CN204854246U - Gasification cinder drying equipment and system - Google Patents
Gasification cinder drying equipment and system Download PDFInfo
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- CN204854246U CN204854246U CN201520269133.9U CN201520269133U CN204854246U CN 204854246 U CN204854246 U CN 204854246U CN 201520269133 U CN201520269133 U CN 201520269133U CN 204854246 U CN204854246 U CN 204854246U
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- gasification
- gasification cinder
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Abstract
The utility model relates to a coal industry field discloses a gasification cinder drying equipment and system. Wherein, equipment includes: conveyor is used for carrying the gasification cinder, steam generates the device for produce steam, and the desiccator, be used for receiving and come from conveyor's gasification cinder with come from the steam of steam formation device, so that the gasification cinder with steam fully contacts the completion convective heat exchange, thereby dry the gasification cinder. The utility model discloses a cinder that will gasify fully contacts the completion convective heat exchange with steam to dry gasification cinder, thus make the gasification cinder can obtain effectual utilization.
Description
Technical field
The utility model relates to coal chemical technology, particularly, relates to a kind of gasification cinder drying equipment and system.
Background technology
Modern Coal-based Chemical is the emerging field of Coal Chemical Industry.China's Coal Chemical Industry constantly makes a breakthrough in technology and equipment, progressively defines based on advanced Coal Gasification Technology, produces product with the derived energy chemical industry-Modern Coal-based Chemical of petroleum replacing chemical products and oil gas product.Wherein, the product produced comprises the novel energy chemical industrial chains such as coal preparing natural gas, coal liquifaction, coal-ethylene glycol, ammonia from coal and downstream olefin product.But because Modern Coal-based Chemical industry is at the early-stage, be in the demonstration phase, the first commercialization of most core technology, technological process and Integration ofTechnology wait to optimize, and engineering problem need further solution.In efficiency level and pollutant emission, Modern Coal-based Chemical industry still has the leeway of improving further.
In Modern Coal-based Chemical industry, olefin hydrocarbon making by coal gasification workshop produces a large amount of gasification cinders.They are moisture about 50% years old.Such gasification cinder mean calorie is only more than 2500 kilocalories.If dried by these gasification cinders, the calorific value of the gasification cinder after oven dry is estimated more than 4000 kilocalories, thus makes these gasification cinders can obtain fully effective utilization.
Utility model content
The purpose of this utility model is to provide a kind of gasification cinder drying equipment and system.Wherein, this equipment, by gasification cinder has fully been contacted convective heat exchange with hot gas, with drying, gasifying cinder, thus makes gasification cinder to be effectively utilized.
To achieve these goals, the utility model provides a kind of gasification cinder drying equipment.This equipment comprises: conveying device, for carrying described gasification cinder; Hot gas generating apparatus, for generation of hot gas; And
Drying machine, for receiving the gasification cinder from described conveying device and the hot gas from described hot gas generating apparatus, to make described gasification cinder fully contact convective heat exchange with described hot gas, thus dry described gasification cinder.
Preferably, described hot gas generating apparatus comprises: hot-blast stove, for producing heat smoke by combustion fuel coal.
Preferably, described hot gas generating apparatus also comprises: air blast, is installed on described hot-blast stove, for cold air is sent into described hot-blast stove; MOD, is installed on described air blast; And frequency converter, be connected with described MOD, for controlling by the openings of sizes controlling described MOD the air quantity entering described hot-blast stove as required.
Preferably, described drying machine comprises: cylindrical shell, has fully contacted heat exchange for being shed gasification cinder by the wing plate that stir-fries to make described gasification cinder with described hot gas, thus dry described gasification cinder; Sealing device, is installed on the front and back end of described cylindrical shell, enters body for preventing outside cold air and leaks described hot gas; Riding wheel apparatus, is installed on the below of the rolling ring of described cylindrical shell, for being played the role of positioning to described cylindrical shell in radial direction by rolling ring, described cylindrical shell is operated reposefully; Transmission device, is installed on the below of the bull gear of described cylindrical shell, for driving body to rotate by the bull gear on described cylindrical shell; And gear riding wheel apparatus, be installed on the below of the sealing device of described cylinder back-end, for preventing the upper and lower play of body.
