CN205590624U - Micelle reaction schizolysis cauldron - Google Patents
Micelle reaction schizolysis cauldron Download PDFInfo
- Publication number
- CN205590624U CN205590624U CN201620111581.0U CN201620111581U CN205590624U CN 205590624 U CN205590624 U CN 205590624U CN 201620111581 U CN201620111581 U CN 201620111581U CN 205590624 U CN205590624 U CN 205590624U
- Authority
- CN
- China
- Prior art keywords
- cracker
- cylinder
- level
- heating agent
- heat medium
- 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
Abstract
The utility model relates to a micelle reaction schizolysis cauldron, including the cracker of rack -mounted at least one -level series connection, each grade cracker all includes conveyer and heat medium barrel, conveyer one end is equipped with the feed inlet, and the other end is equipped with the discharge gate, and the discharge gate and the feed inlet of second level cracker of first order cracker are connected, and the discharge gate and the feed inlet of next stage cracker of second level cracker are connected, heat medium barrel cover is established at the conveyer outsidely, constitutes sealed cavity between heat medium barrel inner wall and the conveyer outer wall, and heat medium barrel one end is equipped with and seals up the heat medium import of cavity intercommunication, and the other end is equipped with and seals up the heat medium export of cavity intercommunication, the heat medium export of last one -level cracker and the heat medium access connection of penultimate level cracker, the heat medium export of penultimate level cracker and the heat medium access connection of last one -level cracker. The utility model discloses it is rational in infrastructure, play energy saving and emission reduction, reduce cost's effect under the prerequisite that does not change the amount of production.
Description
Technical field
This utility model relates to a kind of micelle cracking treating equipment, specifically a kind of micelle reaction cracking still, belongs to technical field of chemical.
Background technology
Micelle cracking is the important step that junked tire recycles, and the rubber fraction in tire resolves into hydro carbons and charcoal under the high temperature conditions, and the recovered post-treatment of this hydro carbons becomes Petroleum, diesel oil etc. to take out as fuel oil.Current tire or the cracking of tire micelle mostly are batch-type cracking technology, first tire or tire micelle are loaded cracking reactor, then it is airtight, replace with nitrogen, reactor is heated up by external thermal source, cracking is started after reaching uniform temperature (generally 400 DEG C), the oil gas produced is derived by pipeline, become tire pyrolysis oil after cooling, maintain temperature of reactor, until no longer producing oil gas, the now residue such as the most surplus charcoal in reactor, reactor must be lowered the temperature, after displacement, residue is drawn off, then the cracking of next batch of material is started, here it is so-called local method tire pyrolysis.In brief, its every outer batch materials processing procedure the most at least includes feed, heats up, cracks, lowers the temperature, five steps of slag dumping, and its shortcoming is, one, and in cracking and discharge process, oil gas and the residue of race damage can bring environmental pollution；Its two, the treatment effeciency of reactor is relatively low, the 3rd, use naked light directly heat to reactor, this process temperature regulation inconvenience, fluctuation is relatively big, and during temperature higher (typically at about 500 DEG C), this journey that rubber decomposes can produce two English, serious environment pollution.
Summary of the invention
The purpose of this utility model is to overcome the deficiencies in the prior art, it is provided that a kind of micelle reaction cracking still, and it is rational in infrastructure, plays energy-saving and emission-reduction, the effect of reduction cost on the premise of not changing volume of production.
