US20140332362A1 - Destructive distillation apparatus - Google Patents
Destructive distillation apparatus Download PDFInfo
- Publication number
- US20140332362A1 US20140332362A1 US14/346,054 US201214346054A US2014332362A1 US 20140332362 A1 US20140332362 A1 US 20140332362A1 US 201214346054 A US201214346054 A US 201214346054A US 2014332362 A1 US2014332362 A1 US 2014332362A1
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- United States
- Prior art keywords
- drum
- destructive distillation
- discharge
- tripper
- feeding
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Abandoned
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Classifications
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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
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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
- C10B47/28—Other processes
- C10B47/30—Other processes in rotary ovens or retorts
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
- F23G5/02—Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment
- F23G5/027—Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment pyrolising or gasifying stage
- F23G5/0276—Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment pyrolising or gasifying stage using direct heating
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
- F23G5/20—Incineration of waste; Incinerator constructions; Details, accessories or control therefor having rotating or oscillating drums
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F27—FURNACES; KILNS; OVENS; RETORTS
- F27B—FURNACES, KILNS, OVENS, OR RETORTS IN GENERAL; OPEN SINTERING OR LIKE APPARATUS
- F27B7/00—Rotary-drum furnaces, i.e. horizontal or slightly inclined
- F27B7/14—Rotary-drum furnaces, i.e. horizontal or slightly inclined with means for agitating or moving the charge
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F27—FURNACES; KILNS; OVENS; RETORTS
- F27B—FURNACES, KILNS, OVENS, OR RETORTS IN GENERAL; OPEN SINTERING OR LIKE APPARATUS
- F27B7/00—Rotary-drum furnaces, i.e. horizontal or slightly inclined
- F27B7/14—Rotary-drum furnaces, i.e. horizontal or slightly inclined with means for agitating or moving the charge
- F27B7/16—Rotary-drum furnaces, i.e. horizontal or slightly inclined with means for agitating or moving the charge the means being fixed relatively to the drum, e.g. composite means
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F27—FURNACES; KILNS; OVENS; RETORTS
- F27B—FURNACES, KILNS, OVENS, OR RETORTS IN GENERAL; OPEN SINTERING OR LIKE APPARATUS
- F27B7/00—Rotary-drum furnaces, i.e. horizontal or slightly inclined
- F27B7/14—Rotary-drum furnaces, i.e. horizontal or slightly inclined with means for agitating or moving the charge
- F27B7/16—Rotary-drum furnaces, i.e. horizontal or slightly inclined with means for agitating or moving the charge the means being fixed relatively to the drum, e.g. composite means
- F27B7/161—Rotary-drum furnaces, i.e. horizontal or slightly inclined with means for agitating or moving the charge the means being fixed relatively to the drum, e.g. composite means the means comprising projections jutting out from the wall
- F27B7/162—Rotary-drum furnaces, i.e. horizontal or slightly inclined with means for agitating or moving the charge the means being fixed relatively to the drum, e.g. composite means the means comprising projections jutting out from the wall the projections consisting of separate lifting elements, e.g. lifting shovels
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F27—FURNACES; KILNS; OVENS; RETORTS
- F27D—DETAILS OR ACCESSORIES OF FURNACES, KILNS, OVENS, OR RETORTS, IN SO FAR AS THEY ARE OF KINDS OCCURRING IN MORE THAN ONE KIND OF FURNACE
- F27D19/00—Arrangements of controlling devices
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G2203/00—Furnace arrangements
- F23G2203/20—Rotary drum furnace
- F23G2203/208—Rotary drum furnace with interior agitating members
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G2203/00—Furnace arrangements
- F23G2203/20—Rotary drum furnace
- F23G2203/211—Arrangement of a plurality of drums
Definitions
- the present invention generally relates to material processing apparatus, more particularly, to a destructive distillation apparatus having different-diameter drums, for processing organic wastes.
- Drums in traditional destructive distillation apparatuses have a straight drum structure.
- a destructive distillation drum, a feeding drum and a discharge drum all have the equal diameter at a front end and at a backward end thereof, and a tripper plate is mounted within the destructive distillation drum.
- a feeding end (i.e., a front end) of the destructive distillation drum is positioned to be higher than a discharge end (i.e., a backward end) thereof, or in other words, the front end is inclined with respect to the backward end at a certain angle, so that during heating process thereof, the materials in the destructive distillation drum successively move from the feeding end to the discharge end, under the action of the tripper plate in the destructive distillation drum, and finally are discharged off the destructive distillation drum through the discharge end thereof.
