CN209363255U - A kind of solid-state hazardous waste processing system - Google Patents
A kind of solid-state hazardous waste processing system Download PDFInfo
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- CN209363255U CN209363255U CN201821679729.6U CN201821679729U CN209363255U CN 209363255 U CN209363255 U CN 209363255U CN 201821679729 U CN201821679729 U CN 201821679729U CN 209363255 U CN209363255 U CN 209363255U
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Abstract
The utility model discloses a kind of solid-state hazardous waste processing system, the solid-state hazardous waste processing system includes at least waste gathering chamber, heat exchanger, retort, combustion chamber, reaction chamber and spray chamber；Wherein, the waste gathering chamber is connected through heat exchanger with the retort, and the combustion chamber is connected to through hot-fluid pipeline with the exterior portion heating layer of the retort；The exterior portion heating layer of the retort is connected through flue with reaction chamber, and the reaction chamber is connected with ozone generator and is connected through spray chamber with smoke evacuation chimney outside smoke.Pass through reaction chamber in this decorum in vent gas treatment portion and spray chamber setting, the harmless treatment that combustion chamber generates tail gas can be completed to greatest extent, the oxide of the sulfide in tail gas, nitride and carbon that burning is generated is recycled in a manner of acid solution, avoids environmental pollution caused by traditional handicraft is discharged into atmosphere.
Description
Technical field
The utility model relates to a kind of refuse disposal installation more particularly to a kind of solid-state hazardous waste processing systems.
Background technique
Domestic and international existing technology of garbage disposal mainly has several techniques of landfill method, composting method, incineration method, due to its every kind
There is certain risk for being applicable in limitation secondary pollution in technology, the resource recovery of its treatment process is relatively not perfect in addition
It is caused to recycle benefit unobvious.For garbage cracking technology since its recycling is horizontal high, the small feature of secondary pollution becomes rubbish
One of the main direction of development of processing technique.And organic waste results from cities and towns organic waste (such as town sewage) and processes
Each stage in journey.Contain a large amount of bacterium and parasite in organic waste, biochemical property is very unstable, to make
It is safe and it is free from environmental pollution be located in set organic waste as a great problem.Directly landfill will cause a large amount of organic waste
Pollutant enters deep layer from earth's surface with percolate, or even threatens underground water and rivers,lakes and seas.It is micro- due to being rich in organic waste
Biology, pathogen, virus etc., organic waste do not carry out the organic waste of hygienization for agricultural there is also very big hidden danger
Object, which enters farmland, may directly threaten the food chain of the mankind down to vegetable plot, to cause damages to human health.
In recent years, the method that people are exploring always energy-efficient, harmless processing organic waste, organic waste are split
Solution carbonization system can convert organic waste to the product that can be utilized, and still, efficiency of heating- utilization is low, and organic waste is split
Solution speed is low, and vent gas treatment is not perfect.Therefore, a kind of solid-state hazardous waste disposal system is needed.
Utility model content
The purpose of the utility model is to overcome the deficiencies in the prior art, provide a kind of solid-state hazardous waste processing system,
The solid-state hazardous waste processing system includes at least waste gathering chamber, heat exchanger, retort, combustion chamber, reaction chamber and spray
Drench room；Wherein, the waste gathering chamber is connected through heat exchanger with the retort, the combustion chamber through hot-fluid pipeline with it is described
The exterior portion heating layer of retort is connected to；The exterior portion heating layer of the retort is connected through flue with reaction chamber, and the reaction chamber connects
It is connected to ozone generator and is connected through spray chamber with smoke evacuation chimney outside smoke.
Solid particle is equipped with according to a preferred embodiment, between the waste gathering chamber and the heat exchanger to crush
Machine.
According to a preferred embodiment, the spray chamber is also connected with acid solution recovery room.
According to a preferred embodiment, the solid-state hazardous waste processing system further includes gas-solid separator, solid
Material collection storehouse, liquid material collecting chamber and gas material collection chamber；The retort is through gas-solid separator respectively at solids
Material collecting bin be connected with the heat transferring medium feed inlet of heat exchanger, the heat transferring medium discharge port of the heat exchanger respectively with liquid material
Collecting chamber is connected with gas material collection chamber, and the liquid material collecting chamber and gas material collection chamber are through tube body and combustion chamber phase
Even.
