CN1436833A - Electrical low-temperature charcoal-producing dry distillation process and apparatus - Google Patents
Electrical low-temperature charcoal-producing dry distillation process and apparatus Download PDFInfo
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- CN1436833A CN1436833A CN02113312A CN02113312A CN1436833A CN 1436833 A CN1436833 A CN 1436833A CN 02113312 A CN02113312 A CN 02113312A CN 02113312 A CN02113312 A CN 02113312A CN 1436833 A CN1436833 A CN 1436833A
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Abstract
The electric low-temperature charcoal-producing dry distillation process includes crushing plant material; drying in a drier, especially one airflow drier, heating the material in a material bin; extruding to form in the spiral extruder at 150-200; and low-temperature carbonating inside an electric carbonating furnace at 270-350 deg.c for 30 min to obtain charcoal product. The continuous production process has the features of hot starting step, homogeneous heating of the material, low temperature dry distillation and high charcoal yield.
Description
Technical field
The present invention relates to by method and corresponding mechanical means wooden or that the herbaceous stem vegetable material is produced charcoal.
Background technology
" wooden or herbaceous stem vegetable material " speech of Shi Yonging comprises biomass widely in this article, as: timber, wood chip, wood chip, branch, stalk, shell, until careless class, leaf etc.This term also comprises the cellulose materials after the processing, and other comes from the biomass of plant as stationery, bagasse, beet pulp etc." the warm start operating mode " of certain operation herein is meant that material temperature was basic identical when the inlet temperature of this operation material and a last operation finished, and promptly goes up and takes advantage of also decline of temperature of charge when an operation finishes, and directly enters subsequent processing and processes." carbonization degree " in the literary composition is the yield of charcoal to absolutely dry wood.The carbonization degree height promptly means the char yield height.
Conventional charcoal production method the earliest is to adopt earth kiln, by loading of kiln, igniting, firing, close operations such as kiln, cooling and carry out charing, there is very big drawback: 1, because the heat transfer property extreme difference of timber, in the kiln of piling up formula, for making most of carbonization of wood complete, must be heated to that high temperature carries out destructive distillation more than 900 ℃, also will keep more than 10 day waste heat baking after closing kiln, could destructive distillation become charcoal.The hyperoxidation situation often takes place in high temperature carbonization, and lumber consumption is big, and charcoal yield (in butt, down together) is very low, and charcoal is of poor quality.2, earth kiln is to heat in the oxidizing fire mode, and therefore, very most of raw material timber is consumed as fuel, greatly influences charcoal yield, simultaneous oxidation combustion effects charcoal quality (the underburnt burning is a common occurrence).3, in the mode of making charcoal of cutting firewood of the thick stem of felling timber, be a significant wastage to timber resources.
Artificial charcoal's serial equipment that Gongyi City, domestic Henan Province The Song Tombs wrapping mechanism factory produces, as branch crushing machine, drying machine, ZTJ spiral extrusion shaping machine, and ZTJ-6 type charring furnace belongs to representational s-generation equipment.This kind equipment was once introduced twice in inventor aspect in 1994, and net result is failed.This equipment disadvantage is too many, especially use the spiral propeller (most important component) in extrusion molding, in cold start-up, rise to again in 350 ℃ of pyritous environment and move suddenly, resistance that is run into and friction are very big, the damage at its most advanced and sophisticated position is exceedingly fast, and repairs very difficult (will repair repeatedly and heat-treatment quenching), can not normally move for a long time.Its charring furnace is to adopt the oxidizing fire mode to heat, and heat temperature raising is extremely slow in the body of heater of piling up formula, and production schedule is too useless soft, because of requiring the burning heating of secluding air, its flue dust is excessive, local method cut firewood the benefit of making charcoal all less than, last aforesaid device becomes a pile scrap iron.
Chinese patent literature discloses a kind of " production method of charcoal " (patent No. 951978519), it is water content to be up to 50% biomass material directly put into the metal tin of reactor carry out destructive distillation under 350-550 ℃ of temperature, (destructive distillation is that charing coal, charcoal etc. heat under the secluding air condition, is decomposed into gas, liquid and solid coke or charcoal." chemical industry dictionary " third edition king chief editor that admonishes P41), makes charcoal.Its shortcoming is, the one, tiny irregular raw material such as wood chip, wood chip, wood shavings, branch etc. are had inadaptability.Because finished product charcoal physical dimension is limited by the raw material shape, the finished product charcoal shape of above-mentioned raw materials is not easy to the user and uses; The 2nd, moisture content is too high during destructive distillation, and the destructive distillation time extends on the one hand, and the consumption of fuel is multiplied; Timber is sharply dry on the other hand since inside and outside be heated inhomogeneously, charcoal forms the crack, reduces the quality of charcoal; The 3rd, from theoretical and experiment, the output of charcoal reduces with the rising of carbonization temperature, and reduces in 270～400 ℃ of temperature ranges big (as to pine and birch pyrolysis experiment).Therefore, its carbonization temperature fixes on 350～550 ℃, and its corresponding char yield is not high enough.
Summary of the invention
The object of the present invention is to provide a kind of electrical low-temperature charcoal-producing dry distillation process, be intended to make the more reasonable and further raising of the temperature-rise period carbonization degree of raw material.Another purpose of the present invention is to be provided for the device of above-mentioned novel process, and it is exclusively used in and is satisfied with this processing requirement.Above-mentioned purpose is achieved through the following technical solutions: a kind of electrical low-temperature charcoal-producing dry distillation process, carry out according to the following steps in turn:
(A) adopt wooden and the herbaceous stem plant is a raw material, with the size and the size of raw material convenient processing of operation through pulverizer is crushed to after;
(B) raw material of being sent by the pulverizer outlet directly enters moisture eliminator, carries out drying;
(C) material that is come by dryer export is sent in the airtight storage bin of heating, and its temperature of charge is controlled at 80-150 ℃;
(D) material of being sent by storage bin directly enters extrusion machine under the situation of secluding air, heats simultaneously and extrusion molding, and the final material temperature is controlled at 150～200 ℃ during extrusion operation;
(E) molding materials that is come by extruder outlet is directly sent under the situation of secluding air in the electric heating charring furnace, destructive distillation under 270～350 ℃ of temperature, 30 minutes time of electric heating charing or still less;
(F) under the situation of secluding air, material after the destructive distillation is cooled to normal temperature, make the finished product charcoal at last.
Each step of above-mentioned A to F is carried out in turn continuously, so that each work in-process step B-E field is in the warm start operating mode.
Above-mentioned moisture eliminator is a pneumatic dryer, and raw material is heated by hot gas flow therein and be dry; Above-mentioned extrusion machine is a screw extrusion press; Adopt Electric heating to keep material during screw extruding briquetting, temperature extrusion molding material is the cylindrical shape of hollow.
Be exclusively used in the device of above-mentioned novel process, this device comprises: a pulverizer is used for above-mentioned raw materials is crushed to convenient size and the size of handling of back operation;
A pneumatic dryer, its opening for feed is connected with the pulverizer discharge port;
An airtight storage bin, the discharge port warp of pneumatic dryer, valve are connected with the storage bin opening for feed;
An electric heater is arranged in the storage bin, is used for the storage bin material is heated;
A screw extrusion press, being used for material forming is the hollow circuit cylinder bar, its opening for feed is communicated with through a valve with the storage bin discharge port;
An electric heater unit is arranged on the screw extrusion press shell, is used for material is heated;
The a plurality of electric heating charring furnaces that are used for the bar that splendid attire screw extrusion press discharge port sends, this charring furnace is a cylindrical shell, housing top is provided with a gas outlet tube, housing bottom is provided with a movable gate, the housing middle part is provided with an electrothermal tube, inner walls is provided with electrothermal film, and a housing inner chamber and an above-mentioned hollow cylindrical bar are suitable, and leave certain interval; The housing outer wall is provided with detachable thermal insulation layer.