Preferably, described equipment also comprises: discharging conveying arrangement, is connected with described drying machine, for dried gasification cinder is transported to product storing and transporting system.
Preferably, described equipment also comprises: particulate retracting device, is connected with described drying machine, for isolating dust granules from the hot gas after convective heat exchange, and reclaims described dust granules.
Preferably, described particulate retracting device comprises: cyclone dust collectors, for isolating described dust granules from the hot gas after convective heat exchange; Conveying worm, for collecting described dust granules; And sealing discharging valve, for the dust granules of collection is entered described discharging conveying arrangement.
Preferably, described equipment also comprises: air-introduced machine, is connected with described particulate retracting device, and being provided for the hot gas after convective heat exchange can enter in air swimmingly.
Preferably, described equipment also comprises: wet scrubber, is connected with described air-introduced machine, for the dust in the hot gas by being formed after mist film and/or spraying layer removing convective heat exchange.
Correspondingly, the utility model also provides a kind of gasification cinder drying system.This system comprises: gasification cinder drying equipment; And control device, be connected with described gasification cinder drying equipment, for controlling described gasification cinder drying equipment.
Preferably, described control device comprises: expansion control interface, for receiving remote control commands; Local control interface, for receiving local control instruction; And controller, for according to described remote control commands or local control instruction, control the operation of described gasification cinder drying equipment.
By technique scheme, gasification cinder is fully contacted convective heat exchange with hot gas, with drying, gasifying cinder, thus gasification cinder can be effectively utilized.
Other features and advantages of the utility model are described in detail in detailed description of the invention part subsequently.
Accompanying drawing explanation
Accompanying drawing is used to provide further understanding of the present utility model, and forms a part for description, is used from explanation the utility model, but does not form restriction of the present utility model with detailed description of the invention one below.In the accompanying drawings:
Fig. 1 is the structural representation of the gasification cinder drying equipment that the utility model provides;
Fig. 2 is the schematic diagram of the detailed description of the invention of the conveying device of the gasification cinder drying equipment that the utility model provides;
Fig. 3 is the schematic diagram of the detailed description of the invention of the hot gas generating apparatus of the gasification cinder drying equipment that the utility model provides;
Fig. 4 is the schematic diagram of the detailed description of the invention of the drying machine of the gasification cinder drying equipment that the utility model provides;
Fig. 5 is the schematic diagram of the detailed description of the invention of the particulate retracting device of the gasification cinder drying equipment that the utility model provides;
Fig. 6 is the structural representation of the gasification cinder drying system that the utility model provides;
Fig. 7 is the schematic diagram of the detailed description of the invention of the control device of the gasification cinder drying system that the utility model provides; And
Fig. 8 is the process chart of the gasification cinder drying equipment that the utility model provides.
Description of reference numerals
1 sealing device 2 riding wheel apparatus
3 cylindrical shell 4 transmission devices
5 gear riding wheel apparatus 10 conveying devices
20 hot gas generating apparatus 30 drying machines
40 belt conveyer 50 sealing feeder
60 hot-blast stove 70 air blasts
80 MOD 90 frequency converters
100 particulate retracting device 110 air-introduced machines
120 wet scrubber 130 cyclone dust collectors
140 conveying worm 150 sealing discharging valves
160 control device 170 gasify cinder drying equipment
180 expansion control interface 190 local control interfaces
200 controller 210 discharging conveying arrangements
Detailed description of the invention
Below in conjunction with accompanying drawing, detailed description of the invention of the present utility model is described in detail.Should be understood that, detailed description of the invention described herein, only for instruction and explanation of the utility model, is not limited to the utility model.
The olefin hydrocarbon making by coal gasification workshop of usual Coal Chemical Industry produces the gasification cinder in a large number with residual heat value.But, due to these gasification cinders moisture about 50%, cause the mean calorie of gasification cinder more than 2500 kilocalories.Therefore, in order to enable gasification cinder be effectively utilized, the utility model spy provides a kind of gasification cinder drying equipment and system.