According to a preferred embodiment, the heat transferring medium discharge port end of the heat exchanger is equipped with gas-liquid separator, and
It is connected respectively with the liquid material collecting chamber and gas material collection chamber through gas-liquid separator.
According to a preferred embodiment, the heat exchanger is dividing wall type, in hybrid or heat storage exchanging apptss
It is a kind of.
Compared with the prior art, the advantages of the utility model are: having been ensured by the setting of solid particle pulverizer useless
Warm of the gurry in heat exchanger can obtain uniform and stable preheating.Meanwhile it improving in waste in retort
Charing efficiency, avoid the occurrence of causes to carbonize halfway happen because object block is excessive.
By reaction chamber in this decorum in vent gas treatment portion and spray chamber setting, combustion chamber production can be completed to greatest extent
The harmless treatment of raw tail gas, the oxide of the sulfide in tail gas, nitride and carbon that burning is generated is with acid solution
Mode recycled, avoid environmental pollution caused by traditional handicraft is discharged into atmosphere.
Detailed description of the invention
Fig. 1 is the structural schematic diagram of Tthe utility model system；
In figure, 101- waste gathering chamber, 102- heat exchanger, 103- retort, 104- gas-solid separator, 105- solids
Expect collecting bin, 106- liquid material collecting chamber, 107- gas material collecting chamber, the combustion chamber 108-, 109- reaction chamber, 110- ozone
Generator, 111- spray chamber, 112- acid solution recovery room, 113- chimney.
Specific embodiment
Illustrate the embodiments of the present invention below by way of specific specific example, those skilled in the art can be by this theory
Content disclosed by bright book understands other advantages and effect of the utility model easily.The utility model can also be by addition
Different specific embodiments are embodied or practiced, and the various details in this specification can also be based on different viewpoints and answer
With carrying out various modifications or alterations under the spirit without departing from the utility model.It should be noted that the case where not conflicting
Under, the feature in following embodiment and embodiment can be combined with each other.
It should be noted that diagram provided in following embodiment only illustrates the basic of the utility model in a schematic way
Conception, only shown in schema then with related component in the utility model rather than component count when according to actual implementation, shape
And size is drawn, when actual implementation kenel, quantity and the ratio of each component can arbitrarily change for one kind, and its assembly layout
Kenel may also be increasingly complex.
Embodiment:
A kind of solid-state hazardous waste processing system gives up as shown in Figure 1, the solid-state hazardous waste processing system includes at least
Gurry collecting chamber 101, heat exchanger 102, retort 103, gas-solid separator 104, liquid material collecting chamber 106, gas material are received
Collect chamber 107, combustion chamber 108, reaction chamber 109, ozone generator 110, spray chamber 111, acid solution recovery room 112 and chimney 113.
Wherein, the waste gathering chamber 101 is used to complete the collection of solid-state, liquid and/or gaseous state organic waste.Institute
State heat exchanger 102 for complete to waste progress the pre-heat treatment.The retort 103 is completely cutting off for completing organic waste
Thermal decomposition is carbon and other products under air.Gas-solid separator 104 is used to complete to carry out solid to the carbonizing production of retort 103
The separation of product and gaseous product.Solid material collecting bin 105 is used to complete the collection storage of the solid material generated to charing.
Liquid material collecting chamber 106 is used to complete the collection of the liquid material generated to charing.Gas material collecting chamber 107 is for completing
Collection to gaseous product after charing.Combustion chamber 108 is used to provide thermal energy for retort 103.Reaction chamber 109 is used for burning tail
Gas carries out oxidation processes.Ozone generator 110 is used to provide strong oxidizer ozone for reaction chamber 109.Spray chamber 111 is used for place
The oxide of sulfur oxide, nitrogen oxide and carbon is absorbed in tail gas after reason, is avoided being discharged into air and is formed acid rain.Acid
Liquid recovery room 112 is used to absorb for the oxide for providing spray chamber 111 for sulfur oxide, nitrogen oxide and carbon
Absorbing liquid, and absorbing liquid is recycled.Chimney 113 is used to carry out outlet to the tail gas of the tail gas after the processing of spray chamber 111.
