US2624401A - Falling film evaporator with subjacent separating chamber - Google Patents

Falling film evaporator with subjacent separating chamber Download PDF

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US2624401A
US2624401A US76718A US7671849A US2624401A US 2624401 A US2624401 A US 2624401A US 76718 A US76718 A US 76718A US 7671849 A US7671849 A US 7671849A US 2624401 A US2624401 A US 2624401A
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vapor
liquor
chamber
subjacent
separating chamber
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US76718A
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Earl A Schilt
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ZAREMBA CO
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ZAREMBA CO
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D1/00Evaporating
    • B01D1/06Evaporators with vertical tubes
    • B01D1/12Evaporators with vertical tubes and forced circulation

Definitions

  • This invention relates to certain new and useful improvements in evaporators, but more Dal.'- ticularly to the falling film type. of evaporator which is used for concentrating all types of liquors and more especially those liquors in which the presence of scale-forming materials constitute a major problem.
  • One of the objects of the invention is to provide an evaporator of this character which isy so designed and constructed that the steamchest thereof is set directly above and supported by the vapor body in Vertical alinement therewith, thereby forming a complete self-supporting unit for bolting to a supporting pad and in which no additional structural steel supports are required.
  • Another object is to provide a falling lm type evaporator having simple and effective babyte means for initiating the separation of the liquor and vapor components in a manner to cause the liquor-vapor mixture to be directed and collected at one side of the vapor body, where the liquor will flow by gravity to the ⁇ receiving chamber thereof and the Vapor will be caused to be directed to a separator at the opposite side of the vapor body without encountering any further streams of liquor.
  • Figure 1 is a central longitudinal section, in part fragmentary, of the evaporator embodying my invention.
  • Figure 2 is a horizontal section taken in substantially the plane of line 2 2, Figure 1.
  • a vapor body or tank I consists generally of a vapor body or tank I and a comparatively long steamchest or chamber Il disposed directly above and supported by and axially of the vapor body, these parts being made in sections and then Welded or otherwise connected to form a unitary structure.
  • the latter is cylindrical in shape and has a dished bottom I2 with the cylindrical wall of such body having a depending supporting extension I3 provided at its lower end with a suitable attaching base I4 for bolting to a pedestal and thereby form a complete self-supporting unit.
  • the steamchest or chamber II has a plurality of vertical tubes I5 therein in which the liquor is boiled and these tubes are supported in top and bottom tube sheets I6 and I1, respectively.
  • a liquor box I8 having a detachable cover I9 and in the lower portion of which, in Spaced relation to such tube sheet, is a removable distributing plate ZIIthrough which the liquor is adapted to flow by gravityy onto the top tube sheet in such a fashionthat a thin nlm of liquor will flow yfrom this tube sheet into all parts of all the tubes.
  • Steam is admitted to the chest through an inlet 2lv and at its lower end a condensate drain 22 is ⁇ provided.
  • the dished bottom of the vapor body I0 is in liquor circulating communication with the liquor box i3 through the medium of piping 23 in which ay circulating pump 24 is interposed.
  • a liquor inlet 25 Connected to the discharge side of thisl piping is a liquor inlet 25 including a control valve 26. and 21 indicates a valve-controlled liquor outlet disposed in the discharge side of the piping below the liquor inlet.
  • the lower portion of the vapor body I0 constitutes a receiving chamber 28 for the liquor and vapor delivered thereto ⁇ from the tubes I5 While the upper portion thereof is shaped to provide a centrifugal separator including an outer annular chamber 29 formed by a yconcentric wall 30 spaced from the outer wallr of the Vapor body.
  • This concentric wall with the lower tube sheet I'I denes a vapor-receiving hood 3
  • the separator wall 30 has a vertical inlet or opening 34 therein through which the Vapor passes to the annular chamber 29 from the chamber 28 and the vapor body has a vapor outlet 35 therein adapted for connection to a condenser or succeeding effect evaporator.
  • An extension 36 on the concentric wall 30 bridged substantially radially across the annular chamber 29 separates the hood-outlet 34 from the bodyoutlet 35, whereby the vapor after entering the annular chamber travels in a circular course before being discharged from the vapor body and any remaining liquor droplets entrained therein are discharged through the drain pipe 33.
  • I provide effective bailling means which preferably consists of a baffle wall 31 disposed at an angle or substantially diagonally across the vapor-receiving hood 3l from the upper end thereof to the lower end thereof, its lower end being spaced from the adjoining portion of the concentric wall 30 to bottom tube sheet and facilitate repair or replacement of the tubes I'5.
  • a liquid level control device 4l is provided for ⁇ regulating the liquor level in the chamber 28, as indicated, by controlling the flow of incoming liquor.
  • the pump 24 delivers liquor from distributing plate in the liquor box I8.
  • This plate allows the liquor to flow by gravity onto thetop tube sheet I6 of the steamchest, distributing it in a fashion so that a thin nlm of liquor will flow from this tube sheet into all parts of'all the tubes.
  • This thin iilrn of liquor will now downward on the walls of the tubes and its iiow will be further accelerated by the vapor velocity generated when the thinl lm of liquor is boiled by thev heat from the steam side of the tubes.
  • vThe liquor issuing from the tubes I5 at a highvvelocity is mixed with the vapor asa iine mist oras a plurality of small droplets and the inclined baillew3l functions to effectively initiate the separation ofthe components by collecting the vapor-liquor mixture and directing it to one side of the vapor body where the liquor mist will agglomerate into larger and heavier particles oi sufcient weight to drop by gravity out of the vapor stream into the pool at the bottom of the chamber 28.
  • the vapor on breaking away from the liquor at this one side of the vapor body, can then pass across toward the opposite side thereof, without encountering any further streams of liquor, and thence pass upwardly where it is directed by the underside of the inclined baille toward the inlet 34 of the separator.
  • vapor body adapted for communication at its upper portion with va chamber for a mixture of liquor and vapor and with its lower portion constitutinga li ucr-receivin chamber, a centrifuthe pool in the bottom of the vapor body to the q g gal separating chamber disposed circumferentially about the upper portion of said vapor body and having a vertical vapor inlet for the passage of vapor thereto ⁇ and a vapor outlet, an inclined baille wall disposed across the upper portion of the vapor body in overhanging relation to and with its underside facing said vapor inlet and with its lower end terminating substanti-allyat the lower elevation of the vapor inlet and laterally short of the adjoining side of said vapor body to provide a discharge for the liquor and vapor, and a lip-like baiiie provided at the op posite side oi the vapor body adjacent the lower end of the separating chamber to prevent the liquor being splashed into the same through said vapor inlet.

