing shrinkage ratios among the heat transfer tubes, the tubular p

Abstract: A heat exchanger has an outer pressure jacket, which is provided with an entry connection for the supply of and an exit connection for the removal of a first heat exchange medium, the jacket surrounding U-shaped, bent pipes through which a second heat exchange medium flows. The pipes are mounted in a pipe supporting floor that is connected with the pressure jacket. The U-shaped pipes are surrounded by a guide jacket which is inwardly radially spaced from the inside wall of the pressure jacket and defines an intermediate annular space therewith. Inner and outer legs of the U-shaped pipes are respectively positioned on one of two concentrical partial circles. The inner pipe legs surround a central pipe which is oriented along the longitudinal axis of the heat exchanger, is connected with the entry connection, is open towards the interior of the heat exchanger, and extends from one end of the heat exchanger to the vicinity of the pipe supporting floor which is located at the other end of the heat exchanger.

Abstract: There is provided a combination for use in a shell and tube heat exchanger which comprises: a shell having a substantially horizontally extending longitudinal axis and an open end; an annular distributor adjacent to the shell end and having an annular chamber defined therein in fluid communication with the shell interior through the shell end; a tubesheet longitudinally spaced from the shell end; a baffle cage having an interior portion in the shell interior and an exterior portion outside the shell between the tubesheet and shell end, wherein the baffle cage is longitudinally spaced from and unconnected to the tubesheet; a bundle of tubes extending from the tubesheet and through the baffle cage and shell interior; and a support member having a lower end fixedly connected to the interior surface of the annular distributor and an upper end contacting but not connected to the exterior portion of the baffle cage at a lowermost location thereof.

Abstract: A heat exchanger 10 comprises a pressure vessel 14 having a feed inlet 11 in an upper part thereof for particulate material to be subjected to heat exchange and an outlet 13 at a lower part thereof for the outflow of particulate material from the vessel 14. A plurality of heat exchange elements, such as heat exchange plates 12, arranged in spaced relationship inside the pressure vessel 14 to define flow passages between adjacent heat exchange elements 12 is provided for particulate material to flow therethrough under the force of gravity. The pressure vessel 14 has an inside wall extending around the heat exchange elements 12 and further comprises a trap, such as a baffle 22, between the heat exchange elements 12 and the inside wall for trapping particulate material leaking from the flow passages between the heat exchange elements 12 to form a gas barrier 26 between the heat exchange elements 12 and the pressure vessel 14.

Abstract: A vapor compression distillation apparatus includes a vessel for containing a liquid to be distilled and a heat exchanger of the shell and tube type immersed in the liquid. The heat exchanger has top and bottom manifolds and vertical tubes surrounded by a shell. Foraminous vortex-drag induction plates extend across the shell between adjacent rows of tubes for inducing turbulence in the vortices to provide a better heat transfer from vapor passing through the shell to liquid in the tubes. Baffles are provided at selected intervals across the shell, between adjacent rows of tubes to produce a sinuous flow path for the heating medium. Steam injecting sparging tubes extend along the lower manifold of the heat exchanger to inject steam bubbles into the liquid to be evaporated. This produces turbulence in the tubes of the heat exchanger, promotes a better flow through the tubes and scrubs the tube interiors.

Abstract: An asymmetrical, or non-uniform arrangement of heat exchanging tubes in a second stage heat exchanger of an integrated flue gas treatment system provides improved flow characteristics and reduces or eliminates flooding caused by the counter-flow of upwardly rising flue gases and downwardly falling reagent and condensate through the heat exchanging tubes. The non-uniform spacing produces a non-uniform velocity profile with at least one low velocity region in each row, allowing reagent and condensate to drain downward at said low velocity region, thereby preventing high gas phase pressure drop caused by the onset of flooding. Embodiments are provided in which one of every six tubes are removed from each row in a uniform array of tubes, or one of every four tubes are removed from each row in a uniform array of tubes. Other asymmetrical, or non-uniform spacings are possible.

