Abstract: A demountable connector assembly for a modular heat exchanger permits individual modules to be removed and replaced without replacement of the entire heat exchanger core. As applied to heat exchanger modules of conventional tube and header construction, an end chamber on each end of the module has a thin flexible wall which allows axial extension of the module when it is installed between parallel inlet and outlet header surfaces to obviate the imposition of damaging stresses on the soldered connection joints between the heat exchanger tubes and the header plates. The mounting assembly also allows the headers to be temporarily sealed while a module is removed to allow continued operation of the heat exchanger until a replacement module can be installed.

Abstract: The invention disclosed herein is a single-pass, horizontal heat exchanger, of the shell and tube type, which is designed for preheating of a viscous material, such as the reactor effluent of a polyethylene solution. The heat exchanger is made in three sections, each of which can be heated independently with a heating fluid, so that a temperature profile can be easily maintained along the entire length of the exchanger. Also, each section can be removed from the exchanger unit independently of the other sections, for cleaning, if the section becomes plugged.

Abstract: A heat exchange module for use with a plurality of similar modules to form a recuperator for use in an gas turbine engine. The module has a center section with a generally rectangular cross-sectional shape, a first side section with a generally triangular cross-sectional shape, and a second side section. The module can be combined with other modules to form a polygonal recuperator with a center aperture.

Abstract: A high pressure heat exchanger has a body with spaced apart parallel plates with side walls joined to the peripheral edge of each plate; a tubular high pressure liquid inlet header external of the body; a tubular high pressure liquid outlet header external of the body; a plurality of separate tubular runs in communication with the inlet and outlet headers; each tubular run including a tubular portion between substantially all adjacent plates of the body; the tubular portions of the same run being interconnected at one end by a tubular liquid return with a tubular portion on the opposite side of a first adjacent body plate and interconnected at the other end by a tubular liquid return with a tubular portion on the opposite side of a second adjacent body plate; the body internal plates having a liquid communication opening which permits a second liquid to flow from the space on one side of a baffle plate to the space on the other side of the baffle plate in a serpentine flow path through the body while in heat

Abstract: A heat exchanger having manifolds in essentially parallel arrangement and having a special-section tube matrix which is arranged in a housing to project into a hot gas stream carried in the housing, the tube matrix being subdivided into sections and containing U-shaped reversal zones, where compressed air to be heated is admitted into the matrix via one manifold, is reversed in its direction and fed to the other manifold. The matrix sections are divided by transverse baffle walls. The ends of transverse supports extending around the tube matrix and the manifolds are connected to the housing in the vicinity of the U-shaped reversal zones, and the manifolds are supported in the housing for axial movement at both ends and are mounted rigidly on one support and axially movably on at least one further support.

Abstract: A multipass heat exchanger comprising an arrangement of a plurality of heat exchanger modules, each module having a plurality of passes for passage of a first heat exchange fluid and a plurality of tubes across such passes for passage of a second heat exchange fluid. The heat exchanger modules are disposed in side-by-side relation, with each successive module adjoining the previous module in a stepped relation, the second exchanger module being positioned relative to the first module so that the first heat exchanger fluid leaving the first pass of the first heat exchanger module enters directly the second pass of the second module, and so on, in a straight through fashion, for as many passes as desired. The result is a highly efficient multipass heat exchanger of minimum weight and pressure loss in the flow path on the shell side of the exchanger, comprised of multiple heat exchanger units, with no reversal of flow in each pass in each exchanger unit.

Abstract: The invention provides a base unit for a cross flow, tube and shell type heat exchanger comprising a substantially flat double frame consisting of an inner frame member delimiting an opening defining an element of a shell flow space, an outer frame member surrounding at least a portion of the inner member at a distance, which distance defines an element of a header flow space, at least two partition walls connecting the inner and the outer frame members and dividing the header element into an inlet header element and an outlet header element, the inlet and the outlet element being thereby separated from each other.

Abstract: A heat exchanger includes a plurality of in-line segments for alternately enveloping one fluid flow with another fluid flow with the fluid flow exchange occurring at the junction of adjacent segments through a geometric surface mathematically termed a complete embedded minimal surface. An encircling cylindrical shell defined in diameter by the perimeter of the junction surface forms the outer boundary of the in-line segments. The fluid flows may be in the same or opposed directions, depending upon the nature of the results sought by the heat exchanger in a specific environment.

Abstract: The present invention relates to a method for recovering heat and separating substances from a flue gas streaming through a heat exchange apparatus comprising a casing with heat exchange elements inserted thereinto, a medium being provided for absorbing heat from the flue gas. According to the invention the medium that shall absorb heat from the flue gas is conducted through the heat exchange elements, the heat exchange elements and the connections to the casing for flue gas being so placed that the flue gas streams perpendicularly to the heat exchange elements, the flue gas being given a flow velocity cross the heat exchange elements of not more than 3 m/sec. Soot in the flue gas is collected on the heat exchange elements and adsorbs and/or dissolves gaseous substances such as sulphur dioxide. The invention also relates to an apparatus for carrying out the method.

Abstract: A combined heat exchanger particularly suited for ammonia converter reactor effluent is described. The combined exchanger includes a first exchanger and a high temperature heat sink, such as a steam superheater, within a single exchanger shell. In a preferred embodiment, gas leaving the ammonia converter is conveyed into a single pass tube bundle which comprises the feed-effluent exchanger section and then passes through a tubesheet which separates the feed effluent exchanger section from the steam superheater section, passing over a U-tube bundle which comprises the steam superheater section in the other part of the shell. Means are provided for protecting the shell in the steam superheater section adjacent the tubesheet.

Abstract: The plumbing module is a self-contained fully operational unit which provides the capabililty of supplying both hot or room temperature and refrigerated water or other beverages. The module may be adapted without significant modification to a wide range of products and uses, including bottled water coolers, drinking fountains and beverage dispensers. A dual parallel condenser coil in the refrigeration system takes approximately one-half the space of conventional coils and provides adequate heat dissipation without requiring forced air cooling fans.

Abstract: A heat recuperator is disclosed having a plurality of serially connected tube sections enclosing a gas which is to be heated by exposing the tube sections to a second gas of elevated temperature. Parallel-flow and/or counter-flow sections of tube sections are provided such that the temperature of the tube section does not decrease below the dew point of the second gas. A particularly significant application is in the area of Compressed Air Energy Storage (CAES) systems in which the recuperator is utilized to preheat air from a storage cavern prior to combustion.

Abstract: An evaporator which is formed, in combination, of a first evaporator of a centrifugal falling-film type; and a second evaporator having a shape formed of a heating side wall portion of a downward-pointing conical configuration, a cover portion defining at least one opening, through which a liquid to be treated is charged and resulting volatile components are discharged, and a bottom portion defining at least one opening permitting discharge of an evaporation residue. A scraping agitator is built in the second evaporator. The side wall portion is externally wrapped with a pipe or the like, whereby a heating medium is caused to pass therethrough for heating the side wall portion. The evaporation residue discharge opening of the first evaporator is connected to the opening of the cover portion of the second evaporator.The above evaporator is suitable to recover a volatile component from a high-viscosity liquid containing tar-like substances. It can achieve a high recovery rate.

Abstract: A heat exchanger for gases under high pressure comprises a pressure vessel, a pluraity of heat exchanger trains arranged in the pressure vessel so that gas flows through the heat exchanger trains, the heat exchanger trains being formed as substantially identical structural units, the heat exchanger trains being connected with one another with a gas deflection therebetween and being connected with the pressure vessel so that they are releasable from and separately removable from the pressure vessel, elements for gas deflection between the heat exchanger trains, and elements for releasably and separately connecting the heat exchange trains to the pressure vessel.

Abstract: The present invention is a variable flow, multiple pass heat exchanger for use in heating various liquids to include cooking oils. The apparatus is comprised of metallic tubing disposed in a baffled stacked configuration disposed within a combustion chamber or other heating element. The tubular configuration is disposed so as to permit the passage of fluid back and forth across the heating element in an upwardly direction and then to repeat this movement in a downwardly direction through a second tubular configuration. The device is capable of being constructed to permit as many passages as are necessary to achieve the desired result. Flow is controlled by varying the number of the tubular members between sucessive tube layers.

Abstract: An apparatus in the form of an air preheater for preheating air for combustion for a combustion process by acting upon the air with hot, NO.sub.x -containing flue gases from the same or an independent combustion process. At the same time, the NO.sub.x contained in the flue gases is reduced. A regenerative or recuperative type air preheater is used, with those surfaces of the heat exchange elements which are exposed to the flue gas being provided with a coating which acts as a catalyst for the NO.sub.x reduction. The heat exchange elements are coated only in a region which has a flue gas temperature greater than the condensation temperature of the reaction products of the materials contained in the flue gas and of the added reducing agent.

