CN204756911U - Circulating vulcanization bed boiler with multilayer level lamina affixad - Google Patents
Circulating vulcanization bed boiler with multilayer level lamina affixad Download PDFInfo
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- CN204756911U CN204756911U CN201520456198.4U CN201520456198U CN204756911U CN 204756911 U CN204756911 U CN 204756911U CN 201520456198 U CN201520456198 U CN 201520456198U CN 204756911 U CN204756911 U CN 204756911U
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- chamber
- support
- vulcanizing chamber
- vulcanizing
- motor
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Abstract
The utility model discloses a circulating vulcanization bed boiler with multilayer level lamina affixad. Install a jar body on the support, the motor is installed to the upper end of the jar body, the pivot is installed to the lower extreme of motor, internal first vulcanizing chamber and the second vulcanizing chamber of divideing into of jar, separate through the fixed plate between first vulcanizing chamber and the second vulcanizing chamber, the second support is installed on the upper portion of fixed plate in the pivot, install second heating fluorescent tube and second spout on the second support, first support is installed to the lower part of fixed plate in the pivot, install first spout and first heating fluorescent tube on the first support, communicating pipe is installed to the lower extreme of first vulcanizing chamber, the lower extreme of second vulcanizing chamber is installed and is stored up the grit chamber, through the slag inlet intercommunication between second vulcanizing chamber and the storage grit chamber, communicating pipe and storage grit chamber intercommunication, store up one side of grit chamber and install the air pump, the gas outlet is installed in one side of motor in the upper end of the jar body, and the inlet pipe is installed to one side of second vulcanizing chamber. The utility model discloses its simple structure is reasonable, and curing efficiency is high, and realizes the cyclic utilization of wastes material.
Description
Technical field
The utility model relates to Fluidized Bed Boiler field, is specifically related to a kind of circulating Fluidized Bed Boiler with multi-layer lamina affixad.
Background technology
The clean combustion technique of the advantages such as recirculating fluidized bed (CFB) combustion technology is that to have fuel tolerance good, and efficiency is high, and pollutant emission is few.In recent years, the development of CFB boiler technology rapidly, kept the large-scale development.Along with maximization development, CFB boiler faces capacity increasing problem.
The increase of boiler capacity is mainly realized by the increase of heating surface, but the increase of amassing due to boiler hearth heating surface and the increase of boiler capacity are not mated, cause CFBB in the process maximized, there is the very scabrous problem of layout of heating surface area, even if or solve, bring again other a lot of problems.
Existing single air distribution plate burner hearth main part adopts rectangular cross section mostly, its cross section as shown in Figure 1, the side of burner hearth is furnished with cyclone separator, Secondary Air is distributed in burner hearth both sides, when expanding burner hearth area, can be subject to the restriction of Secondary Air penetrability, size can not be excessive on Secondary Air direction to which dictates that burner hearth, and this size is often limited to 10m.Therefore, burner hearth amplification can only by increasing its width to realize.Bring the problem of two aspects thus: (1) boiler breadth depth ratio is lacked of proper care, and causes boiler floor space excessive, the fuel feeding system of arranging along furnace chamber width coordinates difficulty, and boiler economics is poor; (2) burner hearth girth increases fast, and water-cooling wall mass flow rate reduces, and reduces boiler safety; (3) burner hearth direction is oversize, causes temperature field in burner hearth, flow field is uneven, reduce boiler performance.Further, single air distribution plate air-distribution device wherein, be subject to the restriction of air distribution plate Central oxygen-supply and length-width ratio, area can not be excessive, is therefore difficult to the needs meeting fluidized bed combustion boiler maximization development.
Utility model content
The purpose of this utility model is the defect for above-mentioned prior art, provides a kind of circulating Fluidized Bed Boiler with multi-layer lamina affixad.It is simple and reasonable, and curing efficiency is high, and realizes the cyclic utilization of waste.
