CN205974420U - Smokeless carbonization system of straw - Google Patents
Smokeless carbonization system of straw Download PDFInfo
- Publication number
- CN205974420U CN205974420U CN201620878549.5U CN201620878549U CN205974420U CN 205974420 U CN205974420 U CN 205974420U CN 201620878549 U CN201620878549 U CN 201620878549U CN 205974420 U CN205974420 U CN 205974420U
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- Prior art keywords
- pipeline
- spray column
- carbonization
- gas
- liquid separation
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Abstract
The utility model discloses a smokeless carbonization system of straw, including gasifier, spray column I, spray column II, air cooler, fan, oil water separator, gas -liquid separation tower, feed screw conveyer belt, host computer, ejection of compact auger delivery area, the gasifier passes through the pipeline and is connected with spray column I, spray column I is connected with spray column II through the pipeline, spray column II is connected with the air cooler through the pipeline, the air cooler passes through the pipeline and is connected with the fan, the fan passes through the pipeline and is connected with oil water separator, oil water separator passes through the pipeline and is connected with the gas -liquid separation tower, the gas outlet is passed through the pipeline and is connected with spray column I, the air inlet passes through the pipeline and is connected with the gas -liquid separation tower, the discharge gate is taken with one side ejection of compact auger delivery and is connected. The utility model discloses the system automation degree is high, and the raw materials is heated evenly, and the carbomorphism rate is high, and the energy resource consumption is little, and the combustion gas is the dust -laden not, pollutes for a short time.
Description
Technical field
This utility model belongs to straw-carbonized field of mechanical technique, particularly to a kind of smokeless carbonization system of straw.
Background technology
What biomass carbonization technology was well recognized as solves the problems, such as one of possible technique measure of climate change, has raw material
Source extensively, low production cost, ecological safety, pollution-free the features such as；And the biomass resource very abundant of China, distribution is wide,
Sustainable supply, therefore can spread biomass carbonization technology；
Traditional charcoal processing technique is nearly all using native formula kiln, and different operations are responsible for by each kiln, and centre is by artificial
Raw material is shifted by the mode of carrying, and retort is mostly fixed, and raw material is heated uneven, and carbonization degree is low, its yield and
Quality is all difficult to be protected；In addition traditional charcoal processing technique is all to provide thermal source using special fuel, and energy-output ratio is big, row
The dust content going out is big, does not meet the requirements of the times of current energy-conserving and environment-protective.
Content of the invention
The purpose of this utility model is to overcome deficiency in prior art, provides a kind of straw smokeless carbonization system, and system is certainly
Dynamicization degree is high, and raw material is heated evenly, and carbonization degree is high, and energy resource consumption is little, expellant gas not dust-laden, and pollution is little.
To achieve these goals, the technical solution adopted in the utility model is：
A kind of smokeless carbonization system of straw, including gasification furnace, spray column I, spray column II, air cooler, blower fan, oil-water separation
Device, gas-liquid separation tower, feed auger conveyer belt, main frame, discharging spiral conveyor；Described gasification furnace passes through pipeline and spray column I
Connect, pipeline is provided with valve；Described spray column I is connected with spray column II by pipeline, described spray column II pass through pipeline with
Air cooler connects, and described air cooler is connected with blower fan by pipeline, and pipeline is provided with valve, described blower and pipeline and profit
Separator connects, and described oil water separator is connected with gas-liquid separation tower by pipeline；Described main frame includes motor, charging aperture, charcoal
Change cylinder, steam vent, gas outlet, carbonization case, cooler bin, main shaft, air inlet, discharging opening, lighter, bearing, preheating dewatering box, spiral shell
Rotation propulsion knife；Described main frame side is provided with motor, and described motor is connected with main shaft, and described main shaft is provided with screw propulsion knife, institute
State and outside screw propulsion knife, be provided with carbonization cylinder, described carbonization cylinder one end is provided with charging aperture, the described carbonization cylinder other end is provided with discharging
Mouthful, described carbonization cylinder side is provided with cooler bin, and described cooler bin side is provided with carbonization case, and described carbonization upper box part is provided with gives vent to anger
Mouthful, if described carbonization bottom portion is provided with dry fire starter, below described lighter, it is provided with bearing, described carbonization case bottom side is provided with
Air inlet, described carbonization case side is provided with preheating dewatering box, and described preheating dehydration upper box part is provided with air vent, described charging aperture with
Side feed auger conveyer belt connects, and described gas outlet is connected with spray column I by pipeline, and described air inlet passes through pipeline and gas
Liquid knockout tower connects, and described discharging opening is connected with side discharging spiral conveyor；Feed auger conveyer belt is by Organic substances such as straws
Material is delivered to charging aperture, and motor drives main shaft rotation, and material is pushed to preheating dewatering box by the screw propulsion knife on main shaft to be carried out
Dry heat, continues for material to push to carbonization case, and then by carbonization, completely material pushes to cooler bin cooling, after cooling
Powdered carbon pushes to discharging opening through screw propulsion knife and discharges main frame, and material transports collection by discharging spiral conveyor；Just start when
Waiting also does not have combustion gas that retort is heated, so needing gasification furnace that biogas are melted into fuel gas, but in gas
There are a lot of impurity, purify, then cooled down by air cooler through spray column I, spray column II, import in oil water separator through blower fan and carry out
Process, enter back into gas-liquid separation tower and fuel gas is dehumidified, become pure fuel gas, at this moment fuel gas enters from air inlet
Enter the pollution waste gas that in carbonization case, burning would not produce thick smoke, the thermal current that burning produces enters to material through preheating dewatering box
Row thermal dehydration, finally discharges from air vent；Biomass carbonated generation fuel gas in carbonization case, enters spray through gas outlet
Drench tower I to purify, enter spray column II, then cooled down by air cooler, import in oil water separator through blower fan and processed, enter back into gas
Liquid knockout tower dehumidifies to fuel gas, becomes pure fuel gas, is at this moment no longer needed for gasification furnace work, by biomass carbon
Change the fuel gas producing and just can circulate carbonization biomass.
Preferably, it is provided with sprayer unit in described cooler bin, powdered carbon is cooled down further, prevent the powdered carbon not exclusively cooling down
Ingress of air produces Mars, produces security incident, and sprayer unit can avoid accident to occur by moistening for powdered carbon spray.
Beneficial effect shows this utility model compared with prior art：
1) system automation degree is high, and screw propulsion knife makes raw material be heated evenly, and carbonization degree is high, and fuel recycle utilizes the energy
Consume little, expellant gas not dust-laden after purified treatment, pollution is little；
2) it is provided with sprayer unit in cooler bin, powdered carbon is cooled down further, prevent the powdered carbon ingress of air not exclusively cooling down
Produce Mars, produce security incident, sprayer unit can avoid accident to occur by moistening for powdered carbon spray；
3) system provides thermal source using the gas fuel burning that raw material itself produces, and air inflow size directly passes through wind
Machine controls, thus arbitrarily carburizing temperature can be controlled it is ensured that powdered carbon stay in grade, and flue gas is through spray and refrigerated separation after-burning
Burn, more environmentally-friendly.
Brief description
Accompanying drawing 1 is a kind of smokeless carbonization system process chart of straw of this utility model；
Accompanying drawing 2 is a kind of straw of this utility model smokeless carbonization system charging-discharging structure schematic diagram；
Accompanying drawing 3 is a kind of smokeless carbonization system structural representation of straw of this utility model；
Accompanying drawing 4 is a kind of straw of this utility model smokeless carbonization system main machine structure schematic diagram；
In figure：11- gasification furnace, 12- spray column I, 13- spray column II, 14- air cooler, 15- blower fan, 16- oil-water separation
Device, 17- gas-liquid separation tower, 18- feed auger conveyer belt, 19- main frame, 20- discharging spiral conveyor, 101- motor, 102- enters
Material mouth, 103- carbonization cylinder, 104- air vent, 105- gas outlet, 106- carbonization case, 107- cooler bin, 108- screw propulsion knife,
109- preheats dewatering box, 110- bearing, 111- lighter, 112- air inlet, 113- discharging opening, 114- main shaft.
Specific embodiment
For convenience of the understanding of those skilled in the art, 1-4 below in conjunction with the accompanying drawings, one is entered to the technical solution of the utility model
Step illustrates.
A kind of smokeless carbonization system of straw, including gasification furnace 11, spray column I 12, spray column II 13, air cooler 14, blower fan
15th, oil water separator 16, gas-liquid separation tower 17, feed auger conveyer belt 18, main frame 19, discharging spiral conveyor 20；Described gas
Change stove 11 to be connected with spray column I 12 by pipeline, pipeline is provided with valve；Described spray column I 12 passes through pipeline and spray column II
13 connections, described spray column II 13 is connected with air cooler 14 by pipeline, and described air cooler 14 is connected with blower fan 15 by pipeline,
Pipeline is provided with valve, and described blower fan 15 is connected with oil water separator 16 by pipeline, and described oil water separator 16 passes through pipeline
It is connected with gas-liquid separation tower 17；Described main frame 19 includes motor 101, charging aperture 102, carbonization cylinder 103, steam vent, gas outlet
105th, carbonization case 106, cooler bin 107, main shaft 114, air inlet 112, discharging opening 113, lighter 111, bearing 110, preheating are de-
Water tank 109, screw propulsion knife 108；Described main frame 19 side is provided with motor 101, and described motor 101 is connected with main shaft 114, described
Main shaft 114 is provided with screw propulsion knife 108, is provided with carbonization cylinder 103, described carbonization cylinder 103 1 outside described screw propulsion knife 108
End is provided with charging aperture 102, and described carbonization cylinder 103 other end is provided with discharging opening 113, and described carbonization cylinder 103 side is provided with cooler bin
107, described cooler bin 107 side is provided with carbonization case 106, and described carbonization case 106 top is provided with gas outlet 105, described carbonization case
If 106 bottoms are provided with dry fire starter 111, below described lighter 111, it is provided with bearing 110, described carbonization case 106 bottom side sets
There is air inlet 112, described carbonization case 106 side is provided with preheating dewatering box 109, described preheating dewatering box 109 top is provided with aerofluxuss
Mouth 104, described charging aperture 102 is connected with side feed auger conveyer belt 18, and pipeline and spray column I are passed through in described gas outlet 105
12 connections, described air inlet 112 is connected with gas-liquid separation tower 17 by pipeline, described discharging opening 113 and side discharging spiral transferring
Send band 20 connection；The organic materials such as straw are delivered to charging aperture 102 by feed auger conveyer belt 18, and motor 101 drives main shaft 114
Rotation, material is pushed to preheating dewatering box 109 and is dried heating by the screw propulsion knife 108 on main shaft 114, continues material
Push to carbonization case 106, then completely material pushes to cooler bin 107 and cools down by carbonization, and the powdered carbon after cooling pushes away through spiral
Feed 108 pushes to discharging opening 113 and discharges main frame 19, and material transports collection by discharging spiral conveyor 20；When just start
Also do not have combustion gas that retort is heated, so needing gasification furnace 11 that biogas are melted into fuel gas, but in gas
There are a lot of impurity, purify, then cooled down by air cooler 14 through spray column I 12, spray column II 13, import oil-water separation through blower fan 15
Processed in device 16, enter back into gas-liquid separation tower 17 and fuel gas is dehumidified, become pure fuel gas, at this moment combustible gas
Body enters, from air inlet 112, the pollution waste gas that would not produce thick smoke that burns carbonization case 106, and the thermal current that burning produces passes through
Preheating dewatering box 109 carries out thermal dehydration to material, finally discharges from air vent 104；Biomass carbonated product in carbonization case 106
Raw fuel gas, enters spray column I 12 through gas outlet 105 and purifies, enter spray column II 13, then cooled down by air cooler 14, warp
Blower fan 15 imports in oil water separator 16 and is processed, and enters back into gas-liquid separation tower 17 and fuel gas is dehumidified, become pure
Fuel gas, is at this moment no longer needed for gasification furnace 11 and works, and just can circulate carbonization by the fuel gas of biomass carbonated generation
Biomass.
