CN107446601A - Biomass carbonated cogeneration facility - Google Patents
Biomass carbonated cogeneration facility Download PDFInfo
- Publication number
- CN107446601A CN107446601A CN201610369512.4A CN201610369512A CN107446601A CN 107446601 A CN107446601 A CN 107446601A CN 201610369512 A CN201610369512 A CN 201610369512A CN 107446601 A CN107446601 A CN 107446601A
- Authority
- CN
- China
- Prior art keywords
- cavity
- housing
- retracting device
- cogeneration facility
- retort
- 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.)
- Pending
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
- C10B53/00—Destructive distillation, specially adapted for particular solid raw materials or solid raw materials in special form
- C10B53/02—Destructive distillation, specially adapted for particular solid raw materials or solid raw materials in special form of cellulose-containing material
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
- C10B57/00—Other carbonising or coking processes; Features of destructive distillation processes in general
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10C—WORKING-UP PITCH, ASPHALT, BITUMEN, TAR; PYROLIGNEOUS ACID
- C10C5/00—Production of pyroligneous acid distillation of wood, dry distillation of organic waste
-
- 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
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Materials Engineering (AREA)
- Organic Chemistry (AREA)
- Life Sciences & Earth Sciences (AREA)
- Wood Science & Technology (AREA)
- Devices For Medical Bathing And Washing (AREA)
Abstract
The present invention proposes a kind of biomass carbonated cogeneration facility, including a retort, the first retracting device being connected with the retort, and the second retracting device being connected with first retracting device, the side of the retort is provided with a heater, first retracting device includes a closed housing, extend through the water pipe in the housing and the first accumulator tank located at the housing bottom, the bottom of the housing forms a funnel relative with the first accumulator tank, second retracting device includes an at least cavity, filter in cavity, shower nozzle in cavity and the second accumulator tank below cavity, the bottom of the cavity forms a funnel corresponding with the second accumulator tank.The biomass carbonated cogeneration facility, the recycling of heat can be focused on, whole process can be realized pollution-free to greatest extent using the energy contained in biomass.
Description
Technical field
The present invention relates to a kind of biomass carbonated cogeneration facility.
Background technology
At present, as the continuous reduction of the disposable energy such as coal, oil, natural gas, the mankind focus more on out
Send out and utilize various new energy.Biomass is as a kind of regenerative resource, its supplement energy as fossil energy
Source, causing the extensive concern of people.Low-grade biomass energy is converted into high-grade energy, at present
Main path includes gasification, liquefaction, charing and Direct-Combustion Technology.Charing obtains charcoal rate height, skill due to it
Art is more ripe, is a kind of very potential transformation technology.
At present, common biomass carbonated method mainly has：Carbonizing kiln, interval charring, closing vexed tank charcoal
Change method and the method for destructive distillation, but its carbonization time is grown, automaticity is low, and carbonization product is of low quality,
The problems such as production environment is severe.Biomass pyrolytic carbonizes generation of the process along with bio oil and combustible gas, wood
The distillates such as tar, pyrolkigneous liquid, alcohol, ester are important industrial chemicals, while can be carbonized by adjustment
Various operation data optimized product structures in journey, existing carbonization device have ignored this goodness, base
Originally it is to take emptying process, that is, polluting environment, waste of resource, these problems all limit Biomass Industry again
Develop in a healthy way.
The content of the invention
The present invention proposes a kind of biomass carbonated cogeneration facility, solves asking for the wasting of resources in the prior art etc.
Topic.
The technical proposal of the invention is realized in this way：
A kind of biomass carbonated cogeneration facility, including a retort, be connected with the retort first recovery dress
The second retracting device put and be connected with first retracting device, the side of the retort are provided with a heating
Device, first retracting device include a closed housing, extend through the water pipe in the housing and set
The first accumulator tank in the housing bottom, the bottom of the housing form a funnel relative with the first accumulator tank,
Second retracting device include an at least cavity, the filter in cavity, the shower nozzle in cavity and
The second accumulator tank below cavity, the bottom of the cavity form a funnel corresponding with the second accumulator tank.
