CN203923096U - Organic materials carbonization decomposition vapourizing furnace - Google Patents
Organic materials carbonization decomposition vapourizing furnace Download PDFInfo
- Publication number
- CN203923096U CN203923096U CN201420303706.0U CN201420303706U CN203923096U CN 203923096 U CN203923096 U CN 203923096U CN 201420303706 U CN201420303706 U CN 201420303706U CN 203923096 U CN203923096 U CN 203923096U
- Authority
- CN
- China
- Prior art keywords
- organic materials
- destructive distillation
- heater
- pyrolysis gasification
- gasification body
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
Classifications
-
- 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
- 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
- C10B19/00—Heating of coke ovens by electrical means
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10K—PURIFYING OR MODIFYING THE CHEMICAL COMPOSITION OF COMBUSTIBLE GASES CONTAINING CARBON MONOXIDE
- C10K1/00—Purifying combustible gases containing carbon monoxide
- C10K1/08—Purifying combustible gases containing carbon monoxide by washing with liquids; Reviving the used wash liquors
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10K—PURIFYING OR MODIFYING THE CHEMICAL COMPOSITION OF COMBUSTIBLE GASES CONTAINING CARBON MONOXIDE
- C10K1/00—Purifying combustible gases containing carbon monoxide
- C10K1/08—Purifying combustible gases containing carbon monoxide by washing with liquids; Reviving the used wash liquors
- C10K1/10—Purifying combustible gases containing carbon monoxide by washing with liquids; Reviving the used wash liquors with aqueous liquids
- C10K1/101—Purifying combustible gases containing carbon monoxide by washing with liquids; Reviving the used wash liquors with aqueous liquids with water only
-
- 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
Abstract
The utility model provides a kind of organic materials carbonization decomposition vapourizing furnace, comprising: pyrolysis gasification body of heater, and described pyrolysis gasification body of heater is provided with opening for feed and air outlet; Multiple destructive distillation chamber, described multiple destructive distillation chamber juxtaposition is in described pyrolysis gasification body of heater, and spaced apart between two adjacent destructive distillation chambers, and bottom, each described destructive distillation chamber is equipped with discharge gate; And electrically heated rod, it is indoor so that the indoor material of described multiple destructive distillation is completely cut off to air destructive distillation, to produce solid carbonaceous material and carbonization gas that described electrically heated rod is located at described multiple destructive distillation vertically.Can at utmost contamination-freely utilize conventional example as the material of low-rank coal foam, resinous shale foam etc., farthest to utilize this organic materials according to organic materials carbonization decomposition vapourizing furnace of the present utility model.
Description
Technical field
The utility model relates to organic materials processing technology field, especially relates to a kind of organic materials carbonization decomposition vapourizing furnace of processing organic materials.
Background technology
Taking domestic refuse as example, the burning disposal mode that tradition adopts all can produce dioxin and follow heavy metal contamination in gas and waste residue.And need oil spout combustion-supporting in burning disposal process, directly cause processing cost too high.
In addition, how by the inflammable gas in foam coal and tar extraction out as everyone knows, the relative lump coal of the utilization ratio of foam coal is much lower,, it is China and even a great problem in the world that while low-rank coal foam becomes high-quality smokeless fuel, similarly also has resinous shale foam with foam coal facies.
For above-mentioned organic materials, how pollution-free and process at low cost to reach organic materials and make full use of, be the technical barrier that this area faces.
Utility model content
The utility model is intended at least solve one of technical problem existing in prior art.
The utility model need to provide a kind of organic materials carbonization decomposition vapourizing furnace, and described organic materials carbonization decomposition vapourizing furnace can at utmost contamination-freely utilize conventional example as the organic materials of rubbish, low-rank coal foam etc., farthest to utilize this organic materials.
According to the organic materials carbonization decomposition vapourizing furnace of the utility model first aspect embodiment, comprising: pyrolysis gasification body of heater, described pyrolysis gasification body of heater is provided with opening for feed and air outlet; Multiple destructive distillation chamber, described multiple destructive distillation chamber juxtaposition is in described pyrolysis gasification body of heater, and spaced apart between two adjacent destructive distillation chambers, and bottom, each described destructive distillation chamber is equipped with discharge gate; And electrically heated rod, it is indoor so that the indoor material of described multiple destructive distillation is completely cut off to air destructive distillation, to produce solid carbonaceous material and carbonization gas that described electrically heated rod is located at described multiple destructive distillation vertically.
According to the organic materials carbonization decomposition vapourizing furnace of embodiment of the present utility model, effectively contamination-freely processing example, as domestic refuse, low-rank coal foam or resinous shale foam etc., is worth utilization maximization thereby realize organic materials.
According to an embodiment of the present utility model, described organic materials is that described organic materials comprises: the byproduct schlempe of domestic refuse, agricultural byproducts stalk, cotton stalk, wine brewing and vinasse, plant leaves, industrial refuse, medical waste, low-rank coal foam, resinous shale foam or its mixture.
Additional aspect of the present utility model and advantage in the following description part provide, and part will become obviously from the following description, or recognize by practice of the present utility model.
Brief description of the drawings
Above-mentioned and/or additional aspect of the present utility model and advantage accompanying drawing below combination is understood becoming the description of embodiment obviously and easily, wherein:
Fig. 1 is according to the schematic diagram of the organic materials carbonization decomposition vapourizing furnace of an embodiment of the utility model;
Fig. 2 is according to the schematic diagram of the distribution device of the organic materials carbonization decomposition vapourizing furnace of an embodiment of the utility model;
Fig. 3 is according to the schematic diagram of the elementary carbonization gas washing tower of an embodiment of the utility model;
Fig. 4 is according to the schematic diagram of the secondary carbonization gas washing tower of an embodiment of the utility model;
Fig. 5 is according to the schematic diagram of the self-cleaning heat-exchange equipment of an embodiment of the utility model; And
Fig. 6 is the schema that adopts the organic materials treatment process of organic materials carbonization decomposition vapourizing furnace of the present utility model.
Embodiment
Describe embodiment of the present utility model below in detail, the example of described embodiment is shown in the drawings, and wherein same or similar label represents same or similar element or has the element of identical or similar functions from start to finish.Be exemplary below by the embodiment being described with reference to the drawings, only for explaining the utility model, and can not be interpreted as restriction of the present utility model.
In description of the present utility model, it will be appreciated that, term " on ", orientation or the position relationship of the instruction such as D score " vertically ", " level ", " top ", " end ", " interior ", " outward " be based on orientation shown in the drawings or position relationship, only the utility model and simplified characterization for convenience of description, instead of indicate or imply that the device of indication or element must have specific orientation, construct and operation with specific orientation, therefore can not be interpreted as restriction of the present utility model.In addition, term " first ", " second " be only for describing object, and can not be interpreted as instruction or hint relative importance or the implicit quantity that indicates indicated technical characterictic.Thus, one or more these features can be expressed or impliedly be comprised to the feature that is limited with " first ", " second ".In description of the present utility model, except as otherwise noted, the implication of " multiple " is two or more.
In description of the present utility model, it should be noted that, unless otherwise clearly defined and limited, term " installation ", " being connected ", " connection " should be interpreted broadly, and for example, can be to be fixedly connected with, and can be also to removably connect, or connect integratedly; Can be mechanical connection, can be also electrical connection; Can be to be directly connected, also can indirectly be connected by intermediary, can be the connection of two element internals.For the ordinary skill in the art, can particular case understand the concrete meaning of above-mentioned term in the utility model.
