← Back to Patent Explorer
US3759496A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for cooling liquids by cross current contact with gases

Assignee: Research Cottrell Inc
•
Filing: 1970-12-29
•
Granted: 1973-09-18
•
Expires: 1990-12-29
📄 Original PDF 🌐 Google Patents 🔄 Sync Now

Abstract

Abstract A process for cooling water by cross-current contact with air is shown. The contact operation takes place in an inverted, frustoconical, annular enclosure packed with a packing such as Tellerettes. The water loading is preferably from 3 to 30 gallons per minute per square foot of packing area in the plane normal to the flow of water and the air loading is from 200 to 800 standard cubic feet per minute per square foot of packing area normal to the flow of air. Substantial savings in the ground area required for the cooling tower and in the height of the cooling tower are achieved through use of the process of this invention.

Inventors

  • 👤 A Teller

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-05 03:05
CPC Classifications
F; F28; F28F; F28F25/00; F28F25/02; F28F25/08; B; B01; B01J; B01J19/00; B01J19/30; F28C; F28C1/00; F28C1/04; B01J2219/00; B01J2219/30; B01J2219/302; B01J2219/30215; B01J2219/304; B01J2219/30466; Y; Y02; Y02B; Y02B30/00; Y02B30/70; Y10; Y10S; Y10S261/00; Y10S261/11; Y10S261/72

Claims Analysis

Total Claims: 6
Claim 1
Independent Claim 318 words
A process for cooling water by cross flow contact with air comprising the steps of: passing said water downwardly into a contacting zone enclosure in the shape of an inverted, frustoconical annulus at a rate of from 3 to 30 gallons per minute, per square foot of contacting zone normal to the direction of flow of water, said enclosure being completely filled with a filamentous packing having little continuous extensive surface, and having about 80-95 percent free volume, said packing consisting of randomly arranged, interlocked tower packing units, the units being made up of approximAtely circular, integrally connected filament portions having their axes approximately tangent to a circle at approximately evenly spaced points therearound, the number of such spaced approximately circular portions being from 6 to 12 and the diameter of such circle being approximately equal to the diameter of one of such approximately circular filament portions plus the diameter of a smaller circle whose circumference is not less than the croos-sectional dimension of the filament portion in the direction of its axis times the number of such filament portions and not greater than the circumference of one of such approximately circular filament portions; drawing air through ports in the outer side of said contacting enclosure, through said packing and through ports in the inner wall of said enclosure by means of a fan mounted centrally within the circle defined by said annular enclosure, at a rate of from 200 to 800 standard cubic feet per minute, per square foot of packed zone normal to the direction of flow of gas so as to realize a pressure drop, in the air, per foot of packing parallel to the direction of flow of said air, of from 0.2 to 0.8 inches of water; expelling the air drawn through said contactIng zone from within the area central thereto; and removing cooled water from the lower end of said contacting enclosure.
Claim 2
Dependent Claim 318 words
A process for cooling water by cross flow contact with air comprising the steps of: passing said water downwardly into a contacting zone enclosure in the shape of an inverted, frustoconical annulus at a rate of from 3 to 30 gallons per minute, per square foot of contacting zone normal to the direction of flow of water, said enclosure being completely filled with a filamentous packing having little continuous extensive surface, and having about 80-95 percent free volume, said packing consisting of randomly arranged, interlocked tower packing units, the units being made up of approximAtely circular, integrally connected filament portions having their axes approximately tangent to a circle at approximately evenly spaced points therearound, the number of such spaced approximately circular portions being from 6 to 12 and the diameter of such circle being approximately equal to the diameter of one of such approximately circular filament portions plus the diameter of a smaller circle whose circumference is not less than the croos-sectional dimension of the filament portion in the direction of its axis times the number of such filament portions and not greater than the circumference of one of such approximately circular filament portions; drawing air through ports in the outer side of said contacting enclosure, through said packing and through ports in the inner wall of said enclosure by means of a fan mounted centrally within the circle defined by said annular enclosure, at a rate of from 200 to 800 standard cubic feet per minute, per square foot of packed zone normal to the direction of flow of gas so as to realize a pressure drop, in the air, per foot of packing parallel to the direction of flow of said air, of from 0.2 to 0.8 inches of water; expelling the air drawn through said contactIng zone from within the area central thereto; and removing cooled water from the lower end of said contacting enclosure.
Claim 3
Dependent Claim 24 words
The process of claim 1 wherein the pressure drop in the gas is from 0.3 to 0.6 inches of water, per foot of packing.
Claim 4
Dependent Claim 96 words
A process for cooling water by cross flow contact with air as recited in claim 1 wherein the flow of water through the packed contacting zone is from 8 to 25 gallons per minute per square foot of contacting zone normal to the direction of the flow of water, the flow of air is from 400 to 700 standard cubic feet per minute per square foot of packed zone normal to the direction of flow of air, and the pressure drop in the air is from 0.3 to 0.6 inches of water per foot of packing.
Claim 5
Dependent Claim 53 words
A process for cooling water by cross flow contact with air as recited in claim 1 wherein said filamentous packing is comprised of a material having a substantially non-wetting surface characteristic, the water in contact therewith tending thereby to form aggregates rather than to spread out in a film on the said surface.
Claim 6
Dependent Claim 26 words
A process for cooling water by cross flow contact with air as recited in claim 4 wherein said filamentous packing is comprised of a resinous material.

References Cited (Backward Citations)

GB190927938A Cited
GB259882A Cited
US2867425A Cited
US3006436A Cited
US3151187A Cited
US3243166A Cited
US3533607A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1976-09-17 1977-03-19 1977-09-18 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1980-09-17 1981-03-19 1981-09-18 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1984-09-17 1985-03-19 1985-09-18 $7700.00 Window Closed / Lapsed

Assigned Categories & Tags

No categories assigned to this patent yet.

Assign Category Tag