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)

Description

E. A. scH'lL-r Jan. 6, 1953 FALLING EVAPORATOR WITH SUBJACENT SEPARATING CHAMBER Filed Feb. 16. 1949 Zhwentor Patented Jan. 6, 1953 FALLING FILM EVAPORATOR WITH SUBJACENT SEPARATING CHAMBER Earl A Schilt uialo, N Ys assigner to Zaremba Company., Yorkv Buffalo, N. Y., a corporation of New Applioation February 16, 1949, Serial No, 76,718
(Cl. 15S-.13)
1 Claim. 1
This invention relates to certain new and useful improvements in evaporators, but more Dal.'- ticularly to the falling film type. of evaporator which is used for concentrating all types of liquors and more especially those liquors in which the presence of scale-forming materials constitute a major problem.
One of the objects of the invention is to provide an evaporator of this character which isy so designed and constructed that the steamchest thereof is set directly above and supported by the vapor body in Vertical alinement therewith, thereby forming a complete self-supporting unit for bolting to a supporting pad and in which no additional structural steel supports are required.
Another object is to provide a falling lm type evaporator having simple and effective baiile means for initiating the separation of the liquor and vapor components in a manner to cause the liquor-vapor mixture to be directed and collected at one side of the vapor body, where the liquor will flow by gravity to the` receiving chamber thereof and the Vapor will be caused to be directed to a separator at the opposite side of the vapor body without encountering any further streams of liquor.
In the accompanying drawings:
Figure 1 is a central longitudinal section, in part fragmentary, of the evaporator embodying my invention. Figure 2 is a horizontal section taken in substantially the plane of line 2 2, Figure 1.
Similar characters of reference indicate corresponding parts throughout the several views.
In the preferred embodiment of the invention shown in the drawing, it consists generally of a vapor body or tank I and a comparatively long steamchest or chamber Il disposed directly above and supported by and axially of the vapor body, these parts being made in sections and then Welded or otherwise connected to form a unitary structure. The latter is cylindrical in shape and has a dished bottom I2 with the cylindrical wall of such body having a depending supporting extension I3 provided at its lower end with a suitable attaching base I4 for bolting to a pedestal and thereby form a complete self-supporting unit.
The steamchest or chamber II has a plurality of vertical tubes I5 therein in which the liquor is boiled and these tubes are supported in top and bottom tube sheets I6 and I1, respectively. Above the top tube sheet is a liquor box I8 having a detachable cover I9 and in the lower portion of which, in Spaced relation to such tube sheet, is a removable distributing plate ZIIthrough which the liquor is adapted to flow by gravityy onto the top tube sheet in such a fashionthat a thin nlm of liquor will flow yfrom this tube sheet into all parts of all the tubes. Steam is admitted to the chest through an inlet 2lv and at its lower end a condensate drain 22 is` provided. IThe dished bottom of the vapor body I0 is in liquor circulating communication with the liquor box i3 through the medium of piping 23 in which ay circulating pump 24 is interposed. Connected to the discharge side of thisl piping is a liquor inlet 25 including a control valve 26. and 21 indicates a valve-controlled liquor outlet disposed in the discharge side of the piping below the liquor inlet.
The lower portion of the vapor body I0 constitutes a receiving chamber 28 for the liquor and vapor delivered thereto` from the tubes I5 While the upper portion thereof is shaped to provide a centrifugal separator including an outer annular chamber 29 formed by a yconcentric wall 30 spaced from the outer wallr of the Vapor body. This concentric wall with the lower tube sheet I'I denes a vapor-receiving hood 3| in direct open communication with the receiving chamber 23, and the ,lower end of the annular chamber 29 is closed by a horizontal wall 32 and has a drain pipe 33 depending therefrom tov a point short of the dished bottom of such receiving chamber. The separator wall 30 has a vertical inlet or opening 34 therein through which the Vapor passes to the annular chamber 29 from the chamber 28 and the vapor body has a vapor outlet 35 therein adapted for connection to a condenser or succeeding effect evaporator. An extension 36 on the concentric wall 30 bridged substantially radially across the annular chamber 29 separates the hood-outlet 34 from the bodyoutlet 35, whereby the vapor after entering the annular chamber travels in a circular course before being discharged from the vapor body and any remaining liquor droplets entrained therein are discharged through the drain pipe 33.
