US1858796A - Apparatus for fluidizing and carbonizing pulverized coal - Google Patents
Apparatus for fluidizing and carbonizing pulverized coal Download PDFInfo
- Publication number
- US1858796A US1858796A US331861A US33186129A US1858796A US 1858796 A US1858796 A US 1858796A US 331861 A US331861 A US 331861A US 33186129 A US33186129 A US 33186129A US 1858796 A US1858796 A US 1858796A
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- US
- United States
- Prior art keywords
- cylinder
- outlet
- fluidizing
- pulverized coal
- carbonizing
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- Expired - Lifetime
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
- C10B47/00—Destructive distillation of solid carbonaceous materials with indirect heating, e.g. by external combustion
- C10B47/18—Destructive distillation of solid carbonaceous materials with indirect heating, e.g. by external combustion with moving charge
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10S48/00—Gas: heating and illuminating
- Y10S48/04—Powdered fuel injection
Definitions
- This invention relates to an apparatus for fluidizing and carbonizing pulverized coal in a continuous manner.
- Fig. 1 is a longitudinal section through an illustrative embodiment of the invention
- Fi 2 is a view partly in section along the line 2-2 of Fig. 1.
- reference character 1 indicates a stationary cylinder that may be horizontal or slightly inclined in one direction.
- An inlet 2 for the pulverized coal enters one end of the cylinder 1.
- An outlet 3 for solid residue is provided at the lower side of the other end of the cylinder 1, and an outlet 4 for volatile products is provided at the upper side of the outlet end of the cylinder.
- a jacket 5 surrounds the cylinder 1 and is provided with a hot gas inlet 6 near the outlet end of the cylinder 1 and a spent gas outlet 7 is provided at the other end.
- a helical partition 8 is provided between the cylinder 1 and the jacket 5 to direct the hot gases several times around the cylinder 1, as indicated by the arrows.
- a shaft 9 extends throu h the center of the cylinder 1 and is journa ed in bearings 10 near opposite ends. This shaft may be driven in any convenient way.
- Radial spokes 14 are connected to the sleeve 15 surrounding the rotatable shaft 9, and attached to the outer extremities of the spokes 14 are longitudinal rods 12, to which are attached stirring fingers 13.
- a helical vane scraper 11 which fits the inside of the cylinder 1 is maintained in position by the longitudinal rods 12 so that it rotates when the shaft 9 is rotated.
- the fingers 13 attached to the rods may be of any desired shape, but it is preferred that they have angular faces, so that when the shaft 9 is revolved, and consequently the arms 14.
- the angular faces will tend to move the material in the cylinder 1 away from the outlet end and towards the inlet end.
- the helical vane 11 is so constructed that it also imparts this motion to the material in the cylinder 1, with the result that when pulverized material is being treated its fluidity is ensured.
- a hand-controlled valve 16 is provided in the outlet 3 which leads to the tubular coke cooler 17. Air enters one side of the cooler at 18 and passes out through the outlet 19. Compartments 20 are provided to cause the cooling air to flow through groups of tubes 21 in counter-current direction to the solid material that descends along the outside of these tubes 21, the direction of the air being indicated by the arrows.
- a valved outlet 22 is provided at the bottom of the coke cooler 17.
- gases and volatile products resulting from the heat treatment of the material in the cylinder 1 together with any gases or "apors that might have been impregnated to assist the process and also some finely divided material in suspension will pass through the outlet 4 for further treatment before storage or use.
- Pulverized coal is introduced through the inlet 2 and is subjected to heat in the cylinder 1 while the shaft 9 (with the sleeve 15, arms 14, longitudinal rods 12. stirrin members 13 and helical vane 11) is rotate thus thoroughly stirring and fluidizing the charge, at the same time the helical vane 11 and the stirring members 13 tend to move the material away from the outlet 3. in this manner ensuring the complete fluidity of the material as it passes to the cylinder 1.
- the volatile products that are distilled oif by the heat, together with any gases or vapors impregnated to assist in the process and some fine solid material in suspension pass out through the outlet 4 and may be cleaned or scrubbed in well known manners, and the condensible products may be recovered by passing the volatile products through a condenser, if desired.
- a'device for fluidizing pulverulent material including a cylinder, an inlet for introducing unfluidized material to one end thereof, an outlet for fluidized material at the opposite end thereof, a helical vane within said cylinder and extending longitudinally thereof formed so as to feed unfluidized material away from said outlet whereby only completely fluidized material reaches said outlet, and stirring arms mounted upon said vane and movable with said vane relatively to said cylinder for fluidizing the material therein.
