US2413717A - Fluid system - Google Patents

Fluid system Download PDF

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Publication number
US2413717A
US2413717A US450546A US45054642A US2413717A US 2413717 A US2413717 A US 2413717A US 450546 A US450546 A US 450546A US 45054642 A US45054642 A US 45054642A US 2413717 A US2413717 A US 2413717A
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United States
Prior art keywords
steam
drum
water
whirl chamber
inlet
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Expired - Lifetime
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US450546A
Inventor
Howard J Kerr
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Babcock and Wilcox Co
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Babcock and Wilcox Co
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Publication date
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Priority to US450546A priority Critical patent/US2413717A/en
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Publication of US2413717A publication Critical patent/US2413717A/en
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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
    • F22B37/22Drums; Headers; Accessories therefor
    • 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
    • F22B37/32Steam-separating arrangements using centrifugal force
    • F22B37/322Steam-separating arrangements using centrifugal force specially adapted for boiler drums

Definitions

  • the invention provides apparatus including a centrifugally acting steam and water separator in which the separation of steam and water is acceleratedby the introduction of feed water tothe whirl chamber of the separator in a substan.-' tially tangential direction, and in such a way as to induce a higher velocity of tangential steam flow into the whirl chamber.
  • Fig. 1 is a vertical section through a steam and water drum equipped with a centrifugal steam separator and-steam washer;
  • Fig. 2 is an enlarged view of the centrifugal separator andsteam washer used in the drum shown in Fig. 1;
  • v v I Fig. 3 is an elevation of the Fig. 1 centrifugal separator and steam washer taken at right-angles to the elevation shown in Fig. 2;
  • Fig. 4 is a plan of the Fig. 3 centrifugal separator and steam washer, looking upwardly as indicated by the arrow at the bottom of Fig. 3.
  • Fig. 1 of the drawing shows the steam and water drum which is intended to be the steam ofitake drum of the steam generator. It is intended to occupy a position similar to that of the drum I2 in Fig.1 of applicant's Patent 2,289,969 which issued on July 14; 1942, upon the parent application, Serial Number 205,229, filed April 30, 1938, of which this application is a division.
  • This drum is connected by steam circulators I12 to a forwardly disposed drum, and it is connected to a submerged drum by the water tubes I14.
  • Feedwater is supplied to the drum I through the tubular member I18 which is connected with a plurality of upwardly extending tubes I80 having nozzles I82 discharging into the tangential inlets I84 of the combined steam separators and steam washers I86. These inlets are in communication with the steam space of the drum I10 so that steam and water mixtures enter the washers I86 tangentially at high velocity.
  • the separated steam is discharged axially of the washers steam oiltake tubes I98 to a superheater or a point of use. Water is discharged tangentially outwardly of the combined separators and washers I86 through the outlets I92 and into the drum I18.
  • each nozzle 184 is disposed in the upper part of the steam space of the drum I10 and that it opens downwardly toward the water space .of the drum.
  • the steam flow entering the nozzle I84 takes place, to a considerable extent, upwardly past an outlet I82.
  • the latter is formed as a nozzle with a flattened outlet end as clearly indicated in Fig. 3.
  • water of less concentration separated from the steam in the whirl chamber I86 is directed in a fiat Wide stream in intersecting relation to the flow of steam into 'a nozzle I84.
  • the position of the feed water nozzle I82 centrally of the inlet I84 (as clearly indicated in Fig.
  • each combined steam washer and whirl chamber I86 effects two stages of steam washing.
  • a steam and water drum having a water level therein, means whereby a steam and water mixture enters the drum, means forming the whirl chamber of a combined steam washer and steam and'water separator disposed in the steam space of the drum, means forming a steam oiftake leading from the drum,
  • the whirl chamber having a separated steam outlet directly connected to said ofitake, means forming a primarywhirl chamber steam and water inlet tangentially arranged with reference to the whirl chamber and receiving steam flow from the drum steam space, a feed water nozzle directly communicating with a source of relatively pure feed water and directing the feed 2.
  • a steam ofltake for said drum means whereby steam and water mixtures enter the drum, means forming the whirl chamber of a centrifugal steam and water separator disposed within the steam space of the drum, means forming a whirl chamber steam inlet open to the steam space of the drum and directing the incoming fluid substantially tangentially into the whirl chamber, means whereby relatively pure feed water is discharged l0 inlet.

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  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Cyclones (AREA)

Description

Jan. 7, 1947. J KERR 2,413,717
FLUID SYSTEM Original Filed April 30, 1938 Fig 1 FEE WATER i I86 STE/4M WATER 60f /92 IN VEN TOR:
Wrd J Kerr,
A TI'ORN E Patented Jan. 7, 1947 UNITED STATE PATENT OFFICE FLUID SYSTEM Howard J. Kerr, Westileld, N. J., assignor to The Babcock & Wilcox Company, Jersey City, N. J
a corporation of New Jersey Original application April 30, 1938, Serial No. 205,229. -Divided and this application July 11, 1942, Serial No. 450,546
2 Claims. ((1122- 459) I I88 and upwardly through the or accelerate the positive separation of steam and water after the washing of the steam.
The invention provides apparatus including a centrifugally acting steam and water separator in which the separation of steam and water is acceleratedby the introduction of feed water tothe whirl chamber of the separator in a substan.-' tially tangential direction, and in such a way as to induce a higher velocity of tangential steam flow into the whirl chamber. I
Other objects of the invention will appear as the following description proceeds.
The invention will be described with reference to the accompanyingdrawing in which a .preferred embodiment is illustrated.
- In the drawing:
Fig. 1 is a vertical section through a steam and water drum equipped with a centrifugal steam separator and-steam washer;
Fig. 2 is an enlarged view of the centrifugal separator andsteam washer used in the drum shown in Fig. 1; v v I Fig. 3 is an elevation of the Fig. 1 centrifugal separator and steam washer taken at right-angles to the elevation shown in Fig. 2;
Fig. 4 is a plan of the Fig. 3 centrifugal separator and steam washer, looking upwardly as indicated by the arrow at the bottom of Fig. 3.
Fig. 1 of the drawing shows the steam and water drum which is intended to be the steam ofitake drum of the steam generator. It is intended to occupy a position similar to that of the drum I2 in Fig.1 of applicant's Patent 2,289,969 which issued on July 14; 1942, upon the parent application, Serial Number 205,229, filed April 30, 1938, of which this application is a division.
This drum is connected by steam circulators I12 to a forwardly disposed drum, and it is connected to a submerged drum by the water tubes I14. Feedwater is supplied to the drum I through the tubular member I18 which is connected with a plurality of upwardly extending tubes I80 having nozzles I82 discharging into the tangential inlets I84 of the combined steam separators and steam washers I86. These inlets are in communication with the steam space of the drum I10 so that steam and water mixtures enter the washers I86 tangentially at high velocity. The separated steam is discharged axially of the washers steam oiltake tubes I98 to a superheater or a point of use. Water is discharged tangentially outwardly of the combined separators and washers I86 through the outlets I92 and into the drum I18.
From an inspection of Figs. 1 to 4, inclusive, it
will be noted that the inlet opening of each nozzle 184 is disposed in the upper part of the steam space of the drum I10 and that it opens downwardly toward the water space .of the drum. With this arrangement the steam flow entering the nozzle I84 takes place, to a considerable extent, upwardly past an outlet I82. The latter is formed as a nozzle with a flattened outlet end as clearly indicated in Fig. 3. Thus, water of less concentration separated from the steam in the whirl chamber I86 is directed in a fiat Wide stream in intersecting relation to the flow of steam into 'a nozzle I84. In addition to this washing effect, the position of the feed water nozzle I82 centrally of the inlet I84 (as clearly indicated in Fig. 2 of the drawing) not only causes an increase in velocity 'of the whirling fluid within the whirl chamber I86, but it also acts to cause considerable mixing of the feed water and steam in the inlet I84 before the whirl chamber is reached. Thus, in eifect, each combined steam washer and whirl chamber I86 effects two stages of steam washing.
I claim:
1. In a steam generator, a steam and water drum having a water level therein, means whereby a steam and water mixture enters the drum, means forming the whirl chamber of a combined steam washer and steam and'water separator disposed in the steam space of the drum, means forming a steam oiftake leading from the drum,
the whirl chamber having a separated steam outlet directly connected to said ofitake, means forming a primarywhirl chamber steam and water inlet tangentially arranged with reference to the whirl chamber and receiving steam flow from the drum steam space, a feed water nozzle directly communicating with a source of relatively pure feed water and directing the feed 2. In a"steam generatona steam and water drum having a water level therein, means forming a steam ofltake for said drum, means whereby steam and water mixtures enter the drum, means forming the whirl chamber of a centrifugal steam and water separator disposed within the steam space of the drum, means forming a whirl chamber steam inlet open to the steam space of the drum and directing the incoming fluid substantially tangentially into the whirl chamber, means whereby relatively pure feed water is discharged l0 inlet.
in a let within the said whirl chamber inlet and EDWARD J. KERR.
US450546A 1938-04-30 1942-07-11 Fluid system Expired - Lifetime US2413717A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
US450546A US2413717A (en) 1938-04-30 1942-07-11 Fluid system

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US205229A US2289969A (en) 1938-04-30 1938-04-30 Fluid heat exchange apparatus
US450546A US2413717A (en) 1938-04-30 1942-07-11 Fluid system

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US2413717A true US2413717A (en) 1947-01-07

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US205229A Expired - Lifetime US2289969A (en) 1938-04-30 1938-04-30 Fluid heat exchange apparatus
US450546A Expired - Lifetime US2413717A (en) 1938-04-30 1942-07-11 Fluid system

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Application Number Title Priority Date Filing Date
US205229A Expired - Lifetime US2289969A (en) 1938-04-30 1938-04-30 Fluid heat exchange apparatus

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US (2) US2289969A (en)
FR (1) FR853654A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2669976A (en) * 1949-04-29 1954-02-23 Foster Wheeler Corp Apparatus for generating vapor
US2669975A (en) * 1949-04-29 1954-02-23 Foster Wheeler Corp Vapor generator
US3446189A (en) * 1967-02-20 1969-05-27 Chemokomplex La Gep Es Berende Apparatus for flash-evaporating liquids
WO1994017330A1 (en) * 1993-01-19 1994-08-04 Keystone International Holdings Corp. Improved steam desuperheater

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2592530A (en) * 1945-05-24 1952-04-15 Foster Wheeler Corp Steam separator
US2825316A (en) * 1952-01-29 1958-03-04 Babcock & Wilcox Co Apparatus for purifying steam
US2739663A (en) * 1952-08-12 1956-03-27 Gurney William Brewster High pressure steam purifier

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2669976A (en) * 1949-04-29 1954-02-23 Foster Wheeler Corp Apparatus for generating vapor
US2669975A (en) * 1949-04-29 1954-02-23 Foster Wheeler Corp Vapor generator
US3446189A (en) * 1967-02-20 1969-05-27 Chemokomplex La Gep Es Berende Apparatus for flash-evaporating liquids
WO1994017330A1 (en) * 1993-01-19 1994-08-04 Keystone International Holdings Corp. Improved steam desuperheater
US5385121A (en) * 1993-01-19 1995-01-31 Keystone International Holdings Corp. Steam desuperheater

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Publication number Publication date
FR853654A (en) 1940-03-26
US2289969A (en) 1942-07-14

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