The purpose of this utility model can be achieved through the following technical solutions: a kind of circulating Fluidized Bed Boiler with multi-layer lamina affixad, comprises support, tank body, dreg chamber, air pump, slag inlet, the first heating fluorescent tube, feed pipe, fixed head, the second heating fluorescent tube, filter screen, gas outlet, motor, rotating shaft, the second support, the second spout, the first support, the first spout, communicating pipe, battery and supercharging device;
Described support is provided with tank body, the upper end of tank body is provided with motor, the lower end of motor is provided with rotating shaft, the first vulcanizing chamber and the second vulcanizing chamber is divided in tank body, separated by fixed head between first vulcanizing chamber and the second vulcanizing chamber, the top of fixed head is provided with the second support in rotating shaft, second support is provided with the second heating fluorescent tube and the second spout, the bottom of fixed head is provided with the first support in rotating shaft, first support is provided with the first spout and the first heating fluorescent tube, the lower end of the first vulcanizing chamber is provided with communicating pipe, the lower end of the second vulcanizing chamber is provided with dreg chamber, second vulcanizing chamber is communicated with by slag inlet with between dreg chamber, communicating pipe is communicated with dreg chamber, the side of described dreg chamber is provided with air pump, the upper end of described tank body is provided with gas outlet in the side of motor, the side of the second vulcanizing chamber is provided with feed pipe.
Preferably, between communicating pipe and dreg chamber, supercharging device is installed.
Preferably, the side of tank body is provided with battery.
In the utility model, by arranging two vulcanizing chambers, by the waste delivery of one of them vulcanizing chamber in another one vulcanizing chamber, achieve the cyclic utilization of waste, effectively improve the maximum using of the energy, it also avoid the waste of the energy, curing efficiency is high simultaneously, while having saved cost, also save space.
Accompanying drawing explanation
Fig. 1 is a kind of circulating Fluidized Bed Boiler front view with multi-layer lamina affixad that the utility model proposes;
In figure: 1 support; 2, tank body; 3, dreg chamber; 4, air pump; 5, slag inlet; 6, the first heating fluorescent tube; 7, feed pipe; 8, fixed head; 9, the second heating fluorescent tube; 10, filter screen; 11, gas outlet; 12, motor; 13, rotating shaft; 14, the second support; 15, the second spout; 16, the first support; 17, the first spout; 18, communicating pipe; 19, battery; 20, supercharging device.
Detailed description of the invention
Below in conjunction with accompanying drawing, detailed description of the invention of the present utility model is described in further detail:
As shown in Figure 1, Fig. 1 is a kind of circulating Fluidized Bed Boiler front view with multi-layer lamina affixad that the utility model proposes.
With reference to Fig. 1, a kind of circulating Fluidized Bed Boiler with multi-layer lamina affixad that the utility model proposes, comprises support 1, tank body 2, dreg chamber 3, air pump 4, slag inlet 5, first heating fluorescent tube 6, feed pipe 7, fixed head 8, second heating fluorescent tube 9, filter screen 10, gas outlet 11, motor 12, rotating shaft 13, second support 14, second spout 15, first support 16, first spout 17, communicating pipe 18, battery 19 and supercharging device 20.
In the present embodiment, support 1 is provided with tank body 2, the upper end of tank body 2 is provided with motor 12, the lower end of motor 12 is provided with rotating shaft 13, the first vulcanizing chamber and the second vulcanizing chamber is divided in tank body 2, separated by fixed head 8 between first vulcanizing chamber and the second vulcanizing chamber, the top of fixed head 8 is provided with the second support 14 in rotating shaft 13, second support 14 is provided with the second heating fluorescent tube 9 and the second spout 15, the bottom of fixed head 8 is provided with the first support 16 in rotating shaft 13, first support 16 is provided with the first spout 17 and the first heating fluorescent tube 6, the lower end of the first vulcanizing chamber is provided with communicating pipe 18, the lower end of the second vulcanizing chamber is provided with dreg chamber 3, be communicated with by slag inlet 5 between second vulcanizing chamber with dreg chamber 3, communicating pipe 18 is communicated with dreg chamber 3, the side of dreg chamber 3 is provided with air pump 4, the upper end of tank body 2 is provided with gas outlet 11 in the side of motor 12, the side of the second vulcanizing chamber is provided with feed pipe 7.
In the present embodiment, between communicating pipe 18 and dreg chamber 3, supercharging device 20 is installed.
In the present embodiment, the side of described tank body 2 is provided with battery 19.
More than show and describe general principle of the present utility model and principal character and advantage of the present utility model.The technology people of the industry should understand; the utility model is not restricted to the described embodiments; what describe in above-described embodiment and description just illustrates principle of the present utility model; under the prerequisite not departing from the utility model spirit and scope; the utility model also has various changes and modifications, and these changes and improvements all fall within the scope of claimed the utility model.The claimed scope of the utility model is defined by appending claims and equivalent thereof.
Claims (3)
1. one kind has the circulating Fluidized Bed Boiler of multi-layer lamina affixad, it is characterized in that, comprise support (1), tank body (2), dreg chamber (3), air pump (4), slag inlet (5), first heating fluorescent tube (6), feed pipe (7), fixed head (8), second heating fluorescent tube (9), filter screen (10), gas outlet (11), motor (12), rotating shaft (13), second support (14), second spout (15), first support (16), first spout (17), communicating pipe (18), battery (19) and supercharging device (20),
Described support (1) is provided with tank body (2), the upper end of tank body (2) is provided with motor (12), the lower end of motor (12) is provided with rotating shaft (13), the first vulcanizing chamber and the second vulcanizing chamber is divided in tank body (2), separated by fixed head (8) between first vulcanizing chamber and the second vulcanizing chamber, the top of fixed head (8) is provided with the second support (14) in rotating shaft (13), second support (14) is provided with the second heating fluorescent tube (9) and the second spout (15), the bottom of fixed head (8) is provided with the first support (16) in rotating shaft (13), first support (16) is provided with the first spout (17) and the first heating fluorescent tube (6), the lower end of the first vulcanizing chamber is provided with communicating pipe (18), the lower end of the second vulcanizing chamber is provided with dreg chamber (3), be communicated with by slag inlet (5) between second vulcanizing chamber with dreg chamber (3), communicating pipe (18) is communicated with dreg chamber (3), the side of described dreg chamber (3) is provided with air pump (4), the upper end of described tank body (2) is provided with gas outlet (11) in the side of motor (12), the side of the second vulcanizing chamber is provided with feed pipe (7).
2. the circulating Fluidized Bed Boiler with multi-layer lamina affixad according to claim 1, is characterized in that, is provided with supercharging device (20) between described communicating pipe (18) and dreg chamber (3).
3. the circulating Fluidized Bed Boiler with multi-layer lamina affixad according to claim 1, is characterized in that, the side of described tank body (2) is provided with battery (19).
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN201520456198.4U CN204756911U (en) | 2015-06-29 | 2015-06-29 | Circulating vulcanization bed boiler with multilayer level lamina affixad |
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CN201520456198.4U CN204756911U (en) | 2015-06-29 | 2015-06-29 | Circulating vulcanization bed boiler with multilayer level lamina affixad |
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CN204756911U true CN204756911U (en) | 2015-11-11 |
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CN201520456198.4U Expired - Fee Related CN204756911U (en) | 2015-06-29 | 2015-06-29 | Circulating vulcanization bed boiler with multilayer level lamina affixad |
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN105457686A (en) * | 2015-12-14 | 2016-04-06 | 天津市天环精细化工研究所 | Method for activating benzene-method maleic anhydride catalyst outside reactor |
-
2015
- 2015-06-29 CN CN201520456198.4U patent/CN204756911U/en not_active Expired - Fee Related
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN105457686A (en) * | 2015-12-14 | 2016-04-06 | 天津市天环精细化工研究所 | Method for activating benzene-method maleic anhydride catalyst outside reactor |
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Date | Code | Title | Description |
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C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20151111 Termination date: 20160629 |
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CF01 | Termination of patent right due to non-payment of annual fee |