The present invention in the characteristics of process aspect is: one, former each separation circuit serialization is carried out, from pulverizing, dry, extrusion molding, and the equal tandem array of electric heating charing, carry out continuously, make each work in-process operation all be in the warm start operating mode, and at the low characteristics of biomass material thermal conductivity, make raw material unlikely loss of heat among the conversion of front and back operation, temperature can not descend, material temperature is among the process that rises that progressively rises and continue all the time, when carrying out charing at last, the inside and outside temperature difference of raw material reaches minimum, for top condition is created in the charing operation.It two is, solved the difficult problem of former extrusion molding well, although biomass material heat-conductive characteristic extreme difference, but this technology material in operations such as pulverizing, drying all heats up gradually, and inside and outside be heated evenly, when entering extrusion machine, temperature of charge has reached 150～160 ℃, at this moment material has been in expansion, softening stress-displacement stage (fluidization), existing wood tar oil is isolated, produce the gummed effect during for extrusion molding, make whole extrusion process can carry out (original equipment is to jump at normal temperatures to carry out extrusion molding to 350 ℃ with temperature) smoothly 200 ℃ of following temperature.Its three, from the theory of the thermal decomposition of wood and experiment, the output of charcoal raises with the reduction of final carbonization temperature, and changes greatlyyer in 270～400 ℃ temperature range, and changes not obvious in 800～700 ℃ of scopes.For pine and birch, when final carbonization temperature was 200 ℃, charcoal reached 90% to the yield (carbonization degree) of absolutely dry wood, and when carbonization temperature was 275 ℃, carbonization degree corresponded to 78% and 71%; When carbonization temperature was 300 ℃, carbonization degree corresponded to 55% and 48%, and when carbonization temperature was 350 ℃, carbonization degree was respectively 43% and 38%, and when carbonization temperature was 550 ℃, carbonization degree was respectively 30% and 27%.The present invention is owing to carry out charing when operation, the material inside and outside temperature rise is very even, so carbonization temperature is controlled in the low scope (270～350 ℃ or 270～300 ℃), in addition, it also is to facilitate one of factor of low-temperature carbonization success that the present invention adopts the charing of short run material), therefore, the present invention reduces carbonization temperature and can effectively improve carbonization degree.Its four, the present invention is with the stick shaped material of extrusion molding, single charing is handled promptly to the independent charing of a small amount of material, thereby carbonization time is as short as 20 minutes.Carbonization time is short, and the pyrolysis side reaction is few, and the loss that side reaction causes is just little, and quality product is higher, and the physical strength of charcoal is higher.In the moulding bar circular hole is arranged, can make calrod insert heating from inside to outside, improve heat utilization efficiency and charing effect.Its five, finished product charcoal shape of the present invention is uniform, the proportion of charcoal is up to 1.2 gram/cm
3, general charcoal proportion is 0.8～0.9 gram/cm only
3, ash content few (being lower than 2%).Its six, the present invention is wide to the adaptation of raw material, the tailing of the shape size processing that all can be used whatsoever.Be particularly useful for utilizing farming, woods waste to make raw material system charcoal, effectively substitute and make charcoal, avoid the destructiveness of timber data and wasteness to use based on the earth kiln of the thick stem that cuts down forest.
Description of drawings
Fig. 1 is a process flow diagram of the present invention;
Fig. 2 is the equipment flowsheet of one embodiment of the invention;
Fig. 3 is the sectional view of electric heating charring furnace shown in Figure 2.