Abstract: A glass tube heat exchanger including a sealing sleeve comprising at least one hydraulic sealing section, an intermediate sealing section and an interior sealing section is disclosed. The hydraulic sealing section has a triangular cross section including one obtuse angle formed by two legs, one of which extends radially outwardly from the longitudinal axis of the seal. The intermediate sealing section comprises a generally cylindrical shaped body and at least one, and preferably two, toroidal belts. The interior sealing section comprises a lip adapted to seal tightly against the glass tube and a flange adapted to seal against the tube sheet. Preferably, the interior sealing section is a mirror image of the hydraulic sealing section.

Abstract: A heat exchanger for two fluids, especially an oil cooler for oil and water in an internal combustion engine. The heat exchanger is made up of a dividing wall having a meander-like cross section which is bounded by two side covers to form longitudinal channels and having a headering system comprising cross channels, connecting channels, feed channels, and inlet and outlet openings located at each end of the heat exchanger. The heat exchanger is of modular design so that it can be easily expanded by the connection of several heat exchanger units.

Abstract: Apparatus for tempering or boiling of compositions for making molded confections, e.g., hard sugar compositions, soft sugar compositions and gelatine moulding compositions, etc., in a continuously operating production plant, involving a short length of stay of the composition, while at the same time effecting an optimum dissolution of the constituents thereof. A container, located between a composition supply duct and a composition removal duct, has several guide metal sheets spaced over the height of the container, with at least one flow opening for the compositions to be processed. At least one flow element is arranged in the axial direction of the container. The flow elements open out at their upper end and lower end into a chamber. A hot medium is passed through the flow elements, which heats the composition or the moulding composition.

Abstract: An outdoor heat exchanger section has lower and upper cabinet sections between which a generally horizontal louvered lower section top cover is disposed. The sides of the lower cabinet section are louvered to promote the entry and upward movement of air thereinto and through a heat exchange coil disposed about the inner periphery thereof. Air drawn into the lower cabinet section is discharged though the radially louvered portion of the lower section top cover. The radial top cover louvers are angled so as to partially deflect the upwardly flowing air leaving the lower cabinet section to the horizontal. The top of the upper cabinet section is essentially flat and solid and overlies the lower cabinet section top cover louvers so that neither debris nor the elements can enter the lower cabinet section from above.

Abstract: An air conditioning or refrigeration system having a subcooler (18) for subcooling liquid or hot gaseous refrigerant before the refrigerant is supplied to a heat exchanger, such as an evaporator (24) or a condenser (14). The refrigerant subcooler or precooler (18, 18A, 18B) utilized in the method and apparatus of the refrigeration system has an inner cylindrical housing (38, 38A) positioned in concentric relation to an outer cylindrical housing (48, 48A) and forming an annulus (53, 53A) therebetween. A small portion of refrigerant is diverted from the main body of refrigerant at the subcooler (18, 18A) and is passed through an expanison valve (32, 32A) for vaporizing upon entering the subcooler (18, 18A).

Abstract: The invention relates to a cooling device for a multi-stage compressor in which two coolers are placed in a common housing. The two coolers cool the medium of the preceiding stage of the multi-stage compressor heated by the input compressor work. The common housing has chambers that are divided into different pressure stages, are connected to the multi-stage compressor by inlet tubes and outlet tubes, and contain water separators with condensate removal pipes associates with them. To be able to conduct the medium to be cooled with a minimum of pressure drops, dividing walls (13, 23) are provided at a distance from the top and bottom end, respectively, of the cooling housing (50). Each dividing wall (13, 23) forms a cylindrical space (24, 14) with the housing wall (51) and the respective end walls (57, 56) of the cooling housing (50) for the installation of the water separators (15, 25).

Abstract: A gas-tight crossflow heat exchanger consisting of a metal casing with two gas inlet nozzles and two gas outlet nozzles, at least one installation cover on the top of the casing, a block consisting of a number of ceramic heat-exchange elements mounted completely accurately in cuboid form with gas ducts arranged in layers one above the other and running at right angles to each other, four side surfaces having gas-duct openings, and the bottom and top surfaces being free of openings, the heat exchanger further consisting of thermal insulation between the metal casing and the block of ceramic heat-exchange elements.

