CN204644267U - The drying of a kind of internal combustion type biological particles material, charing, activation integral stove - Google Patents
The drying of a kind of internal combustion type biological particles material, charing, activation integral stove Download PDFInfo
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- CN204644267U CN204644267U CN201520269231.2U CN201520269231U CN204644267U CN 204644267 U CN204644267 U CN 204644267U CN 201520269231 U CN201520269231 U CN 201520269231U CN 204644267 U CN204644267 U CN 204644267U
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Abstract
The utility model discloses a kind of internal combustion type biological particles material dry, charing, activation integral stove, comprise vertical body of heater, described body of heater is provided with dryer section from the top down successively, material envelope section, charing section, activation section, steam generation section and cooling section, the sidewall of described dryer section is provided with the wet flue gas outlet pipe being communicated with its inner chamber, upper tube box is provided with in charing section, internal combustion chamber is provided with in activation section, described internal combustion chamber top is communicated with lower tube box, described lower tube box is communicated with by heat exchanging pipe with between upper tube box, described upper tube box is by being communicated with wet flue gas outlet pipe through the rising smoke pipe of material envelope section, described internal combustion chamber is communicated with the sleeve extended to outside body of heater, the external port of described sleeve is provided with the burner being communicated with combustion air inlet house steward and gas pipe, be provided with the water cooling chamber of bottom for water spray orifice plate in described steam generation section, described cooling section outer wall is provided with spiral coil cooling tube, and described water cooling chamber is communicated with spiral coil cooling tube by water-cooled endless tube.
Description
Technical field
The utility model relates to carbonaceous material carbide furnace field, is specifically related to the drying of a kind of internal combustion type biological particles material, charing, activation integral stove.
Background technology
Biomass (biomass) refer to any organism utilizing sun power to synthesize through photosynthesis, comprise during farming, forestry, animal husbandry, sideline production and fishery are produced the stalk and biomass byproduct and industrial wood waste that produce, also comprise the mud of city domestic sewage treatment plant, aquaculture fowl and animal excrement, changing food waste the like waste.The main component of these abandoned biomass is carbohydrate, and principal element consists of the trace element such as the bioelements such as C, H, O, N, P, K and a small amount of S, Ca, Si, Fe, is a kind of reproducible resource.According to incomplete estimation, the whole world produces this type of biomass waste year and reaches billions of ton, and adopt is burned or landfill stabilization more, and utilization ratio is very low; The only straw biomass of China, year generation reach more than 800,000,000 ton, utilization ratio, less than 50%, is directly burned in field greatly, is not only wasted resource, again serious environment pollution.
In recent years, thermo-cracking is adopted to be mainly study flourish at home and abroad containing the application of stationary state biomass charcoal by Wood Adhesives from Biomass, a large amount of fundamental researchs proves: biomass charcoal is loose porous, there is huge surface-area and cation exchange capacity, can soil physico-chemical property be improved, and moisturizing and ventilation property, make crop yield, and the pollutent that can adsorb in soil, reduce its biological effectiveness and Transport And Transformation ability; The bio-toxicity that the alkalescence of biomass charcoal reduces pollutant in soil for improvement acid soil has very large potential; Biomass charcoal can also provide the place of growth and breeding for microorganism, is conducive to the degraded to pollutent, but can protect again by the degraded from microorganism of the organism that adsorbs simultaneously, different on different microorganisms impact; Biomass charcoal is also useful to soil useful animals such as earthworms; In addition, biomass charcoal also can make chemical fertilizer have slow releasing function, improves fertilising efficiency.
The carbon remittance effect in biomass charcoal also field is expected to include CDM carbon transaction in, by biomass charcoal also field 1hm
2compensate 5 dollars of meters, 100,000,000 hm
2compensation volume will reach more than 500,000,000 dollars, this for China's agricultural development and increasing peasant income favourable, therefore, develop straw-carbonized also field, can at carbon fixation and emission reduction, increasing soil fertility to improve in per unit area yield and increasing peasant income receive opportunity.
