CN204478121U - A kind of powder coal gasification furnace wet ash re-use device - Google Patents
A kind of powder coal gasification furnace wet ash re-use device Download PDFInfo
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- CN204478121U CN204478121U CN201520076364.8U CN201520076364U CN204478121U CN 204478121 U CN204478121 U CN 204478121U CN 201520076364 U CN201520076364 U CN 201520076364U CN 204478121 U CN204478121 U CN 204478121U
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- 239000003245 coal Substances 0.000 title claims abstract description 151
- 238000002309 gasification Methods 0.000 title claims abstract description 40
- 239000000843 powder Substances 0.000 title claims abstract description 35
- 230000007246 mechanism Effects 0.000 claims abstract description 33
- 238000002156 mixing Methods 0.000 claims abstract description 29
- 239000000203 mixture Substances 0.000 claims abstract description 24
- 238000001035 drying Methods 0.000 claims abstract description 16
- 239000000706 filtrate Substances 0.000 claims description 15
- 239000002893 slag Substances 0.000 claims description 10
- 238000000151 deposition Methods 0.000 claims description 9
- 230000008520 organization Effects 0.000 claims description 6
- 239000002817 coal dust Substances 0.000 claims description 5
- 238000000034 method Methods 0.000 abstract description 28
- 230000008569 process Effects 0.000 abstract description 21
- 238000002485 combustion reaction Methods 0.000 description 11
- 238000010298 pulverizing process Methods 0.000 description 8
- 238000007599 discharging Methods 0.000 description 5
- 230000000694 effects Effects 0.000 description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- 239000003610 charcoal Substances 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 239000007921 spray Substances 0.000 description 2
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000003575 carbonaceous material Substances 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 230000018044 dehydration Effects 0.000 description 1
- 238000006297 dehydration reaction Methods 0.000 description 1
- 238000011049 filling Methods 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 238000000227 grinding Methods 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 230000035800 maturation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- 229910052698 phosphorus Inorganic materials 0.000 description 1
- 239000011574 phosphorus Substances 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 230000009466 transformation Effects 0.000 description 1
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Abstract
The utility model discloses a kind of powder coal gasification furnace wet ash re-use device, belong to coal gasification apparatus field, comprise the dewatering device carrying out primary drying for dewing ash be connected successively with described powder coal gasification furnace, conveying mechanism and mixing mechanism, described mixing mechanism comprises middle warehouse, batcher, coal slurrypump, raw coal warehouse, feeder and coal pulverizer, described middle warehouse is connected with the first input end of described coal pulverizer by described batcher, described raw coal warehouse is connected with the second input of described coal pulverizer by described feeder, the output of described coal pulverizer is connected with pulverized coal distributor.The utility model utilizes said apparatus to process the powder coal gasification furnace ash that wets, and will wet ash repeatedly after drying, and mix in right amount, then burn, both ensure that the secondary of wet ash utilizes, also improved the utilization rate of wet ash with raw coal.
Description
Technical field
The utility model relates to coal gasification apparatus field, more specifically, relate to a kind of powder coal gasification furnace wet ash re-use device.
Background technology
Along with the day by day maturation of Coal Gasification Technology, the day of petroleum resources is becoming tight, and make the Coal Chemical Industry of China enter fast-developing period, powdered coal pressuring gasified Processes and apparatus occupies market rapidly.There is the high problem of phosphorus content in the wet ash of powder coal gasification furnace discharge, the dry base caloric value of wet ash is about 6000kcal/kg.
At present, the wet major way of ash of most factory processes is export trade, the transport resource of export trade process not only at substantial, and the processing cost that improve wet ash.And be usually less than 50 μm due to the diameter of wet ash particle, easily spread with the wind, it is stacked and also can to periphery and environment on the way in transportation.
Chinese patent literature application notification number CN103968369A discloses, and " in a kind of coal gasification, refuse wets the secondary charcoal combustion system in ash, conveyer is in series with successively along wet grey transporting direction, warehouse, helixes feed equipment, pressure conveyer device, heater and burner, this utility model inputs in warehouse to carry out concentrating by the imperfect combustion carbonaceous material (i.e. wet ash) that coal gasification apparatus produces by conveyer and stores, then stirring conveying by helixes feed equipment squeezes in pressure conveyer device by wet ash, formed in wet grey high-pressure delivery to burner and carry out burning utilization, be incubated by the wet ash of heat tracing pipe to High voltage output in high-pressure delivery process, ensure the unimpeded flowing in the duct of wet ash." this secondary charcoal combustion system disclosed in this utility model only carries out primary drying, cause the water content of wet ash higher, and wet grey calorific value own is relatively low, the wet ash through heating directly enters burner burning, is difficult to the Thorough combustion ensureing wet ash.