- a device for fluidizing pulverulent material including a cylinder, an inlet for introducing unfluidized material thereto, an outlet for fluidized material, a helical vane rotatably mounted within said cylinder and operable so as to feed unfluidized material away from said outlet whereby only completely fluidized material reaches said outlet, and stirring mechanism supported on said vane and including arms extending longitudinally of said cylinder and outwardly projecting fingers on said arms.
- a'device for fluidizing pulverulent material including a cylinder, an inlet for introducing unfluidized material to one end thereof, an outlet for fluidized material at the opposite end thereof, a helical vane within said cylinder and extending longitudinally thereof formed so as to feed unfluidized material away from said outlet whereby only completely fluidized material reaches said outlet, and stirring arms mounted upon said vane and movable with said vane relatively to said cylinder for fluidizing the material therein.
- a device for fluidizing pulverulent material including a cylinder, an inlet for introducing unfluidized material thereto, an outlet for fluidized material, a helical vane rotatably mounted within said cylinder and operable so as to feed unfluidized material away from said outlet whereby only completely fluidized material reaches said outlet, and stirring mechanism supported on said vane and including arms extending longitudinally of said cylinder and outwardly projecting fingers on said arms.
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- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Combustion & Propulsion (AREA)
- Materials Engineering (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Chemistry (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Description
May 17, 1932 L. s. WILCOXSON APPARATUS FOR FLUIDIZING AND CARFONIZING PULVERIZED COAL Filed Jan. 11, 1929 INVENTOR Patented May 17, 1932 UNITED STATES PATENT OFFICE LESLIE S. WILCOXSON, OF RIDGE-WOOD, NEW JERSEY, ASSIGNOB TO THE BABCOCK & WILOOX COMPANY, OF BAYONNE, NEW JERSEY, A CORPORATION OF NEW JERSEY APPARATUS FOR FLUIDIZING AND CARBONIZING PULVEBIZED COAL Application filed January 11, 1928. Serial No. 381,881.
This invention relates to an apparatus for fluidizing and carbonizing pulverized coal in a continuous manner.
The invention will be understood from the description in connection with the accompanying drawings in which Fig. 1 is a longitudinal section through an illustrative embodiment of the invention, and Fi 2 is a view partly in section along the line 2-2 of Fig. 1.
In the drawings reference character 1 indicates a stationary cylinder that may be horizontal or slightly inclined in one direction. An inlet 2 for the pulverized coal enters one end of the cylinder 1. An outlet 3 for solid residue is provided at the lower side of the other end of the cylinder 1, and an outlet 4 for volatile products is provided at the upper side of the outlet end of the cylinder.
A jacket 5 surrounds the cylinder 1 and is provided with a hot gas inlet 6 near the outlet end of the cylinder 1 and a spent gas outlet 7 is provided at the other end. A helical partition 8 is provided between the cylinder 1 and the jacket 5 to direct the hot gases several times around the cylinder 1, as indicated by the arrows.
A shaft 9 extends throu h the center of the cylinder 1 and is journa ed in bearings 10 near opposite ends. This shaft may be driven in any convenient way. Radial spokes 14 are connected to the sleeve 15 surrounding the rotatable shaft 9, and attached to the outer extremities of the spokes 14 are longitudinal rods 12, to which are attached stirring fingers 13. A helical vane scraper 11 which fits the inside of the cylinder 1 is maintained in position by the longitudinal rods 12 so that it rotates when the shaft 9 is rotated. The fingers 13 attached to the rods may be of any desired shape, but it is preferred that they have angular faces, so that when the shaft 9 is revolved, and consequently the arms 14. rods 12, stirrers 13 and helical vane 11, the angular faces will tend to move the material in the cylinder 1 away from the outlet end and towards the inlet end. The helical vane 11 is so constructed that it also imparts this motion to the material in the cylinder 1, with the result that when pulverized material is being treated its fluidity is ensured.
A hand-controlled valve 16 is provided in the outlet 3 which leads to the tubular coke cooler 17. Air enters one side of the cooler at 18 and passes out through the outlet 19. Compartments 20 are provided to cause the cooling air to flow through groups of tubes 21 in counter-current direction to the solid material that descends along the outside of these tubes 21, the direction of the air being indicated by the arrows. A valved outlet 22 is provided at the bottom of the coke cooler 17.
The gases and volatile products resulting from the heat treatment of the material in the cylinder 1 together with any gases or "apors that might have been impregnated to assist the process and also some finely divided material in suspension will pass through the outlet 4 for further treatment before storage or use.
The operation is as follows: Pulverized coal is introduced through the inlet 2 and is subjected to heat in the cylinder 1 while the shaft 9 (with the sleeve 15, arms 14, longitudinal rods 12. stirrin members 13 and helical vane 11) is rotate thus thoroughly stirring and fluidizing the charge, at the same time the helical vane 11 and the stirring members 13 tend to move the material away from the outlet 3. in this manner ensuring the complete fluidity of the material as it passes to the cylinder 1. The volatile products that are distilled oif by the heat, together with any gases or vapors impregnated to assist in the process and some fine solid material in suspension pass out through the outlet 4 and may be cleaned or scrubbed in well known manners, and the condensible products may be recovered by passing the volatile products through a condenser, if desired.
The residue or solid particles move gradually towards the outlet end of the cylinder 1, g
and pass through the outlet 3 and then through the coke cooler 17 where it is cooled below the ignition temperature before it passes out through the outlet 22 to a place of storage or use.
I claim:
1. The combination in a'device for fluidizing pulverulent material including a cylinder, an inlet for introducing unfluidized material to one end thereof, an outlet for fluidized material at the opposite end thereof, a helical vane within said cylinder and extending longitudinally thereof formed so as to feed unfluidized material away from said outlet whereby only completely fluidized material reaches said outlet, and stirring arms mounted upon said vane and movable with said vane relatively to said cylinder for fluidizing the material therein.
2. The combination in a device for fluidizing pulverulent material including a cylinder, an inlet for introducing unfluidized material thereto, an outlet for fluidized material, a helical vane rotatably mounted within said cylinder and operable so as to feed unfluidized material away from said outlet whereby only completely fluidized material reaches said outlet, and stirring mechanism supported on said vane and including arms extending longitudinally of said cylinder and outwardly projecting fingers on said arms.
LESLIE S. WILCOXSON.
CERTIFICATE OF CORRECTION.
Patent No. 1,858,796. May 17, 1932.
LESLIE S. WILCOXSON.
It is hereby certified that error appears in the printed specification of the above numbered patent requiring correction as follows: Page 1, line 68, for "impregnated" read introduced; and that the said Letters Patent should be read with this correction therein that the some may conform to the record of the case in the Patent Office.
Signed and sealed this 6th day of September, A. D. 1932.
M. J. Moore, (Seal) Acting Commissioner of Patents.
I claim:
1. The combination in a'device for fluidizing pulverulent material including a cylinder, an inlet for introducing unfluidized material to one end thereof, an outlet for fluidized material at the opposite end thereof, a helical vane within said cylinder and extending longitudinally thereof formed so as to feed unfluidized material away from said outlet whereby only completely fluidized material reaches said outlet, and stirring arms mounted upon said vane and movable with said vane relatively to said cylinder for fluidizing the material therein.
2. The combination in a device for fluidizing pulverulent material including a cylinder, an inlet for introducing unfluidized material thereto, an outlet for fluidized material, a helical vane rotatably mounted within said cylinder and operable so as to feed unfluidized material away from said outlet whereby only completely fluidized material reaches said outlet, and stirring mechanism supported on said vane and including arms extending longitudinally of said cylinder and outwardly projecting fingers on said arms.
LESLIE S. WILCOXSON.
CERTIFICATE OF CORRECTION.
Patent No. 1,858,796. May 17, 1932.
LESLIE S. WILCOXSON.
It is hereby certified that error appears in the printed specification of the above numbered patent requiring correction as follows: Page 1, line 68, for "impregnated" read introduced; and that the said Letters Patent should be read with this correction therein that the some may conform to the record of the case in the Patent Office.
Signed and sealed this 6th day of September, A. D. 1932.
M. J. Moore, (Seal) Acting Commissioner of Patents.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US331861A US1858796A (en) | 1929-01-11 | 1929-01-11 | Apparatus for fluidizing and carbonizing pulverized coal |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US331861A US1858796A (en) | 1929-01-11 | 1929-01-11 | Apparatus for fluidizing and carbonizing pulverized coal |
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US1858796A true US1858796A (en) | 1932-05-17 |
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US331861A Expired - Lifetime US1858796A (en) | 1929-01-11 | 1929-01-11 | Apparatus for fluidizing and carbonizing pulverized coal |
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US (1) | US1858796A (en) |
Cited By (12)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2497295A (en) * | 1946-08-01 | 1950-02-14 | Pompes Noel Liverdun Soc | Device for manipulating sand and other pulverulent substances |
US2571300A (en) * | 1949-03-07 | 1951-10-16 | Simpson Martha Offenhauser | Mixing and cutting machine |
US2627668A (en) * | 1949-05-17 | 1953-02-10 | New Jersey Zinc Co | Method of contacting solids and gases |
US2628077A (en) * | 1949-05-17 | 1953-02-10 | New Jersey Zinc Co | Method of effecting indirect heat transfer |
US2657022A (en) * | 1951-04-27 | 1953-10-27 | Nat Dairy Res Lab Inc | Beater mechanism for softening ice cream |
US2989291A (en) * | 1958-07-14 | 1961-06-20 | Julius W Bedner | Continuous mixing machine for concrete and similar substances |
US3096165A (en) * | 1960-09-21 | 1963-07-02 | Eugene W Lane | Combine mounted grain dryer |
US3171476A (en) * | 1962-01-22 | 1965-03-02 | Pietro J Laurito | Fluid treatment device |
US4784081A (en) * | 1986-01-17 | 1988-11-15 | Siemens Aktiengesellschaft | Mixing device for cross-blending of developer mix in developing stations of electrophotographic printer devices |
US5320861A (en) * | 1992-01-03 | 1994-06-14 | Ocean Spray Cranberries, Inc. | Fruit extraction and infusion |
WO1999043422A1 (en) * | 1998-02-25 | 1999-09-02 | Bonilla Leanos Eliseo Alfredo | Device for the treatment of liquids by mechanical vibration |
US20160001241A1 (en) * | 2013-06-27 | 2016-01-07 | Dongguk University Industry-Academic Cooperation Foundation | Apparatus for storing gas hydrate pellets |
-
1929
- 1929-01-11 US US331861A patent/US1858796A/en not_active Expired - Lifetime
Cited By (15)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2497295A (en) * | 1946-08-01 | 1950-02-14 | Pompes Noel Liverdun Soc | Device for manipulating sand and other pulverulent substances |
US2571300A (en) * | 1949-03-07 | 1951-10-16 | Simpson Martha Offenhauser | Mixing and cutting machine |
US2627668A (en) * | 1949-05-17 | 1953-02-10 | New Jersey Zinc Co | Method of contacting solids and gases |
US2628077A (en) * | 1949-05-17 | 1953-02-10 | New Jersey Zinc Co | Method of effecting indirect heat transfer |
US2657022A (en) * | 1951-04-27 | 1953-10-27 | Nat Dairy Res Lab Inc | Beater mechanism for softening ice cream |
US2989291A (en) * | 1958-07-14 | 1961-06-20 | Julius W Bedner | Continuous mixing machine for concrete and similar substances |
US3096165A (en) * | 1960-09-21 | 1963-07-02 | Eugene W Lane | Combine mounted grain dryer |
US3171476A (en) * | 1962-01-22 | 1965-03-02 | Pietro J Laurito | Fluid treatment device |
US4784081A (en) * | 1986-01-17 | 1988-11-15 | Siemens Aktiengesellschaft | Mixing device for cross-blending of developer mix in developing stations of electrophotographic printer devices |
US5320861A (en) * | 1992-01-03 | 1994-06-14 | Ocean Spray Cranberries, Inc. | Fruit extraction and infusion |
US5419251A (en) * | 1992-01-03 | 1995-05-30 | Ocean Spray Cranberries, Inc. | Fruit extraction and infusion |
WO1999043422A1 (en) * | 1998-02-25 | 1999-09-02 | Bonilla Leanos Eliseo Alfredo | Device for the treatment of liquids by mechanical vibration |
US6655826B1 (en) * | 1998-02-25 | 2003-12-02 | Eliseo Alfredo Bonilla Leanos | Device for the treatment of liquids by mechanical vibration |
US20160001241A1 (en) * | 2013-06-27 | 2016-01-07 | Dongguk University Industry-Academic Cooperation Foundation | Apparatus for storing gas hydrate pellets |
US9839887B2 (en) * | 2013-06-27 | 2017-12-12 | Dongshin Hydraulics Co., Ltd. | Apparatus for storing gas hydrate pellets |
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