CN207298971U - Powdered activated carbon drying and incineration treatment system - Google Patents
Powdered activated carbon drying and incineration treatment system Download PDFInfo
- Publication number
- CN207298971U CN207298971U CN201720868275.6U CN201720868275U CN207298971U CN 207298971 U CN207298971 U CN 207298971U CN 201720868275 U CN201720868275 U CN 201720868275U CN 207298971 U CN207298971 U CN 207298971U
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- Prior art keywords
- heat
- natural gas
- furnace
- waste
- oil furnace
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- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 title claims abstract description 26
- 238000001035 drying Methods 0.000 title abstract description 3
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 claims abstract description 48
- 239000003345 natural gas Substances 0.000 claims abstract description 24
- 229910052799 carbon Inorganic materials 0.000 claims abstract description 14
- 239000002918 waste heat Substances 0.000 claims abstract description 14
- 238000012545 processing Methods 0.000 claims description 11
- 239000002912 waste gas Substances 0.000 claims description 7
- 238000010438 heat treatment Methods 0.000 claims description 5
- 230000008676 import Effects 0.000 claims description 3
- 238000002485 combustion reaction Methods 0.000 abstract description 9
- 230000008901 benefit Effects 0.000 abstract description 7
- 239000007789 gas Substances 0.000 abstract description 5
- 239000003245 coal Substances 0.000 abstract description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 4
- 239000002699 waste material Substances 0.000 abstract description 3
- 239000002351 wastewater Substances 0.000 abstract description 3
- 239000003921 oil Substances 0.000 abstract 9
- 239000010724 circulating oil Substances 0.000 abstract 2
- 239000002002 slurry Substances 0.000 abstract 2
- 239000003250 coal slurry Substances 0.000 description 7
- RAHZWNYVWXNFOC-UHFFFAOYSA-N Sulphur dioxide Chemical compound O=S=O RAHZWNYVWXNFOC-UHFFFAOYSA-N 0.000 description 4
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 1
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- 230000004913 activation Effects 0.000 description 1
- 229910003481 amorphous carbon Inorganic materials 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000002283 diesel fuel Substances 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 239000003546 flue gas Substances 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 230000036541 health Effects 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 230000001788 irregular Effects 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000011017 operating method Methods 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 210000002345 respiratory system Anatomy 0.000 description 1
Landscapes
- Combustion Of Fluid Fuel (AREA)
Abstract
The utility model relates to a powdery active carbon drying and burning treatment system, which comprises a natural gas combustion system, a heat conducting oil furnace system, a tail gas utilization system and an air outlet system; the natural gas combustion system comprises an air blower, a combustor and a natural gas pipeline, wherein the air blower is communicated with the combustor through a flue A, and the upper end of the combustor is also communicated with the natural gas pipeline; the heat conduction oil furnace system comprises a heat conduction oil furnace and a circulating oil pump, the heat conduction oil furnace is communicated with the burner, and the heat conduction oil furnace is also communicated with the circulating oil pump through a pipeline; the tail gas utilization system comprises a waste heat furnace, and the waste heat furnace is communicated with the heat-conducting oil furnace through a flue B; the air outlet system comprises an induced draft fan and a chimney, the inlet of the induced draft fan is communicated with the waste heat furnace through a flue C, and the outlet of the induced draft fan is communicated with the chimney through a pipeline D. The utility model has the advantages that: the coal water slurry heat-conducting oil furnace is changed into a natural gas oil furnace system, so that the ignition is convenient, no waste residue or waste water is generated after combustion, and the coal water slurry heat-conducting oil furnace has the advantages of safety in use, high heat value, cleanness and the like.
Description
Technical field
The utility model belongs to clean energy technology field, is related to a kind of clean energy resource processing system, more particularly to a kind of
Powdered active carbon dries burning processing system.
Background technology
Activated carbon is black powder or granular amorphous carbon.Activated carbon principal component is also aerobic in addition to carbon, hydrogen
Deng element.Activated carbon, since microcrystalline carbon is irregular alignment, there is pore in structure between interconnection, can be produced in activation
Raw carbon tissue defects, therefore it is a kind of porous carbon, bulk density is low, and specific surface area is big.
