CN205701817U - One way of life rubbish and agriculture and forestry organic waste material carbonization circulation comprehensive processing system - Google Patents
One way of life rubbish and agriculture and forestry organic waste material carbonization circulation comprehensive processing system Download PDFInfo
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Abstract
The utility model discloses one way of life rubbish and agriculture and forestry organic waste material carbonization circulation comprehensive processing system, relate to house refuse and agriculture and forestry organic waste material processing technology field；Described system includes the first breaker, sorting unit, the first drying device, the second breaker, the second drying device, anaerobic cracker and combustion furnace；Described system also includes cooling down storehouse and composting guiding device, and described cooling storehouse is connected on described anaerobic cracker；Described composting guiding device is connected to cool down on storehouse；The beneficial effects of the utility model are: rubbish and agriculture and forestry organic waste material process thoroughly, whole processing procedure non-secondary pollution, are truly realized recycling of rubbish and agriculture and forestry organic waste material；Whole process does not has secondary pollution, and product quality is high, the output value is high, and raw material sources are reliable and stable, fully achieve industrialization, sustainable development.
Description
[technical field]
This utility model relates to house refuse and agriculture and forestry organic waste material processing technology field, and in particular, this utility model relates to one way of life rubbish and agriculture and forestry organic waste material carbonization circulation comprehensive processing system.
[background technology]
The annual rate of growth of domestic waste was all at 5%-8% in recent years, and the annual rate of growth of minority big city rubbish reaches 8%-10%, and daily output quantity of refuse is more than 1 kilogram per capita, close to medium advanced industrial country level.China's municipal refuse generation amount presents and sharply increases, and increases the fastest trend.The a large amount of of house refuse produce and the imperfection for the treatment of technology, economic development, the quality of life of the people and the natural environment of country are caused increasingly serious negative effect.Countries in the world, while being fully recognized that this development bottleneck, are the most actively concentrated strength on exploitation and can be realized innoxious and disposal of resources rubbish effective technology, and wherein cracking technology is considered most future, especially anaerobic cracking technique.
The harm burnt away the refuse is by common cognition, correlation technique is also improving constantly, multistage incinerator after improvement, including fluidized bed incinerator, although improve efficiency of combustion, reduce pollutant emission to a certain extent, but still need to optional equipment and high operation removes the produced harmful substance of burning, and the resource degree of rubbish and efficiency the lowest.Widely used grate furnace and fluid bed furnace, compare with traditional incinerator, burns more abundant, furnace temperature is improved, newly-increased multistage or multicell burning structure so that burn the most abundant, main burning room oxygen deprivation or few oxygen burning can also be controlled, reach partial gasification or the effect of part cracking.Part cracking technology, under the unclassified precondition of rubbish, burning condition controls difficulty, unstable working condition.Due to the change of the uneven of rubbish He composition, the process conditions amplitude of variation such as furnace temperature is relatively big, and fluctuation of operating conditions makes to operate the most difficult.Part cracking or the produced gas of gasification, its calorific value is the lowest, it is difficult to directly use gas engine generating, and widely used steam turbine power production is inefficient so that refuse disposal resource level is restricted.By condensation dehydration and spray, although eliminate some pollutant, decrease corrosion and the discharge in later stage, but gas heating value is not obviously improved.
Additionally, agriculture and forestry organic waste material fuel refers to that using agriculture and forestry organic waste material, the solid waste such as rice husk, straw pavilion, sugarcane slag, wood chip, wood flour, sawdust, bamboo bits, bamboo silk, animal wastes is raw material, pressurization, a kind of fuel of density molding after pulverizing, it has bulk, the various shape such as spherical, bar-shaped, its have volume little, than burning great, resistance to, be easy to store and the advantage such as transport.In agriculture and forestry organic waste material fuel, fugitive constituent accounts for the overwhelming majority, and it can produce the imflammable gas such as a large amount of first a heatable brick bed when heating, and imflammable gas burning can produce a large amount of heat energy.Agriculture and forestry organic waste material, as the fourth-largest energy resources, occupies critical role in regenerative resource, and exploitation biomass energy both can supplement the shortage of conventional energy resource, it may have great environmental benefit.
Compared with other agriculture and forestry organic waste material energy technologys, agriculture and forestry organic waste material granular fuel technology is easier to realize people's large-scale production and use, the comfort level using agriculture and forestry organic waste material granular fuel can match in excellence or beauty with combustion gas, fuel oil equal energy source, utilize agriculture and forestry organic waste material solidification equipment to produce granular fuel project and meet national industrial policies, there is preferable economic benefit and benefit mouth is put in society.
The production technology of the agriculture and forestry organic waste material granular fuel that the fuel of agriculture and forestry organic waste material is commonly used a few days ago, including: dry, broken, add binding agent, it is dried stirring, the step such as extruded, the final agriculture and forestry organic waste material granular fuel that obtains is gone forward side by side sector-style cool-drying, existing production technology uses equipment more, cause energy consumption higher, the agriculture and forestry organic waste material time in generating agriculture and forestry organic waste material Fuel Process is long, energy consumption is big, easily coking, production efficiency is relatively low, the most also need to add the agriculture and forestry organic waste material raw material with adhesiveness, and make it be uniformly mixed, cause technique relatively complicated, molding is the most difficult.
[utility model content]
The purpose of this utility model is effectively to overcome the deficiency of above-mentioned technology, one way of life rubbish and agriculture and forestry organic waste material carbonization circulation comprehensive processing system are provided, rubbish and agriculture and forestry organic waste material process thoroughly, whole processing procedure non-secondary pollution, are truly realized recycling of rubbish and agriculture and forestry organic waste material.
The technical solution of the utility model is achieved in that its improvements: it includes the first breaker, sorting unit, the first drying device, the second breaker, the second drying device, anaerobic cracker and combustion furnace；
Described first breaker is used for putting into house refuse and house refuse carrying out break process, and described first breaker, sorting unit and the first drying device are sequentially connected with, and described sorting unit is used for sub-electing plastics；Described second breaker is used for putting into agriculture and forestry organic waste material and agriculture and forestry organic waste material being carried out break process, described second drying device is connected on the second breaker, and described first drying device and the second drying device are both connected on anaerobic cracker, described anaerobic cracker is connected to combustion furnace, for being delivered in combustion furnace by combustible gas, described combustion furnace is for heating the first drying device；
Described system also includes cooling down storehouse and composting guiding device, and described cooling storehouse is connected on described anaerobic cracker, for receiving the charcoal from anaerobic cracker；Described composting guiding device is connected to cool down on storehouse, for charcoal is made charcoal base manure.
In such a configuration, described anaerobic cracker includes pyrolysis furnace, feed appliance, degasifier, reformer, heater and multipass sort device；
Described degasifier is arranged on the exit of described feed appliance, and described feed appliance is for pyrolysis furnace internal feeding raw material；
Described heater is arranged on the side of pyrolysis furnace, it is provided that the heat of pyrolysis furnace reaction；
Described reformer is arranged on pyrolysis furnace top, and described multipass sort device is connected on reformer, described multipass sort device is provided with an air vent, is provided with a pressure valve between described air vent and multipass sort device；
Described pyrolysis furnace lower end has slag charge mouth.
In such a configuration, described anaerobic cracker also includes that circulating fan and heating rod, described heating rod are arranged on inside pyrolysis furnace, and one end of described circulating fan is connected on multipass sort device, and the other end of circulating fan is connected on heating rod；
Described anaerobic cracker also includes that pressure relief device, described pressure relief device are arranged on described degasifier.
In such a configuration, described system also includes molding apparatus processed and heat energy circulating device, described molding apparatus processed is for making plastic material by isolated for sorting unit plastics, described heat energy circulating device is arranged between described anaerobic cracker and the second drying device, for the heat that anaerobic cracker produces is sent to the second drying device；
Being also associated with proportioner on described composting guiding device, this proportioner is for adding composting dispensing to composting guiding device；Described composting dispensing is bio-bacterial manure；
In such a configuration, the baking temperature in described first drying device is 250-350 DEG C.
In such a configuration, the baking temperature in described first drying device is 300 DEG C.
The beneficial effects of the utility model are: house refuse of the present utility model and agriculture and forestry organic waste material carbonization circulation comprehensive processing system, rubbish and agriculture and forestry organic waste material process thoroughly, whole processing procedure non-secondary pollution, is truly realized recycling of rubbish and agriculture and forestry organic waste material；This utility model employing processes organic substance waste etc., including organic substance parts and the various animals and plants gurry of house refuse, can solve house refuse and environmental problem that straw stalk causes and waste, can solve again the sludge problem of changing food waste and sewage treatment plant；More solving the underground water pollution caused because of landfill, floor space greatly and simply burns the series of problems of the air pollution caused, and more effectively creates the energy and return in the charcoal base manure in soil, it is achieved the green circulatory of regenerative resource；The scheme used does not has secondary pollution in whole process, and product quality is high, the output value is high, and raw material sources are reliable and stable, fully achieve industrialization, sustainable development；Novel structure is skillfully constructed and the city of let us can become cleaner environmental protection.