Fig. 1 illustrates, and is that biomass material is at first pulverized with wooden or herbaceous stem vegetable material, is crushed to back operation such as drying process especially air stream drying operation and convenient size and the size of handling of extrusion molding operation.As for air stream drying, raw material granularity is diameter＜3mm, and length＜5mm can be at φ 10 * 20mm to the extrusion molding raw material granularity.Nature for being smalls shape material such as wood chip etc. originally, just needn't pass through pulverizing process.Because the effect of mechanical disintegration, material after the pulverizing, temperature generally can reach 30～40 ℃, needless to say its temperature descends, crushing rear material directly enters drying process and handles, preferably adopt the air stream drying mode, hot gas flow makes below the material fast dewatering to 10%, and making the material outlet temperature rise to 70～80 ℃, dried material is sent in the airtight storage bin of heating, and storage bin is set, the one, the shock absorption of a material, Flow of Goods and Materials and working ability in back extrusion molding operation are complementary, the 2nd, control and the initial temperature when adjusting material and entering extrusion molding are carried out smoothly to guarantee extrusion molding.Temperature is controlled at 80～150 ℃ in the storage bin, preferably 130～150 ℃, in the actual production, material carries out extrusion molding and adds man-hour under the storage bin temperature, material has been in and has expanded and the half fluidization stage of remollescent, the cutting out partial wood tar oil provides natural adhesive during for extrusion molding, finishes the extrusion molding operation smoothly.Generally also can adopt shaped by fluid pressure, the present invention adopts screw extrusion press here, adopt Electric heating to keep temperature of charge during screw extruding briquetting at 150～200 ℃, preferably 180～200 ℃, and the extrusion molding material is the cylindrical shape of hollow, is of a size of internal diameter 3cm, external diameter 8cm, long 80cm does not get rid of other size herein.Those skilled in the art can calculate the weight of the processing materials that is complementary with electric heating charing power at an easy rate.Thereby draw its concrete size.Molding materials after extruding is directly sent into the electric heating charring furnace under the secluding air situation, destructive distillation under 270～350 ℃ of temperature, and carbonization time 30 minutes or still less is preferably in destructive distillation under 270～300 ℃ of temperature, about 20 minutes of carbonization time.Compared with prior art, because the reduction of final carbonization temperature is improved the carbonization degree (output) of charcoal, while biomass material other product of pyrolytic such as tar, the yield of organism, gas etc. decreases.The compressed moulding of the charcoal of this technology is fired and is formed, and density is big, reaches 1.2 gram/cm
3(general charcoal 0.8,0.9 gram/cm
3), calorific value is greater than general charcoal, and calorific value is 6500～7500 kilocalorie/kilograms, greater than general charcoal.
Fig. 2 illustrates, and pulverizer 1 (as branch crushing machine) discharge port connects the opening for feed of pneumatic dryer 2 (adding warm air as thermal medium, if with rare gas element---the gas of oxidizing fire reaction does not take place with material, then better as thermal medium); The pneumatic dryer discharge port connects storage bin 3 opening for feeds through valve 2b, and the storage bin discharge port is connected with screw extrusion press 4 opening for feeds through valve 3b, when the opening for feed valve of storage bin and discharge port valve closes, whole storage bin seals, and is promptly isolated with air; Electric heater 3a is arranged in the storage bin 3, and material in the storage bin is heated; Spiral extrusion machine 4, be used for the material extrusion molding is the cylindrical bar of hollow, electric heater unit 4a, be arranged on screw extrusion press 4 shells, be used for material is fed in raw material, electric gate valve 5 is arranged on the screw extrusion press discharge port, as control discharge port with to electric heating charring furnace 6 one by one gradation feed, (can adopt other control mode) as carrying out work, with the requirement of satisfying one by one, gradation is feeded by electrical equipment control screw extrusion press resting period property.Electric heating charring furnace 6 (referring to Fig. 3) is a cylindrical shell 3a, and housing top is provided with a gas outlet tube 6a.(wood gas can be drawn and be made the dry heat thermal source, or other is used to draw work), housing bottom is provided with a movable gate 5a, the housing middle part is provided with an electrothermal tube 1a, inner walls is provided with electrothermal film 7a, housing inner chamber and above-mentioned hollow cylindrical bar are suitable, and leave certain interval and do the gas passage, and the housing outer wall is provided with detachable thermal insulation layer 4a.During use, the moulding bar 2a that packs among each charring furnace, electrothermal tube 1a inserts in the circular hole at bar center.Electrothermal tube from inside to outside matches with the electrothermal film 7a heating of outside to the bar heating, the bar heating surface is big, be heated evenly, add a small amount of material and carry out destructive distillation, the pyrolysis side reaction is very little, carbonization time was as short as about 20 minutes, so finally reached the technique effect of low-temperature pyrolysis and raising char yield.
