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US3971634A Expired / Lapsed US ⏱️ 0.0 years remaining

Heat pipe methanator

Assignee: Energy Research and Development Administration ERDA
•
Filing: 1975-04-25
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Granted: 1976-07-27
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Expires: 1995-04-25
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Abstract

Abstract A heat pipe methanator for converting coal gas to methane. Gravity return heat pipes are employed to remove the heat of reaction from the methanation promoting catalyst, transmitting a portion of this heat to an incoming gas pre-heat section and delivering the remainder to a steam generating heat exchanger.

Inventors

  • 👤 William A. Ranken
  • 👤 Joseph E. Kemme

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-26 13:43
CPC Classifications
F; F28; F28D; F28D15/00; F28D15/02; F28D15/04; F28D15/046; C; C07; C07C; C07C1/00; C07C1/02; C07C1/04; C07C1/0405; C07C1/042; F28D15/0275

Claims Analysis

Total Claims: 14
Claim 1
Independent Claim 184 words
A coal gas methanator of the type employing heat pipes comprising: an elongated pressure shell having a methanation section, a preheat section, a heat exchanger section and a start-up heat exchanger section; separating means for separating said heat exchanger section from said methanation section and for separating said start-up heat exchanger section from said methanation section; a plurality of heat pipes enclosed in said elongated pressure shell; heat pipe supporting means in said separating means; A catalyst coating on the exterior walls of said plurality of heat pipes in said methanation section, said catalyst reacting hydrogen and carbon monoxide to produce methane in an exothermic reaction; transfer means containing a working fluid within said plurality of heat pipes to transfer the heat of reaction at constant temperature from said methanation section to said preheat section, and to transfer remaining heat to said heat exchanger section; and temperature control means including an inert gas in said plurality of heat pipes together with said working fluid to vary the amount of working fluid in the heat exchanger section, keeping the temperature in said methanation section constant.
Claim 2
Dependent Claim 184 words
A coal gas methanator of the type employing heat pipes comprising: an elongated pressure shell having a methanation section, a preheat section, a heat exchanger section and a start-up heat exchanger section; separating means for separating said heat exchanger section from said methanation section and for separating said start-up heat exchanger section from said methanation section; a plurality of heat pipes enclosed in said elongated pressure shell; heat pipe supporting means in said separating means; A catalyst coating on the exterior walls of said plurality of heat pipes in said methanation section, said catalyst reacting hydrogen and carbon monoxide to produce methane in an exothermic reaction; transfer means containing a working fluid within said plurality of heat pipes to transfer the heat of reaction at constant temperature from said methanation section to said preheat section, and to transfer remaining heat to said heat exchanger section; and temperature control means including an inert gas in said plurality of heat pipes together with said working fluid to vary the amount of working fluid in the heat exchanger section, keeping the temperature in said methanation section constant.
Claim 3
Dependent Claim 42 words
In the coal gas methanator set forth in claim 1, said transfer means comprising: means enabling evaporation of said working fluid in said heat pipes in the region of said methanation section and conducting said evaporated working fluid to said preheat section.
Claim 4
Dependent Claim 19 words
In the coal gas methanator set forth in claim 2, said heat exchanger section condensing said evaporated working fluid.
Claim 5
Dependent Claim 23 words
In the coal gas methanator set forth in claim 3, means for returning said working fluid in liquid form to said methanation section.
Claim 6
Dependent Claim 48 words
In the coal gas methanator set forth in claim 4, said means for returning said working fluid comprising: separating means for separating liquid working fluid from gaseous working fluid; and providing a tilt in said heat pipes enabling said liquid working fluid to return to the methanation section.
Claim 7
Dependent Claim 83 words
In the coal gas methanator set forth in claim 5, said separating means comprising: perforated baffle means in the heat exchanger section of said heat pipe enabling condensed working fluid to flow beneath said baffle means; an artery in the methanation section of said heat pipes to return said working fluid condensed under said baffle to said methanation section; and, dispensing means for dispersing said condensed working fluid from said artery to the inner walls of the heat pipes in the methanation section.
Claim 8
Dependent Claim 39 words
In the coal gas methanator set forth in claim 6, said dispensing means comprising: an aperture in said artery; wick means on the inner walls of said heat pipe; and dispensing means connecting said aperture to said wick means.
Claim 9
Dependent Claim 23 words
In the coal gas methanator set forth in claim 7, said wick means comprising screening lining the inner wall of the heat pipe.
Claim 10
Dependent Claim 27 words
In the coal gas methanator set forth in claim 7, said wick means comprising a plurality of circumferential grooves in the inner wall of the heat pipe.
Claim 11
Dependent Claim 86 words
In a heat pipe methanator, the combination of: a reaction chamber and a heat exchanger; a heat pipe having an evaporating section in operative relation with said reaction chamber and a condensing section in operative relation with said heat exchanger; thimble means in said heat exchanger for receiving said condensing section; means for containing a working fluid in said heat pipe; and temperature control means including an inert gas in said heat pipe, held by said working fluid adjacent the end wall of said condensing section.
Claim 12
Dependent Claim 86 words
In a heat pipe methanator, the combination of: a reaction chamber and a heat exchanger; a heat pipe having an evaporating section in operative relation with said reaction chamber and a condensing section in operative relation with said heat exchanger; thimble means in said heat exchanger for receiving said condensing section; means for containing a working fluid in said heat pipe; and temperature control means including an inert gas in said heat pipe, held by said working fluid adjacent the end wall of said condensing section.
Claim 13
Dependent Claim 45 words
In the heat pipe methanator set forth in claim 10, said thimble means having a first end open to said reaction chamber and adapted to receive the condensing end of said heat pipe, and a closed end sealing said reaction chamber from said heat exchanger.
Claim 14
Dependent Claim 72 words
In the heat pipe methanator set forth in claim 11, said temperature control means including a varying reduced wall thickness on said heat pipe in said condensing section defining a varying width gap between the inner wall of said thimble and the outer wall of said heat pipe, and enabling expansion and contraction of said inert gas to control the amount of heat supplied by said working fluid to said heat exchanger.

References Cited (Backward Citations)

US2778610A Cited
US3734173A Cited
US3779310A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1979-07-27 1980-01-26 1980-07-27 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1983-07-27 1984-01-26 1984-07-27 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1987-07-27 1988-01-26 1988-07-27 $7700.00 Window Closed / Lapsed

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