US3745978A - Apparatus for drying and superheating steam - Google Patents

Apparatus for drying and superheating steam Download PDF

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Publication number
US3745978A
US3745978A US00203311A US3745978DA US3745978A US 3745978 A US3745978 A US 3745978A US 00203311 A US00203311 A US 00203311A US 3745978D A US3745978D A US 3745978DA US 3745978 A US3745978 A US 3745978A
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Prior art keywords
shell
banks
steam
inlet
superheater
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US00203311A
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English (en)
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M Armand
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Babcock Atlantique SA
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Babcock Atlantique SA
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    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F22—STEAM GENERATION
    • F22G—SUPERHEATING OF STEAM
    • F22G1/00—Steam superheating characterised by heating method
    • F22G1/005—Steam superheating characterised by heating method the heat being supplied by steam
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F22—STEAM GENERATION
    • F22B—METHODS OF STEAM GENERATION; STEAM BOILERS
    • F22B37/00—Component parts or details of steam boilers
    • F22B37/02—Component parts or details of steam boilers applicable to more than one kind or type of steam boiler
    • F22B37/26—Steam-separating arrangements
    • F22B37/266—Separator reheaters

Definitions

  • the present invention relates generally to apparatus serving to remove water from a damp saturated steam and then to heat the resulting dry saturated steam in order to form superheated steam.
  • the invention applies particularly to thermal electricity generating installations which use steam as working fluid.
  • Superheater driers associated with these installations generally comprise a horizontally elongated cylindrical casing in which there are a bottom zone containing a wet steam distributor and a water extractor, and an upper zone in which the dry steam bathes a surface exchanger forming a superheater.
  • the object of the present invention is to provide an apparatus for drying and heating steam which overcomes these problems and, in particular, permits the selection of a smaller number of superheater-driers of high individual power in a given water vapour generation and utilisation installation.
  • Another object of the invention is to provide a superheater pennitting substantial reductions of volume of the superheater-drier appliances of the type described above, facilitating their supervision, maintenance, and repair, as well as the arrangement of their outlet apertures, more effectively feeding these appliances with wet steam, and more conveniently discharging the water extracted from this steam.
  • the superheater is a bank of rectilinear tubes parallel to 'the axis of the shell in which they are accommodated.
  • this bank of tubes is given as compact a shape as possible so that, viewed in cross-section, its height dimension is equal or substantially equal to its width dimension.
  • apparatus of this kind it is customary to circulate the steam to be treated from bottom to top,'causing it to pass in succession through the drier and the superheater, so that the space available for the latter is substantially greater in width than height.
  • Another object of the invention is to provide an apparatus which takes advantage of this circumstance, without complicating the construction and does so by making the superheater in the form of a plurality of independent banks of tubes parallel to the axis of the shell and disposed side by side in the width of the shell.
  • an apparatus for drying and heating steam comprising a horizontally elongated shell, a surface exchanger forming a superheater, inlet and outlet means in said casing for circulating the steam therein from bottom to top along a path successively passing through a moisture: extractor and said surface exchanger, outlet apertures to said casing for these exchanger elements, said superheater being composed of a plurality of independent banks of tubes which are elongated in the longitudinal direction of said shell and in cross-section occupy less space in height than in width.
  • the superheater is divided not only in width but also in the direction of its length, and is in the form of a' plurality of parallel rows, each of which is composed of a plurality of independent banks of tubes placed end to end over the entire length of the shell.
  • each bank it is advantageous for each bank to be placed on a running track to facilitate its removal and replacement; according to another characteristic, the outlet apertures, each of which is reserved for one bank or one row of banks, are distributed in equal shares over the two end walls of the shell, thus substantially reducing the problems of constructionof these walls, each of which is provided with only half the openings necessary for the entire superheater.
  • the banks disposed at a plurality of levels form superimposed groups, each of which is associated with an individual source of heating fluid and which constitute a plurality of superheating stages.