Abstract: The subject of the invention is a plate-type heat exchanger including a leaktight vessel (1) of elongate shape divided transversely into at least two independent segments and a plate bundle (3) arranged in the leaktight vessel (1) and formed by a stack of metal plates which are equipped with corrugations defining gaps between them. One gap in two forms a longitudinal main circuit for a first fluid A stretching along the entire length of the plate bundle (3), and the other gaps are divided transversely in order to form at least two secondary and independent circuits for the circulation of a second fluid B and at least one third fluid C and D perpendicular to the direction of circulation of the first fluid A.

Abstract: A low prime, high heat exchange efficiency oxygenator is provided which includes an oxygenation portion and a heat exchanger portion. Disposed within the heat exchanger portion is a hollow tube heat exchanger wound bundle which includes a plurality of hollow tubes knitted into a mat, the mat wound under tension into a bundle which includes from 16 to 24 layers of the mat. The oxygenator provided permits prime volumes of 180 to 240 mLs.

Abstract: The invention relates to an apparatus for exchanging heat between a small volumetric flow liquid medium and a large volumetric gaseous medium and provides for a plurality of radially disposed and interconnected concentric annular flow channels for the gaseous medium and a plurality of pipes extending axially through said annular flow channels providing flow passages for the liquid medium, said annular flow channels being preferably formed by successive convolutions of a heat insulating web.

Abstract: An impingement distributor for a shell and tube heat exchanger and a method of recovering waste heat from a hot gas which minimizes adverse heat flux at the outermost banks of tubes for enhanced operational reliability. The impingement distributor has a cylindrical distribution plate having evenly arranged rows of longitudinal perforations and a plurality of impact bars longitudinally aligned with the perforations. The hot fluid impinges on the impact bars, and direct impingement on the tubes is avoided.

Abstract: A shell and tube heat exchanger for exchanging heat between a shell side fluid and a tube side fluid has a longitudinally extending shell, a longitudinally extending tube bundle and one or more baffles positioned within the shell for directing the shell side fluid to flow across the tube bundle. One or more valves is also provided within the shell of the heat exchanger. Each valve is operable between a first position and a second position and co-operates with a baffle for adjusting the flow of shell side fluid through the shell side of the exchanger. Each of the valves is controlled by an external actuator.

Abstract: An evaporator, which includes a water chamber for receiving water to be evaporated. A plurality of evaporator tubes which when heated, and when water is on an inner wall of a tube, evaporates at least a portion of that water. A plurality of distributors spatially connecting the water chamber with the evaporator tubes in a manner so that each distributor uniformly and distributes the water from the water chamber to an inner wall of a corresponding evaporator tube. A heat source, which heats the plurality of tubes to an evaporation temperature. Apparatus distills the water vapor resulting from the water evaporation to provide distilled water.

Abstract: A heat exchanger for a multi oil furnace is disclosed wherein the external cabinet shell houses a central ventilation chamber divided into inlet and outlet sides by a generally vertical barrier. Combustion gases flow from the burner chamber into an upper bank of conduits and a lower bank of conduits, all of which pass horizontally through the ventilation chamber. Headers operably coupling the burner chamber, the upper and lower banks of conduits and a discharge opening define a flow path for the combustion gases created by the ignition of the used oil within the burner chamber. By positioning the burner chamber vertically between the upper and lower banks of conduits, the ambient ventilation air must pass over the burner chamber and the upper and lower banks of conduits twice while passing through the ventilation chamber, thereby providing a 360 degree loop of heat exchange.

Abstract: For the sealing of a gap between at least two components or groups of components which are movably arranged with respect to one another, particularly of a heat exchanger, a device is indicated in the case of which a strip-shaped sealing body, which is connected with one component, is sealingly and movably guided in a groove of the other component, and in the case of which the sealing body is composed in the manner of layers of elements, in the longitudinal direction of the gap. The layers are arranged to be displaceable and freely expandable, are suspended at one component in a swivelling manner, and are spatially movably guided on the other component by way of the groove, with a clamping effect.

Abstract: The heat exchange comprises a housing of tube-shaped inside cross-section as part of an outer thermal cycle, and at least one tube attached in the housing as part of a second thermal cycle. Each tube is formed from a flexible material. The tubes and housing comprise separate inlets and outlets, and at least one element is disposed transversely to the longitudinal housing axis to fit tightly within the housing crosssection to provide passages for the tubes. The element is shaped as a helix so that the tubes are flowed around in a helical fashion by the medium contained in the first thermal cycle. The helical element forces a flow which passes diagonally at a tangent against and around the tubes.

