CN209568061U - Carbonized by means of superheated steam furnace continuous discharge cooling conveying device - Google Patents
Carbonized by means of superheated steam furnace continuous discharge cooling conveying device Download PDFInfo
- Publication number
- CN209568061U CN209568061U CN201822254899.6U CN201822254899U CN209568061U CN 209568061 U CN209568061 U CN 209568061U CN 201822254899 U CN201822254899 U CN 201822254899U CN 209568061 U CN209568061 U CN 209568061U
- Authority
- CN
- China
- Prior art keywords
- screw conveyor
- cooling
- water
- discharge port
- jacket
- 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.)
- Active
Links
- 238000001816 cooling Methods 0.000 title claims abstract description 89
- 239000000463 material Substances 0.000 claims abstract description 16
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 97
- 238000007689 inspection Methods 0.000 claims description 7
- 239000007788 liquid Substances 0.000 claims description 4
- 150000003839 salts Chemical class 0.000 abstract description 13
- 238000003763 carbonization Methods 0.000 abstract description 12
- 239000002893 slag Substances 0.000 abstract description 10
- 238000005516 engineering process Methods 0.000 abstract description 7
- 238000005336 cracking Methods 0.000 abstract description 5
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 abstract description 4
- 229910052799 carbon Inorganic materials 0.000 abstract description 4
- 238000004064 recycling Methods 0.000 abstract description 2
- 238000003756 stirring Methods 0.000 description 10
- 239000000543 intermediate Substances 0.000 description 8
- 238000007664 blowing Methods 0.000 description 5
- 238000007599 discharging Methods 0.000 description 5
- 239000005416 organic matter Substances 0.000 description 4
- 239000002351 wastewater Substances 0.000 description 4
- 238000000034 method Methods 0.000 description 3
- 238000006243 chemical reaction Methods 0.000 description 2
- 239000002826 coolant Substances 0.000 description 2
- 239000000498 cooling water Substances 0.000 description 2
- 230000008878 coupling Effects 0.000 description 2
- 238000010168 coupling process Methods 0.000 description 2
- 238000005859 coupling reaction Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 239000003814 drug Substances 0.000 description 2
- 238000004043 dyeing Methods 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 239000010813 municipal solid waste Substances 0.000 description 2
- 239000000575 pesticide Substances 0.000 description 2
- 238000007639 printing Methods 0.000 description 2
- 239000002910 solid waste Substances 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- 239000003638 chemical reducing agent Substances 0.000 description 1
- 238000004332 deodorization Methods 0.000 description 1
- 230000000994 depressogenic effect Effects 0.000 description 1
- 238000004090 dissolution Methods 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 230000008676 import Effects 0.000 description 1
- 239000010842 industrial wastewater Substances 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 239000002574 poison Substances 0.000 description 1
- 231100000614 poison Toxicity 0.000 description 1
- 239000010802 sludge Substances 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
Landscapes
- Processing Of Solid Wastes (AREA)
Abstract
The utility model relates to overheat steam technology fields, more particularly, to a kind of carbonized by means of superheated steam furnace continuous discharge cooling conveying device, comprising: the first screw conveyor, the second screw conveyor and third screw conveyor；The top of the lower end of first screw conveyor is provided with for making the feed inlet that material enters after carbonized by means of superheated steam, and the lower part of the higher-end of the first screw conveyor is provided with discharge port；The top of the lower end of second screw conveyor is provided with feed inlet, and the lower part of the higher-end of the second screw conveyor is provided with discharge port；One end top of third spiral transferring is provided with feed inlet, and the feed inlet of third spiral transferring is connect with the discharge port of the second screw conveyor.Carbonized by means of superheated steam furnace continuous discharge cooling conveying device provided by the utility model, it is ensured that with high salt, high COD and other organic matters are smoothly slagged tap, packed or recycling and reusing by the slag salt and other carbon slags after the continuous anaerobic carbonization cracking of superheated steam.
Description
Technical field
The utility model relates to overheat steam technology fields, cold more particularly, to a kind of carbonized by means of superheated steam furnace continuous discharge
But conveying device.