[accompanying drawing explanation]
Fig. 1 is one way of life rubbish of the present utility model and the flow chart of agriculture and forestry organic waste material carbonization circulation comprehensive processing method.
Fig. 2 is the theory diagram of the anaerobic cracker of one way of life rubbish of the present utility model and the process of agriculture and forestry organic waste material carbonization circulation comprehensive.
[detailed description of the invention]
The utility model will be further described with embodiment below in conjunction with the accompanying drawings.
With reference to shown in Fig. 1, the one way of life rubbish of this utility model announcement and agriculture and forestry organic waste material carbonization circulation comprehensive processing system, concrete, this utility model provides a specific embodiment, in the present embodiment, described system includes the first breaker, sorting unit, the first drying device, the second breaker, the second drying device, anaerobic cracker and combustion furnace；Described first breaker is used for putting into house refuse and house refuse carrying out break process, and described first breaker, sorting unit and the first drying device are sequentially connected with, and described sorting unit is used for sub-electing plastics；Described second breaker is used for putting into agriculture and forestry organic waste material and agriculture and forestry organic waste material being carried out break process, described second drying device is connected on the second breaker, and described first drying device and the second drying device are both connected on anaerobic cracker, described anaerobic cracker is connected to combustion furnace, for combustible gas is delivered in combustion furnace, described combustion furnace is for heating the first drying device, in the present embodiment, baking temperature in first drying device is 300 DEG C, it should be noted that, baking temperature in first drying device can be adjusted according to actual needs, its temperature range is 250-350 DEG C；Described system also includes cooling down storehouse and composting guiding device, and described cooling storehouse is connected on described anaerobic cracker, for receiving the charcoal from anaerobic cracker；Described composting guiding device is connected to cool down on storehouse, for charcoal is made charcoal base manure.
Further, in the present embodiment, house refuse and agriculture and forestry organic waste material carbonization circulation comprehensive processing system also include molding apparatus processed and heat energy circulating device, described molding apparatus processed is for making plastic material by isolated for sorting unit plastics, described heat energy circulating device is arranged between described anaerobic cracker and the second drying device, for the heat that anaerobic cracker produces is sent to the second drying device；Being also associated with proportioner on described composting guiding device, this proportioner is for adding composting dispensing to composting guiding device；Described composting dispensing is bio-bacterial manure.
With reference to shown in Fig. 2, for described anaerobic cracker, this utility model provides a specific embodiment, and described anaerobic cracker includes pyrolysis furnace 10, feed appliance 20, degasifier 30, reformer 40, heater 50 and multipass sort device 60；Described degasifier 30 is arranged on the exit of described feed appliance 20, and described feed appliance 20 is for pyrolysis furnace 10 internal feeding raw material；Described heater 50 is arranged on the side of pyrolysis furnace 10, it is provided that the heat of pyrolysis furnace 10 reaction；Described reformer 40 is arranged on pyrolysis furnace 10 top, and described multipass sort device 60 is connected on reformer 40, described multipass sort device 60 is provided with an air vent 601, is provided with a pressure valve between described air vent 601 and multipass sort device 60；Described pyrolysis furnace 10 lower end has slag charge mouth 101.Additionally, in the present embodiment, described anaerobic cracker also includes that circulating fan 80 and heating rod 90, described heating rod 90 are arranged on pyrolysis furnace 10 inside, one end of described circulating fan 80 is connected on multipass sort device 60, and the other end of circulating fan 80 is connected on heating rod 90；Described anaerobic cracker also includes that pressure relief device 70, described pressure relief device 70 are arranged on described degasifier 30.