- the materials undergo processing flows such as water evaporation (at a temperature in a range of 100-200° C.), organic matter pyrolysis (at a temperature in a range of 400-500° C.), carbonization (at a temperature in a range of 500-600° C.), and activation (at a temperature of 750-950° C.).
- water evaporation at a temperature in a range of 100-200° C.
- organic matter pyrolysis at a temperature in a range of 400-500° C.
- carbonization at a temperature in a range of 500-600° C.
- activation at a temperature of 750-950° C.
- an object of the present invention is to remove or alleviate at least one aspect of the above problems and defects in the prior arts.
- the present invention provides a destructive distillation apparatus, comprising:
- a feeding drum and a discharge drum respectively located at each of two ends of the destructive distillation drum, wherein the feeding drum is provided with a spiral feeding plate therein and the discharge drum is provided with a spiral discharge plate therein,
- each row of the tripper and guiding plates are consisted of a plurality of tripper and guiding plates, each tripper and guiding plate is formed by a flat plane and a triangle having a slope, the flat planes of each row of the tripper and guiding plates are horizontally arranged, a pointed end of the triangle is directed toward a discharge port of the destructive distillation drum,
- the destructive distillation drum is placed into a combustion chamber, outer was of the feeding drum and the discharge drum each are mounted with supporting roller rings, which are situated onto supporting rollers; an outer wall of the discharge drum is provided with a drive gear ring, which is driven by an electric motor so as to forwards or backwards rotate with the destructive distillation drum and the feeding drum.
- the feeding drum is connected with a gas collecting chamber in the destructive distillation apparatus; and the discharge drum is connected with a discharge chamber of the destructive distillation apparatus.
- a connecting part between the destructive distillation drum and the discharge drum is a conical cylinder, in which a discharge plate is provided.
- an intersection angle of spiral discharge plate to be left-handed with an axis of the discharge drum is 20°-35°.
- an intersecting angle of the spiral feeding plate to be right-handed with an axis of the feeding drum is 25°-35°.
- an intersection angle of the slope of the tripper and guiding plate with the axis of the destructive distillation drum is 10°-30°.
- the destructive distillation drum, the feeding drum, the discharge drum, the tripper and guiding plates, the spiral feeding plate, the discharge plate, the discharge plate and the conical cylinder all are made of 310S stainless steel materials.
- the present invention has the following technical effects:
- the destructive distillation apparatus having a different-diameter drum in accordance with the present invention is not reported or disclosed in the prior art.
- FIG. 1 is a structural schematic view of a different-diameter drum in accordance with the present invention.
- FIG. 2 is a sectional view cut along a line A-A of FIG. 1 , showing a structure and a shape of tripper and guiding plates.
- FIG. 3 is a schematic view showing the different-diameter drum installed onto the destructive distillation apparatus in accordance with the present invention.
- FIG. 4 is a sectional view cut along a line B-B of FIG. 3 .
- the present invention provides a destructive distillation apparatus, comprising:
- a feeding drum and a discharge drum respectively located at each of two ends of the destructive distillation drum, wherein the destructive distillation drum has a larger diameter than the feeding drum and the discharge drum.
- An inner wall of the destructive distillation drum is installed with rows of tripper and guiding plates, and every two adjacent rows of the tripper and guiding plates are kept at a spacing.
- Each row of the tripper and guiding plates are consisted of a plurality of tripper and guiding plates.
- Each tripper and guiding plate is formed by a flat plane and a triangle having a slope, the flat planes of each row of the tripper and guiding plates are horizontally arranged, and a pointed end of the triangle is directed toward a discharge port of the destructive distillation drum.
- the destructive distillation drum is placed into a combustion chamber, and outer walls of the feeding drum and the discharge drum each are mounted with supporting roller rings, which are situated onto supporting rollers.
- An outer wall of the discharge drum is provided with a drive gear ring, which is driven by an electric motor so as to rotate with the destructive distillation drum and the feeding drum.
- the feeding drum is connected with a gas collecting chamber in the destructive distillation apparatus; and the discharge drum is connected with a discharge chamber of the destructive distillation apparatus.
- a connecting part between the destructive distillation drum and the small discharge drum is a conical cylinder, in which a discharge plate is provided.
- an expansion slit or gap is remained between two tripper and guiding plates in each row.
- the discharge drum is provided with a spiral discharge plate therein and an intersection angle of spiral discharge plate to be left-handed with an axis of the discharge drum is 20°-35°.
- the feeding drum is provided with a spiral discharge plate therein and an intersecting angle of the spiral feeding plate to be right-handed with an axis of the feeding drum is 20°-35°.