Abstract: A recuperative or restorative spiral heat exchanger with separating walls spirally extending between fluid streams of medium having an exploitable temperature gradient. Each two adjacent separating walls enclose between themselves a flow duct for one of the two streams of medium and the spiral space between two flow ducts forms the path of flow for the other stream of medium. The spiral is provided in the form of a multiple or multi-channel spiral by arranging a plurality of flow ducts. In particular, the spiral heat exchanger consists of two multiple spirals with opposed directions of current.

Abstract: A heat recuperator having a triple pass cross-flow ceramic core comprising ribbed layers bonded together has divider ribs thicker than other supporting ribs in order to provide greater seal area to adjoining layer.

Abstract: An exhaust gas containing sulfur trioxide is passed through a first heat exchanger which cools the gas to a temperature which is above the sulfur trioxide dewpoint, so that condensation of sulfur trioxide does not occur in the first heat exchanger, but below a material limit operating temperature of a second heat exchanger, which further cools the gas below the sulfur trioxide dewpoint, whereby the first heat exchanger is protected against corrosion and the second heat exchanger is protected against thermal damage.

Abstract: The heat exchanger designed, for example, for cooling highly viscous, especially intrinsically viscous free-flowing substances is provided with cooling elements (1) consisting of flat tubes which are built into a straight flow-through area (4) for the free-flowing substance to be cooled. In order to make possible a heat exchanger for intrinsically viscous, free-flowing substances which is as compact as possible, yet very effective, the cooling tubes (1) are arranged in spaced, adjacent rows in parallel planes which run obliquely to the direction of flow (X) of the heat exchanger and are at a distance from each other in the direction of flow of the heat exchanger. The cooling elements (2, 3) arranged in two adjacent planes intersect each other, viewed in the direction of flow of the heat exchanger, at an angle of 90.degree..

Abstract: Disclosed is a nuclear power plant comprising a high-temperature pebble bed reactor contained in a cylindrical steel pressure vessel in which an upper part of the cylindrical steel pressure vessel, which contains a heat utilization system, is retracted and equipped with a cover upon which circulating blowers are placed. The heat utilization system comprises, in a known manner, a single steam generator. The steam generator comprises at least two sub-systems independent of one another, with their own distributors and collectors, and with their own inlet and outlet lines. A first shut-down arrangement comprises a plurality of absorber rods insertable into bores of the side reflector from above and comprises rod drives arranged outside the steel pressure vessel in the area of its retracted upper part. A second shut-down arrangement comprises small absorber spheres for introducing into the core of the reactor, and several storage containers and annular conduits for said spheres.

Abstract: A heat exchange apparatus including a generally cylindrical hollow housing having an upper end and a lower end, and a heating device disposed in the lower portion of the housing. A heating coil assembly is disposed within the housing over the heating device, and includes a radially inner coil bank and a radially outer coil bank adjacent the inner wall of the housing. An intermediate coil bank is connected between the inner and outer coil bank and includes a plurality of helical convolutions of increasing diameter as they successively occur in an axial direction from the lower end of the housing toward the upper end thereof. A baffle frame assembly interconnects and spacially orients the inner and intermediate coil banks, and radially outwardly deflects heated gases from the heating device.

Abstract: A reaction gas cooler, including a refractory lined gas inlet, a first stage in the form of a tube bundle heat exchanger through which gas flows, an intermediate chamber, and a second stage in the form of a tube bundle heat exchanger through which gas flows. The second stage has a double flow design, which is effected by a central pipe which is disposed in the intermediate chamber and divides the second stage into an in-flow zone and a reverse-flow zone.

Abstract: A multistage evaporation boiling equipment is disclosed in the form of a single unit, each stage operating at a different pressure. Two or more bundle type heat exchanger units are horizontally positioned along a central column, part of which units protrude from the column. Attached to the protruding part of each unit is a flange which is covered by a sealing tube wall. A cover over a passageway communicating with this sealing tube wall provides a second seal. One or more walls inside the column separate the heat exchanger units. Openings, which may hold a choke means, are found in the separating wall to control passage of vapor.

Abstract: A heater comprising two separate tube nests of which one (29) heats the circulating water by condensation and supercooling and the other (39) heats a partial flow of this water by the desuperheating of steam. Steam is admitted through pipe (16). The foregoing partial flow of water comes from the desuperheating zone of a heater located downstream and is admitted through a manifold (41). Pipes (39) are wound round a central drum (43).

