US2256115A - Separator - Google Patents

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US2256115A
US2256115A US178164A US17816437A US2256115A US 2256115 A US2256115 A US 2256115A US 178164 A US178164 A US 178164A US 17816437 A US17816437 A US 17816437A US 2256115 A US2256115 A US 2256115A
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steam
space
drum
water
separator
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US178164A
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James C Hobbs
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    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F22STEAM GENERATION
    • F22BMETHODS OF STEAM GENERATION; STEAM BOILERS
    • F22B37/00Component parts or details of steam boilers
    • F22B37/02Component parts or details of steam boilers applicable to more than one kind or type of steam boiler
    • F22B37/26Steam-separating arrangements
    • F22B37/265Apparatus for washing and purifying steam
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F22STEAM GENERATION
    • F22BMETHODS OF STEAM GENERATION; STEAM BOILERS
    • F22B37/00Component parts or details of steam boilers
    • F22B37/02Component parts or details of steam boilers applicable to more than one kind or type of steam boiler
    • F22B37/26Steam-separating arrangements
    • F22B37/30Steam-separating arrangements using impingement against baffle separators
    • F22B37/303Steam-separating arrangements using impingement against baffle separators specially adapted for boiler drums

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  • the present invention relates in general to the construction and operation of gas washing and separating apparatus and more particularly to apparatus of this type which is adapted tobe incorporated in the steam and water drum of a specific object is the provision of moisture separating apparatus of the above type which is further characterized by a uniform distribution of the separating load throughout the separator surface, its ease of installation,accessibility of the associated tube connections, low pressure drop and velocity flow through the separating parts, compactness, and simplicity of construction.
  • Another specific object is the provision of gas washing apparatus of the type described which is further characterized by the passage of the vapor being treated in successive effective washing contacts with the washing liquid and by its effective arrangement relative to the associated separating apparatus.
  • Fig. 1 is a somewhat diagrammatic sectional elevation of a high pressure steam and water drum having steam washing and separating pro-' visions constructed and arranged according to my invention
  • Fig. 2 is a view similar to Fig. 1 illustrating I a modified construction
  • Fig. 3 is a view similar to Figs. 1 and 2 illustrating a second modification
  • Fig. 4 is a transverse section taken on the line 4-4 of Fig. 3;
  • Fig.5 is a view similar to Figs. 1, 2 and 3, illustrating a third modification
  • Fig. 6 is a transversev section taken on the line 6-6 of Fig. 5.
  • Fig. 1 I have illustrated a relatively small diameter thick walled drum II) as constructed for the steam and water drum of a high capacity high pressure steam generating unit, the normal water level in the drum being indicated by the broken line I I.
  • the drum receives the discharge from a multiplicity of steam generating tubes I2 opening through the .drum wall alongv the length of and below the normal water level in the drum.
  • Submerged downcomer tubes l3 are also radially connected to the bottom of the drum at one side of the tubes I2.
  • Steam outlet tubes I4 open to the upper part of the steam space of the drum.
  • the drum includes provisions for successively efiecting a primary separation of the steam and water, washing of the steam, and a secondary separation of the moisture from the washed steam.
  • the primary separating provisions include a transversely curved ballle 20 extending from the bottom of the drum between the riser tubes l2 and downcomers l3 to a point above the normal water level.
  • the batlle 20 is divided into sections longitudinally of the drum, each section having its lower end hinged to the drum wall, as indicated at 2
  • the baflle plate 23 is suitably supported in the position shown and provided with upper and lower laterally extending plates 25 and 26 sloping towards the adjacent portion of the drum Wall.
  • An inwardly sloping plate 21' extends from the drum wall towards and intermediate the plates 25 and 26 and provides. a sinuous flow path for the ascending wet steam between the baflle plate 23 and the drum wall.
  • the space enclosed by the baflles 20 and 23 extends the full length of the portion of the drum to which the tubes [2 and I3 are connected and may be wholly or partly closed at its ends.
  • a submerged portion of each curved baflle section 20 is of double walled construction to form a passage 28 therein opening to the remaining portion of the drum water space.
  • pipes 30 are connected to some or all of the discharge ends of a group of economizer tubes 3
  • Each pipe 30 extends upwardly into the steam space of the drum to a slotted sections.
  • V I r The separator section 42 is locatedadjacent" the ends of the steam outletpipes l4. All of I 4 from the separator sections.
  • tubes I2 passes across the water space of the drum and impinges against the bafiie plate whereby the fluid jets are broken up, facilitating .the separation, of the-steam-bubblespand the discharge distributed' over, the water surface area in' the chamber.
  • the steam then passes upwardly through the sinuous passage between the baflie 23 and the drum wall, and in this zone is subjected to successive washing and passes over the upper end of the baflle 23 into the portion yond. 7 i I
  • the separator sections 40, '41 nd 42 are arranged along 'thetop of the drum with their upper endssubstantially inconi-tact with the drum wall and are supported from the drum wall'by hangers '43"ca fying a common i"'b0tt0 mp1at e"44.
  • v j i w 1 As shown, the'section 40 and the corresponding portion of thebottom plate 44 have a greater inclination than the section 4
  • Openings 48 are provided in a sleeve 49 extending between the lower end of each pipe 41 and a nipple 50 welded to the drum wall for the discharge of separated water into the water space.
  • extends between the side plate 46 and bottom plate 44 adjacent the separator section 42 to separate the steam flow space from the drain connections.
  • Openings 52 are formed in the lower end of the plate 5
  • FIG. 2 The construction shown in Fig. 2 employs a modified steam washing construction having a.
  • baffle members 25, 26, and 21 are omittedand the bafiie plate 23 curved and supported from the drum wall.
  • a sloping bafiie plate 55 extends from the outer'side ofthe plate 45 to a point below the upper end of'the baffle 23
  • the washing pipes 30 extend through thebafile 55 with their upper slotted ends above the upper'endof the baflie 23 With this arrangement the wash water is discharged onto the baffle 55 from which it drops onto the bafile'20.
  • the wet steam is forced to pass successively through the descending wash water to reach the remaining portion of the steam space.
  • and 42 are preferably more closelyspaced than those in the section 40, since most of the solids in suspension in the steam will be separated in the section '40, permitting narrower steam passages to be used in-the other In the modified construction illustrated in Figs. 3 and 4, the steam washing provisions are omitted and different primary'and secondary separators employed.
  • the primary separator section is formed by an inclined corrugated'separator section 6
  • a uniform distribution of the generating tube discharge to the separator channels is effected by the location "of a'perforated diffusion plate 60 along and substantially in contact with the lower edges of the corrugated plates; Rods 62 aid in supporting the plate 60 and separator section 6
  • Fig. 3 the corrugated secondary separator sections 63, 64, 65, 66 are arranged in. a sym-. metrical twin formation along the top of'the drum with a common steam collecting chamber 61 therebetween to which the outlet pipes M are connected. Plates 68 are supported in spaced relation from the V-shaped plate 69 forming the bottom of the chamber 67 above each drain pipe 61 to avoid the exiting steam picking up separated moisture flowing to the drain connection.
  • ] are arranged along the outlet side of the sections 64 and 65 to create a flow resistancev providing a substantially uniform steam flow through the channels of the corresponding section.
  • I v In Figs. 5 and 6, some of the present improvements are incorporated in a twin type corruin the steam and water drum of a B. & W.
  • cross drumboiler having circulator tubes ll entering along the side of the drum above the normal water level and downcomer tubes 12.
  • a back flow of a substantial portion of the separated moisture is provided by extending the inclined bottom plate 13 along a major portion oi the bottom of each separator section and lowering the pressure drop and steam velocity through the sections by avoiding any flow restriction at the inlet side of the separator, sections.
  • the bottom plates 13 terminate at the outer edge" of the corrugated plates except for short extensions 14 to which hanger bolts 15 are connected.
  • the bottom plates 13 are oppositely inclined below the inner ends of the sections to form a moisture collecting space 19 to which the drain pipes 80 open.
  • corrugated separator sections de- S'lllbfifd substantially all of the corrugated plate surface is utilized for moisture separation under steam flow conditions highly suitable for moisture separation and drainage.
  • the described construction and location of the drum internal pirts facilitate their installation and provide easy access to the tubes entering the drum.
  • a steam and water drum having a water space and a steam space, a steam outlet from said steam space, a steam and water separator in said steam space comprising a multiplicity of side-by-side inclined corrugated moisture collecting plates arranged to form unobstructed narrow channels therebetween having an unobstructed inlet thereto and a subste ntially uniform flow area throughout their extent, an inclined bottom plate arranged to close the bottom of said channels for at least a major portion of their length, means forming a moisture collecting chamber opening to the remaining portion of said channels, and continuously closed drain pipes connected to said collecting chamber and having their lower ends submerged in and opening to said water space.
  • a horizontally elongated steam and water drum having a water space and a steam space, a steam outlet from said steam space, a steam and water separator in said steam space comprising a plurality of inclined separator sections, each having a multiplicity of sideby-side corrugated moisture collecting plates arranged to form unobstructed narrow channels therebetween, each of said sections having an unobstructed inlet thereto and a substantially uniform flow area throughout extent andan inclined stepped bottom plate arranged to close the bottom of said channels for at least a major portion of their length,'means forminga moisture collecting chamber openingftofthe' remaining portion of said channels, 'and continuous drain pipes connected to said collecting chamber and having theirf lowerends-submerged in and opening to said water spacei f v, I
  • a horizontally elongated steam and water drum havingfa water space and a steam space, a, steam outlet from said steam space, a steam'andwate'r separator'in' said, steam space comprising a' plurality of oppositely inclined separator.sections',", each having aflmultiplicity of side-by-side,corrugated moist'ureqcollecting plates arrangedtto form unobstructed narrow channels therebetWeem'each of said sections having an unobstructed "inlet thereto and a substantiallyuniform flow area throughout its extent andgan inclined bottoint platearranged to 'close the bottom of said channels for atfleast a major portion of their length, means forming a moisture collecting chamber opening to the-remaining portion of said channels, and continuously closed drain pipes connected to said collecting chamber and having their lower ends submerged in and opening to said waterspace.
  • a steam' and water; drum having a water space and a steam space, a steam outlet from'said steam space, a steam and" water separator comprising a plurality of inclined separator sections arranged for a steam flow serially therethrough, each having a multiplicityof sideby-side corrugated moisture collecting fplates arranged to form narrow channels therebetween, said sections having aninclined steppcdbottom plate arranged to close thebottom of said channels, and a downwardly curved lip at thelower end oi said bottom plate extending into the path of steam flow to the inlet end of said channels.
  • a horizontally elongated steam and water drum having a Water space and a steam space,'a steam ou let from said steam space, steam generating tubes opening into said water space along the length of said drum, a submerged impingement baflle extending upwardly over the discharge ends of said-generating tubes, a baffle forming a continuation in the steam space of said impingement baflle and defining a steam flow space along one side of said drum, and means for passing the steam ascending through said steam flow space in successive washing contacts with a washing liquid.
  • a horizontally elongated steam and water drum having a water space and a steam space, a steam outlet from said steam space, steam generating tubes arranged to discharge upwardly into said water space along the length of said drum, a submerged impingement baflle extending upwardly over the discharge ends of said generating tubes, a baflle forming a continuation in the steam space of said impingement bafile and defining a steam flow space along one side of said drum, means for passing the steam while ascending through said steam flow space in successive washing contacts with a descending washing liquid, and means for separating moisture from the washed steam.
  • a horizontally elongated steam and water drum having a water space and a steam space, a steam outlet from said steam space, steam generating tubes arranged to discharge upwardly into said water space along the length of said drum, a submerged impingement I baffle extending upwardly over the discharge ends of said generating tubes, a baille forming -a. continuation'in the steam space 01 said impingement batlie and defining a steam flow space along one side of said drum, means for passing the steam after ascending through said steam flow space in successive washing contacts with a" water space, and a. group ofside-by-side corrugated plates in said water space arranged to form narrow sinuous channels therebetween extending across the discharge ends of said generating tubes.