Background technique
It is generated in many Intermediates Industry production processes such as medicine intermediate, pesticide intermediate, printing and dyeing intermediate, food big
With high salt, the high-COD waste water of amount, the improvement discharge of such waste water are always the world-famous puzzle of wastewater from chemical industry industry.It is steamed by multiple-effect
The solid slag salt formed is dried in hair, embrane method filtering, spray, and waste liquid is formally only transformed into solid waste form, having substantially
There is no eliminate for the harmful organic matter of poison.It, can will be in slag salt currently, superheated steam anaerobic carbonization technology disclosed in the relevant technologies
Organic carbon cracking, to make dangerous waste slag salt become available industry byproduct or common solid waste, so that counter push away solution
The emission problem of high COD, industrial wastewater with high salt.But for up to 600 DEG C after the cracking of superheated steam high temperature cabonization
How left and right slag salt, which is cooled down, discharged, collected, recycled etc., still remains certain difficulty.
The information disclosed in the background technology section is intended only to deepen the reason to the general background technology of the utility model
Solution, and it is known to those skilled in the art existing to be not construed as recognizing or imply that the information is constituted in any form
Technology.
Utility model content
The purpose of this utility model is to provide a kind of carbonized by means of superheated steam furnace continuous discharge cooling conveying devices, to solve
The technical problems existing in the prior art.
To achieve the goals above, the utility model uses following technical scheme:
The utility model provides a kind of carbonized by means of superheated steam furnace continuous discharge cooling conveying device comprising: the first spiral
Conveyer, the second screw conveyor and third screw conveyor；
First screw conveyor is inclined to set, and the top setting of the lower end of first screw conveyor is useful
The feed inlet that material enters after making carbonized by means of superheated steam, the lower part of the higher-end of first screw conveyor is provided with discharging
Mouthful；Second screw conveyor is inclined to set, and first screw conveyor is parallel with first screw conveyor
Setting, the top of the lower end of second screw conveyor is provided with feed inlet, the higher-end of second screw conveyor
Lower part be provided with discharge port, the discharge port of first screw conveyor and the feed inlet of second screw conveyor pass through
Blowing stopper connection；The third screw conveyor is in horizontally disposed, the third screw conveyor and second helical feed
Machine is arranged in a crossed manner, and one end top of the third spiral transferring is provided with feed inlet, the feed inlet and second of the third spiral transferring
The discharge port of screw conveyor connects, and the bottom interval of the third screw conveyor is provided with the first discharge port, the second discharging
Mouth and third discharge port.
As a kind of further technical solution, it is provided between the feed inlet and discharge port of first screw conveyor
First water(-cooling) jacket, the first water(-cooling) jacket coaxial package is in the working cavity of first screw conveyor, and described first
The lower end lower part of water(-cooling) jacket is provided with water inlet, and the higher-end top of first water(-cooling) jacket is provided with water outlet.
As a kind of further technical solution, first screw conveyor is set in the two sides of first water(-cooling) jacket
It is equipped with inspection socket.
As a kind of further technical solution, the discharge port of first screw conveyor is located at second spiral transferring
Send the surface of the feed inlet of machine.
As a kind of further technical solution, it is provided between the feed inlet and discharge port of second screw conveyor
Second water(-cooling) jacket, the second water(-cooling) jacket coaxial package is in the working cavity of second screw conveyor, and described second
The lower end lower part of water(-cooling) jacket is provided with water inlet, and the higher-end top of second water(-cooling) jacket is provided with water outlet.
As a kind of further technical solution, second screw conveyor is set in the two sides of second water(-cooling) jacket
It is equipped with inspection socket.
As a kind of further technical solution, the discharge port of second screw conveyor is located at the third spiral transferring
Send the surface of the feed inlet of machine.
As a kind of further technical solution, the first discharge port and the second discharge port of the third screw conveyor it
Between be provided with a third water(-cooling) jacket, be provided with one between the second discharge port and third discharge port of the third screw conveyor
Third water(-cooling) jacket, two third water(-cooling) jackets difference coaxial packages in the working cavity of the third screw conveyor,
One end lower part of the third water(-cooling) jacket is provided with water inlet, and one end other end top of the third water(-cooling) jacket is provided with
Water outlet.
As a kind of further technical solution, first discharge port, second discharge port and third discharging
Mouth is respectively arranged with pneumatic gate valve, and is connected to liquid reserve tank/material storing box/jumbo bag.