Abstract: A heat exchanger also serving for suppressing exhaust gas noise includes a water jacket, a water inlet header and a water outlet header together surrounding the exhaust gas flow space and a plurality heat exchanging water tubes connecting the inlet header and outlet header are provided through the gas flow space and partition walls having gas-passing connection holes is provided to partition the gas flow pass into at least two parts of mutually differing volume.

Abstract: A heat exchange device for transferring heat from a first medium to a second medium. The device includes a first chamber through which the first medium passes, a second chamber through which the second medium passes, the second chamber having a common boundary with at least a portion of the first chamber, and guide structure for causing the second medium to move in a spiral path through the second chamber and over the common boundary between the first and second chambers.

Abstract: The disclosed invention relates to a counterflow type heat exchanger composed of plural heat exchange units characterized by unique inlet and outlet headers. Each header has an end face providing an opening to the header interior and a closed end face, both of which extend obliquely from the tube sheet to join at an apex and which are symmetrically arranged with respect to each other. Such a construction enables the flow of fluid passing through each heat exchange unit to be uniform across the width of the heat exchange unit.

Abstract: A tube and support system for a heat exchanger in which a first and second series of spaced tubes extend from opposite sides of a header. Each tube extends in a serpentine pattern, with the tubes of the first series being offset from the tubes of the second series. Each tube in one of the series is bent in a manner to extend in a same plane as the other series of tubes. A support member extends between the bent tube portions and the corresponding portions of the tubes of the other series.

Abstract: A condenser-evaporator for use in a large air separation plant in which the condenser-evaporator is provided between an upper column and a lower column, the condenser-evaporator condensing nitrogen gas, ascending from the lower column through first conduit, by heat exchange with liquid oxygen flowing down from an upper column through second conduit. The condenser-evaporator includes a plurality of condenser blocks wherein the oxygen chambers of each condenser block are divided in a vertically multistage manner by partition members and wherein the nitrogen chambers of each condenser block form common passages through all the stages.

Abstract: Disclosed herein is a glue applicator for a corrugator machine in which a starch glue in a glue pan is applied to ridge portions of a corrugated core sheet by an applicator roll, the applicator comprising: a stock tank holding a stock of starch glue; a glue heater having a couple of upper and lower glue pooling chambers for reserving the starch glue supplied from the stock tank, a heat medium chamber defined between the upper and lower pooling chamber and holding a heat medium, a plural number of heat exchange pipes inserted vertically across the heat medium chamber in contact with said heat medium and communicating at the upper and lower ends with the upper and lower pooling chambers to permit flows of the starch glue between the upper and lower pooling chambers, and a steam blow pipe opened into a bottom portion of the heat medium chamber for blowing steam thereinto; and a glue feed pipe connecting the upper pooling chamber of the glue heater to the glue pan.

Abstract: A heated tank such as in a railroad tank car has a heat exchanger spaced from the bottom of the car to define a dead air space to insulate the heat exchanger from the bottom. The heat exchanger extends substantially longitudinally and transversely across the entire bottom of the car to provide a large heating transfer surface to the lading supported by the exchanger. A portion of the exchanger substantially encompasses a discharge valve of the tank car to provide heat transfer to the valve during unloading. The heat exchanger slopes toward the discharge valve to facilitate total removal of the lading. An inlet and an outlet associated with the heat exchanger are disposed adjacent the discharge valve for additional transfer of heat to the discharge valve. Baffles in the heat exchanger define a plurality of serpentine passages for conducting a heating medium.

Abstract: The Claus process gas is cooled in a condenser to condense most of the sulfur vapor in solid form. The gas leaving the condenser is then further cooled to condense water without producing substantially any sulfur in an undesirable form. The resulting gas of reduced water content is useful in Claus reaction, particularly the low temperature Claus reaction in which the product sulfur is adsorbed on the catalyst.

Abstract: A heat exchanger including a plurality of tubes arranged in at least three side-by-side planes, the tubes being held at their ends in the sidewalls of an even-sided polygon of at least six sidewalls, each sidewall being connected to its opposite sidewall by tubes in at least one of the planes.

Abstract: An annular heat exchanger assembly includes a plurality of low thermal growth ceramic heat exchange members with inlet and exit flow ports on distinct faces. A mounting member locates each ceramic member in a near-annular array and seals the flow ports on the distinct faces into the separate flow paths of the heat exchanger. The mounting member adjusts for the temperature gradient in the assembly and the different coefficients of thermal expansion of the members of the assembly during all operating temperatures.