  • a steam and water drum having a water space and a steam space, a steam outlet from said steamspace, steam generating tubes arranged to discharge upwardly into said water space, a submerged group of side-by-side corrugated plates arranged to form narrow sin- 9.
  • a steam and water drum tubes arranged to discharge upwardly into said water space, a group of side-by-side' corrugated plates in said water space arranged to form narrow sinuous channels therebetween extending across the discharge ends of said generating tubes, a second group of sideby-side corrugated plates in the upper part of said steam space ar ranged to form narrow sinuous channels there-- betwben, and means for directing the steam through the channels of said second group before reaching said steam outlet.
  • a steam and water drum having a water space and a steam space, a steam outlet from said steam space, a steam and water separator in said steam? space
  • a milltiplicity of side-by-side inclined corrugated moisture collecting plates arranged to form unobstructed narrow channels therebetween having an unobstructed inlet thereto
  • an inclined bottom plate arranged to close the bottom ofv said channels for at least a major portion of their length and having a downwardly curved lip at its lower end extending into the path of steam flow to the inlet end of said channels
  • continuously clcsed drain pipes connected to said collecting chamber and having their lower ends submerged in and opening to said water space.

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  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Separating Particles In Gases By Inertia (AREA)

Description

Sept. 16, 1941. J, c, HOBBS 2,256,115 I SEPARATOR Filed Dec. 4, 1937 4 Sheets'Sheet 1 NVENTOR.
James C blys 'WRQEY.
SepLlG, 1941. .1, HOBBS 2,25 ,115
SEPARAI'IOR Filed Dec. 4, 1957 4 Sheets-Sheet 2 INVEN 1 OR.
ma? C Hobbs ATTORNEY.
Sept. 16, 1941.
J. c. Hsss 2,256,115
SEPARATOR Filed Dec. 4, 19-37 ,Fig 3' 4 Sheets-Sheet 3 INVENTOR.
I James C Hobbs ATTORNEY.
Sept. 16, 1941. J. c. HOBBS SEPARATOR I Filed Dec. 4, 1937 4 Sheets-Sheet 4 e Z f ssssssssisssssssssssfissssssssss? INVENTOR. James C Hobbs Patented Sept. 16, 1941 UNITED STATES PATENT OFFICE SEPARATOR James C. llobbs, Painesville, Ohio Application December 4, 1937, Serial No. 178,164 12 Claims. (Cl. 122-491) The present invention relates in general to the construction and operation of gas washing and separating apparatus and more particularly to apparatus of this type which is adapted tobe incorporated in the steam and water drum of a specific object is the provision of moisture separating apparatus of the above type which is further characterized by a uniform distribution of the separating load throughout the separator surface, its ease of installation,accessibility of the associated tube connections, low pressure drop and velocity flow through the separating parts, compactness, and simplicity of construction. Another specific object is the provision of gas washing apparatus of the type described which is further characterized by the passage of the vapor being treated in successive effective washing contacts with the washing liquid and by its effective arrangement relative to the associated separating apparatus.
The various features of novelty which characterize my invention are pointed out with particularity in the claims annexed to and forming a part of this specification. For a better understanding of the invention, its operating advantages and specific objects attained by its use, reference should be had to the accompanying drawings and descriptive matter in which I have illusrrated and described various embodiments of my invention.
Of the drawings:
Fig. 1 is a somewhat diagrammatic sectional elevation of a high pressure steam and water drum having steam washing and separating pro-' visions constructed and arranged according to my invention;
Fig. 2 is a view similar to Fig. 1 illustrating I a modified construction;
Fig. 3 is a view similar to Figs. 1 and 2 illustrating a second modification;
Fig. 4 is a transverse section taken on the line 4-4 of Fig. 3;
Fig.5 is a view similar to Figs. 1, 2 and 3, illustrating a third modification; and
Fig. 6 is a transversev section taken on the line 6-6 of Fig. 5.
In Fig. 1 I have illustrated a relatively small diameter thick walled drum II) as constructed for the steam and water drum of a high capacity high pressure steam generating unit, the normal water level in the drum being indicated by the broken line I I. The drum receives the discharge from a multiplicity of steam generating tubes I2 opening through the .drum wall alongv the length of and below the normal water level in the drum. Submerged downcomer tubes l3 are also radially connected to the bottom of the drum at one side of the tubes I2. Steam outlet tubes I4 open to the upper part of the steam space of the drum.