As shown in Fig. 1-Fig. 6, comprise organic materials carbonization decomposition vapourizing furnace 100, carbonization gas washing plant and self-cleaning heat-exchange equipment 300 according to the organic materials treatment system of the utility model embodiment.
First it should be noted that, in the description of embodiment of the present utility model: shown in for example, arrow in " above-below direction " Fig. 1, Fig. 3-Fig. 5.But also it should be noted that, the instruction of this direction is for exemplary purposes, instead of in order to limit protection domain of the present utility model.
According to the organic materials treatment system of the utility model embodiment, this organic materials treatment system can be used for processing the organic materialss such as domestic refuse, straw, low-rank coal foam and/or resinous shale foam.And in description below the disclosure, describe as example for the treatment of low-rank coal foam and/or resinous shale foam taking organic materials treatment system.Need to further illustrate, low-rank coal foam refers to all not adhesive brown coal, bituminous coal and hard coal herein.
Certainly, those skilled in the art are appreciated that, this organic materials treatment system only describes as example for the treatment of low-rank coal foam and/or resinous shale foam, and be not limited to this, also can be used for processing the pending material of other types according to organic materials treatment system of the present utility model, the organic materials mixture such as byproduct schlempe and vinasse, plant leaves, industrial refuse and medical waste of such as agricultural byproducts stalk, cotton stalk, wine brewing.
As depicted in figs. 1 and 2, the bottom that the top of organic materials carbonization decomposition vapourizing furnace 100 has opening for feed and air outlet and organic materials carbonization decomposition vapourizing furnace 100 has discharge gate, wherein organic materials enters and in organic materials carbonization decomposition vapourizing furnace 100, completely cuts off air destructive distillation and organic materials is discharged from discharge gate from opening for feed, and the carbonization gas of generation is discharged from air outlet.Wherein, the composition of carbonizing gas comprises other mixing of the Multiple components such as methane, hydrogen, hydrocarbon polymer, carbon monoxide and trace nitrogen, oxygen.
As shown in Figure 3 and Figure 4, carbonization gas washing plant is connected to the carbonization gas of the Qie Duicong air outlet, downstream of organic materials carbonization decomposition vapourizing furnace 100 discharging and receives also washing, purifying.
As shown in Figure 5, self-cleaning heat-exchange equipment 300 is connected to the downstream of carbonization gas washing plant the carbonization gas after washing, purifying is processed to obtain clean flammable carbonizing gas, and this is flammable, and carbonizing gas can part instead of natural gas supply industry and gas.
According to the organic materials treatment system of the utility model embodiment, carry out destructive distillation and produce carbonization gas by first organic materials being passed into organic materials carbonization decomposition vapourizing furnace 100, again carbonization gas is passed into successively in carbonization gas washing plant and self-cleaning heat-exchange equipment 300, carry out washing, purifying and processing, finally can obtain clean flammable carbonizing gas, can reduce thus the impact of organic materials on environment, and by the above-mentioned treating processes to organic materials, the flammable energy can also be obtained, thereby the maximization of organic materials utility value can be made.
Below with reference to Fig. 1, describe in detail according to the organic materials carbonization decomposition vapourizing furnace 100 of the utility model embodiment, as shown in Figure 1, this organic materials carbonization decomposition vapourizing furnace 100 comprises pyrolysis gasification body of heater 110, multiple destructive distillation chamber 120 and electric heater unit.In an embodiment of the present utility model, this electric heater unit can be electrically heated rod 130.
Opening for feed and air outlet are formed on the top of pyrolysis gasification body of heater 110.With reference to Fig. 1, in pyrolysis gasification body of heater 110, limit and hold the spatial accommodation for the treatment of destructive distillation material, the top of pyrolysis gasification body of heater 110 has opening for feed to feed the material for the treatment of destructive distillation in spatial accommodation, and the top of pyrolysis gasification body of heater 110 has air outlet and discharges by this air outlet with the gas that destructive distillation is obtained.
Multiple destructive distillation chamber 120 is located in pyrolysis gasification body of heater 110 side by side, and spaced apart by partition wall 121 between two adjacent destructive distillation chambers 120, and 120 bottoms, each destructive distillation chamber are equipped with discharge gate 122.In the example of Fig. 1, multiple destructive distillation chamber 120 is located at the bottom of pyrolysis gasification body of heater 110 in parallel with each other, spaced apart by partition wall 121 between adjacent destructive distillation chamber 120, the material falling from top to receive is opened wide at the top of destructive distillation chamber 120, and the bottom of each destructive distillation chamber 120 all has discharge gate 122 and discharges from this discharge gate 122 with such as smokeless fuel of solid matter or the powder of building trade use and the additive of cement industry use etc. that destructive distillation is obtained.It will be appreciated that, the quantity of destructive distillation chamber 120 can be according to actual requirement setting, to have better destructive distillation effect.
Electrically heated rod 130 is located in multiple destructive distillation chamber 120 vertically the material in multiple destructive distillation chamber 120 is completely cut off to air destructive distillation to produce solid carbonaceous material, carbonization gas and tar.For example, in the example of Fig. 1, the interior electrically heated rod 130 that is all provided with vertically in each destructive distillation chamber 120, electrically heated rod 130 completely cuts off air destructive distillation to the destructive distillation material for the treatment of in each destructive distillation chamber 120 respectively, that is to say, treat for example organic materials completely isolated air destructive distillation in retort process of destructive distillation material, obtain solid carbonaceous material, carbonization gas and tar.It will be appreciated that, the indoor temperature of destructive distillation can arbitrarily regulate with organic materials different in kind.And electrically heated rod 130 is located in multiple destructive distillation chamber 120 vertically, than the horizontally disposed situation of electrically heated rod 130, can prevent from that material from falling to make electrically heated rod 130 flexural deformations.It should be noted that, in an embodiment of the present utility model, electrically heated rod 130 also can flatly arrange, so that organic materials is fully heated.
Particularly, electrically heated rod 130 can use interchange or DC voltage power supply to completely cut off air destructive distillation to produce high temperature hot gas body to treat the material of destructive distillation.Particularly, electrically heated rod 130 comprises electrical heating wire and is set in its outer insulation layer.Because which output gas heating value is higher, for example low-rank coal foam and/or the every side's gas of resinous shale foam calorific value are more than 4000 kilocalories, tolerance is larger, for example aerogenesis per ton is more than 400 cubes, one ton of low-rank coal foam of every processing and/or resinous shale foam, electric energy that electrically heated rod consumes only accounts for the sub-fraction of gas production rate generation calorific value per ton, and therefore running cost is lower.For the organic materials of for example domestic refuse, the every side's gas of gas calorific value by which output is more than 6000 kilocalories, tolerance is larger, for example aerogenesis per ton is more than 800 cubes, one ton of domestic refuse of every processing, for example electric energy that electrically heated rod consumes of electric heater only accounts for the sub-fraction of gas production rate generation calorific value per ton, and therefore running cost is lower.
The organic materials for the treatment of destructive distillation enters organic materials carbonization decomposition vapourizing furnace 100 and carries out destructive distillation, discharge the powder of smokeless fuel product or building trade use and the additive that cement industry uses, produce continuously carbonizing gas and tar products simultaneously, the carbonizing gas wherein producing can be inflammable gas, this inflammable gas can be used for the generating of internal combustion generator group, also can replace town gas or Sweet natural gas for user directly.
According to the organic materials carbonization decomposition vapourizing furnace 100 of the utility model embodiment, can completely cut off air destructive distillation processing to organic materials, not only environmental friendliness but also cost are low, can make full use of existing resource.See as an example of the industrial experiment result of low order matter coal foam and resinous shale foam example, combustiblecomponents in these two kinds of materials all can be decomposed out according to organic materials treatment system of the present utility model, taking Hami mire hair lake brown coal as example, inflammable gas can all be separated out and partly be separated out and do not have foeign element to produce new ash content.Raw coal enters stove and smokeless fuel is come out of the stove material ratio by 1.6:1 ton left and right (being referred to air dried basis coal foam), and discharge device is for doing material system device, and without any water content consumption, the smokeless fuel of discharge is low temperature siccative.The light-end products rate of recovery is that raw material oil product content reaches 98%, and is all light-end products, and proportion is in 0.9 left and right.Brown coal inflammable gas productive rate is at 400m
3/ t raw coal, calorific value is at 17-33MJ/m
3left and right.
In the time the organic materials of for example domestic refuse being completely cut off to air destructive distillation processing, in the gas that destructive distillation obtains and polity's ejecta, can not produce dioxin, and heavy metal free pollutes, the solid ejecta of output can be used as smokeless fuel, combustion-supporting without oil spout, not only environmental friendliness but also with low cost, thus make full use of existing resource.
In addition, this organic materials carbonization decomposition vapourizing furnace 100 is easy to use, starts to produce and to stop production process simple, and technique whole process can realize automatization control.
In an embodiment of the present utility model, multiple destructive distillation chamber 120 is arranged side by side in the horizontal direction, and each destructive distillation chamber 120 extends along the vertical direction, as shown in Figure 1.
In an embodiment of the present utility model, organic materials carbonization decomposition vapourizing furnace 100 also comprises: top feed bin 141 and automatic feeding device 142.
The top of top feed bin 141 is opened wide, and the bottom of top feed bin 141 is communicated with the opening for feed of pyrolysis gasification body of heater 110.For example, in the example of Fig. 1, top feed bin 141 is located at the top of pyrolysis gasification body of heater 110, the top of top feed bin 141 opens wide that the material for the treatment of destructive distillation is fed from the top of top feed bin 141, the bottom of top feed bin 141 is connected with the opening for feed of pyrolysis gasification body of heater 110, so that the material in top feed bin 141 is fed in pyrolysis gasification body of heater 110 by this opening for feed, for example top feed bin 141 is formed as doline.Certainly, the utility model is not limited to this, and in other example of the present utility model, top feed bin 141 also can be formed as cylindrical, the cylindroid bodily form, the long cylinder bodily form or the prism bodily form etc.
With reference to Fig. 1, automatic feeding device 142 is located between the bottom of top feed bin 141 and the opening for feed of pyrolysis gasification body of heater 110 and feeds in pyrolysis gasification body of heater 110 with the material of controlling in top feed bin 141.In the example of Fig. 1, automatic feeding device 142 is for being located at the valve on the pipeline between the bottom of top feed bin 141 and the opening for feed of pyrolysis gasification body of heater 110.Further, automatic feeding device 142 is motorized valve.
Further, the opening for feed place of pyrolysis gasification body of heater 110 is further provided with the distribution passage 150 for distributing material.With reference to Fig. 1, distribute passage 150 to be located between the bottom of top feed bin 141 and the top of body of heater, to distribute the material feeding in body of heater.
Particularly, distribute passage 150 to be formed as down Y shape, and distribute passage 150 to comprise the upper channel 151, the first lower channel 153 and the second lower channel 152 that communicate with each other.Wherein the top of upper channel 151 is communicated with the bottom of top feed bin 141, and the bottom of the first lower channel 153 and the second lower channel 152 is led to respectively in pyrolysis gasification body of heater 110.
For example, in the example of Fig. 1, upper channel 151 extends along the vertical direction, and the top of upper channel 151 is connected with the bottom of top feed bin 141, the bottom of upper channel 151 is connected with the top of the first lower channel 153 and the top of the second lower channel 152 respectively, particularly, first oblique left-hand downward-extension of the first lower channel 153, extend straight down again, under the first oblique dextrad of the second lower channel 152, extend straight down again, the bottom of the first lower channel 153 and the second lower channel 152 is connected with the top of pyrolysis gasification body of heater 110 respectively and communicates with the spatial accommodation of pyrolysis gasification body of heater 110, so that the destructive distillation material for the treatment of in top feed bin 141 is passed in pyrolysis gasification body of heater 110.
In an embodiment of the present utility model, organic materials carbonization decomposition vapourizing furnace 100 further comprises: distribution device 160, distribution device 160 is located at opening for feed below and distributes with the material that opening for feed is fed.See figures.1.and.2, distribution device 160 is located in the spatial accommodation of pyrolysis gasification body of heater 110 and is positioned at the top of spatial accommodation, the material feeding from top feed bin 141 is distributed to equably in multiple destructive distillation chamber 120 of below.
Further, as depicted in figs. 1 and 2, distribution device 160 comprises strut member 161 and multiple backgauge part 162.Strut member 161 extends along longitudinal (left and right directions as shown in Figure 1) of pyrolysis gasification body of heater 110.
One end of each backgauge part 162 is connected on strut member 161, and the other end of each backgauge part 162 extends to the inwall place of contiguous pyrolysis gasification body of heater 110.See figures.1.and.2, multiple backgauge part 162 each intervals are arranged, and each backgauge part 162 all extends towards the direction of the inwall of pyrolysis gasification body of heater 110 from a side wall surface of strut member 161, it will be appreciated that, can try one's best near the inwall of pyrolysis gasification body of heater 110, to have good cloth effect in one end away from strut member 161 of backgauge part 162.
Further, multiple backgauge parts 162 comprise multiple the first backgauge parts and multiple the second backgauge part, multiple the first backgauge parts and multiple the second backgauge part are spaced apart from each other along the length direction of strut member 161 respectively, and multiple the first backgauge part and multiple the second backgauge parts spaced apart predetermined distance on the width of strut member 161.
In one of them example of the present utility model, multiple the first backgauge parts and multiple the second backgauge part are corresponding one by one respectively on the length direction of strut member 161, as shown in Figure 2.Certainly, the utility model is not limited to this, in other examples of the present utility model, multiple the first backgauge parts and multiple the second backgauge part also can be on the length direction of strut member 161 staggered arrangement (scheming not shown).
Further, for example, in the example of Fig. 1 and Fig. 2, backgauge part 162 is along laterally (fore-and-aft direction as shown in Figure 1) extension, and now backgauge part 162 is substantially vertical with strut member 161, that is to say, the angle between strut member 161 and each backgauge part 162 is roughly 90 °.But, in other examples of the present utility model, backgauge part 162 is also tiltably connected on strut member 161, now the angle between strut member 161 and each backgauge part 162 is roughly between 0 °～90 ° or 90 °～180 °, here, it should be noted that, the angle between strut member 161 and each backgauge part 162 does not comprise 90 °.
Further, multiple backgauge parts 162 are evenly distributed on the both lateral sides of strut member 161.In other words, as depicted in figs. 1 and 2, on the length direction of strut member 161, between backgauge part 162 adjacent one another are, spaced distance is roughly equal.
In an example of the present utility model, strut member 161 is identical with the shape of backgauge part 162, particularly, as shown in Figure 2, each in strut member 161 and backgauge part 162 includes symmetrically arranged the first plate and the second plate on cross section, forms the angle of 30-180 degree between the first plate and the connection of the second plate upper end and the first plate and the second plate.