Fig. 1 is the structural representation of the gasification cinder drying equipment that the utility model provides.As shown in Figure 1, the gasification cinder drying equipment that the utility model provides comprises: conveying device 10, for carrying described gasification cinder; Hot gas generating apparatus 20, for generation of hot gas; And drying machine 30, for receiving the gasification cinder from described conveying device and the hot gas from described hot gas generating apparatus, to make described gasification cinder fully contact convective heat exchange with described hot gas, thus dry described gasification cinder.By this, dry gasification cinder, thus improve the mean calorie of gasification cinder.
Fig. 2 is the schematic diagram of the detailed description of the invention of the conveying device of the gasification cinder drying equipment that the utility model provides.As shown in Figure 2, described conveying device 10 comprises: belt conveyer 40 and sealing feeder 50.In a particular embodiment, belt conveyer 40 is transported to sealing feeder 50 for the gasification cinder produced in workshop of being gasified by olefin hydrocarbon making by coal and temporarily deposits.Then, gasification cinder is given to drying machine 30 with certain feeding coal by sealing feeder 50.
Fig. 3 is the schematic diagram of the detailed description of the invention of the hot gas generating apparatus of the gasification cinder drying equipment that the utility model provides.As shown in Figure 3, in a particular embodiment, described hot gas generating apparatus 20 comprises: hot-blast stove 60, for producing heat smoke by combustion fuel coal.Preferably, described hot gas generating apparatus also comprises: air blast 70, is installed on described hot-blast stove 60, for cold air is sent into described hot-blast stove; MOD 80, is installed on described air blast 70; And frequency converter 90, be connected with described MOD 80, for controlling by the openings of sizes controlling described MOD the air quantity entering described hot-blast stove as required.By this, appropriate heat smoke can be produced according to actual conditions.
Fig. 4 is the schematic diagram of the detailed description of the invention of the drying machine of the gasification cinder drying equipment that the utility model provides.As shown in Figure 4, in a particular embodiment, preferably, described drying machine 30 comprises: cylindrical shell 3, has fully contacted heat exchange for being shed gasification cinder by the wing plate that stir-fries to make described gasification cinder with described hot gas, thus dry described gasification cinder; Sealing device 1, is installed on the front and back end of described cylindrical shell, enters body for preventing outside cold air and leaks described hot gas; Riding wheel apparatus 2, is installed on the below of the rolling ring of described cylindrical shell, for being played the role of positioning to described cylindrical shell in radial direction by rolling ring, described cylindrical shell is operated reposefully; Transmission device 4, is installed on the below of the bull gear of described cylindrical shell, for driving body to rotate by the bull gear on described cylindrical shell; And gear riding wheel apparatus 5, be installed on the below of the sealing device of described cylinder back-end, for preventing the upper and lower play of body.By this, the drying to gasification cinder can be completed smoothly.
In a particular embodiment, cylindrical shell 3 slant setting of drying machine 30, gradient is generally 3 ~ 5%.The rotating speed of cylindrical shell 3 is about 2 ~ 8 revs/min, and the gasification time of staying of cinder in drying machine 30 is 8 ~ 12 minutes.The drying machine more than 30 that coal industry uses adopts downflow type operation.That is, heat smoke and gasification cinder enter from one end of drying machine, and discharge from the other end of drying machine.In this process, gasification cinder and heat smoke complete the drying to gasification cinder in the mode of convective heat exchange in merging maneuver.Main specifications and the model of drying machine see the following form:
| JNG type cylinder specification | Φ2.4×14m | Φ2.8×16m | Φ3.4×20m | Φ4.2×24m |
| Disposal ability t/h | 20-35 | 35-70 | 70-100 | 120-140 |
| Product moisture/% | 15-25 | 15-25 | 15-25 | 15-25 |
| Evaporation intensity kg/hm 3 | 75-100 | 75-100 | 75-100 | 75-100 |
| The thermal efficiency/% | ＞80 | ＞80 | ＞80 | ＞80 |
| Motor power (output) kw | 45 | 75 | 185 | 250 |
| Complete machine weight t | 43 | 80 | 125 | 220 |
Suitable drying machine is selected in the drying machine specification that coal chemical industry enterprises can go out from upper tabular according to the output of gasification cinder.
