CN103980922B - Co-producing bio charcoal, biological vinegar and the system of biological tar - Google Patents
Co-producing bio charcoal, biological vinegar and the system of biological tar Download PDFInfo
- Publication number
- CN103980922B CN103980922B CN201410246575.1A CN201410246575A CN103980922B CN 103980922 B CN103980922 B CN 103980922B CN 201410246575 A CN201410246575 A CN 201410246575A CN 103980922 B CN103980922 B CN 103980922B
- Authority
- CN
- China
- Prior art keywords
- biological
- furnace
- furnace shell
- outlet
- chamber
- 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.)
- Expired - Fee Related
Links
Classifications
-
- 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
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/10—Biofuels, e.g. bio-diesel
Landscapes
- Carbon And Carbon Compounds (AREA)
Abstract
The present invention relates to a kind of use the carbonaceous material co-producing bio charcoals such as agriculture wastes, biological vinegar and the system of biological tar.Co-producing bio charcoal of the present invention, biological vinegar and the system of biological tar, including pyrolysis installation, cleaner unit, refrigerated separation tower and precipitator tower, described precipitator tower is vertically arranged, precipitator tower includes housing and inner chamber, the cone that inner chamber is big up and small down, the top of housing offers the charging aperture with inner space, the biological vinegar outlet with inner space is offered at the middle part of described housing, the biological tar outlet with inner space is offered in the bottom of housing, the lime-ash outlet with inner space is offered in the bottom of housing, the gas outlet of described pyrolysis installation connects with the air inlet of cleaner unit, the air outlet of cleaner unit connects with the air inlet of refrigerated separation tower, the condensate outlet of refrigerated separation tower connects with the charging aperture of precipitator tower.Present configuration is simple, low cost, easy and simple to handle, and do not result in air pollution.
Description
Technical field
The present invention relates to the processing system of a kind of agricultural wastes, particularly relate to the carbonaceous materials such as a kind of use agriculture wastes
Co-producing bio charcoal, biological vinegar and the system of biological tar.
Background technology
The farming and animal husbandry surplus resources such as the straw of China are the abundantest, and the yield of the residue biomass such as annual straw is about 600,000,000 tons of left sides
The right side, the process of these residue biomass resources just seems by for important have some peasants to keep the fertile of soil and process side
Just, directly these residue biomass are burnt in farmland, although using this processing mode simple and easy to operate, but the most not
Only make living resources utilization rate low, and bigger air pollution can be caused.
Summary of the invention
The technical problem to be solved in the present invention is to provide a kind of simple in construction, low cost, co-producing bio charcoal easy and simple to handle, biology
Vinegar and the system of biological tar, and do not result in air pollution.
Co-producing bio charcoal of the present invention, biological vinegar and the system of biological tar, including pyrolysis installation, cleaner unit, refrigerated separation tower and
Precipitator tower, described precipitator tower is vertically arranged, and precipitator tower includes housing and inner chamber, the cone that inner chamber is big up and small down, housing
Top offers the charging aperture with inner space, offers the biological vinegar outlet with inner space at the middle part of described housing, at shell
The bottom of body offers the biological tar outlet with inner space, offers the lime-ash outlet with inner space in the bottom of housing,
The gas outlet of described pyrolysis installation connects with the air inlet of cleaner unit, and the air outlet of cleaner unit connects with the air inlet of refrigerated separation tower,
The condensate outlet of refrigerated separation tower connects with the charging aperture of precipitator tower, and wherein said pyrolysis installation includes heating furnace and chamber furnaced,
Described heating furnace includes furnace shell and heating chamber, and heating chamber is up big and down small, the top in heating chamber be cylindrical, bottom for conical,
Being provided with heater in the furnace shell of heating furnace, the top of heating furnace offers upper feeding mouth, under the bottom of heating furnace offers
Charging aperture, the bottom of heating furnace offers air inlet, is further opened with gas outlet at the top of heating furnace, and described chamber furnaced includes stove
Shell and inner chamber, offer air inlet and gas outlet at the top of chamber furnaced, offers discharging opening in the bottom of chamber furnaced, described point
Discharging opening from stove is positioned at the top of the lower charging of described heating furnace, and the lower charging aperture of the discharging opening of described chamber furnaced and heating furnace
Connection, the air inlet of chamber furnaced connects with the gas outlet of heating furnace, and the gas outlet of chamber furnaced connects with the air inlet of cleaner unit.