Preferably, the waste gathering chamber 101 is connected through heat exchanger 102 with the retort 103.Further, charcoal
Changing 103 operating temperature of furnace is 300-1200 DEG C, to be completed by heat exchanger 102 to the danger collected in waste gathering chamber 101
Dangerous waste is preheated, and the material after preheating is delivered in retort 103 and completes charing process.
Preferably, solid particle pulverizer is equipped between the waste gathering chamber 101 and the heat exchanger 102.For reality
Pulverization process now is carried out to big blocky dangerous solid-state castoff, to ensure warm energy of the waste in heat exchanger 102
Access uniform and stable preheating.Meanwhile charing efficiency in waste in retort 103 is improved, it avoids the occurrence of because of object
Block is excessive and causes to carbonize halfway happen.
Preferably, retort 103 through gas-solid separator 104 changing respectively at solid material collecting bin 105 and heat exchanger 102
Thermal medium feed inlet is connected.To by gas-solid separator 104 complete the high-temperature product that retort 103 is generated carry out gas with
Solid separation, and solid product is input in solid material collecting bin 105 and is stored, to obtain activated charcoal solid
Grain.High-temperature gas product is input in heat exchanger 102, realizes that the condensation to high-temperature gas product cools down, is completed at the same time exchange
The preheating of waste in hot device 102.
Preferably, the heat transferring medium discharge port of heat exchanger 102 respectively with liquid material collecting chamber 106 and gas material collection
Chamber 107 is connected.Further, the heat exchanger 102 is one of dividing wall type, hybrid or heat storage exchanging apptss.
Further, the heat transferring medium discharge port end of heat exchanger 102 is equipped with gas-liquid separator, and through gas-liquid separator point
It is not connected with the liquid material collecting chamber 106 and gas material collection chamber 107.The high-temperature gas product that retort 103 generates
Fixed gas and liquid material are obtained after completing condensation cooling in heat exchanger 102.Preferably, fixed gas be hydrogen, carbon monoxide,
Carbon dioxide, hydro carbons goods and materials.Liquid material is water and oil.To complete liquid material by liquid material collecting chamber 106 respectively
It collects, the collection of gas material is completed by gas material collecting chamber 107.User can be to the liquid material and/or gas of collection
Material carries out the processing such as storage sale or personal burning.
Preferably, liquid material collecting chamber 106 and gas material collection chamber 107 are connected through tube body with combustion chamber 108.Burning
The fuel that room 108 inputs liquid material collecting chamber 106 and gas material collection chamber 107 carries out burning and obtains thermal energy completion pair
The high-temperature heating of retort 103.
Further, combustion chamber 108 is connected to through hot-fluid pipeline with the exterior portion heating layer of the retort 103.Further
Ground, hot-fluid duct wraps are in 103 outside of retort.To further ensure the stability of heat in retort 103.
Preferably, the heating layer of the retort 103 is also connected to through pipeline with reaction chamber 109, for completing to combustion chamber
Smoke in the 108 heating hot-fluids generated carries out Strong oxdiative vent gas treatment.
Preferably, reaction chamber 109 is connected with ozone generator 110.By ozone generator 110 generate strong oxidizer ozone with
Completion aoxidizes the oxide of sulfur oxide, nitrogen oxide and carbon in reaction chamber 109.
Preferably, reaction chamber 109 is connected through tube body with spray chamber 111, and the absorbing liquid sprayed by spray chamber 111 is completed to right
The oxide of sulfur oxide, nitrogen oxide and carbon is absorbed in tail gas after processing, is avoided being discharged into air and is formed acid rain.
Preferably, spray chamber 111 is connected with acid solution recovery room 112.It is to provide spray chamber 111 by acid solution recovery room 112
For the absorbing liquid that the oxide of sulfur oxide, nitrogen oxide and carbon is absorbed, and absorbing liquid is recycled.Acid solution
The recovered liquid for recycling indoor storage is pure water, after pure water absorbs the oxide of sulfur oxide, nitrogen oxide and carbon
In acidic liquid, and before acid solution reaches saturation, the liquid can be used as absorbing liquid repeatedly, to save water resource simultaneously
Obtain available acidic liquid.