Abstract: Heat exchanger comprising at least one pipe bundle (5, 27, 31) for a first fluid, a jacket (1, 17) surrounding said pipe bundle (5, 27, 31), closed at each end by end pieces (2, 23, 24) through which the pipes (5, 27, 31) extend, and with at least one entrance (3, 29, 33) and one exit (4, 30, 32) for a second fluid, with baffle walls (6, 39) between the entrance and exit, perpendicular to the pipes (5, 27, 31), for reversing the direction of flow of the second fluid, whereby said baffle walls leave a passage (10) for said second fluid alternately on one side and the other of the jacket (1, 17), characterised in that the baffle walls (6, 39) are formed by at least one baffle plate (7, 28, 34) and at least one wall (8, 37, 38) extending over part of the inner circumference of the jacket (1, 17) and pointing inwards, to which is connected the outer edge of the baffle plate (7, 28, 34), so that where there is no wall (8, 37, 38), the passage (10) for the second fluid remains open.

Abstract: A vertical heat exchanger including a vertical tube bundle connected between a lower inlet manifold and upper outlet manifold. The tube bundle comprises numerous pairs of concentric tubes with the inner tube being spaced from the outer tube to form an annular flow passage positioned around an inner flow passage. The inner tubes are welded between outer tube sheets that form a part of the upper and lower manifolds while the outer tubes are welded between inner tube sheets forming part of these manifolds. Each of the manifolds has a distributor ring which has radially directed openings throughout its periphery so as to provide for a radial flow in the manifold. Fluid enters the lower manifold through suitable inlet nozzles and exits the upper manifold through suitable outlet nozzles. A high temperature heating gas is directed up through the inner tubes of each pair of tubes by a conical inlet distributor and exits the upper end of the tube bundle through a similar conical distributor.

Abstract: An improved heat exchanger utilizing a primary heated fluid to vaporize a secondary fluid flowing axially therethrough including a preheater assembly located within a cold leg side of the heat exchanger to allow axial flow of the secondary fluid through a preheater assembly to heat the secondary fluid to it boiling point temperature. The heat exchanger generally comprises a vertical shell portion with a tubesheet disposed adjacent a lower end thereof and a tube bundle which includes a plurality of U-shaped tubes through which the primary fluid flows. The preheater assembly is located in the vicinity of the tubesheet wherein the secondary fluid enters the preheater through a fluid inlet nozzle into a lower feedwater inlet box which is disposed around the inlet nozzle for dispersing the secondary fluid from the nozzle over a greater area.

Abstract: An evaporator including a frame which defines a fluid inlet plenum and an interchangeable baffle plate positioned in the plenum along with an interchangeable fluid spray bar. A transition element carries fluid from a standard round tubular fluid inlet and distributes the fluid equally across the width of the spray bar. By forming a plurality of interchangeable baffling plates each having at least one of the placement, configuration and size of holes therethrough different than the other interchangeable baffling plates and forming a plurality of interchangeable spray bars each having a different fluid outlet configuration, the baffle plates and spray bars can be interchanged to design an evaporator for air conditioners and the like with the least amount of internal fluid pressure drop and the best fluid inlet flow balance with the best heat performance.

Abstract: In a heat exchanger such as a steam generator equipping a nuclear power station the secondary fluid is injected into the upper part of an annular space (30) formed between an outer envelope (10) and a bundle or core envelope (26) having a common vertical axis. Injection takes place by means of a supply pipe (44), which issues into an overflow or weir (62). The latter has an upper horizontal edge (64) from which the secondary fluid is discharged onto a deflecting wall (54). The secondary fluid flows along this wall towards the bottom of the annular space (30). A device (60) for trapping migrating bodies can also be placed in the overflow (62) or between the latter and the deflecting wall (54).