.For the purpose of obtaining adequate primary separation of the liquor and the vapor issuing from the tube section of the steamchest into the upper portion of the vapor body, I provide effective bailling means which preferably consists of a baffle wall 31 disposed at an angle or substantially diagonally across the vapor-receiving hood 3l from the upper end thereof to the lower end thereof, its lower end being spaced from the adjoining portion of the concentric wall 30 to bottom tube sheet and facilitate repair or replacement of the tubes I'5.
A liquid level control device 4l is provided for` regulating the liquor level in the chamber 28, as indicated, by controlling the flow of incoming liquor. Y
In operation, the pump 24 delivers liquor from distributing plate in the liquor box I8. This plate allows the liquor to flow by gravity onto thetop tube sheet I6 of the steamchest, distributing it in a fashion so that a thin nlm of liquor will flow from this tube sheet into all parts of'all the tubes. This thin iilrn of liquor will now downward on the walls of the tubes and its iiow will be further accelerated by the vapor velocity generated when the thinl lm of liquor is boiled by thev heat from the steam side of the tubes. As the high velocity mixture of liquor and v-apor leaves the lower ends of the tubes and enters the upper end of the vapor body IB, it strikes the sloping face of the baiiie 31 which guides and directs it to one side of such body for passage through the opening 38 into the upper end of the receiving chamber 28. The liquor strikes the adjoining side wall of this chamber and runs down the samev to collect in the pool in the'bottom, while. the Vapor, being lighter, and following the path of least resistance reverses its directionrand passes upwardly around the bottom of the inclined baille into the open vapor hood 3l, from whichY it passes into the annular chamber 29 of the centrifugal separator where any remaining liquor droplets are thrown out and removed through the drain pipe 33. Y
vThe liquor issuing from the tubes I5 at a highvvelocity is mixed with the vapor asa iine mist oras a plurality of small droplets and the inclined baillew3l functions to effectively initiate the separation ofthe components by collecting the vapor-liquor mixture and directing it to one side of the vapor body where the liquor mist will agglomerate into larger and heavier particles oi sufcient weight to drop by gravity out of the vapor stream into the pool at the bottom of the chamber 28. The vapor, on breaking away from the liquor at this one side of the vapor body, can then pass across toward the opposite side thereof, without encountering any further streams of liquor, and thence pass upwardly where it is directed by the underside of the inclined baille toward the inlet 34 of the separator.
I claim as my invention:
In anl evaporator of the character described, a
vapor body adapted for communication at its upper portion with va chamber for a mixture of liquor and vapor and with its lower portion constitutinga li ucr-receivin chamber, a centrifuthe pool in the bottom of the vapor body to the q g gal separating chamber disposed circumferentially about the upper portion of said vapor body and having a vertical vapor inlet for the passage of vapor thereto `and a vapor outlet, an inclined baille wall disposed across the upper portion of the vapor body in overhanging relation to and with its underside facing said vapor inlet and with its lower end terminating substanti-allyat the lower elevation of the vapor inlet and laterally short of the adjoining side of said vapor body to provide a discharge for the liquor and vapor, and a lip-like baiiie provided at the op posite side oi the vapor body adjacent the lower end of the separating chamber to prevent the liquor being splashed into the same through said vapor inlet. l
EARL A. SCHILT.
REFERENCES CITED The following references-are of record in the le ofv this patent:
UNITED STATES PATENTS Lindsay Jan. 1,7, o
US76718A 1949-02-16 1949-02-16 Falling film evaporator with subjacent separating chamber Expired - Lifetime US2624401A (en)

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Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2742083A (en) * 1952-07-02 1956-04-17 Roy O Henszey Falling film evaporator
US2914120A (en) * 1957-01-09 1959-11-24 Dow Chemical Co Devolatilizer
US2960160A (en) * 1956-03-21 1960-11-15 Apv Co Ltd Evaporators
US3082815A (en) * 1959-03-24 1963-03-26 Luwa Ag Feeding device for falling-film evaporators
US3107194A (en) * 1961-06-12 1963-10-15 Hans C Bechtler Centrifugal falling film evaporator
US3216480A (en) * 1963-02-18 1965-11-09 Zaremba Company Climbing and falling film evaporator with intermediate separation
US3244601A (en) * 1962-12-04 1966-04-05 Gen Electric Fluted tubular distillation apparatus
US3595297A (en) * 1967-12-20 1971-07-27 Knapsack Ag Apparatus for thickening or concentrating highly fluid solutions
US4040898A (en) * 1972-05-18 1977-08-09 Blaw-Knox Food And Chemical Equipment, Inc. Evaporating apparatus and process
FR2594043A1 (en) * 1986-02-10 1987-08-14 Graver Co PROCESS FOR TRANSFORMING A LONG VERTICAL TUBE EVAPORATOR TO A FALLING FILM EVAPORATOR AND THIS EVAPORATOR
US20070164462A1 (en) * 2003-11-06 2007-07-19 Zhaoyan Liu Grid falling film devolatilizer
CN111760307A (en) * 2020-07-16 2020-10-13 天津恒脉机电科技股份有限公司 Environment-friendly tubular falling film evaporation system

Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US466862A (en) * 1892-01-12 Tiitttp
US470060A (en) * 1892-03-01 The norbis feters co
US1005553A (en) * 1909-03-27 1911-10-10 Kestner Evaporator Company Evaporating apparatus.
US1079474A (en) * 1912-02-05 1913-11-25 Davis Oil Refining Co Process of making coffee extract.
US1246824A (en) * 1917-04-23 1917-11-13 William H C Smith Evaporator.
US1735980A (en) * 1926-07-09 1929-11-19 Swenson Evaporator Company Process of evaporation
US2150860A (en) * 1937-09-15 1939-03-14 Zaremba Company Evaporator
US2257531A (en) * 1938-08-08 1941-09-30 David D Peebles Evaporating apparatus and method
US2494767A (en) * 1945-04-02 1950-01-17 Smith Corp A O Removable vertical tube evaporator

Patent Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US466862A (en) * 1892-01-12 Tiitttp
US470060A (en) * 1892-03-01 The norbis feters co
US1005553A (en) * 1909-03-27 1911-10-10 Kestner Evaporator Company Evaporating apparatus.
US1079474A (en) * 1912-02-05 1913-11-25 Davis Oil Refining Co Process of making coffee extract.
US1246824A (en) * 1917-04-23 1917-11-13 William H C Smith Evaporator.
US1735980A (en) * 1926-07-09 1929-11-19 Swenson Evaporator Company Process of evaporation
US2150860A (en) * 1937-09-15 1939-03-14 Zaremba Company Evaporator
US2257531A (en) * 1938-08-08 1941-09-30 David D Peebles Evaporating apparatus and method
US2494767A (en) * 1945-04-02 1950-01-17 Smith Corp A O Removable vertical tube evaporator

Cited By (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2742083A (en) * 1952-07-02 1956-04-17 Roy O Henszey Falling film evaporator
US2960160A (en) * 1956-03-21 1960-11-15 Apv Co Ltd Evaporators
US2914120A (en) * 1957-01-09 1959-11-24 Dow Chemical Co Devolatilizer
US3082815A (en) * 1959-03-24 1963-03-26 Luwa Ag Feeding device for falling-film evaporators
US3107194A (en) * 1961-06-12 1963-10-15 Hans C Bechtler Centrifugal falling film evaporator
US3244601A (en) * 1962-12-04 1966-04-05 Gen Electric Fluted tubular distillation apparatus
US3216480A (en) * 1963-02-18 1965-11-09 Zaremba Company Climbing and falling film evaporator with intermediate separation
US3595297A (en) * 1967-12-20 1971-07-27 Knapsack Ag Apparatus for thickening or concentrating highly fluid solutions
US4040898A (en) * 1972-05-18 1977-08-09 Blaw-Knox Food And Chemical Equipment, Inc. Evaporating apparatus and process
FR2594043A1 (en) * 1986-02-10 1987-08-14 Graver Co PROCESS FOR TRANSFORMING A LONG VERTICAL TUBE EVAPORATOR TO A FALLING FILM EVAPORATOR AND THIS EVAPORATOR
US20070164462A1 (en) * 2003-11-06 2007-07-19 Zhaoyan Liu Grid falling film devolatilizer
US7959133B2 (en) 2003-11-06 2011-06-14 Zhaoyan Liu Grid falling film devolatilizer
CN111760307A (en) * 2020-07-16 2020-10-13 天津恒脉机电科技股份有限公司 Environment-friendly tubular falling film evaporation system

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