In conjunction with house refuse described above and agriculture and forestry organic waste material carbonization circulation comprehensive processing system, this utility model additionally provides one way of life rubbish and agriculture and forestry organic waste material carbonization circulation comprehensive processing method, in the present first embodiment, house refuse and agriculture and forestry organic waste material carbonization circulation comprehensive processing method comprise the following steps:
The break process of A, house refuse and agriculture and forestry organic waste material: house refuse is delivered in the first breaker, carries out break process, during agriculture and forestry organic waste material delivers to the second breaker simultaneously, carries out break process；
After B, house refuse carry out the first breaker process, by sorting unit, plastics are separated, and by the effect of molding apparatus processed, make plastic material；Additionally sorting unit is in separation process, and the house refuse after break process is separated into liquid refuse and solid refuse, and isolated liquid refuse enters sewage disposal system, discharges and utilize after the purified process of waste water in liquid refuse；The solid waste separated carries out secondary separation, stone, brick, glass, these nonmetallic inorganic materials of cinder is separated；
In the present embodiment, needing it is further noted that described sorting unit includes electromagnetic eddy sorting unit, electromagnetic eddy sorting unit is used for the metal in house refuse, battery is separated；
C, through sorting unit process after solid waste, by the dried of the first drying device, its baking temperature is 300 DEG C, and the solid waste after processing is delivered in anaerobic pyrolysis furnace；Meanwhile, agriculture and forestry organic waste material, after the break process by the second breaker, is delivered to the second drying device and is dried process, after dried, delivers in anaerobic pyrolysis furnace；
In D, anaerobic cracker, solid waste through dried and the agriculture and forestry organic waste material through dried are carried out thermal cracking operation, generate combustible gas, steam and solid biologic charcoal, wherein, a part of combustible gas is sent in combustion furnace, for providing the heat energy needed for the first drying device, the steam of high temperature passes through heat energy circulating device, for providing the heat energy needed for the second drying device；Meanwhile, the charcoal of generation cools down in delivering to cool down storehouse；
E, charcoal after cooling, enter composting guiding device, and proportioner provides bio-bacterial manure in composting guiding device simultaneously, by the effect of composting guiding device, generates charcoal base manure.
Carrying out anaerobic cracking technology in anaerobic cracker, the technique of described anaerobic cracking comprises the following steps:
D1, the solid waste through dried and the agriculture and forestry organic waste material through dried are entered in pyrolysis furnace by the effect of feed appliance 20, and before entering pyrolysis furnace, described degasifier 30 carries out deoxygenation process to it, the oxygen entrained by removing；
Pyrolysis furnace is heated by D2, described heater 50, heating rod 90, material in pyrolysis furnace is heated to fluidized state, organic substance is sent to the hot cracked device of thermal cracking operation and cracks out organic gas, water vapour and charcoal, and charcoal is sent into cooling storehouse and enters composting guiding device；Organic gas and water vapour enter filter progress and remove chloride, sulfur, hydrargyrum harmful substance through defecator；
In the present embodiment, organic substance is through fluidisation sand-bath course of reaction in thermal cracker, and reaction temperature is 600 DEG C；
In the present embodiment, in thermal cracker, the catalyst of reaction is basic salt, and described basic salt is KNO3；
In the present embodiment, catalytic reforming operation is under 900 DEG C of high temperature, reforms under conditions of the normal low pressure of catalyst and water vapour and water vapour/organic gas are than for 1-5: 1；Catalyst in catalytic reforming reaction is NiO-ZnO/Al2O3；
Organic gas and water vapour after D3, removing harmful substance enter catalytic reforming operation, and its primary product is containing H2O、H2、CO、CO2、CH4Mixed gas, this mixed gas through heat exchange remove the overwhelming majority water after, remaining mixture be not required to separate, be directly entered fuel synthesis procedure；Fuel synthesis procedure is carried out in multipass sort device 60, and the fuel mixture after synthesis is fractionated into tower again and fractionates out gasoline, kerosene, diesel oil, paraffin and mixed tail gas, and described tail gas includes CO2、CO、CH4, and water vapour, mixed tail gas is sent in composting guiding device；
D4, a fuel mixture part are back to pyrolysis furnace by circulating fan 80, heat heating rod 90, and fuel mixture another part is then discharged from air vent 601.