Preferably, the spray chamber 111 is connected through chimney 113 with the external world.Chimney 113 is for handling through spray chamber 111
The tail gas of tail gas carries out outlet afterwards.
The processing to various organic hazardous wastes can be completed by the utility model solid-state hazardous waste processing system,
Both it had solved waste and has disorderly arranged the pollution problem left about to environment, while adequately having completed to the sharp again of various organic wastes
With the recycling treatment that waste of organic matter turns waste into wealth being realized by carbonizing cracking process, so that organic waste is not yet
It is the pollution sources that everybody begins to detest again, but using the resource that can be utilized.
Specific embodiment of the present utility model above described embodiment only expresses, the description thereof is more specific and detailed,
But it should not be understood as limiting the scope of the patent of the utility model.It should be pointed out that for the common of this field
For technical staff, without departing from the concept of the premise utility, various modifications and improvements can be made, these all belong to
In the protection scope of the utility model.
Claims (6)
1. a kind of solid-state hazardous waste processing system, which is characterized in that the solid-state hazardous waste processing system includes at least useless
Gurry collecting chamber (101), heat exchanger (102), retort (103), combustion chamber (108), reaction chamber (109) and spray chamber (111)；
Wherein, the waste gathering chamber (101) is connected through heat exchanger (102) with the retort (103), the combustion chamber
(108) it is connected to through hot-fluid pipeline with the exterior portion heating layer of the retort (103)；
The exterior portion heating layer of the retort (103) is connected through flue with reaction chamber (109), and the reaction chamber (109) is connected with
Ozone generator (110) is simultaneously connected through spray chamber (111) with the outer smoke evacuation chimney (113) of smoke.
2. solid-state hazardous waste processing system as described in claim 1, which is characterized in that the waste gathering chamber (101) with
Solid particle pulverizer is equipped between the heat exchanger (102).
3. solid-state hazardous waste processing system as described in claim 1, which is characterized in that the spray chamber (111) is also connected with
Acid solution recovery room (112).
4. solid-state hazardous waste processing system as described in claim 1, which is characterized in that the solid-state hazardous waste processing system
It further include gas-solid separator (104), solid material collecting bin (105), liquid material collecting chamber (106) and gas material collection chamber
(107)；
The retort (103) is through gas-solid separator (104) respectively at solid material collecting bin (105) and heat exchanger (102)
Heat transferring medium feed inlet be connected, the heat transferring medium discharge port of the heat exchanger (102) respectively with liquid material collecting chamber (106) and
Gas material collecting chamber (107) is connected, the liquid material collecting chamber (106) and gas material collection chamber (107) through tube body and
Combustion chamber (108) is connected.
5. solid-state hazardous waste processing system as claimed in claim 4, which is characterized in that the heat exchange of the heat exchanger (102) is situated between
Matter discharge port end be equipped with gas-liquid separator, and through gas-liquid separator respectively with the liquid material collecting chamber (106) and gas object
Expect that collecting chamber (107) are connected.
6. solid-state hazardous waste processing system as described in claim 1, which is characterized in that the heat exchanger (102) be dividing wall type,
One of hybrid or heat storage exchanging apptss.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821679729.6U CN209363255U (en) | 2018-10-17 | 2018-10-17 | A kind of solid-state hazardous waste processing system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821679729.6U CN209363255U (en) | 2018-10-17 | 2018-10-17 | A kind of solid-state hazardous waste processing system |
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| Publication Number | Publication Date |
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| CN209363255U true CN209363255U (en) | 2019-09-10 |
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| CN201821679729.6U Active CN209363255U (en) | 2018-10-17 | 2018-10-17 | A kind of solid-state hazardous waste processing system |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109317499A (en) * | 2018-10-17 | 2019-02-12 | 四川锐源能环科技有限公司 | A kind of solid-state hazardous waste processing system |
-
2018
- 2018-10-17 CN CN201821679729.6U patent/CN209363255U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109317499A (en) * | 2018-10-17 | 2019-02-12 | 四川锐源能环科技有限公司 | A kind of solid-state hazardous waste processing system |
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