← Back to Patent Explorer
US3875988A Expired / Lapsed US ⏱️ 0.0 years remaining

Multiple effect evaporator apparatus

Assignee: Ebara Corp
•
Filing: 1973-02-23
•
Granted: 1975-04-08
•
Expires: 1993-02-23
📄 Original PDF 🌐 Google Patents 🔄 Sync Now

Abstract

Abstract Multiple effect evaporator apparatus includes a plurality of evaporator chambers, a plurality of thin-film flow-down type vertical heat exchange tubes the ends of which are connected to partition plates which divide the apparatus into the various evaporator chambers, a vessel disposed above the heat exchange tubes for receiving a solution, pressure difference maintaining means and solution distributing means interposed between the vessel and heat exchange tubes whereby evaporation and uniform distribution of the solution is facilitated, and means to facilitate the directional flow of the non-condensed gas through the chambers so as to prevent stagnation of the gas therein, such means being either asymmetrically located or centrally located with respect to the chambers and including passage means to interconnect the evaporator chambers.

Inventors

  • 👤 Shunichi Machida
  • 👤 Masaharu Tsujita
  • 👤 Shintaro Nakaya
  • 👤 Ryoji Ueno

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-08 20:58
CPC Classifications
B; B01; B01D; B01D1/00; B01D1/06; B01D1/065; B01D1/26

Claims Analysis

Total Claims: 9
Claim 1
Independent Claim 386 words
A multiple effect evaporator comprising: a vertically oriented cylindrical shell; a plurality of superposed chambers in said shell formed by horizontally disposed, vertically spaced tubesheets; a vertical heat exchange tube bundle provided within each of said chambers for the serial passage through said tube bundles of a solution to be evaporated, the lower ends of said tubes being fixed within said tubesheets; vessel means, disposed upon the upper ends of each of said tube bundles, provided within each of said chambers for receiving a heated solution and vapor from the lower ends of said tubes of the immediately preceding bundle of heat exchange tubes and which vessel means fluidically communicates, through a pressure difference maintaining means for maintaining a pressure difference between the pressure within said vessel means and that within the immediately succeeding vessel means and a solution distribution means disposed below said pressure difference maintaining means and above said upper ends of said tubes for defining a solution containing chamber between said distribution means and said tubes, within said vessel means, so as to uniformly distribute said solution into a succeeding bundle of heat exchange tubes, and through said succeeding bundle of heat exchange tubes, with said succeeding vessel means therebelow for conducting the resulting amount of said solution to said succeeding vessel means so as to evaporate said solution within said succeeding bundle of heat exchange tubes and to condense the major portion of said vapor from said preceding bundle of tubes about the tubes of said succeeding bundle, said vapor being used as a heat source, and including separating means for separating said vapor from said solution and for conducting said separate vapor from said preceding bundle of heat exchange tubes into said respective chamber containing said succeeding bundle; and a plurality of vapor and non-condensable gas flow passageway means for successively interconnecting the condensing portions of said chambers for causing a directional vapor flow in conjunction with said separated vapor flow from said vapor separating and conducting means about each of said bundles of heat exchange tubes within each of said condensing chambers and for conducting said flow from a preceding condensing chamber to a succeeding condensing chamber for increasing the heat exchange coefficient of said heat exchange tube bundles by preventing the stagnation of the non-condensed gas around said tubes.
Claim 2
Dependent Claim 386 words
A multiple effect evaporator comprising: a vertically oriented cylindrical shell; a plurality of superposed chambers in said shell formed by horizontally disposed, vertically spaced tubesheets; a vertical heat exchange tube bundle provided within each of said chambers for the serial passage through said tube bundles of a solution to be evaporated, the lower ends of said tubes being fixed within said tubesheets; vessel means, disposed upon the upper ends of each of said tube bundles, provided within each of said chambers for receiving a heated solution and vapor from the lower ends of said tubes of the immediately preceding bundle of heat exchange tubes and which vessel means fluidically communicates, through a pressure difference maintaining means for maintaining a pressure difference between the pressure within said vessel means and that within the immediately succeeding vessel means and a solution distribution means disposed below said pressure difference maintaining means and above said upper ends of said tubes for defining a solution containing chamber between said distribution means and said tubes, within said vessel means, so as to uniformly distribute said solution into a succeeding bundle of heat exchange tubes, and through said succeeding bundle of heat exchange tubes, with said succeeding vessel means therebelow for conducting the resulting amount of said solution to said succeeding vessel means so as to evaporate said solution within said succeeding bundle of heat exchange tubes and to condense the major portion of said vapor from said preceding bundle of tubes about the tubes of said succeeding bundle, said vapor being used as a heat source, and including separating means for separating said vapor from said solution and for conducting said separate vapor from said preceding bundle of heat exchange tubes into said respective chamber containing said succeeding bundle; and a plurality of vapor and non-condensable gas flow passageway means for successively interconnecting the condensing portions of said chambers for causing a directional vapor flow in conjunction with said separated vapor flow from said vapor separating and conducting means about each of said bundles of heat exchange tubes within each of said condensing chambers and for conducting said flow from a preceding condensing chamber to a succeeding condensing chamber for increasing the heat exchange coefficient of said heat exchange tube bundles by preventing the stagnation of the non-condensed gas around said tubes.
Claim 3
Dependent Claim 38 words
A multiple effect evaporator as set forth in claim 1, wherein said vapor flow passageway means are located at the center of each said condensing chambers so as to attain a uniform distribution of vapor throughout said chambers.
Claim 4
Dependent Claim 42 words
A multiple effect evaporator as set forth in claim 1, wherein said vapor flow passageway means are asymmetrically located within a side wall of each of said condensing chambers so as to attain a uniform distribution of vapor flow throughout said chambers.
Claim 5
Dependent Claim 25 words
A multiple effect evaporator as set forth in claim 1, wherein said passageway means include iris means for controlling the pressure difference between said chambers.
Claim 6
Dependent Claim 18 words
A multiple effect evaporator as set forth in claim 1, wherein said plurality of chambers are vertically aligned.
Claim 7
Dependent Claim 50 words
A multiple effect evaporator as set forth in claim 1, wherein said vapor and non-condensable gas flow passageway means include a plurality of fine holes permitting non-condensable gases and a minor portion of vapor to flow therethrough from one of said condensing chambers to the next of said condensing chambers.
Claim 8
Dependent Claim 27 words
A multiple effect evaporator as set forth in claim 6, wherein said fine holes of said vapor flow passageway means are used as pressure difference maintaining means.
Claim 9
Dependent Claim 33 words
A multiple effect evaporator as set forth in claim 7, wherein the diameters of the upper ones of said fine holes are smaller than that of the lower ones of said fine holes.

References Cited (Backward Citations)

US466862A Cited
US1049425A Cited
US1424992A Cited
US2114873A Cited
US2750999A Cited
US3303106A Cited
US3487873A Cited
US3578004A Cited
US3702807A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1978-04-07 1978-10-07 1979-04-08 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1982-04-07 1982-10-07 1983-04-08 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1986-04-07 1986-10-07 1987-04-08 $7700.00 Window Closed / Lapsed

Assigned Categories & Tags

No categories assigned to this patent yet.

Assign Category Tag