Embodiment 1
With the branch is raw material, be crushed to below φ 10 * 20mm, 40 ℃ of pulverizer outlet material temperature, 70 ℃ of dry back temperature of charge, dry back material moisture 10%, 150 ℃ of feed bin drop temperatures, 200 ℃ of extruding outlet temperatures, 350 ℃ of electric heating carbonization temperatures, carbonization time 25 minutes, carbonization degree 41% after tested, and the proportion of finished product charcoal is 1.19 gram/cm
3
Embodiment 2
With the wood chip is raw material, need not pulverize convection drying, 80 ℃ of dry back temperature of charge, water content 8%, 100 ℃ of feed bin drop temperatures, 180 ℃ of extruding outlet temperatures, 300 ℃ of electric heating carbonization temperatures, carbonization time 20 minutes, carbonization degree 49% after tested, and the proportion of finished product charcoal is 1.2 gram/cm
3
Embodiment 3
With the stalk is raw material, is crushed to length below 2mm, 75 ℃ of dry back temperature, and water content 9%, 80 ℃ of feed bin drop temperatures, 190 ℃ of extruding outlet temperatures, 270 ℃ of electric heating carbonization temperatures, carbonization time 20 minutes, carbonization degree 50% after tested.
Embodiment 4
With bagasse is raw material, need not pulverize, and convection drying, 72 ℃ of dry back temperature of charge, water content 9%, 130 ℃ of feed bin drop temperatures, 150 ℃ of extruding outlet temperatures, 280 ℃ of electric heating carbonization temperatures, carbonization time 18 minutes, carbonization degree 41% after tested.
Claims (7)
1, a kind of electrical low-temperature charcoal-producing dry distillation process, carry out according to the following steps in turn:
(A) adopt wooden and the herbaceous stem plant is a raw material, with the size and the size of raw material convenient processing of operation through pulverizer is crushed to after;
(B) raw material of being sent by the pulverizer outlet directly enters moisture eliminator, carries out drying;
(C) material that is come by dryer export is sent in the airtight storage bin of heating, and its temperature of charge is controlled at 80-150 ℃;
(D) material of being sent by storage bin directly enters extrusion machine under the situation of secluding air, heats simultaneously and extrusion molding, and the final material temperature is controlled at 150～200 ℃ during extrusion operation;
(E) molding materials that is come by extruder outlet is directly sent under the situation of secluding air in the electric heating charring furnace, destructive distillation under 270～350 ℃ of temperature, 30 minutes time of electric heating charing or still less;
(F) under the situation of secluding air to destructive distillation after material be cooled to normal temperature, make the finished product charcoal at last.
Each step of above-mentioned A to F is carried out in turn continuously, so that each work in-process step B-E field is in the warm start operating mode.
2, electrical low-temperature charcoal-producing dry distillation process according to claim 1 is characterized in that, described moisture eliminator is a pneumatic dryer, and raw material is heated by hot gas flow therein and be dry; Described extrusion machine is a screw extrusion press; Adopt Electric heating to keep temperature of charge during screw extruding briquetting.
3, charcoal new process of production according to claim 2 is characterized in that, described extrusion molding material is the cylindrical shape of hollow, is of a size of internal diameter 3cm, external diameter 8cm, long 80cm.
4, according to claim 1 or 2 or 3 described charcoal new process of production, it is characterized in that, temperature of charge is controlled at 130～150 ℃ in the described storage bin, and described extrusion operation final material temperature is controlled at 180～200 ℃, about 20 minutes of described electric heating carbonization time.
5, charcoal new process of production according to claim 4 is characterized in that, the temperature of described pulverizer outlet material is 30～40 ℃, and described dry back material outlet temperature is 70～80 ℃.
