CN205773374U - Energy saving and environment friendly Carbon bisulfide gasification reacting furnace - Google Patents
Energy saving and environment friendly Carbon bisulfide gasification reacting furnace Download PDFInfo
- Publication number
- CN205773374U CN205773374U CN201620626245.XU CN201620626245U CN205773374U CN 205773374 U CN205773374 U CN 205773374U CN 201620626245 U CN201620626245 U CN 201620626245U CN 205773374 U CN205773374 U CN 205773374U
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- China
- Prior art keywords
- gasification
- furnace
- carbon bisulfide
- reacting furnace
- heater
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/10—Process efficiency
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- Gasification And Melting Of Waste (AREA)
Abstract
This utility model belongs to coke method carbon disulphide production equipment technology field, high in order to solve the external heating mode energy consumption with the presence of coke method Carbon bisulfide gasification reacting furnace furnace rear, environment is polluted in waste gas discharge more, produce impacted and floor space is big, furnace fireproofing material consumes the defects such as many, this utility model provides a kind of energy saving and environment friendly Carbon bisulfide gasification reacting furnace, including being located at the interior and connected body of heater of same closed chamber and sulfur gasification port, body of heater top is provided with Carbon bisulfide recovery channel, front discharge flue and rear discharge flue it is arranged with on the front wall of described closed chamber and rear wall, the bottom of body of heater is provided with externally heated oven.This utility model is by being symmetrical arranged discharge flue before and after gasification furnace on wall, externally heated oven is located at the bottom of gasification furnace simultaneously, there is energy consumption height in the furnace rear external heating mode efficiently solving existing coke method Carbon bisulfide gasification reacting furnace, pollute big, floor space is big, and furnace fireproofing material consumes the defect problem of grade more.
Description
Technical field
This utility model belongs to coke method carbon disulphide production equipment technology field, is specifically related to a kind of energy saving and environment friendly two
Nitric sulfid gasification reacting furnace.
Background technology
Existing coke method produces Carbon bisulfide gasification reacting furnace and all uses the mode of external heat after gasification reaction furnace body, i.e.
At the externally heated oven disposed behind of gasification reaction body of heater, the heat of externally heated oven reaches gasification reaction after reacting furnace body of heater
The periphery of body of heater, when making gasification reacting furnace body temperature be heated to 800-900 DEG C, in stove, coke and sulfur react generation two
Nitric sulfid product.The mode of this gasification reacting furnace furnace rear external heat, is primarily present externally heated oven to gasification reaction body of heater heat supply
Distance, external heat body of heater and quirk heat absorption are many, and fuel consumption is many, waste the energy, and owing to the fuel of current externally heated oven is equal
For raw coal or coke, the waste gas such as CO2 and CO that a part of raw coal of many burnings or coke produce and SO2 must be in air
Discharge, brings certain environmental pollution.Discharge secondly because be only provided with flue gas at Qiang Shang angle, gasification reacting furnace stokehold
Passage, on gasification reaction furnace rear wall there is thermal current dead angle in angle and front wall inferior horn, and the most each position uneven heating is even, especially often
The performance of secondary blowing-in operation initial stage is substantially so that the gasification reacting furnace blow-on initial stage can not comparatively fast obtain normal production target, and impact is produced
Amount.Three be gasification reacting furnace external heat table to build floor space by laying bricks or stones relatively big, furnace fireproofing material consumes many.
In sum, it is high to there is energy consumption in the furnace rear external heating mode of existing coke method Carbon bisulfide gasification reacting furnace, waste gas
Environment is polluted in discharge more, produces impacted and floor space big, and furnace fireproofing material consumes the defects such as many.
Summary of the invention
This utility model is in order to solve the external heating mode energy consumption with the presence of coke method Carbon bisulfide gasification reacting furnace furnace rear
Height, waste gas discharges and pollutes environment more, produces impacted and floor space big, and furnace fireproofing material consumes the defects such as many, it is provided that
A kind of energy saving and environment friendly Carbon bisulfide gasification reacting furnace.
This utility model adopts the following technical scheme that
A kind of energy saving and environment friendly Carbon bisulfide gasification reacting furnace, including being located at the interior and connected body of heater of same closed chamber and sulfur
Sulphur gasification port, body of heater top is provided with Carbon bisulfide recovery channel, and the front wall of described closed chamber and rear wall are arranged with front row
Cigarette channel and rear discharge flue, the bottom of body of heater is provided with externally heated oven.
Being provided with fire bars in described externally heated oven, it is corresponding through that the sidewall of externally heated oven is provided with the epicoele with fire bars, cavity of resorption
Fuel add entrance, slag removal mouth.
Described fuel adds porch and is provided with and is automatically added to fuel-device, is provided with and automatically unloads slag device at slag removal mouth；
Described fire bars is automatic rotary grate device, logical including drivewheel, support, rotary fire grate and driven pulley, drivewheel and driven pulley
Crossing support to be connected to one, rotary fire grate is arranged around drivewheel, support and driven pulley；The described fuel that is automatically added to fills
It is arranged in the oblique upper of the stroke feeding end of rotary fire grate, automatically unloads slag device and be located at stroke discharging end oblique of rotary fire grate
Lower section.
Described body of heater, externally heated oven, rear discharge flue, front discharge flue, sulfur gasification port and automatic rotary grate dress
High temperature resistant 1000-1200 DEG C of high-alumina brick is all used to build connection by laying bricks or stones between putting.
Described externally heated oven is heated by gas device, is provided with gas piping in externally heated oven, and gas piping is provided with some
Coal spraying jet.
Described gas piping uses seamless steel pipe.
Between described body of heater, externally heated oven, rear discharge flue, front discharge flue, sulfur gasification port and gas piping all
High temperature resistant 1000-1200 DEG C of high-alumina brick is used to build connection by laying bricks or stones.
This utility model is the mode of external heat after existing gasification reaction furnace body to be improved to bottom gasification reaction body of heater
The mode of external heat, will be arranged on the bottom of Carbon bisulfide gasification reaction body of heater by externally heated oven, and at gasification reaction body of heater
On rear wall, angle increase arranges a flue gas passing away.So arrange, compare existing externally heated oven and be arranged on Carbon bisulfide gas
Changing after reacting furnace-e/or, have floor space little, furnace fireproofing material consumption is few, and fuel consumption is few, and pre-heating temperature elevation is fast etc.
Advantage.
The above gasification reaction body of heater, externally heated oven, angle flue gas passing away, gasification reaction on gasification reaction furnace rear wall
Qiang Shang angle, stokehold flue gas passing away, sulfur gasification port all uses high temperature resistant 1000-1200 DEG C of high-alumina brick to build connection by laying bricks or stones.
The mode of external heat after existing gasification reaction furnace body is improved to the mode of external heat bottom gasification reaction body of heater,
Also help increasing gasification reaction furnace body capacity, improve yield.
As further improvement of the utility model, arrange in the externally heated oven burner hearth arranged bottom gasification reaction body of heater
Machine automatization adds fuel and automatically unloads slag facility, including being automatically added to fuel-device, automatic rotary grate device, unloads automatically
Slag device, automatic rotary grate device is horizontally set on bottom external heat furnace chamber, is automatically added to fuel-device against external heat
Furnace rear wall is arranged on automatic rotary grate device side, automatically unloads slag device and is arranged on rotation automatically against externally heated oven front wall
Fire grate device opposite side.It is automatically added to fuel-device and automatically unloads slag device company fixing with automatic rotary grate device respectively
Connecing, preferably electric welding connects.Described automatic rotary grate device, including drivewheel, driven pulley, rotary fire grate, support, drivewheel is tight
Outer heating furnace front wall is arranged on front wall root, and driven pulley wall after externally heated oven is arranged on rear the foot of a wall portion, drivewheel and from
Driving wheel is connected to one by support, and rotary fire grate is arranged around drivewheel, support, driven pulley periphery.
Described gasification reaction body of heater, externally heated oven, angle flue gas passing away, gasification reaction stokehold on gasification reaction furnace rear wall
Flue gas passing away in angle on wall, sulfur gasification port, automatic rotary grate device all uses high temperature resistant 1000-1200 DEG C of high-alumina brick
Build connection by laying bricks or stones.
Arrange machine automatization add fuel and automatically unload slag facility and be conducive to alleviating artificial interpolation fuel and removing slag
Physical work, be advantageously implemented the on-line automatic control of externally heated oven, stablize furnace temperature, it is achieved stable normal produce.
Further improve as of the present utility model, be not provided with charge door, fire bars in described externally heated oven furnace chamber, come out of the stove
Cinder notch, is also not provided with machine automatization charging and deslagging device, and bunker coal heating is changed into heated by gas, and coal gas is occurred by coal gas
Stove provides, and arranges gas piping, control valve for coal gas, coal spraying jet at furnace chamber bottom even, and control valve for coal gas is arranged on heating-furnace
After bottom chamber outside wall on gas piping, control valve for coal gas is fixing with gas piping employing flange gasket to be connected；Coal spraying jet sets
Putting on the gas piping of heating-furnace intracavity outside, coal spraying jet and gas piping use electric welding to be connected to one.
Heated by gas is changed in bunker coal heating, changes externally heated oven furnace cavity structure simultaneously, be more beneficial for alleviating manually
Add fuel and the physical work of removing slag, quick adjusting furnace temperature, improve working environment, be more beneficial for realizing externally heated oven and exist
Line automatically controls, and stablizes furnace temperature, it is achieved high and stable yields.
This utility model can effectively solve the furnace rear external heating mode of existing coke method Carbon bisulfide gasification reacting furnace and exist
Energy consumption is high, and environment is polluted in waste gas discharge more, produces impacted and floor space big, the defects such as furnace fireproofing material consumption is many
Technical problem.
Reasonable in design of the present utility model is reliable, can save the energy, reduces and pollutes, and improves yield, can save again
Furnace building material, reduces brickwork cost, reduces body of heater area occupied, is remarkably improved business economic and environmental benefit.
Accompanying drawing explanation
Fig. 1 is the vertical elevational schematic view of existing furnace rear external heating type Carbon bisulfide gasification reacting furnace；
Fig. 2 is the vertical elevational schematic view (embodiment 1) of this utility model furnace bottom heated type Carbon bisulfide gasification reacting furnace；
Fig. 3 is that the vertical facade being provided with the Carbon bisulfide gasification reacting furnace that machine automatization addition fuel unloads slag facility automatically shows
It is intended to (embodiment 2)；
Fig. 4 is the vertical elevational schematic view that bottom is provided with the Carbon bisulfide gasification reacting furnace of externally heated oven heated by gas furnace chamber
(embodiment 3)；
In figure: 1-body of heater, 2-externally heated oven, 3-fuel add discharge flue after entrance, 4-fire bars, 5-slag removal mouth, 6-,
Before 7-Carbon bisulfide recovery channel, 8-, discharge flue, 9-sulfur gasification port, 10-are automatically added to fuel-device, 11-automatic rotary
Converter arranging device, 12-unload slag device, 13-drivewheel, 14-support, 15-rotary fire grate, 16-driven pulley, 17-coal gas automatically
Pipeline, 18-control valve for coal gas, 19-coal spraying jet.
Detailed description of the invention
In conjunction with accompanying drawing, detailed description of the invention of the present utility model is described further:
Embodiment 1,
Energy saving and environment friendly Carbon bisulfide gasification reacting furnace as shown in Figure 2, including gasification reaction body of heater 1, externally heated oven 2,
Angle flue gas passing away 6 on gasification reaction furnace rear wall, Carbon bisulfide recovery channel, 7, on gasification reacting furnace front wall, angle flue gas is discharged
Passage 8, sulfur gasification port 9, described externally heated oven 2 includes that fuel adds entrance 3, fire bars 4, slag removal mouth 5, described curing
Carbon recovery channel 7 is arranged on that gasification reaction body of heater 1 top and gasification reacting furnace are fixing to be connected.Described gasification reaction body of heater 1, additional
Hot stove 2, angle flue gas passing away 6 on gasification reaction furnace rear wall, angle flue gas passing away 8, sulfury on gasification reacting furnace front wall
Changing port 9 all uses high temperature resistant 1000-1200 DEG C of high-alumina brick to build connection by laying bricks or stones.
Embodiment 2
Energy saving and environment friendly Carbon bisulfide gasification reacting furnace as shown in Figure 3, including gasification reaction body of heater 1, externally heated oven 2,
Angle flue gas passing away 6 on gasification reaction furnace rear wall, Carbon bisulfide recovery channel 7, on gasification reacting furnace front wall, angle flue gas is discharged
Passage 8, sulfur gasification port 9, described Carbon bisulfide recovery channel 7 is arranged on gasification reaction body of heater 1 top and gasification reacting furnace
Fixing connection.Arrange machine automatization in described externally heated oven 2 furnace chamber add fuel and be automatically drained out slag facility, including automatically adding
Entering fuel-device 10, automatic rotary grate device 11, automatically unload slag device 12, automatic rotary grate device 11 is horizontally set on
Bottom external heat furnace chamber, it is automatically added to fuel-device 10 wall after externally heated oven and is arranged on automatic rotary grate device 11 1
Side, automatically unloads slag device 12 and is arranged on automatic rotary grate device 11 opposite side against externally heated oven front wall.It is automatically added to combustion
Material device 10 and automatically unload that slag device 12 is fixing with automatic rotary grate device 11 respectively to be connected, preferably electric welding connection.Described
Automatic rotary grate device 11, including drivewheel 13, support 14, rotary fire grate 15, driven pulley 16, drivewheel 13 is against external heat
Stokehold wall is arranged on front wall root, and driven pulley 16 wall after externally heated oven is arranged on rear the foot of a wall portion, drivewheel 13 and driven pulley
16 are connected to one by support 14, and rotary fire grate 15 is arranged around drivewheel, support, driven pulley periphery.
Embodiment 3
Energy saving and environment friendly Carbon bisulfide gasification reacting furnace as shown in Figure 4, including gasification reaction body of heater 1, externally heated oven 2,
Angle flue gas passing away 6 on gasification reaction furnace rear wall, Carbon bisulfide recovery channel 7, on gasification reacting furnace front wall, angle flue gas is discharged
Passage 8, sulfur gasification port 9, described Carbon bisulfide recovery channel 7 is arranged on gasification reaction body of heater 1 top and gasification reacting furnace
Fixing connection.Described externally heated oven 2 furnace chamber bottom even arranges gas piping 17, control valve for coal gas 18, coal spraying jet 19, coal gas control
Valve 18 processed be arranged on bottom heating stove furnace chamber after outside wall on gas piping 17, control valve for coal gas 19 and gas piping 17 use method
Blue sealing gasket is fixing to be connected；Coal spraying jet 19 is arranged on the gas piping 17 in externally heated oven furnace chamber, coal spraying jet 19 and gas pipe
Road 17 uses electric welding to be connected to one.
Described gasification reaction body of heater 1, externally heated oven 2, angle flue gas passing away 6, gasification reaction on gasification reaction furnace rear wall
Qiang Shang angle, stokehold flue gas passing away 8, sulfur gasification port 9, gas piping 17 all uses high temperature resistant 1000-1200 DEG C of high-alumina brick
Build connection by laying bricks or stones.
In addition to the externally heated oven chamber structure that this utility model gasification reacting furnace bottom of furnace body external heating mode is given, additional
The burner hearth of hot body of heater can also have other distressed structures or different because adding the structure of fuel difference burner hearth, all these stoves
The malformation of thorax belongs to protection domain of the present utility model.
The component not making specified otherwise in this utility model is prior art.
Claims (7)
1. an energy saving and environment friendly Carbon bisulfide gasification reacting furnace, including the body of heater (1) being located in same closed chamber and be connected and
Sulfur gasification port (9), body of heater (1) top is provided with Carbon bisulfide recovery channel (7), it is characterised in that: before described closed chamber
Being arranged with front discharge flue (8) and rear discharge flue (6) on wall and rear wall, the bottom of body of heater (1) is provided with externally heated oven (2).
Energy saving and environment friendly Carbon bisulfide gasification reacting furnace the most according to claim 1, it is characterised in that: described externally heated oven
(2) being provided with fire bars (4) in, the sidewall of externally heated oven (2) is provided with and adds with the epicoele of fire bars (4), the corresponding through fuel of cavity of resorption
Entrance (3), slag removal mouth (5).
Energy saving and environment friendly Carbon bisulfide gasification reacting furnace the most according to claim 2, it is characterised in that: described fuel adds
Mouth (3) place is provided with and is automatically added to fuel-device (10), and slag removal mouth (5) place is provided with unloads slag device (12) automatically；Described stove
Bar (4) is automatic rotary grate device (11), including drivewheel (13), support (14), rotary fire grate (15) and driven pulley (16),
Drivewheel (13) and driven pulley (16) are connected to one by support (14), rotary fire grate (15) around drivewheel (13),
Support (14) and driven pulley (16) are arranged；The described fuel-device (10) that is automatically added to is located at the stroke feeding of rotary fire grate (15)
The oblique upper of end, unloads the obliquely downward that slag device (12) is located at the stroke discharging end of rotary fire grate (15) automatically.
Energy saving and environment friendly Carbon bisulfide gasification reacting furnace the most according to claim 3, it is characterised in that: described body of heater (1),
Externally heated oven (2), rear discharge flue (6), front discharge flue (8), sulfur gasification port (9) and automatic rotary grate device (11)
Between all use high temperature resistant 1000-1200 DEG C of high-alumina brick to build connection by laying bricks or stones.
Energy saving and environment friendly Carbon bisulfide gasification reacting furnace the most according to claim 1, it is characterised in that: described externally heated oven
(2) being heated by gas device, be provided with gas piping (17) in externally heated oven (2), gas piping (17) is provided with some coal spraying jets
(19).
Energy saving and environment friendly Carbon bisulfide gasification reacting furnace the most according to claim 5, it is characterised in that: described gas piping
(17) seamless steel pipe is used.
Energy saving and environment friendly Carbon bisulfide gasification reacting furnace the most according to claim 6, it is characterised in that: described body of heater (1),
All adopt between externally heated oven (2), rear discharge flue (6), front discharge flue (8), sulfur gasification port (9) and gas piping (17)
Connection is built by laying bricks or stones with high temperature resistant 1000-1200 DEG C of high-alumina brick.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2016202893725 | 2016-04-11 | ||
| CN201620289372 | 2016-04-11 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205773374U true CN205773374U (en) | 2016-12-07 |
Family
ID=58130283
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620626245.XU Withdrawn - After Issue CN205773374U (en) | 2016-04-11 | 2016-06-23 | Energy saving and environment friendly Carbon bisulfide gasification reacting furnace |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205773374U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105948048A (en) * | 2016-04-11 | 2016-09-21 | 阳城县绿色铸造研发中心 | Energy-saving environment-friendly carbon bisulfide gasification reaction furnace |
| CN107298443A (en) * | 2017-07-28 | 2017-10-27 | 阳城县绿色铸造研发中心 | Carbon disulfide gasification reacting furnace sulphur feeding device |
-
2016
- 2016-06-23 CN CN201620626245.XU patent/CN205773374U/en not_active Withdrawn - After Issue
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105948048A (en) * | 2016-04-11 | 2016-09-21 | 阳城县绿色铸造研发中心 | Energy-saving environment-friendly carbon bisulfide gasification reaction furnace |
| CN107298443A (en) * | 2017-07-28 | 2017-10-27 | 阳城县绿色铸造研发中心 | Carbon disulfide gasification reacting furnace sulphur feeding device |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| AV01 | Patent right actively abandoned |
Granted publication date: 20161207 Effective date of abandoning: 20171226 |