Utility model content
In order to overcome the defect of prior art, technical problem to be solved in the utility model is to propose a kind of powder coal gasification furnace and wets the re-use device of ash, will wet ash repeatedly after drying, mix in right amount with raw coal, burn again, both ensure that the secondary of wet ash utilizes, also improved the utilization rate of wet ash.
For reaching this object, the utility model by the following technical solutions:
A kind of powder coal gasification furnace that the utility model provides wet ash re-use device, comprise the dewatering device carrying out primary drying for dewing ash be connected successively with described powder coal gasification furnace, conveying mechanism and mixing mechanism, described mixing mechanism comprises the middle warehouse for storing wet ash, for controlling the batcher of wet grey charging rate, for storing the raw coal warehouse of raw coal, for controlling the feeder of raw coal charging rate and the coal pulverizer for mixing the mixture of raw coal and wet ash, described middle warehouse is connected with the first input end of described coal pulverizer by described batcher, described raw coal warehouse is connected with the second input of described coal pulverizer by described feeder, the output of described coal pulverizer is connected with the pulverized coal distributor for shunting coal dust.
Further technical scheme of the present utility model: described mixing mechanism also comprises the coal slurrypump that the wet ash for exporting described batcher pressurizes, described coal slurrypump is arranged on below described batcher, is connected with described coal pulverizer.
Further technical scheme of the present utility model: also comprise the air preheater be arranged on boiler, the hot air outlet of described air preheater is connected with described coal pulverizer, for carrying out redrying to wet ash in described coal pulverizer.
Further technical scheme of the present utility model: the hot air temperature that the hot air outlet of described air preheater is discharged controls between 250 DEG C ~ 380 DEG C.
Further technical scheme of the present utility model: described dewatering device is made up of at least two vacuum filters.
Further technical scheme of the present utility model: the first output of described vacuum filter is connected with described conveying mechanism, is disposed to wet ash on described conveying mechanism, and its second output is connected with filtrate depositing reservoir, filtrate is delivered in filtrate depositing reservoir.
Further technical scheme of the present utility model: described structure for conveying comprises:
First ribbon conveyer, for receiving the wet ash from described dewatering device.
Three-way diverter valve, for carrying out break-in to the conveying of wet ash.
Second ribbon conveyer, for receiving the wet ash from described three-way diverter valve.
Middle slag field, for the wet ash of temporary reservoir.
The input port of described three-way diverter valve is positioned at immediately below the discharge end of described first ribbon conveyer, and its first output is positioned at the top of described second belt conveyor, and its second output is positioned at the top of described middle slag field.
Further technical scheme of the present utility model: described structure for conveying also comprises the 3rd ribbon conveyer for wet ash being delivered to described mixed organization, the discharge end of described second ribbon conveyer is connected with the feed end of described 3rd ribbon conveyer.
Further technical scheme of the present utility model: after described mixed organization mixing, form the mixture of wet ash and raw coal, the ratio of this mixture contained humidity should control 15% ~ 30%.
The above-mentioned powder coal gasification furnace of the utility model wet ash re-use device implement as follows:
S00: discharge wet ash from described powder coal gasification furnace;
S10: wet ash carries out primary drying process through described dewatering device;
S20: the wet ash after primary drying process is delivered to described mixing mechanism through described conveying mechanism;
S30: in described mixing mechanism, will wet ash and raw coal mixing, form the mixture of wet ash and raw coal, and carry out redrying process and pulverization process to mixture;
S40: the mixture through redrying process and pulverization process is delivered to pulverized-coal fired boiler.
The beneficial effects of the utility model are:
The utility model provide powder coal gasification furnace wet ash re-use device, be provided with mixing mechanism, coal pulverizer in mixing mechanism is connected with middle warehouse with raw coal warehouse respectively, realize the mixing to wet ash and raw coal, and coal-grinding function carries out pulverization process to wet ash and raw coal mixture, ensure the mixture Thorough combustion of wet ash and raw coal, thus reach the object reducing raw coal consumption.Be provided with dewatering device and air preheater, primary drying and redrying can be carried out to wet ash respectively, ensure that the water content in the mixture of wet ash and raw coal is lower.By the effect of three-way diverter valve, in normal conditions, wet ash can be delivered to middle warehouse, under fault condition, wet ash can be delivered to middle slag field, therefore when this device is in fault condition, powder coal gasification furnace also can normal deslagging.
