CN108424772A - Biogas, charcoal, fertilizer, acetic acid, the multi-joint-production apparatus of heat and its method - Google Patents
Biogas, charcoal, fertilizer, acetic acid, the multi-joint-production apparatus of heat and its method Download PDFInfo
- Publication number
- CN108424772A CN108424772A CN201810217720.1A CN201810217720A CN108424772A CN 108424772 A CN108424772 A CN 108424772A CN 201810217720 A CN201810217720 A CN 201810217720A CN 108424772 A CN108424772 A CN 108424772A
- Authority
- CN
- China
- Prior art keywords
- charcoal
- combustion gas
- delivery outlet
- furnace body
- heat
- 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
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B32/00—Carbon; Compounds thereof
- C01B32/30—Active carbon
- C01B32/312—Preparation
- C01B32/318—Preparation characterised by the starting materials
- C01B32/324—Preparation characterised by the starting materials from waste materials, e.g. tyres or spent sulfite pulp liquor
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B32/00—Carbon; Compounds thereof
- C01B32/30—Active carbon
- C01B32/312—Preparation
- C01B32/336—Preparation characterised by gaseous activating agents
-
- C—CHEMISTRY; METALLURGY
- C05—FERTILISERS; MANUFACTURE THEREOF
- C05D—INORGANIC FERTILISERS NOT COVERED BY SUBCLASSES C05B, C05C; FERTILISERS PRODUCING CARBON DIOXIDE
- C05D9/00—Other inorganic fertilisers
-
- 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
- C10B1/00—Retorts
- C10B1/10—Rotary retorts
-
- 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
-
- 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
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/10—Process efficiency
- Y02P20/129—Energy recovery, e.g. by cogeneration, H2recovery or pressure recovery turbines
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Organic Chemistry (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Materials Engineering (AREA)
- Inorganic Chemistry (AREA)
- Environmental & Geological Engineering (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Life Sciences & Earth Sciences (AREA)
- Wood Science & Technology (AREA)
- Fertilizers (AREA)
- Processing Of Solid Wastes (AREA)
Abstract
The invention discloses a kind of biogas, the multi-joint-production apparatus of charcoal, fertilizer, acetic acid, heat.Package unit feeds by biomass, is carbonized, produces biological fuel gas, and charcoal processing, extraction biomass acetic acid, preparing carbon-based fertilizer, waste heat recovery steam etc., several parts form.All recycling can be used for power generation or heat supply to fuel gas during carbonization, carbon-based fertilizer can be made for improveing soil in charcoal, activated carbon can also be made, for purifying air, the biomass acetic acid of extraction can be made herbicide and substitute glyphosate etc., chemical pesticide can also be substituted, people is eliminated and the pesticide residue in vegetables and fruits is worried;Steam is used for heat supply, substitutes coal or natural gas.Whole process zero emission and pollution, high added value, sustainable development.
Description
Technical field
The present invention relates to a kind of biomass multi-production device more particularly to a kind of biogas, charcoal, fertilizer, acetic acid, heat it is more
Combined production device.
Background technology
It is zero-emission there was only the carbon of biomass in new energy.So being favored by countries in the world.However regenerative resource is given birth to
The popularization of substance, countries in the world are all to lean on government subsidy, China no exception.How can just enable regenerative resource have through
Benefit of helping is global scientific and technical personnel all in the especially big problem of exploration.Then everybody common recognition is;Implement Poly-generation to improve
Economic benefit;But this concept of Poly-generation has carried at least 10 years, and there has been no the industrialization devices of Poly-generation so far.It can be seen that really
It is big to implement difficulty.
The device of the present invention does not burn directly, without chimney, zero-emission." gas " is combustion gas, can be supplied to boiler combustion
It burns;" liquid " is made of tar and vinegar liquid, and biomass pesticides are manufactured after extraction, can export trade earn foreign exchange;" solid " is high-quality activity
Charcoal or charcoal base manure, more there is economic value, realize real zero-emission.
Invention content:
The purpose of the present invention is overcome the deficiencies of the prior art and provide a kind of biogas, charcoal, fertilizer, acetic acid, heat it is multi-joint
Produce device.The technical solution that the present invention specifically uses is as follows:
The multi-joint-production apparatus of a kind of biogas, charcoal, fertilizer, acetic acid, heat, including biomass silo, feed controller, cloth
Device, carbonization furnace hearth, upper water seal, tar cracking device, activating velocity controller, vibrating screen, lower water seal, the first distributor,
Storehouse, charcoal base manure delivery outlet, activated carbon system is added in two distributors, charcoal preparing device, charcoal delivery outlet, charcoal base manure pellet fabrication device, trace element
Standby device, activated carbon prepare connector, steam gas bag, activation agent generator, burner, activated carbon delivery outlet, steam follower, combustion
Pump, combustion gas delivery outlet is sucked out in feed channel, combustion gas;
It is biomass silo at the top of device, the discharge port of biomass silo connects distributing device import, and the interconnecting piece of the two
Position is equipped with feed controller;The material outlet of distributing device is set at the top of carbonization furnace hearth;The main body stove of carbonization furnace hearth uses
Two-part structure, and epimere furnace body outer diameter is less than hypomere furnace body, epimere furnace body is co-axially mounted with hypomere furnace body and can be along center
Axis relatively rotates, and is carried out between the two by the upper water seal of annular setting closed;Hypomere bottom of furnace body is installed on base of furnace body,
And hypomere furnace body and base of furnace body contact site be also surrounded with lower water seal carry out it is closed;In the hypomere furnace body of carbonization furnace hearth
Equipped with vibrating screen, tar cracking device is fixed on the inner wall of hypomere furnace body, the air inlet of tar cracking device is connected to carbide furnace
Burner hearth, gas outlet are sucked out pump by combustion gas and are connected to combustion gas delivery outlet;
The hypomere furnace body intracavity bottom of carbonization furnace hearth is separately connected the first distributor and the second distributor;Described first
Charcoal is connected after distributor and manufactures device, and the charcoal delivery outlet that charcoal manufactures device connects charcoal base manure pellet fabrication device, and charcoal base manure pellet fabrication device is equipped with charcoal
Base manure delivery outlet simultaneously connects trace element addition storehouse;Activated carbon preparing device is connected after second distributor, prepared by activated carbon
The outlet of device by activated carbon prepare connector with activation agent generator be connected, activation agent generator at the top of connection steam drum with
Steam follower, activation agent generator bottom connect activated carbon delivery outlet, and side is equipped with the burner for providing heat;It is described
Burner connection with activating velocity controller gas pipeline.
Based on said program, can also further provide for one or more in following preferred embodiment:The combustion gas is inhaled
Go out and be equipped with vinegar liquid extraction element between pump and combustion gas delivery outlet, vinegar liquid extraction element bottom connects vinegar liquid holding vessel.The work
It is the control valve for regulating gas feed flow to change speed control.Condensation is equipped in the vinegar liquid extraction element inner cavity
Equipment, the inlet and outlet of inner cavity are sequentially connected combustion gas and pump and combustion gas delivery outlet are sucked out.It is equipped in the activation agent generator
Steam generation facility, and by the heat of burner offer liquid water vapor.The hypomere furnace body and furnace body of the carbonization furnace hearth
Pedestal can be relatively rotated along central shaft.The burner is connect with carbonization furnace hearth or combustion gas delivery outlet obtains combustion gas.Institute
The steam follower stated, which is exported to outside, consumes vapour equipment, including electric turbine.
A kind of Poly-generation method using the biogas of above-mentioned multi-joint-production apparatus, charcoal, fertilizer, acetic acid, heat, step is such as
Under:
First, biomass material is entered into distributing device by biomass silo, and biomass is controlled by feed controller
The charging rate of material makes biomass material pass through distributing device and is evenly distributed in the burner hearth of entire carbonization furnace hearth, and gradually
Fill up burner hearth;By controlling the rotation of the epimere furnace body and hypomere furnace body of carbonization furnace hearth, the material inside burner hearth is set to be distributed equal
Even, biomass material is gradually carbonized in burner hearth, gasifies, and so that charcoal ash is deposited to burner hearth bottom under the action of the sieve,
And volatile matter then enters tar cracking device under the swabbing action that pump is sucked out in combustion gas, and the tar contained in combustion gas is split
Solution;Combustion gas after cracking enters vinegar liquid extraction element and isolates biomass vinegar liquid in combustion gas, and biomass vinegar liquid is stored in
In vinegar liquid holding vessel, clean biological fuel gas is exported from combustion gas delivery outlet and is directly used for user;Carbonization furnace hearth bottom
Part charcoal ash activated carbon preparing device entered by the second distributor be prepared to pressed active carbon, activated carbon passes through activated carbon system
It after standby connector output, contacts and is activated with the vapor generated in activation agent generator, the activated carbon after activation is from activity
It is packed or is stored after the output of charcoal delivery outlet;Extra water vapour enters steam gas bag in activation agent generator, and from steam
Follower access is external to consume vapour equipment;The liquid water vaporescence of activation agent generator provides heat, and burner by burner
Used combustion gas is obtained via gas pipeline from carbonization furnace hearth or combustion gas delivery outlet, and combustion gas flow is by activating speed
Controller is spent to adjust;The part charcoal ash of carbonization furnace hearth bottom are input to charcoal preparing device by the first distributor and are prepared into charcoal, charcoal
It is input to the particle that charcoal base manure is made in charcoal base manure pellet fabrication device by charcoal delivery outlet, the trace element that storehouse is added is added with trace element
It is mixed together, then is packed or stored through the output of charcoal base manure delivery outlet.In device operational process, activating velocity control can be passed through
The manufacturing schedule of device and feed controller linkage control device processed.
The present invention has the advantage that compared with prior art:
1) adaptability of the present invention is extensive, changes control as a result of charging control and carbon (gas), can by way of speed governing
To generator yield, active carbon yield, biological vinegar liquid yield control effectively, to keep the adaptability that product yield adjusts big
To relax.According to the market in market, the yield of the costly product of regulating economy.Adaptability to raw material is wide simultaneously, and annoying (charcoal) is changed
Almost biomass, such as wood, bamboo, cotton stalk, rice husk, maize straw rubbish stick.
2) present invention ensure that the environmental protection in entire production process in structure;Almost zero-emission no pollution.Gas (charcoal) is changed
When biomass, charcoal, gas processed, acetic acid can be produced in set of device, waste heat also can steam processed for steam turbine power generation, realize Poly-generation and
It recycles.All to any type energy, utilize more abundant, externally discharge is fewer;It is exactly zero-emission thoroughly to utilize
No pollution.The present apparatus has accomplished making full use of and thoroughly utilizing to the energy;
3) capacity of the invention is big, efficient;Gasifiable biomass is at 5 tons or more per hour, 150,000 tons of annual amount for the treatment of with
On;
4) raw material are taken from soil, and final product is used for charcoal base manure returning to the field and biomass pesticides again, and field is taken from realization,
The purpose in field also, and whole process forms the economic industry chain of a cycle without any pollutant emission.
5) whole system of the invention, only needs technical staff on duty, is not necessarily to operator.To reduce human error and reduction
Labour cost.
Description of the drawings
Fig. 1 is the multi-joint-production apparatus structural schematic diagram of a kind of biogas, charcoal, fertilizer, acetic acid, heat.
In figure:Biomass silo 1, feed controller 2, distributing device 3, carbonization furnace hearth 4, upper water seal 5, tar cracking device
6, activating velocity controller 7, vibrating screen 8, lower water seal 9, the first distributor 10, the second distributor 11, charcoal preparing device 12, charcoal output
Storehouse 15, charcoal base manure delivery outlet 16, activated carbon preparing device 17, activated carbon preparation is added in mouth 13, charcoal base manure pellet fabrication device 14, trace element
Connector 18, steam gas bag 19, activation agent generator 20, burner 21, activated carbon delivery outlet 22, steam follower 23, combustion gas
Pump 25, vinegar liquid extraction element 26, combustion gas delivery outlet 27, vinegar liquid holding vessel 28 is sucked out in pipeline 24, combustion gas.
Specific implementation mode
The present invention is further elaborated in the following with reference to the drawings and specific embodiments, so that those skilled in the art are more preferable
Ground understands the essence of the present invention.
As shown in Figure 1, package unit by carbon (gas) changes stove main furnace body and charcoal base manure, to prepare and prepare activated carbon etc. three big
Part forms.Its critical piece includes biomass silo 1, feed controller 2, distributing device 3, carbon (gas) change stove burner hearth 4, upper water seal
5, tar cracking device 6, activating velocity controller 7, vibrating screen 8, lower water seal 9, the first distributor 10, the second distributor 11, charcoal
Storehouse 15, charcoal base manure delivery outlet 16, activated carbon preparation is added in preparing device 12, charcoal delivery outlet 13, charcoal base manure pellet fabrication device 14, trace element
Device 17, activated carbon prepare connector 18, steam gas bag 19, activation agent generator 20, burner 21, activated carbon delivery outlet 22, steam
Pump 25, vinegar liquid extraction element 26, combustion gas delivery outlet 27, vinegar liquid holding vessel 28 is sucked out in vapour follower 23, gas pipeline 24, combustion gas.
It is biomass silo 1 at the top of device, biomass silo 1 is for storing biomass material, such as wood, bamboo, cotton stalk, rice
Shell, maize straw rubbish stick etc..The discharge port of biomass silo 1 connects 3 import of distributing device, and the connecting portion of the two be equipped with into
Expect controller 2.The effect of feed controller 2 is that the charging rate of biomass material can be controlled according to the need of working condition, can be with
It is realized using the valve of aperture can be can control.The material outlet of distributing device 3 is set to 4 top of carbonization furnace hearth, and the two is close
Close combination.
The main body stove of carbonization furnace hearth 4 uses two-part structure, and epimere furnace body outer diameter is slightly less than hypomere furnace body, epimere stove
Body is co-axially mounted with hypomere furnace body, and the two can realize fixation by being arranged circumferentially support element in hypomere inboard wall of furnace body, between the two
Fixation be only limitted to vertical direction or horizontal direction, but the two can be relatively rotated along central shaft, but be needed in binding site logical
Cross annular setting upper water seal 5 carry out it is closed.The design is to be able to that furnace body is made to pass through rotation, realizes uniformly dividing for material
Cloth prevents dead angle or material uneven phenomenon.Hypomere bottom of furnace body is also turnably installed on base of furnace body, and hypomere
Furnace body and base of furnace body contact site be also surrounded with lower water seal 9 carry out it is closed.It should be noted that in the position for having water seal
It sets, needs to carry out water proof measure between water seal cavity and burner hearth, prevent water from entering burner hearth by gap.Under carbonization furnace hearth 4
It is equipped with the vibrating screen 8 for causing vibrational perturbation for the material to top in section furnace body, tar is fixed on the inner wall of hypomere furnace body
Cracker 6.The air inlet of tar cracking device 6 is connected to carbonization furnace hearth 4, and gas outlet is sucked out pump 25 by combustion gas and is connected to combustion
Gas delivery outlet 27, and combustion gas is sucked out between pump 25 and combustion gas delivery outlet 27 and is equipped with vinegar liquid extraction element 26, vinegar liquid extraction element 26
Bottom connects vinegar liquid holding vessel 28.In burner hearth, biomass material forms charcoal ash and volatile matter by carbonization, gasification, including
The various recoverable materials such as biomass vinegar liquid, biomass coke tar, biomass coal gas.The effect of tar cracking device 6 is by stove
The tar contained in gas in thorax is cracked, and various existing devices in the prior art may be used and realize.By cracking
Gas go successively to vinegar liquid extraction element 26 carry out vinegar liquid extraction work.The prior art may be used in vinegar liquid extraction element 26
In equipment, such as equipment inner cavity air stream through condensing plant is arranged on path, so that acetic acid is condensed herein, to from gas
Middle separation.The inlet and outlet of equipment inner cavity is sequentially connected combustion gas and pump 25 and combustion gas delivery outlet 27 is sucked out.By cracking and vinegar liquid
After collection, clean biological fuel gas is exported from combustion gas delivery outlet 27 and is directly used for user.
The hypomere furnace body intracavity bottom of carbonization furnace hearth 4 is separately connected the first distributor 10 and the second distributor 11, two
Distributor can need to adjust aperture according to technique, to which the bottom charcoal ash of different proportion are transported to follow-up equipment.First distribution
Charcoal is connected after device 10 and manufactures device 12, and molding charcoal can be made in charcoal ash by charcoal manufacture device 12, and charcoal manufactures the charcoal delivery outlet 13 of device 12
Connection charcoal base manure pellet fabrication device 14 is granulated, and charcoal base manure pellet fabrication device 14, which is equipped with charcoal base manure delivery outlet 16 and connects trace element, to be added
Put in storage 15.Storehouse 15 is added for storing trace element materials to be added in trace element, can be modified to waste material.Second distribution
Activated carbon preparing device 17 is connected after device 11, charcoal ash can be molded by activated carbon preparing device 17, and activated carbon preparing device 17 goes out
Mouth prepares connector 18 by activated carbon and is connected with activation agent generator 20, and activated carbon, which prepares connector 18, can also be set as aperture
Adjustable connector, to control charging rate.Activation agent generator 20 is used to generate activator needed for activated carbon, and one
As activator be vapor, therefore activate agent generator 20 in steam generation facility can be set, the heat of steam generation facility can
It is provided by burner 21, by liquid water vapor.Gas pipeline 24 of the connection of burner 21 with activating velocity controller 7, combustion gas
24 end of pipeline can be connect with carbonization furnace hearth 4 or combustion gas delivery outlet 27 obtains combustion gas.Activating velocity controller 7 may be used can
The control valve for degree of tuning to open is used for regulating gas feed flow.Prepared by activator moiety and activated carbon exports in connector 18
Charcoal contacts, and is activated to it, and the activated carbon delivery outlet 22 then connected from 20 bottom of activation agent generator exports.Work as vapor
When extra, steam heat can also be externally provided in 20 top connection steam drum 19 of activation agent generator and steam follower 23
Vapour equipment is consumed outside source, such as output to electric turbine, or directly feeds user.
The Poly-generation method of biogas, charcoal, fertilizer, acetic acid, heat based on above-mentioned apparatus, its step are as follows:
First, biomass material is entered into distributing device 3 by biomass silo 1, and biology is controlled by feed controller 2
The charging rate of material makes biomass material pass through distributing device 3 and is evenly distributed in the burner hearth of entire carbonization furnace hearth 4, and
Gradually fill up burner hearth;By controlling the rotation of the epimere furnace body and hypomere furnace body of carbonization furnace hearth 4, make the material point inside burner hearth
Cloth is uniform, and biomass material is gradually carbonized in burner hearth, gasifies, and so that charcoal ash is deposited to burner hearth under the action of vibrating screen 8
Bottom, and volatile matter then enters tar cracking device 6, the tar that will contain in combustion gas under the swabbing action that pump 25 is sucked out in combustion gas
It is cracked;Combustion gas after cracking enters vinegar liquid extraction element 26 and isolates biomass vinegar liquid in combustion gas, biomass vinegar
Liquid is stored in vinegar liquid holding vessel 28, and clean biological fuel gas is exported from combustion gas delivery outlet 27 and directly used for user;Carbon
The part charcoal ash for changing 4 bottom of stove burner hearth are prepared to pressed active carbon by the second distributor 11 into activated carbon preparing device 17,
After activated carbon prepares the output of connector 18 by activated carbon, contacts and live with the vapor generated in activation agent generator 20
Change, the activated carbon after activation is packed or stored after the output of activated carbon delivery outlet 22;It is extra in agent generator 20 to activate
Water vapour enters steam gas bag 19, and accesses external consumption vapour equipment from steam follower 23;Activate the liquid water of agent generator 20
Vaporescence provides heat by burner 21, and combustion gas used by burner 21 via gas pipeline 24 from carbonization furnace hearth
4 or combustion gas delivery outlet 27 in obtain, combustion gas flow pass through activating velocity controller 7 adjust;The part of 4 bottom of carbonization furnace hearth
Charcoal ash are input to charcoal preparing device 12 by the first distributor 10 and are prepared into charcoal, and charcoal is input to charcoal base manure by charcoal delivery outlet 13 and pelletizes
The particle of charcoal base manure is made in device 14, and the trace element that storehouse 15 is added, which is added, with trace element is mixed together, then is exported through charcoal base manure
16 output of mouth is packed or is stored, for targetedly being applied fertilizer to soil, to improve validity of the soil to fertilizer.
In device operational process, by the production of 2 linkage control device of activating velocity controller 7 and feed controller into
The inventory of degree, the control input of feed controller 2 is more, and subsequent activation speed control 7 should also be as control fuel gas supply rate
It is bigger, to meet activated carbon activation requirements.
Package unit feeds by biomass, is carbonized, produces biological fuel gas, charcoal processing, extraction biomass acetic acid, prepare it is carbon-based
Several part compositions such as fertilizer, waste heat recovery steam.All recycling can be used for generating electricity or supply fuel gas during carbonization
Heat, charcoal can be made carbon-based fertilizer for improveing soil, activated carbon can also be made, the biomass acetic acid for purifying air extraction
Herbicide can be made and substitute glyphosate etc., chemical pesticide can also be substituted, eliminate people and the pesticide residue in vegetables and fruits is worried;
Steam is used for heat supply, substitutes coal or natural gas.Whole process zero emission and pollution, high added value, sustainable development.
Above-mentioned embodiment is only a preferred solution of the present invention, so it is not intended to limiting the invention.Have
The those of ordinary skill for closing technical field can also make various changes without departing from the spirit and scope of the present invention
Change with modification or use the function of a part therein.Therefore all modes for taking equivalent substitution or equivalent transformation are obtained
Technical solution or use partial function therein, all fall in protection scope of the present invention.
Claims (10)
1. the multi-joint-production apparatus of a kind of biogas, charcoal, fertilizer, acetic acid, heat, it is characterised in that including biomass silo (1), charging
Controller (2), distributing device (3), carbonization furnace hearth (4), upper water seal (5), tar cracking device (6), activating velocity controller
(7), vibrating screen (8), lower water seal (9), the first distributor (10), the second distributor (11), charcoal preparing device (12), charcoal delivery outlet
(13), charcoal base manure pellet fabrication device (14), trace element are added storehouse (15), charcoal base manure delivery outlet (16), activated carbon preparing device (17), live
Property charcoal prepare connector (18), steam gas bag (19), activation agent generator (20), burner (21), activated carbon delivery outlet (22),
Pump (25), combustion gas delivery outlet (27) is sucked out in steam follower (23), gas pipeline (24), combustion gas;
It is biomass silo (1) at the top of device, the discharge port of biomass silo (1) connects distributing device (3) import, and the company of the two
Socket part position is equipped with feed controller (2);The material outlet of distributing device (3) is set at the top of carbonization furnace hearth (4);Carbonization furnace hearth
(4) main body stove uses two-part structure, and epimere furnace body outer diameter is less than hypomere furnace body, and epimere furnace body is coaxially pacified with hypomere furnace body
It fills and can be relatively rotated along central shaft, carried out between the two by the upper water seal (5) of annular setting closed;Hypomere bottom of furnace body
Be installed on base of furnace body, and hypomere furnace body and base of furnace body contact site be also surrounded with lower water seal (9) carry out it is closed;Carbon
Change and be equipped with vibrating screen (8) in the hypomere furnace body of stove burner hearth (4), tar cracking device (6) is fixed on the inner wall of hypomere furnace body, it is burnt
The air inlet connection carbonization furnace hearth (4) of oil-breaking device (6), gas outlet are sucked out pump (25) by combustion gas and are connected to combustion gas output
Mouth (27);The hypomere furnace body intracavity bottom of carbonization furnace hearth (4) is separately connected the first distributor (10) and the second distributor (11);
First distributor (10) connects charcoal manufacture device (12) afterwards, and the charcoal delivery outlet (13) that charcoal manufactures device (12) connects charcoal base manure system
Grain device (14), charcoal base manure pellet fabrication device (14), which is equipped with charcoal base manure delivery outlet (16) and connects trace element, is added storehouse (15);It is described
The second distributor (11) connect activated carbon preparing device (17) afterwards, the outlet of activated carbon preparing device (17), which passes through activated carbon and prepares, to be connected
It connects device (18) with activation agent generator (20) to be connected, connection steam drum (19) and steam output at the top of activation agent generator (20)
Device (23), activation agent generator (20) bottom connection activated carbon delivery outlet (22), side are equipped with the burner for providing heat
(21);The gas pipeline (24) of burner (21) connection with activating velocity controller (7).
2. the multi-joint-production apparatus of biogas as described in claim 1, charcoal, fertilizer, acetic acid, heat, it is characterised in that the combustion
Aspiration, which goes out, is equipped with vinegar liquid extraction element (26) between pump (25) and combustion gas delivery outlet (27), the connection of vinegar liquid extraction element (26) bottom
Vinegar liquid holding vessel (28).
3. the multi-joint-production apparatus of biogas as described in claim 1, charcoal, fertilizer, acetic acid, heat, it is characterised in that the work
It is the control valve for regulating gas feed flow to change speed control (7).
4. the multi-joint-production apparatus of biogas as described in claim 1, charcoal, fertilizer, acetic acid, heat, it is characterised in that the vinegar
Condensing plant is equipped in liquid extraction element (26) inner cavity, the inlet and outlet of inner cavity is sequentially connected combustion gas and pump (25) and combustion gas is sucked out
Delivery outlet (27).
5. the multi-joint-production apparatus of biogas as described in claim 1, charcoal, fertilizer, acetic acid, heat, it is characterised in that the work
It is equipped with steam generation facility in agent generator (20), and the heat of liquid water vapor is provided by burner (21).
6. the multi-joint-production apparatus of biogas as described in claim 1, charcoal, fertilizer, acetic acid, heat, it is characterised in that the carbon
The hypomere furnace body and base of furnace body for changing stove burner hearth (4) can be relatively rotated along central shaft.
7. the multi-joint-production apparatus of biogas as described in claim 1, charcoal, fertilizer, acetic acid, heat, it is characterised in that the combustion
Burner (21) is connect with carbonization furnace hearth (4) or combustion gas delivery outlet (27) obtains combustion gas.
8. the multi-joint-production apparatus of biogas as described in claim 1, charcoal, fertilizer, acetic acid, heat, it is characterised in that the steaming
Vapour equipment, including electric turbine are consumed in vapour follower (23) output to outside.
9. a kind of Poly-generation method using the biogas of multi-joint-production apparatus as described in claim 1, charcoal, fertilizer, acetic acid, heat,
It is characterized in that, steps are as follows:
First, biomass material is entered into distributing device (3) by biomass silo (1), and is controlled and is given birth to by feed controller (2)
The charging rate of substance material makes biomass material pass through the burner hearth that distributing device (3) is evenly distributed in entire carbonization furnace hearth (4)
It is interior, and gradually fill up burner hearth;By controlling the rotation of the epimere furnace body and hypomere furnace body of carbonization furnace hearth (4), make inside burner hearth
Material be evenly distributed, biomass material is gradually carbonized in burner hearth, gasifies, and makes charcoal ash under the action of vibrating screen (8)
Burner hearth bottom is deposited to, and volatile matter then enters tar cracking device (6) under the swabbing action that pump (25) is sucked out in combustion gas, will fire
The tar contained in gas is cracked;Combustion gas after cracking enters vinegar liquid extraction element (26) and isolates biology in combustion gas
Matter vinegar liquid, biomass vinegar liquid are stored in vinegar liquid holding vessel (28), and clean biological fuel gas is defeated from combustion gas delivery outlet (27)
Go out and is directly used for user;The part charcoal ash of carbonization furnace hearth (4) bottom are prepared by the second distributor (11) into activated carbon
Device (17) is prepared to pressed active carbon, after activated carbon prepares connector (18) output by activated carbon, with activation agent generator
(20) the vapor contact generated in is activated, and the activated carbon after activation is packed after activated carbon delivery outlet (22) output
Or storage;Extra water vapour enters steam gas bag (19) in activation agent generator (20), and is accessed from steam follower (23)
Outside consumption vapour equipment;The liquid water vaporescence for activating agent generator (20) provides heat, and burner by burner (21)
(21) combustion gas used by is obtained via gas pipeline (24) from carbonization furnace hearth (4) or combustion gas delivery outlet (27), burning
Throughput is adjusted by activating velocity controller (7);The part charcoal ash of carbonization furnace hearth (4) bottom pass through the first distributor (10)
It is input to charcoal preparing device (12) and is prepared into charcoal, charcoal is input to charcoal base manure pellet fabrication device (14) by charcoal delivery outlet (13) and charcoal base manure is made
Particle, with trace element be added storehouse (15) be added trace element be mixed together, then through charcoal base manure delivery outlet (16) export into
Row packaging or storage.
10. Poly-generation method as claimed in claim 9, which is characterized in that in device operational process, controlled by activating velocity
The manufacturing schedule of device (7) and feed controller (2) linkage control device.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201810217720.1A CN108424772A (en) | 2018-03-16 | 2018-03-16 | Biogas, charcoal, fertilizer, acetic acid, the multi-joint-production apparatus of heat and its method |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201810217720.1A CN108424772A (en) | 2018-03-16 | 2018-03-16 | Biogas, charcoal, fertilizer, acetic acid, the multi-joint-production apparatus of heat and its method |
Publications (1)
Publication Number | Publication Date |
---|---|
CN108424772A true CN108424772A (en) | 2018-08-21 |
Family
ID=63158296
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201810217720.1A Pending CN108424772A (en) | 2018-03-16 | 2018-03-16 | Biogas, charcoal, fertilizer, acetic acid, the multi-joint-production apparatus of heat and its method |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN108424772A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN111530225A (en) * | 2020-04-29 | 2020-08-14 | 沈阳东大山汇环境科技有限公司 | Circular ecological environment-friendly treatment process for agriculture and forestry organic waste and flue gas |
CN116515511A (en) * | 2023-05-06 | 2023-08-01 | 西安交通大学 | Biomass gasification comprehensive utilization system |
Citations (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2004189788A (en) * | 2002-12-09 | 2004-07-08 | Tokan:Kk | Preparation method of pyrolignous acid or bamboo vinegar and carbonizing furnace |
CN2771210Y (en) * | 2005-03-18 | 2006-04-12 | 苏州北岛能源技术有限公司 | Coal gas producer |
CN201351934Y (en) * | 2008-12-12 | 2009-11-25 | 扬州工业职业技术学院 | Household low-tar biomass gasifier |
JP2010222471A (en) * | 2009-03-24 | 2010-10-07 | Jfe Steel Corp | Method for producing biomass charcoal and apparatus for producing biomass charcoal used therefor |
CN101955803A (en) * | 2009-07-15 | 2011-01-26 | 山东科技大学 | Low-rank coal carbonization method |
CN105505466A (en) * | 2015-11-30 | 2016-04-20 | 南京林业大学 | Technology for shells downdraft fixed bed gasification power generation and co-production of active carbon and heat |
CN106518475A (en) * | 2016-12-12 | 2017-03-22 | 北京神雾环境能源科技集团股份有限公司 | System and method for preparing biomass charcoal-based urea fertilizer from straw |
CN108728165A (en) * | 2018-08-16 | 2018-11-02 | 福建中化智胜化肥有限公司 | Charcoal base manure resources of production method of comprehensive utilization based on updraft type charcoal gas coproduction stove |
CN208218789U (en) * | 2018-03-16 | 2018-12-11 | 浙江华尚新能源股份有限公司 | A kind of biogas, charcoal, fertilizer, acetic acid, heat multi-joint-production apparatus |
CN212713295U (en) * | 2020-08-04 | 2021-03-16 | 陈鼎熙 | Preparation system of straw carbon-based fertilizer |
CN115746916A (en) * | 2022-12-02 | 2023-03-07 | 云南程盈森林资源开发控股集团有限公司 | Gasification system and process for carbon and electricity combined production of substances and gasification furnace |
-
2018
- 2018-03-16 CN CN201810217720.1A patent/CN108424772A/en active Pending
Patent Citations (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2004189788A (en) * | 2002-12-09 | 2004-07-08 | Tokan:Kk | Preparation method of pyrolignous acid or bamboo vinegar and carbonizing furnace |
CN2771210Y (en) * | 2005-03-18 | 2006-04-12 | 苏州北岛能源技术有限公司 | Coal gas producer |
CN201351934Y (en) * | 2008-12-12 | 2009-11-25 | 扬州工业职业技术学院 | Household low-tar biomass gasifier |
JP2010222471A (en) * | 2009-03-24 | 2010-10-07 | Jfe Steel Corp | Method for producing biomass charcoal and apparatus for producing biomass charcoal used therefor |
CN101955803A (en) * | 2009-07-15 | 2011-01-26 | 山东科技大学 | Low-rank coal carbonization method |
CN105505466A (en) * | 2015-11-30 | 2016-04-20 | 南京林业大学 | Technology for shells downdraft fixed bed gasification power generation and co-production of active carbon and heat |
CN106518475A (en) * | 2016-12-12 | 2017-03-22 | 北京神雾环境能源科技集团股份有限公司 | System and method for preparing biomass charcoal-based urea fertilizer from straw |
CN208218789U (en) * | 2018-03-16 | 2018-12-11 | 浙江华尚新能源股份有限公司 | A kind of biogas, charcoal, fertilizer, acetic acid, heat multi-joint-production apparatus |
CN108728165A (en) * | 2018-08-16 | 2018-11-02 | 福建中化智胜化肥有限公司 | Charcoal base manure resources of production method of comprehensive utilization based on updraft type charcoal gas coproduction stove |
CN212713295U (en) * | 2020-08-04 | 2021-03-16 | 陈鼎熙 | Preparation system of straw carbon-based fertilizer |
CN115746916A (en) * | 2022-12-02 | 2023-03-07 | 云南程盈森林资源开发控股集团有限公司 | Gasification system and process for carbon and electricity combined production of substances and gasification furnace |
Non-Patent Citations (1)
Title |
---|
李燃,常文韬,闫平,孙静编: "《农村生态环境改善 适用技术与工程实践》", vol. 1, 天津大学出版社, pages: 184 - 185 * |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN111530225A (en) * | 2020-04-29 | 2020-08-14 | 沈阳东大山汇环境科技有限公司 | Circular ecological environment-friendly treatment process for agriculture and forestry organic waste and flue gas |
CN116515511A (en) * | 2023-05-06 | 2023-08-01 | 西安交通大学 | Biomass gasification comprehensive utilization system |
CN116515511B (en) * | 2023-05-06 | 2024-03-12 | 西安交通大学 | Biomass gasification comprehensive utilization system |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN104017590B (en) | A kind of agricultural-forestry biomass continuous pyrolysis charing method | |
CN104804775B (en) | The method and system of domestic garbage pyrolysis gasification production combustible gas | |
CN102559220B (en) | Precisely controlled biomass gas and biomass carbon preparation system | |
CN106629715A (en) | System and method for preparing active carbon by biomass | |
CN106944461A (en) | A kind of system and method for domestic rubbish disposal | |
CN106350084A (en) | Biochemical substance fuel production system of high-performance active carbon and production method thereof | |
CN208776670U (en) | A kind of biomass comprehensive utilizes system | |
CN202054794U (en) | Recovery device for using straws to produce carbon, gas and byproducts | |
CN106495150A (en) | A kind of utilization straw prepares the system and method for activated carbon base calcium magnesium phosphate material | |
CN104789240A (en) | Biomass and straw comprehensive utilization coproduction line and coproduction method | |
CN105925336A (en) | Biomass composite fuel with high combustion efficiency and a preparation method thereof | |
CN108424772A (en) | Biogas, charcoal, fertilizer, acetic acid, the multi-joint-production apparatus of heat and its method | |
CN104861994B (en) | Cooling device in biomass carbonization stove | |
CN105710114A (en) | Carbonization circulation overall treatment system and method for household refuse and forestry and agricultural residues | |
CN205701817U (en) | One way of life rubbish and agriculture and forestry organic waste material carbonization circulation comprehensive processing system | |
CN208218789U (en) | A kind of biogas, charcoal, fertilizer, acetic acid, heat multi-joint-production apparatus | |
CN105542870B (en) | It is a kind of to carry out charcoal, air-liquid, the system and production method of oily coproduction using biomass | |
CN204607940U (en) | The system of combustible gas is produced in domestic garbage pyrolysis gasification | |
CN205709880U (en) | A kind of Arundo donax produces the system of activated carbon coproduction generating | |
CN205766675U (en) | The carbonization processing device of mah-jong mat bamboo chip | |
CN210438685U (en) | Device for extracting wood vinegar through straw graded heating | |
CN110257093A (en) | The control method of carbonization system in a kind of hot charcoal co-generation system of biomass external heating | |
CN201269555Y (en) | Stalk gasification and combustion device | |
CN106145107A (en) | A kind of Arundo donax produces activated carbon, the system and method for bio oil coproduction generating | |
CN102863975A (en) | Device and method for carbonizing straw |
Legal Events
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 |