The technical scheme provided according to this utility model: micelle reaction cracking still, it is characterised in that: include that the cracker that rack-mounted at least one-level is connected in series, every one-level cracker all include conveyer and heating agent cylinder；Described conveyer one end is provided with charging aperture, the other end is provided with discharging opening, the charging aperture of first order cracker is used for sending into micelle, the discharging opening of first order cracker is connected with the charging aperture of second level cracker, the discharging opening of second level cracker is connected with the charging aperture of next stage cracker, and the discharging opening of afterbody cracker is for exporting cracked residue；Wherein one-level cracker is provided with oil gas vent, and the oil gas produced in process of production thus exports；Described heating agent barrel jacket is located at outside conveyer, constitute between heating agent cylinder inboard wall and conveyer outer wall and seal chamber, described heating agent cylinder one end is provided with and seals the Heating medium of chamber, the other end is provided with and seals the heating agent outlet of chamber, the Heating medium of afterbody cracker is used for being passed through thermal medium, the heating agent outlet of afterbody cracker is connected with the Heating medium of penultimate stage cracker, the heating agent outlet of penultimate stage cracker is connected with the Heating medium of upper level cracker, the heating agent outlet of first order cracker is for exporting the thermal medium after heat exchange.
As a further improvement on the present invention, described frame is multiple structure, installs one-level cracker for every layer, and Heating medium, heating agent outlet on every grade of cracker lay respectively at the bottom at heating agent cylinder two ends, top.
As further improvement of the utility model, the discharge outlet of described cracker is provided with thermocouple.
As further improvement of the utility model, wherein one-level cracker is provided with venting.
As a further improvement on the present invention, described conveyer uses conveying worm, and it includes that cylinder, rotary shaft, helical blade and motor reducer, described cylinder are fixed in frame, and top, cylinder one end arranges charging aperture, arranges discharging opening bottom the other end；Described rotary shaft is arranged in cylinder, and rotating shaft terminal is stretched out from cylinder two ends and supported by bearing block respectively, and described bearing block is fixed on support, and described support is fixed on cylinder two ends；Being provided with black box between described rotary shaft and cylinder, rotary shaft one end is connected transmission with the output shaft of motor reducer, and rotary shaft is positioned at the part of cylinder and installs helical blade.
As further improvement of the utility model, described black box includes sealing shroud, airtight and watertight padding and gland, described sealing shroud is screwed at barrel end, and airtight and watertight padding is filled out in being located at sealing shroud and compresses with gland, and described gland screw is connected on sealing shroud.
As further improvement of the utility model, driven sprocket is installed in described rotary shaft one end, described motor reducer is arranged on rotary shaft one end side, the output shaft of motor reducer is installed drive sprocket, is connected transmission by chain between described drive sprocket and driven sprocket.
This utility model compared with prior art, has the advantage that
(1), this utility model cracker of using thtee-stage shiplock to connect realize continuously conveying, three grades of cracker multi-tier arrangement, under the length not changing material heat exchange, shorten the entire length of equipment, reduce manufacture difficulty and the cost of manufacture of equipment.
(2), this utility model select the less conveying worm of diameter to carry out material conveying, reduce the hollow space in conveying worm, decrease heat losses, less owing to running material, can the most fully crack with cylinder heat exchanging process, significantly carry minimizing pyrolysis time, improve productivity.
(3), this utility model plays energy-saving and emission-reduction on the premise of not changing volume of production, reduces the effect of cost.
Accompanying drawing explanation
Fig. 1 is the structural front view of this utility model embodiment.
Fig. 2 is the left view of Fig. 1.
Fig. 3 is the top view of Fig. 1.
Detailed description of the invention
Below in conjunction with concrete drawings and Examples, the utility model is described in further detail.
As shown in the figure: the cracker that the micelle reaction cracking still in embodiment is mainly connected by the thtee-stage shiplock being arranged in frame 1 forms.