- the diameter of the destructive distillation drum is 1000 mm-1500 mm, and the length thereof is 2 m-10 m.
- the diameters of the feeding drum and the discharge drum are respectively 500 mm-800 mm, and the lengths thereof are 1200-2500 mm.
- the destructive distillation drum, the feeding drum, the discharge drum, the tripper and guiding plates, the spiral feeding plate, the discharge plate, the discharge plate and the conical cylinder all are made of 310S stainless steel materials.
- FIG. 3 a middle part of which is a destructive distillation drum 1 , wherein a feeding drum 2 is located at one end of the destructive distillation drum whereas a discharge drum 3 is located at the other end thereof.
- the destructive distillation drum 1 has a larger diameter than the feeding drum 2 and the discharge drum 3 .
- the destructive distillation drum 1 can have a diameter in a range of 1000 mm-1500 mm, and the feeding drum 2 and the discharge drum 3 can have a diameter in a range of 500 mm-800 mm.
- FIG. 1 shows a structural front view of the destructive distillation drum of the present invention, and FIG. 4 illustrates an end view thereof.
- the feeding drum 2 is connected with a gas collecting chamber 14 of the destructive distillation apparatus 1 ; and the discharge drum is connected to a discharge chamber 11 of the destructive distillation apparatus.
- the destructive distillation drum 1 is positioned within a combustion chamber 15 .
- the feeding drum 2 and the discharge drum 3 are respectively provided with supporting roller rings 9 at an outer wall thereof, which are supported by supporting rollers 12 .
- An outer wall of the discharge drum 3 is disposed with a drive gear ring 10 , which is driven by an electric motor 13 , so as to rotate the discharge drum 3 , the destructive distillation chamber 1 and the feeding drum 2 .
- a connecting part between the destructive distillation drum 1 and the discharge drum 3 is a conical cylinder 8 , which is provided with a discharge plate 7 therein.
- An inner wall of the destructive distillation drum 1 is installed with rows of tripper and guiding plates 4 , two adjacent rows of which are kept at a certain distance. Two tripper and guiding plates 4 in each row are provided with an expansion gap. An angle between a slope of the tripper and guiding plate 4 and an axis of the drum is 10-30°.
- the discharge drum 3 therein is provided with a spiral discharge plate 6 , and an intersection angle of the spiral discharge plate 6 to be left-handed with the axis of the small discharge drum 3 is 20°-35°.
- the feeding drum 2 therein is provided with a spiral feeding plate 5 , and an intersection angle of the spiral feeding plate 5 to be right-handed with the axis of the small feeding drum 2 is 20°-35°.
- the destructive distillation drum 1 in the destructive distillation apparatus of the present invention is a reducing drum or a different-diameter drum.
- the feeding drum 2 is provided at one end of the destructive distillation drum, whereas the discharge drum 3 is located at the other end.
- the feeding drum 2 is connected with the gas collecting chamber 14 of the destructive distillation apparatus.
- the discharge drum is connected with the discharge chamber 11 of the destructive distillation apparatus, and the destructive distillation drum 1 is located in the combustion chamber 15 .
- the cuter walls of the feeding drum 2 and the discharge drum 3 are provided with the respective supporting roller rings 9 , which are situated onto the supporting roller 12 .
- the outer wall of the discharge drum 3 is disposed with the drive gear ring 10 .
- the drive gear ring 10 is driven by the electric motor 13 , so as to forwards or backwards rotate with the small discharge drum 3 , the destructive distillation chamber 1 and the small feeding drum 2 (For purpose of brevity, detailed description of it is omitted as they are well-known techniques in the art).
- a connecting part between the destructive distillation drum 1 and the discharge drum 3 is configured to be the conical cylinder 8 , which is provided with the discharge plate 7 therein.
- the inner wall of the large destructive distillation drum 1 is installed with rows of tripper and guiding plates 4 , two adjacent of which is kept with a certain distance.
- the expansion gap is disposed between two tripper and guiding plates 4 in each row.
- Two adjacent rows of the tripper and guiding plates 4 are spaced apart from each other with a spacing, and each row of the tripper and guiding plates 4 is consisted of a plurality of tripper and guiding plates.
- Each tripper and guiding plate is composed of a flat plane and a triangle having a slope.
- each tripper and guiding plate The length of the flat plane and slope of each tripper and guiding plate is respectively 300 mm, and the intersection angle of the slope with the drum axis is 25°.
- the flat planes of the each row of the tripper and guiding plates are horizontally arranged, and the pointed angle of the triangle is directed toward the discharge port of the heating drum (as shown in FIG. 2 ).
- the discharge drum 3 therein is provided with a spiral discharge plate 6 , and an intersection angle of the spiral discharge plate 6 to be left-handed with the axis of the small discharge drum 3 is 30°.
- the feeding drum 2 therein is provided with a spiral feeding plate 5 , and an intersection angle of the spiral feeding plate 5 to be right-handed with the axis of the small feeding drum 2 is 30°.
- a diameter of the destructive distillation drum 1 is 1300 mm, and the length thereof is 8 m.
- the diameters of the feeding drum 2 and the discharge drum 3 are respectively 800 mm.
- the lengths of the feeding drum 2 and the discharge drum 3 are respectively 1500 mm, and 2500 mm.
- all of the destructive distillation drum 1 , the feeding drum 2 , the discharge drum 3 , the tripper and guiding plates 4 , the spiral feeding plate 5 , the spiral discharge plate 6 , the discharge plate 7 , and the conical cylinder 8 are made of 310S stainless steel.
- the destructive distillation drum 1 , the feeding drum 2 , and the discharge drum 3 rotate clockwise (seen from the end of the gas collecting chamber 14 ).
- the materials are transported into the feeding drum 2 by a material transport device 17 (herein it is not described in detail as they are known in the art), and enter the large destructive distillation drum 1 under the action of the spiral feeding plate 5 .
- the materials in the large destructive distillation drum 1 are stirred up and heated up by the tripper and guiding plates 4 .
- the materials are heated to 100-200° C. to vaporize the water.
- the temperature is increased up to 400-500° C. to perform the organic matter pyrolysis.
- the temperature is increased up to 500-600° C., to perform the process of carbonization.
- the temperature is increased up to 750-950° C. to perform the process of activation.
- it is possible to accurately control the temperature of the combustion chamber 15 at different stages, in order to save energy source and ensure quality of the product.
- the processing times of the materials in the destructive distillation drum 1 during each process flow and the entire flow can be controlled and adjusted, so as to control the quality of the product.
- the destructive distillation drum 1 , the feeding drum 2 and the discharge drum 3 rotate in an anti-clockwise direction (seen from the end of the gas collecting chamber 14 ).
- the materials in the large destructive distillation drum 1 move from the feeding end to the discharge end, under the action of the tripper and guiding plates 4 ; and under the action of the discharge plate 7 enter the discharge drum 3 .
- the materials enter the discharge chamber under the action of the spiral discharge plate 6 in the discharge drum 3 .
Abstract
The present invention discloses a destructive distillation apparatus, comprising a destructive distillation drum; a feeding drum and a discharge drum, respectively located at each of two ends of the destructive distillation drum. The destructive distillation drum has a larger diameter than the feeding drum and the discharge drum. An inner wall of the destructive distillation drum is installed with rows of tripper and guiding plates, and a spacing is kept between every two adjacent rows of the tripper and guiding plates. Each row of the tripper and guiding plates are consisted of a plurality of tripper and guiding plates, and each tripper and guiding plate is formed by a flat plane and a triangle having a slope. The flat planes of each row of the tripper and guiding plates are horizontally arranged, and a pointed end of the triangle is directed toward a discharge port of the destructive distillation drum. The destructive distillation drum is placed into a combustion chamber. Outer walls of the feeding drum and the discharge drum each are mounted with supporting roller rings, which are situated onto supporting rollers. An outer wall of the discharge drum is provided with a drive gear ring, which is driven by an electric motor so as to forwards or backwards rotate with the destructive distillation drum and the feeding drum. The present invention can control and adjust processing times of the materials in the destructive distillation drum during each process flow and the whole flow, so as to control product quality.
Description
- 1. Field of the Invention
- The present invention generally relates to material processing apparatus, more particularly, to a destructive distillation apparatus having different-diameter drums, for processing organic wastes.
- 2. Description of the Related Art
- Drums in traditional destructive distillation apparatuses have a straight drum structure. A destructive distillation drum, a feeding drum and a discharge drum all have the equal diameter at a front end and at a backward end thereof, and a tripper plate is mounted within the destructive distillation drum. On installation, a feeding end (i.e., a front end) of the destructive distillation drum is positioned to be higher than a discharge end (i.e., a backward end) thereof, or in other words, the front end is inclined with respect to the backward end at a certain angle, so that during heating process thereof, the materials in the destructive distillation drum successively move from the feeding end to the discharge end, under the action of the tripper plate in the destructive distillation drum, and finally are discharged off the destructive distillation drum through the discharge end thereof.
- The traditional drum structures have the following drawbacks:
- 1) During the destructive distillation, the materials undergo processing flows such as water evaporation (at a temperature in a range of 100-200° C.), organic matter pyrolysis (at a temperature in a range of 400-500° C.), carbonization (at a temperature in a range of 500-600° C.), and activation (at a temperature of 750-950° C.). In order to achieve the above processes, the traditionally straight drum is heated in a stepwise way, and thus it is difficult to accurately control the temperature of each process flow, or this causes waste of energy source or affects product quality.
- 2) When the traditionally straight drum is operating, the materials are continuously fed into the drum. Because the materials fed into the drum contain different contents of water and organic matters, it is difficult for the traditionally straight drum to adjust processing times of the materials in the drum during each process flow and the whole flow, on basis of water percentage of the fed materials and so on, and thus it is impossible to control product quality.
- 3) As for the destructive distillation of a certain material, it needs a relatively long processing time in the drum, and thus the traditionally straight drum needs to have a very long length to meet the requirement. After increasing of the length of the drum, thickness and material thereof are necessary to increase accordingly. Since the destructive distillation is performed under a high temperature, after increasing the length of the drum to a certain degree, strength of the drum in the high temperature does not meet the requirement.
- In view of the above, an object of the present invention is to remove or alleviate at least one aspect of the above problems and defects in the prior arts.
- In order to achieve the above object, the present invention provides a destructive distillation apparatus, comprising:
- a destructive distillation drum;
- a feeding drum and a discharge drum, respectively located at each of two ends of the destructive distillation drum, wherein the feeding drum is provided with a spiral feeding plate therein and the discharge drum is provided with a spiral discharge plate therein,
- wherein the destructive distillation drum has a larger diameter than the feeding drum and the discharge drum, an inner wall of the destructive distillation drum is installed with rows of tripper and guiding plates, every two adjacent rows of the tripper and guiding plates are kept at a spacing; each row of the tripper and guiding plates are consisted of a plurality of tripper and guiding plates, each tripper and guiding plate is formed by a flat plane and a triangle having a slope, the flat planes of each row of the tripper and guiding plates are horizontally arranged, a pointed end of the triangle is directed toward a discharge port of the destructive distillation drum,
- wherein the destructive distillation drum is placed into a combustion chamber, outer was of the feeding drum and the discharge drum each are mounted with supporting roller rings, which are situated onto supporting rollers; an outer wall of the discharge drum is provided with a drive gear ring, which is driven by an electric motor so as to forwards or backwards rotate with the destructive distillation drum and the feeding drum.
- In one embodiment, the feeding drum is connected with a gas collecting chamber in the destructive distillation apparatus; and the discharge drum is connected with a discharge chamber of the destructive distillation apparatus.
- Further, a connecting part between the destructive distillation drum and the discharge drum is a conical cylinder, in which a discharge plate is provided.
- Specifically, an intersection angle of spiral discharge plate to be left-handed with an axis of the discharge drum is 20°-35°.
- Specifically, an intersecting angle of the spiral feeding plate to be right-handed with an axis of the feeding drum is 25°-35°.
- Specifically, an intersection angle of the slope of the tripper and guiding plate with the axis of the destructive distillation drum is 10°-30°.
- Specifically, the destructive distillation drum, the feeding drum, the discharge drum, the tripper and guiding plates, the spiral feeding plate, the discharge plate, the discharge plate and the conical cylinder all are made of 310S stainless steel materials.
- As compared to the prior art, the present invention has the following technical effects:
- 1) After transporting the materials into the large destructive distillation drum, the temperatures of different stages are accurately controlled depending on the different stages of the process flows, so as to save energy source and ensure the product quality.
- 2) The processing times of the materials in the large destructive distillation drum during each process flow and the entire flow are controlled and adjusted on basis of the different contents of the water and organic matters contained by the transported materials in the large destructive distillation drum, so as to control the product quality.
- 3) It is also possible to control the processing time of the materials in the large destructive distillation drum based on the processing requirements, without increasing the length of the drum, thereby improving operation reliability of the apparatus.
- The destructive distillation apparatus having a different-diameter drum in accordance with the present invention is not reported or disclosed in the prior art.
-
FIG. 1 is a structural schematic view of a different-diameter drum in accordance with the present invention. -
FIG. 2 is a sectional view cut along a line A-A ofFIG. 1 , showing a structure and a shape of tripper and guiding plates. -
FIG. 3 is a schematic view showing the different-diameter drum installed onto the destructive distillation apparatus in accordance with the present invention. -
FIG. 4 is a sectional view cut along a line B-B ofFIG. 3 . - 1 destructive distillation drum
- 2 feeding drum
- 3 discharge drum
- 4 tripper and guiding plate
- 5 spiral feeding plate
- 6 spiral discharge plate
- 7 discharge plate
- 8 conical cylinder
- 9 supporting roller ring
- 10 drive gear ring
- 11 discharge chamber
- 12 supporting roller
- 13 electric motor
- 14 gas collecting chamber
- 15 combustion chamber
- 16 destructive distillation apparatus
- 17 material transport device
- The present invention provides a destructive distillation apparatus, comprising:
- a destructive distillation drum;
- a feeding drum and a discharge drum, respectively located at each of two ends of the destructive distillation drum, wherein the destructive distillation drum has a larger diameter than the feeding drum and the discharge drum.
- An inner wall of the destructive distillation drum is installed with rows of tripper and guiding plates, and every two adjacent rows of the tripper and guiding plates are kept at a spacing. Each row of the tripper and guiding plates are consisted of a plurality of tripper and guiding plates. Each tripper and guiding plate is formed by a flat plane and a triangle having a slope, the flat planes of each row of the tripper and guiding plates are horizontally arranged, and a pointed end of the triangle is directed toward a discharge port of the destructive distillation drum.
- The destructive distillation drum is placed into a combustion chamber, and outer walls of the feeding drum and the discharge drum each are mounted with supporting roller rings, which are situated onto supporting rollers. An outer wall of the discharge drum is provided with a drive gear ring, which is driven by an electric motor so as to rotate with the destructive distillation drum and the feeding drum.
- In one embodiment, the feeding drum is connected with a gas collecting chamber in the destructive distillation apparatus; and the discharge drum is connected with a discharge chamber of the destructive distillation apparatus.
- Further, a connecting part between the destructive distillation drum and the small discharge drum is a conical cylinder, in which a discharge plate is provided.
- Specifically, an expansion slit or gap is remained between two tripper and guiding plates in each row.
- Specifically, the discharge drum is provided with a spiral discharge plate therein and an intersection angle of spiral discharge plate to be left-handed with an axis of the discharge drum is 20°-35°.
- Specifically, the feeding drum is provided with a spiral discharge plate therein and an intersecting angle of the spiral feeding plate to be right-handed with an axis of the feeding drum is 20°-35°.
- The diameter of the destructive distillation drum is 1000 mm-1500 mm, and the length thereof is 2 m-10 m.
- The diameters of the feeding drum and the discharge drum are respectively 500 mm-800 mm, and the lengths thereof are 1200-2500 mm.
- Specifically, the destructive distillation drum, the feeding drum, the discharge drum, the tripper and guiding plates, the spiral feeding plate, the discharge plate, the discharge plate and the conical cylinder all are made of 310S stainless steel materials.
- Now the present invention is explained in detail below in connecting with the figures.
- As shown, a destructive distillation apparatus provided by the present invention is shown in
FIG. 3 , a middle part of which is adestructive distillation drum 1, wherein afeeding drum 2 is located at one end of the destructive distillation drum whereas adischarge drum 3 is located at the other end thereof. Thedestructive distillation drum 1 has a larger diameter than the feedingdrum 2 and thedischarge drum 3. In the present invention, thedestructive distillation drum 1 can have a diameter in a range of 1000 mm-1500 mm, and the feedingdrum 2 and thedischarge drum 3 can have a diameter in a range of 500 mm-800 mm.FIG. 1 shows a structural front view of the destructive distillation drum of the present invention, andFIG. 4 illustrates an end view thereof. - The feeding
drum 2 is connected with agas collecting chamber 14 of thedestructive distillation apparatus 1; and the discharge drum is connected to adischarge chamber 11 of the destructive distillation apparatus. Thedestructive distillation drum 1 is positioned within acombustion chamber 15. The feedingdrum 2 and thedischarge drum 3 are respectively provided with supporting roller rings 9 at an outer wall thereof, which are supported by supportingrollers 12. - An outer wall of the
discharge drum 3 is disposed with adrive gear ring 10, which is driven by anelectric motor 13, so as to rotate thedischarge drum 3, thedestructive distillation chamber 1 and the feedingdrum 2. A connecting part between thedestructive distillation drum 1 and thedischarge drum 3 is aconical cylinder 8, which is provided with adischarge plate 7 therein. - An inner wall of the
destructive distillation drum 1 is installed with rows of tripper and guidingplates 4, two adjacent rows of which are kept at a certain distance. Two tripper and guidingplates 4 in each row are provided with an expansion gap. An angle between a slope of the tripper and guidingplate 4 and an axis of the drum is 10-30°. - The