6, a kind of device that is used to realize the novel process of claim 1, this device comprises:
A pulverizer (1) is used for above-mentioned raw materials is crushed to convenient size and the size of handling of back operation;
A pneumatic dryer (3), its opening for feed is connected with the pulverizer discharge port;
An airtight storage bin, the discharge port of pneumatic dryer is connected with the storage bin opening for feed through a valve;
An electric heater is arranged in the storage bin, is used for the storage bin material is heated;
A screw extrusion press (4), being used for material forming is the hollow cylindrical bar, its opening for feed is communicated with through a valve with the storage bin discharge port;
An electric heater unit is arranged on the screw extrusion press shell, is used for material is heated;
The a plurality of electric heating charring furnaces that are used for the bar that splendid attire screw extrusion press discharge port sends, this charring furnace is a cylindrical shell (3a), housing top is provided with a gas outlet tube (6a), housing bottom is provided with a movable gate (5a), the housing middle part is provided with an electrothermal tube (1a), inner walls is provided with electrothermal film (7a), and a housing inner chamber and an above-mentioned hollow cylindrical bar are suitable, and leave certain interval; The housing outer wall is provided with detachable thermal insulation layer (4a).
7, device according to claim 6 is characterized in that, described screw extrusion press discharge port is provided with an electric gate valve, feeds one by one as the control discharging with to the electric heating charring furnace.
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| Application Number | Priority Date | Filing Date | Title |
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| CN021133123A CN1216129C (en) | 2002-02-04 | 2002-02-04 | Electrical low-temperature charcoal-producing dry distillation process and apparatus |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN021133123A CN1216129C (en) | 2002-02-04 | 2002-02-04 | Electrical low-temperature charcoal-producing dry distillation process and apparatus |
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| CN1436833A true CN1436833A (en) | 2003-08-20 |
| CN1216129C CN1216129C (en) | 2005-08-24 |
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Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101920975A (en) * | 2010-02-10 | 2010-12-22 | 上海元宝能源技术有限公司 | Method for reducing comprehensive energy consumption of coal synthesis ammonia |
| CN102533292A (en) * | 2011-12-15 | 2012-07-04 | 江苏省农业科学院 | Method of preparing biomass charcoal with biomass material and carbonization furnace |
| CN101730733B (en) * | 2007-04-27 | 2013-10-16 | 学校法人近畿大学 | Biocoke producing apparatus, method of controlling the same and process for production thereof |
| CN107903917A (en) * | 2017-12-15 | 2018-04-13 | 广州中天联合高新技术发展有限公司 | A kind of effective integrated retort of vacuum |
| CN110330989A (en) * | 2019-07-25 | 2019-10-15 | 扬州三源机械有限公司 | A kind of efficient pyrocrack furnace body structure of domestic rubbish disposal |
| CN110745805A (en) * | 2018-07-24 | 2020-02-04 | 张森 | Method for preparing hemp stalk carbon powder |
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2002
- 2002-02-04 CN CN021133123A patent/CN1216129C/en not_active Expired - Fee Related
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101730733B (en) * | 2007-04-27 | 2013-10-16 | 学校法人近畿大学 | Biocoke producing apparatus, method of controlling the same and process for production thereof |
| CN101920975A (en) * | 2010-02-10 | 2010-12-22 | 上海元宝能源技术有限公司 | Method for reducing comprehensive energy consumption of coal synthesis ammonia |
| CN102533292A (en) * | 2011-12-15 | 2012-07-04 | 江苏省农业科学院 | Method of preparing biomass charcoal with biomass material and carbonization furnace |
| CN107903917A (en) * | 2017-12-15 | 2018-04-13 | 广州中天联合高新技术发展有限公司 | A kind of effective integrated retort of vacuum |
| CN107903917B (en) * | 2017-12-15 | 2024-01-05 | 广州中天联合高新技术发展有限公司 | Vacuum efficient integrated carbonization furnace |
| CN110745805A (en) * | 2018-07-24 | 2020-02-04 | 张森 | Method for preparing hemp stalk carbon powder |
| CN110330989A (en) * | 2019-07-25 | 2019-10-15 | 扬州三源机械有限公司 | A kind of efficient pyrocrack furnace body structure of domestic rubbish disposal |
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| Publication number | Publication date |
|---|---|
| CN1216129C (en) | 2005-08-24 |
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