As shown in Figure 1, preferably, described equipment also comprises: discharging conveying arrangement 210, is connected with described drying machine 30, for dried gasification cinder is transported to product storing and transporting system.By this, in time dried gasification cinder can be transported out of described drying machine, improve the drying efficiency of drying machine to gasification cinder.
As shown in Figure 1, preferably, described equipment also comprises: particulate retracting device 100, is connected with described drying machine 30, for isolating dust granules from the hot gas after convective heat exchange, and reclaims described dust granules.By this, eliminate the particulate matter in hot gas, thus prevent the hot gas entering air to cause particle contamination to environment.Fig. 5 is the schematic diagram of the detailed description of the invention of the particulate retracting device of the gasification cinder drying equipment that the utility model provides.As shown in Figure 5, in a particular embodiment, described particulate retracting device comprises: cyclone dust collectors 130, for isolating described dust granules from the hot gas after convective heat exchange; Conveying worm 140, for collecting described dust granules; And sealing discharging valve 150, for the dust granules of collection is entered described discharging conveying arrangement.Particularly, the position relationship of these parts in particulate retracting device should be as the criterion with the rational method specifically implemented.Such as, conveying worm 140 can be positioned at the below of the discharging opening of cyclone dust collectors 130, and sealing discharging valve 150 can be positioned at the exit of conveying worm 140.
As shown in Figure 1, preferably, described equipment also comprises: air-introduced machine 110, is connected with described particulate retracting device 100, and being provided for the hot gas after convective heat exchange can enter in air swimmingly.By this, the hot gas after convective heat exchange can be made can to discharge drying machine in time, thus enter particulate retracting device.
As shown in Figure 1, preferably, described equipment also comprises: wet scrubber 120, is connected with described air-introduced machine 110, for the dust in the hot gas by being formed after mist film and/or spraying layer removing convective heat exchange.By this, the dust in hot gas can be removed further, thus ensure that the cleannes of the hot gas entering air.
Fig. 6 is the structural representation of the gasification cinder drying system that the utility model provides.As shown in Figure 6, the gasification cinder drying system that the utility model provides comprises: gasification cinder drying equipment 170; And control device 160, be connected with described gasification cinder drying equipment 170, for controlling described gasification cinder drying equipment.By this, the operation of gasification cinder drying equipment can automatically be controlled.
Fig. 7 is the schematic diagram of the detailed description of the invention of the control device of the gasification cinder drying system that the utility model provides.As shown in Figure 7, in a particular embodiment, preferably, described control device 160 comprises: expansion control interface 180, for receiving remote control commands; Local control interface 190, for sending local control instruction; And controller 200, for according to described remote control commands or local control instruction, control the operation of described gasification cinder drying equipment.By this, can control gasification cinder drying equipment easily.
In a particular embodiment, such as, the on-off model that expansion control interface 180 can receive from DCS control system controls critical pieces such as drying machines, but also the output of 4 ~ 20mA analog signals to gasification cinder drying equipment that can receive from DCS control system carries out step-less adjustment, reaches the optimum performance coupling of whole equipment.Such as, the control instruction that local control interface 190 can receive from import color touch screen controls gasification cinder drying equipment 170.Color touch screen is by the running status of the feedback signal display gasification cinder drying equipment of gasification cinder drying equipment 170.It should be noted that, feedback signal is sent to color touch screen via local control interface 190.Such as, controller 200 can adopt the Programmable Logic Controller of Siemens S7 series, because this controller can be adapted to the middle-size and small-size control system of some complexity.