American-European and Japan wait developed country for biomass carbonization research carry out less, biomass pyrolytic carbonization and equipment research thereof mainly concentrate on the developing country such as Brazil in India in Asia, Philippines, Thailand, South America.China improves some traditional carbonization techniques and carbonizing apparatus from 20 century 70s.
Applicant is disclose a kind of vertical low-temperature pyrolysis stove in the Chinese utility model patent of " ZL201220003775.0 " in the patent No., destructive distillation also claims carbonization, adopt air guide wing and gas skirt the combustion gas produced in biomass through pyrolysis process to be drawn burner hearth and carry out recovery storage, then the combustion chamber be arranged on outside gas retort is sent into, its shortcoming comprises: one, storage process is reclaimed in combustion gas needs corresponding equipment, increase fund input, and storage facilities is reclaimed in combustion gas and combustion chamber will take very large space; Two, combustion gas recovery storage will cool, and a large amount of heat energy wastes, and the process of the heat energy feeding gas retort of combustion chamber generation also exists certain heat-energy losses; What three, activator adopted is outer for steam, and cost is high.
Summary of the invention
The technical problems to be solved in the utility model is to provide the drying of a kind of internal combustion type biological particles material, charing, activation integral stove, the combustion chamber that can solve existing gas retort is arranged on outside body of heater, causes taking up room greatly, heat-energy losses is many and need the outer problem for steam.
The utility model is achieved through the following technical solutions:
A kind of internal combustion type biological particles material is dry, charing, activation integral stove, comprise vertical body of heater, described body of heater top is provided with hopper loader, bottom is provided with unloading machine, described body of heater is provided with dryer section from the top down successively, material envelope section, charing section, activation section, steam generation section and cooling section, the sidewall of described dryer section is provided with the wet flue gas outlet pipe being communicated with its inner chamber, upper tube box is provided with in charing section, internal combustion chamber is provided with in activation section, described internal combustion chamber top is communicated with lower tube box, described lower tube box is communicated with by heat exchanging pipe with between upper tube box, described upper tube box is by being communicated with wet flue gas outlet pipe through the rising smoke pipe of material envelope section, described internal combustion chamber is communicated with the sleeve extended to outside body of heater, the external port of described sleeve is provided with the burner being communicated with combustion air inlet house steward and gas pipe, be provided with the water cooling chamber of bottom for water spray orifice plate in described steam generation section, described cooling section outer wall is provided with spiral coil cooling tube, and described water cooling chamber is communicated with spiral coil cooling tube by water-cooled endless tube.
Further scheme of the present utility model is, the wall of described charing section is provided with the top pyrolysis gas being communicated with its inner chamber and derives house steward and bottom pyrolysis gas derivation house steward.
Further scheme of the present utility model is, the wall of described charing section and activation section is provided with the inspection window of multiple communication with cavity.
Further scheme of the present utility model is that described internal combustion chamber is connected by sand sealing groove with between lower tube box.
Further scheme of the present utility model is, described rising smoke pipe upper port extends to dryer section bottom, and is provided with venting bell at this port, and described wet flue gas outlet pipe internal port is positioned at dryer section top, and is provided with gas collection bell at this port.
Further scheme of the present utility model is, is also communicated with the inlet of cold air pipe extended to outside body of heater in described rising smoke pipe.
Further scheme of the present utility model is, the top of described water cooling chamber is connected to the bottom of internal combustion chamber.
Further scheme of the present utility model is, described internal combustion chamber is also connected with and extends to viewing window outside body of heater and temperature survey mouth.
The utility model advantage is compared with prior art:
The water vapor produced when one, extinguishing pyrocarbon with cooling section, as activator, does not need outer for steam, easy, energy-conservation, effectively reduces the low cost of manufacture of target product;
Two, adopt sand sealing groove that internal combustion chamber and lower tube box can vertically be floated, eliminate the thermal stresses that heat exchange core produces due to thermal expansion, both increased the service life, be convenient to again dismounting and repair;
Three, internal combustion chamber is set in burner hearth, improves compactedness, reduce thermosteresis;
Four, adopt the outer heat of heat exchanging pipe, decrease pyrolysis tolerance, improve the calorific value of self-produced combustion gas, reduce the load of cooling recovery system, reduce investment, energy efficient.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model.
Fig. 2 is that the A of Fig. 1 is to sectional view.
Embodiment
A kind of internal combustion type biological particles material is as depicted in figs. 1 and 2 dry, charing, activation integral stove, comprise vertical body of heater, described body of heater top is provided with hopper loader 1, bottom is provided with unloading machine 27, described body of heater is provided with dryer section from the top down successively, material envelope section, charing section, activation section, steam generation section and cooling section, the sidewall of described dryer section is provided with the wet flue gas outlet pipe 3 being communicated with its inner chamber, upper tube box 6 is provided with in charing section, the wall of described charing section is provided with the top pyrolysis gas being communicated with its inner chamber and derives house steward 8 and bottom pyrolysis gas derivation house steward 12, the wall of described charing section and activation section is provided with the inspection window 11 of multiple communication with cavity, internal combustion chamber 15 is provided with in activation section, described internal combustion chamber 15 top is communicated with lower tube box 13 by sand sealing groove 14, described lower tube box 13 is communicated with by heat exchanging pipe 10 with between upper tube box 6, the cross section of described heat exchanging pipe 10 is preferably oblate, described upper tube box 6 communicates through the rising smoke pipe 5 of material envelope section, described rising smoke pipe 5 upper port extends to dryer section bottom, and at this port, venting bell 28 is installed, described wet flue gas outlet pipe 3 internal port is positioned at dryer section top, and at this port, gas collection bell 2 is installed, the inlet of cold air pipe 4 extended to outside body of heater is also communicated with in described rising smoke pipe 5, described internal combustion chamber 15 is communicated with the sleeve 21 extended to outside body of heater, the external port of described sleeve 21 is provided with the burner 20 being communicated with combustion air inlet house steward 16 and gas pipe 18, described internal combustion chamber 15 is also connected with two and extends to viewing window outside body of heater and temperature survey mouth 28, measure the flame temperature of corresponding two burners 20 respectively, in order to regulate coefficient of excess air, being provided with bottom in described steam generation section for water spray orifice plate 26, top is connected to water cooling chamber 22 bottom internal combustion chamber 15, and described cooling section outer wall is provided with spiral coil cooling tube 24, and described water cooling chamber 22 is communicated with spiral coil cooling tube 24 by water-cooled endless tube 23.
Upper tube box 6 and wet flue gas outlet pipe 3 material preferably 304 stainless steels, lower tube box 13, sand sealing groove 14, internal combustion chamber 15 and heat exchanging pipe 10 are when target product is gac, the preferred 310s stainless steel of material, when target product is biomass charcoal, material is 304 stainless steels preferably.
Biological particles material (diameter 8-15mm, long 10-15mm, water content 15%-25%) is promoted through loading machine 1 shove charge by lift, described loading machine 1 is rotary type air locking machine preferably, through gas collection bell 2 cloth, by deadweight, from top to bottom drying section, material seal section, charing section, activation section, steam generation section, cooling section successively, after there is series of physical-chemical transformation, by the outer row of the unloading machine 27 of bottom, the preferred rotary type air locking machine of described unloading machine.
Wherein, the effect of dryer section is that moisture biological particles material is removed moisture, in dryer section, biological particles material is by gas mixture (the temperature <200 DEG C) direct heating risen from venting bell 28, described gas mixture forms by after the high-temperature flue gas of heat exchanging pipe 10 and the freezing air temperature adjustment to be sent into by inlet of cold air pipe 4, after carrying out heat, mass transter with biological particles material, through gas collection bell 2, the outer row of wet flue gas outlet pipe 3.
The effect of material envelope section prevents from the pyrolysis gas of charing section generation is gone here and there dryer section.
Charing section is main technique section, its effect makes biological particles material carry out pyrolysis, in this section, biological particles material is heated by the high-temperature flue gas in heat exchanging pipe 10, temperature constantly raises until carbonize final temperature about 500 DEG C, generate biomass charcoal, bio oil, wood vinegar and combustion gas, wherein bio oil, wood vinegar and combustion gas pyrolysis product derive house steward by pyrolysis gas derives, when thinking that voluminous bio-oil produces combustion gas less, self-produced combustion gas can be derived house steward 8 from top pyrolysis gas and being sent to condensate recovery system; When thinking the combustion gas of few product bio-oil fecund, self-produced combustion gas can be derived house steward 12 from bottom pyrolysis gas and being sent to condensate recovery system.
When target product is gac, keep activation section temperature to be 800 DEG C-850 DEG C, activator is that the water vapor extinguishing pyrocarbon generation in stove carries out physically activated, and water vapor consumption is 0.3-0.6 times of charcoal weight; When target product is biomass charcoal, only activation section temperature need be reduced.
Burning coal gas and combustion air produce high-temperature flue gas through burner 20, sleeve 21 in internal combustion chamber 15, and needed for dry, charing, reactivation process, high-temperature flue gas enters into heat exchanging pipe 10 through lower tube box 13, by partition, heat is passed to biological particles material.
Stove biomass will be entered and make particulate material, and the process intensity of stove can be significantly improved, be conducive to cloth, gas distribution, improve the homogeneity of process, reduce furnace gas resistance, reduce dust; Adopt internal combustion type, make compact construction, in stove, the thermograde of vertical direction is reasonable.
Claims (8)
1. an internal combustion type biological particles material is dry, charing, activation integral stove, comprise vertical body of heater, described body of heater top is provided with hopper loader (1), bottom is provided with unloading machine (27), it is characterized in that: described body of heater is provided with dryer section from the top down successively, material envelope section, charing section, activation section, steam generation section and cooling section, the sidewall of described dryer section is provided with the wet flue gas outlet pipe (3) being communicated with its inner chamber, upper tube box (6) is provided with in charing section, internal combustion chamber (15) is provided with in activation section, described internal combustion chamber (15) top is communicated with lower tube box (13), be communicated with by heat exchanging pipe (10) between described lower tube box (13) with upper tube box (6), described upper tube box (6) is by being communicated with wet flue gas outlet pipe (3) through the rising smoke pipe (5) of material envelope section, described internal combustion chamber (15) is communicated with the sleeve extended to outside body of heater (21), the external port of described sleeve (21) is provided with the burner (20) being communicated with combustion air inlet house steward (16) and gas pipe (18), be provided with the water cooling chamber (22) of bottom for water spray orifice plate (26) in described steam generation section, described cooling section outer wall is provided with spiral coil cooling tube (24), and described water cooling chamber (22) are communicated with spiral coil cooling tube (24) by water-cooled endless tube (23).
2. a kind of internal combustion type biological particles material drying as claimed in claim 1, charing, activation integral stove, is characterized in that: the wall of described charing section is provided with the top pyrolysis gas being communicated with its inner chamber and derives house steward (8) and bottom pyrolysis gas derivation house steward (12).
3. a kind of internal combustion type biological particles material drying as claimed in claim 1, charing, activation integral stove, is characterized in that: the wall of described charing section and activation section is provided with the inspection window (11) of multiple communication with cavity.
4. a kind of internal combustion type biological particles material drying as claimed in claim 1, charing, activation integral stove, be is characterized in that: be connected by sand sealing groove (14) between described internal combustion chamber (15) with lower tube box (13).