By adopting the above technical scheme, the utility model has the following beneficial effects:
Carbonized by means of superheated steam furnace continuous discharge cooling conveying device provided by the utility model, it is ensured that with high salt, high COD
And other organic matters are smoothly slagged tap, pack or are returned by slag salt and other carbon slags after the continuous anaerobic carbonization cracking of superheated steam
It receives and recycles.
Detailed description of the invention
It, below will be right in order to illustrate more clearly of specific embodiment of the present invention or technical solution in the prior art
Specific embodiment or attached drawing needed to be used in the description of the prior art are briefly described, it should be apparent that, it is described below
In attached drawing be that some embodiments of the utility model are not paying creativeness for those of ordinary skill in the art
Under the premise of labour, it is also possible to obtain other drawings based on these drawings.
Fig. 1 is the first party of carbonized by means of superheated steam furnace continuous discharge cooling conveying device provided by the embodiment of the utility model
To status diagram；
Fig. 2 is the second party of carbonized by means of superheated steam furnace continuous discharge cooling conveying device provided by the embodiment of the utility model
To status diagram.
Icon: the first screw conveyor of 15-；16- inspection socket；17- drainage interface；The second screw conveyor of 19-；20-
Three screw conveyors；21- collection device；71- Blowing stopper；The first water(-cooling) jacket of 151-；The second water(-cooling) jacket of 191-；201- is pneumatic
Gate valve；203- third water(-cooling) jacket.
Specific embodiment
The technical solution of the utility model is clearly and completely described below in conjunction with attached drawing, it is clear that described
Embodiment is the utility model a part of the embodiment, instead of all the embodiments.Based on the embodiments of the present invention, originally
Field those of ordinary skill every other embodiment obtained without making creative work belongs to practical
Novel protected range.
It is in the description of the present invention, it should be noted that term " center ", "upper", "lower", "left", "right", " perpendicular
Directly ", the orientation or positional relationship of the instructions such as "horizontal", "inner", "outside" is to be based on the orientation or positional relationship shown in the drawings, and is only
For ease of description the utility model and simplify description, rather than the device or element of indication or suggestion meaning must have it is specific
Orientation, be constructed and operated in a specific orientation, therefore should not be understood as limiting the present invention.In addition, term " the
One ", " second ", " third " are used for descriptive purposes only and cannot be understood as indicating or suggesting relative importance.
In the description of the present invention, it should be noted that unless otherwise clearly defined and limited, term " is pacified
Dress ", " connected ", " connection " shall be understood in a broad sense, for example, it may be being fixedly connected, may be a detachable connection, or integrally
Connection；It can be mechanical connection, be also possible to be electrically connected；Can be directly connected, can also indirectly connected through an intermediary,
It can be the connection inside two elements.For the ordinary skill in the art, on can understanding as the case may be
State the concrete meaning of term in the present invention.
Specific embodiment of the present utility model is described in detail below in conjunction with attached drawing.It should be understood that herein
Described specific embodiment is only used for describing and explaining the present invention, and is not intended to limit the utility model.
Embodiment one
In conjunction with shown in Fig. 1 to Fig. 2, the present embodiment provides a kind of carbonized by means of superheated steam furnace continuous discharge cooling conveying device,
Comprising: the first screw conveyor 15, the second screw conveyor 19 and third screw conveyor 20；First screw conveyor
15 are inclined to set, and the top of the lower end of first screw conveyor 15 is provided with for making material after carbonized by means of superheated steam
The lower part of the feed inlet of entrance, the higher-end of first screw conveyor 15 is provided with discharge port；Second helical feed
Machine 19 is inclined to set, and first screw conveyor 15 is arranged in parallel with first screw conveyor 15, and described second
The top of the lower end of screw conveyor 19 is provided with feed inlet, the lower part setting of the higher-end of second screw conveyor 19
There is discharge port, the discharge port of first screw conveyor 15 and the feed inlet of second screw conveyor 19 pass through Blowing stopper
71 connections；The third screw conveyor 20 is in horizontally disposed, the third screw conveyor 20 and second helical feed
Machine 19 is arranged in a crossed manner, and one end top of the third spiral transferring is provided with feed inlet, the feed inlet of the third spiral transferring and
The discharge ports of two screw conveyors 19 connects, and the bottom interval of the third screw conveyor 20 is provided with the first discharge port, the
Two discharge ports and third discharge port.Material after superheated steam high temperature cabonization is up to 600 DEG C or so, through this embodiment may be used
Realization drops to 80 DEG C at the appointed time, in the confined space and collects, packs hereinafter, facilitating and discharging, and facilitates dissolution, recycles.
