CN208151286U - A kind of condensate recycling device for plastic fuel oil - Google Patents
A kind of condensate recycling device for plastic fuel oil Download PDFInfo
- Publication number
- CN208151286U CN208151286U CN201820617754.5U CN201820617754U CN208151286U CN 208151286 U CN208151286 U CN 208151286U CN 201820617754 U CN201820617754 U CN 201820617754U CN 208151286 U CN208151286 U CN 208151286U
- Authority
- CN
- China
- Prior art keywords
- hydrogen chloride
- water
- recycling device
- condensate recycling
- condensation
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
Landscapes
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Abstract
The utility model discloses a kind of condensate recycling devices for plastic fuel oil, it belongs to condensate recycling device technical field, including air inlet pipe, the air inlet pipe is connected with hydrogen chloride filter assemblies, the hydrogen chloride filter assemblies are connected with condensation, the condensation is connected separately with air accumulator and water-oil separating component, and the water-oil separating component is connected with oil storage tank；The utility model can first be removed the hydrogen chloride in gaseous mixture by hydrogen chloride filter assemblies, avoid hydrogen chloride from causing to corrode to pipeline and subsequent condensate recycling device, to greatly extend the service life of the utility model.
Description
Technical field
The utility model relates to condensate recycling device technical fields, and in particular to a kind of being condensed back to for plastic fuel oil
Receiving apparatus.
Background technique
Currently, the processing of waste plastics mainly has three ways, such as landfill, power generation by waste combustion and recycles, wherein fill and burn
It burns power generation both of which and is easy to produce secondary pollution, gradually start to eliminate, recycling is increasingly becoming Treatment of Waste Plastics
Mainstream, the mode of recycling mainly include two kinds：One, after to waste plastics recovery and granulation, then various utensil articles are made etc.；
Two, waste plastics catalytic pyrolysis is made to the fuel oil products of high added value, this kind of mode has higher economic benefit, extensively
It is applied in ubiquitous research and production.
It is by the main flow that the fuel oil products of high added value are made in waste plastics catalytic pyrolysis：One, waste plastics is crushed
At certain size, it is sent into after dry by hopper and melts in oil refining furnace and slowly decompose, generate gaseous mixture, the gaseous mixture
Mainly include water, hydrogen chloride, fuel gas oil and incoagulable gas (incoagulable gas at this refer to condensation point lower than fuel oil and
The mixed gas of the condensation point of water).Gaseous mixture is usually first passed into cold by traditional method by gaseous mixture purification
It condenses in condenser, so that water and gaseous state fuel oil form condensate liquid, is then separated the moisture in condensate liquid by water-oil separating
Out；Uncooled gaseous mixture is removed hydrogen chloride by absorption tower, and remaining incoagulable gas can be used as a kind of gas
Fluid fuel recycles.But since hydrogen chloride is a kind of gas with strong corrosive, according to the method described above, hydrogen chloride meeting
Existing condensate recycling device is caused to corrode, greatly reduces the service life of condensate recycling device.
Utility model content
For the problems of in the prior art, a kind of being condensed back to for plastic fuel oil provided by the utility model
Receiving apparatus can remove the hydrogen chloride in gaseous mixture at the first time, reduce corrosion of the hydrogen chloride to condensate recycling device,
Extend the service life of condensate recycling device.
To achieve the goals above, the technical solution adopted in the utility model is as follows：
A kind of condensate recycling device for plastic fuel oil, including air inlet pipe, the air inlet pipe are connected with hydrogen chloride mistake
Component is filtered, the hydrogen chloride filter assemblies are connected with condensation, and the condensation is connected separately with air accumulator and grease point
From component, the water-oil separating component is connected with oil storage tank.
As a kind of perferred technical scheme, the hydrogen chloride filter assemblies are set as the tube body filled with metal oxide,
Electric heating piece is enclosed with outside the tube body.
As a kind of perferred technical scheme, the condensation include spiral pipe and be set to the spiral pipe
External cooling cylinder.
As a kind of perferred technical scheme, the air accumulator and the water-oil separating component with the spiral pipe
Bottom connection.
As a kind of perferred technical scheme, the water-oil separating component is set as compressed air oil water separator.
As a kind of perferred technical scheme, between the air inlet pipe and the hydrogen chloride filter assemblies, the hydrogen chloride
Between filter assemblies and the condensation, the condensation respectively with the air accumulator and the water-oil separating component and
Anti-corrosion pipe is equipped between the water-oil separating component and the oil storage tank to connect.
The beneficial effects of the utility model are shown：
The utility model can first be removed the hydrogen chloride in gaseous mixture by hydrogen chloride filter assemblies, avoid chlorine
Change hydrogen pipeline and subsequent condensate recycling device are caused to corrode, to greatly extend the service life of the utility model.
Detailed description of the invention
Fig. 1 is a kind of overall structure diagram of the condensate recycling device for plastic fuel oil of the utility model；
In figure：1- air inlet pipe, 2- electric heating piece, 3- tube body, 4- cooling cylinder, 5- spiral pipe, 6- air accumulator, 7- grease point
From component, 8- oil storage tank.
Specific embodiment
In order to facilitate the understanding of those skilled in the art, the utility model will be further described below with reference to the accompanying drawings.
As shown in Figure 1, the utility model includes air inlet pipe 1, air inlet pipe 1 is connected with hydrogen chloride filter assemblies, gaseous state mixing
Object is flowed by air inlet pipe 1, and hydrogen chloride filter assemblies are used to remove the hydrogen chloride in gaseous mixture；Hydrogen chloride filter assemblies connect
Be connected to condensation, condensation can by gaseous mixture water and gaseous state fuel oil condense；Condensation is separately connected
There are air accumulator 6 and water-oil separating component 7, remaining incoagulable gas is flowed into air accumulator 6 in gaseous mixture, water-oil separating
Component 7 separates the water of liquid and fuel oil；Water-oil separating component 7 is connected with oil storage tank 8, and oil storage tank 8 is for storing fuel oil.
Wherein, hydrogen chloride filter assemblies are set as the tube body 3 filled with metal oxide, are enclosed with electric heating piece outside tube body 3
2, metal oxide can be one or more of calcium oxide, zinc oxide, magnesia or copper oxide, electric heating piece 2 for pair
Tube body 3 is heated, and the temperature in tube body 3 is made to be in (generally 350 DEG C of suitable temperature of metal oxide and hcl reaction
Left and right)；Condensation includes spiral pipe 5 and the cooling cylinder 4 outside spiral pipe 5, spiral pipe 5 be set as to
Under it is inclined, flowed down convenient for the water and fuel oil of condensation, cooling cylinder 4 can be set to water circulating condensing or using semiconductor refrigerating
The cold end of piece is condensed；Air accumulator 6 and water-oil separating component 7 are connect with the bottom of spiral pipe 5, the water of condensation and combustion
Material oil can be fed directly in water-oil separating component 7, and remaining incoagulable gas can enter in escape pipe；Air inlet pipe 1
Between hydrogen chloride filter assemblies, between hydrogen chloride filter assemblies and condensation, condensation respectively with air accumulator 6 and grease
It is equipped with anti-corrosion pipe between separation assembly 7 and water-oil separating component 7 and oil storage tank 8 to connect, can be further improved
The service life of the utility model.
Above content is only the structure example and explanation to the utility model, the technologies of affiliated the art
Personnel make various modifications or additions to the described embodiments or are substituted in a similar manner, without departing from
The structure of utility model or beyond the scope defined by this claim, all should belong to the protection range of the utility model.
Claims (6)
1. a kind of condensate recycling device for plastic fuel oil, characterized in that including air inlet pipe, the air inlet pipe is connected with chlorine
Change hydrogen filter assemblies, the hydrogen chloride filter assemblies are connected with condensation, the condensation be connected separately with air accumulator and
Water-oil separating component, the water-oil separating component are connected with oil storage tank.
2. a kind of condensate recycling device for plastic fuel oil according to claim 1, characterized in that the hydrogen chloride
Filter assemblies are set as the tube body filled with metal oxide, are enclosed with electric heating piece outside the tube body.
