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US3973623A Expired / Lapsed US ⏱️ 0.0 years remaining

Heat exchange apparatus

Assignee: Mobil Oil AS
•
Filing: 1974-12-06
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Granted: 1976-08-10
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Expires: 1994-12-06
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Abstract

Abstract The invention provides apparatus for heat exchange treatment of a liquid having a mean density within a predetermined range, comprising: At least one substantially horizontal cylindrical elongated tube with an inlet at one end thereof and an outlet at the other end thereof for flow of said liquid therethrough; Means for sweeping the outer surface of said cylindrical tube with fluid for conveying heat; a hollow gas tight shaft rotatably supported within said cylindrical tube so as to be substantially coaxial with said tube; A plurality of preferably spring-loaded longitudinal scraper blades mounted in sequence upon and along the length of said shaft and adapted to scrape substantially all the inner surface of said cylindrical tube upon rotation of the shaft; drive means for rotating the shaft during the passage of liquid therethrough; And wherein the weight per unit length of tube, of said liquid displaced at maximum mean operational temperature thereof by said shaft and scrapers amounts to at least ninety percent of the weight per unit length of tube of said shaft and scrapers.

Inventors

  • 👤 Peter Geoffrey Sarll

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-05 00:37
CPC Classifications
F; F28; F28F; F28F19/00; F28F19/008

Claims Analysis

Total Claims: 4
Claim 1
Independent Claim 250 words
Apparatus for heat exchange treatment of a liquid having a mean density within a predetermined range, comprising: at least one substantially horizontal cylindrical elongated tube with an inlet at one end thereof and an outlet at the other end thereof for flow of said liquid therethrough; means for sweeping the outer surface of said cylindrical tube with fluid for conveying heat; a hollow gas tight shaft having a plurality of tubular gas tight sections joined end to end rotatably supported within said cylindrical tube so as to be substantially coaxial with said tube, each said section extending between bearing supports located at intervals along the tube with a free frictional fit therein to permit the entire assembly of shaft, scrapers and supports to be withdrawn endwise for servicing; a plurality of longitudinal scraper blades mounted in sequence upon and along the length of said shaft and adapted to scrape substantially all the inner surface of said cylindrical tube upon rotation of the shaft; drive means for rotating the shaft during the passage of liquid through said cylindrical tube; and wherein the weight per unit length of tube, of said liquid displaced at maximum mean operational temperature thereof by said shaft and scrapers amounts to at least ninety percent of the weight per unit length of tube of said shaft and scrapers whereby the load in said bearing supports is minimized and uniform scraping action is achieved as the scraper blades bear against all the exchanger surface with substantially equal force.
Claim 2
Dependent Claim 250 words
Apparatus for heat exchange treatment of a liquid having a mean density within a predetermined range, comprising: at least one substantially horizontal cylindrical elongated tube with an inlet at one end thereof and an outlet at the other end thereof for flow of said liquid therethrough; means for sweeping the outer surface of said cylindrical tube with fluid for conveying heat; a hollow gas tight shaft having a plurality of tubular gas tight sections joined end to end rotatably supported within said cylindrical tube so as to be substantially coaxial with said tube, each said section extending between bearing supports located at intervals along the tube with a free frictional fit therein to permit the entire assembly of shaft, scrapers and supports to be withdrawn endwise for servicing; a plurality of longitudinal scraper blades mounted in sequence upon and along the length of said shaft and adapted to scrape substantially all the inner surface of said cylindrical tube upon rotation of the shaft; drive means for rotating the shaft during the passage of liquid through said cylindrical tube; and wherein the weight per unit length of tube, of said liquid displaced at maximum mean operational temperature thereof by said shaft and scrapers amounts to at least ninety percent of the weight per unit length of tube of said shaft and scrapers whereby the load in said bearing supports is minimized and uniform scraping action is achieved as the scraper blades bear against all the exchanger surface with substantially equal force.
Claim 3
Dependent Claim 54 words
Apparatus according to claim 1, wherein the scrapers are spring-loaded and disposed in diametrically opposed pairs, each pair being displaced round the shaft in relation to the next pair, and the total length of all the pairs being substantially equal to the total length of tubular shaft, apart from any fixed scraper blades present.
Claim 4
Dependent Claim 38 words
Apparatus according to claim 2, wherein each scraper blade is mounted in slots in at least two telescopic posts each welded to the shaft and encircled by a coil spring applying pressure between the blade and the shaft.

References Cited (Backward Citations)

CA586169A Cited
US2943845A Cited
US3395419A Cited
US3731339A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1979-08-10 1980-02-09 1980-08-10 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1983-08-10 1984-02-09 1984-08-10 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1987-08-10 1988-02-09 1988-08-10 $7700.00 Window Closed / Lapsed

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