It addition, this utility model additionally provides one way of life rubbish and agriculture and forestry organic waste material carbonization circulation comprehensive processing method, in this second embodiment, house refuse and agriculture and forestry organic waste material carbonization circulation comprehensive processing method comprise the following steps:
The break process of A, house refuse and agriculture and forestry organic waste material: house refuse is delivered in the first breaker, carries out break process, during agriculture and forestry organic waste material delivers to the second breaker simultaneously, carries out break process；
After B, house refuse carry out the first breaker process, by sorting unit, plastics are separated, and by the effect of molding apparatus processed, make plastic material；Additionally sorting unit is in separation process, and the house refuse after break process is separated into liquid refuse and solid refuse, and isolated liquid refuse enters sewage disposal system, discharges and utilize after the purified process of waste water in liquid refuse；The solid waste separated carries out secondary separation, stone, brick, glass, these nonmetallic inorganic materials of cinder is separated；
In the present embodiment, needing it is further noted that described sorting unit includes electromagnetic eddy sorting unit, electromagnetic eddy sorting unit is used for the metal in house refuse, battery is separated；
C, through sorting unit process after solid waste, by the dried of the first drying device, its baking temperature is 250 DEG C, and the solid waste after processing is delivered in anaerobic pyrolysis furnace；Meanwhile, agriculture and forestry organic waste material, after the break process by the second breaker, is delivered to the second drying device and is dried process, after dried, delivers in anaerobic pyrolysis furnace；
In D, anaerobic cracker, solid waste through dried and the agriculture and forestry organic waste material through dried are carried out thermal cracking operation, generate combustible gas, steam and solid biologic charcoal, wherein, a part of combustible gas is sent in combustion furnace, for providing the heat energy needed for the first drying device, the steam of high temperature passes through heat energy circulating device, for providing the heat energy needed for the second drying device；Meanwhile, the charcoal of generation cools down in delivering to cool down storehouse；
E, charcoal after cooling, enter composting guiding device, and proportioner provides bio-bacterial manure in composting guiding device simultaneously, by the effect of composting guiding device, generates charcoal base manure.
Carrying out anaerobic cracking technology in anaerobic cracker, the technique of described anaerobic cracking comprises the following steps:
D1, the solid waste through dried and the agriculture and forestry organic waste material through dried are entered in pyrolysis furnace by the effect of feed appliance 20, and before entering pyrolysis furnace, described degasifier 30 carries out deoxygenation process to it, the oxygen entrained by removing；
Pyrolysis furnace is heated by D2, described heater 50, heating rod 90, material in pyrolysis furnace is heated to fluidized state, organic substance is sent to the hot cracked device of thermal cracking operation and cracks out organic gas, water vapour and charcoal, and charcoal is sent into cooling storehouse and enters composting guiding device；Organic gas and water vapour enter filter progress and remove chloride, sulfur, hydrargyrum harmful substance through defecator；
In the present embodiment, organic substance is through fluidisation sand-bath course of reaction in thermal cracker, and reaction temperature is 500 DEG C；
In the present embodiment, in thermal cracker, the catalyst of reaction is basic salt, and described basic salt is KNO3；
In the present embodiment, catalytic reforming operation is under 800 DEG C of high temperature, reforms under conditions of the normal low pressure of catalyst and water vapour and water vapour/organic gas are than for 1-5: 1；Catalyst in catalytic reforming reaction is NiO-ZnO/Al2O3；
Organic gas and water vapour after D3, removing harmful substance enter catalytic reforming operation, and its primary product is containing H2O、H2、CO、CO2、CH4Mixed gas, this mixed gas through heat exchange remove the overwhelming majority water after, remaining mixture be not required to separate, be directly entered fuel synthesis procedure；Fuel synthesis procedure is carried out in multipass sort device 60, and the fuel mixture after synthesis is fractionated into tower again and fractionates out gasoline, kerosene, diesel oil, paraffin and mixed tail gas, and described tail gas includes CO2、CO、CH4, and water vapour, mixed tail gas is sent in composting guiding device；
D4, a fuel mixture part are back to pyrolysis furnace by circulating fan 80, heat heating rod 90, and fuel mixture another part is then discharged from air vent 601.
It addition, this utility model additionally provides one way of life rubbish and agriculture and forestry organic waste material carbonization circulation comprehensive processing method, in this second embodiment, house refuse and agriculture and forestry organic waste material carbonization circulation comprehensive processing method comprise the following steps:
The break process of A, house refuse and agriculture and forestry organic waste material: house refuse is delivered in the first breaker, carries out break process, during agriculture and forestry organic waste material delivers to the second breaker simultaneously, carries out break process；
After B, house refuse carry out the first breaker process, by sorting unit, plastics are separated, and by the effect of molding apparatus processed, make plastic material；Additionally sorting unit is in separation process, and the house refuse after break process is separated into liquid refuse and solid refuse, and isolated liquid refuse enters sewage disposal system, discharges and utilize after the purified process of waste water in liquid refuse；The solid waste separated carries out secondary separation, stone, brick, glass, these nonmetallic inorganic materials of cinder is separated；
In the present embodiment, needing it is further noted that described sorting unit includes electromagnetic eddy sorting unit, electromagnetic eddy sorting unit is used for the metal in house refuse, battery is separated；
C, through sorting unit process after solid waste, by the dried of the first drying device, its baking temperature is 350 DEG C, and the solid waste after processing is delivered in anaerobic pyrolysis furnace；Meanwhile, agriculture and forestry organic waste material, after the break process by the second breaker, is delivered to the second drying device and is dried process, after dried, delivers in anaerobic pyrolysis furnace；
In D, anaerobic cracker, solid waste through dried and the agriculture and forestry organic waste material through dried are carried out thermal cracking operation, generate combustible gas, steam and solid biologic charcoal, wherein, a part of combustible gas is sent in combustion furnace, for providing the heat energy needed for the first drying device, the steam of high temperature passes through heat energy circulating device, for providing the heat energy needed for the second drying device；Meanwhile, the charcoal of generation cools down in delivering to cool down storehouse；
E, charcoal after cooling, enter composting guiding device, and proportioner provides bio-bacterial manure in composting guiding device simultaneously, by the effect of composting guiding device, generates charcoal base manure.