Abstract: Heat exchange apparatus (10) for use in large vessels exposed to high thermal expansion and prone to acoustical noise and tube bundle resonance associated with high gas velocity comprises a shell (12) having a fluid inlet (14) and a fluid outlet (16). A plurality of heat exchange tubes (18, 20) are housed in the shell and extend parallel to each other substantially the length of the shell. The tubes are arranged so there is a central core (22), an inner layer (24) of tubes surrounding the central core, and an outer layer (26) of tubes surrounding the inner layer. The inner and outer layers of tubes are all in a common tube pattern. The tubes in one layer are rotated with respect to the tubes in the other layer. This results in tubes in both layers being arranged in different tube patterns in different portions or segments of each layer. That is, the pattern (34) of the tubes in one segment (28A) differs from the pattern (32) in adjoining arcuate and radial segments (28B, 28L, 30A).

Abstract: A heat exchanger has a shell baffles, tube supporting means and tubes, in addition to end caps for the shell once formed, to furnish an intergral heat exchanger. The sheet for forming the tubular sheet and baffles are formed from a singular sheet of material. The tube supporting means includes he baffles which have a plurality of openings formed therein receive the tubes. The sheet is laser or die cut to form the integral baffles and rails, for insertion into the outer tubular shell, and in a further embodiment, with its closure end caps, forming the complete heat exchanger.

Abstract: A heat exchanger for use in exchanging heat between corrosive or electrolc fluids has wetted components which are comprised of corrosion and erosion resistant materials. The use of corrosion and erosion resistant tube sheets, shell, and tubes permits the heat exchanger to operate at high flow rates to produce turbulent flow through the inlet tube sheet and tubes, thereby optimizing transfer efficiency between a corrosive fluid in the tubes and the regenerated fluid pumped through the shell.In order to eliminate problems of temperature gradient and vibrations at the area where the tubes are joined to the inlet tube sheet, the shell is comprised of an inner and outer shell section to form annular flow diverting chambers therebetween. The inner shell section of each chamber is apertured so that flow is diffused over the entire surface, thereby avoiding direct impingement of fluid over the tubes.

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: Heat exchange apparatus (10) for use in large vessels exposed to high thermal expansion and prone to acoustical noise and tube bundle resonance associated with high gas velocity comprises a shell (12) having a fluid inlet (14) and a fluid outlet (16). A plurality of heat exchange tubes (18, 20) are housed in the shell and extend parallel to each other substantially the length of the shell. The tubes are arranged so there is a central core (22) devoid of tubes, an inner layer (24) of tubes surrounding the central core, and an outer layer (26) of tubes surrounding the inner layer. The inner and outer layers of tubes are divided into segments (28, 30). The pattern (34) of the tubes in one segment (28A) is different from the pattern (32) of the tubes in the adjoining arcuate and radial segments (28B, 28L, 30A) so a checkered pattern of two different tube layouts is formed to reduce acoustical noise and prevent bundle resonance.

Abstract: A heat exchanger for exchanging heat between fluids comprising a shell and five tube bundles laid out as to collectively form a series of concentric pentagons, wherein each adjacent pair of tube bundles define an angle of 108.degree. and extend longitudinally within said shell and define a central space between them, said central space also extending longitudinally in said shell and being parallel to said tubes; each tube bundle consisting of a plurality of longitudinally extending parallel tubes in end view laid out in a set of parallel lines wherein each tube on a first parallel line with the two nearest tubes each on a second line adjacent to said first line forms an isosceles triangle having one angle of 72.degree. and two angles each of 54.degree.. This allows simple heat exchanger tube layout which is easy to fabricate and provide a compact tube bundle. The tube layout utilizes core tube entry of fluids and can accommodate internal core tubes or bypasses to cope with differential expansion.

Abstract: A shell and tube heat exchanger is disclosed in which the distribution of the fluid on the shell is substantially improved by the positioning of flow-restrictive disks on the tubes near the inlet and outlet regions of the exchanger. Positioning of the disks in other regions of the exchanger is also disclosed in order to create turbulence and increased beat transfer.

Abstract: In the finned-tube heat exchanger of silicon-infiltrated silicon carbide, in which the tubes of a tube bundle, with the cooling medium flowing around the tubes, are arranged mutually parallel in a housing provided with an inlet and outlet for the cooling medium, the tubes of the tube bundle are joined to one another by fins. The fins have apertures and are arranged transversely to the tube bundle.