Further, on strut member 161, be formed with ventilating pit, be connected with the ventpipe 163 of vertical extension on ventilating pit, wherein air outlet is made up of ventpipe 163.For example, in the example of Fig. 1 and Fig. 2, the center of top of strut member 161 is formed with the ventilating pit that runs through it, ventpipe 163 vertically extends, and the bottom of ventpipe 163 is connected with ventilating pit, its top is connected with the top of pyrolysis gasification body of heater 110, the carbonizing gas producing after destructive distillation is discharged via ventpipe 163, and the composition of carbonizing gas can comprise methane, hydrogen, hydrocarbon polymer, carbon monoxide, carbonic acid gas, nitrogen etc.Certainly, the utility model is not limited to this, in other example of the present utility model, also can be formed with multiple ventilating pits on strut member 161, is connected with respectively the ventpipe 163 (scheming not shown) of multiple vertical extensions on multiple ventilating pits.
In an embodiment of the present utility model, organic materials carbonization decomposition vapourizing furnace 100 further comprises: multiple automatic-sealed discharge devices 170, multiple automatic-sealed discharge devices 170 are located at respectively the discharge gate 122 of multiple destructive distillation chamber 120 and sentence opening and closing discharge gate 122.As shown in Figure 1, multiple automatic-sealed discharge devices 170 are located at respectively the bottom of multiple destructive distillation chamber 120, and when automatic-sealed discharge device 170 is during in open mode, the solid matter that the interior destructive distillation of pyrolysis gasification body of heater 110 obtains can be discharged via discharge gate 122.
Further, with reference to Fig. 1, organic materials carbonization decomposition vapourizing furnace 100 also comprises sealing discharging storehouse 180 and chain type discharge device 200.Sealing discharging storehouse 180 is located at the bottom of pyrolysis gasification body of heater 110, and sealing discharging storehouse 180 and pyrolysis gasification body of heater 110 internal communication, wherein the bottom of multiple destructive distillation chamber 120 extend in sealing discharging storehouse 180, and the solid matter that destructive distillation obtains falls in sealing discharging storehouse 180 after discharging via discharge gate 122.
Chain type discharge device 200 is located in sealing discharging storehouse 180 to be received from material that dynamic seal discharge device 170 discharges and by its discharge.
Further, organic materials carbonization decomposition vapourizing furnace 100 also comprises: support frame of furnace body 190, support frame of furnace body 190 is located on the outer side wall of lower portion of furnace body so that body of heater is supported.For example, in the example of Fig. 1, support frame of furnace body 190 is located at the bottom of body of heater, and is positioned at the top in sealing discharging storehouse 180.
The working process of organic materials carbonization decomposition vapourizing furnace 100 is as follows: the material for the treatment of destructive distillation enters in organic materials carbonization decomposition vapourizing furnace 100 continuously, run into the high temperature hot gas being risen by bottom and carry out reverse exchange, remove the moisture that carry material outside, material is advanced into interior being dried respectively and destructive distillation in multiple destructive distillation chamber 120 of below under continuing, provide continuous carbonization thermal source by the electrically heated rod in destructive distillation chamber 120, the additive that the powder that such as smokeless fuel of the solid matter that destructive distillation afterwards obtains or building trade are used and cement industry use etc. is discharged by the automatic-sealed discharge device 170 of pyrolysis gasification body of heater 110 bottoms, the gas that destructive distillation obtains is discharged via the ventpipe 163 of pyrolysis gasification body of heater 110 tops.
In embodiment more of the present utility model, organic materials treatment system can also comprise primary screen subset (scheming not shown), and primary screen subset is connected to the upstream of organic materials carbonization decomposition vapourizing furnace 100 so that pending organic materials is sieved.For example, in embodiment more of the present utility model, for low-rank coal foam and/or resinous shale foam, the particle diameter of coal foam or resinous shale foam can be screened as being not more than 5mm, to carry out better destructive distillation.
Particularly, this primary screen subset can comprise strip-type screen (scheming not shown), and strip-type screen is for screening out a part of heavy seeds of pending organic materials.Particularly, use strip-type screen can go out taking metal as main a small amount of heavy seeds.
In embodiment more of the present utility model, organic materials treatment system also comprises the dewatering unit (scheming not shown) for organic materials is dewatered, and dewatering unit is located between primary screen subset and organic materials carbonization decomposition vapourizing furnace 100.Particularly, the impurity after primary screen subset screens out can carry out processed in dewatering unit.
In embodiment more of the present utility model, when organic materials is byproduct schlempe and vinasse, plant leaves, industrial refuse, medical waste, low-rank coal foam, resinous shale foam or its mixture of rubbish alive, agricultural byproducts stalk, cotton stalk, wine brewing, organic materials treatment system also comprises molding device (scheming not shown), and molding device is located between dewatering unit and organic materials carbonization decomposition vapourizing furnace 100 with by the organic materials mixing moulding after dehydration.
As shown in Figure 3, in embodiment more of the present utility model, carbonization gas washing plant can comprise elementary carbonization gas washing tower 210.Particularly, as shown in Figure 3, elementary carbonization gas washing tower 210 can comprise the first tower body 211 and flashback tank 212.
Wherein, the top of the first tower body 211 has the first carbonization gas entrance 2111, the carbonization gas producing through organic materials carbonization decomposition vapourizing furnace 100, from discharge the air outlet of organic materials carbonization decomposition vapourizing furnace 100, can enter in the first tower body 211 and wash via this first carbonization gas entrance 2111.And the top of the first tower body 211 has the first recirculated water entrance 2112, what be worth understanding is, this the first recirculated water entrance 2112 is positioned at the first carbonization gas entrance 2111 tops, so that the carbonization gas entering from the first carbonization gas entrance 2111, mix through the recirculated water flowing into the first recirculated water entrance 2112 from the upper side, thereby complete washing.Elementary carbonization gas washing tower 210 can be removed most of dust, the heavy wet goods in carbonization gas.
As shown in Figure 3, the middle part of the first tower body 211 can be provided with the first carbonization gas outlet 2113, at the interior carbonization gas through washing of the first tower body 211, can discharge and proceed from this first carbonization gas outlet 2113 operation in downstream.The bottom of the first tower body 211 is provided with water oil-in 2114, the carbonization gas producing through organic materials carbonization decomposition vapourizing furnace 100 is after the interior washing of the first tower body 211, can produce water-oil mixture body, this mixed solution can enter into from this water oil-in 2114 flashback tank 212 that is arranged in the first tower body 211 bottoms, be that flashback tank 212 is communicated with by this water oil-in 2114 with the first tower body 211, wherein, the top of flashback tank 212 is formed with the first tar overflow port 2121, in water-oil mixture body flow into flashback tank 212, and when liquid level slowly rises to the first tar overflow port 2121, water-oil mixture can overflow and can collect it from this first tar overflow port 2121, in order to avoid too much water-oil mixture is too much guided in the first tower body 211 from water oil-in 2114 in the interior storage of this flashback tank 212.
Preferably, as shown in Figure 3, elementary carbonization gas washing tower 210 can also be provided with water dispenser box 213.This water dispenser box 213 can be located at the top of the first tower body 211, and the first recirculated water entrance 2112 is located on water dispenser box 213.Particularly, this the first recirculated water entrance 2112 can be located at the top of water dispenser box 213, on the diapire of water dispenser box 213 or sidewall, can be provided with multiple water dispenser mouths, the recirculated water flowing into from the first recirculated water entrance 2112, can flow out from multiple water dispenser mouths, thus, recirculated water can flow to the first tower body 211 inside from multiple directions carbonization gas is cleaned, in other words, at the top of the first tower body 211, water dispenser box 213 is set, thereby can distribute equably recirculated water, improve the contact area of recirculated water and carbonization gas, clean more even.
In optional embodiment more of the present utility model, elementary carbonization gas washing tower 210 can also comprise multiple the first Venturi meters 214, multiple the first water spray pipe 215 and the second Venturi meter 216.Particularly, multiple the first Venturi meters 214, multiple the first water spray pipe 215 and the second Venturi meter 216 can all be located in the first tower body 211.
Wherein, as shown in Figure 3, multiple the first Venturi meters 214 can be arranged side by side and each the first Venturi meter 214 extends along vertical direction, and the top of multiple the first Venturi meters 214 can be lower than the first carbonization gas entrance 2111.Further, one end (example upper end as shown in Figure 3) of each the first water spray pipe 215 is connected with water dispenser box 213, particularly, each the first water spray pipe 215 upper ends can be connected on the multiple water dispenser mouths on water dispenser box 213, and each first water spray pipe 215 the other ends (example lower end as shown in Figure 3) can stretch in corresponding the first Venturi meter 214 to the carbonization gas entering from the first carbonization gas entrance 2111 is rinsed.That is to say, multiple the first water spray pipes 215 arrange one to one with multiple the first Venturi meters 214, like this, the carbonization gas entering from the first carbonization gas entrance 2111, can enter into respectively in multiple the first Venturi meters 214 that are arranged side by side, and rinse under the sprinkling of the first water spray pipe 215 in each the first Venturi meter 214.
Wherein, the second Venturi meter 216 can be positioned at multiple the first Venturi meter 214 belows, and the carbonization gas after rinsing respectively from multiple the first Venturi meters 214 can collect and flow to the bottom of the first tower body 211 in the second Venturi meter 216.
In embodiment more of the present utility model, carbonization gas washing plant can also comprise secondary carbonization gas washing tower 220.Secondary carbonization gas washing tower 220 can be located at the downstream of elementary carbonization gas washing tower 210.
Particularly as shown in Figure 4, secondary carbonization gas washing tower 220 comprises the second tower body 221, the second water spray pipe 222 and multiple distribution heat exchange tower tray 223.The bottom of the second tower body 221 has the second carbonization gas entrance 2211, and the carbonization gas of discharging from the first carbonization gas outlet 2113 of elementary carbonization gas washing tower 210 can enter in secondary carbonization gas washing tower 220 and carry out secondary washing from the second carbonization gas entrance 2211.The top of the second tower body 221 can be provided with the second carbonization gas outlet 2212, and the carbonization gas after 220 washings of secondary carbonization gas washing tower can be discharged from this second carbonization gas outlet 2212, and proceeds the operation in downstream.Wherein, secondary carbonization gas washing tower 220 can be from removing the lightweight oil carbonization gas and being unfavorable for the washing liq of burning.
Alternatively, as shown in Figure 4, the second carbonization gas entrance 2211 is connected with dry main 226, and the other end of dry main 226 extends upwardly to the top that exceeds the second tower body 221.Like this, carbonization gas, from elementary carbonization gas washing tower 210 is discharged, can flow in the second tower body 221 from dry main 226, can make thus to enter into carbonization gas in the second tower and first flow through one section of pipeline and carry out coolingly, improves cleaning performance.
Wherein, the second water spray pipe 222 can be provided with and insert into the inner from the middle part of the second tower body 221, and recirculated water can flow into and be sprayed onto the second his tower body from this second water spray pipe 222.Advantageously, the second water spray pipe 222 can be multiple and interval arranges, and on each the second water spray pipe 222, can be provided with multiple isolated water and spray mouthful, can make thus recirculated water more all be sprayed onto in the second tower, and then can improve the homogeneity of the flushing to carbonization gas.
As shown in Figure 4, multiple distribution heat exchange tower trays 223 can and be spaced apart from each other along the vertical direction along the radially setting of the second tower body 221.In other words, each distribution heat exchange tower tray 223 can be along the radially setting of the second tower body 221, and multiple distribution heat exchange tower tray 223 can be spaced apart from each other respectively along the vertical direction.Here what deserves to be explained is, the complicated component of carbonization gas is various, the density difference of the gas of each composition, can cause thus in the second tower body 221, the gaseous constituent that density is little can rise to the second tower body 221 tops rapidly, and the speed that the large gaseous constituent of density rises is relatively slower, for can being mixed, multicomponent gas discharges the second tower body 221, can arrange and distribute heat exchange tower tray 223 along the radial direction of the second tower body 221 thus, distribute thus heat exchange tower tray 223 to play the effect of keeping out to zooming gas, multi-component gas continues to rise after can mixing below distribution heat exchange tower tray 223 again.Further, by multiple multiple distribution heat exchange tower trays 223 that arrange are along the vertical direction set, thereby can multi-component gas through repeatedly mixing, finally discharge from the second carbonization gas outlet 2212 again.
Alternatively, secondary carbonization gas washing tower 220 can also comprise water seal cylinder 224 and washings liquid discharge pipe 225.As shown in Figure 4, the top of water seal cylinder 224 has the second tar overflow port 2241, one end (for example upper end in Fig. 4) of washings liquid discharge pipe 225 is communicated with the bottom of the second tower body 221, for example, and the second end of washings liquid discharge pipe 225 (lower end in Fig. 4) extend into the bottom in water seal cylinder 224, the lower end of water seal cylinder 224 lower than the lower end of the second tower body 221 so that the water of condensation in the second tower body 221 is discharged in water seal cylinder 224.And by the second tar overflow port 2241 is set, thereby after can making to be pooled in water seal cylinder 224 to a certain degree, be that liquid level is while exceeding the second tar overflow port 2241, washings can be discharged and can collect it from this second tar overflow port 2241, in order to avoid washings is got back in the second tower body 221 from washings liquid discharge pipe 225 adverse currents.
As shown in Figure 4, in a preferred exemplary of the present utility model, the bottom of the second tower body 221 can also be provided with cleanout opening 2213, and cleanout opening 2213 is lower than one end of washings liquid discharge pipe 225.By this cleanout opening 2213 is set, thereby operator can carry out the cleaning of impurity from this cleanout opening 2213, facilitate impurity or pollutant sediment to the second tower body 221 bottoms, even stop up washings liquid discharge pipe 225.
As shown in Figure 5, self-cleaning heat-exchange equipment 300 can be located at the downstream of secondary carbonization gas washing tower 220, self-cleaning heat-exchange equipment 300 comprises at least self-cleaning interchanger 310 of one-level, and each self-cleaning interchanger 310 comprises housing 311, multiple heat transfer tube 312, gas filter 313 and multiple self-cleaning heat exchange tower tray 314.
In housing 311, can there is directed along the vertical direction square tube shape gas compartment, the top of housing 311 has pneumatic outlet 3111, can discharge from this pneumatic outlet 3111 at the interior carbonization gas after clean of self-cleaning heat-exchange equipment 300, the bottom of housing 311 has gas inlet 3112, the carbonization gas of discharging from secondary carbonization gas washing tower 220 like this, can flow into self-cleaning heat-exchange equipment 300 and clean from this gas inlet 3112.
Multiple heat transfer tubes 312 are distributed as the multilayer being spaced apart from each other on above-below direction, and each heat transfer tube 312 can be configured to for example, be configured to plum blossom-shaped along laterally (in Fig. 5 with the perpendicular direction of above-below direction).In each heat transfer tube 312, be connected with water coolant, thus, the carbonization gas flowing out from gas inlet 3112 upwards flow, and with each heat exchange after carry out heat exchange, obtain cooling.Gas filter 313 be located at bottom in housing 311 and higher than gas inlet 3112 with to entering the gas filtration in housing 311, multiple self-cleaning heat exchange tower trays 314 are along the radially setting of housing 311 and be spaced apart from each other along the vertical direction, and wherein each self-cleaning heat exchange tower tray 314 can be arranged on wherein between two-layer heat transfer tube 312.Similar with the distribution heat exchange tower tray 223 in secondary carbonization gas washing tower 220, by self-cleaning heat exchange tower tray 314 is set, thereby can make the multi-component gas rising mix rear discharge.
Wherein, the bottom of housing 311 is provided with washings relief outlet 3113, and wherein washings, higher than washings relief outlet 3113, thus, can be discharged from this washings relief outlet 3113 in gas inlet 3112.
In a concrete example of the present utility model, as shown in Figure 4, self-cleaning heat exchange tower tray 314 comprises three.Can, ensureing, under other prerequisites that mix of multicomponent, to reduce equipment investment, reduce costs thus.
As shown in Figure 5, in an optional example of the present utility model, on housing 311, can have cooling water connector 3114, cooling water connector 3114 is communicated with to feed water coolant with multiple heat transfer tubes 312.
On the outer wall of housing 311, be also provided with water wall 315.On this water wall 315, can pass into water coolant with this, with further with self-cleaning heat-exchange equipment 300 in carbonization gas carry out heat exchange, make it cooling.
In embodiment more of the present utility model, each self-cleaning interchanger 310 can also comprise exporting flutters day with fog 316, self-cleaning uniform divider 317 and desulfurizing scrubber 318.
Outlet is flutterred day with fog 316 and is located in housing 311 and is arranged in pneumatic outlet 3111 belows and separate with the drop that gas is mingled with, self-cleaning uniform divider 317 is located at multiple heat transfer tubes 312 tops and carries out uniformly distributing with the gas in housing 311, desulfurizing scrubber 318 is located in housing 311 and flutters between day with fog 316 and self-cleaning uniform divider 317, so that gas is carried out to desulfurization in outlet.
That is to say, pneumatic outlet 3111, outlet are flutterred day with fog 316, desulfurizing scrubber 318, self-cleaning uniform divider 317 and self-cleaning heat exchange tower tray 314 and are arranged in order from top to bottom.
Gas inlet 3112 is connected with dry main 226, and the other end of dry main 226 extends upwardly to the top that exceeds housing 311.Thus, first the carbonization gas of discharging from secondary carbonization gas washing tower 220, can flow and lower the temperature from this dry main 226, then in self-cleaning heat-exchange equipment 300.
To sum up, after washing, gas carries out de-oiling, dehydration, cooling through self-cleaning heat-exchange equipment 300, and the lightweight oil that self-cleaning heat-exchange equipment 300 produces and weakly alkaline liquid can carry out desulfurization, de-naphthalene to gas.
In embodiment more of the present utility model, organic materials treatment system can also comprise washings circulation vessel (scheming not shown).Washings circulation vessel is communicated with the second tar overflow port 2241 and second water spray pipe 222 of the first tar overflow port 2121 of elementary carbonization gas washing tower 210 and the first recirculated water entrance 2112, secondary carbonization gas washing tower 220 respectively, the first washings that wherein the interior first washing of elementary carbonization gas washing tower 210 produces is afterwards discharged in washings circulation vessel and isolates tar, dust and the first water of condensation from the first tar overflow port 2121, and the first water of condensation is got back to the first recirculated water entrance 2112; The second washings producing after secondary carbonization gas washing tower 220 interior secondary washing is discharged to state in washings circulation vessel from the second tar overflow port 2241 isolates tar, dust and the second water of condensation, and the first water of condensation is got back to the second water spray pipe 222.
That is to say, by this washings circulation vessel is set, thereby elementary carbonization gas washing tower 210 can be entered to the impurity such as tar, dust that interior washing produces with secondary carbonization gas washing tower 220 separates with water of condensation, and by water of condensation send back to elementary carbonization gas washing tower 210 enter with secondary carbonization gas washing tower 220 in, carry out recycle.Tar after sedimentation can regularly be drawn to oil tank China and foreign countries and sell.
Further, the washings that this washings circulation vessel can also be connected and discharge to receive with the self-cleaning interchanger 310 of one-level at least, and the impurity such as tar, dust in this washings is separated with the 3rd water of condensation, and the 3rd water of condensation is sent back to cooling water connector 3114.
According to the organic materials treatment system of the utility model embodiment, carry out destructive distillation and produce carbonization gas by first organic materials being passed into organic materials carbonization decomposition vapourizing furnace 100, again carbonization gas is passed into successively in carbonization gas washing plant and self-cleaning heat-exchange equipment 300, carry out washing, purifying and processing, finally can obtain clean flammable carbonizing gas, can reduce thus the impact of organic materials on environment, and by the above-mentioned treating processes to organic materials, the flammable energy can also be obtained, thereby the maximization of organic materials utility value can be made.
As mentioned above, for the organic materials of for example domestic refuse, compared with the existing processing mode of burning away the refuse generally adopting, the gas producing according to the organic materials treatment system of the utility model embodiment and solid emission all do not produce dioxin and heavy metal contamination, after processing without waste residue, the solid of output can be used as smokeless fuel, its calorific value is more than per kilogram 5000 kilocalories, certainly also can follow according to actual needs, allow the complete destructive distillation of material, the additive that the powder that output building trade is used and cement industry use.Simultaneously output is used for the carbonizing gas of generating, taking domestic refuse as example: calorific value is more than every cubic metre of 6000 kilocalories.For the lignitoid coal foam of example, according to organic materials treatment system of the present utility model, not only can obtain the recovering of vaporized hydrocarbons rate up to 98%, and the gas yield of routine lignitoid conny can reach 400m
3/ t raw coal, calorific value is at 17-33MJ/m
3left and right.
In process of production, the temperature of organic materials carbonization decomposition vapourizing furnace 100 inside can arbitrarily regulate, start production and stop production process simple, technique whole process can realize automatization control, the inflammable gas producing both can, with the generating of internal combustion generator group, also can replace town gas or Sweet natural gas for user directly.This technique can also further be applicable to following material: the organic materials mixtures such as the byproduct schlempe of agricultural byproducts stalk, cotton stalk wine brewing and vinasse, plant leaves, industrial refuse, medical waste, domestic refuse.
In the time being used for cracking low-rank coal foam and resinous shale foam according to organic materials treatment system of the present utility model, production process is safe and reliable, operation is full-automatic, discharge without three wastes material, make coal at a low price become smokeless fuel, reduce the pollution to environment, the Application Areas of coal is more extensive, environmental protection.
Below with reference to Fig. 6, this organic materials treatment process is described.
As shown in Figure 6, this treatment process comprises the following steps.Organic materials is completely cut off to air destructive distillation and produces solid materials, carbonization gas and tar (step S1).Step S1 can complete in organic materials carbonization decomposition vapourizing furnace 100.
Carbonization gas is carried out to washing, purifying to remove tar (step S2).This step S2 can complete in carbonization gas washing plant, and particularly, this step S2 can complete in elementary carbonization gas washing tower 210 and secondary carbonization gas washing tower 220.
Carbonization gas after washing, purifying in step S2 is carried out to elementary de-oiling, dehydration, desulfurization, de-naphthalene, and obtain clean gas (step S3).By this step S3, the impurity such as tar, dust in organic materials can be separated, and carry out de-oiling, dehydration, desulfurization, de-naphthalene, and obtain clean gas, finally can obtain clean gas, can reach industry and civilian combustible gas use standard.
Further, step S2 can comprise the steps:
S21, carbonization gas is carried out to first washing to remove dust and heavy tar.Particularly, in this step, can carry out the first washing of spraying by the recirculated cooling water of 60-65 degree.