3. a kind of condensate recycling device for plastic fuel oil according to claim 1, characterized in that the condensation group
Part includes spiral pipe and the cooling cylinder outside the spiral pipe.
4. a kind of condensate recycling device for plastic fuel oil according to claim 3, characterized in that the air accumulator
It is connect with the bottom of the spiral pipe with the water-oil separating component.
5. a kind of condensate recycling device for plastic fuel oil according to claim 1, characterized in that the grease point
Compressed air oil water separator is set as from component.
6. a kind of condensate recycling device for plastic fuel oil according to claim 1, characterized in that the air inlet pipe
Between the hydrogen chloride filter assemblies, between the hydrogen chloride filter assemblies and the condensation, the condensation point
It is not equipped between the air accumulator and the water-oil separating component and the water-oil separating component and the oil storage tank anti-
Corrosion pipeline is to connect.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820617754.5U CN208151286U (en) | 2018-04-27 | 2018-04-27 | A kind of condensate recycling device for plastic fuel oil |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820617754.5U CN208151286U (en) | 2018-04-27 | 2018-04-27 | A kind of condensate recycling device for plastic fuel oil |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN208151286U true CN208151286U (en) | 2018-11-27 |
Family
ID=64376739
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201820617754.5U Expired - Fee Related CN208151286U (en) | 2018-04-27 | 2018-04-27 | A kind of condensate recycling device for plastic fuel oil |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN208151286U (en) |
-
2018
- 2018-04-27 CN CN201820617754.5U patent/CN208151286U/en not_active Expired - Fee Related
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN106281396B (en) | Waste plastic cracking equipment and method | |
| CN103611377A (en) | Gas purification pretreatment method and device | |
| US20160216033A1 (en) | Method For Recycling Residual Heat and Dust In Flue Gas During Reclaimed Copper Refining | |
| CN105366751A (en) | Energy-saving environment-friendly integrated recycling and utilization method of coal chemical gasification washing black water high-temperature flashing steam | |
| CN103333705B (en) | Zero-heat carrier powdered coal low-temperature dry distillation carbonization method | |
| CN204400885U (en) | The purification and recover equipment of solvent dimethyl sulfoxide (DMSO) in a kind of carbon fiber production process | |
| CN102602960B (en) | Method for stilling ammonia by aid of waste heat of flue gas of coke oven and equipment | |
| CN107057744B (en) | It slags tap after a kind of continuity auger the equipment and technique of formula environmental protection oil refining | |
| CN110330988A (en) | A kind of wholegrain diameter coal cracking sub-prime utilizes production technology | |
| CN102091527A (en) | Method and device for absorbing waste chlorine generated in lithium production process by utilizing iron powder | |
| CN210320092U (en) | Tail gas treatment system in carbon disulfide production | |
| CN208151286U (en) | A kind of condensate recycling device for plastic fuel oil | |
| CN101913669A (en) | Multi-effect energy-saving ammonia recovery process and device | |
| CN104560151A (en) | Method for refining gasoline and diesel from waste lubricating oil | |
| CN102491285A (en) | Waste sulphuric acid concentrating and recycling equipment | |
| CN209368197U (en) | A kind of coking process crude benzol section utilization system | |
| CN212246924U (en) | Comprehensive utilization system for waste heat of raw coke oven gas | |
| CN202400846U (en) | Waste sulfuric acid concentrating and recovering plant | |
| CN114807464A (en) | Flash evaporation cooling heat recovery system for slag flushing water | |
| CN114014274A (en) | Sulfur paste reduced-pressure vaporization sulfur extraction device and process thereof | |
| CN212025417U (en) | Environment-friendly and energy-saving rare earth concentrate sectional roasting system | |
| CN210595933U (en) | Novel coal tar pitch preparation system | |
| CN106744720A (en) | The circulation recycling system and its operation process of trichloroacetaldehyde by-product dilute sulfuric acid | |
| CN109911871B (en) | Temperature-changing phase-changing separation method and system for elemental phosphorus in phosphorus-containing tail gas | |
| CN108854456B (en) | System and method for recycling heat energy of desorption tower |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| 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: 20181127 Termination date: 20210427 |