  • a wet steam distributor of the invention is provided with at least one inlet passing through the bottom of the shell at an intermediate point on the latter and serving, on each side of that intermediate point, a plurality of feed ducts which have perforated walls and which are disposed in the lengthwise direction of the shell and are situated on each side of the transversal plane of the apparatus at the aforesaid admission point.
  • the ducts are transversely independent of the shell and are situated at a distance from the inner face of the shell to permit the free flow of water along this face, and the top wall of each duct projects horizontally over its perforated walls, thus preventing the water which falls from the extractor from trickling along the perforated walls and overloading with moisture the steam to be treated.
  • FIG. 1 shows in longitudinal axial section a superheater-drier of the invention
  • FIG. 2 is a plan section along the line II-II in FIG.
  • FIG. 3 is a diagrammatic end view in the direction of the arrow III in FIG. 1;
  • FIG. 4 is a diagrammatic cross-section along the line lV-IV in FIG. 1;
  • FIG. 5 illustrates on a larger scale and in greater detail an end portion of the apparatus, situated on the left in the view shown in FIG. 1;
  • FIGS. 6 and 7 show on a still larger scale two details of FIG. 5;
  • FIG. 8 is a partial cross-section on a larger scale, taken along the line VIIIVIII in FIG. 2 but limited to the portions of the apparatus situated above the horizontal sectional plane II-II;
  • FIG. 9 is a longitudinal axial section in elevation of the middle portion of the apparatus.
  • FIG. 10 shows on a larger scale a detail of construction relating to FIG. 9;
  • FIG. 11 is a partial cross-section on a larger scale, taken along the line IV-IV in FIG. 1 and limited to the bottom portion of the apparatus;
  • FIGS. 12 and 13 show wet steam distribu-tion ducts in cross-section and on a still larger scale.
  • the apparatus illustrated in the drawings comprises, inside a horizontally elongated casing V, a drier S, a wet steam distributor D, and a superheater E.
  • the drier is a mattress of metal fabric disposed along a horizontal plane in the bottom half of the casing V, in such a manner as to divide into two unequal portions the entire space bounded by the cylindrical wall 1 of the casing V and by its end vertical partitions 2 and 3.
  • the space situated beneath the drier S receives the distributor D, which is served by dry steam inlet connection 4, 5, and the upper space occupied by the superheater E is served by three dry steam outlet connections 6, 7, 8.
  • a series of water drains 9 are disposed along the bottom generatrix of the shell 1.
  • the wet steam entering through the connections 4, 5, and distributed by the distributor over the entire length of the apparatus, passes from bottom to top through the mattress S, which retains the water contained therein, and then bathes the superheater E, constituted by a tubular bank surface exchanger.
  • the steam thus superheated is directed towards its utilisation point through the outlet connections 6, 7, 8.
  • the shell 1 is stiffened and surrounded on its outer face by two circular carrier frames 10, which transmit the loads of the apparatus to supports 11 with the aid of expansion bearings 12. At its two ends it terminates in two hemispherical domes l3 and 14 respectively, which are curved outwardly and which are connected to the shell 1 in vertical planes defined by the previously mentioned terminal partitions 2, 3. These partitions, welded over their entire periphery to the inner face of the shell, are each provided with six circular passage apertures 15 (FIG. 5), which are intended for six respective banks of tubes, to which further reference will be made hereinbelow.
  • Two middle vertical partitions 16, 17, closely spaced one on each side of the median transversal plane of the apparatus are each bounded (FIG. 8) by a top horizontal edge 18, a bottom horizontal edge 19, and two edges 20 in the form of arcs of circles, along which they are welded to the inner face of the shell.
  • In each of these median partitions are provided six circular passage apertures 15 intended for the same purposes as the previously mentioned apertures 15.
  • the beams 21 nearest the inner face of the shell each carry a running rail 22 on their upper flange, two rails 22 resting similarly on the top flange of each of the intermediate beams 21. All these rails, which pass through the space between the two middle partitions l6, 17, form together three upper running tracks which extend without interruption from the partition 2 to the partition 3.
  • Three bottom running tracks are similarly formed by rails 22 suspended on the bottom flanges of the beams 21, or by rails 23 resting directly on these flanges.
  • the space bounded by the shell 1, the partitions 2, 16, and the mattress S receives six horizontally elongated banks of tubes which form half of the heat exchanger E intended to superheat the steam.
  • Three of these banks are composed of tubes T bent into U-shape or hairpin shape, the bent portions of which project over the partition l6, penetrating into the space bounded by the 7 two intermediate partitions 16, 17, while the ends of their parallel rectilinear branches are connected to a tubular plate 24 situated in line with the terminal partition 2 (FIG. 5) (the banks of tubes may also be constituted by straight tubes between two tubularplates).
  • a hemispherical cap 25 forms together with the plate 24 a box divided by a partition 26 into two compartments 27 and 28 which serve respectively for the admission and discharge of a heating fluid, each U-tube being in communication by one of its two rectilinear branches with the compartment 27 and by its other rectilinear parts with the compartment 28.
  • These two compartments are connected to service connections and piping, partly illustrated and not given references, which pass through the terminal dome l3 and which, since they may be of any known type, will not be described in greater detail.
  • the cap 25 is provided with one or more inspection windows 29 provided with covers.
  • the tubes pass through a circular plate 30 the outer face 31 of which is flush with the inner face 32 of the corresponding middle partition, while its peripheral edge 33, situated in the space between the two intermediate partitions 16, 17, is surrounded by a sealing guide ring-composed of a plurality of segments 34 bolted on the inner face 32 of the intermediate partition.
  • the inner face 35 of the tubular plate 24 is flush with the inner face 36 of the end partition 2.
  • the tubular plate 24 On its periphery the tubular plate 24 has a groove or slot 37 of rectangular profile, which receives a circular retaining collar composed of a plurality of segments 38 bolted on the outer face 39 of the end partition 2.
  • each bank C has in crosssection a profile of space occupied of a rectangular shape.
  • the tubes, fitted with spacing and support elements (not illustrated) transfer the loads of the bank to two vertical plates 40, which frame it on both sides and which are provided with wheels 41 resting on one of the running tracks previously mentioned.
  • the other three banks of tubes on the left-hand half of the apparatus which are designated by the reference A, comprise the same elements as the banks C (designated by the same reference numbers), except as regards the heating fluid admission and discharge box.
  • the tubular plate 24 of a bank A is connected to a cylindrical sleeve 42 which, passing through the terminal dome 13, projects to the outside and tenninates in a hemispherical cap 43.
  • a partition 44 separates into two compartments 45, 46 for the admission and discharge of heating fluid respectively the space bounded by the elements 24, 42, 43, which form a distribution box capable of passing freely through the corresponding hole 15.
  • the hemispherical cap 43 is provided with one or more inspection holes 47 with covers.
  • the sleeve 42 is surrounded by a coating sleeve 48, which also passes through the dome l3 and projects to the outside.
  • the sleeve 48 is welded on the one hand to the dome 13, on the periphery 49 of the passage aperture provided in the latter, and on the other hand, by its outer edge 50, to a spacer ring 51 welded on the other face of the sleeve 42.
  • the sleeve 48 is gripped in asealing and guide ring composed of a plurality of segments bolted on the outer face 39 of the partition 2.
  • the bank A is provided with sealing and guide elements 30, 34 similar to the elements bearing the same references with which the banks C are equipped, and the same applies to the support and running elements 40, 41.
  • the banks of tubes are thus fixed at their outer end either by embedded collars 38 (banks C) or by welding 50 (bank A), but are free to expand in length under the action of temperature.
  • the six banks A, C of the left-hand half of the apparatus form two rows superimposed vertically and each composed of three banks placed side by side at the same level, each of them having its own source of heating fluid, the heating fluid of the upper row being hotter at the inlet than that of the bottom row.
  • the wet steam inlet connection 4 is situated approximately half-way along the length of the half of the apparatus situated on the left in FIG. 1.
  • This connection which passes through the shell 1 at the bottom, is crowned by a hemispherical dome 61, from which start six ducts which form two groups each of three ducts, these two groups being disposed one on each side of the transverse] plane of the apparatus situated in line with the inlet connection 4 and defined by its trace YY (FIG. 2).
  • Each group is composed of a central duct 62 and two side ducts 63.
  • the central duct shown on a larger scale in FIG. 12, is composed of a plurality of folded sheet metal elements welded to one another. It has a bottom 64, two vertical side walls 65, 66 and a top wall 67 in the form of a roof with two sloping sides bordered by two gutters 68.
  • the vertical walls which are set back in relation to the gutters 68, are provided with perforations 69.
  • These same walls approach one another progressively starting from the inlet connection, in such a manner as to give the duct 62 a tapered shape in plan view (FIG. 2) and to give it the form of a blind duct the outlet apertures of which are formed exclusively on its side walls 65, 66.
  • the side ducts 63 are functionally similar to the duct 62 and differ from the latter only in respect of shape. Their elements corresponding to those of the .duct 62 are designated by the same reference numerals accom-panied by the prime index, and their bottom 64' is inclined as the consequence of the incurved shape of the bottom of the shell 1, instead of being horizontal like the bottom 64 of the duct 62. y l