discharge drum 3 therein is provided with aspiral discharge plate 6, and an intersection angle of thespiral discharge plate 6 to be left-handed with the axis of thesmall discharge drum 3 is 20°-35°. - The feeding
drum 2 therein is provided with aspiral feeding plate 5, and an intersection angle of thespiral feeding plate 5 to be right-handed with the axis of thesmall feeding drum 2 is 20°-35°. - Preferred Embodiments of the Invention:
- The
destructive distillation drum 1 in the destructive distillation apparatus of the present invention is a reducing drum or a different-diameter drum. The feedingdrum 2 is provided at one end of the destructive distillation drum, whereas thedischarge drum 3 is located at the other end. The feedingdrum 2 is connected with thegas collecting chamber 14 of the destructive distillation apparatus. The discharge drum is connected with thedischarge chamber 11 of the destructive distillation apparatus, and thedestructive distillation drum 1 is located in thecombustion chamber 15. The cuter walls of the feedingdrum 2 and thedischarge drum 3 are provided with the respective supporting roller rings 9, which are situated onto the supportingroller 12. The outer wall of thedischarge drum 3 is disposed with thedrive gear ring 10. Thedrive gear ring 10 is driven by theelectric motor 13, so as to forwards or backwards rotate with thesmall discharge drum 3, thedestructive distillation chamber 1 and the small feeding drum 2 (For purpose of brevity, detailed description of it is omitted as they are well-known techniques in the art). - A connecting part between the
destructive distillation drum 1 and thedischarge drum 3 is configured to be theconical cylinder 8, which is provided with thedischarge plate 7 therein. The inner wall of the largedestructive distillation drum 1 is installed with rows of tripper and guidingplates 4, two adjacent of which is kept with a certain distance. The expansion gap is disposed between two tripper and guidingplates 4 in each row. Two adjacent rows of the tripper and guidingplates 4 are spaced apart from each other with a spacing, and each row of the tripper and guidingplates 4 is consisted of a plurality of tripper and guiding plates. Each tripper and guiding plate is composed of a flat plane and a triangle having a slope. The length of the flat plane and slope of each tripper and guiding plate is respectively 300 mm, and the intersection angle of the slope with the drum axis is 25°. The flat planes of the each row of the tripper and guiding plates are horizontally arranged, and the pointed angle of the triangle is directed toward the discharge port of the heating drum (as shown inFIG. 2 ). - The
discharge drum 3 therein is provided with aspiral discharge plate 6, and an intersection angle of thespiral discharge plate 6 to be left-handed with the axis of thesmall discharge drum 3 is 30°. The feedingdrum 2 therein is provided with aspiral feeding plate 5, and an intersection angle of thespiral feeding plate 5 to be right-handed with the axis of thesmall feeding drum 2 is 30°. - A diameter of the
destructive distillation drum 1 is 1300 mm, and the length thereof is 8 m. The diameters of the feedingdrum 2 and thedischarge drum 3 are respectively 800 mm. The lengths of the feedingdrum 2 and thedischarge drum 3 are respectively 1500 mm, and 2500 mm. in an exemplary example, all of thedestructive distillation drum 1, the feedingdrum 2, thedischarge drum 3, the tripper and guidingplates 4, thespiral feeding plate 5, thespiral discharge plate 6, thedischarge plate 7, and theconical cylinder 8 are made of 310S stainless steel. - When the destructive distillation apparatus begins to operate, the
destructive distillation drum 1, the feedingdrum 2, and thedischarge drum 3 rotate clockwise (seen from the end of the gas collecting chamber 14). The materials are transported into the feedingdrum 2 by a material transport device 17 (herein it is not described in detail as they are known in the art), and enter the largedestructive distillation drum 1 under the action of thespiral feeding plate 5. During the destructive distillation, the materials in the largedestructive distillation drum 1 are stirred up and heated up by the tripper and guidingplates 4. At first, the materials are heated to 100-200° C. to vaporize the water. When the water vaporizing process is finished, the temperature is increased up to 400-500° C. to perform the organic matter pyrolysis. When the process of the organic matter pyrolysis is completed, the temperature is increased up to 500-600° C., to perform the process of carbonization. When the process of carbonization is finished, the temperature is increased up to 750-950° C. to perform the process of activation. In accordance with different stages of the process flow, it is possible to accurately control the temperature of thecombustion chamber 15 at different stages, in order to save energy source and ensure quality of the product. On basis of the different contents of the water and organic matters contained in the feed-in materials of thedestructive distillation drum 1, the processing times of the materials in thedestructive distillation drum 1 during each process flow and the entire flow can be controlled and adjusted, so as to control the quality of the product. - After finishing the activation process, the
destructive distillation drum 1, the feedingdrum 2 and thedischarge drum 3 rotate in an anti-clockwise direction (seen from the end of the gas collecting chamber 14). The materials in the largedestructive distillation drum 1 move from the feeding end to the discharge end, under the action of the tripper and guidingplates 4; and under the action of thedischarge plate 7 enter thedischarge drum 3. Then the materials enter the discharge chamber under the action of thespiral discharge plate 6 in thedischarge drum 3.
Claims (7)
1. A destructive distillation apparatus, comprising:
a destructive distillation drum;
a feeding drum and a discharge drum, respectively located at each of two ends of the destructive distillation drum, wherein the feeding drum is provided with a spiral feeding plate therein and the discharge drum is provided with a spiral discharge plate therein,
wherein the destructive distillation drum has a larger diameter than the feeding drum and the discharge drum, an inner wall of the destructive distillation drum is installed with rows of tripper and guiding plates, every two adjacent rows of the tripper and guiding plates are kept at a spacing; each row of the tripper and guiding plates are consisted of a plurality of tripper and guiding plates, each tripper and guiding plate is formed by a flat plane and a triangle having a slope, the flat planes of each row of the tripper and guiding plates are horizontally arranged, a pointed end of the triangle is directed toward a discharge port of the destructive distillation drum,
wherein the destructive distillation drum is placed into a combustion chamber, outer walls of the feeding drum and the discharge drum each are mounted with supporting roller rings, which are situated onto supporting rollers; an outer wall of the discharge drum is provided with a drive gear ring, which is driven by an electric motor so as to forwards or backwards rotate with the destructive distillation drum and the feeding drum.
2. The destructive distillation apparatus as claimed in claim 1 , wherein the feeding drum is connected with a gas collecting chamber in the destructive distillation apparatus; and the discharge drum is connected with a discharge chamber of the destructive distillation apparatus.
3. The destructive distillation apparatus as claimed in claim 1 , wherein a connecting part between the destructive distillation drum and the discharge drum is a conical cylinder, in which a discharge plate is provided.
4. The destructive distillation apparatus as claimed in claim 1 , wherein an intersection angle of spiral discharge plate to be left-handed with an axis of the discharge drum is 20°-35°.
5. The destructive distillation apparatus as claimed in claim 1 , wherein an intersecting angle of the spiral feeding plate to be right-handed with an axis of the feeding drum is 25°-35°.
6. The destructive distillation apparatus as claimed in claim 1 , wherein an intersection angle of the slope of the tripper and guiding plate with the axis of the destructive distillation drum is 10°-30°.
7. The destructive distillation apparatus as claimed in claim 1 , wherein the destructive distillation drum, the feeding drum, the discharge drum, the tripper and guiding plates, the spiral feeding plate, the discharge plate, the discharge plate and the conical cylinder all are made of 310S stainless steel materials.
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN2011102830465A CN103013537A (en) | 2011-09-22 | 2011-09-22 | Destructive distillation device |
CN201110283046.5 | 2011-09-22 | ||
PCT/CN2012/081406 WO2013041002A1 (en) | 2011-09-22 | 2012-09-14 | Destructive distillation equipment |
Publications (1)
Publication Number | Publication Date |
---|---|
US20140332362A1 true US20140332362A1 (en) | 2014-11-13 |
Family
ID=47913877
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US14/346,054 Abandoned US20140332362A1 (en) | 2011-09-22 | 2012-09-14 | Destructive distillation apparatus |
Country Status (3)
Country | Link |
---|---|
US (1) | US20140332362A1 (en) |
CN (1) | CN103013537A (en) |
WO (1) | WO2013041002A1 (en) |
Cited By (2)
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CN106753467A (en) * | 2016-12-25 | 2017-05-31 | 赖德勤 | Drum-type gas retort |
US10604705B2 (en) * | 2016-12-12 | 2020-03-31 | Shuhong ZHU | Material heating device |
Families Citing this family (1)
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CN108750527A (en) * | 2018-08-08 | 2018-11-06 | 重庆新格有色金属有限公司 | A kind of roller transport system of built-in bucket type material guiding parts |
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Also Published As
Publication number | Publication date |
---|---|
WO2013041002A1 (en) | 2013-03-28 |
CN103013537A (en) | 2013-04-03 |
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