With industrial expansion, the application of activated carbon is more and more wider, the increase of demand, to the processing side after activated carbon use
Method also produces accordingly；It can be reused after producer's reclaiming of way general at present, it is general during reclaiming
Burnt by water-coal slurry furnace, and water-coal slurry furnace because fuel be water-coal-slurry, water-coal slurry furnace is to operator's each side energy
Power requires height, to maintenance mans' skill set requirements height, and heavy workload, attrition component are more, and spare parts cost is high；And water-coal-slurry essence is still
Coal, the content of sulfur dioxide produced after burning is still very high, and dust content is high in tail gas, is very easy to block convection current
Section, influences the heat exchange of conduction oil and the outlet air of boiler；And it is more demanding to have to carry out preheating using diesel oil to go forward side by side to put stove
Row companion is burnt to complete smooth combustion, uneconomical.
Utility model content
The utility model aims to provide a kind of powdered active carbon drying burning processing system, by changing water-coal-slurry conduction oil
Stove is natural gas oil oven system, has that igniting is convenient, while is produced after burning without waste residue, waste water, has that safe to use, calorific value is high
And the advantage such as cleaning.
The technical solution of the utility model is：A kind of powdered active carbon dries burning processing system, its innovative point is：
Including natural gas burning system, thermal oil heating piping system, waste gas utilization system and outlet system of air；
The natural gas burning system includes air blower, burner and natural gas line, the air blower by flue A with
Burner connects, and the upper end of burner is also connected with natural gas line；
The thermal oil heating piping system includes heat-conducting oil furnace and oil circulating pump, and the heat-conducting oil furnace is connected with burner, and is led
Hot oil furnace also connects oil circulating pump by pipeline；
The waste gas utilization system includes waste-heat oven, and the waste-heat oven is connected by flue B with heat-conducting oil furnace；
The outlet system of air includes air-introduced machine and chimney, and the import of the air-introduced machine is connected with waste-heat oven by flue C, drawn
The outlet of wind turbine is connected by pipeline D with chimney.
The utility model has the advantage of：The utility model powdered active carbon dries burning processing system, changes original water
Coal slurry heat-conducting oil furnace is natural gas oil oven system, and what natural gas produced in combustion can influence human respiratory system's health
Material is few, and the carbon dioxide of generation is only 40% of coal or so, and the sulfur dioxide of generation is also seldom, and nothing after combustion of natural gas
Waste residue, waste water produce, and have that safe to use, calorific value is high, the advantage such as clean；Meanwhile in this way, also there is igniting conveniently
Efficiently advantage.
Brief description of the drawings
The utility model is described in further detail with reference to the accompanying drawings and detailed description.
Fig. 1 is the structure diagram that the utility model powdered active carbon dries burning processing system.
Embodiment
The following examples can make professional and technical personnel that the utility model be more fully understood, but therefore will not
The utility model is limited among the embodiment described scope.
Embodiment
The present embodiment powdered active carbon dries burning processing system, as shown in Figure 1, including natural gas burning system, leading
Deep fat furnace system, waste gas utilization system and outlet system of air；Natural gas burning system includes air blower 1, burner 2 and natural gas tube
Road 3, air blower 1 is connected by flue A with burner 2, and the upper end of burner 2 is also connected with natural gas line 3.
Thermal oil heating piping system includes heat-conducting oil furnace 4 and oil circulating pump 5, and heat-conducting oil furnace 4 is connected with burner 2, and conduction oil
Stove 4 also connects oil circulating pump 5 by pipeline.
Waste gas utilization system includes waste-heat oven 6, and waste-heat oven 6 is connected by flue B with heat-conducting oil furnace 4.
Outlet system of air includes air-introduced machine 7 and chimney 8, and the import of air-introduced machine 7 is connected by flue C with waste-heat oven 6, air-introduced machine
7 outlet is connected by pipeline D with chimney 8.
In embodiment, air blower 1 act as burner 2 and provides oxygen in combustion system, and day feed channel 3 is act as to burning
Device 2 provides natural gas, and oil circulating pump 5 act as to be flowed to deep fat in thermal oil heating piping system；Heat-conducting oil furnace 4 act as to
Burner 2 provides combustion space and conduction oil is heated；In waste gas utilization system waste heat boiler 6 act as using tail gas into
Row cooling and output steam；The tail gas that air-introduced machine 7 act as to produce in burner hearth in outlet system of air is moved in chimney 8 and discharged.
