CN205856389U - A kind of organic waste cracking oil, gas purification recovery device - Google Patents
A kind of organic waste cracking oil, gas purification recovery device Download PDFInfo
- Publication number
- CN205856389U CN205856389U CN201620842734.9U CN201620842734U CN205856389U CN 205856389 U CN205856389 U CN 205856389U CN 201620842734 U CN201620842734 U CN 201620842734U CN 205856389 U CN205856389 U CN 205856389U
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- Prior art keywords
- cooling
- purifying
- gas
- oil
- separator
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Abstract
The utility model discloses a kind of organic waste cracking oil, gas purification recovery device, including multistage cooling and purifying separator, gas phase decompression mozzle and liquid phase mozzle it is provided with between cooling and purifying separators at different levels, being provided with water in cooling and purifying separators at different levels, cooling and purifying separator bottom at different levels are provided with wax oil outlet;One-level cooling and purifying separator top is provided with gas phase mozzle, and gas phase mozzle gos deep under one-level cooling and purifying separator liquid level, and one-level cooling and purifying separator lower end is provided with fluid infusion mouth;Final stage cooling and purifying separator upper end is provided with fixed gas outlet and fuel oil exports, and bottom is provided with sewage draining exit.This utility model has advantage highlighted below: with liquid water for refrigerated separation medium, quickly institute's waxy oil, fuel oil, fixed gas in oil gas is separated;Gas phase decompression mozzle makes system keep the safety in production at ambient pressure, solves building the pressure and vapour lock problem in liquid phase conduction pipe in cooling and purifying separator cavity at different levels.
Description
Technical field
This utility model relates to a kind of organic waste cracking oil, gas purification recovery device, makes height the most at ambient pressure
Institute's waxy oil, fuel oil, fixed gas sharp separation and collection in temperature oil gas.
Background technology
Organic solid waste thing makes polyolefin in organic waste big by high-temperature heating in the pyrolysis furnace of normobaric hypoxia state
Molecule chain rupture, cracking is small-molecule substance and separates out, and after entering this system with gaseous state, major part is converted into liquid condition,
I.e. cracked oil, and the gas that can not liquefy is fixed gas.For a long time, the cracked oil of debirs, the highly effective and safe of gas are collected
Always perplex a great problem of debirs treatment industry.People generally use following methods, one of which method: waste and old take turns
The cracking process such as tire, rubber, plastics have the cutin that cracks the most completely and produce bubble, after bubbles burst uncracked cutin with
Gas is pulled away, and after using simple separating treatment, is directly sent to oil gas in cooler cool down, due to dust and uncracked
Cutin glues wall, causes oil collection efficiency low, causes cooler to be frequently occluded, it is impossible to continues to produce.Another kind of method: oil gas is led to
Enter airtight multiple-stage separator, under oil cooling while, produce substantial amounts of high temperature oil water vapour, form pressure in separator
Raise, in liquid phase conduction pipe, often with the presence of vapour lock, although oil collection efficiency is high, but potential safety hazard is big.
Summary of the invention
For perplexing the predicament that organic solid waste thing cracking industry oil is collected for a long time, this utility model provides one to have
Effect solves the high vapour lock problem with liquid phase diversion pipeline of pressure in cooling and purifying separator, and the most efficient but also safe and environment-friendly is organic
Garbage cracked oil, gas purification recovery device.
The purpose of this utility model is achieved in that
A kind of organic waste cracking oil, gas purification recovery device, including multistage cooling and purifying separator, coolings at different levels are clean
It is provided with gas phase decompression mozzle and liquid phase mozzle between separator, in cooling and purifying separators at different levels, is provided with water, Ge Jileng
But wax oil outlet it is provided with bottom decontaminating separator;One-level cooling and purifying separator top is provided with gas phase mozzle, gas phase mozzle
Going deep under one-level cooling and purifying separator liquid level, one-level cooling and purifying separator lower end is provided with fluid infusion mouth;Final stage cooling and purifying
Separator upper end is provided with fixed gas outlet and fuel oil exports, and bottom is provided with sewage draining exit.
It is equipped with tube type liquid level gage on cooling and purifying separators at different levels.
Gas bag is connected at gas phase mozzle air inlet.
Fixed gas outlet connects pyrolysis furnace and strile-backs device, and fixed gas outlet and pyrolysis furnace strile-back and be provided with water seal between device
Tank.
Gas phase draft-tube diameter is 250-400mm, is shaped as the bend pipe of one end band elbow, and elbow is 90 °, and elbow port is certainly
Cooling and purifying separator top is inserted in water, and the level that submerges is 200mm.
Gas phase decompression draft-tube diameter be 150-200mm, be shaped as the bend pipe of two ends band elbow, elbow be all 90 ° or
135 °, bend pipe passes from upper level cooling and purifying separator top, inserts water from next stage cooling and purifying separator top, does not has
Entering level is 200mm.
All having two liquid phase mozzles on middle cooling and purifying separators at different levels, the nozzle position of two liquid phase mozzles is cold
But contour plane and mutually perpendicular radial position on decontaminating separator.
Liquid phase draft-tube diameter is 100-150mm, inserts in water, and the level that submerges is 200mm.
Middle cooling and purifying separator intracavity at different levels arrange the oil baffle of one piece of thickness 6-10mm.
Compared with prior art, this utility model has an advantage highlighted below:
1) with liquid water for refrigerated separation medium, quickly institute's waxy oil, fuel oil, fixed gas in oil gas are separated.
2) gas phase decompression mozzle makes system keep the safety in production at ambient pressure, solves in cooling and purifying separator cavity at different levels
Build the pressure and liquid phase conduction pipe in vapour lock problem.
3) system is divided into three independent parts by the water in one-level multifunctional separator and the water in water sealed tank, is respectively solely
Vertical process system, makes system safer.
Accompanying drawing explanation
Fig. 1 is this utility model structural representation.
1 cracking oil gas, 2 gas bags, 3 gas phase mozzles, 4 one-level cooling and purifying separators, 41 water, 42 mend
Liquid mouth, 43 wax oil outlets, 44 tube type liquid level gage, 5 gas phase decompression mozzles, 6 liquid phase mozzles, 7 two grades of coolings
Decontaminating separator, 71 oil baffles, 72 discharge outlet, 8 fuel oil service tanks, 9 three grades of cooling and purifying separators, 91 do not coagulate
Gas exports, 92 fuel oil outlets, 93 sewage draining exits, 10 wax oil storage tanks, 11 fixed gases, 12 water sealed tanks, 13 cracking
Stove burner.
Detailed description of the invention
As it is shown in figure 1, a kind of organic waste cracking oil, gas purification recovery device, including three grades of cooling and purifying separators,
It is provided with gas phase decompression mozzle 5 and liquid phase mozzle 6 between cooling and purifying separators at different levels, sets in cooling and purifying separators at different levels
Water 41, cooling and purifying separator bottom at different levels is had to be provided with wax oil outlet 43;One-level cooling and purifying separator top is provided with gas phase and leads
Flow tube 3, gas phase mozzle 3 gos deep under one-level cooling and purifying separator liquid level 4, and one-level cooling and purifying separator lower end is provided with benefit
Liquid mouth 42;Three grades of cooling and purifying separator 9 upper ends are provided with fixed gas outlet 91 and fuel oil outlet 92, and bottom is provided with sewage draining exit
93。
It is equipped with tube type liquid level gage 44 on cooling and purifying separators at different levels.
Connecting gas bag 2 at gas phase mozzle 3 air inlet, cracking oil gas 1 is first collected to gas bag 2, then through gas phase mozzle 3
Enter one-level cooling and purifying separator 4.
Fixed gas outlet 91 connection pyrolysis furnaces strile-back device 13, and fixed gas outlet 91 and pyrolysis furnace strile-back and set between device 13
Having water sealed tank 12, fixed gas 11, from fixed gas outlet 91 outflow, enters pyrolysis furnace after water sealed tank 12 water seal and strile-backs device 13.
The a diameter of 250-400mm of gas phase mozzle 3, is shaped as the bend pipe of one end band elbow, and elbow is 90 °, elbow port
Inserting in water from cooling decontaminating separator top, the level that submerges is 200mm.
Gas phase decompression a diameter of 150-200mm of mozzle 5, be shaped as the bend pipe of two ends band elbow, elbow be all 90 ° or
135 °, bend pipe passes from upper level cooling and purifying separator top, inserts water from next stage cooling and purifying separator top, does not has
Entering level is 200mm.
All having two liquid phase mozzles on middle cooling and purifying separators at different levels, the nozzle position of two liquid phase mozzles is cold
But contour plane and mutually perpendicular radial position on decontaminating separator, liquid phase draft-tube diameter is 100-150mm, inserts in water,
The level that submerges is 200mm.
Two grades of cooling and purifying separator intracavity arrange the oil baffle 71 of one piece of thickness 6-10mm.
Work process:
Organic solid waste thing, in the pyrolysis furnace of normobaric hypoxia state, makes polyolefin in organic waste big by high-temperature heating
Molecule chain rupture, cracking is small-molecule substance and separates out, and cracking oil gas 1 enters gas bag 2, enters this organic waste through gas phase mozzle 3
Gurry cracked oil, gas purification recovery device.
Preset a certain amount of water 41 in one-level cooling and purifying separator 4, is used for making Pintsch process oil gas 1 lower the temperature and making wax
Oil, fuel oil and fixed gas 11 separate, and substantial amounts of cracking oil gas 1 is entered one-level cooling and purifying separator by gas phase mozzle 3
In water 41, after water 41 refrigerated separation, on fuel oil climbs up on top of the water, enter two grades of cooling and purifyings through liquid phase mozzle 6 and separate
In device 7, the wax oil containing a small amount of impurity sinks under water, and through wax oil outlet 43 entrance wax oil storage tank 10, high-temperature oil gas passes through water
The profit steam of middle generation and original fixed gas 11, enter two grades of cooling and purifying separators 7 through gas phase decompression mozzle 5, this
Sample, the water in one-level cooling and purifying separator needs periodically, supplements from the fluid infusion mouth 42 of one-level cooling and purifying separator lower end in time;
It is respectively provided with a tube type liquid level gage 44 in cooling and purifying separator liquid level regions at different levels, can facilitate and clearly observe cooling only
Liquid level change in separator, timely fluid infusion.
Two grades of cooling and purifying separators 7 by its interior oil baffle 71, aqueous by from one-level cooling and purifying separator 4
Oil separates, and purer fuel oil enters three grades of cooling and purifying separators 9 through liquid phase mozzle, and a small amount of wax oil goes out through wax oil
Mouth enters wax oil storage tank 10, and remaining a small amount of aqueous fixed gas enters three grades of cooling and purifying separators 9 through gas phase decompression mozzle,
By the profit steam of gas phase decompression mozzle 5, cooled down further in two grades of cooling and purifying separators 7, so, two grades
Water in cooling and purifying separator can be cumulative, arranges a discharge outlet 72 at the middle part of two grades of cooling and purifying separators 7, periodically
Get rid of the water got off that is cooled.
After fuel oil from two grades of cooling and purifying separators 7 is settled by three grades of cooling and purifying separators 9, go out through fuel oil
Mouth 92 enters fuel oil service tanks 8, is then delivered to oil storage system;The impurity and the water that settle down are discharged through sewage draining exit 94, and system is not
The fixed gas 15 of cooling can enter water sealed tank 12 through fixed gas outlet 91, the pyrolysis furnace that arrives safe and sound after crossing water sealed tank 12 strile-backs device
13 strile-back safely, and water sealed tank 12 is provided with Pressure gauge and evacuation port.
In order to make fixed gas cool down further, a condenser can be set between fixed gas outlet 91 and water sealed tank 12.
Above-described is only preferred implementation of the present utility model, it is noted that for those skilled in the art
For, without departing under this utility model general idea premise, it is also possible to making some changes and improvements, these also should be considered as
Protection domain of the present utility model.
Claims (9)
1. an organic waste cracking oil, gas purification recovery device, it is characterised in that: include multistage cooling and purifying separator,
It is provided with gas phase decompression mozzle and liquid phase mozzle between cooling and purifying separators at different levels, is provided with in cooling and purifying separators at different levels
Water, cooling and purifying separator bottom at different levels are provided with wax oil outlet;One-level cooling and purifying separator top is provided with gas phase mozzle, gas
Phase mozzle gos deep under one-level cooling and purifying separator liquid level, and one-level cooling and purifying separator lower end is provided with fluid infusion mouth;Final stage
Cooling and purifying separator upper end is provided with fixed gas outlet and fuel oil exports, and bottom is provided with sewage draining exit.
A kind of organic waste cracking oil, gas purification recovery device, it is characterised in that: Ge Jileng
But it is equipped with tube type liquid level gage on decontaminating separator.
A kind of organic waste cracking oil, gas purification recovery device, it is characterised in that: gas phase is led
Gas bag is connected at flow tube air inlet.
A kind of organic waste cracking oil, gas purification recovery device, it is characterised in that: fixed gas
Outlet connects pyrolysis furnace and strile-backs device, and fixed gas outlet and pyrolysis furnace strile-back and be provided with water sealed tank between device.
A kind of organic waste cracking oil, gas purification recovery device, it is characterised in that: gas phase is led
The a diameter of 250-400mm of flow tube, is shaped as the bend pipe of one end band elbow, and elbow is 90 °, and elbow port is from cooling down decontaminating separator
Top is inserted in water, and the level that submerges is 200mm.
A kind of organic waste cracking oil, gas purification recovery device, it is characterised in that: gas phase subtracts
Pressure draft-tube diameter is 150-200mm, is shaped as the bend pipe of two ends band elbow, and elbow is all 90 ° or 135 °, and bend pipe is from upper one
Level cooling and purifying separator top passes, and inserts water from next stage cooling and purifying separator top, and the level that submerges is
200mm。
A kind of organic waste cracking oil, gas purification recovery device, it is characterised in that: middle each
All having two liquid phase mozzles on level cooling and purifying separator, the nozzle position of two liquid phase mozzles is on cooling and purifying separator
Contour plane and mutually perpendicular radial position.
8. according to organic waste cracking oil a kind of described in claim 1 or 7, gas purification recovery device, it is characterised in that: liquid phase
Draft-tube diameter is 100-150mm, inserts in water, and the level that submerges is 200mm.
A kind of organic waste cracking oil, gas purification recovery device, it is characterised in that: middle each
The oil baffle of one piece of thickness 6-10mm is set in level cooling and purifying separator.
Priority Applications (1)
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CN201620842734.9U CN205856389U (en) | 2016-08-05 | 2016-08-05 | A kind of organic waste cracking oil, gas purification recovery device |
Applications Claiming Priority (1)
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CN201620842734.9U CN205856389U (en) | 2016-08-05 | 2016-08-05 | A kind of organic waste cracking oil, gas purification recovery device |
Publications (1)
Publication Number | Publication Date |
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CN205856389U true CN205856389U (en) | 2017-01-04 |
Family
ID=57656943
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CN201620842734.9U Expired - Fee Related CN205856389U (en) | 2016-08-05 | 2016-08-05 | A kind of organic waste cracking oil, gas purification recovery device |
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106085472A (en) * | 2016-08-05 | 2016-11-09 | 河南亚太能源科技股份有限公司 | A kind of organic waste cracking oil, gas cleaning and recovering process and purification recovery device |
-
2016
- 2016-08-05 CN CN201620842734.9U patent/CN205856389U/en not_active Expired - Fee Related
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106085472A (en) * | 2016-08-05 | 2016-11-09 | 河南亚太能源科技股份有限公司 | A kind of organic waste cracking oil, gas cleaning and recovering process and purification recovery device |
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Legal Events
Date | Code | Title | Description |
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C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
CF01 | Termination of patent right due to non-payment of annual fee | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20170104 Termination date: 20180805 |