The utility model also adopts method below to recycle the wet ash of a kind of powder coal gasification furnace, and after wet ash mixes with raw coal by the method according to a certain percentage, then carry out burning process, this method can recycle wet ash, also can reduce the consumption of raw coal.
Accompanying drawing explanation
Fig. 1 is that powder coal gasification furnace that the utility model detailed description of the invention provides wets the mechanism map of re-use device of ash;
Fig. 2 is that powder coal gasification furnace that the utility model detailed description of the invention provides wets the flow chart of reuse method of ash.
In figure:
1, powder coal gasification furnace; 41, middle warehouse; 42, batcher; 43, raw coal warehouse; 44, feeder; 45, coal pulverizer; 46, pulverized coal distributor; 47, coal slurrypump; 21, vacuum filter; 5, filtrate depositing reservoir; 31,
First ribbon conveyer; 32, the second ribbon conveyer; 33, the 3rd ribbon conveyer; 34, three-way diverter valve; 35, middle slag field.
Detailed description of the invention
The technical solution of the utility model is further illustrated by detailed description of the invention below in conjunction with accompanying drawing.
Embodiment one
As shown in Figure 1, a kind of powder coal gasification furnace provided in the present embodiment one wet ash re-use device, comprise dewatering device, conveying mechanism and mixing mechanism, dewatering device, conveying mechanism and mixing mechanism are connected with powder coal gasification furnace 1 successively.Dewatering device is used for dewing ash and carries out first time drying process, and be called for short primary drying, conveying mechanism is used for wet ash to be delivered to mixed organization from powder coal gasification furnace 1, and mixed organization is used for wet ash and raw coal to carry out mixing and pulverizing.
Mixing mechanism comprises middle warehouse 41, batcher 42, raw coal warehouse 43, feeder 44 and coal pulverizer 45, the feeding mouth of middle warehouse 41 is positioned at one end of conveying mechanism, its discharging opening is connected with the input port of batcher 42, the delivery outlet of batcher 42 is connected with the first input end of coal pulverizer 45, the discharging opening of raw coal warehouse 43 is connected with the input port of feeder 44, and the delivery outlet of feeder 44 is connected with the second input of coal pulverizer 45.Wherein, middle warehouse 41 is for the storage of wet ash; Batcher 42 is for controlling wet grey charging rate; Raw coal warehouse 43 is for the storage of raw coal; Feeder 44 is for controlling raw coal charging rate; Coal pulverizer 45 is for carrying out mixed processing and pulverization process to the mixture of raw coal and wet ash.
From the wet ash of middle warehouse 41 under the effect of batcher 42, be delivered to the first input end of coal pulverizer 45, from raw coal warehouse 43 raw coal feeder 44 act under, be delivered to the second input of coal pulverizer 45, wet ash and raw coal mixing in coal pulverizer 45, and transform into coal dust by the pulverization process of coal pulverizer 45.The output of coal pulverizer 45 is connected with pulverized coal distributor 46, and pulverized coal distributor 46 is for shunting coal dust, and the coal dust after shunting sprays in the burner hearth of pulverized-coal fired boiler and burns.
Further, mixing mechanism also comprises coal slurrypump 47, and it is arranged on the below of batcher 42, is connected with coal pulverizer 45, and namely the input port of coal slurrypump 47 is connected with the delivery outlet of batcher 42, and its delivery outlet is connected with the first input end of coal pulverizer 45.Coal slurrypump 47 pressurizes for the wet ash exported batcher 42, forms the wet ash of high pressure, is convenient to realize remote conveying and delivers in coal pulverizer 45.
Further, the powder coal gasification furnace provided in the present embodiment wet ash re-use device also comprise air preheater, air preheater is arranged on other heat-producing devices such as boiler usually.The hot air outlet of air preheater is connected with coal pulverizer 45 the 3rd input, and the 3rd input is the hot air inlet on coal pulverizer 45, and the hot-air flowed out from air preheater carries out redrying to wet ash coal pulverizer 45.
Preferred further, the hot air temperature that the hot air outlet of air preheater is discharged controls between 250 DEG C ~ 380 DEG C, this temperature can ensure in the process of redrying, and wet grey drying effect is good, also can prevent wet ash and raw coal from coal pulverizer, in advance oxidation reaction occurring.
Further, dewatering device is made up of the vacuum filter 21 of at least two.First output of vacuum filter 21 is connected with conveying mechanism, is disposed on conveying mechanism by wet ash, and its second output is connected with filtrate depositing reservoir 5, filtrate is delivered in filtrate depositing reservoir 5.Act on through vacuum filter 21, the water content control in wet ash, in the scope of 30% ~ 50%, after filtrate is then collected, by Cemented filling in filtrate depositing reservoir 5, realizes the recycling to filtrate.