The drum includes provisions for successively efiecting a primary separation of the steam and water, washing of the steam, and a secondary separation of the moisture from the washed steam. The primary separating provisions include a transversely curved ballle 20 extending from the bottom of the drum between the riser tubes l2 and downcomers l3 to a point above the normal water level. The batlle 20 is divided into sections longitudinally of the drum, each section having its lower end hinged to the drum wall, as indicated at 2|, and its upper end clamped to a horizontal extension 22 of a longitudinally extending vertical bafile plate or partition 23, as indicated at 24. The baflle plate 23 is suitably supported in the position shown and provided with upper and lower laterally extending plates 25 and 26 sloping towards the adjacent portion of the drum Wall. An inwardly sloping plate 21' extends from the drum wall towards and intermediate the plates 25 and 26 and provides. a sinuous flow path for the ascending wet steam between the baflle plate 23 and the drum wall. The space enclosed by the baflles 20 and 23 extends the full length of the portion of the drum to which the tubes [2 and I3 are connected and may be wholly or partly closed at its ends. A submerged portion of each curved baflle section 20 is of double walled construction to form a passage 28 therein opening to the remaining portion of the drum water space.
The described arrangement and construction of the plates 23, 25, 26, and 21 is advantageous for washing the ascending wet steam. For this purpose pipes 30 are connected to some or all of the discharge ends of a group of economizer tubes 3| entering the drum adjacent the downcomer tubes l3. Each pipe 30 extends upwardly into the steam space of the drum to a slotted sections. V I r The separator section 42 is locatedadjacent" the ends of the steam outletpipes l4. All of I 4 from the separator sections.
discharge end 32 above the plate 25 and directs a sheet of feed water onto the plate 25 from which it cascades onto the plates 21 and 26 before reaching the body of water in the drum.
With the described baffle arrangement, the
mixture of steam and water discharged by the.
tubes I2 passes across the water space of the drum and impinges against the bafiie plate whereby the fluid jets are broken up, facilitating .the separation, of the-steam-bubblespand the discharge distributed' over, the water surface area in' the chamber. The steam then passes upwardly through the sinuous passage between the baflie 23 and the drum wall, and in this zone is subjected to successive washing and passes over the upper end of the baflle 23 into the portion yond. 7 i I In this section of the steam space the steam of the steam' space therebe- '15 actions by the cascading sheet of wash water:-
issubjectedfto .a .secondary separating action. The secondary separation is formed by a plurality being swept along the corrugated surfaces beyond' a single section. "The separator sections 40, '41 nd 42 are arranged along 'thetop of the drum with their upper endssubstantially inconi-tact with the drum wall and are supported from the drum wall'by hangers '43"ca fying a common i"'b0tt0 mp1at e"44. v j i w 1 As shown, the'section 40 and the corresponding portion of thebottom plate 44 have a greater inclination than the section 4|, while the section 42' is'slightly inclined oppositely. to the the steam'outlet-pipe connections and extend V downwardly adjacent the baflie 20 towards the bottom of the drum. Openings 48 are provided in a sleeve 49 extending between the lower end of each pipe 41 and a nipple 50 welded to the drum wall for the discharge of separated water into the water space. A sloping plate 5| extends between the side plate 46 and bottom plate 44 adjacent the separator section 42 to separate the steam flow space from the drain connections. Openings 52 are formed in the lower end of the plate 5| for the passage of moisture separated in the section 42 and in the space above the plate 5| to the drain pipes 41.