As shown in Fig. 1 ~ Fig. 3, in this utility model embodiment, described frame 1 is three-decker, installs one-level cracker for every layer；Every one-level cracker all includes conveyer 2 and heating agent cylinder 3；Described conveyer 2 one end is provided with charging aperture a, the other end is provided with discharging opening b, the charging aperture a of first order cracker is used for sending into micelle, the discharging opening b of first order cracker is connected with the charging aperture a of second level cracker, the discharging opening b of second level cracker is connected with the charging aperture a of third level cracker, and the discharging opening b of third level cracker is for exporting cracked residue；Second level cracker is provided with oil gas vent f, and the oil gas produced in process of production thus exports；It is outside that described heating agent cylinder 3 is set in conveyer 2, constitute between heating agent cylinder 3 inwall and conveyer 2 outer wall and seal chamber, described heating agent cylinder 3 one end is provided with and seals the Heating medium c of chamber, the other end is provided with and seals the heating agent outlet d of chamber, the Heating medium c of third level cracker is used for being passed through thermal medium, the heating agent outlet d of third level cracker is connected with the Heating medium c of second level cracker, the heating agent outlet d of second level cracker is connected with the Heating medium c of first order cracker, the heating agent outlet d of first order cracker is for exporting the thermal medium after heat exchange.
As shown in Fig. 1 ~ Fig. 3, in this utility model embodiment, owing to three grades of crackers are divided into three layers of layout, in order to preferably mate this arrangement, Heating medium c, heating agent outlet d on every grade of cracker lay respectively at the bottom at heating agent cylinder 3 two ends, top.
As shown in Fig. 1 ~ Fig. 3, in this utility model embodiment, thermocouple 4 is installed at the discharging opening b of described cracker, so can detect whether the cracking temperature of each section in production process meets Production requirement in real time, it is simple to control state of the art.
As shown in Fig. 1 ~ Fig. 3; in this utility model embodiment; third level cracker 2 is provided with venting e, described venting e and can solve the problem that equipment damages, in maloperation, equipment instrument, the danger do not changed for a long time or occur under extreme case, plays the safety measure of protection equipment and personnel.
As shown in Fig. 1 ~ Fig. 3, in this utility model embodiment, 2 use conveying worm 2, it is mainly made up of cylinder 2.1, rotary shaft 2.2, helical blade 2.3 and motor reducer 2.4, described cylinder 2.1 is fixed in frame 1, top, cylinder 2.1 one end arranges charging aperture a, arranges discharging opening b bottom the other end；Described rotary shaft 2.2 is arranged in cylinder 2.1, and rotary shaft 2.2 two ends are stretched out from cylinder 2.1 two ends and supported by bearing block 2.5 respectively, and described bearing block 2.5 is fixed on support 2.6, and described support 2.6 is fixed on cylinder 2.1 two ends；It is provided with black box between described rotary shaft 2.2 and cylinder 2.1, described black box is mainly made up of sealing shroud 2.7, airtight and watertight padding 2.8 and gland 2.9, described sealing shroud 2.7 is screwed in cylinder 2.1 end, airtight and watertight padding 2.8 is filled out in being located at sealing shroud 2.7 and compresses with gland 2.9, and described gland 2.9 screw is connected on sealing shroud 2.7；Driven sprocket 2.10 is installed in described rotary shaft 2.2 one end, described motor reducer 2.4 is arranged on rotary shaft 2.2 one end side, drive sprocket 2.11 is installed on the output shaft of motor reducer 2.4, being connected transmission by chain 2.12 between described drive sprocket 2.11 and driven sprocket 2.10, rotary shaft 2.2 is positioned at the part of cylinder 2.1 and installs helical blade 2.3.
Operation principle of the present utility model and work process are as follows:
The material needing cracking adds from charging aperture a, and motor reducer 2.4, by driving conveying worm 2 to operate, carries material；Heating agent enters from adding Heating medium c, and the sealing chamber thermotropism matchmaker between heating agent cylinder 3 and conveyer 2 exports d flowing, and the material in helical feed is heated in flow process by heating agent, provides heat to the cracking of material.Suitable pyrolysis time is regulated by controlling the rotating speed of conveying worm 2.