Beneficial effects of the present invention are：
Biomass carbonated cogeneration facility in the present invention, the energy contained in biomass can be utilized to greatest extent
Amount, focuses on the recycling of heat, and whole process can realize pollution-free, automation mechanized operation, is preparing biology
Also liquid holdup thing has been obtained while matter charcoal, it there can be good popularization as high-quality industrial chemicals
Property and very high use value.
Brief description of the drawings
In order to illustrate more clearly about the embodiment of the present invention or technical scheme of the prior art, below will be to implementing
The required accompanying drawing used is briefly described in example or description of the prior art, it should be apparent that, describe below
In accompanying drawing be only some embodiments of the present invention, for those of ordinary skill in the art, do not paying
On the premise of going out creative work, other accompanying drawings can also be obtained according to these accompanying drawings.
Fig. 1 is the structural representation of the biomass carbonated cogeneration facility of the present invention.
In figure：
100th, biomass carbonated cogeneration facility；10th, retort；20th, the first retracting device；30th, second time
Receiving apparatus；11st, cylinder；12nd, lid；13rd, objective table；15th, heater；40th, temperature display fills
Put；50th, sensor；60th, the first body；61st, control valve；21st, housing；22nd, water pipe；23rd,
One accumulator tank；25th, funnel；31st, cavity；32nd, filter；33rd, shower nozzle；310th, the first cavity；311、
Second cavity；312nd, the 3rd cavity；35th, the second accumulator tank；70th, water pump；80th, temperature control equipment；
36th, the second body；37th, the 3rd body；38th, the 4th body；39th, the 5th body；80th, suction fan；
90th, chimney；92nd, support member.
Embodiment
Below in conjunction with the accompanying drawing in the embodiment of the present invention, the technical scheme in the embodiment of the present invention is carried out clear
Chu, it is fully described by, it is clear that described embodiment is only part of the embodiment of the present invention, rather than
Whole embodiments.Based on the embodiment in the present invention, those of ordinary skill in the art are not making creation
Property work under the premise of the every other embodiment that is obtained, belong to the scope of protection of the invention.
As shown in figure 1, the biomass carbonated cogeneration facility 100 includes a retort 10 and the retort 10
First retracting device 20 of connection and the second retracting device 30 being connected with first retracting device 20.
The retort 10 includes the cylinder 11 of a top end opening and is covered on a lid on the top of cylinder 11
12.The lid 12 is removable installed on the cylinder 11.Bottom in the cylinder 11 is provided with a grid
The objective table 13 of shape, for carrying biomass material.The side of the cylinder 11 is provided with a heater 15,
Make its charing to carry out heating to the biomass material in retort 10.The outside of the cylinder 11 is additionally provided with
One temperature indicating device 40.The lid 12 is provided with a sensor 50, and the bottom of the sensor 50 is stretched into
To cylinder 11, its top is exposed on lid 12.The sensor 50 passes through with temperature indicating device 40
Wire electrically connects.Temperature in retort 10 is sensed by the sensor 50 and passes through temperature indicating device 40 again
Show.
The bottom of first retracting device 20 is connected by one first body 60 with the bottom of retort 10,
And it is provided with control valve 61 with first body 60.It is tower-like closed that first retracting device 20 includes one
Housing 21, the water pipe 22 that is arranged in the housing 21 and the first accumulator tank located at the bottom of housing 21
23.The bottom of the housing 21 forms a funnel 25.First accumulator tank 23 is located under the funnel 25
Side.In this implementation, the water pipe 22 is snakelike, its extension of longitudinally reciprocal bending along housing 21.Specifically
During implementation, the structure of the water pipe 22 is not limited to the case for this embodiment, and it is alternatively spiral shape or other shapes
Shape.One end of the water pipe 22 is located at the top of housing 21, as its water inlet；The other end is located at housing 21
Bottom, as its delivery port.
Second retracting device 30 includes three cavitys 31, the filter 32 in each cavity 31, is located at
Shower nozzle 33 in each cavity 31 and the second accumulator tank 35 located at each lower section of cavity 31.Three cavitys
31 are arranged side by side, and it includes the first cavity 310, the second cavity 311 and the 3rd cavity 312.Each cavity
31 bottom forms a funnel.Second accumulator tank 35 is located at the lower section of each funnel.Second accumulator tank
35 side is connected with a water pump 70 by water pipe.The water pump 70 is connected by water pipe with each shower nozzle 33.Institute
The bottom for stating the first cavity 310 is connected by the second body 36 with the top of housing 21.Second body 36
Middle part be connected with a temperature control equipment 80, the front side of the temperature control equipment 80 is provided with a valve.This
The top of one cavity 310 is connected by the 3rd body 37 with the top of the second cavity 311, second cavity 311
Bottom be connected by the 4th body 38 with the bottom of the 3rd cavity 312.Each cavity 310 is Longitudinal extending
Strip, be provided with three filters 32 at equal intervals in it.Each gear of filter 32 is in cavity 31, and by chamber
It is divided into equally spaced three chambers in body 31.The mesh of each filter 32 is 1mm.It is provided with each cavity 31
One shower nozzle 33.
The top of 3rd cavity 312 is connected by the 5th body 39 with a suction fan 80.The air-breathing
The gas outlet of fan 80 is connected with a chimney 90.
The gasification of biomass combined production device 100 also includes being located at the first retracting device 20 and the second retracting device 30
One support member 92 of lower section.Three of the housing 21 of first retracting device 20, the second retracting device 30
Cavity 31 and suction fan 80 are on the support member 92, the funnel 25 and each cavity 31 of the lower section of housing 21
The funnel of lower section is stretched into support member 92.First accumulator tank 35, the second accumulator tank 35 and water pump 70 are received
It is dissolved in the support member 92.
In use, by biomass material in retort 10 and on objective table 13, filled by heating
Putting 15 makes biomass material be carbonized in retort 10.First pipe is passed through by the flue gas generated in retort 10
Body 60 is entered in the first retracting device 20, partly via the cold water in the water pipe on the first retracting device 20
After being cooled down, the pyrolkigneous liquid formed after cooling is collected by the first accumulator tank 23；Remaining flue gas passes through second
In each cavity of retracting device 30, spray to formation network of rivers cooling on filter 32, formed via shower nozzle 33
Pyrolkigneous liquid collected by the second accumulator tank 35.The liquid such as the pyrolkigneous liquid and water that are collected into the second accumulator tank 35
Absorbed by water pump 70 and sprayed again by shower nozzle 33 to each cavity, reciprocal cooling recovery is pure so as to extract
Net pyrolkigneous liquid.Unnecessary flue gas is absorbed into chimney discharge via suction fan 80.
The biomass carbonated cogeneration facility 100, the energy contained in biomass, note can be utilized to greatest extent
The recycling for the amount of reheating, whole process can realize pollution-free, automation mechanized operation, prepare biomass carbon
Liquid holdup thing is also obtained simultaneously, it can be as high-quality industrial chemicals, with good generalization and very
High use value.
When it is implemented, the number of the cavity 31 is not limited by the present embodiment, it can be three, also may be used
It can also be one for two.
The foregoing is merely illustrative of the preferred embodiments of the present invention, is not intended to limit the invention, all in this hair
Within bright spirit and principle, any modification, equivalent substitution and improvements made etc., this hair should be included in
Within bright protection domain.
Claims (8)
- A kind of 1. biomass carbonated cogeneration facility, it is characterised in that：Connect including a retort, with the retort The first retracting device connect and the second retracting device being connected with first retracting device, the retort Side is provided with a heater, and first retracting device includes a closed housing, extended through located at the shell Internal water pipe and the first accumulator tank located at the housing bottom, the bottom of the housing form one and first time The relative funnel of groove is received, second retracting device includes an at least cavity, the filter in cavity, set In the shower nozzle in cavity and the second accumulator tank below cavity, the bottom of the cavity forms one and second Funnel corresponding to accumulator tank.
- 2. biomass carbonated cogeneration facility as claimed in claim 1, it is characterised in that：The retort Outside is additionally provided with a temperature indicating device, and the top of the retort electrically connects provided with one with temperature indicating device Sensor.
- 3. biomass carbonated cogeneration facility as claimed in claim 1 or 2, it is characterised in that：The water pipe To be snakelike, and extending along the longitudinally reciprocal bending of housing, one end of the water pipe is located at the top of housing, as Its water inlet；The other end is located at the bottom of housing, as its delivery port.
- 4. biomass carbonated cogeneration facility as claimed in claim 1, it is characterised in that：Second recovery The side of groove is connected with a water pump by a water pipe, and the water pump is connected by water pipe with each shower nozzle.
- 5. biomass carbonated cogeneration facility as claimed in claim 1, it is characterised in that：In the cavity etc. Three filters are interval with, each filter gear will be divided into equally spaced three chambers in cavity in cavity Room, each cavity is interior to be provided with a shower nozzle.
- 6. biomass carbonated cogeneration facility as claimed in claim 1, it is characterised in that：The net of the filter Hole is 1mm.
- 7. biomass carbonated cogeneration facility as claimed in claim 1, it is characterised in that：The cavity is three Individual, it includes the first cavity, the second cavity and the 3rd cavity being arranged side by side, the bottom of first cavity Connected by the top of the second body and housing, a temperature control equipment be connected with the middle part of second body, The front side of the temperature control equipment is provided with a valve, and the top of first cavity passes through the 3rd body and the second chamber The top connection of body, the bottom of second cavity is connected by the 4th body with the bottom of the 3rd cavity.
- 8. biomass carbonated cogeneration facility as claimed in claim 7, it is characterised in that：3rd cavity Top be connected by the 5th body with a suction fan, the gas outlet of the suction fan is connected with a chimney.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610369512.4A CN107446601A (en) | 2016-05-30 | 2016-05-30 | Biomass carbonated cogeneration facility |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610369512.4A CN107446601A (en) | 2016-05-30 | 2016-05-30 | Biomass carbonated cogeneration facility |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN107446601A true CN107446601A (en) | 2017-12-08 |
Family
ID=60484839
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201610369512.4A Pending CN107446601A (en) | 2016-05-30 | 2016-05-30 | Biomass carbonated cogeneration facility |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN107446601A (en) |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0578503A1 (en) * | 1992-07-10 | 1994-01-12 | Hiroshi Shimizu | Apparatus for pyrolizing organic waste matter |
| CN103992805A (en) * | 2014-04-29 | 2014-08-20 | 图们市龙泉农工贸有限公司 | Production equipment and production method for charcoal, tar, wood vinegar and charcoal gas |
| CN204039318U (en) * | 2014-04-09 | 2014-12-24 | 曲维祥 | Many autoclaves effective botanic charred furnace |
-
2016
- 2016-05-30 CN CN201610369512.4A patent/CN107446601A/en active Pending
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0578503A1 (en) * | 1992-07-10 | 1994-01-12 | Hiroshi Shimizu | Apparatus for pyrolizing organic waste matter |
| CN204039318U (en) * | 2014-04-09 | 2014-12-24 | 曲维祥 | Many autoclaves effective botanic charred furnace |
| CN103992805A (en) * | 2014-04-29 | 2014-08-20 | 图们市龙泉农工贸有限公司 | Production equipment and production method for charcoal, tar, wood vinegar and charcoal gas |
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| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20171208 |
|
| RJ01 | Rejection of invention patent application after publication |