It is worth noting that the present embodiment carbonized by means of superheated steam furnace continuous discharge cooling conveying device is not limited among medicine
With high salt, the high-COD waste water generated in the intermediates production processes such as body, pesticide intermediate, printing and dyeing intermediate, food processing, processing
Organic carbon processing in (derivative) the high COD slag salt generated, also includes the electronics rubbish such as mobile phone, electric wire, cable, wiring board
The carbonization treatment of the intermediate organic matter such as rubbish, sludge, greasy filth.
In the present embodiment, it is preferable that be provided with first between the feed inlet and discharge port of first screw conveyor 15
Water(-cooling) jacket 151,151 coaxial package of the first water(-cooling) jacket are described in the working cavity of first screw conveyor 15
The lower end lower part of first water(-cooling) jacket 151 is provided with water inlet, and the higher-end top of first water(-cooling) jacket 151 is provided with
Water outlet.Preferably, first screw conveyor 15 is provided with inspection socket 16 in the two sides of first water(-cooling) jacket 151.
Preferably, the discharge port of first screw conveyor 15 is located at the surface of the feed inlet of second screw conveyor 19.
In the present embodiment, it is preferable that be provided with second between the feed inlet and discharge port of second screw conveyor 19
Water(-cooling) jacket 191,191 coaxial package of the second water(-cooling) jacket are described in the working cavity of second screw conveyor 19
The lower end lower part of second water(-cooling) jacket 191 is provided with water inlet, and the higher-end top of second water(-cooling) jacket 191 is provided with
Water outlet.Preferably, second screw conveyor 19 is provided with inspection socket 16 in the two sides of second water(-cooling) jacket 191.
Preferably, the discharge port of second screw conveyor 19 is located at the surface of the feed inlet of the third screw conveyor 20.
In the present embodiment, it is preferable that set between the first discharge port and the second discharge port of the third screw conveyor 20
It is equipped with a third water(-cooling) jacket 203, is provided between the second discharge port and third discharge port of the third screw conveyor 20
One third water(-cooling) jacket 203, two third water(-cooling) jackets 203 distinguish coaxial package in the third screw conveyor 20
Working cavity, one end lower part of the third water(-cooling) jacket 203 are provided with water inlet, one end of the third water(-cooling) jacket 203
Other end top is provided with water outlet.Preferably, first discharge port, second discharge port and the third discharge port point
It is not provided with pneumatic gate valve 201, and is connected to liquid reserve tank/material storing box/jumbo bag (can always be referred to as collection device 21).
Preferably, each screw conveyor is provided with drainage interface in the lower part of its first end.
For the water inlet of each water(-cooling) jacket and water outlet, it can use independent way of supplying water certainly can also
Using concentration cooling cycle way of supplying water.Such as:
1. the present embodiment further includes pump group, one end of the pump group is connect with water source, the other end and first third
The water inlet of water(-cooling) jacket 203 connects, the water outlet of first third water(-cooling) jacket 203 and second adjacent third water
The water inlet of coolant jacket 203 connects, the water outlet of second third water(-cooling) jacket 203 and the water inlet of the second water(-cooling) jacket 191
Connection, the water outlet of the second water(-cooling) jacket 191 are connect with the water inlet of the first water(-cooling) jacket 151, and the first water(-cooling) jacket 151 goes out
The mouth of a river is connect with water source.
2. the present embodiment further includes pump group, one end of the pump group is connect with cooling water source pond, and the other end is respectively with first
Water(-cooling) jacket, the second water(-cooling) jacket, the connection of third water(-cooling) jacket water inlet, and using hydraulic pressure the first water(-cooling) jacket, the second water
Coolant jacket, third water(-cooling) jacket water outlet hot water cooling water source pond is depressed by pipeline, utilize cooling column is unified to cool down.
It is worth noting that the quantity of screw conveyor (stirring cage) can be 1,2,3, even more quantity.It is cold
But the combination for the stirring cage, lag cooler of discharging can be stirring cage+lag cooler, be also designed to stirring cage+lag cooler+stirring cage, stirring cage quantity
It is unlimited, it is needed to carry out permutation and combination according to scene.Stirring cage design can be with level design, and band inclination angle is designed.Stirring cage is connected with each other,
It can be connected with straight line, multi-angle connection can also be intersected.71 position of Blowing stopper is not limited to the position designed in figure, in combination with existing
The specific layout in field, installs stirring cage quantity, different positions is selected to install；Blowing stopper 71 can be by motor, electrical automatic control
System, may be designed in weight (weight) formula Mechanical course.600 DEG C or so materials are applicable in the design of this device, same needle after carbonization
To 700~800 DEG C, 500 DEG C, 300 DEG C of materials below also this applicable device.
To sum up, a kind of carbonized by means of superheated steam furnace continuous discharge cooling conveying device provided in this embodiment has following excellent
Point:
1), the material after 600 DEG C or so of carbonization conveys by the cooling stirring cage of more piece, lag cooler, cools, and can be down to
80 DEG C are collected hereinafter, lower temperature discharge can also be down to.
2) the cooling conveying of material, discharge process are controlled by variable-frequency motor, speed reducer after, being carbonized, conveying speed, conveying capacity,
Cooling temperature is controlled by ordinary appliances, switching knob, can also transfer to automation control in PLC programming set.
3) discharge of materials after, cooling, collection, pack, recycling, convenient and efficient.
Embodiment two
For carbonized by means of superheated steam furnace continuous discharge cooling conveying device, in the lower end of the first screw conveyor 15
Top be provided with feed inlet, which can connect with the discharge port of the continuous anaerobic carbonization operating unit of superheated steam.The mistake
The continuous anaerobic carbonization operating unit of hot steam includes: superheated steam pipeline assembly and the first carbonization set gradually from top to bottom
Furnace, the second carbide furnace, third carbide furnace；The upper entrance of the first end of first carbide furnace is for inputting object to be processed
Material, the lower part outlet of the second end of first carbide furnace are connect with the upper entrance of the second end of second carbide furnace, institute
The lower part outlet for stating the first end of the second carbide furnace is connect with the upper entrance of the first end of the third carbide furnace, the third
The lower part outlet of the second end of carbide furnace is used to export the material after carbonization；The superheated steam pipeline assembly includes: that overheat is steamed
Vapour general pipeline, superheated steam branch pipe, exhaust main and exhaust branch pipe；The superheated steam general pipeline passes through each superheated steam branch pipe point
It is not connect with first carbide furnace, the second carbide furnace, third carbide furnace, the exhaust main is distinguished by each exhaust branch pipe
It is connect with first carbide furnace, the second carbide furnace, third carbide furnace.
Preferably, the exhaust branch pipe includes first exhaust branch pipe, second exhaust branch pipe and third exhaust branch pipe, and described
One exhaust branch pipe is connected to the middle part of first carbide furnace, and the second exhaust branch pipe is connected in second carbide furnace
Portion, the third exhaust branch pipe are connected to the middle part of third carbide furnace；The superheated steam branch pipe includes: the first superheated steam branch
Pipe, the second superheated steam branch pipe and third superheated steam branch pipe, the first superheated steam branch pipe are connected to first carbonization
The middle part of furnace, the second superheated steam branch pipe are connected to the middle part of second carbide furnace, the third superheated steam branch pipe
It is connected to the middle part of third carbide furnace.
Preferably, certainly, exhaust branch pipe and superheated steam branch pipe can be independently arranged, can also gathers together and sets
Set, such as: exhaust branch pipe and superheated steam branch pipe can be set in one (such as: superheated steam branch pipe is located at center, and exhaust is propped up
Pipe coaxial package is in the periphery of superheated steam branch pipe).The organic matter in high organic matter or other materials in slag salt passes through first
Carbide furnace, the second carbide furnace, third carbide furnace, come into full contact with superheated steam, and the organic exhaust gas after anaerobic carbonization cracking passes through
Exhaust branch pipe imports exhaust main, is extracted into rear end deodorization stove high-temperature oxydation and clean processing using the centrifugal blower of exhaust emissions.