Further, structure for conveying comprises the first 32, one, ribbon conveyer 31, second ribbon conveyer or multiple stage the 3rd ribbon conveyer 33, middle slag field 35 and three-way diverter valve 34.First ribbon conveyer 31 is positioned at the below of vacuum filter 21 discharging opening, from the wet ash through primary drying that vacuum filter 21 is discharged, falls on the first ribbon conveyer 31.The input port of three-way diverter valve 34 is positioned at immediately below the discharge end of the first ribbon conveyer 31, and the wet ash flowed out from the discharge end of the first ribbon conveyer 31 is fallen three-way diverter valve 34.Three-way diverter valve 34 first output is positioned at the top of the second belt conveyor, and its second output is positioned at the top of middle slag field 35.Due to the transformation of three-way diverter valve 34, in normal conditions, wet ash can be delivered to middle warehouse 41; Under fault condition, wet ash can be delivered to middle the slag field 35 of the ash that to wet for temporary reservoir, when making this device be in fault condition, powder coal gasification furnace 1 also can normally hydrofuge be grey.Second ribbon conveyer 32, for receiving the wet ash from three-way diverter valve 34, and is delivered to the wet grey level of discharging from three-way diverter valve 34 on the 3rd ribbon conveyer 33.The discharge end of the second ribbon conveyer 32 is connected with the feed end of the 3rd ribbon conveyer 33, and the 3rd ribbon conveyer 33 is tilting transporter, has three, the wet ash being in lower can be delivered to and have in the middle warehouse 41 of certain altitude.
Preferred further, after mixed organization mixing, form the mixture of wet ash and raw coal, the feedback signal that can be detected by moisture on-line, control the mixed proportion of wet ash and raw coal, the ratio of mixture contained humidity should be controlled 15% ~ 30%, thus ensure that mixture has good combustion characteristics.
Embodiment two
The reuse method of a kind of grey re-use device that wets for powder coal gasification furnace provided in embodiment two, mix for 500t/h HTHP pulverized-coal fired boiler and burn wet ash, implement as follows:
S00 step: the wet ash of discharging from powder coal gasification furnace 1, due to moisture more, also can be called buck, i.e. the mixture of ash discharge and water.
S10 step: wet ash carries out primary drying process through dewatering device, and namely carry out filtering means dehydration process by vacuum filter 21, filtrate is recycled by filtrate depositing reservoir 5.Low-moisture wet grey combustion characteristics following (see table 1) is fallen:
Table 1 wets grey combustion characteristics
S20 step: by the wet ash after primary drying process, delivers in the middle warehouse 41 in mixing mechanism through the first ribbon conveyer 31, second ribbon conveyer 32 and the 3rd ribbon conveyer 33.When re-use device is in fault condition, also can passes through three-way diverter valve 34 break-in effect, wet ash is disposed to middle slag field 35.
S30 step: in mixing mechanism, coal pulverizer 45 will wet ash and raw coal mixing, and carry out shattering process, form the mixture of wet grey and raw coal, then carry out redrying process by air preheater to mixture.Raw coal burnup characteristics following (see table 2):
Table 2 raw coal combustion characteristic
Mixture after super-dry process and pulverization process sprays in the burner hearth of pulverized-coal fired boiler and burns.Mixture burns characteristic following (see table 3):
Table 3 mixture burns characteristic
S40 step: the mixture through redrying process and pulverization process is delivered in pulverized-coal fired boiler.
After wet ash mixes with raw coal by the method according to a certain percentage, then carry out burning process, this method can recycle wet ash, also can reduce the consumption of raw coal.By boiler rating, when all adopting raw coal as combustion material, former the consumption of coal is about 70.89t/h as calculated; When adopting raw coal to mix wet ash as combustion material, former the consumption of coal is about 61.91t/h as calculated, and the burning amount of mixing of wet ash is about 24t/h.
Shown by raw coal consumption result of calculation:, 500t/h HTHP pulverized-coal fired boiler reduces raw coal consumption 8.98t by rated capacity is per hour after mixing and burning powder coal gasification furnace 1 (HT-L) the wet ash that discharges.
The utility model is described by preferred embodiment, and those skilled in the art know, when not departing from spirit and scope of the present utility model, can carry out various change or equivalence replacement to these characteristic sum embodiments.The utility model is not by the restriction of specific embodiment disclosed herein, and other embodiments fallen in the claim of the application all belong to the scope of the utility model protection.
