CN107828456A - A kind of Bamboo leftover multiplexer and method - Google Patents
A kind of Bamboo leftover multiplexer and method Download PDFInfo
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- CN107828456A CN107828456A CN201711284808.7A CN201711284808A CN107828456A CN 107828456 A CN107828456 A CN 107828456A CN 201711284808 A CN201711284808 A CN 201711284808A CN 107828456 A CN107828456 A CN 107828456A
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- Prior art keywords
- bamboo
- leftover
- module
- bamboo charcoal
- combustion gas
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Classifications
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L5/00—Solid fuels
- C10L5/40—Solid fuels essentially based on materials of non-mineral origin
- C10L5/44—Solid fuels essentially based on materials of non-mineral origin on vegetable substances
- C10L5/442—Wood or forestry 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
-
- 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
- Y02E50/30—Fuel from waste, e.g. synthetic alcohol or diesel
Abstract
The invention discloses a kind of Bamboo leftover multiplexer and method, it is related to bamboo product production field, the device includes：Feedstock treating module, thermochemical conversion module, low nitrogen burning module and barbecue bamboo charcoal production module, Feedstock treating module is used to be pre-processed Bamboo leftover, thermochemical conversion module is used to the Bamboo leftover by pretreatment being converted to bamboo charcoal particle and biomass thermal combustion gas, low nitrogen burning module is used to fully be burnt biomass thermal combustion gas, and the bamboo charcoal particle after abundant burning is reconfigured shaping by barbecue bamboo charcoal production module.Due to Bamboo leftover being multiplexed, improve the utilization ratio of Bamboo leftover, simultaneously, biological fuel gas produces steam by low nitrogen burning can substitute the arcola of bamboo processing, environment protection emission, boiler exhaust gas is further used for drying system energy, realizes that using energy source optimizes, the bamboo charcoal of production further is made into roasted charcoal can produce huge economic value.
Description
Technical field
The present invention relates to bamboo product production field, more particularly to a kind of Bamboo leftover multiplexer and method.
Background technology
Now, resource has become focus of concern with economic sustainable development.The bamboo resource in China is rich
Richness, the title of " bamboo kingdom " is known as, the area and bamboo wood yield of bamboo, accounts for 1/3 of the world or so.But current Chinese bamboo processing
Utilization rate it is low, average utilization only has 40%.Such as ring, bamboo caused by after bamboo processing are end to end, bamboo branch and bamboo scraps discard
Thing, be generally used for the arcola fuel of bamboo processing process, or for traditional earth kiln charcoal processing, it is not energy efficient, economic benefit compared with
It is low.
Bamboo leftover is used as arcola fuel, and efficiency utilization rate is less than 50%, and easy over-emitting black exhaust, according to《Air
Prevention and cure of pollution action plan》Provide, most domestic place is strictly limited pollution arcola at present.Bamboo leftover utilizes
Traditional earth kiln technique charcoal processing, the energy do not make full use of, and can discharge a large amount of black smokes, pollute environment, and the rectification pair of environmentally friendly emphasis
One of as.
The content of the invention
The technical problem to be solved in the present invention is to provide a kind of Bamboo leftover multiplexer and method, solves existing skill
Roast bamboo charcoal production technology in art to fall behind, the technical problem that Bamboo leftover utilization ratio is low, environmental pollution is serious.
In order to solve the above-mentioned technical problem, the technical scheme is that：
A kind of Bamboo leftover multiplexer, including：Feedstock treating module, thermochemical conversion module, low nitrogen burning mould
Block and barbecue bamboo charcoal production module, the Feedstock treating module are used to be pre-processed Bamboo leftover, the heat chemistry
Modular converter is used to the Bamboo leftover by pretreatment being converted to bamboo charcoal particle and biomass thermal combustion gas, the low nitrogen combustion
Burn module to be used to fully be burnt biomass thermal combustion gas, the barbecue bamboo charcoal produces module by the bamboo charcoal after abundant burning
Grain reconfigures shaping.
Wherein, the Feedstock treating module includes disintegrating machine and Bamboo leftover drying oven, Bamboo leftover pass through
Crusher in crushing by Bamboo leftover drying oven into being dried after fritter bamboo material, then is transported to the thermochemical conversion mould
In block.
Wherein, the thermochemical conversion module is mixed suction gas-carbon cogeneration stove, remaining for pretreated bamboo to be processed
Thing pyrolytic gasification, obtain biomass thermal combustion gas and bamboo charcoal particle.
Wherein, the low nitrogen burning module includes deduster, boiler and burner, for biomass thermal combustion gas fully to be fired
Burn.
Wherein, the barbecue bamboo charcoal production module includes flour mill, batch mixer, screw extruder, roller briquetting machine and bamboo
Charcoal dryer, the barbecue bamboo charcoal production module are used to reconfigure bamboo charcoal particle as finished product bamboo charcoal.
A kind of Bamboo leftover multiplexing method, including：Bamboo leftover is pre-processed first, pre- place will be passed through
The product pyrolytic gasification of reason, afterwards fully burns the biomass thermal combustion gas of generation, and bamboo charcoal particle is reintegrated into shaping.
Wherein, process Bamboo leftover pre-processed includes：Bamboo leftover is first broken into fritter bamboo
Material, then fritter bamboo material is subjected to drying and arrived below water content set in advance.
Wherein, the process of the product pyrolytic gasification by pretreatment is included：The Bamboo leftover of pretreatment is conveyed
To mixed suction gas-carbon cogeneration stove, carry out pyrolytic gasification and react to obtain bamboo charcoal particle and biomass thermal combustion gas.
Wherein, the clean-burning process of biomass thermal combustion gas of generation is included：Biomass thermal combustion gas progress particle is gone
Remove, then be delivered to boiler and burnt, generate steam.
Wherein, bamboo charcoal particle is reintegrated to the process of shaping to be included：The bamboo charcoal particle of generation is milled, by bamboo charcoal
Powder adds bonding agent and hot water carries out batch mixing, then by extrusion forming, is finally dried to obtain bamboo charcoal finished product.
Using above-mentioned technical proposal, due to Bamboo leftover being multiplexed, the utilization of Bamboo leftover is improved
Efficiency, meanwhile, biological fuel gas produces steam by low nitrogen burning can substitute the arcola of bamboo processing, environment protection emission, boiler
Tail gas is further used for drying system energy, realizes that using energy source optimizes, the bamboo charcoal of production further is made into barbecue type
Charcoal can produce huge economic value.
Brief description of the drawings
Fig. 1 is the structural representation of Bamboo leftover multiplexer of the present invention；
Fig. 2 is the structural representation that suction gas-carbon cogeneration stove is mixed in the present invention.
In figure, 1- disintegrating machines, 2- Bamboo leftover drying ovens, 3- feeding bins, 4- belt material-feeding machines, the mixed suction gas charcoals of 5-
Coproduction stove, 51- bias fire grates, 52- break doctor blade devices, 53- char zones, 54- pyrolysis zones, 55- feeding seal valves, 56- combustion gas
Outlet, 6- air blowers, 7- dedusters, 8- high temperature draught fans, 9- low NOs, 10- air blowers, 11- boilers, 12- gas-distributing cylinders,
13- dedusters, 14- air-introduced machines, 15- chimneys, 16- flour mills, 17- batch mixers, 18- screw extruders, 19- roller briquetting machines,
20- dryers.
Embodiment
The embodiment of the present invention is described further below in conjunction with the accompanying drawings.Herein it should be noted that for
The explanation of these embodiments is used to help understand the present invention, but does not form limitation of the invention.It is in addition, disclosed below
As long as each embodiment of the invention in involved technical characteristic do not form conflict can each other and be mutually combined.
As the first embodiment of the present invention, a kind of Bamboo leftover multiplexer is proposed, as shown in figure 1, including：By
The Feedstock treating module that disintegrating machine 1 and Bamboo leftover drying oven 2 are formed, Bamboo leftover are transported from stockyard, poured into brokenly
Broken machine 1 is broken into fritter bamboo material, and disintegrating machine 1 can cause airborne dust unlike pulverizer, and disintegrating machine 1 in use may be used
Effectively to prevent airborne dust, after Bamboo leftover is fractured into below 10cm fritter bamboo material, fritter bamboo material is transported to
Bamboo leftover drying oven 2 is dried, and Bamboo leftover drying oven 2, which can dry fritter bamboo material to water content, to exist
Less than 20%.
Afterwards, fritter bamboo material is transported to feeding bin 3 and is transported to mixed suction gas charcoal by the belt material-feeding machine 4 of High angle
In coproduction stove 5, as shown in Fig. 2 mixed suction gas-carbon cogeneration stove 5 include eccentric fire grate 51, break doctor blade device 52, char zone 53,
Pyrolysis zone 54, feeding seal valve 55 and gas outlet 56, as shown in Figure 1, 2, suction gas-carbon cogeneration stove 5 are mixed respectively in char zone 53
Oxidant is conveyed by air blower 6 with pyrolysis zone 54, used using air as oxidant in the present embodiment, the use of oxidant
Amount is adjusted respectively according to the temperature of char zone 53 and pyrolysis zone 54, and is automatically controlled by controller, or uses server
Carry out remote control.Controller also controls the reaction temperature of char zone 53 and pyrolysis zone 54, wherein, the reaction temperature of pyrolysis zone 54
Scope between 400 degrees Celsius to 550 degrees Celsius, the range of reaction temperature of char zone 53 750 degrees Celsius to 850 degrees Celsius it
Between.The bottom of mixed suction gas-carbon cogeneration stove 5 is provided with eccentric fire grate 51, and break doctor blade device is provided with eccentric fire grate 51
52, bamboo charcoal coking can be prevented, ensures the uniformity of reaction.Continue as shown in Fig. 2 mixing the charging of suction gas-carbon cogeneration stove 5
Feeding seal valve 55 is set on mouth so that the biological fuel gas generated during the course of the reaction will not be revealed, while controller controls
The fuel gas temperature of gas outlet 56 effectively prevent the generation of tar and waste water between 250 degrees Celsius to 300 degrees Celsius.
Again as shown in figure 1, biological fuel gas caused by mixed suction gas-carbon cogeneration stove 5 sloughs bamboo charcoal particle by deduster 7
Thing, then be transported to by high temperature draught fan 8 in low NO 9, biological fuel gas and air blower 10 are defeated in low NO 9
The air sent is sufficiently mixed, and is fully burnt into boiler 11 afterwards, and the flue gas for generation of burning dries as Bamboo leftover
The thermal source of dry stove 2, by the proportioning of thermostatic control steam, to control the temperature of Bamboo leftover drying oven 2, temperature range exists
Between 150 degrees Celsius to 180 degrees Celsius, the tail gas after drying is discharged into chimney after the processing of deduster 13 by air-introduced machine 14
15；The steam of burning generation enters gas-distributing cylinder 12, and a part is used for bamboo charcoal finished product drying machine thermal source, and others are used as bamboo processing factory
Other use energy.
Continue as shown in figure 1, sloughing bamboo charcoal from bamboo charcoal particle caused by mixed suction gas-carbon cogeneration stove 5 and via deduster 7
Particulate matter is polished into bamboo carbon powder by flour mill 16, and the particle diameter of bamboo carbon powder is 60 to 100 mesh, subsequently into batch mixer 17.
Weight is added according to bamboo carbon powder, is quantitatively adding 3%~5% binding agent, adds 15%~30% hot water, hot water temperature's control
System stirs 45 minutes at 40~60 degrees Celsius.Subsequently into screw extruder 18, pass through roller press briquetting after being pressed further by batch mixing
Roasted charcoal is made in machine 19.Finally, roasted charcoal product, which enters in dryer 20, is dried to moisture below 5%, and dryer makes
The steam produced by the use of biological mass gas burnnig boiler 14 is as thermal source, and the temperature control of dryer is at 60 to 80 degrees Celsius.So as to obtain
The bamboo charcoal structure of shaping.
The high-efficiency environment friendly that the present embodiment realizes Bamboo leftover utilizes, and roasted charcoal, which is made, in the bamboo charcoal of production to produce
Raw huge economic value, biological fuel gas produces steam by low nitrogen burning can substitute the arcola of bamboo processing, environmental protection row
Put, boiler exhaust gas is further used for drying system energy, realizes that using energy source optimizes.By the process system of the present invention, build
If serving the energy, environment and the bamboo of ecological construction circulation Industry Model from Bamboo leftover utilization, make with low-carbon
Economy is the Recycling Economy System of core.
As the second embodiment of the present invention, propose that a kind of bamboo processing corresponding with Bamboo leftover multiplexer is surplus
Excess multiplexing method, including：
Step S1：After Bamboo leftover is broken into below 10cm fritter bamboo material, fritter bamboo material is dried into dryer
Do below fixed moisture；I.e. water content is below 20%.
Step S2：Product after drying is pyrolyzed by high angle belt conveyer conveyer into mixed suction gas-carbon cogeneration stove
Gasification reaction, generate biomass thermal combustion gas and bamboo charcoal particle；
Afterwards, fritter bamboo material is transported to feeding bin 3 and is transported to mixed suction gas charcoal by the belt material-feeding machine 4 of High angle
In coproduction stove 5, mixed suction gas-carbon cogeneration stove 5 includes eccentric fire grate 51, break doctor blade device 52, char zone 53, pyrolysis zone 54, entered
Expect sealing valve 55 and gas outlet 56, it is defeated by air blower 6 in char zone 53 and pyrolysis zone 54 respectively to mix suction gas-carbon cogeneration stove 5
Send oxidant, used in the present embodiment using air as oxidant, the usage amount of oxidant is according to char zone 53 and pyrolysis zone
54 temperature is adjusted respectively, and is automatically controlled by controller, or carries out remote control using server.Controller is also controlled
The reaction temperature of char zone 53 and pyrolysis zone 54 processed, wherein, the range of reaction temperature of pyrolysis zone 54 is taken the photograph at 400 degrees Celsius to 550
Between family name's degree, the range of reaction temperature of char zone 53 is between 750 degrees Celsius to 850 degrees Celsius.Mixed suction gas-carbon cogeneration stove 5
Bottom is provided with eccentric fire grate 51, and break doctor blade device 52 is provided with eccentric fire grate 51, can prevent bamboo charcoal coking, ensures
The uniformity of reaction.Feeding seal valve 55 is set on the charging aperture of mixed suction gas-carbon cogeneration stove 5 so that give birth to during the course of the reaction
Into biological fuel gas will not reveal, while controller control gas outlet 56 fuel gas temperature it is Celsius at 250 degrees Celsius to 300
Between degree, the generation of tar and waste water effectively prevent.
Step S3：Biomass thermal combustion gas is transported to after cyclone dust collectors separate bamboo charcoal particle by high temperature draught fan
The low NO of biological mass gas burnnig boiler；
Step S3 '：Biological fuel gas is burnt in biological mass gas burnnig boiler by reasonable wind distribution, and the steam of production is used respectively
In bamboo charcoal finished product drying and bamboo charcoal processing factory energy.
Biological fuel gas caused by mixed suction gas-carbon cogeneration stove 5 sloughs bamboo charcoal particle thing by deduster 7, then passes through high temperature
Air-introduced machine 8 is transported in low NO 9, and biological fuel gas and the air that air blower 10 conveys are abundant in low NO 9
Mixing, is fully burnt into boiler 11 afterwards, the thermal source of the flue gas of generation of burning as Bamboo leftover drying oven 2,
By the proportioning of thermostatic control steam, to control the temperature of Bamboo leftover drying oven 2, temperature range at 150 degrees Celsius extremely
Between 180 degrees Celsius, the tail gas after drying is discharged into chimney 15 after the processing of deduster 13 by air-introduced machine 14；Burning generation
Steam enter gas-distributing cylinder 12, a part is used for bamboo charcoal finished product drying machine thermal source, other to be used as bamboo processing factory other use energy.
Step S4：The bamboo charcoal particle that the deduster 7 of the bamboo charcoal particle sum of mixed suction gas-carbon cogeneration stove production is deviate from passes through gas
Power is transported in flour mill, is ground into bamboo carbon powder of the particle diameter in 60~100 mesh；
Step S4 '：Bamboo carbon powder in batch mixer, add a certain proportion of binding agent and hot water and be stirred batch mixing；
Step S4 "：Well mixed material enters roller briquetting machine after extruding mixing, bamboo is made by screw extruder
Charcoal finished product；
Step S4 " '：Bamboo charcoal finished product dries moisture in dryer.
Wherein, dryer uses in step S3 ' caused steam as thermal source.
Using above-mentioned technical proposal, due to Bamboo leftover being multiplexed, the utilization of Bamboo leftover is improved
Efficiency, meanwhile, biological fuel gas produces steam by low nitrogen burning can substitute the arcola of bamboo processing, environment protection emission, boiler
Tail gas is further used for drying system energy, realizes that using energy source optimizes, the bamboo charcoal of production further is made into barbecue type
Charcoal can produce huge economic value.
Embodiments of the present invention are explained in detail above in association with accompanying drawing, but the invention is not restricted to described implementation
Mode.For a person skilled in the art, in the case where not departing from the principle of the invention and spirit, to these embodiments
A variety of change, modification, replacement and modification are carried out, are still fallen within protection scope of the present invention.
Claims (10)
- A kind of 1. Bamboo leftover multiplexer, it is characterised in that including：It is Feedstock treating module, thermochemical conversion module, low Nitrogen combustion module and barbecue bamboo charcoal production module, the Feedstock treating module are used to be pre-processed Bamboo leftover, institute Thermochemical conversion module is stated to be used to the Bamboo leftover by pretreatment being converted to bamboo charcoal particle and biomass thermal combustion gas, institute State low nitrogen burning module to be used to fully be burnt biomass thermal combustion gas, after the barbecue bamboo charcoal production module will fully burn Bamboo charcoal particle reconfigure shaping.
- 2. Bamboo leftover multiplexer according to claim 1, it is characterised in that the Feedstock treating module includes Disintegrating machine and Bamboo leftover drying oven, Bamboo leftover are surplus into being processed by bamboo after fritter bamboo material by crusher in crushing Excess drying oven is dried, then is transported in the thermochemical conversion module.
- 3. Bamboo leftover multiplexer according to claim 1, it is characterised in that：The thermochemical conversion module is Mixed suction gas-carbon cogeneration stove, for by pretreated Bamboo leftover pyrolytic gasification, obtaining biomass thermal combustion gas and bamboo charcoal Particle.
- 4. Bamboo leftover multiplexer according to claim 1, it is characterised in that：The low nitrogen burning module includes Deduster, boiler and burner, for biomass thermal combustion gas fully to be burnt.
- 5. Bamboo leftover multiplexer according to claim 1, it is characterised in that：The barbecue bamboo charcoal production module Including flour mill, batch mixer, screw extruder, roller briquetting machine and bamboo charcoal dryer, the barbecue bamboo charcoal production module is used for Bamboo charcoal particle is reconfigured as finished product bamboo charcoal.
- A kind of 6. Bamboo leftover multiplexing method, it is characterised in that including：Bamboo leftover is pre-processed first, By the product pyrolytic gasification by pretreatment, the biomass thermal combustion gas of generation is fully burnt afterwards, bamboo charcoal particle is again whole Synthesis type.
- 7. Bamboo leftover multiplexing method according to claim 6, it is characterised in that carry out Bamboo leftover pre- The process of processing includes：Bamboo leftover is first broken into fritter bamboo material, then fritter bamboo material is subjected to drying to presetting Water content below.
- 8. Bamboo leftover multiplexing method according to claim 6, it is characterised in that by the product heat by pretreatment The process of solution gasification includes：The Bamboo leftover of pretreatment is delivered to mixed suction gas-carbon cogeneration stove, it is anti-to carry out pyrolytic gasification Bamboo charcoal particle and biomass thermal combustion gas should be obtained.
- 9. Bamboo leftover multiplexing method according to claim 6, it is characterised in that by the biomass thermal combustion gas of generation Clean-burning process includes：Biomass thermal combustion gas is subjected to particle removal, then is delivered to boiler and is burnt, generates steam.
- 10. Bamboo leftover multiplexing method according to claim 6, it is characterised in that reintegrate bamboo charcoal particle The process of shaping includes：The bamboo charcoal particle of generation is milled, bamboo carbon powder is added into bonding agent and hot water carries out batch mixing, then By extrusion forming, finally dried to obtain bamboo charcoal finished product.
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| Application Number | Priority Date | Filing Date | Title |
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| CN201711284808.7A CN107828456A (en) | 2017-12-07 | 2017-12-07 | A kind of Bamboo leftover multiplexer and method |
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| CN201711284808.7A CN107828456A (en) | 2017-12-07 | 2017-12-07 | A kind of Bamboo leftover multiplexer and method |
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| CN201711284808.7A Pending CN107828456A (en) | 2017-12-07 | 2017-12-07 | A kind of Bamboo leftover multiplexer and method |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
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| CN108622876A (en) * | 2018-06-29 | 2018-10-09 | 临安新能生物科技有限公司 | Pollution-free bamboo charcoal production line |
| CN110682381A (en) * | 2019-11-05 | 2020-01-14 | 宁波奉化万米电子科技有限公司 | Preparation equipment for biological carbon far infrared material |
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Application publication date: 20180323 |