S22, to carbonization gas carry out secondary washing with remove tar light oil.Particularly, in this step, can carry out secondary washing by the cold cycle water coolant of 40-60 degree.
Further, after this organic materials treatment process also comprises the steps: step S2 to process with in S3 the washings that obtains reclaim, sedimentation separate to obtain dust, tar and water coolant, in cooling water circulation treating processes of getting back to step S2 (step S4).Particularly, in this step S4, also comprise that washings is heated to 60-65 degree isolates tar with natural sedimentation.
Further, as shown in Figure 6, this organic materials treatment process can also comprise the step (step S5) that the solid materials to producing in step S1 reclaims.
In some optional embodiment, in the time for example processing the organic materialss such as domestic refuse, further comprising the steps of before step S1: S01: organic materials is carried out to elementary screening.This step can be carried out in primary screen subset.Particularly, this light material is crushed to below 5 millimeters.S02: the organic materials that step S01 is obtained carries out processed and light material fragmentation is wherein pulverized.This step can complete in dewatering unit.S03: the organic materials of processing through step S02 is carried out to mixing moulding processing.
And for the organic materials of for example low-rank coal foam and/or resinous shale foam, further comprising the steps of before step S1: S01: described organic materials is carried out to elementary screening, and the particle diameter of wherein said organic materials is not more than 5mm; S02: the organic materials that step S01 is obtained carries out processed and light material fragmentation is wherein pulverized.
By adopting according to this organic materials treatment process, the impurity such as tar, dust in organic materials can be separated, and carry out de-oiling, dehydration, desulfurization, de-naphthalene, and obtain clean gas, finally can obtain clean gas, can reach industry and civilian combustible gas use standard.In above-mentioned organic materials treatment system and method, can at utmost contamination-freely utilize conventional example as the organic materials of rubbish, low-rank coal foam etc., farthest to make full use of this organic materials.
In the description of this specification sheets, the description of reference term " embodiment ", " some embodiment ", " illustrative examples ", " example ", " concrete example " or " some examples " etc. means to be contained at least one embodiment of the present utility model or example in conjunction with specific features, structure, material or the feature of this embodiment or example description.In this manual, the schematic statement of above-mentioned term is not necessarily referred to identical embodiment or example.And specific features, structure, material or the feature of description can be with suitable mode combination in any one or more embodiment or example.
Although illustrated and described embodiment of the present utility model, those having ordinary skill in the art will appreciate that: in the situation that not departing from principle of the present utility model and aim, can carry out multiple variation, amendment, replacement and modification to these embodiment, scope of the present utility model is limited by claim and equivalent thereof.
Claims (15)
1. an organic materials carbonization decomposition vapourizing furnace, is characterized in that, comprising:
Pyrolysis gasification body of heater, described pyrolysis gasification body of heater is provided with opening for feed and air outlet;
Multiple destructive distillation chamber, described multiple destructive distillation chamber juxtaposition is in described pyrolysis gasification body of heater, and spaced apart between two adjacent destructive distillation chambers, and bottom, each described destructive distillation chamber is equipped with discharge gate; And
Electrically heated rod, it is indoor so that the indoor material of described multiple destructive distillation is completely cut off to air destructive distillation, to produce solid carbonaceous material and carbonization gas that described electrically heated rod is located at described multiple destructive distillation vertically.
2. organic materials carbonization decomposition vapourizing furnace according to claim 1, it is characterized in that, described multiple destructive distillation chamber juxtaposition is in described pyrolysis gasification body of heater, and two adjacent described destructive distillation chambers are spaced apart from each other, and described discharge gate is located at respectively the bottom of each described destructive distillation chamber.
3. organic materials carbonization decomposition vapourizing furnace according to claim 1, is characterized in that, also comprises:
Top feed bin, the top of described top feed bin is opened wide, and the bottom of described top feed bin is communicated with the opening for feed of described pyrolysis gasification body of heater; And
Sealed automatic feeding device, the material that described sealed automatic feeding device is located between the bottom of described top feed bin and the opening for feed of described pyrolysis gasification body of heater to completely cut off air and control in the feed bin of top is supplied in described pyrolysis gasification body of heater.
4. organic materials carbonization decomposition vapourizing furnace according to claim 3, is characterized in that, described top feed bin is formed as doline.
5. organic materials carbonization decomposition vapourizing furnace according to claim 3, is characterized in that, described sealed automatic feeding device is the motorized valve on the pipeline being located between the bottom of described top feed bin and the opening for feed of described pyrolysis gasification body of heater.
6. organic materials carbonization decomposition vapourizing furnace according to claim 3, is characterized in that, the opening for feed place of described pyrolysis gasification body of heater is further provided with:
For distributing the distribution passage of material, described distribution channels configuration becomes described material is introduced in described pyrolysis gasification body of heater equably.
7. organic materials carbonization decomposition vapourizing furnace according to claim 6, it is characterized in that, described distribution tunnel-shaped becomes down Y shape and comprises the upper channel, the first lower channel and the second lower channel that communicate with each other, the top of wherein said upper channel is communicated with the bottom of described top feed bin, and the bottom of the first lower channel and the second lower channel is led to respectively in described pyrolysis gasification body of heater.
8. according to the organic materials carbonization decomposition vapourizing furnace described in any one in claim 3-7, it is characterized in that, further comprise:
Distribution device, described distribution device is located at described opening for feed below, carries out uniformly distributing with the material that described opening for feed is fed.
9. organic materials carbonization decomposition vapourizing furnace according to claim 8, is characterized in that, described distribution device comprises:
Strut member, described strut member is extending longitudinally along described pyrolysis gasification body of heater;
Multiple backgauge parts, one end of each described backgauge part is connected on described strut member and the other end extends along the horizontal inner side-wall towards described pyrolysis gasification body of heater.
10. organic materials carbonization decomposition vapourizing furnace according to claim 9, is characterized in that, described backgauge part extends transversely; And described multiple backgauge part is evenly distributed on the both lateral sides of described strut member.
11. organic materials carbonization decomposition vapourizing furnaces according to claim 9, it is characterized in that, described strut member is identical with the shape of described backgauge part, and each in described strut member and described backgauge part includes symmetrically arranged the first plate and the second plate on cross section, between described the first plate and the connection of the second plate upper end and described the first plate and the second plate, form the angle of 30-180 degree.
12. organic materials carbonization decomposition vapourizing furnaces according to claim 9, it is characterized in that, on described strut member, be fixedly installed the ventpipe of vertical extension, described ventpipe is formed with the venting channels being connected with the inside of described pyrolysis gasification body of heater, and described air outlet is formed on the exit end of described venting channels.
13. organic materials carbonization decomposition vapourizing furnaces according to claim 1, is characterized in that, further comprise:
Multiple automatic-sealed discharge devices, described multiple automatic-sealed discharge devices are located at respectively the described discharge gate place of described multiple destructive distillation chamber, so that blowing is carried out in described destructive distillation chamber.
14. organic materials carbonization decomposition vapourizing furnaces according to claim 13, is characterized in that, also comprise:
Sealing discharging storehouse, described sealing discharging storehouse be located at the bottom of described pyrolysis gasification body of heater and with described pyrolysis gasification body of heater internal communication, the bottom of wherein said multiple destructive distillation chamber extend in described sealing discharging storehouse;
Chain type discharge device, described chain type discharge device is located at material the discharge of in described sealing discharging storehouse, discharging to receive described automatic-sealed discharge device.
15. organic materials carbonization decomposition vapourizing furnaces according to claim 1, is characterized in that, described organic materials is low-rank coal foam or resinous shale foam.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420303706.0U CN203923096U (en) | 2013-06-09 | 2014-06-09 | Organic materials carbonization decomposition vapourizing furnace |
Applications Claiming Priority (5)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201310231560 | 2013-06-09 | ||
| CN201310231560.3 | 2013-06-09 | ||
| CN201310231392 | 2013-06-09 | ||
| CN201310231392.8 | 2013-06-09 | ||
| CN201420303706.0U CN203923096U (en) | 2013-06-09 | 2014-06-09 | Organic materials carbonization decomposition vapourizing furnace |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203923096U true CN203923096U (en) | 2014-11-05 |
Family
ID=51818951
Family Applications (2)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420303706.0U Expired - Fee Related CN203923096U (en) | 2013-06-09 | 2014-06-09 | Organic materials carbonization decomposition vapourizing furnace |
| CN201410253099.6A Active CN104232121B (en) | 2013-06-09 | 2014-06-09 | Organic materials carbonization decomposition gasification furnace and organic materials processing method |
Family Applications After (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201410253099.6A Active CN104232121B (en) | 2013-06-09 | 2014-06-09 | Organic materials carbonization decomposition gasification furnace and organic materials processing method |
Country Status (3)
| Country | Link |
|---|---|
| CN (2) | CN203923096U (en) |
| BR (1) | BR112015030168B1 (en) |
| WO (1) | WO2014198180A1 (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104232121A (en) * | 2013-06-09 | 2014-12-24 | 山东汉菱电气有限公司 | Organic material retorting cracking and gasifying furnace and organic material treatment method |
Families Citing this family (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105400527A (en) * | 2015-12-08 | 2016-03-16 | 北京神雾环境能源科技集团股份有限公司 | Pyrolysis reactor |
| DE102016006884A1 (en) * | 2016-06-03 | 2017-12-07 | Bernd Schottdorf | Apparatus and process for the continuous production of biochar and biochar produced by this process |
| CN107325834B (en) * | 2017-07-24 | 2018-05-25 | 辽宁清道夫环保工程有限公司 | Greasy dirt solid waste processing system and greasy dirt solid waste substance treating method |
| CN109666512A (en) * | 2019-02-18 | 2019-04-23 | 中国华能集团清洁能源技术研究院有限公司 | A kind of downlink Quench furnace moves the dry coal powder pressure gasifying device of heat outside |
| PL3919586T3 (en) * | 2020-06-04 | 2024-02-12 | Reimund SCHUSTER | Device for producing vegetable charcoal by pyrolysis of biomass |
Family Cites Families (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4469488A (en) * | 1980-05-27 | 1984-09-04 | Albert Calderon | Method for gasifying coal |
| CN2457159Y (en) * | 2000-11-24 | 2001-10-31 | 浙江省林业科学研究院 | Tubular type movable bed dry distillation carbide furnace |
| CN2564574Y (en) * | 2002-03-29 | 2003-08-06 | 康成 | Vertical coke oven |
| CN100532501C (en) * | 2006-08-25 | 2009-08-26 | 神木县三江煤化工有限责任公司 | Low-temperature coal carbonization kiln |
| JP2008297464A (en) * | 2007-05-31 | 2008-12-11 | Okawara Mfg Co Ltd | Cleaning method and device for pyrolysis gas |
| CN101230283B (en) * | 2008-02-01 | 2011-06-08 | 抚顺矿业集团有限责任公司 | Oil shale retorting process reclaiming method |
| CN102492432A (en) * | 2011-12-09 | 2012-06-13 | 新疆美特镁业有限公司 | Pulverized coal coking equipment and method |
| CN202898371U (en) * | 2012-11-13 | 2013-04-24 | 山东汉菱电气有限公司 | Weak-base source self-cleaning heat exchanger for purification, desulfurization, oil removal and dehydration of coal gas |
| CN102965129B (en) * | 2012-12-13 | 2014-01-15 | 山东汉菱电气有限公司 | Organic material gasification furnace |
| BR112015030168B1 (en) * | 2013-06-09 | 2021-04-27 | Shan Dong Hi-Link Electricity Co. Ltd | DRY DISTILLATION AND GASIFICATION OVEN FOR ORGANIC MATERIALS, AND SYSTEM FOR ORGANIC MATERIALS PROCESSING |
-
2014
- 2014-05-23 BR BR112015030168-1A patent/BR112015030168B1/en not_active IP Right Cessation
- 2014-05-23 WO PCT/CN2014/078332 patent/WO2014198180A1/en active Application Filing
- 2014-06-09 CN CN201420303706.0U patent/CN203923096U/en not_active Expired - Fee Related
- 2014-06-09 CN CN201410253099.6A patent/CN104232121B/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104232121A (en) * | 2013-06-09 | 2014-12-24 | 山东汉菱电气有限公司 | Organic material retorting cracking and gasifying furnace and organic material treatment method |
| CN104232121B (en) * | 2013-06-09 | 2018-06-19 | 山东汉菱电气有限公司 | Organic materials carbonization decomposition gasification furnace and organic materials processing method |
Also Published As
| Publication number | Publication date |
|---|---|
| CN104232121A (en) | 2014-12-24 |
| WO2014198180A1 (en) | 2014-12-18 |
| CN104232121B (en) | 2018-06-19 |
| BR112015030168A2 (en) | 2019-12-17 |
| BR112015030168B1 (en) | 2021-04-27 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN203923096U (en) | Organic materials carbonization decomposition vapourizing furnace | |
| CN103881738B (en) | Organic materials treatment system | |
| CN102776007A (en) | Continuous biomass pyrolytic carbon gas-oil poly-generation system | |
| EP2650347A1 (en) | Combined mixed gas system with gas purification and gas purification device | |
| CN103897713B (en) | A kind of organic materials total system and treatment process | |
| CN105841159A (en) | Garbage pyrolysis and catalytic splitting system | |
| CN203451476U (en) | Organic material dry distillation and cracking gasifier | |
| CN102786951B (en) | Crude gas guiding device for coal pyrolyzing furnace | |
| CN203128495U (en) | Organic material comprehensive processing system | |
| CN102815673B (en) | Sulfur slurry or sulfur paste conversion device and conversion process | |
| CN204644269U (en) | Stereo chamber type heat source type biological particles charring furnace | |
| CN202953980U (en) | Wild coal gas condensing device of coal pyrolysis furnace | |
| CN102786952B (en) | Crude gas condensing device for coal pyrolyzing furnace | |
| CN206483805U (en) | The system that a kind of sludge microwave residue after gasifying targets renovation of organic pollution soil | |
| CN205628880U (en) | System for handle organic rubbish | |
| CN205261567U (en) | Waste gasification boiler | |
| CN103087783B (en) | Device for exporting, condensing, recycling and purifying raw gas in coal pyrolysis furnace | |
| CN2921014Y (en) | Pool type stalks comprehensive utilization carbonizing device | |
| CN202898323U (en) | Raw gas exporting device of coal pyrolyzing furnace | |
| CN202881216U (en) | Delivery, condensation, recovery and purification device of raw gas in coal pyrolysis furnace | |
| CN205115380U (en) | Biomass pyrolyzing furnace | |
| CN203229490U (en) | External thermal-radiation type oil shale dry distillation system | |
| CN102936509B (en) | External heat radiation type dry distillation system for oil shale | |
| CN102786974A (en) | Automatic control method for crude gas lead-out and condensation of coal pyrolyzing furnace | |
| CN108611107A (en) | A kind of technique that low order coal grading high-efficiency cleaning utilizes |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20141105 Termination date: 20170609 |