CN205347319U - Split type carbomorphism bank of ovens - Google Patents
Split type carbomorphism bank of ovens Download PDFInfo
- Publication number
- CN205347319U CN205347319U CN201620113114.1U CN201620113114U CN205347319U CN 205347319 U CN205347319 U CN 205347319U CN 201620113114 U CN201620113114 U CN 201620113114U CN 205347319 U CN205347319 U CN 205347319U
- Authority
- CN
- China
- Prior art keywords
- retort
- combustion furnace
- main pipe
- hot
- steam main
- 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
- 238000002485 combustion reaction Methods 0.000 claims abstract description 31
- 238000003763 carbonization Methods 0.000 claims abstract description 17
- 239000002184 metal Substances 0.000 claims description 8
- 239000000779 smoke Substances 0.000 claims description 6
- 239000011148 porous material Substances 0.000 claims description 5
- 238000009413 insulation Methods 0.000 claims description 4
- 230000008878 coupling Effects 0.000 claims description 3
- 238000010168 coupling process Methods 0.000 claims description 3
- 238000005859 coupling reaction Methods 0.000 claims description 3
- 239000007789 gas Substances 0.000 abstract description 11
- 239000002028 Biomass Substances 0.000 abstract description 7
- 238000000034 method Methods 0.000 abstract description 7
- 238000004519 manufacturing process Methods 0.000 abstract description 6
- 239000000446 fuel Substances 0.000 abstract description 4
- 239000010902 straw Substances 0.000 abstract description 4
- 238000005516 engineering process Methods 0.000 abstract description 3
- 238000003912 environmental pollution Methods 0.000 abstract description 2
- 238000010438 heat treatment Methods 0.000 abstract description 2
- 238000010304 firing Methods 0.000 abstract 2
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 abstract 1
- 230000015572 biosynthetic process Effects 0.000 abstract 1
- 238000010924 continuous production Methods 0.000 abstract 1
- 239000003546 flue gas Substances 0.000 abstract 1
- 238000000197 pyrolysis Methods 0.000 abstract 1
- 239000000126 substance Substances 0.000 abstract 1
- 239000003610 charcoal Substances 0.000 description 6
- 239000000463 material Substances 0.000 description 5
- 239000002023 wood Substances 0.000 description 4
- 206010021143 Hypoxia Diseases 0.000 description 2
- 239000006227 byproduct Substances 0.000 description 2
- 238000010276 construction Methods 0.000 description 2
- -1 timber Substances 0.000 description 2
- 235000021419 vinegar Nutrition 0.000 description 2
- 239000000052 vinegar Substances 0.000 description 2
- 239000011276 wood tar Substances 0.000 description 2
- 206010002660 Anoxia Diseases 0.000 description 1
- 241000976983 Anoxia Species 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 229910003481 amorphous carbon Inorganic materials 0.000 description 1
- 230000007953 anoxia Effects 0.000 description 1
- 239000011449 brick Substances 0.000 description 1
- 239000003638 chemical reducing agent Substances 0.000 description 1
- 238000006731 degradation reaction Methods 0.000 description 1
- 238000004821 distillation Methods 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 230000001146 hypoxic effect Effects 0.000 description 1
- 238000005272 metallurgy Methods 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 239000002689 soil Substances 0.000 description 1
- 239000011269 tar Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/10—Biofuels, e.g. bio-diesel
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/10—Process efficiency
- Y02P20/129—Energy recovery, e.g. by cogeneration, H2recovery or pressure recovery turbines
Landscapes
- Solid-Fuel Combustion (AREA)
Abstract
The utility model discloses a split type carbomorphism bank of ovens, it is constituteed by firing burning furnace, steam pump and retort, fires burning furnace, steam pump and retort and connects gradually through the pipeline, and it is the detached to fire burning furnace and retort, and the retort is the three or three above parallelly connected technology that inserts. The utility model discloses a dry distillation technology is placed biomass feedstock such as timber, shell, straw in inclosed retort, adds fuel in firing burning furnace, and the burning heat formation is gaseous, send the hot gas into the retort through the steam pump in, to the living beings heating and then realize the anaerobic carbomorphism, the flammable accessory substance that generates among the carbonization process gets into the combustion chamber burning through the pipeline again, the gaseous chimney that gets into after the burning passes through to discharge in the air after flue gas filter handles, has avoided environmental pollution. The utility model discloses to fire burning furnace and the retort parts to with the parallelly connected access of a plurality of retorts, can make every retort manipulate alone, do not influence other operations, realized half continuous production of retort, reduced working strength, improved equipment production efficiency.
Description
Technical field
It is bench of burners that this utility model relates to a kind of split type carbonization, belongs to carbonization device technical field.
Background technology
The biomass materials such as timber, shell, straw are under anoxia or hypoxic condition, and degradation reaction can occur in heating, generate Linesless charcoal, and by-product includes: wood tar, wood vinegar and wood gas etc..Linesless charcoal is to maintain in the original structure of timber and hole the impure amorphous carbon of residual tar, is widely used as industry metallurgy reducing agent and fuel, also plays significant role in fields such as purification of water quality, pollutant absorption.
At present, Linesless charcoal produces the overwhelming majority and adopts local method burning process, by a part of raw material that burns in soil system or brick kiln, makes to reach in kiln carbonization temperature, then cold stoking.Thus there is a lot of problem, as big in fuel consumption, the thermal efficiency is low, the production cycle is long, unstable product quality, it is often more important that the wood gas of generation, wood tar and wood vinegar etc. do not process, and directly discharge, environment causes very big pollution.Also having and use retort to produce Linesless charcoal, be typically all retort and combustion furnace one, operation during interval, the operating time is longer, and production efficiency is relatively low, and each combustion furnace is required for special messenger's operation, lost labor.
Summary of the invention
This utility model is solve existing problem in the art, it is provided that a kind of split type carbonization is bench of burners.
Problem described in the utility model is solved by techniques below scheme: a kind of split type carbonization is bench of burners, it is made up of combustion furnace, hot-air pump and retort, described combustion furnace, hot-air pump and retort are sequentially connected with by pipeline, described combustion furnace and retort separate, described retort is three or more than three, and described retort is linked into the mode in integrated artistic for coupling access parallel.
Above-mentioned split type carbonization is bench of burners, and described combustion furnace is externally provided with heat-insulation layer, and described combustion furnace is provided with chimney, and described chimney top is provided with smoke filter.
Above-mentioned split type carbonization is bench of burners, bottom steam main pipe it is provided with bottom described retort, described bottom steam main pipe tiles along retort basal diameter direction, described bottom steam main pipe is provided with two or more perforated metal tubes, described perforated metal tube is vertical on the direction parallel with retort bottom surface with bottom steam main pipe to be connected, described bottom steam main pipe is connected with combustion furnace by pipeline, described bottom steam main pipe is arranged over belt hole support frame plate, described retort is provided with central hot airway, the upper end of described central hot airway is connected with retort top center, the lower end of described central hot airway is connected with bottom steam main pipe in the position of retort bottom centre, described central hot airway is provided with pore, described retort is provided with feeding gate, described retort upper end is provided with passage, pipeline between described retort and combustion furnace is provided with return-air valve, pipeline between described retort and hot-air pump is provided with hot-blast valve.
This utility model adopts distillation process, the biomass materials such as timber, shell, straw are placed in airtight retort, fuel is added in combustion furnace, burning generates hot gas, sending in retort by hot-air pump by hot gas, biomass are heated and then realizes anaerobic carbonization, the combustible byproducts generated in carbonization process enters combustion chamber burning further through pipeline, gas after burning enters and is discharged in the air after chimney processes by smoke filter, it is to avoid environmental pollution.Combustion furnace and retort are separated by this utility model, and multiple retort parallel connections are accessed, and each retort can be made individually operated to use, do not affect other operation, achieve the semi-successive cultivation of retort, decrease working strength, improve production efficiency of equipment.
This utility model simple in construction, each parts combine linking closely, easy to operate, safety and stability, and efficiency is high, and production process is totally-enclosed, will not produce to pollute to environment.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model.
Fig. 2 is the structural representation of bottom steam main pipe.
In figure, each part numbers is: 1-combustion furnace；2-hot-air pump；3-retort；4-heat-insulation layer；5-chimney；6 smoke filters；7-hot-blast valve；8-return-air valve；9-central hot airway；10-pore；11-belt hole support frame plate；12-feeding gate；Steam main pipe bottom 13-；14-perforated metal tube；15-passage.
Detailed description of the invention
With reference to the accompanying drawings this utility model detailed description of the invention is described in detail.
Referring to Fig. 1, Fig. 2, a kind of split type carbonization is bench of burners, it is made up of combustion furnace 1, hot-air pump 2 and retort 3, described combustion furnace 1, hot-air pump 2 and retort 3 are sequentially connected with by pipeline, described combustion furnace 1 and retort 3 separate, described retort 3 is three or more than three, and described retort 3 is linked into the mode in integrated artistic for coupling access parallel.Described combustion furnace 1 is externally provided with heat-insulation layer 4, and described combustion furnace 1 is provided with chimney 5, and described chimney 5 top is provided with smoke filter 6.Bottom steam main pipe 13 it is provided with bottom described retort 3, described bottom steam main pipe 13 tiles along retort 3 basal diameter direction, described bottom steam main pipe 13 is provided with two or more perforated metal tubes 14, described perforated metal tube 14 is vertical on the direction parallel with retort 3 bottom surface with bottom steam main pipe 13 to be connected, described bottom steam main pipe 13 is connected with combustion furnace 1 by pipeline, described bottom steam main pipe 13 is arranged over belt hole support frame plate 11, described retort 3 is provided with central hot airway 9, the upper end of described central hot airway 9 is connected with retort 3 top center, the lower end of described central hot airway 9 is connected with bottom steam main pipe 13 in the position of retort 3 bottom centre, described central hot airway 9 is provided with pore 10, described retort 3 is provided with feeding gate 12, described retort 3 upper end is provided with passage 15, pipeline between described retort 3 and combustion furnace 1 is provided with return-air valve 8, pipeline between described retort 3 and hot-air pump 2 is provided with hot-blast valve 7.