Preferably, each carbide furnace can also use double-screw type with single screw.
Such as: carbide furnace includes: furnace body shell, furnace body inner casing, the first output shaft, the second output shaft, gear-box, shaft coupling
The mechanical, electrical machine of device, frequency conversion speed-down；It is formed between the furnace body shell and the furnace body inner casing for being connected with superheated steam branch pipe
Internal air flue, the internal air flue are provided with several stomatas along its length.The motor passes through frequency conversion speed-down machine, shaft coupling
Device is connect with gear-box, and the gear-box exports axis connection, first output shaft and second with the first output shaft, second respectively
Output axis connection is located in the furnace body inner casing, and the two rotates synchronously.It is set on first output shaft, the second output shaft
It is equipped with helical blade structure.
Finally, it should be noted that the above various embodiments is only to illustrate the technical solution of the utility model, rather than it is limited
System；Although the present invention has been described in detail with reference to the aforementioned embodiments, those skilled in the art should
Understand: it is still possible to modify the technical solutions described in the foregoing embodiments, or to some or all of
Technical characteristic is equivalently replaced；And these are modified or replaceed, it does not separate the essence of the corresponding technical solution, and this is practical new
The range of each embodiment technical solution of type.
Claims (9)
1. a kind of carbonized by means of superheated steam furnace continuous discharge cooling conveying device characterized by comprising the first screw conveyor,
Second screw conveyor and third screw conveyor；
First screw conveyor is inclined to set, and the top of the lower end of first screw conveyor is provided with for making
The feed inlet that material enters after carbonized by means of superheated steam, the lower part of the higher-end of first screw conveyor is provided with discharge port；
Second screw conveyor is inclined to set, and first screw conveyor is parallel with first screw conveyor sets
It sets, the top of the lower end of second screw conveyor is provided with feed inlet, the higher-end of second screw conveyor
Lower part is provided with discharge port, and the discharge port of first screw conveyor and the feed inlet of second screw conveyor pass through pass
Blower connection；The third screw conveyor is in horizontally disposed, the third screw conveyor and second screw conveyor
Arranged in a crossed manner, one end top of the third spiral transferring is provided with feed inlet, the feed inlet and the second spiral shell of the third spiral transferring
The discharge port connection of conveyer is revolved, the bottom interval of the third screw conveyor is provided with the first discharge port, the second discharge port
With third discharge port.
2. carbonized by means of superheated steam furnace continuous discharge cooling conveying device according to claim 1, which is characterized in that described
Be provided with the first water(-cooling) jacket between the feed inlet and discharge port of one screw conveyor, the first water(-cooling) jacket coaxial package in
The working cavity of first screw conveyor, the lower end lower part of first water(-cooling) jacket are provided with water inlet, and described
The higher-end top of one water(-cooling) jacket is provided with water outlet.
3. carbonized by means of superheated steam furnace continuous discharge cooling conveying device according to claim 2, which is characterized in that described
One screw conveyor is provided with inspection socket in the two sides of first water(-cooling) jacket.
4. carbonized by means of superheated steam furnace continuous discharge cooling conveying device according to claim 2, which is characterized in that described
The discharge port of one screw conveyor is located at the surface of the feed inlet of second screw conveyor.
5. carbonized by means of superheated steam furnace continuous discharge cooling conveying device according to claim 1, which is characterized in that described
Be provided with the second water(-cooling) jacket between the feed inlet and discharge port of two screw conveyors, the second water(-cooling) jacket coaxial package in
The working cavity of second screw conveyor, the lower end lower part of second water(-cooling) jacket are provided with water inlet, and described
The higher-end top of two water(-cooling) jackets is provided with water outlet.
6. carbonized by means of superheated steam furnace continuous discharge cooling conveying device according to claim 5, which is characterized in that described
Two screw conveyors are provided with inspection socket in the two sides of second water(-cooling) jacket.
7. carbonized by means of superheated steam furnace continuous discharge cooling conveying device according to claim 5, which is characterized in that described
The discharge port of two screw conveyors is located at the surface of the feed inlet of the third screw conveyor.
8. carbonized by means of superheated steam furnace continuous discharge cooling conveying device according to claim 5, which is characterized in that described
A third water(-cooling) jacket, the third helical feed are provided between the first discharge port and the second discharge port of three screw conveyors
A third water(-cooling) jacket is provided between the second discharge port and third discharge port of machine, two third water(-cooling) jackets are same respectively
Axle sleeve is loaded on the working cavity of the third screw conveyor, and one end lower part of the third water(-cooling) jacket is provided with water inlet,
One end other end top of the third water(-cooling) jacket is provided with water outlet.
9. carbonized by means of superheated steam furnace continuous discharge cooling conveying device according to claim 8, which is characterized in that described
One discharge port, second discharge port and the third discharge port are respectively arranged with pneumatic gate valve, and are connected to liquid storage
Case/material storing box/jumbo bag.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201822254899.6U CN209568061U (en) | 2018-12-29 | 2018-12-29 | Carbonized by means of superheated steam furnace continuous discharge cooling conveying device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201822254899.6U CN209568061U (en) | 2018-12-29 | 2018-12-29 | Carbonized by means of superheated steam furnace continuous discharge cooling conveying device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN209568061U true CN209568061U (en) | 2019-11-01 |
Family
ID=68331483
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201822254899.6U Active CN209568061U (en) | 2018-12-29 | 2018-12-29 | Carbonized by means of superheated steam furnace continuous discharge cooling conveying device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN209568061U (en) |
-
2018
- 2018-12-29 CN CN201822254899.6U patent/CN209568061U/en active Active
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN103591780B (en) | The main drying of the continuous drying system of slurry or powder | |
| CN206886940U (en) | Sewage sludge harmlessness handles complete set of equipments | |
| CN209568061U (en) | Carbonized by means of superheated steam furnace continuous discharge cooling conveying device | |
| CN201825832U (en) | Sludge dewatering-drying device system | |
| CN206566738U (en) | A kind of smelting device recycled with waste heat recovery | |
| CN209584110U (en) | The continuous anaerobic carbonization cracking furnace installation of superheated steam | |
| CN205653405U (en) | Superheated steam carbide furnace | |
| CN209584109U (en) | Carbonized by means of superheated steam furnace continuous discharge cools down novel conveying device | |
| CN205893035U (en) | Low heat value mud " three change " processing apparatus | |
| CN205628892U (en) | Continuous anaerobic carbonization organic waste's of superheated steam device | |
| CN209584107U (en) | The continuous anaerobic carbonization pyrolysis furnace new device of superheated steam | |
| CN209568060U (en) | The feeding device of superheated steam anaerobic carbonization cracking | |
| CN2592267Y (en) | Rotary dual-cone filtering, washing drying and pulverizing machine | |
| WO2022247423A1 (en) | Device for continuously treating materials containing volatile components | |
| CN105546975A (en) | Two-section rotating pyrolysis reactor | |
| CN109456779A (en) | The continuous anaerobic carbonization cracking furnace installation of superheated steam and method | |
| CN213049124U (en) | Integrated equipment for harmless treatment of fine chemical waste salt | |
| CN205586603U (en) | Crystallization kettle with belt cleaning device | |
| CN205061853U (en) | Pipe chain serialization mud fatlute carbonization system | |
| CN109456778A (en) | The continuous anaerobic carbonization pyrolysis furnace new device of superheated steam and method | |
| CN209568062U (en) | The continuous anaerobic carbonization running gear of superheated steam | |
| CN209636171U (en) | A kind of microwave-assisted pyrolysis bio-oils device | |
| CN206367863U (en) | A kind of multi-functional pharmacy system of dust-free sterile self-cleaning | |
| CN206566222U (en) | A kind of full closed aseptic intelligent integral pharmacy system | |
| CN205974427U (en) | Gasification furnace |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20231201 Address after: 225400 Hanzhuang Road, Huangqiao Industrial Park, Taixing City, Taizhou City, Jiangsu Province Patentee after: Jiangsu Blue Green Environmental Protection Technology Co.,Ltd. Address before: Hanzhuang Road, Huangqiao Economic Development Zone, Taixing City, Taizhou City, Jiangsu Province, 225411 Patentee before: JIANGSU YIER PLASMA SCIENCE & TECHNOLOGY Co.,Ltd. |