Claims (7)
1. micelle reaction cracking still, it is characterised in that: include that the cracker that at least one-level being arranged in frame (1) is connected in series, every one-level cracker all include conveyer (2) and heating agent cylinder (3)；Described conveyer (2) one end is provided with charging aperture (a), the other end is provided with discharging opening (b), the charging aperture (a) of first order cracker is used for sending into micelle, the discharging opening (b) of first order cracker is connected with the charging aperture (a) of second level cracker, the discharging opening (b) of second level cracker is connected with the charging aperture (a) of next stage cracker, and the discharging opening (b) of afterbody cracker is for exporting cracked residue；Wherein one-level cracker is provided with oil gas vent (f), and the oil gas produced in process of production thus exports；It is outside that described heating agent cylinder (3) is set in conveyer (2), constitute between heating agent cylinder (3) inwall and conveyer (2) outer wall and seal chamber, described heating agent cylinder (3) one end is provided with and seals the Heating medium (c) of chamber, the other end is provided with and seals heating agent outlet (d) of chamber, the Heating medium (c) of afterbody cracker is used for being passed through thermal medium, heating agent outlet (d) of afterbody cracker is connected with the Heating medium (c) of penultimate stage cracker, heating agent outlet (d) of penultimate stage cracker is connected with the Heating medium (c) of upper level cracker, heating agent outlet (d) of first order cracker is for exporting the thermal medium after heat exchange.
2. micelle reaction cracking still as claimed in claim 1, it is characterized in that: described frame (1) is multiple structure, installing one-level cracker for every layer, Heating medium (c), heating agent outlet (d) on every grade of cracker lay respectively at the bottom at heating agent cylinder (3) two ends, top.
3. micelle reaction cracking still as claimed in claim 1, it is characterised in that: discharging opening (b) place of described cracker is provided with thermocouple (4).
4. micelle reaction cracking still as claimed in claim 1, it is characterised in that: wherein one-level cracker is provided with venting (e).
5. micelle reaction cracking still as claimed in claim 1, it is characterized in that: described conveyer (2) uses conveying worm (2), it includes cylinder (2.1), rotary shaft (2.2), helical blade (2.3) and motor reducer (2.4), described cylinder (2.1) is fixed in frame (1), cylinder (2.1) top, one end arranges charging aperture (a), arranges discharging opening (b) bottom the other end；Described rotary shaft (2.2) is arranged in cylinder (2.1), rotary shaft (2.2) two ends are stretched out from cylinder (2.1) two ends and are supported by bearing block (2.5) respectively, described bearing block (2.5) is fixed on support (2.6), and described support (2.6) is fixed on cylinder (2.1) two ends；Being provided with black box between described rotary shaft (2.2) and cylinder (2.1), rotary shaft (2.2) one end is connected transmission with the output shaft of motor reducer (2.4), and rotary shaft (2.2) is positioned at the part of cylinder (2.1) and installs helical blade (2.3).
6. micelle reaction cracking still as claimed in claim 5, it is characterized in that: described black box includes sealing shroud (2.7), airtight and watertight padding (2.8) and gland (2.9), described sealing shroud (2.7) is screwed in cylinder (2.1) end, airtight and watertight padding (2.8) is filled out in being located at sealing shroud (2.7) and compresses with gland (2.9), and described gland (2.9) screw is connected on sealing shroud (2.7).
7. micelle reaction cracking still as claimed in claim 5, it is characterized in that: driven sprocket (2.10) is installed in described rotary shaft (2.2) one end, described motor reducer (2.4) is arranged on rotary shaft (2.2) one end side, drive sprocket (2.11) is installed on the output shaft of motor reducer (2.4), between described drive sprocket (2.11) with driven sprocket (2.10), is connected transmission by chain (2.12).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620111581.0U CN205590624U (en) | 2016-02-02 | 2016-02-02 | Micelle reaction schizolysis cauldron |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620111581.0U CN205590624U (en) | 2016-02-02 | 2016-02-02 | Micelle reaction schizolysis cauldron |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205590624U true CN205590624U (en) | 2016-09-21 |
Family
ID=56927511
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620111581.0U Active CN205590624U (en) | 2016-02-02 | 2016-02-02 | Micelle reaction schizolysis cauldron |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205590624U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105542831A (en) * | 2016-02-02 | 2016-05-04 | 无锡市泰新环保科技有限公司 | Colloidal particle reaction pyrolysis kettle |
| CN109019990A (en) * | 2018-09-21 | 2018-12-18 | 深圳市齐欣实业有限公司 | A kind of oil storage tank base oil sludge Recovery Purifying treatment process device |
-
2016
- 2016-02-02 CN CN201620111581.0U patent/CN205590624U/en active Active
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105542831A (en) * | 2016-02-02 | 2016-05-04 | 无锡市泰新环保科技有限公司 | Colloidal particle reaction pyrolysis kettle |
| CN109019990A (en) * | 2018-09-21 | 2018-12-18 | 深圳市齐欣实业有限公司 | A kind of oil storage tank base oil sludge Recovery Purifying treatment process device |
| CN109019990B (en) * | 2018-09-21 | 2021-07-20 | 深圳市齐欣实业有限公司 | Oil storage tank bottom oil sludge purification and recovery treatment process device |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN108018062A (en) | Waste rubber cracking method and system | |
| CN201665655U (en) | Novel horizontal external-heat type rotary carbonization carbocoal furnace | |
| CN104357077B (en) | For the horizontal screw structure pyrolysis furnace of damaged tire resource recoveryization | |
| CN201665533U (en) | External-heating charing converter used for activated carbon producing process | |
| CN205590624U (en) | Micelle reaction schizolysis cauldron | |
| CN110938451A (en) | Waste tire cracking carbonization cooling system | |
| CN107829078A (en) | A kind of improved gaseous phase deposition stove | |
| CN102432914B (en) | Method and equipment for decomposing and recovering glass fiber reinforced plastics | |
| CN104194809A (en) | Continuous microwave-heating cracking equipment for biomass and organic wastes | |
| CN104477885A (en) | Vertical continuous induction type high-temperature graphitization furnace | |
| CN204779473U (en) | Prevent pyrolysis of coal of dust and carry matter rotary furnace | |
| CN205590623U (en) | Micelle is sealed schizolysis system in succession | |
| CN211570562U (en) | Sectional type continuous thermal cracking device for waste plastics | |
| CN105542831A (en) | Colloidal particle reaction pyrolysis kettle | |
| CN113213449A (en) | Continuous reaction treatment method for graphite cathode material/phosphate and ternary anode material of lithium ion battery | |
| CN110846063B (en) | High-efficient processing system of junked tire micelle | |
| CN112760117A (en) | Waste rubber and plastic high-efficiency pyrolysis device with heat transfer enhanced coupling grinding function | |
| CN203282687U (en) | Oil heat type heating device used for injection molding machine | |
| CN204529316U (en) | Two section type graphitizing furnace equipment | |
| CN204039329U (en) | A kind of continuous-type microwave heating biological matter and organic waste cracking apparatus | |
| CN108998066B (en) | Low-temperature cracking furnace | |
| CN204752613U (en) | Pyrolysis coal cooling discharging device | |
| CN211339392U (en) | Waste tire cracking carbonization cooling system | |
| CN210906116U (en) | Hindered phenol antioxidant continuous ester exchange reaction production device | |
| CN104560077B (en) | Infrared radiation biomass thermochemical converter unit |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20211103 Address after: 210000 No. 19, Suyuan Avenue, Jiangning District, Nanjing, Jiangsu Province Patentee after: Everbright green environmental protection technology service (Jiangsu) Co.,Ltd. Address before: 214196 No. 236, Dongsheng Road, Donggang Town, Xishan District, Wuxi City, Jiangsu Province Patentee before: WUXI TAIXIN ENVIRONMENTAL PROTECTION TECHNOLOGY Co.,Ltd. |