The construction shown in Fig. 2 employs a modified steam washing construction having a.
parallel flow of the steam and the wash water in contrast to the contra-flow arrangement of In the Fig. 2 construction, the baffle members 25, 26, and 21 are omittedand the bafiie plate 23 curved and supported from the drum wall. A sloping bafiie plate 55 extends from the outer'side ofthe plate 45 to a point below the upper end of'the baffle 23 The washing pipes 30 extend through thebafile 55 with their upper slotted ends above the upper'endof the baflie 23 With this arrangement the wash water is discharged onto the baffle 55 from which it drops onto the bafile'20. The wet steam is forced to pass successively through the descending wash water to reach the remaining portion of the steam space. V
section 4|. The flow'a'rea through the separator sections'is relatively large to permit a low steam velocity therethrough and a. pressure drop low enoughto allow the. separated moisture toflow downwardly alongthe bottom plate 44 against the steam flow. At. its steam inlet end the bottom plate 44 has a downwardly curved lip 44* which causes the steam flowing past the underside of the plate to exert a wiping entrainment or ejector effect on the moisture flowing over the lip, particularly at high'water levels in the drum. The corrugated plates in the separator sections 4| and 42 are preferably more closelyspaced than those in the section 40, since most of the solids in suspension in the steam will be separated in the section '40, permitting narrower steam passages to be used in-the other In the modified construction illustrated in Figs. 3 and 4, the steam washing provisions are omitted and different primary'and secondary separators employed. The primary separator section is formed by an inclined corrugated'separator section 6| extending between spaced'portions of the drum wall and over the discharge end of the tubes 2. At its upper end the section has aprogressively increasing amount of corrugated surface, as shown in Fig. 3, while its lower portion is normally submerged. A uniform distribution of the generating tube discharge to the separator channels is effected by the location "of a'perforated diffusion plate 60 along and substantially in contact with the lower edges of the corrugated plates; Rods 62 aid in supporting the plate 60 and separator section 6|. With this construction all of the steam discharged by the tubes I2 is caused to pass through the narrow sinuous passages between the plates of the separator 'sec- I in the steam space decreases the circulation head required.
In Fig. 3 the corrugated secondary separator sections 63, 64, 65, 66 are arranged in. a sym-. metrical twin formation along the top of'the drum with a common steam collecting chamber 61 therebetween to which the outlet pipes M are connected. Plates 68 are supported in spaced relation from the V-shaped plate 69 forming the bottom of the chamber 67 above each drain pipe 61 to avoid the exiting steam picking up separated moisture flowing to the drain connection.
Perforated plates 6|] are arranged along the outlet side of the sections 64 and 65 to create a flow resistancev providing a substantially uniform steam flow through the channels of the corresponding section. I v In Figs. 5 and 6, some of the present improvements are incorporated in a twin type corruin the steam and water drum of a B. & W.
cross drumboiler having circulator tubes ll entering along the side of the drum above the normal water level and downcomer tubes 12. A back flow of a substantial portion of the separated moisture is provided by extending the inclined bottom plate 13 along a major portion oi the bottom of each separator section and lowering the pressure drop and steam velocity through the sections by avoiding any flow restriction at the inlet side of the separator, sections. For this purpose the bottom plates 13 terminate at the outer edge" of the corrugated plates except for short extensions 14 to which hanger bolts 15 are connected. A V-shaped perforated plate structureJGsurrounds the common steam collecting space 11 to which steam outlet pipes 18 open. The bottom plates 13 are oppositely inclined below the inner ends of the sections to form a moisture collecting space 19 to which the drain pipes 80 open.
With this arrangement the separated moisture reaching the bottom of a major portion of the corrugations will flow back along the bottom plates 13 and over the inlet edge of the plates 13, while the remaining portion of the separated moisture iiows into the chamber 19 to the drain pipes 80.
In all of the corrugated separator sections de- S'lllbfifd, substantially all of the corrugated plate surface is utilized for moisture separation under steam flow conditions highly suitable for moisture separation and drainage. The described construction and location of the drum internal pirts facilitate their installation and provide easy access to the tubes entering the drum.
While in accordance with the provisions of the statutes I have illustrated and described herein the best forms of the invention now known to me, those skilled in the art will understand that changes may be made in the form of the apparatus disclosed without departing from the spirit of the invention covered by my claims, and that certain features of my invention may sometimes be used to advantage without a corresponding use of other features.