The present embodiment powdered active carbon dries the operating procedure of burning processing system, as follows：
1st, all components are checked, it is ensured that all components can normal operation, water level is normal in waste heat boiler 6；
2nd, ON cycle oil pump 5, makes conduction oil reach the flow of needs；
3rd, open before detecting valve before the valve in day feed channel 3 send natural gas to burner 2, and regulate natural gas
Pressure；
4 open air-introduced machines 7, open burner 2, during air blower 1 can be opened by program designation, combustion chamber draft carries out a little
Fire；
5th, after the success of burner normal ignition, the frequency for adjusting air blower 7 and air-introduced machine 8 ensures that burner hearth is in negative pressure state；
6th, pay attention to the flue gas that observation chimney 8 is discharged, and adjusted accordingly.
The advantages of basic principle and main feature and the utility model of the utility model has been shown and described above.This
The technical staff of industry is retouched in above embodiments and description it should be appreciated that the present utility model is not limited to the above embodiments
That states simply illustrates the principle of the utility model, on the premise of not departing from the spirit and scope of the utility model, the utility model
Various changes and modifications are also had, these various changes and improvements fall within the scope of the claimed invention.This practicality is new
Type is claimed scope and is defined by the appending claims and its equivalent thereof.
Claims (1)
1. a kind of powdered active carbon dries burning processing system, it is characterised in that：Including natural gas burning system, heat-conducting oil furnace
System, waste gas utilization system and outlet system of air；
The natural gas burning system includes air blower, burner and natural gas line, and the air blower passes through flue A and burning
Device connects, and the upper end of burner is also connected with natural gas line；
The thermal oil heating piping system includes heat-conducting oil furnace and oil circulating pump, and the heat-conducting oil furnace is connected with burner, and conduction oil
Stove also connects oil circulating pump by pipeline；
The waste gas utilization system includes waste-heat oven, and the waste-heat oven is connected by flue B with heat-conducting oil furnace；
The outlet system of air includes air-introduced machine and chimney, and the import of the air-introduced machine is connected by flue C with waste-heat oven, air-introduced machine
Outlet connected by pipeline D with chimney.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720868275.6U CN207298971U (en) | 2017-07-18 | 2017-07-18 | Powdered activated carbon drying and incineration treatment system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720868275.6U CN207298971U (en) | 2017-07-18 | 2017-07-18 | Powdered activated carbon drying and incineration treatment system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207298971U true CN207298971U (en) | 2018-05-01 |
Family
ID=62450763
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720868275.6U Active CN207298971U (en) | 2017-07-18 | 2017-07-18 | Powdered activated carbon drying and incineration treatment system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN207298971U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111503647A (en) * | 2020-04-10 | 2020-08-07 | 中国船舶重工集团公司第七一八研究所 | Negative pressure ignition and combustion system and method for using negative pressure ignition and stable combustion of system |
-
2017
- 2017-07-18 CN CN201720868275.6U patent/CN207298971U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111503647A (en) * | 2020-04-10 | 2020-08-07 | 中国船舶重工集团公司第七一八研究所 | Negative pressure ignition and combustion system and method for using negative pressure ignition and stable combustion of system |
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| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CP03 | Change of name, title or address | ||
| CP03 | Change of name, title or address |
Address after: 226200 Changjiang Town, Rugao City, Rugao, Nantong, Jiangsu, No. 6, Xiangjiang Road Co-patentee after: Jiangsu hundred Sichuan high science and technology new materials Limited by Share Ltd Patentee after: Nantong hundred Sichuan new materials Co., Ltd. Co-patentee after: Rugao ran chemical materials Co., Ltd. Address before: 226500 Changjiang Town, Rugao City, Rugao, Nantong, Jiangsu, No. 6, Xiangjiang Road Co-patentee before: Wuxi Baichuan Chemical Industrial Co., Ltd. Patentee before: Baichuan Chemical (Rugao) Co., Ltd. Co-patentee before: Rugao ran chemical materials Co., Ltd. |