This utility model is so work: first open feeding gate 12, by timber, shell, the biomass materials such as straw are placed in retort 3, close feeding gate 12 and passage 15, open hot-blast valve 7 and return-air valve 8, light combustion furnace 1, open hot-air pump 2, in combustion furnace 1, the temperature of gas quickly raises, hot gas is pumped to bottom steam main pipe 13 by hot-air pump 2, part steam flows out from perforated metal tube 14 and biomass material is started from bottom-heated, part steam starts to heat from the center of retort 3 by the pore 10 on central hot airway 9, the slow carbonization of biomass material generates Linesless charcoal, and generate many combustible gases, imflammable gas enters combustion furnace 1 by pipeline and burns, gas after burning enters chimney 5, it is discharged into aerial after being processed by smoke filter 6.After carbonization terminates, close hot-blast valve 7 and return-air valve 8, open feeding gate 12 and passage 15, begin to cool down, when being cooled to below 35 DEG C, charcoal can be gone out.After hot-blast valve 7 and return-air valve 8 closedown, the retort of other parallel connection still can continue operation.
This utility model simple in construction, each parts combine linking closely, easy to operate, safety and stability, and efficiency is high, and production process is totally-enclosed, will not produce to pollute to environment.
Claims (3)
1. a split type carbonization is bench of burners, it is characterized in that: it is made up of combustion furnace (1), hot-air pump (2) and retort (3), described combustion furnace (1), hot-air pump (2) and retort (3) are sequentially connected with by pipeline, described combustion furnace (1) and retort (3) separate, described retort (3) is three or more than three, and described retort (3) is linked into the mode in integrated artistic for coupling access parallel.
2. split type carbonization is bench of burners according to claim 1, it is characterised in that: described combustion furnace (1) is externally provided with heat-insulation layer (4), and described combustion furnace (1) is provided with chimney (5), and described chimney (5) top is provided with smoke filter (6).
3. split type carbonization is bench of burners according to claim 1, it is characterized in that: described retort (3) bottom is provided with bottom steam main pipe (13), described bottom steam main pipe (13) is tiled along retort (3) basal diameter direction, described bottom steam main pipe (13) is provided with two or more perforated metal tubes (14), described perforated metal tube (14) is vertical on the direction parallel with retort (3) bottom surface with bottom steam main pipe (13) to be connected, described bottom steam main pipe (13) is connected with combustion furnace (1) by pipeline, described bottom steam main pipe (13) is arranged over belt hole support frame plate (11), described retort (3) is provided with central hot airway (9), the upper end of described central hot airway (9) is connected with retort (3) top center, the lower end of described central hot airway (9) is connected with bottom steam main pipe (13) in the position of retort (3) bottom centre, described central hot airway (9) is provided with pore (10), described retort (3) is provided with feeding gate (12), described retort (3) upper end is provided with passage (15), pipeline between described retort (3) and combustion furnace (1) is provided with return-air valve (8), pipeline between described retort (3) and hot-air pump (2) is provided with hot-blast valve (7).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620113114.1U CN205347319U (en) | 2016-02-04 | 2016-02-04 | Split type carbomorphism bank of ovens |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620113114.1U CN205347319U (en) | 2016-02-04 | 2016-02-04 | Split type carbomorphism bank of ovens |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205347319U true CN205347319U (en) | 2016-06-29 |
Family
ID=56183105
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620113114.1U Expired - Fee Related CN205347319U (en) | 2016-02-04 | 2016-02-04 | Split type carbomorphism bank of ovens |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205347319U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105524629A (en) * | 2016-02-04 | 2016-04-27 | 辛集市远翔环保能源科技有限公司 | Split type carbonization furnace set |
-
2016
- 2016-02-04 CN CN201620113114.1U patent/CN205347319U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105524629A (en) * | 2016-02-04 | 2016-04-27 | 辛集市远翔环保能源科技有限公司 | Split type carbonization furnace set |
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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: 20160629 Termination date: 20200204 |