I claim:
1. In combination, a steam and water drum having a water space and a steam space, a steam outlet from said steam space, a steam and water separator in said steam space comprising a multiplicity of side-by-side inclined corrugated moisture collecting plates arranged to form unobstructed narrow channels therebetween having an unobstructed inlet thereto and a subste ntially uniform flow area throughout their extent, an inclined bottom plate arranged to close the bottom of said channels for at least a major portion of their length, means forming a moisture collecting chamber opening to the remaining portion of said channels, and continuously closed drain pipes connected to said collecting chamber and having their lower ends submerged in and opening to said water space.
2. In combination, a horizontally elongated steam and water drum having a water space and a steam space, a steam outlet from said steam space, a steam and water separator in said steam space comprising a plurality of inclined separator sections, each having a multiplicity of sideby-side corrugated moisture collecting plates arranged to form unobstructed narrow channels therebetween, each of said sections having an unobstructed inlet thereto and a substantially uniform flow area throughout extent andan inclined stepped bottom plate arranged to close the bottom of said channels for at least a major portion of their length,'means forminga moisture collecting chamber openingftofthe' remaining portion of said channels, 'and continuous drain pipes connected to said collecting chamber and having theirf lowerends-submerged in and opening to said water spacei f v, I
3. In combination, a horizontally elongated steam and water drum havingfa water space and a steam space, a, steam outlet from said steam space, a steam'andwate'r separator'in' said, steam space comprising a' plurality of oppositely inclined separator.sections',", each having aflmultiplicity of side-by-side,corrugated moist'ureqcollecting plates arrangedtto form unobstructed narrow channels therebetWeem'each of said sections having an unobstructed "inlet thereto and a substantiallyuniform flow area throughout its extent andgan inclined bottoint platearranged to 'close the bottom of said channels for atfleast a major portion of their length, means forming a moisture collecting chamber opening to the-remaining portion of said channels, and continuously closed drain pipes connected to said collecting chamber and having their lower ends submerged in and opening to said waterspace.
4. In combination, a steam' and water; drum having a water space and a steam space, a steam outlet from'said steam space, a steam and" water separator comprising a plurality of inclined separator sections arranged for a steam flow serially therethrough, each having a multiplicityof sideby-side corrugated moisture collecting fplates arranged to form narrow channels therebetween, said sections having aninclined steppcdbottom plate arranged to close thebottom of said channels, and a downwardly curved lip at thelower end oi said bottom plate extending into the path of steam flow to the inlet end of said channels.
5. In combination, a horizontally elongated steam and water drum having a Water space and a steam space,'a steam ou let from said steam space, steam generating tubes opening into said water space along the length of said drum, a submerged impingement baflle extending upwardly over the discharge ends of said-generating tubes, a baffle forming a continuation in the steam space of said impingement baflle and defining a steam flow space along one side of said drum, and means for passing the steam ascending through said steam flow space in successive washing contacts with a washing liquid.
6. In combination, a horizontally elongated steam and water drum having a water space and a steam space, a steam outlet from said steam space, steam generating tubes arranged to discharge upwardly into said water space along the length of said drum, a submerged impingement baflle extending upwardly over the discharge ends of said generating tubes, a baflle forming a continuation in the steam space of said impingement bafile and defining a steam flow space along one side of said drum, means for passing the steam while ascending through said steam flow space in successive washing contacts with a descending washing liquid, and means for separating moisture from the washed steam.
7. In combination, a horizontally elongated steam and water drum having a water space and a steam space, a steam outlet from said steam space, steam generating tubes arranged to discharge upwardly into said water space along the length of said drum, a submerged impingement I baffle extending upwardly over the discharge ends of said generating tubes, a baille forming -a. continuation'in the steam space 01 said impingement batlie and defining a steam flow space along one side of said drum, means for passing the steam after ascending through said steam flow space in successive washing contacts with a" water space, and a. group ofside-by-side corrugated plates in said water space arranged to form narrow sinuous channels therebetween extending across the discharge ends of said generating tubes.
between extending across the discharge ends of said generating tubes, and a submerged perforated diifusion plate arranged across the lower edge of said plates and tending to uniformly distribute -the discharge from said generating I tubes to said channels.