Claims (8)
1. powder coal gasification furnace wets a re-use device for ash, comprise be connected successively with described powder coal gasification furnace (1) for grey dewatering device and the conveying mechanism carrying out primary drying of dewing, it is characterized in that:
Also comprise mixing mechanism;
Described mixing mechanism comprise middle warehouse (41) for storing wet ash, for control wet grey charging rate batcher (42), for store raw coal raw coal warehouse (43), for controlling the feeder (44) of raw coal charging rate and the coal pulverizer (45) for mixing raw coal and wet grey mixture;
Described middle warehouse (41) is connected by the first input end of described batcher (42) with described coal pulverizer (45), and described raw coal warehouse (43) is connected by second input of described feeder (44) with described coal pulverizer (45);
The output of described coal pulverizer (45) is connected with the pulverized coal distributor (46) for shunting coal dust.
2. powder coal gasification furnace according to claim 1 wet ash re-use device, it is characterized in that:
Described mixing mechanism also comprises the coal slurrypump (47) that the wet ash for exporting described batcher (42) pressurizes;
Described coal slurrypump (47) is arranged on described batcher (42) below, is connected with described coal pulverizer (45).
3. powder coal gasification furnace according to claim 1 wet ash re-use device, it is characterized in that:
Also comprise the air preheater be arranged on boiler;
The hot air outlet of described air preheater is connected with described coal pulverizer (45), for carrying out redrying to wet ash in described coal pulverizer (45).
4. powder coal gasification furnace according to claim 3 wet ash re-use device, it is characterized in that:
The hot air temperature that the hot air outlet of described air preheater is discharged controls between 250 DEG C ~ 380 DEG C.
5. powder coal gasification furnace according to claim 1 wet ash re-use device, it is characterized in that:
Described dewatering device is made up of at least two vacuum filters (21).
6. powder coal gasification furnace according to claim 5 wet ash re-use device, it is characterized in that:
First output of described vacuum filter (21) is connected with described conveying mechanism, wet ash is disposed on described conveying mechanism, its second output is connected with filtrate depositing reservoir (5), filtrate is delivered in filtrate depositing reservoir (5).
7. powder coal gasification furnace according to claim 1 wet ash re-use device, it is characterized in that, described structure for conveying comprises:
First ribbon conveyer (31), for receiving the wet ash from described dewatering device;
Three-way diverter valve (34), for carrying out break-in to the conveying of wet ash;
Second ribbon conveyer (32), for receiving the wet ash from described three-way diverter valve (34);
Middle slag field (35), for the wet ash of temporary reservoir;
The input port of described three-way diverter valve (34) is positioned at immediately below the discharge end of described first ribbon conveyer (31), its first output is positioned at the top of described second belt conveyor, and its second output is positioned at the top of described middle slag field (35).
8. powder coal gasification furnace according to claim 7 wet ash re-use device, it is characterized in that, described structure for conveying also comprises:
3rd ribbon conveyer (33), for being delivered to described mixed organization by wet ash;
The discharge end of described second ribbon conveyer (32) is connected with the feed end of described 3rd ribbon conveyer (33).
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| CN201520076364.8U CN204478121U (en) | 2015-02-03 | 2015-02-03 | A kind of powder coal gasification furnace wet ash re-use device |
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| CN201520076364.8U CN204478121U (en) | 2015-02-03 | 2015-02-03 | A kind of powder coal gasification furnace wet ash re-use device |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104791826A (en) * | 2015-02-03 | 2015-07-22 | 航天长征化学工程股份有限公司 | Recycling device and method for wet ash of pulverized coal gasification furnace |
| CN105819231A (en) * | 2016-03-28 | 2016-08-03 | 徐州工业职业技术学院 | Pipeline conveying method and device for gas-making wet coal ash |
| CN109160480A (en) * | 2018-06-25 | 2019-01-08 | 安徽恒宇环保设备制造股份有限公司 | A kind of dry ash mixes burning transportation system |
-
2015
- 2015-02-03 CN CN201520076364.8U patent/CN204478121U/en active Active
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104791826A (en) * | 2015-02-03 | 2015-07-22 | 航天长征化学工程股份有限公司 | Recycling device and method for wet ash of pulverized coal gasification furnace |
| CN105819231A (en) * | 2016-03-28 | 2016-08-03 | 徐州工业职业技术学院 | Pipeline conveying method and device for gas-making wet coal ash |
| CN109160480A (en) * | 2018-06-25 | 2019-01-08 | 安徽恒宇环保设备制造股份有限公司 | A kind of dry ash mixes burning transportation system |
| CN109160480B (en) * | 2018-06-25 | 2020-06-16 | 安徽恒宇环保设备制造股份有限公司 | Dry ash blending combustion conveying system |
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