Fig. 8 is the process chart of the gasification cinder drying equipment that the utility model provides.As shown in Figure 8, the gasification cinder that Coal Chemical Industry olefin hydrocarbon making by coal gasification workshop produces is transported to the sealing feeder 50 of conveying device 10 by the belt conveyer 40 of conveying device 10.Then, gasification cinder is given to drying machine 30 with certain feeding coal by sealing feeder 50.In addition, drying machine 30 also receives the heat smoke that hot-blast stove 60 is produced by combustion fuel coal.Then, drying machine 30 is shed gasification cinder by the wing plate that stir-fries and has fully been contacted heat exchange to make gasification cinder with right flue gas, thus drying, gasifying cinder.Dried gasification cinder is transported to self-owned power plant boiler to carry out burning electricity generation by discharging conveying arrangement 210, and the heat smoke after heat exchange is separated the dust granules of more than 5 ~ 10 μm by particulate retracting device 100.This dust granules is transported to self-owned power plant boiler by discharging conveying arrangement 210 and carries out burning electricity generation together with dried gasification cinder.In this process, air-introduced machine 110 provides power to impel the heat smoke after heat exchange by particulate retracting device 100.In order to the further dedusting of the heat smoke after heat exchange, gasification cinder drying equipment is also provided with wet scrubber 120.This wet scrubber 120 is by forming the dust in the heat smoke after mist film and/or spraying layer removing heat exchange.Afterwards, heat smoke is discharged in air.
In concrete application, coal chemical industry enterprises produces wet gasification cinder 100,000 tons every year, and the price of wet gasification cinder per ton is 0 yuan.Wet gasification cinder is after super-dry, and coal chemical industry enterprises can produce dry gasification cinder 5.88 ten thousand tons, and by the market price with calorific value coal, the price of dry gasification cinder per ton is 200 yuan.Removing drying cost (comprising water rate, steam cost, the wage of electric power and workman and welfare), the annual cost capable of saving fuel 508.7 ten thousand yuan of coal chemical industry enterprises, and Automobile Transportation expense 3,000,000 yuan can be saved.In addition, stacking cost of floor space can also be reduced, extend the service life in stockyard.
The gasification cinder drying equipment that the utility model provides and system, by gasification cinder has fully been contacted convective heat exchange with hot gas, with drying, gasifying cinder, thus make gasification cinder to be effectively utilized.In addition, this gasification cinder drying equipment and system are also equipped with two-stage dust arrester, thus make the dry run very environmental protection of gasification cinder.
Below preferred embodiment of the present utility model is described by reference to the accompanying drawings in detail; but; the utility model is not limited to the detail in above-mentioned embodiment; within the scope of technical conceive of the present utility model; can carry out multiple simple variant to the technical solution of the utility model, these simple variant all belong to protection domain of the present utility model.
It should be noted that in addition, each the concrete technical characteristic described in above-mentioned detailed description of the invention, in reconcilable situation, can be combined by any suitable mode.In order to avoid unnecessary repetition, the utility model illustrates no longer separately to various possible combination.
In addition, also can be combined between various different embodiment of the present utility model, as long as it is without prejudice to thought of the present utility model, it should be considered as content disclosed in the utility model equally.
Claims (11)
1. gasify a cinder drying equipment, and it is characterized in that, described equipment comprises:
Conveying device, for carrying described gasification cinder;
Hot gas generating apparatus, for generation of hot gas; And
Drying machine, for receiving the gasification cinder from described conveying device and the hot gas from described hot gas generating apparatus, to make described gasification cinder fully contact convective heat exchange with described hot gas, thus dry described gasification cinder.
2. gasification cinder drying equipment according to claim 1, is characterized in that, described hot gas generating apparatus comprises:
Hot-blast stove, for producing heat smoke by combustion fuel coal.
3. gasification cinder drying equipment according to claim 2, is characterized in that, described hot gas generating apparatus also comprises:
Air blast, is installed on described hot-blast stove, for cold air is sent into described hot-blast stove;
MOD, is installed on described air blast; And
Frequency converter, is connected with described MOD, for controlling by the openings of sizes controlling described MOD the air quantity entering described hot-blast stove as required.
4. gasification cinder drying equipment according to claim 1, it is characterized in that, described drying machine comprises:
Cylindrical shell, has fully contacted heat exchange to make described gasification cinder with described hot gas for being shed gasification cinder by the wing plate that stir-fries, thus dry described gasification cinder;
Sealing device, is installed on the front and back end of described cylindrical shell, enters body for preventing outside cold air and leaks described hot gas;
Riding wheel apparatus, is installed on the below of the rolling ring of described cylindrical shell, for by rolling ring in radial direction to described
Cylindrical shell plays the role of positioning and described cylindrical shell is operated reposefully;
Transmission device, is installed on the below of the bull gear of described cylindrical shell, large for by described cylindrical shell
Gear ring drives body to rotate; And
Gear riding wheel apparatus, is installed on the below of the sealing device of described cylinder back-end, for preventing body
Lower play.
5. gasification cinder drying equipment according to claim 1, it is characterized in that, described equipment also comprises:
Discharging conveying arrangement, is connected with described drying machine, for dried gasification cinder is transported to product storing and transporting system.
6. gasification cinder drying equipment according to claim 5, it is characterized in that, described equipment also comprises:
Particulate retracting device, is connected with described drying machine, for isolating dust granules from the hot gas after convective heat exchange, and reclaims described dust granules.
7. gasification cinder drying equipment according to claim 6, is characterized in that, described particulate retracting device comprises:
Cyclone dust collectors, for isolating described dust granules from the hot gas after convective heat exchange;
Conveying worm, for collecting described dust granules; And
Sealing discharging valve, for entering described discharging conveying arrangement by the dust granules of collection.
8. gasification cinder drying equipment according to claim 6, it is characterized in that, described equipment also comprises:
Air-introduced machine, is connected with described particulate retracting device, and being provided for the hot gas after convective heat exchange can enter in air swimmingly.
9. gasification cinder drying equipment according to claim 8, it is characterized in that, described equipment also comprises:
Wet scrubber, is connected with described air-introduced machine, for the dust in the hot gas by being formed after mist film and/or spraying layer removing convective heat exchange.
10. gasify a cinder drying system, and it is characterized in that, described system comprises:
Gasification cinder drying equipment any one of claim 1-9 described in claim; And
Control device, is connected with described gasification cinder drying equipment, for controlling described gasification cinder drying equipment.
11. gasification cinder drying systems according to claim 10, it is characterized in that, described control device comprises:
Expansion control interface, for receiving remote control commands;
Local control interface, for receiving local control instruction; And
Controller, for according to described remote control commands or local control instruction, controls the operation of described gasification cinder drying equipment.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520269133.9U CN204854246U (en) | 2015-04-29 | 2015-04-29 | Gasification cinder drying equipment and system |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520269133.9U CN204854246U (en) | 2015-04-29 | 2015-04-29 | Gasification cinder drying equipment and system |
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| CN204854246U true CN204854246U (en) | 2015-12-09 |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104833189A (en) * | 2015-04-29 | 2015-08-12 | 神华集团有限责任公司 | Gasification coal cinder drying equipment and system |
| CN110283630A (en) * | 2019-07-27 | 2019-09-27 | 河南心连心化学工业集团股份有限公司 | A kind of coal chemical industry fixed-end forces device and processing method |
| CN110553495A (en) * | 2019-09-24 | 2019-12-10 | 河南心连心化学工业集团股份有限公司 | energy-saving and environment-friendly coal gasification solid waste treatment device and treatment method |
-
2015
- 2015-04-29 CN CN201520269133.9U patent/CN204854246U/en active Active
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104833189A (en) * | 2015-04-29 | 2015-08-12 | 神华集团有限责任公司 | Gasification coal cinder drying equipment and system |
| CN110283630A (en) * | 2019-07-27 | 2019-09-27 | 河南心连心化学工业集团股份有限公司 | A kind of coal chemical industry fixed-end forces device and processing method |
| CN110553495A (en) * | 2019-09-24 | 2019-12-10 | 河南心连心化学工业集团股份有限公司 | energy-saving and environment-friendly coal gasification solid waste treatment device and treatment method |
| CN110553495B (en) * | 2019-09-24 | 2023-11-21 | 河南心连心化学工业集团股份有限公司 | Energy-saving and environment-friendly coal gasification solid waste treatment device and treatment method |
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