7 11. In combination, a steam and water drum having a water space and a steam space, a steam outlet from said steamspace, steam generating tubes arranged to discharge upwardly into said water space, a submerged group of side-by-side corrugated plates arranged to form narrow sin- 9.In combination, a steam and water drum tubes arranged to discharge upwardly into said water space, a group of side-by-side' corrugated plates in said water space arranged to form narrow sinuous channels therebetween extending across the discharge ends of said generating tubes, a second group of sideby-side corrugated plates in the upper part of said steam space ar ranged to form narrow sinuous channels there-- betwben, and means for directing the steam through the channels of said second group before reaching said steam outlet.
" 1 0. In combinatiomasteam and water dr having a water space and a steam space, a steam outlet from said steam space, steam generating tubes arranged to discharge upwardly into said water space," a submerged group of side-by-side plates arranged to form narrow channels thereuous channels therebetween extending across the discharge ends of said generating tubes, and a submerged perforated diifusion plate arranged across the lower edge of said corrugated plates and tending to uniformly distribute the discharge from said generating tubes to said sinuous channels.
12. In combination, a steam and water drum having a water space and a steam space, a steam outlet from said steam space, a steam and water separator in said steam? space comprising a milltiplicity of side-by-side inclined corrugated moisture collecting plates arranged to form unobstructed narrow channels therebetween having an unobstructed inlet thereto, an inclined bottom plate arranged to close the bottom ofv said channels for at least a major portion of their length and having a downwardly curved lip at its lower end extending into the path of steam flow to the inlet end of said channels, means forming a moisture collecting chamber opening to the remaining portion of said channels, and continuously clcsed drain pipes connected to said collecting chamber and having their lower ends submerged in and opening to said water space.
JAMES C. HOBBS.
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Cited By (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2424212A (en) * 1944-07-29 1947-07-22 Riley Stoker Corp Steam purifying apparatus
US2463382A (en) * 1944-01-08 1949-03-01 James C Hobbs Liquid and gas separating apparatus
US2655905A (en) * 1950-08-26 1953-10-20 Springfield Boiler Company Steam purifier
US2700376A (en) * 1941-01-24 1955-01-25 Foster Wheeler Corp Apparatus for purifying steam
US2921647A (en) * 1958-06-02 1960-01-19 Gen Electric Moisture separator
US2946401A (en) * 1958-10-13 1960-07-26 Serner Herbert Edward Entrainment separator
US3043280A (en) * 1959-09-29 1962-07-10 Riley Stoker Corp Feedwater system
US3256865A (en) * 1964-01-24 1966-06-21 Babcock & Wilcox Co Liquid-vapor separator
US3370574A (en) * 1966-11-04 1968-02-27 Superior Comb Ind Inc Steam generating apparatus
US3656281A (en) * 1968-06-27 1972-04-18 Bbc Brown Boveri & Cie Water separator-superheater
US3702527A (en) * 1967-06-19 1972-11-14 Colonial Sugar Refining Particle separator

Cited By (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2700376A (en) * 1941-01-24 1955-01-25 Foster Wheeler Corp Apparatus for purifying steam
US2463382A (en) * 1944-01-08 1949-03-01 James C Hobbs Liquid and gas separating apparatus
US2424212A (en) * 1944-07-29 1947-07-22 Riley Stoker Corp Steam purifying apparatus
US2655905A (en) * 1950-08-26 1953-10-20 Springfield Boiler Company Steam purifier
US2921647A (en) * 1958-06-02 1960-01-19 Gen Electric Moisture separator
US2946401A (en) * 1958-10-13 1960-07-26 Serner Herbert Edward Entrainment separator
US3043280A (en) * 1959-09-29 1962-07-10 Riley Stoker Corp Feedwater system
US3256865A (en) * 1964-01-24 1966-06-21 Babcock & Wilcox Co Liquid-vapor separator
US3370574A (en) * 1966-11-04 1968-02-27 Superior Comb Ind Inc Steam generating apparatus
US3702527A (en) * 1967-06-19 1972-11-14 Colonial Sugar Refining Particle separator
US3656281A (en) * 1968-06-27 1972-04-18 Bbc Brown Boveri & Cie Water separator-superheater

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