Abstract: A heat exchange apparatus includes a core mounted within a casing and two fans arranged to draw air from the exterior of a building through the core in a first path and to draw air from the interior of the building through the core in a second path. The core is made up from a plurality of tubular cells each formed from a single folded sheet of aluminum and having a slot shaped cross section. The short sides of the slot are arranged to face the inlet of cold exterior air so that it impinges upon the outer surface of the short side. The fan drawing the warm air is arranged to direct air onto the other surface of the short side so that the short side and the surrounding portions of the long sides act as an effective heat exchange surface free from the seam of the tubular core which is arranged adjacent opposite the short side. A differentially perforated baffle plate spreads the cold air over core such that more cold air is directed to the warm end of the core.

Abstract: A modular bundle of tubes for a steam condenser comprises two perforated plates (24, 25), a series of tubes (22) interconnecting the perforated plates, and a set of intermediate supporting plates (23) distributed between the two perforated plates. The improvement wherein both perforated plates are the same size, each being surrounded by a reinforcing frame (24, 25) which is thicker than the perforated plate, and wherein drawbars (26) fitted with length-adjusting means (27) interconnect the perforated plates, said drawbars being fixed to said frames and being distributed along the said frames.

Abstract: Exhaust gas treatment method and apparatus extract heat from an exhaust gas by operating in a water-condensing mode which allows more heat to be recovered, removes particulate matter and condensed acid from the exhaust gas, and washes heat exchange surfaces to keep them clean and wet to improve heat transfer. Systems for heating water, air and both water and air are disclosed. Methods of constructing and assembling improved heat exchangers are disclosed.

Abstract: A heat exchanger serving for the heating of an organic transfer liquid by combustion gases from a burner has a metallic housing in the shape of an upright cylinder with a widened upper part; the transfer liquid flows through an inner coil extending over nearly the full height of the housing and in series therewith through an outer coil surrounding the inner coil in the widened upper part. The two coils are enveloped by combustion gases, generated within or outside the housing, which rise from its bottom to the top inside the inner coil and then descend around the outer coil to an exit port provided near the lower end thereof. The top, bottom and upper cylinder part are overlain by conduits carrying a cooling fluid, preferably the same transfer liquid; in a preferred embodiment, these conduits are designed as half-pipes welded onto the outer housing surfaces to form cooling channels.

Abstract: A cooling arrangement for a liquid-cooled internal combustion engine with combined seawater-fresh water cooling is disclosed. The arrangement comprises a first heat exchanger for seawater-fresh water exchange and a second heat exchanger for seawater-lubricating-oil heat exchange, and a housing within which the first and second heat exchangers are arranged. The housing includes an inlet duct, a short-circuit duct and a thermostat for fresh water. An additional thermostat and an exchange filter for the lubricating oil are provided adjacent to the first and second heat exchangers.

Abstract: A heat exchanger of the shell and tube type particularly suitable as an intercooler between compression stages of a compressor is disclosed. The heat exchanger includes a generally cylindrical shell having first and second coil banks disposed therein. The banks are spaced from each other and from the wall of the shell. The incoming fluid flows between the heat exchange coil banks and outwardly therethrough, passing in heat exchange relationship with a fluid flowing through the coils. The fluid velocity is reduced, substantially minimizing carryover of liquid in the fluid, and directional changes in the fluid flow causes disentrainment of liquid. A sump is provided in the bottom of the heat exchanger for removing the condensed liquids, and separate demistors or separators are not required. Access to the coils for cleaning and/or servicing may be had through a manway disposed in the shell, or through an openable end of the shell.

Abstract: A recuperative tubular heat exchanger comprised of a plurality of tube-bundle heat exchange modules (20) stacked in a spaced array and interconnected by U-shaped, open-end header conduits (30) to form a serpentine flowpath through which a fluid to be heated is passed in heat exchange relationship with a heating fluid passing in cross flow over the tube bundle modules. The interconnected modules together with the header conduits form an integral assembly which is free to slide on support beams (26) so as to float within the housing (12) of the heat exchanger in response to the thermal deformation of the tube bundle modules.

Abstract: A method of and system for removing silicon from a high temperature liquid sodium coolant system for a nuclear reactor. The sodium is cooled to a temperature below the silicon saturation temperature and retained at such reduced temperature while inducing high turbulence into the sodium flow for promoting precipitation of silicon compounds and ultimate separation of silicon compound particles from the liquid sodium.