Co-producing bio charcoal of the present invention, biological vinegar and the system of biological tar, wherein said precipitator tower also includes the containing cavity of cylinder,
Described containing cavity is positioned at the top of inner chamber, containing cavity and inner space, and the charging aperture of precipitator tower connects with containing cavity, at housing
Top is further opened with waste gas outlet.
Co-producing bio charcoal of the present invention, biological vinegar and the system of biological tar, wherein said waste gas outlet is with active carbon purifying device even
Connect.
Co-producing bio charcoal of the present invention, biological vinegar and the system of biological tar, the bottom of wherein said heating furnace is further opened with steam and enters
Mouthful.
Co-producing bio charcoal of the present invention, biological vinegar and the system of biological tar, wherein said pyrolysis installation includes furnace shell and heating chamber,
The left end of described furnace shell offers fuel inlet and air inlet, offers at least one ash hole in the front side of furnace shell, in heating chamber
Inside being also equipped with furnace tube, described furnace tube is rotating to be fixed on furnace shell, is installed with in spiral distribution on the inwall of furnace tube
And some lifting blades that rotation direction is to the right, the left end at furnace shell is also installed with steam pipe and airduct, and the right-hand member of airduct stretches into furnace tube
In, the right-hand member of steam pipe inserts in airduct, and the right-hand member of steam pipe is positioned at outside airduct, the left end at furnace shell be also installed with into
Hopper, the lower end of described feed hopper is fixed with feed pipe, and the upper end of described feed pipe connects with feed hopper, and the lower end of feed pipe is stretched
In entering furnace tube and not contacting with furnace tube, the bottom of described furnace tube right-hand member offers slag notch, and the upside of furnace tube right-hand member offers gives vent to anger
Mouthful, the gas outlet of described furnace tube connects with the air inlet of cleaner unit.
Co-producing bio charcoal of the present invention, biological vinegar and the system of biological tar, wherein said furnace tube is the most downward-sloping, and stove
The axis of cylinder is 5 ° with the angle of horizontal plane.
Co-producing bio charcoal of the present invention, biological vinegar and the system of biological tar, wherein said pyrolysis installation includes furnace shell and heating chamber,
The bottom of described furnace shell is provided with 4 blow vents connected with heating chamber, and described 4 blow vents are from left to right along the bottom of furnace shell
Evenly distributed, 3 blow vents in described left side are passed through hot blast, and 1 blow vent on right side is passed through high-temperature steam, described heating chamber
Inside being provided with transmission carrier bar, described transmission carrier bar is fixedly mounted on furnace shell, the carrier bar of described transmission carrier bar uniformly offers many
Individual air-vent, the left upper end of described furnace shell is provided with feed hopper, and the discharging opening of described feed hopper is positioned at and transmits just going up of carrier bar left end
Side, the bottom righthand side of described furnace shell offers slag notch, and described slag notch is positioned at the underface transmitting carrier bar right-hand member, described furnace shell
Offering gas outlet on the upside of right-hand member, the gas outlet on described furnace shell connects with the air inlet of cleaner unit.
Co-producing bio charcoal of the present invention, biological vinegar and the system of biological tar, wherein said pyrolysis installation also includes air stove, institute
The hot-blast outlet stating air stove is connected with three blow vents in the left side of furnace shell lower end by pipeline, the steam (vapor) outlet of air stove and stove
1 blow vent connection on the right side of shell lower end.
Co-producing bio charcoal of the present invention, biological vinegar and the system of biological tar, wherein said transmission carrier bar is the most downward-sloping to be set
Put.
The system difference from prior art of co-producing bio charcoal of the present invention, biological vinegar and biological tar is that the present invention passes through to arrange
Pyrolysis installation, dust arrester, refrigerated separation tower and precipitator tower, after the agricultural leftover resource of straw being pyrolyzed by pyrolysis installation,
Obtain mixed gas, after mixed gas removing dust device dedusting, enter in refrigerated separation tower and condense, the condensed fluid obtained after condensation
Entering in precipitator tower and staticly settle, i.e. can get biological tar and biological vinegar, charcoal will be obtained after biomass pyrolytic by pyrolysis installation
Arrive.Therefore, the present invention can improve the utilization rate of living resources, it is to avoid causes air pollution.
Below in conjunction with the accompanying drawings the system of the co-producing bio charcoal of the present invention, biological vinegar and biological tar is described further.
Accompanying drawing explanation
Fig. 1 is the structural representation of the embodiment 1 of co-producing bio charcoal of the present invention, biological vinegar and biological tar；
Fig. 2 is the structural representation of the embodiment 2 of co-producing bio charcoal of the present invention, biological vinegar and biological tar；
Fig. 3 is the structural representation of the embodiment 3 of co-producing bio charcoal of the present invention, biological vinegar and biological tar.
Detailed description of the invention
Biomass resource divides with three classes according to big I: the first kind is fine particle thing, such as rice husk etc.；Equations of The Second Kind is straw etc.；
3rd class is the tiny branch tip etc.；The three below embodiment of the present invention is respectively used to process this three biolobic materials resource efficiently,
Obtain charcoal, biological vinegar and biological tar.
Embodiment 1
The present embodiment is for processing the tiny this kind of biomass resources of particulate matter such as rice husk.As it is shown in figure 1, co-producing bio charcoal of the present invention,
The system of biological vinegar and biological tar includes pyrolysis installation 10, cleaner unit 11, refrigerated separation tower 12 and precipitator tower 13.Precipitator tower
13 are vertically arranged, and precipitator tower 13 includes housing and inner chamber 14, the cone that inner chamber 14 is big up and small down, and the top of housing is offered
There is the charging aperture 15 connected with inner chamber 14, offer the biological vinegar outlet 17 connected with inner chamber 14 at the middle part of housing, at housing
Bottom offer connect with inner chamber 14 biological tar outlet 19, offer the lime-ash connected with inner chamber 14 in the bottom of housing
Outlet 18.The gas outlet of pyrolysis installation 10 connects with the air inlet of cleaner unit 11, the air outlet 20 of cleaner unit 11 and cooling point
Air inlet from tower 12 connects, and the condensate outlet of refrigerated separation tower 12 connects with the charging aperture 15 of precipitator tower 13.Cleaner unit
11 can use cyclone dust extractor or sack cleaner.
Precipitator tower 13 also includes the containing cavity 21 of cylinder in the present embodiment, and containing cavity 21 is positioned at the top of inner chamber 14, holds
Putting chamber 21 to connect with inner chamber 14, the charging aperture 15 of precipitator tower 13 connects with containing cavity 21, is further opened with giving up at the top of housing
Gas outlet 22, waste gas outlet 22 is connected with active carbon purifying device 25.
In the present embodiment, pyrolysis installation 10 includes heating furnace 23 and chamber furnaced 24.Heating furnace 23 includes furnace shell and heating chamber, adds
Hot chamber is up big and down small, the top in heating chamber be cylindrical, bottom for conical, be provided with heater in the furnace shell of heating furnace 23,
Heater can use electrical heating or gas heating or high-temperature steam heating device.The top of heating furnace 23 offers upper feeding
Mouthful, lower charging aperture is offered in the bottom of heating furnace 23, the bottom of heating furnace 23 offers air inlet, passes through at air inlet
Pipeline connects aerator 27.It is further opened with gas outlet at the top of heating furnace 23.Chamber furnaced 24 includes furnace shell and inner chamber,
The top of chamber furnaced 24 offers air inlet and gas outlet, offers discharging opening, going out of chamber furnaced 24 in the bottom of chamber furnaced 24
Material mouth is positioned at the top of the lower charging aperture of heating furnace 23, and the discharging opening of chamber furnaced 24 connects with the lower charging aperture of heating furnace 23,
The air inlet of chamber furnaced 24 connects with the gas outlet of heating furnace 23, and the gas outlet of chamber furnaced 24 connects with the air inlet of cleaner unit 11
Logical.The bottom of heating furnace 23 is further opened with steam inlet.
Rice husk in use, is first sent into heating intracavity, simultaneously in the upper feeding mouth that the top of heating furnace 23 is offered by this device
Being passed through air by the aerator 27 air inlet to the bottom of heating furnace 23, the heater of heating furnace 23 provides hot environment to make
Rice husk is pyrolyzed, and the rice husk after pyrolysis is entered by the gas outlet at heating furnace 23 top after being blown afloat by the air entered bottom heating furnace 23
Entering chamber furnaced 24, in chamber furnaced 24, the granule of non-carbonization sinks in chamber furnaced 24, has bottom chamber furnaced 24
Discharging opening enters the lower charging aperture of heating furnace 23 and is again pyrolyzed.The gas of formation after rice husk is pyrolyzed enters in cleaner unit 11,
Charcoal therein is separated by cleaner unit 11, and the gas after dedusting enters refrigerated separation tower 12 and is condensed into liquid, condensation
After the condensed fluid that obtains enter in precipitator tower 13 and staticly settle, biological vinegar outlet offered by biological vinegar from the middle part of precipitator tower 13 housing
17 obtain, and the biological tar outlet 19 that biological tar is offered from the bottom of precipitator tower 13 housing obtains.
Owing to the bottom of heating furnace is cone, and the discharging opening of chamber furnaced 24 is positioned at the top of lower charging aperture of heating furnace 23,
Make the connecting line of the two and angle (the i.e. axis of connecting line and connecting line and the mother of heating furnace connection of heating furnace 23
The angle of line) less than 45 °, thus avoid the granule quilt of the non-carbonization of the discharging opening entrance heating furnace of chamber furnaced 24
The air that aerator is passed through blows back.
The present embodiment can also be passed through steam, such that it is able to obtain the charcoal with micropore in the air inlet of heating furnace 23.
Embodiment 2
The present embodiment is used for processing this kind of biomass resources such as straw.As in figure 2 it is shown, co-producing bio charcoal of the present invention, biological vinegar and
The system of biological tar includes pyrolysis installation 10, cleaner unit 11, refrigerated separation tower 12 and precipitator tower 13.Precipitator tower 13 is vertical
Arranging, precipitator tower 13 includes housing and inner chamber 14, the cone that inner chamber 14 is big up and small down, and the top of housing offers with interior
The charging aperture 40 of chamber 14 connection, offers the biological vinegar outlet 44 connected with inner chamber 14, in the bottom of housing at the middle part of housing
Offer the biological tar outlet 42 connected with inner chamber 14, offer the lime-ash outlet 43 connected with inner chamber 14 in the bottom of housing.
The gas outlet of pyrolysis installation 10 connects with the air inlet of cleaner unit 11, the air outlet 45 of cleaner unit 11 and refrigerated separation tower 12
Air inlet connects, and the condensate outlet of refrigerated separation tower 12 connects with the charging aperture 40 of precipitator tower 13.Cleaner unit 11 can be adopted
With cyclone dust extractor or sack cleaner.
Precipitator tower 13 also includes the containing cavity 46 of cylinder in the present embodiment, and containing cavity 46 is positioned at the top of inner chamber 14, holds
Putting chamber 46 to connect with inner chamber 14, the charging aperture 40 of precipitator tower 13 connects with containing cavity 46, is further opened with giving up at the top of housing
Gas outlet (not shown), waste gas outlet is connected with active carbon purifying device (not shown).
In the present embodiment, pyrolysis installation 10 includes furnace shell and heating chamber 48, and the left end of furnace shell offers fuel inlet 49 and air inlet
50, at least one ash hole 51 is offered in the front side of furnace shell, in the present embodiment, ash hole has 3.In heating chamber 48 also
Furnace tube 52 is installed.Furnace tube 52 is rotating to be fixed on furnace shell, i.e. the two ends of furnace tube 52 are fixed on furnace shell by bearing block.
The inwall of furnace tube 52 is installed with in spiral distribution and rotation direction some lifting blade (not shown)s to the right, works as furnace tube
During 52 rotation, can be that the material in furnace tube 52 moves from left to right.Left end at furnace shell is also installed with steam pipe (figure
Not shown in) and airduct 55, the right-hand member of airduct 55 stretches in furnace tube 52, and the right-hand member of steam pipe inserts in airduct 55, and steams
The right-hand member of steam pipe is positioned at outside airduct 55.Left end at furnace shell is also installed with feed hopper 56, and the lower end of feed hopper 56 is fixed with
Feed pipe 57, the upper end of feed pipe 57 connects with feed hopper 56, in furnace tube 52 is stretched in the lower end of feed pipe 57 and not with furnace tube
52 contacts, during i.e. the lower end of feed pipe 57 tilts to stretch into the left end opening of furnace tube 52.The bottom of furnace tube 52 right-hand member offers out
Cinder notch 58, the upside of furnace tube 52 right-hand member offers gas outlet 59, and the gas outlet of furnace tube 52 connects with the air inlet of cleaner unit 11.
In the present embodiment, furnace tube 52 is the most downward-sloping, and the angle of the axis of furnace tube 52 and horizontal plane is 5 °.
This device is in use, it is necessary first to straw is carried out pre-treatment.The pre-treating technology of straw follows the steps below: 1,
Straw is carried out manually or mechanically bundling；2, the straw after bundling is carried out remove impurity process, remove the foreign material in straw；3, will
Crushed stalk after remove impurity；4, the stalk briquette after pulverizing；5, the straw after briquetting is carried out carbonization/activation processing.
The block straw obtained after above-mentioned PROCESS FOR TREATMENT adds feed hopper 56, and block straw is entered furnace tube by feed pipe 57
In 52, along with the rotation of furnace tube 52, move the most from left to right, in moving process, the fuel added in heating chamber 48
Producing high temperature, make straw be pyrolyzed, the gas obtained after straw pyrolysis is admitted in cleaner unit 11 along with the wind being passed through in airduct 55,
Charcoal therein is separated by cleaner unit 11, and the gas after dedusting enters refrigerated separation tower 12 and is condensed into liquid, condensation
After the condensed fluid that obtains enter in precipitator tower 13 and staticly settle, biological vinegar outlet offered by biological vinegar from the middle part of precipitator tower 13 housing
44 obtain, and the biological tar outlet 42 that biological tar is offered from the bottom of precipitator tower 13 housing obtains.Simultaneously by furnace tube 52
What the slag notch 58 of low order end was discharged is also charcoal.
Embodiment 3
The present embodiment is applicable to process this kind of biomass resources such as the tiny branch tip.As it is shown on figure 3, co-producing bio charcoal of the present invention,
The system of biological vinegar and biological tar includes pyrolysis installation 10, cleaner unit 11, refrigerated separation tower 12 and precipitator tower 13.Precipitator tower
13 are vertically arranged, and precipitator tower 13 includes housing and inner chamber 14, the cone that inner chamber 14 is big up and small down, and the top of housing is offered
There is the charging aperture 70 connected with inner chamber 14, offer the biological vinegar outlet 72 connected with inner chamber 14 at the middle part of housing, at housing
Bottom offer connect with inner chamber 14 biological tar outlet 74, offer the lime-ash connected with inner chamber 14 in the bottom of housing
Outlet 73.The gas outlet of pyrolysis installation 10 connects with the air inlet of cleaner unit 11, the air outlet 45 of cleaner unit 11 and cooling point
Air inlet from tower 12 connects, and the condensate outlet of refrigerated separation tower 12 connects with the charging aperture 70 of precipitator tower 13.Cleaner unit
11 can use cyclone dust extractor or sack cleaner.
Offer waste gas outlet 75 in the present embodiment on the lower end sidewall of refrigerated separation tower 12, waste gas outlet 75 by pipeline with
Active carbon purifying device (not shown) connects.Active carbon purifying device is used for oxysulfide, the nitrogen oxidation removing in waste gas
The pollutant such as thing, it is to avoid exhaust emission air.
Exhaust-gas treatment mode in the present embodiment can also use the processing mode provided in embodiment 1.I.e. precipitator tower also includes circle
The containing cavity of cylindricality, containing cavity is positioned at the top of inner chamber, containing cavity and inner space, the charging aperture of refrigerated separation tower and containing cavity
Connection, is further opened with waste gas outlet at the top of housing, and waste gas outlet is connected with active carbon purifying device.
In the present embodiment, pyrolysis installation 10 includes furnace shell and heating chamber.The bottom of furnace shell is provided with 4 ventilations connected with heating chamber
Mouthful, 4 blow vents are from left to right evenly distributed along the bottom of furnace shell, and 3 blow vents 78 in left side are passed through hot blast, the 1 of right side
Individual blow vent 79 is passed through high-temperature steam.Heating intracavity is provided with transmission carrier bar, transmits carrier bar and is fixedly mounted on furnace shell.Conveyer chain
Plate includes that driving shaft, driven shaft and carrier bar, driving shaft and driven shaft are all fixedly mounted on furnace shell by bearing, driving shaft and from
Moving axis be arranged in parallel, and is all installed with sprocket wheel on driving shaft and driven shaft, and carrier bar ringwise, and is arranged on sprocket wheel, chain
Multiple air-vent is uniformly offered on plate.Transmit the most downward-sloping setting of carrier bar of carrier bar.Driving shaft passes through reducing motor
Drive, drive carrier bar to rotate, thus realize the conveying of material on carrier bar.The left upper end of furnace shell is provided with feed hopper 81, feed hopper
The discharging opening of 81 is positioned at the surface transmitting carrier bar left end, and the bottom righthand side of furnace shell offers slag notch 82, and slag notch 82 is positioned at biography
Send the underface of carrier bar right-hand member.Gas outlet is offered, the gas outlet on furnace shell and the air inlet of cleaner unit 11 on the upside of the right-hand member of furnace shell
Connection.
Pyrolysis installation 10 in the present embodiment also includes air stove 83, and air stove 83 is by furnace shell, furnace chamber and heat exchanger tube (in figure
Not shown) composition, heat exchanger tube part in furnace chamber is presented in coil pipe, to increase heat exchange area.The bottom of furnace shell is also
Offering fuel inlet 86 and air inlet (not shown), wherein air inlet is connected with aerator (not shown).Stove
Ash hole 88 is offered in the bottom of shell.The top of furnace shell offers hot-blast outlet 89, and the two ends that heat exchanger tube 85 is positioned at outside furnace shell are respectively
Water inlet 90 and steam (vapor) outlet 91.After water is entered by the water inlet of heat exchanger tube 85, in furnace chamber 84, form high-temperature steam, then
Steam (vapor) outlet 91 is had to discharge.The hot-blast outlet of this air stove 83 is connected by three blow vents 78 of pipeline with the left side of furnace shell lower end
Logical, the steam (vapor) outlet of air stove 83 connects with 1 blow vent 79 on the right side of furnace shell lower end.
First tiny this kind of biomass resource of the branch tip is added feed hopper 81 by this device, and the tiny branch tip is from feed hopper
Fall in 81, fall and transmitting on carrier bar, along with the rotation of transmission carrier bar, move the most from left to right, in moving process,
3 blow vents 78 in left side are passed through hot blast, and 1 blow vent 79 on right side is passed through steam, makes the tiny branch tip be pyrolyzed, tiny
The gas outlet that the gas obtained after the pyrolysis of the branch tip is offered on the upside of the right-hand member of furnace shell is admitted to cleaner unit 11, and cleaner unit 11 will
Charcoal therein is separated, and the gas after dedusting enters refrigerated separation tower 12 and is condensed into liquid, the condensation obtained after condensation
Liquid enters in precipitator tower 13 and staticly settles, and biological vinegar is offered biological vinegar outlet 72 and obtained from the middle part of precipitator tower 13 housing, biological
The biological tar outlet 74 that tar is offered from the bottom of precipitator tower 13 housing obtains.Simultaneously by slagging tap that the bottom righthand side of furnace shell is offered
What mouth 82 was discharged is also charcoal.
Embodiment described above is only to be described the preferred embodiment of the present invention, not carries out the scope of the present invention
Limiting, on the premise of designing spirit without departing from the present invention, technical scheme is made by those of ordinary skill in the art
Various deformation and improvement, all should fall in the protection domain that claims of the present invention determines.
Claims (9)
1. a co-producing bio charcoal, biological vinegar and the system of biological tar, it is characterised in that: include pyrolysis installation, cleaner unit,
Refrigerated separation tower and precipitator tower, described precipitator tower is vertically arranged, and precipitator tower includes housing and inner chamber, the circle that inner chamber is big up and small down
Taper, the top of housing offers the charging aperture with inner space, offers the biology with inner space at the middle part of described housing
Vinegar exports, and offers the biological tar outlet with inner space in the bottom of housing, offers and inner space in the bottom of housing
Lime-ash outlet, the gas outlet of described pyrolysis installation connects with the air inlet of cleaner unit, the air outlet of cleaner unit and refrigerated separation tower
Air inlet connection, the condensate outlet of refrigerated separation tower connects with the charging aperture of precipitator tower, and described pyrolysis installation includes heating furnace
And chamber furnaced, described heating furnace includes furnace shell and heating chamber, and heating chamber is up big and down small, and the top in heating chamber is cylindrical, bottom
For cone, being provided with heater in the furnace shell of heating furnace, the top of heating furnace offers upper feeding mouth, under heating furnace
Portion offers lower charging aperture, and the bottom of heating furnace offers air inlet, is further opened with gas outlet at the top of heating furnace, described point
Include furnace shell and inner chamber from stove, offer air inlet and gas outlet at the top of chamber furnaced, offer discharging in the bottom of chamber furnaced
Mouthful, the discharging opening of described chamber furnaced is positioned at the top of the lower charging aperture of described heating furnace, and the discharging opening of described chamber furnaced and heating
The lower charging aperture connection of stove, the air inlet of chamber furnaced connects with the gas outlet of heating furnace, and the gas outlet of chamber furnaced is entered with cleaner unit
Air port connects.
Co-producing bio charcoal the most according to claim 1, biological vinegar and the system of biological tar, it is characterised in that: described heavy
Shallow lake tower also includes the containing cavity of cylinder, and described containing cavity is positioned at the top of inner chamber, containing cavity and inner space, entering of precipitator tower
Material mouth connects with containing cavity, is further opened with waste gas outlet at the top of housing.
Co-producing bio charcoal the most according to claim 2, biological vinegar and the system of biological tar, it is characterised in that: described useless
Gas outlet is connected with active carbon purifying device.
Co-producing bio charcoal the most according to claim 3, biological vinegar and the system of biological tar, it is characterised in that add described in:
The bottom of hot stove is further opened with steam inlet.
5. according to the co-producing bio charcoal described in claim 1 or 2 or 3, biological vinegar and the system of biological tar, it is characterised in that:
Described pyrolysis installation includes furnace shell and heating chamber, and the left end of described furnace shell offers fuel inlet and air inlet, in the front side of furnace shell
Offering at least one ash hole, be also equipped with furnace tube at heating intracavity, described furnace tube is rotating to be fixed on furnace shell, at stove
Being installed with in spiral distribution and rotation direction some lifting blades to the right on the inwall of cylinder, the left end at furnace shell is also installed with steaming
Steam pipe and airduct, the right-hand member of airduct stretches in furnace tube, and the right-hand member of steam pipe inserts in airduct, and the right-hand member of steam pipe is positioned at airduct
Outward, the left end at furnace shell is also installed with feed hopper, and the lower end of described feed hopper is fixed with feed pipe, described feed pipe upper
End connects with feed hopper, in furnace tube is stretched in the lower end of feed pipe and does not contacts with furnace tube, and the bottom of described furnace tube right-hand member offers out
Cinder notch, the upside of furnace tube right-hand member offers gas outlet, and the gas outlet of described furnace tube connects with the air inlet of cleaner unit.
Co-producing bio charcoal the most according to claim 5, biological vinegar and the system of biological tar, it is characterised in that: described stove
Cylinder is the most downward-sloping, and the angle of the axis of furnace tube and horizontal plane is 5 °.
7. according to the co-producing bio charcoal described in claim 1 or 2 or 3, biological vinegar and the system of biological tar, it is characterised in that:
Described pyrolysis installation includes furnace shell and heating chamber, and the bottom of described furnace shell is provided with 4 blow vents connected with heating chamber, described
4 blow vents are from left to right evenly distributed along the bottom of furnace shell, and 3 blow vents in described left side are passed through hot blast, 1 of right side
Blow vent is passed through high-temperature steam, and described heating intracavity is provided with transmission carrier bar, and described transmission carrier bar is fixedly mounted on furnace shell, institute
Stating to transmit and uniformly offer multiple air-vent on the carrier bar of carrier bar, the left upper end of described furnace shell is provided with feed hopper, described feed hopper
Discharging opening be positioned at transmit carrier bar left end surface, the bottom righthand side of described furnace shell offers slag notch, and described slag notch is positioned at biography
Send the underface of carrier bar right-hand member, on the upside of the right-hand member of described furnace shell, offer gas outlet, the gas outlet on described furnace shell and cleaner unit
Air inlet connects.
Co-producing bio charcoal the most according to claim 7, biological vinegar and the system of biological tar, it is characterised in that: described heat
Solving device and also include air stove, the hot-blast outlet of described air stove is connected by three blow vents of pipeline with the left side of furnace shell lower end
Logical, the steam (vapor) outlet of air stove connects with 1 blow vent on the right side of furnace shell lower end.
Co-producing bio charcoal the most according to claim 8, biological vinegar and the system of biological tar, it is characterised in that: described biography
Send carrier bar the most downward-sloping setting.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410246575.1A CN103980922B (en) | 2014-06-05 | 2014-06-05 | Co-producing bio charcoal, biological vinegar and the system of biological tar |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410246575.1A CN103980922B (en) | 2014-06-05 | 2014-06-05 | Co-producing bio charcoal, biological vinegar and the system of biological tar |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN103980922A CN103980922A (en) | 2014-08-13 |
| CN103980922B true CN103980922B (en) | 2017-01-04 |
Family
ID=51273095
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201410246575.1A Expired - Fee Related CN103980922B (en) | 2014-06-05 | 2014-06-05 | Co-producing bio charcoal, biological vinegar and the system of biological tar |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN103980922B (en) |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2002273171A (en) * | 2001-03-19 | 2002-09-24 | Meeting Room:Kk | White smoke treatment device attached to charcoal making apparatus |
| CN101955780A (en) * | 2010-09-17 | 2011-01-26 | 陕西亿鑫生物能源科技开发有限公司 | Co-production system and co-production method for biomass carbon, gas, wood tar and wood vinegar |
| CN103614154A (en) * | 2013-12-06 | 2014-03-05 | 广州迪森热能技术股份有限公司 | Ecological oil preparation system |
| CN203513582U (en) * | 2013-08-20 | 2014-04-02 | 合肥德博生物能源科技有限公司 | Biomass pyrolysis device |
| CN203976713U (en) * | 2014-06-05 | 2014-12-03 | 邹炎 | The system of co-producing bio charcoal, biological vinegar and biological tar |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US8927793B2 (en) * | 2011-07-29 | 2015-01-06 | Uop Llc | Processes for converting lignocellulosics to reduced acid pyrolysis oil |
-
2014
- 2014-06-05 CN CN201410246575.1A patent/CN103980922B/en not_active Expired - Fee Related
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2002273171A (en) * | 2001-03-19 | 2002-09-24 | Meeting Room:Kk | White smoke treatment device attached to charcoal making apparatus |
| CN101955780A (en) * | 2010-09-17 | 2011-01-26 | 陕西亿鑫生物能源科技开发有限公司 | Co-production system and co-production method for biomass carbon, gas, wood tar and wood vinegar |
| CN203513582U (en) * | 2013-08-20 | 2014-04-02 | 合肥德博生物能源科技有限公司 | Biomass pyrolysis device |
| CN103614154A (en) * | 2013-12-06 | 2014-03-05 | 广州迪森热能技术股份有限公司 | Ecological oil preparation system |
| CN203976713U (en) * | 2014-06-05 | 2014-12-03 | 邹炎 | The system of co-producing bio charcoal, biological vinegar and biological tar |
Also Published As
| Publication number | Publication date |
|---|---|
| CN103980922A (en) | 2014-08-13 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN104017590B (en) | A kind of agricultural-forestry biomass continuous pyrolysis charing method | |
| CN202530040U (en) | Continuous biomass dry-distillation carbonization apparatus | |
| CN102643657A (en) | Continuous biomass carbonization process | |
| CN103275739B (en) | High-efficiency straw carbonization device | |
| CN104861996B (en) | A kind of technique for biomass pyrolysis carbon gas oil polygenerations systeme | |
| CN104973597A (en) | Production method of active carbon | |
| CN106281397B (en) | Field biomass through pyrolysis oil refining apparatus based on solar energy heating and from heat supply | |
| CN105000557A (en) | Recycling production method for agricultural wastes | |
| CN105130520A (en) | Treatment method and equipment for vegetable and fruit waste | |
| CN103265964B (en) | Device for promoting reaction by direct contact between blast furnace slag particles and biomass particles | |
| CN105950195A (en) | Cocurrent downward circulating fluidized bed millisecond pyrolysis and liquefaction technology for biomass | |
| CN202808710U (en) | Ore catalyst bed biomass flash pyrolysis oil production device | |
| CN105036126A (en) | Device for recycling agricultural wastes | |
| CN104973598A (en) | Active carbon production apparatus | |
| CN104910935A (en) | Biomass carbon, gas, oil, liquid, heat, electricity poly-generation device and method | |
| CN103980922B (en) | Co-producing bio charcoal, biological vinegar and the system of biological tar | |
| CN105176564B (en) | A kind of hydrolysis baking pyrolysis roasting four-part form that couples prepares bio oil and the method and device of white carbon simultaneously | |
| CN106635111A (en) | Novel system for co-producing liquid fuel and biochar by biomass pyrolysis | |
| CN203976713U (en) | The system of co-producing bio charcoal, biological vinegar and biological tar | |
| CN113736496B (en) | Organic waste drying pyrolysis carbonization powder making system and method and heat and mass transfer ball | |
| CN103160297A (en) | Ore catalytic bed biomass fast pyrolysis oil-making device | |
| CN110093259A (en) | The system and method for handling small towns organic waste | |
| CN210030574U (en) | Vertical biomass pyrolysis reaction system | |
| CN206428186U (en) | A kind of charcoal preparation system | |
| CN208517346U (en) | A kind of continuous biomass fast thermal decomposition device |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| 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: 20170104 Termination date: 20190605 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |