CN205740877U - A kind of continuous-production-type rotary unloading retort - Google Patents
A kind of continuous-production-type rotary unloading retort Download PDFInfo
- Publication number
- CN205740877U CN205740877U CN201620652231.5U CN201620652231U CN205740877U CN 205740877 U CN205740877 U CN 205740877U CN 201620652231 U CN201620652231 U CN 201620652231U CN 205740877 U CN205740877 U CN 205740877U
- Authority
- CN
- China
- Prior art keywords
- carbonization
- continuous
- rotary unloading
- blanking
- production
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Active
Links
Landscapes
- Solid Fuels And Fuel-Associated Substances (AREA)
Abstract
This utility model relates to a kind of continuous-production-type blanking retort, the upper port of biomass material carbonization storage bin blanking tank continuous with carbonization solids is connected, carbonization aerogenesis room is circumferentially positioned at the bottom of biomass material carbonization storage bin, connected by screen cloth between carbonization aerogenesis room with biomass material carbonization storage bin, it is provided with blanking rotating disk between biomass material carbonization storage bin and the continuous blanking tank of carbonization solids, transportation pipeline connects with carbonization aerogenesis room, the lower port of the continuous blanking tank of carbonization solids is connected with the upper port of carbonization material collecting bin, the lower port of carbonization material collecting bin passes through seal cap sealing, rotary unloading power source is used for driving blanking rotating disk, material lifting device is connected with carbonization material collecting bin, for the finished product materials in carbonization material collecting bin is sent to outside.This utility model is little to the pollution of environment, and artificial Meteorological is low, and automaticity is high.
Description
Technical field
This utility model belongs to biomass carbonated technical field, is specifically related to a kind of continuous-production-type rotary unloading carbonization
Stove.
Background technology
At present, the biomass energy of China is the abundantest, and in annual rural area, agricultural crop straw yield is about 700,000,000 tons, can make
For about 300,000,000 tons of power applications, about convert into 1.5 hundred million tons of standard coals.But have many areas but directly to be burnt by the straw in farmland
Burning processes, and the energy not only causes huge waste, and thick smoke also result in huge pollution to air, environment.
China has been promoted a conservation culture very important strategic importance by visible Biomass Energy Development, biomass carbonated technology.
Present stage, there is a lot of producer to put in the research of biomass generating apparatus again, but overall technology level all compares
Low, function is the most complete, and versatility is poor；More advanced Mobile chamber type stove, there is also the carbonization cycle long, equipment cost
Height, floor space is big, the shortcomings such as automatic and mechanical level is low.
Summary of the invention
The purpose of this utility model is to provide a kind of continuous-production-type rotary unloading retort.This device context is polluted
Little, artificial Meteorological is low, and automaticity is high.
The technical solution adopted in the utility model: a kind of continuous-production-type rotary unloading retort, it includes that biomass are former
Material carbonization storage bin, hydraulic pressure automatic blanking hold-down mechanism, carbonization aerogenesis room, the continuous blanking tank of carbonization solids, rotary unloading move
Power source, carbonization material collecting bin, material lifting device, transportation pipeline, oil gas flowing power source, oil gas pressurization condensation separation
Device, tar liquid storage tank and finished product gas storage tanks, biomass material carbonization storage bin and the continuous blanking tank of carbonization solids
Upper port connect, carbonization aerogenesis room is circumferentially positioned at the bottom of biomass material carbonization storage bin, and carbonization aerogenesis room is with biological
Connected by screen cloth between raw material carbonization storage bin, biomass material carbonization storage bin and the continuous blanking tank of carbonization solids it
Between be provided with blanking rotating disk, transportation pipeline connects with carbonization aerogenesis room, the lower port of the continuous blanking tank of carbonization solids
Being connected with the upper port of carbonization material collecting bin, the lower port of carbonization material collecting bin passes through seal cap sealing, and rotary unloading moves
Power source is used for driving blanking rotating disk, material lifting device to be connected with carbonization material collecting bin, for by carbonization material collecting bin
Interior finished product materials is sent to outside, wherein, is positioned at carbonization aerogenesis room on the lower sides of biomass material carbonization storage bin
Be provided with several lighting-up tuyere and several oxygen feeder at a distance above；Transportation pipeline is first with oil gas flowing power source even
Connecing, then be connected with oil gas pressurization condensation separator, oil gas pressurization condensation separator is deposited with tar liquid respectively by two outlets
Storage tank connects with finished product gas storage tanks, and the tar wherein separated enters tar liquid storage tank, and isolated gas enters
Enter finished product gas storage tanks；It is provided with gas composition analyzer between finished product gas storage tanks and oil gas pressurization condensation separator,
Data after analyzing pass to oil gas flowing power source to regulate air current flow speed.
Further, described biomass material carbonization storage bin is cylinder-like structure, biomass material carbonization storage bin
The partial carbonization district that by superposed raw material district, is positioned at middle part and be positioned at bottom and near lighting-up tuyere and the carbonization of carbonization aerogenesis room
District forms.
Further, described cylinder-like structure is by outer layer stainless steel layer, middle high temperature resistant Margarita sand thermal insulation layer and internal layer
High temperature stainless steel layer is connected in sequence.
Further, the sidewall of described biomass material carbonization storage bin is provided with several temperature detection mouth.
Further, described carbonization aerogenesis room is arc-shaped, and is double-decked insulation, and its internal layer and outer layer are high temperature
Stainless steel layer, centre is that high temperature resistant Margarita sand is heat insulation.
Further, the described continuous blanking tank of carbonization solids is cone shape, and upper port is big opening, and lower port is
Little opening.
Further, described rotary unloading power source motor output power, slows down through V-shaped belt pulley, is delivered to pendulum
Line pinwheel reducer, is delivered in blanking rotating disk after secondary speed-reducing.
Further, the described carbonization material collecting bin side of being cone shape, upper port is big mouth, and lower end is osculum.
Further, described material lifting device is cylindrical in shape, and inside is helical blade structure, at helical blade
Structure realizes the lifting transmission of material during rotating, the two ends of material lifting device have end cover to be sealed against, material
Discharging opening is arranged at the top of lifting device, and carbonization finished product is discharged from discharging opening, has Water-fog dusting apparatus at discharging opening.
Further, the outside bag of described transportation pipeline is provided with insulation material integument；Oil gas pressurization condensation separation
Device is made up of gas compressor and gas condenser.
Compared with prior art it provides the benefit that this utility model: use this utility model can realize biomass material
Seriality carbonization, need not in carbonization process cease fire, and production efficiency is high.In whole production process, environmental pollution is little, manually puts into
Expense is low, and automaticity is high, by functions such as frequency controls, the constant product quality of production, is reliable, easy to control.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model.
Detailed description of the invention
As it is shown in figure 1, a kind of continuous-production-type rotary unloading retort, it includes biomass material carbonization storage bin 1, liquid
Pressure automatic blanking hold-down mechanism 2, carbonization aerogenesis room 3, the continuous blanking tank of carbonization solids 4, rotary unloading power source 5, carbide
Material collecting bin 6, material lifting device 7, transportation pipeline 8, oil gas flowing power source 9, oil gas pressurization condensation separator 10, liquid
State tar storage tank 11 and finished product gas storage tanks 12, biomass material carbonization storage bin 1 and the continuous blanking tank of carbonization solids 4
Upper port connect, carbonization aerogenesis room 3 is circumferentially positioned at the bottom of biomass material carbonization storage bin 1, and carbonization aerogenesis room 3 is with raw
Connected by screen cloth between raw material of substance carbonization storage bin 1, prevent the solid granule in carbide from entering carbonization aerogenesis room 3
In, blocking aerogenesis room or transportation pipeline 8.Between biomass material carbonization storage bin 1 and the continuous blanking tank of carbonization solids 4
Being provided with blanking rotating disk, transportation pipeline 8 connects with carbonization aerogenesis room 3, the lower port of the continuous blanking tank of carbonization solids 4
Being connected with the upper port of carbonization material collecting bin 6, the lower port of carbonization material collecting bin 6 passes through seal cap sealing, rotary unloading
Power source 5 is used for driving blanking rotating disk, material lifting device 7 to be connected with carbonization material collecting bin 6, for being received by carbonization material
Finished product materials in collection storehouse 6 is sent to outside, wherein, is positioned at carbonization on the lower sides of biomass material carbonization storage bin 1
Aerogenesis room 3 be provided with several lighting-up tuyere 15 and several oxygen feeder at a distance above；Transportation pipeline 8 elder generation and gas stream
Dynamic power source 9 connects, then is connected with oil gas pressurization condensation separator 10, and oil gas pressurization condensation separator 10 is by two outlets point
Not connecting with tar liquid storage tank 11 and finished product gas storage tanks 12, the tar wherein separated enters tar liquid storage
Tank 11, isolated gas enters finished product gas storage tanks 12；Finished product gas storage tanks 12 and oil gas pressurization condensation separator 10
Between be provided with gas composition analyzer 13, for will analyze after data pass to oil gas flowing power source 9 to regulate air-flow stream
Dynamic speed.
Described biomass material carbonization storage bin 1 is cylinder-like structure, biomass material carbonization storage bin 1 by being positioned on
The raw material district in portion, it is positioned at the partial carbonization district at middle part and is positioned at bottom and near lighting-up tuyere 15 and the char zone group of carbonization aerogenesis room 3
Become.For storing graininess of different nature or the nodular raw materials such as straw, fruit tree, forage.Described cylinder-like structure is by outer layer
Stainless steel layer, middle high temperature resistant Margarita sand thermal insulation layer and internal layer high temperature stainless steel layer are connected in sequence.
It is provided with several temperature detection mouth on the sidewall of described biomass material carbonization storage bin 1.With oxygen feeding amount and suction
Air force controls carbonization time, temperature, Yield and quality in stove.
Described carbonization aerogenesis room 3 is arc-shaped, and is double-decked insulation, and its internal layer and outer layer are high temperature stainless steel
Layer, centre is that high temperature resistant Margarita sand is heat insulation.This structure can prevent gas in course of conveying, and tar cooling blocks pipeline.
The described continuous blanking tank of carbonization solids 4 is cone shape, and upper port is big opening, and lower port is little opening.
Described rotary unloading power source 5 motor output power, slows down through V-shaped belt pulley, is delivered to cycloidal-pin wheel and subtracts
Speed device, is delivered in blanking rotating disk after secondary speed-reducing.While blanking rotating disk rotates, it is achieved finished product carbide
Move down circulation.For avoiding decelerator ambient temperature too high, damage decelerator, around decelerator, have insulating water device for cooling, it is ensured that
The normal use of decelerator.
Described carbonization material collecting bin 6 side of being cone shape, upper port is big mouth, and lower end is osculum.This collecting bin merit
It can be the finished product materials collecting to get off in the continuous blanking tank of carbonization solids 4.
Described material lifting device 7 is cylindrical in shape, and inside is helical blade structure 14, at helical blade structure 14
Realizing the lifting transmission of material during rotation, the two ends of material lifting device 7 have end cover to be sealed against, material lifting
Discharging opening is arranged at the top of device 7, and carbonization finished product is discharged from discharging opening, has Water-fog dusting apparatus at discharging opening, it is to avoid dust is to ring
The pollution in border.
The outside bag of described transportation pipeline 8 is provided with insulation material integument；Oil gas pressurization condensation separator 10 is by gas
Gas compressor and gas condenser composition, it is to avoid oil gas produces tar in course of conveying and condenses pipeline blockage.
Oil gas flowing power source 9 includes roots blower, motor and variable-frequency governor, according to producing gas composition analyzer 13
The wind-force size of data point reuse blower fan.
Oil gas pressurization condensation separator 10 is made up of gas compressor and gas condenser, and effect is by gas and tar etc.
Liquid separates in this device.
Tar liquid storage tank 11, the profile of this tank is cylindrical barrel structure, and feature is that the sealing to tar have employed
Watertight construction.
Gas composition analyzer 13, the effect of this instrument is the percentage ratio of the composition particularly oxygen analyzing gas, to blower fan
Wind-force size adjust given foundation.
Finished product gas storage tanks 12 is to store the container of finished product gas, with pressure reading instument.
Operation principle: opening hydraulic pressure automatic blanking hold-down mechanism 2, material enters in biomass material carbonization storage bin 1,
According to the setting of pressure transducer, hydraulic pressure automatic blanking hold-down mechanism 2 can automatically roll and material is compacted to certain pressure, and
Quit work, ready for carbonization.
Open the sealing lid on carbonization lighting-up tuyere 15, gradually light a fire from each lighting-up tuyere 15, be open at rear road work simultaneously
The blower fan of the cleaning system of sequence and other controlled valves.After fire burning, each shop fire hole cover is loaded onto, makes fire hole the closeest
Envelope.Hereafter biomass will the most gradually start carbonization from firing tip.After carbonization a period of time, internal temperature is stepped up, and arrives
Reach temperature at the screen cloth of carbonization aerogenesis room 3 and reached the highest.The whole charcoal of bottom material of now biomass material carbonization storage bin 1
Changing, the material intensity after carbonization reduces, and becomes fragility.Now, opening rotary unloading power source 5, finished product materials begins to decline entrance
Carbonization material collecting bin 6, opens material lifting device 7 simultaneously, and material collects transport vehicle by material lifting device 7 is elevated
In.
The products such as tar gas can be produced while carbonization, can flow out through carbonization aerogenesis room 3.Gas passes through oil-gas transportation
Pipeline 8 enters into oil gas pressurization condensation separator 10, and after Oil-gas Separation, the liquid such as tar is stored up by tar liquid storage tank 11
Deposit.Gas enters partly into finished product gas storage tanks 12 and stores.
Embodiment 1: in the continuous flow procedure of limit carbonization limit discharging, going out charcoal speed is certain value, at this moment transfers out
Carbide effect is not up to application indexes, should slow down the velocity of rotation of rotary unloading in time, reduces discharging speed, and continuous observation
It is conveyed out the material charred effect of material, until after the material charred effect being conveyed out reaches application indexes, keeping charcoal speed
Spending constant, at this moment carbonization is complete, and energy discharging in time, makes input and output material speed reach dynamic equilibrium, it is ensured that the seriality of input and output material.
Embodiment 2: in the continuous flow procedure of limit carbonization limit discharging, observes the change of stove body temperature, at any time such as temperature
Degree persistently reduces, and illustrates that discharging is fast, should adjust the speed of blanking in time, when temperature rises to certain value, and when keeping constant,
The speed of blanking device is constant, and at this moment carbonization is complete, and energy discharging in time, makes input and output material speed reach dynamic equilibrium, it is ensured that
The seriality of discharging.
In carbonization, the cyclic process of gas is, air from the entrance suitable for reading of biomass material carbonization storage bin 1 under feed bin
All gas after end carries out carbonization reaction chemical reaction with material is deposited through carbonization aerogenesis room 3 and pipeline entrance tar liquid thereof
Storage tank 11 and finished product gas storage tanks 12.Can adjust according to the ratio of oxygen in analyser through gas composition analyzer 13 in Tu
The air force of whole roots blower, the speed governing of extension set is completed by frequency conversion, it is ensured that the content of oxygen is in the range of safe level.
Claims (10)
1. a continuous-production-type rotary unloading retort, compresses including biomass material carbonization storage bin, hydraulic pressure automatic blanking
Mechanism, carbonization aerogenesis room, the continuous blanking tank of carbonization solids, rotary unloading power source, carbonization material collecting bin, material lifting dress
Put, transportation pipeline, oil gas flow power source, oil gas pressurizes, and condensation separator, tar liquid storage tank and finished product gas are deposited
Storage tank, it is characterised in that the upper port of biomass material carbonization storage bin blanking tank continuous with carbonization solids is connected, carbonization is produced
Air chamber is circumferentially positioned at the bottom of biomass material carbonization storage bin, between carbonization aerogenesis room and biomass material carbonization storage bin
Connected by screen cloth, between biomass material carbonization storage bin and the continuous blanking tank of carbonization solids, be provided with blanking rotating disk,
Transportation pipeline connects with carbonization aerogenesis room, and the lower port of the continuous blanking tank of carbonization solids is upper with carbonization material collecting bin
Port connects, and the lower port of carbonization material collecting bin passes through seal cap sealing, and rotary unloading power source is used for driving blanking to rotate
Dish, material lifting device is connected with carbonization material collecting bin, outside the finished product materials in carbonization material collecting bin being sent to
Portion, wherein, is positioned at the setting at a distance above of carbonization aerogenesis room on the lower sides of biomass material carbonization storage bin
There are several lighting-up tuyere and several oxygen feeder；Transportation pipeline is first connected with oil gas flowing power source, then condenses with oil gas pressurization
Separator connect, oil gas pressurization condensation separator by two outlet respectively with tar liquid storage tank and finished product gas storage tanks
Connection, the tar wherein separated enters tar liquid storage tank, and isolated gas enters finished product gas storage tanks；Finished product
Being provided with gas composition analyzer between gas storage tanks and oil gas pressurization condensation separator, the data after analyzing are passed to
Oil gas flowing power source regulates air current flow speed.
A kind of continuous-production-type rotary unloading retort the most according to claim 1, it is characterised in that described biomass
Raw material carbonization storage bin is cylinder-like structure, biomass material carbonization storage bin by superposed raw material district, be positioned at middle part
Partial carbonization district forms with being positioned at bottom and the char zone near lighting-up tuyere and carbonization aerogenesis room.
A kind of continuous-production-type rotary unloading retort the most according to claim 2, it is characterised in that described cylindrical shape
Structure is connected in sequence by outer layer stainless steel layer, middle high temperature resistant Margarita sand thermal insulation layer and internal layer high temperature stainless steel layer.
A kind of continuous-production-type rotary unloading retort the most according to claim 1, it is characterised in that described biomass
Several temperature detection mouth it is provided with on the sidewall of raw material carbonization storage bin.
A kind of continuous-production-type rotary unloading retort the most according to claim 1, it is characterised in that described carbonization is produced
Air chamber is arc-shaped, and is double-decked insulation, and its internal layer and outer layer are high temperature stainless steel layer, centre be high temperature resistant Margarita sand every
Heat.
A kind of continuous-production-type rotary unloading retort the most according to claim 1, it is characterised in that described carbonization is solid
The continuous blanking tank of body thing is cone shape, and upper port is big opening, and lower port is little opening.
A kind of continuous-production-type rotary unloading retort the most according to claim 1, it is characterised in that under described rotation
Material power source motor output power, slows down through V-shaped belt pulley, is delivered to planet-cycloid reducer, pass after secondary speed-reducing
It is delivered in blanking rotating disk.
A kind of continuous-production-type rotary unloading retort the most according to claim 1, it is characterised in that described carbide
The material collecting bin side of being cone shape, upper port is big mouth, and lower end is osculum.
A kind of continuous-production-type rotary unloading retort the most according to claim 1, it is characterised in that described material carries
Rising device is cylindrical in shape, and inside is helical blade structure, realizes carrying of material during helical blade structure rotates
Rising transmission, the two ends of material lifting device have end cover to be sealed against, and discharging opening is arranged at the top of material lifting device, and carbonization becomes
Product are discharged from discharging opening, have Water-fog dusting apparatus at discharging opening.
A kind of continuous-production-type rotary unloading retort the most according to claim 1, it is characterised in that described oil gas
The outside bag of transfer pipeline is provided with insulation material integument；Oil gas pressurization condensation separator is by gas compressor and gas condenser group
Become.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620652231.5U CN205740877U (en) | 2016-06-27 | 2016-06-27 | A kind of continuous-production-type rotary unloading retort |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620652231.5U CN205740877U (en) | 2016-06-27 | 2016-06-27 | A kind of continuous-production-type rotary unloading retort |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205740877U true CN205740877U (en) | 2016-11-30 |
Family
ID=57381371
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620652231.5U Active CN205740877U (en) | 2016-06-27 | 2016-06-27 | A kind of continuous-production-type rotary unloading retort |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205740877U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112852449A (en) * | 2020-12-24 | 2021-05-28 | 阿拉善盟正杰工程建设有限公司 | Carbonization furnace for secondary utilization of raw coal smoke |
-
2016
- 2016-06-27 CN CN201620652231.5U patent/CN205740877U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112852449A (en) * | 2020-12-24 | 2021-05-28 | 阿拉善盟正杰工程建设有限公司 | Carbonization furnace for secondary utilization of raw coal smoke |
| CN112852449B (en) * | 2020-12-24 | 2022-01-28 | 阿拉善盟正杰工程建设有限公司 | Carbonization furnace for secondary utilization of raw coal smoke |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN106350084B (en) | A kind of the biochemical substances fuel processing system and its production method of high performance active carbon | |
| CN201756534U (en) | Fixed bed biomass gas industrial boiler system | |
| CN107892931B (en) | Device and method for preparing biochar through mobile pyrolysis | |
| CN103773809B (en) | The garage type dry method fermentation comprehensive processing method of changing food waste and organic waste | |
| CN106077021A (en) | Kitchen is remaining, market of farm produce garbage as resource processes anaerobic fermentation system and method | |
| CN108191474A (en) | A kind of animal wastes harmless resource recycles intelligent processing system and method | |
| CN202881186U (en) | Synchronous and continuous biomass charcoal and gas production system | |
| CN205740877U (en) | A kind of continuous-production-type rotary unloading retort | |
| CN104861994B (en) | Cooling device in biomass carbonization stove | |
| CN104861993B (en) | Tower-type continuous carbonization furnace for biomass | |
| CN201737895U (en) | Device for evaluating small-granule oil shale solid heat carrier dry distillation process | |
| CN104355357B (en) | A kind of filter for plant's excrement and urine water treatment | |
| CN208500789U (en) | A kind of animal wastes harmless resource recycling intelligent processing system | |
| CN201809316U (en) | Fixed-bed biomass gasification and power generation device | |
| CN105885873A (en) | Continuous production type rotary discharging carbonization furnace | |
| CN109370881B (en) | Novel methane tank | |
| CN104973598A (en) | Active carbon production apparatus | |
| CN105036126A (en) | Device for recycling agricultural wastes | |
| CN204689938U (en) | Tower biological matter continuous carbonization furnace | |
| CN201386087Y (en) | Semi-automatic integrated biomass coal making device | |
| CN107312709B (en) | Rural methane-generating pit intelligence temperature control system of using with preliminary treatment | |
| CN205550853U (en) | Biomass boiler lime -ash separator | |
| CN205740879U (en) | One can produce box type carbide furnace continuously | |
| CN212955034U (en) | Spiral cooling system for biological coal production | |
| CN109628117B (en) | Biomass self-heating carbonization device and application thereof |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant |