CN206122313U - Light catalytic cracking separator - Google Patents
Light catalytic cracking separator Download PDFInfo
- Publication number
- CN206122313U CN206122313U CN201621048749.4U CN201621048749U CN206122313U CN 206122313 U CN206122313 U CN 206122313U CN 201621048749 U CN201621048749 U CN 201621048749U CN 206122313 U CN206122313 U CN 206122313U
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- valve
- heat exchanger
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Abstract
The utility model discloses a light catalytic cracking separator, including light catalytic cracker, knockout drum, heat exchanger and water sealed tank, still including the airtight feeding storehouse, screw extrusion feeder, a nitrogen purging valve, the feeding control valve that connect gradually, it observes sight glass, bottom solid ejection of compact observation sight glass, pyrolysis furnace bulk temperature meter and solid reactant blow -down valve to be equipped with the top on light catalytic cracker, at light catalytic cracker to being equipped with thermometer, pipeline sight glass and first pressure gauge between the knockout drum, be equipped with bottom flowing back valve bottom the knockout drum, be equipped with low level flowing back valve on the heat exchanger, be equipped with first emptying valve, the second temperature meter and third pressure gauge between heat exchanger to water sealed tank, be equipped with second emptying valve, water seal and feed liquor valve on the water sealed tank, be provided with the 2nd nitrogen purging valve, check valve, flowmeter, control valve and sample valve on the pipeline between nitrogen supply (NS) device and water sealed tank. The utility model discloses can effectively separate organic matter in the rubbish and inorganic matter.
Description
Technical field：
This utility model is related to a kind of segregation apparatuss, more particularly to a kind of photocatalytic cleavage segregation apparatuss, can be by solid
Organic waste break chemical bonds resolve into organic molecule gaseous state and liquid product.
Background technology：
Rubbish is the available resources for mislaying, and is unique a kind of continuous growth on the earth, never exhausted resource.People
Class is all manufacturing rubbish daily, according to statistics：Averagely to abandon 440 kilograms of rubbish for each person every year in China.To 2015,
Moreover the total amount of China's only house refuse is more than 8,600,000,000 tons still incremental with annual 6～700,000,000 tons of house refuse amoun.Life rubbish
Rubbish fills close 1,000,000 mu of floor space, and garbage-surrounded city phenomenon all occurred in most cities.On the one hand, due to plastics,
The sharp increase of the light specific gravities such as rubber, resin, bulky artificial organic articles, causes the huge pressure of refuse landfill off-capacity
Power；On the other hand, China human mortality is numerous, separate waste collection is difficult to, and causes that component of refuse is complicated, intractability is big.Cause
This, by rubbish single firing method occur as soon as, incineration treatment of garbage just into rubbish volume reduction, decrement it is a kind of helpless it
Lift.Waste incineration power generation project is also given birth to therefrom, becomes governmental support, the awkward Predicament of Development of common people's opposition.
The birth of artificial high-molecular organic material, the material life that class is given people really brings many facilities, changes people
The living habit of class.But the organic macromolecule of these synthesis is difficult to decompose, and severe contamination is caused to environment, city week is also affected
The city look and feel of Region In Yanbian, meanwhile, impact is caused on the life of the mankind.Because these organic macromolecules of mankind's synthesis are difficult
Process, have no alternative but to take single firing incinerating method.This method huge energy consumption, post processing is complicated, waste resource, and
The poison in century can also be produced ----bioxin.Material does not go out, and organic waste burns the result of minimizing, and being exactly will be this
Solid waste becomes a kind of pollutant transfer process of air pollutants.Although governmental support waste incineration power generation project,
But it is very low to this garbage direct generation of electricity efficiency of rubbish.Because component of refuse is complicated, various Organic substances and inorganic matters all may
Exist, high temperature necessarily causes various endothermic chemical reactions generations to flog a dead horse；Aphlogistic inorganic matters also need heat absorption in rubbish
The consumption amount of heat that heats up flogs a dead horse；Mix the Organic substance of inorganic matters also can not fire completely because reducing with air contact area
Burning flogs a dead horse etc., and these are all that rubbish just has the special feature that, ineffective energy consumption is too high, useful work is too low.Therefore, no matter burn
How stove improves, and is impossible to be improved garbage power amount.If especially containing substantial amounts of halogenated alkane in rubbish, burn
Dioxin severe toxicity product will be produced.Though human research is it has also been found that temperature of the dioxin severe toxicity product more than 800 DEG C
Under can decompose completely, but decomposition reaction needs certain hour to react completely.If waste incineration is without secondary
Burning solves rubbish and once burns formed product, and a large amount of bioxin are necessarily contained in the flue gas for giving off.Such one
Come, the cost not only caused on equipment is greatly improved, but also must consume a part of natural gas carry out it is combustion-supporting, it is undoubtedly necessary
Increase several procedures.Thus, it could be seen that even if waste incineration and generating electricity technology is advanced again, technique is ripe again, it is all inevitably deposited
Incomplete combustion, calorific value consume it is big, produce bioxin hidden danger, cost of electricity-generating is high the shortcomings of.
Utility model content：
Technical problem to be solved in the utility model is：For the existing difficulties and problems of rubbish comprehensive utilization, carry
Effectively organic matter in garbage and inorganic matters can be carried out into detached photocatalytic cleavage segregation apparatuss for one kind, SOLID ORGANIC can be given up
Gurry break chemical bonds resolve into organic molecule gaseous state and liquid product, and the gaseous products isolated can produce clean fuel,
Liquid product can produce fuel oil and Organic Chemicals, and solid inorganic thing is through concentration and refines, then by magnetic separation, weight
Choosing, flotation, can form the inorganic mineral products of recycling.
This utility model is adopted the technical scheme that to solve technical problem：
A kind of photocatalytic cleavage segregation apparatuss, including photocatalytic cleavage stove, knockout drum, heat exchanger and water sealed tank, also include
Closed-type feed storehouse, screw extrusion charger, the first nitrogen purge valve, the inlet control valve being sequentially connected；The photocatalytic cleavage
Top observation visor, bottom solids exit observation visor, pyrolysis furnace body temperature meter and solid reactant discharge are provided with stove
Valve；Thermometer, pipeline viewing mirror and first pressure are provided with the photocatalytic cleavage stove to the pipeline between the knockout drum
Meter；The knockout drum bottom is provided with bottom tapping valve；Arrange on the knockout drum to the pipeline between the heat exchanger
There are the first thermometer and second pressure meter；Low level tapping valve is provided with the heat exchanger, in heat exchanger and water supply installation
Cooling water water inlet control valve is provided with pipeline, on the pipeline of heat exchanger and circulating water recovery device cooling water water outlet is provided with
Control valve；The first dirt discharging valve, second temperature meter and the 3rd are provided with the heat exchanger to the pipeline between the water sealed tank
Piezometer；The second dirt discharging valve, water seal and liquid feed valve are provided with the water sealed tank；Nitrogen supply (NS) device and the water sealed tank it
Between connecting pipeline on be provided with the second nitrogen purge valve, check (non-return) valve, effusion meter, control valve and sampling valve.
Described closed-type feed storehouse and screw extrusion charger keeps air-tight state in fill process；The first described nitrogen
Gas blow down valve and the second nitrogen purge valve carry out thoroughly purging displacement at the beginning and end of reaction to device.
The power source of the photocatalytic cleavage stove is electromagnetic wave, or for mechanical wave.
Described electromagnetic wave is light wave, microwave, radio wave；Described mechanical wave is sound wave, ultrasound wave, infrasonic wave.
This utility model by solid organic castoff break chemical bonds by resolving into organic molecule gaseous state and liquid product
Thing, the gaseous products isolated can produce clean fuel, and liquid product can produce fuel oil and Organic Chemicals, and solid without
Machine thing is through concentration and refines, then by magnetic separation, gravity treatment, flotation, can form the inorganic mineral products of recycling.
This utility model can process the species of solid organic castoff and include medical waste, house refuse, crops straw
Stalk, dead Carnis Sus domestica, dead chicken, dead duck birdss etc., the cracked gas of generation are organic mixed vapour of the boiling point below 400 DEG C, Jing water
Most of with liquid condition collection after cooling, small part not by gas holder collected by condensable gases；The solid-state that cracking is produced has
Machine thing, using exhaust heat recovering method by its Btu utilization, is down to the solid-state of room temperature, and gained solid can carry out calorimetry, test
Go out its calorific value, if calorific value is higher can to replace coal-fired as solid fuel, it is also possible to analyze its constituent content, determine magnetic separation, gravity treatment
Or flotation, improve the added value of solid.
This utility model can realize the harmless treatment of rubbish volume reduction decrement, can make full use of again organic in rubbish
Thing, is generated clean gas, fuel oil or Organic Ingredientss, reduces production cost, reduces postprocessing working procedures, it is important that
Dioxin Poisons will not be produced.
Description of the drawings：
Fig. 1 is principle schematic diagram. of the present utility model.
Specific embodiment：
Below in conjunction with the accompanying drawings the utility model is further explained and explanation with specific embodiment：
Embodiment：A kind of photocatalytic cleavage segregation apparatuss, including photocatalytic cleavage stove 31, knockout drum 9, heat exchanger 12 and water
Sealed cans 23, also including the closed-type feed storehouse 1, screw extrusion charger 2, the first nitrogen purge valve 3, inlet control valve being sequentially connected
4；Top observation visor 5, bottom solids exit observation visor 30, pyrolysis furnace body temperature are provided with photocatalytic cleavage stove 31
Meter 29 and solid reactant drain valve 32；Be provided with photocatalytic cleavage stove 31 to the pipeline between knockout drum 9 thermometer 6,
Pipeline viewing mirror 7 and first pressure meter 8；The bottom of knockout drum 9 is provided with bottom tapping valve 28；Knockout drum 9 to heat exchanger 12 it
Between pipeline on be provided with the first thermometer 10 and second pressure meter 11；Low level tapping valve 13 is provided with heat exchanger 12,
Cooling water water inlet control valve 26 is provided with heat exchanger 2 and the pipeline of water supply installation 34, is filled in heat exchanger 12 and circulating water reclamation
Cooling water outlet water control valve 27 is provided with the pipeline for putting 25；Is provided with heat exchanger 12 to the pipeline between water sealed tank 23
One dirt discharging valve 14, the piezometer 16 of second temperature meter 15 and the 3rd；The second dirt discharging valve 24, the and of water seal 25 are provided with water sealed tank 23
Liquid feed valve 22；The second nitrogen purge valve 17 is provided with connecting pipeline between nitrogen supply (NS) device 33 and water sealed tank 23, is stopped
Inverse valve 18, effusion meter 29, control valve 20 and sampling valve 21.
Wherein：Closed-type feed storehouse 1 and screw extrusion charger 2 keep air-tight state in fill process；First nitrogen blows
Sweep the nitrogen purge valve 17 of valve 3 and second carries out thoroughly purging displacement at the beginning and end of reaction to device.
The power source of photocatalytic cleavage stove 31 is electromagnetic wave, or for mechanical wave；Electromagnetic wave is light wave, microwave, radio
Ripple；Mechanical wave sound wave, ultrasound wave, infrasonic wave.
This utility model by solid organic castoff break chemical bonds by resolving into organic molecule gaseous state and liquid product
Thing, the gaseous products isolated can produce clean fuel, and liquid product can produce fuel oil and Organic Chemicals, and solid without
Machine thing is through concentration and refines, then by magnetic separation, gravity treatment, flotation, can form the inorganic mineral products of recycling, reduces and produces into
This, reduces postprocessing working procedures, it is important that will not produce dioxin Poisons.
Claims (4)
1. a kind of photocatalytic cleavage segregation apparatuss, including photocatalytic cleavage stove (31), knockout drum (9), heat exchanger (12) and water seal
Tank (23), it is characterised in that：Described photocatalytic cleavage segregation apparatuss also include closed-type feed storehouse (1), the spiral being sequentially connected
Extruding charger (2), the first nitrogen purge valve (3), inlet control valve (4)；Top is provided with the photocatalytic cleavage stove (31)
Portion's observation visor (5), bottom solids exit observation visor (30), pyrolysis furnace body temperature meter (29) and solid reactant drain valve
(32)；Thermometer (6), pipeline are provided with pipeline between the photocatalytic cleavage stove (31) to the knockout drum (9) to regard
Mirror (7) and first pressure meter (8)；The knockout drum (9) bottom is provided with bottom tapping valve (28)；In the knockout drum (9)
The first thermometer (10) and second pressure meter (11) are provided with pipeline to the heat exchanger (12)；In the heat exchanger
(12) low level tapping valve (13) is provided with, on the pipeline between heat exchanger (12) and water supply installation (34) cooling water is provided with
Water inlet control valve (26), is provided with cooling water and goes out water control on the pipeline between heat exchanger (12) and circulating water recovery device (35)
Valve (27) processed；Be provided with the heat exchanger (12) to the pipeline between the water sealed tank (23) the first dirt discharging valve (14), the
Two thermometeies (15) and the 3rd piezometer (16)；Be provided with the water sealed tank (23) the second dirt discharging valve (24), water seal (25) and
Liquid feed valve (22)；The second nitrogen is provided with connecting pipeline between nitrogen supply (NS) device (33) and the water sealed tank (23) to blow
Sweep valve (17), check (non-return) valve (18), effusion meter (19), control valve (20) and sampling valve (21).
2. photocatalytic cleavage segregation apparatuss according to claim 1, it is characterised in that：Described closed-type feed storehouse (1) and
Screw extrusion charger (2) keeps air-tight state in fill process；Described the first nitrogen purge valve (3) and the second nitrogen blows
Sweep valve (17) carries out thoroughly purging displacement at the beginning and end of reaction to device.
3. photocatalytic cleavage segregation apparatuss according to claim 1, it is characterised in that：The photocatalytic cleavage stove (31)
Power source is electromagnetic wave, or for mechanical wave.
4. photocatalytic cleavage segregation apparatuss according to claim 3, it is characterised in that：Described electromagnetic wave is light wave, micro-
Ripple, radio wave；Described mechanical wave is sound wave, ultrasound wave, infrasonic wave.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621048749.4U CN206122313U (en) | 2016-09-12 | 2016-09-12 | Light catalytic cracking separator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621048749.4U CN206122313U (en) | 2016-09-12 | 2016-09-12 | Light catalytic cracking separator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206122313U true CN206122313U (en) | 2017-04-26 |
Family
ID=58569356
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201621048749.4U Withdrawn - After Issue CN206122313U (en) | 2016-09-12 | 2016-09-12 | Light catalytic cracking separator |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206122313U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106475395A (en) * | 2016-09-12 | 2017-03-08 | 河南光解环保科技有限公司 | Solid waste is innoxious, recycling processing method and processing meanss |
-
2016
- 2016-09-12 CN CN201621048749.4U patent/CN206122313U/en not_active Withdrawn - After Issue
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106475395A (en) * | 2016-09-12 | 2017-03-08 | 河南光解环保科技有限公司 | Solid waste is innoxious, recycling processing method and processing meanss |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| AV01 | Patent right actively abandoned | ||
| AV01 | Patent right actively abandoned |
Granted publication date: 20170426 Effective date of abandoning: 20190621 |