  • the right-hand half of the apparatus contains the same elements as the left-handhalf.
  • it is provided with six banks of tubes, three of which are of the type A and three of the type C, and these banks are situated respectively in line with the six banks A and C of the left-hand part.
  • the heat exchanger E is therefore composed of six rows of banks, each row being formed of two banks placed end to end. The banks are disposed in such a manner that each of these rows contains one bank of type A and one of type C.
  • the banks of one side are staggered in. relation to those of the other type (FIG. 3).
  • the two middle partitions l6, 17 are connected together along their top edges by a plate 71 provided with a covered manhole 73, and along their bottom edges by a plate 72.
  • These plates plates 71, 72 constitute baffles which prevent the steam from short-circuiting the banks of tubes and force it to pass through the latter before leaving the apparatus through the connections 6, 7, 8.
  • the wet steam distribution ducts 62, 63 are entirely clear of the inner faces of the shell 1 and do not form an obtacle to the flow of water along these walls.
  • the wet steam admitted at the connections 4 is distributed by the ducts 62, 63 over the entire length of the apparatus, leaves these ducts through the perforations 69, 69', and passes through the mattress S from bottom to top, the uniform feeding of steam over the length of this mattress being assisted on the one hand by the arrangement of the ducts in a plurality of longitudinal rows distributed over the width of the apparatus, and on the other hand by the progressively decreasing cross-section of the ducts, starting from the point of admission of the wet steam.
  • the water given up by the wet steam in the mattress S falls either along the inner faces of the shell, which conduct it without obstruction to the drains 9, or on the roofs 67, 67 and thence to the gutters 68, 68', which conduct them in a falling slope to the dome crowning the corresponding admission connection 4 or 5, and Finally to the bottom of the shell and to the drains 9.
  • the water which falls off the mattress S is thus prevented from remixing with the wet stream which leaves the apertures 69, 69'.
  • tubular plates and the connections of tubes to these plates are inspected directly from the outside, through the windows 47 in the case of the banks A.
  • the operator inspects them through the windows 29 after entering the apparatus through the manhole 74 or 75.
  • a bank A is removed by cutting away the corresponding coacting sleeve 48 along the transversal plane HH (FIG. 5) and removing the sealing and guide ring 34, whereupon the bank is moved towards the outside on its running track.
  • HH transversal plane
  • the bank A situated in line with it is moved out in the manner described above, and it is moved along the same outward path along the track freed by the bank A.
  • the arrangements according to the invention therefore make it possible to provide only six outlet apertures for the twelve banks of tubes, and to provide only It should be pointed out that the partitioning elements, such as terminal and middle partitions, sealing rings and the like, are arranged so as to prevent the short-circuiting of the banks of tubes by the steam to be superheated, and not in such a manner as to create differences of pressure on each side of these partitioning elements.
  • the partitioning elements such as terminal and middle partitions, sealing rings and the like, are arranged so as to prevent the short-circuiting of the banks of tubes by the steam to be superheated, and not in such a manner as to create differences of pressure on each side of these partitioning elements.
  • An apparatus for drying and heating steam comprising a horizontally elongated shell, a surface exchanger forming a superheater, inlet and outlet means in said casing for circulating the steam therein from bottom to top along a path successively passing through a moisture extractor and said surface exchanger, outlet apertures to said casing for these exchanger elements, said superheater being composed of a plurality of independent banks of tubes which are elongated in the longitudinal direction of said shell and disposed side by side throughout the substantial width of the shell, said bank being of cross-section occupying less space in height than in width.
  • each said bank occupies only a fraction of the length of said shell.
  • An apparatus characterised in that said banks are distributed in rows, each of which is composed of a plurality of banks disposed end to end from one end to the other of the apparatus, each said row being provided with a single outlet aperture disposed in an end wall of said shell.
  • An apparatus characterised in that said banks of tubes are disposed at a plurality of levels.
  • An apparatus characterised in that said banks form a plurality of stages, each of which has an individual heating fluid inlet, to constitute a plurality of superheating stages.
  • An apparatus characterised in that said banks are distributed in vertically aligned groups of banks, said banks of one of these groups being provided with a common support formed by two longitudinal beams situated one on each side of this group.
  • each said bank is placed on a longitudinal running track.
  • each said bank is framed laterally by two plates in erect positions which serve to support it and which are provided with wheels resting on said running track.
  • An apparatus characterised by partitioning elements disposed in contact with the bottom and/or top edges of theside support plates of said banks and forming with said plates guide paths for the steam through said banks.
  • An apparatus for drying and heating steam comprising a horizontally elongated shell, a surface exchanger forming a superheater, inlet and outlet means in said casing for circulating the steam therein from bottom to top along a path successively passing through a moisture extractor and said surface exchanger, outlet apertures to said casing for these exchanger elements, said superheater being composed of a plurality of independent banks of tubes which are elongated in the longitudinal direction of said shell and disposed side by side in the width of the shell, said bank being of crosssection occupying less space in height than in width, at least those of the banks which are disposed side by side being all of the same length and forming a group equipped at each end with a flat erect partition providing for each bank a passage hole equipped with a perforated plate through which the tubes of said bank pass, said two erect partitions being connected fluid-tightly to said shell and forming between them a guide path for the steam through said banks of said groups.
  • An apparatus for drying and heating steam comprising a horizontally elongated shell, inlet and outlet means for circulating the steam therein from bottom to top along a path passing in succession through a moisture extractor and a surface exchanger forming a superheater, a wet steam inlet comprising at least one inlet passing through the bottom of said shell at an intermediate point therein and feeding a plurality of distribution ducts which have perforated walls and extend in the longitudinal direction of said shell and disposed on each side of the transversal plane of the apparatus situated in line with said inlet point.
  • An apparatus characterised by' a plurality of such inlets which are spaced over the length of the apparatus, the ducts of each inlet extending only over a fraction of said length.
  • An apparatus characterised by water collection and evacuation gutters bordering the top walls of said ducts.
  • An apparatus characterised in that said ducts are situated at a distance from the wall of said shell, in such a manner as not to obstruct the flow of water along said wall.
  • An apparatus characterised by a plurality of water drains spaced out along the bottom generatrix of said shell.
  • An apparatus for drying and heating steam comprising a horizontally elongated shell, a surface exchanger forrning a superheater, inlet and outlet means in said casing for circulating the steam therein from bottom to top along a path successively passing through a moisture extractor and said surface exchanger, outlet apertures to said casing for these exchanger elements, said superheater being composed of a plurality of independent banks of tubes which are elongated in the lon- I gitudinal direction of said shell and in cross-section occupy less space in height than in width, at least those of the banks which are disposed side by side being all of the same length and forming a group equipped at each end with a flat erect partition providing for each bank a passage hole equipped with a perforated plate through which the tubes of said bank pass, said two erect partitions being connected fluidtightly to said shell and forming between them a guide path for the steam through said banks of said groups, one of said perforated plates which is situated at the end of the
  • An apparatus for drying and heating steam comprising a horizontally elongated shell, inlet and outlet means for circulating the steam therein from bottom to top along a path passing in succession through a moisture extractor and a surface exchanger forming a superheater, a wet steam inlet comprising at least one inlet passing through the bottom of said shell at an intermediate point therein and feeding a plurality of distribution ducts which have perforated walls and extend in the longitudinal directionof said shell and disposed on each side of the transversal plane of the apparatus situated in line with said inlet point, said ducts having a polygonal profile, composed of two perforated vertical walls, a roof with gutters projecting beyond the line of said walls, and a floor situated at a distance from the bottom of said shell. 7
  • An apparatus for drying and heating steam comprising a horizontally elongated shell, inlet and outlet means for circulating the steam therein along a path passing in succession through a moisture extractor and a surface exchanger forming a superheater, said moisture extractor being a foraminous wall extending lengthwise of the shell and dividing the chamber defined thereby into a lower space and a higher space with the latter containing the superheater, a wet steam inlet comprising at least one inlet passing through the bottom of said shell at an intermediate point therein and feeding a plurality of distribution ducts which have perforated walls and extend in the longitudinal direction of said shell within said lower space and disposed on each side of the transversal plane of the apparatus situated in line with said inlet point.

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  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Drying Of Solid Materials (AREA)
  • Freezing, Cooling And Drying Of Foods (AREA)
US00203311A 1970-12-02 1971-11-30 Apparatus for drying and superheating steam Expired - Lifetime US3745978A (en)

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Application Number Priority Date Filing Date Title
FR7043292A FR2116645A5 (enrdf_load_stackoverflow) 1970-12-02 1970-12-02

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US3745978A true US3745978A (en) 1973-07-17

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US (1) US3745978A (enrdf_load_stackoverflow)
JP (1) JPS5218326B1 (enrdf_load_stackoverflow)
CH (1) CH553374A (enrdf_load_stackoverflow)
DE (1) DE2158920A1 (enrdf_load_stackoverflow)
FR (1) FR2116645A5 (enrdf_load_stackoverflow)
GB (1) GB1372205A (enrdf_load_stackoverflow)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4114684A (en) * 1977-04-11 1978-09-19 General Electric Company Tube support system for heat exchanger
US4708093A (en) * 1985-06-22 1987-11-24 L. & C. Steinmuller Gmbh Apparatus for drying and superheating steam
US5042432A (en) * 1989-01-19 1991-08-27 Stein Industrie Superheat bundle for a horizontal tube steam separator-superheater
US6701067B2 (en) * 2001-09-22 2004-03-02 Rieter Icbt Vapor phase heaters
US20090288418A1 (en) * 2006-08-28 2009-11-26 Issaku Fujita Moisture separator

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2553867B1 (fr) * 1983-10-19 1985-12-27 Stein Industrie Separateur surchauffeur de vapeur et son procede de montage

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2256882A (en) * 1939-03-11 1941-09-23 Griscom Russell Co Heat exchanger
US2995343A (en) * 1957-07-29 1961-08-08 Griscom Russell Co Heat exchanger construction
US3574303A (en) * 1968-09-30 1971-04-13 Westinghouse Electric Corp Moisture separator reheater for pressurized vapor
US3667430A (en) * 1970-06-04 1972-06-06 Gen Electric Modular combined moisture separator and reheater

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2256882A (en) * 1939-03-11 1941-09-23 Griscom Russell Co Heat exchanger
US2995343A (en) * 1957-07-29 1961-08-08 Griscom Russell Co Heat exchanger construction
US3574303A (en) * 1968-09-30 1971-04-13 Westinghouse Electric Corp Moisture separator reheater for pressurized vapor
US3667430A (en) * 1970-06-04 1972-06-06 Gen Electric Modular combined moisture separator and reheater

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4114684A (en) * 1977-04-11 1978-09-19 General Electric Company Tube support system for heat exchanger
US4708093A (en) * 1985-06-22 1987-11-24 L. & C. Steinmuller Gmbh Apparatus for drying and superheating steam
US5042432A (en) * 1989-01-19 1991-08-27 Stein Industrie Superheat bundle for a horizontal tube steam separator-superheater
US6701067B2 (en) * 2001-09-22 2004-03-02 Rieter Icbt Vapor phase heaters
US20090288418A1 (en) * 2006-08-28 2009-11-26 Issaku Fujita Moisture separator
US7993426B2 (en) * 2006-08-28 2011-08-09 Mitsubishi Heavy Industries, Ltd. Moisture separator

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Publication number Publication date
FR2116645A5 (enrdf_load_stackoverflow) 1972-07-21
JPS5218326B1 (enrdf_load_stackoverflow) 1977-05-20
DE2158920A1 (de) 1972-06-29
GB1372205A (en) 1974-10-30
CH553374A (fr) 1974-08-30

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