It is provided with sprayer unit in described cooler bin 107, powdered carbon is cooled down further, prevent the powdered carbon not exclusively cooling down from contacting
Air produces Mars, produces security incident, and sprayer unit can avoid accident to occur by moistening for powdered carbon spray.
Above content is only to structure example of the present utility model and explanation, the technology of affiliated the art
Personnel are made various modifications or supplement or substituted using similar mode to described specific embodiment, without departing from
The structure of utility model or surmount scope defined in the claims, all should belong to protection domain of the present utility model.
Claims (2)
1. the smokeless carbonization system of a kind of straw, including gasification furnace, spray column I, spray column II, air cooler, blower fan, oil-water separation
Device, gas-liquid separation tower, feed auger conveyer belt, main frame, discharging spiral conveyor；It is characterized in that described gasification furnace passes through pipeline
It is connected with spray column I；Described spray column I is connected with spray column II by pipeline, and described spray column II passes through pipeline and air cooler
Connect, described air cooler is connected with blower fan by pipeline, and described blower and pipeline is connected with oil water separator, and described profit divides
It is connected with gas-liquid separation tower by pipeline from device；Described main frame includes motor, charging aperture, carbonization cylinder, steam vent, gas outlet, charcoal
Change case, cooler bin, main shaft, air inlet, discharging opening, lighter, bearing, preheating dewatering box, screw propulsion knife；Described main frame side
It is provided with motor, described motor is connected with main shaft, described main shaft is provided with screw propulsion knife, is provided with charcoal outside described screw propulsion knife
Change cylinder, described carbonization cylinder one end is provided with charging aperture, and the described carbonization cylinder other end is provided with discharging opening, and described carbonization cylinder side is provided with cold
But case, described cooler bin side is provided with carbonization case, and described carbonization upper box part is provided with gas outlet, and described carbonization bottom portion is provided with some
Lighter, is provided with bearing below described lighter, and described carbonization case bottom side is provided with air inlet, and described carbonization case side is provided with
Preheating dewatering box, described preheating dehydration upper box part is provided with air vent, and described charging aperture is connected with side feed auger conveyer belt, institute
State gas outlet to be connected with spray column I by pipeline, described air inlet is connected with gas-liquid separation tower by pipeline, described discharging opening with
Discharging spiral conveyor in side connects.
2. a kind of smokeless carbonization system of straw according to claim 1 is it is characterised in that be provided with spraying in described cooler bin
Device.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620878549.5U CN205974420U (en) | 2016-08-13 | 2016-08-13 | Smokeless carbonization system of straw |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620878549.5U CN205974420U (en) | 2016-08-13 | 2016-08-13 | Smokeless carbonization system of straw |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205974420U true CN205974420U (en) | 2017-02-22 |
Family
ID=59977227
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620878549.5U Expired - Fee Related CN205974420U (en) | 2016-08-13 | 2016-08-13 | Smokeless carbonization system of straw |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205974420U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108326009A (en) * | 2018-02-01 | 2018-07-27 | 上海盛弘环境科技有限公司 | A kind of rubbish is converted into the processing system of distributed energy |
| CN110317618A (en) * | 2018-03-29 | 2019-10-11 | 安徽省升泰节能科技服务有限公司 | A kind of stalk pyrolysis carbonizing plant |
| CN111825429A (en) * | 2020-08-07 | 2020-10-27 | 绥棱县灵透黑陶文化艺术有限公司 | Preparation method of dotted crystal black pottery |
-
2016
- 2016-08-13 CN CN201620878549.5U patent/CN205974420U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108326009A (en) * | 2018-02-01 | 2018-07-27 | 上海盛弘环境科技有限公司 | A kind of rubbish is converted into the processing system of distributed energy |
| CN110317618A (en) * | 2018-03-29 | 2019-10-11 | 安徽省升泰节能科技服务有限公司 | A kind of stalk pyrolysis carbonizing plant |
| CN111825429A (en) * | 2020-08-07 | 2020-10-27 | 绥棱县灵透黑陶文化艺术有限公司 | Preparation method of dotted crystal black pottery |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20170222 Termination date: 20170813 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |