CN205603521U - A raw material feed device that is arranged in pyrolysis of coal revolver chemical industry system reacting furnace - Google Patents
A raw material feed device that is arranged in pyrolysis of coal revolver chemical industry system reacting furnace Download PDFInfo
- Publication number
- CN205603521U CN205603521U CN201620390382.8U CN201620390382U CN205603521U CN 205603521 U CN205603521 U CN 205603521U CN 201620390382 U CN201620390382 U CN 201620390382U CN 205603521 U CN205603521 U CN 205603521U
- Authority
- CN
- China
- Prior art keywords
- ribbon
- coal
- spiral
- reacting furnace
- pyrolysis
- 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.)
- Withdrawn - After Issue
Links
Landscapes
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Abstract
The utility model provides a raw material feed device that is arranged in pyrolysis of coal revolver chemical industry system reacting furnace, the left end and the screw conveyer power package (3) of solid shafting spiral (4) are connected, right -hand member connection tube (5), right -hand member at the barrel is provided with spiral shell tape spool cover (12), spiral shell tape spool cover is supported by spiral shell tape spool cover mount (11), the upper portion of dry coal bunker (2) sets up weighing module (1), control the inside material level height of dry coal bunker through weighing module with screw conveyer power package's linkage, carry spiral shell area (7) inside being equipped with of barrel, carry spiral shell area left end to be connected with the spindle nose of solid shafting spiral, carry the right -hand member in spiral shell area to connect spiral shell tape spool cover, being close to the one end of solid shafting spiral at the barrel and having offered gas outlet (8), the gas outlet is connected with cooling device, and its feed is even, and the raise dust is few, reduces because of the blocking phenomenon that the oil gas in the drying furnace bonded and brings on helical blade, avoids getting into the potential safety hazard of bringing in the drying furnace along transfer passage because of reacting furnace gas.
Description
Technical field
This utility model relates to a kind of feedstock device, specifically a kind of reacting furnace in pyrolysis of coal revolving burner chemical system
Feedstock device, belong to pyrolysis of coal chemical technology field.
Background technology
Coal is the most uncleanly resource in the three macrofossil energy, and its discharge intensity developing process is 2 times of natural gas,
30% is exceeded than oil.Country's correlation report shows, in the PM2.5 that coal produces, about 6 one-tenth is generation of directly being burnt by coal
, about 4 one-tenth is the key industry discharge used with coal, produces high value added product by the method for improving quality of coal by pyrolysis
Be clean, utilize the effective way of coal resources efficiently.
At present, the feed arrangement of revolving reaction stove in pyrolysis of coal chemical industry, the common conveying worm of general employing directly will be from baking
The moisture-free coal processed in dry stove delivers in reacting furnace, and its feeding is uneven, and airborne dust is more；Contained oil gas in moisture-free coal
Can be bonded on helical blade, result in blockage phenomenon；The gas that reacting furnace reaction produces also can enter along transfer passage and dry
In stove, cause potential safety hazard to drying course；The oil gas produced after traditional reacting furnace reaction need to be by special oil-gas recovery system
Being collected transhipment to process, its structure is complicated, and operation easier is big.
Summary of the invention
The problem existed for above-mentioned prior art, this utility model provides one anti-in pyrolysis of coal revolving burner chemical system
Answering the feedstock device of stove, its feeding is uniform, and airborne dust is few, reduces because the oil gas in drying oven is bonded on helical blade band
The clogging come, it is to avoid because reacting furnace gas enters in drying oven the potential safety hazard brought along transfer passage, simple in construction,
Convenient to operate.
To achieve these goals, this utility model provides a kind of raw material of reacting furnace in pyrolysis of coal revolving burner chemical system
Feed arrangement, including being dried coal bunker and being arranged on the solid shafting spiral of dry coal bunker bottom；The left end of solid shafting spiral and spiral shell
Rotation conveyer power packages connects, and right-hand member connector drum, the right-hand member at cylinder is provided with ribbon axle sleeve, and ribbon axle sleeve is by ribbon axle
Set fixed mount supports, and the top of described dry coal bunker arranges Weighing module, by Weighing module and conveying worm power packages
Linkage control to be dried controlling level within coal bunker；It is provided with conveying ribbon, described conveying ribbon left end in inner barrel
Being connected with the spindle nose of solid shafting spiral, the right-hand member of conveying ribbon connects ribbon axle sleeve；At cylinder near one end of solid shafting spiral
Offering gas outlet, gas outlet connects chiller.
As further improvement of the utility model, uniform some ribbon support bars on the circumference of conveying ribbon.
As further improvement of the utility model, at cylinder, expansion joint is set near the part of right-hand member, described expansion joint with
Reacting furnace burner stationary seal ring connects.
As further improvement of the utility model, ribbon axle sleeve fixed mount is set at least three, its one end and ribbon axle sleeve
Connecting, the other end is connected with the inwall of cylinder.
As further improvement of the utility model, described chiller is oil gas cooling tower.
Dry coal bunker of the present utility model stores for raw material, permissible with the interlocking of conveying worm power packages by Weighing module
Setting certain thickness of feed layer, this thickness of feed layer can increase air resistance, prevents reacting furnace gas from entering along transfer passage
Drying oven, during material carries, the thickness of feed layer of moisture-free coal must bury whole bottom ribbon cylinder, the driest
Coal just can clear up the tar being bonded on ribbon voluntarily, and moisture-free coal is walked in ribbon cylinder bottom, and oil gas, part oil are walked in top
Gas is bonded on ribbon and is dried coal and clears up return reacting furnace voluntarily, and remaining oil gas is entered by the gas outlet on ribbon cylinder top
Enter oil gas cooling tower or oil gas purifier, thus play feedstock transportation and the effect of oil gas derivation；Its feeding is uniform, airborne dust
Few, reduce because the oil gas in drying oven is bonded in the clogging brought on helical blade, it is to avoid because reacting furnace gas is along defeated
Passage is sent to enter the potential safety hazard brought in drying oven, simple in construction, it is simple to operation, processing and fabricating cost is cheap, practicality
By force.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model；
Fig. 2 is that the A-A of Fig. 1 is to sectional view.
In figure: 1, Weighing module, 2, be dried coal bunker, 3, conveying worm power packages, 4, solid shafting spiral, 5, cylinder,
6, ribbon support bar, 7, ribbon, 8, gas outlet, 9, expansion joint, 10, reacting furnace burner stationary seal ring, 11, spiral shell
Band axle sleeve fixed mount, 12, ribbon axle sleeve.
Detailed description of the invention
The utility model is described in further detail below in conjunction with the accompanying drawings.
As shown in Figure 1 to Figure 2, a kind of feedstock device of reacting furnace in pyrolysis of coal revolving burner chemical system, including
It is dried coal bunker 2 and is arranged on the solid shafting spiral 4 of dry coal bunker 2 bottom；The left end of solid shafting spiral 4 and conveying worm
Power packages 3 connects, right-hand member connector drum 5, and the right-hand member at cylinder 5 is provided with ribbon axle sleeve 12, and ribbon axle sleeve 12 is by ribbon
Axle sleeve fixed mount 11 supports, and the top of described dry coal bunker 2 arranges Weighing module 1, by Weighing module 1 and spiral transferring
The linkage sending mechanomotive force group 3 controls to be dried the controlling level within coal bunker 2, in feed coal course of conveying, is dried coal bunker 2
Keep certain controlling level, it becomes possible to ensureing that solid shafting spiral 4 is full pipe condition, the thickness of feed layer in cylinder 5 to keep
Bury the bottom of whole cylinder 5, control the thickness of the bed of material in cylinder 5 according to the rotary speed of conveying worm power packages 3,
Conveying worm power packages 3 is cvt controller；Conveying ribbon 7, described conveying ribbon 7 it is provided with inside cylinder 5
Left end is connected with the spindle nose of solid shafting spiral 4, and the right-hand member of conveying ribbon 7 connects ribbon axle sleeve 12；At cylinder 5 near solid
One end of axle spiral 4 offers gas outlet 8, and gas outlet 8 connects chiller.
Preferably, prevent, in order to increase the rigidity of conveying ribbon 7, the deformation produced because of ribbon rigidity difference, at conveying ribbon 7
Circumference on uniform some ribbon support bars 6.
Preferably, in order to increase the sealing of cylinder 5, arranging expansion joint 9 at cylinder 5 near the part of right-hand member, described is swollen
Swollen joint 9 is connected with reacting furnace burner stationary seal ring 10.
Preferably, ribbon axle sleeve fixed mount 11 is set at least three, and its one end is connected with ribbon axle sleeve 12, the other end with
The inwall of cylinder 5 connects.
Preferably, chiller is oil gas cooling tower.
During use, drying oven the feed coal after drying enters dry coal bunker 2 and stores, and its controlling level is by Weighing module 1 He
The motor linkage of conveying worm power packages 3 controls, and adjusts conveying worm rotating speed and controls the thickness of feed layer in cylinder 5,
During feedstock transportation, certain thickness of feed layer need to be ensured, thus increase air resistance, prevent reacting furnace gas along defeated
Passage is sent to enter drying oven；The moisture-free coal of solid shafting spiral 4 part is full packages operation thus reaches certain resistance and seal work
It is connected with reacting furnace burner stationary seal ring 10 with expansion joint 9 with, ribbon transport portion thus plays sealing function；Conveying ribbon
The circumference uniform distribution ribbon support bar 6 of 7, prevents because ribbon rigidity difference is deformed to increase ribbon rigidity；Moisture-free coal is through solid
Axle spiral 4 delivers into ribbon transport portion, and the thickness of the bed of material must bury whole bottom ribbon, and such moisture-free coal is the most permissible
Cleaning is bonded in the tar on conveying ribbon 7 voluntarily, and moisture-free coal is walked in cylinder 5 bottom, and oil gas is walked on top, and a part is bonded in
Oil gas on conveying ribbon 7 is dried coal and clears up voluntarily and return reacting furnace with dry coal, and remaining oil gas is by cylinder 5 top
Gas outlet 8 enters oil gas cooling tower.
Claims (5)
1. a feedstock device for reacting furnace in the pyrolysis of coal revolving burner chemical system, including dry coal bunker (2) with
And it is arranged on the solid shafting spiral (4) of dry coal bunker (2) bottom；The left end of solid shafting spiral (4) is motor-driven with helical feed
Power group (3) connects, and right-hand member connector drum (5), the right-hand member at cylinder (5) is provided with ribbon axle sleeve (12), ribbon axle sleeve
(12) supported by ribbon axle sleeve fixed mount (11), it is characterised in that the top of described dry coal bunker (2) arranges and weighs
Module (1), controls to be dried coal bunker (2) by the linkage of Weighing module (1) Yu conveying worm power packages (3) internal
Controlling level；Ribbon (7) is carried, described conveying ribbon (7) left end and solid shafting spiral shell internal being provided with of cylinder (5)
The spindle nose of rotation (4) connects, and the right-hand member of conveying ribbon (7) connects ribbon axle sleeve (12)；At cylinder (5) near solid shafting
One end of spiral (4) offers gas outlet (8), and gas outlet (8) connects chiller.
A kind of feedstock device of reacting furnace in pyrolysis of coal revolving burner chemical system the most according to claim 1,
It is characterized in that, uniform some ribbon support bars (6) on the circumference of conveying ribbon (7).
A kind of feedstock dress of reacting furnace in pyrolysis of coal revolving burner chemical system the most according to claim 1 and 2
Put, it is characterised in that arranging expansion joint (9) at cylinder (5) near the part of right-hand member, described expansion joint (9) is with anti-
Stove burner stationary seal ring (10) is answered to connect.
A kind of feedstock dress of reacting furnace in pyrolysis of coal revolving burner chemical system the most according to claim 1 and 2
Put, it is characterised in that described ribbon axle sleeve fixed mount (11) is set at least three, its one end and ribbon axle sleeve (12)
Connecting, the other end is connected with the inwall of cylinder (5).
A kind of feedstock device of reacting furnace in pyrolysis of coal revolving burner chemical system the most according to claim 3,
It is characterized in that, described chiller is oil gas cooling tower.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620390382.8U CN205603521U (en) | 2016-04-29 | 2016-04-29 | A raw material feed device that is arranged in pyrolysis of coal revolver chemical industry system reacting furnace |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620390382.8U CN205603521U (en) | 2016-04-29 | 2016-04-29 | A raw material feed device that is arranged in pyrolysis of coal revolver chemical industry system reacting furnace |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205603521U true CN205603521U (en) | 2016-09-28 |
Family
ID=56968213
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620390382.8U Withdrawn - After Issue CN205603521U (en) | 2016-04-29 | 2016-04-29 | A raw material feed device that is arranged in pyrolysis of coal revolver chemical industry system reacting furnace |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205603521U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105778943A (en) * | 2016-04-29 | 2016-07-20 | 徐州曹氏化工机械制造有限公司 | Raw material feeding device for reaction furnace of coal pyrolysis rotary furnace chemical process system |
-
2016
- 2016-04-29 CN CN201620390382.8U patent/CN205603521U/en not_active Withdrawn - After Issue
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105778943A (en) * | 2016-04-29 | 2016-07-20 | 徐州曹氏化工机械制造有限公司 | Raw material feeding device for reaction furnace of coal pyrolysis rotary furnace chemical process system |
| CN105778943B (en) * | 2016-04-29 | 2019-03-08 | 徐州曹氏化工机械制造有限公司 | A kind of feedstock device for reacting furnace in pyrolysis of coal revolving burner chemical system |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN202530040U (en) | Continuous biomass dry-distillation carbonization apparatus | |
| CN109477010A (en) | For waste plastic to be converted to the system and technique of fuel | |
| CN102703121B (en) | Biomass gas generation system | |
| CN102643657A (en) | Continuous biomass carbonization process | |
| EP2553050B1 (en) | Method and apparatus for torrefaction of biomass material | |
| CN206069777U (en) | A kind of low order low-temperature pyrolysis of coal horizontal revolving kiln | |
| CN110003927B (en) | Grinding belt type biomass rapid catalytic pyrolysis device and method | |
| CN103589441B (en) | Improved energy-saving continuous gasification cracking furnace | |
| US4348211A (en) | Gas generating system | |
| CN205603521U (en) | A raw material feed device that is arranged in pyrolysis of coal revolver chemical industry system reacting furnace | |
| CN106393782A (en) | Device and method for preparing rice hull forming and briquetting fuel | |
| CN105953575A (en) | Self-detection indirect heating type rotary furnace | |
| CN110846063B (en) | High-efficient processing system of junked tire micelle | |
| CN205974420U (en) | Smokeless carbonization system of straw | |
| CN106082576A (en) | A kind of low temperature continuous pyrolysis processes mud fixed bed reactors and method | |
| CN205821244U (en) | Particulate biomass continuous carbonization device | |
| CN106281381A (en) | Rotatable radiation bed | |
| CN206472802U (en) | A kind of normal pressure hot blast chain type drying baker | |
| US3331595A (en) | Apparatus for effecting contact between solids and gases | |
| CN105778955A (en) | Dynamic continuous organic solid waste gas-carbon oil cogeneration device | |
| CN105778943A (en) | Raw material feeding device for reaction furnace of coal pyrolysis rotary furnace chemical process system | |
| CN105318681A (en) | Dryer or pyrolyzer | |
| CN205684468U (en) | The continuous conveying device of heat treated material under protective atmosphere | |
| CN203498319U (en) | Improved energy-saving continuous gasification cracking furnace | |
| CN105692612A (en) | Oxidation carbonization device and method of coal-base activated carbon |
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: 20160928 Effective date of abandoning: 20190308 |