CN205740879U - One can produce box type carbide furnace continuously - Google Patents
One can produce box type carbide furnace continuously Download PDFInfo
- Publication number
- CN205740879U CN205740879U CN201620652482.3U CN201620652482U CN205740879U CN 205740879 U CN205740879 U CN 205740879U CN 201620652482 U CN201620652482 U CN 201620652482U CN 205740879 U CN205740879 U CN 205740879U
- Authority
- CN
- China
- Prior art keywords
- carbonization
- finished product
- discharging area
- layer
- carbonization chamber
- 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
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- 238000003763 carbonization Methods 0.000 claims abstract description 78
- 239000000463 material Substances 0.000 claims abstract description 32
- 238000007599 discharging Methods 0.000 claims abstract description 24
- 239000007789 gas Substances 0.000 claims abstract description 20
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims abstract description 4
- 239000001301 oxygen Substances 0.000 claims abstract description 4
- 229910052760 oxygen Inorganic materials 0.000 claims abstract description 4
- 239000002994 raw material Substances 0.000 claims abstract description 4
- 238000009413 insulation Methods 0.000 claims description 9
- 235000005956 Cosmos caudatus Nutrition 0.000 claims description 6
- 244000293323 Cosmos caudatus Species 0.000 claims description 6
- 229910000831 Steel Inorganic materials 0.000 claims description 6
- 239000004576 sand Substances 0.000 claims description 6
- 229910001220 stainless steel Inorganic materials 0.000 claims description 6
- 239000010935 stainless steel Substances 0.000 claims description 6
- 239000010959 steel Substances 0.000 claims description 6
- 241000239290 Araneae Species 0.000 claims description 3
- 230000005540 biological transmission Effects 0.000 claims description 3
- 238000001514 detection method Methods 0.000 claims description 3
- 239000002028 Biomass Substances 0.000 abstract description 6
- 238000004519 manufacturing process Methods 0.000 abstract description 5
- 238000000034 method Methods 0.000 abstract description 3
- 238000005516 engineering process Methods 0.000 description 3
- 238000010924 continuous production Methods 0.000 description 2
- 239000010902 straw Substances 0.000 description 2
- 230000007547 defect Effects 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 239000000779 smoke Substances 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
- 238000003466 welding Methods 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
Landscapes
- Carbon And Carbon Compounds (AREA)
Abstract
This utility model relates to one can produce box type carbide furnace continuously, it includes carbonization chamber, carbonization aerogenesis room, finished product discharging area, oil gas collection tank, finished product material collecting bin, carbonization chamber is a case structure, and carbonization chamber is from top to bottom divided into raw material layer, half charring layer and carbonization finished layer, carbonization aerogenesis room is arranged on the both sides of the carbonization finished layer of carbonization chamber, and pass through filter screen between carbonization aerogenesis room and carbonization chamber, being provided with several lighting-up tuyere and several oxygen feeder on the sidewall of carbonization chamber, carbonization aerogenesis room is connected by gas pipeline with oil gas collection tank；Finished product discharging area is arranged on the lower end of the carbonization finished layer of carbonization chamber, and the material of carbonization finished layer enters into finished product discharging area, and finished product material collecting bin is arranged on the lower end of finished product discharging area, moves down finished product material by finished product discharging area to finished product material collecting bin；Several supporting parts are had to support below whole body of heater.This utility model uses this utility model can realize the seriality carbonization of biomass material, need not cease fire in carbonization process, and production efficiency is high.
Description
Technical field
This utility model belongs to biomass carbonated technical field, is specifically related to one and can produce box type carbide furnace continuously.
Background technology
At present, the biomass energy of China is the abundantest, and in annual rural area, agricultural crop straw yield is about 700,000,000 tons, can make
For about 300,000,000 tons of power applications, about convert into 1.5 hundred million tons of standard coals.But have many areas but directly to be burnt by the straw in farmland
Burning processes, and the energy not only causes huge waste, and thick smoke also result in huge pollution to air, environment.
China has been promoted a conservation culture very important strategic importance by visible Biomass Energy Development, biomass carbonated technology.
Present stage, there is a lot of producer to put in the research of biomass generating apparatus again, but overall technology level all compares
Low, function is the most complete, and versatility is poor；More advanced Mobile chamber type stove, there is also the carbonization cycle long, equipment cost
Height, floor space is big, the shortcomings such as automatic and mechanical level is low；There is storing space in columnar continuous production rotary carbide furnace
Little, the unsuitable excessive defect of retort diameter.
Summary of the invention
The purpose of this utility model is to provide one can produce box type carbide furnace continuously.This device can be carried out as required
Large range of expand or shrink, it is simple to form the equipment of seriation.
The technical solution adopted in the utility model: one can produce box type carbide furnace continuously, it includes that carbonization chamber, carbonization are produced
Air chamber, finished product discharging area, oil gas collection tank, finished product material collecting bin, carbonization chamber is a case structure, and carbonization chamber from top to bottom divides
Making a living the bed of material, half charring layer and carbonization finished layer, carbonization aerogenesis room is arranged on the both sides of the carbonization finished layer of carbonization chamber, and carbonization
By filter screen between aerogenesis room and carbonization chamber, the sidewall of carbonization chamber is provided with several lighting-up tuyere and several oxygen feeder, carbonization
Aerogenesis room is connected by gas pipeline with oil gas collection tank；Finished product discharging area is arranged on the lower end of the carbonization finished layer of carbonization chamber,
The material of carbonization finished layer enters into finished product discharging area, and finished product material collecting bin is arranged on the lower end of finished product discharging area, by under finished product
Material district moves down finished product material to finished product material collecting bin；Several supporting parts are had to support below whole body of heater.
Further, the case structure of described carbonization chamber is by the internal high temperature stainless steel bed of material, middle high temperature resistant Margarita sand
Thermal insulation layer and the outside stainless steel bed of material are connected in sequence；The outer rim on case structure top be provided with angle steel or channel-section steel welding and
Become seal groove.
Further, the sidewall of described carbonization chamber is provided with several temperature detection mouth.
Further, described carbonization aerogenesis room is double-decked insulation, middle heat insulation with high temperature resistant Margarita sand.
Further, described carbonization aerogenesis room, according to the different length of body of heater, is divided into separate several sections, every section has
Pipeline leads to oil gas collection tank, and each pipeline leaves gas-distributing pipe valve.
Further, described oil gas collection tank is provided with switch total valve and air outlet valve flange-interface.
Further, described finished product discharging area is according on the length direction of body of heater, and horizontal arrangement number props up blanking device, blanking device
Two ends have bearing spider to be supported, and one has the power that travelling gear transmission motor transmits, and there is protecting wire net both sides, discharging area.
Further, the cross sectional shape of described finished product material collecting bin is triangular in shape, bottom circular arc, and there is screw feeding inside
Device, has the spiral feeder within the drive of motor power device to rotate outside collecting bin.
Compared with prior art it provides the benefit that this utility model: it is raw that this utility model uses this utility model to realize
The seriality carbonization of raw material of substance, need not in carbonization process cease fire, and production efficiency is high.Environmental pollution in whole production process
Little, artificial Meteorological is low, and automaticity is high, by functions such as frequency controls, the constant product quality of production, reliable, easily
In control.Comparing more columnar continuous production rotary carbide furnace, this utility model storage bin volume can be carried out relatively as required
Expand or shrink on a large scale, it is simple to form the production equipment of seriation.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model.
Detailed description of the invention
As it is shown in figure 1, one can produce box type carbide furnace continuously, it includes carbonization chamber 1, carbonization aerogenesis room 2, finished product blanking
District 3, oil gas collection tank 4, finished product material collecting bin 5, carbonization chamber 1 is a case structure, and carbonization chamber 1 is from top to bottom divided into raw material
Layer, half charring layer and carbonization finished layer, carbonization aerogenesis room 2 is arranged on the both sides of the carbonization finished layer of carbonization chamber 1, and carbonization aerogenesis
By filter screen between room 2 and carbonization chamber 1, the sidewall of carbonization chamber 1 is provided with several lighting-up tuyere 6 and several oxygen feeder, carbonization
Aerogenesis room 2 is connected by gas pipeline 8 with oil gas collection tank 4；Finished product discharging area 3 is arranged on the carbonization finished layer of carbonization chamber 1
Lower end, the material of carbonization finished layer enters into finished product discharging area 3, and finished product material collecting bin 5 is arranged on the lower end of finished product discharging area 3, logical
Cross finished product discharging area 3 and move down finished product material to finished product material collecting bin 5；Several supporting parts 9 are had to support below whole body of heater.
The case structure of described carbonization chamber 1 by the internal high temperature stainless steel bed of material, middle high temperature resistant Margarita sand thermal insulation layer and
The outside stainless steel bed of material is connected in sequence；Sealing that the outer rim on case structure top is provided with angle steel or channel-section steel is welded
Groove.
Several temperature detection mouth it is provided with on the sidewall of described carbonization chamber 1.
Described carbonization aerogenesis room 2 is double-decked insulation, middle heat insulation with high temperature resistant Margarita sand.
Described carbonization aerogenesis room 2, according to the different length of body of heater, is divided into separate several sections, every section has gas pipeline
8 lead to oil gas collection tank 4, and each gas pipeline 8 leaves gas-distributing pipe valve 10.
Switch total valve 11 and air outlet valve flange-interface 12 it is provided with on described oil gas collection tank 4.
Described finished product discharging area 3 is according on the length direction of body of heater, and horizontal arrangement number props up blanking device 13, blanking device 13 two ends
Having bearing spider 14 to be supported, one has travelling gear 15 to transmit the power that motor transmits, and there is protecting wire net 16 both sides, discharging area.
The cross sectional shape of described finished product material collecting bin 5 is triangular in shape, bottom circular arc, and there is spiral feeder inside, receives
The spiral feeder within the drive of motor power device is had to rotate outside collection storehouse.
Claims (8)
1. can produce a box type carbide furnace continuously, it include carbonization chamber, carbonization aerogenesis room, finished product discharging area, oil gas collection tank,
Finished product material collecting bin, it is characterised in that carbonization chamber is a case structure, and carbonization chamber is from top to bottom divided into raw material layer, half carbonization
Layer and carbonization finished layer, carbonization aerogenesis room is arranged on the both sides of the carbonization finished layer of carbonization chamber, and carbonization aerogenesis room and carbonization chamber
Between by filter screen, the sidewall of carbonization chamber is provided with several lighting-up tuyere and several oxygen feeder, carbonization aerogenesis room is received with oil gas
Collection tank is connected by gas pipeline；Finished product discharging area is arranged on the lower end of the carbonization finished layer of carbonization chamber, the material of carbonization finished layer
Entering into finished product discharging area, finished product material collecting bin is arranged on the lower end of finished product discharging area, is received to finished product material by finished product discharging area
Ji Cang moves down finished product material；Several supporting parts are had to support below whole body of heater.
One the most according to claim 1 can produce box type carbide furnace continuously, it is characterised in that described carbonization chamber box
Structure be sequentially connected with by the internal high temperature stainless steel bed of material, middle high temperature resistant Margarita sand thermal insulation layer and the outside stainless steel bed of material and
Become；The outer rim on case structure top is provided with angle steel or channel-section steel is welded seal groove.
One the most according to claim 1 can produce box type carbide furnace continuously, it is characterised in that the sidewall of described carbonization chamber
On be provided with several temperature detection mouth.
One the most according to claim 1 can produce box type carbide furnace continuously, it is characterised in that described carbonization aerogenesis room is
Double-decked insulation, middle heat insulation with high temperature resistant Margarita sand.
5. can produce box type carbide furnace continuously according to the one described in claim 1 or 4, it is characterised in that described carbonization aerogenesis
Room, according to the different length of body of heater, is divided into separate several sections, every section has pipeline lead to oil gas collection tank, each pipeline stays
There is gas-distributing pipe valve.
One the most according to claim 1 can produce box type carbide furnace continuously, it is characterised in that on described oil gas collection tank
It is provided with switch total valve and air outlet valve flange-interface.
One the most according to claim 1 can produce box type carbide furnace continuously, it is characterised in that described finished product discharging area root
According on the length direction of body of heater, horizontal arrangement number props up blanking device, and blanking device two ends have bearing spider to be supported, and one has transmission
The power that gear transmission motor transmits, there is protecting wire net both sides, discharging area.
One the most according to claim 1 can produce box type carbide furnace continuously, it is characterised in that described finished product material collecting bin
Cross sectional shape triangular in shape, bottom circular arc, there is spiral feeder inside, has motor power device to drive outside collecting bin
Internal spiral feeder rotates.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620652482.3U CN205740879U (en) | 2016-06-27 | 2016-06-27 | One can produce box type carbide furnace continuously |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620652482.3U CN205740879U (en) | 2016-06-27 | 2016-06-27 | One can produce box type carbide furnace continuously |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205740879U true CN205740879U (en) | 2016-11-30 |
Family
ID=57381347
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620652482.3U Expired - Fee Related CN205740879U (en) | 2016-06-27 | 2016-06-27 | One can produce box type carbide furnace continuously |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205740879U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2018223320A1 (en) * | 2017-06-07 | 2018-12-13 | 东莞市裕证工业设备有限公司 | Continuous carbonization system |
-
2016
- 2016-06-27 CN CN201620652482.3U patent/CN205740879U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2018223320A1 (en) * | 2017-06-07 | 2018-12-13 | 东莞市裕证工业设备有限公司 | Continuous carbonization system |
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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: 20161130 |