5. a kind of internal combustion type biological particles material drying as claimed in claim 1, charing, activation integral stove, it is characterized in that: described rising smoke pipe (5) upper port extends to dryer section bottom, and at this port, venting bell (28) is installed, described wet flue gas outlet pipe (3) internal port is positioned at dryer section top, and is provided with gas collection bell (2) at this port.
6. a kind of internal combustion type biological particles material drying as described in claim 1 or 5, charing, activation integral stove, is characterized in that: be also communicated with the inlet of cold air pipe (4) extended to outside body of heater in described rising smoke pipe (5).
7. a kind of internal combustion type biological particles material drying as claimed in claim 1, charing, activation integral stove, is characterized in that: the top of described water cooling chamber (22) is connected to the bottom of internal combustion chamber (15).
8. dry, the charing of a kind of internal combustion type biological particles material as claimed in claim 1, activation integral stove, is characterized in that: described internal combustion chamber (15) is also connected with and extends to viewing window outside body of heater and temperature survey mouth (28).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520269231.2U CN204644267U (en) | 2015-04-30 | 2015-04-30 | The drying of a kind of internal combustion type biological particles material, charing, activation integral stove |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520269231.2U CN204644267U (en) | 2015-04-30 | 2015-04-30 | The drying of a kind of internal combustion type biological particles material, charing, activation integral stove |
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| CN204644267U true CN204644267U (en) | 2015-09-16 |
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| CN201520269231.2U Withdrawn - After Issue CN204644267U (en) | 2015-04-30 | 2015-04-30 | The drying of a kind of internal combustion type biological particles material, charing, activation integral stove |
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Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104789236A (en) * | 2015-04-30 | 2015-07-22 | 吴植仁 | Internal-combustion type biomass particle material drying, carbonizing and activating integrated furnace |
| CN105905894A (en) * | 2016-01-28 | 2016-08-31 | 赵英杰 | Carbonization and activation device for active coke production |
| CN105923618A (en) * | 2015-11-27 | 2016-09-07 | 姜良政 | Carbonization or activation equipment for organic matter with high water content and carbonization or activation process |
| CN108203093A (en) * | 2015-11-27 | 2018-06-26 | 湖南鼎玖能源环境科技有限公司 | Charing and activation equipment and charing and activating process |
| CN110079337A (en) * | 2019-04-29 | 2019-08-02 | 河南科技大学 | A kind of retort of pyrolysis gas of biomass recycling and biomass carbonated method |
-
2015
- 2015-04-30 CN CN201520269231.2U patent/CN204644267U/en not_active Withdrawn - After Issue
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104789236A (en) * | 2015-04-30 | 2015-07-22 | 吴植仁 | Internal-combustion type biomass particle material drying, carbonizing and activating integrated furnace |
| CN105923618A (en) * | 2015-11-27 | 2016-09-07 | 姜良政 | Carbonization or activation equipment for organic matter with high water content and carbonization or activation process |
| CN105923618B (en) * | 2015-11-27 | 2017-05-10 | 湖南鼎玖能源环境科技有限公司 | Carbonization or activation equipment for organic matter with high water content and carbonization or activation process |
| CN108203093A (en) * | 2015-11-27 | 2018-06-26 | 湖南鼎玖能源环境科技有限公司 | Charing and activation equipment and charing and activating process |
| CN108203093B (en) * | 2015-11-27 | 2021-07-20 | 湖南鼎玖能源环境科技股份有限公司 | Carbonization and activation equipment and carbonization and activation process |
| CN105905894A (en) * | 2016-01-28 | 2016-08-31 | 赵英杰 | Carbonization and activation device for active coke production |
| CN110079337A (en) * | 2019-04-29 | 2019-08-02 | 河南科技大学 | A kind of retort of pyrolysis gas of biomass recycling and biomass carbonated method |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| AV01 | Patent right actively abandoned | ||
| AV01 | Patent right actively abandoned |
Granted publication date: 20150916 Effective date of abandoning: 20170412 |