Carrying out anaerobic cracking technology in anaerobic cracker, the technique of described anaerobic cracking comprises the following steps:
D1, the solid waste through dried and the agriculture and forestry organic waste material through dried are entered in pyrolysis furnace by the effect of feed appliance 20, and before entering pyrolysis furnace, described degasifier 30 carries out deoxygenation process to it, the oxygen entrained by removing；
Pyrolysis furnace is heated by D2, described heater 50, heating rod 90, material in pyrolysis furnace is heated to fluidized state, organic substance is sent to the hot cracked device of thermal cracking operation and cracks out organic gas, water vapour and charcoal, and charcoal is sent into cooling storehouse and enters composting guiding device；Organic gas and water vapour enter filter progress and remove chloride, sulfur, hydrargyrum harmful substance through defecator；
In the present embodiment, organic substance is through fluidisation sand-bath course of reaction in thermal cracker, and reaction temperature is 700 DEG C；
In the present embodiment, in thermal cracker, the catalyst of reaction is basic salt, and described basic salt is K2CO3；
In the present embodiment, catalytic reforming operation is under 950 DEG C of high temperature, reforms under conditions of the normal low pressure of catalyst and water vapour and water vapour/organic gas are than for 1-5: 1；Catalyst in catalytic reforming reaction is NiO-ZnO/Al2O3；
Organic gas and water vapour after D3, removing harmful substance enter catalytic reforming operation, and its primary product is containing H2O、H2、CO、CO2、CH4Mixed gas, this mixed gas through heat exchange remove the overwhelming majority water after, remaining mixture be not required to separate, be directly entered fuel synthesis procedure；Fuel synthesis procedure is carried out in multipass sort device 60, and the fuel mixture after synthesis is fractionated into tower again and fractionates out gasoline, kerosene, diesel oil, paraffin and mixed tail gas, and described tail gas includes CO2、CO、CH4, and water vapour, mixed tail gas is sent in composting guiding device；
D4, a fuel mixture part are back to pyrolysis furnace by circulating fan 80, heat heating rod 90, and fuel mixture another part is then discharged from air vent 601.
House refuse of the present utility model and agriculture and forestry organic waste material carbonization circulation comprehensive processing system, rubbish and agriculture and forestry organic waste material process thoroughly, whole processing procedure non-secondary pollution, are truly realized recycling of rubbish and agriculture and forestry organic waste material；This utility model employing processes organic substance waste etc., including organic substance parts and the various animals and plants gurry of house refuse, can solve house refuse and environmental problem that straw stalk causes and waste, can solve again the sludge problem of changing food waste and sewage treatment plant；More solving the underground water pollution caused because of landfill, floor space greatly and simply burns the series of problems of the air pollution caused, and more effectively creates the energy and return in the charcoal base manure in soil, it is achieved the green circulatory of regenerative resource；The scheme used does not has secondary pollution in whole process, and product quality is high, the output value is high, and raw material sources are reliable and stable, fully achieve industrialization, sustainable development；Novel structure is skillfully constructed and the city of let us can become cleaner environmental protection.
Described above is only preferred embodiment of the present utility model, and above-mentioned specific embodiment is not to restriction of the present utility model.In technological thought category of the present utility model, various deformation and amendment can occur, retouching, amendment or the equivalent that all those of ordinary skill in the art are made as described above, belong to the scope that this utility model is protected.
Claims (6)
1. one way of life rubbish and agriculture and forestry organic waste material carbonization circulation comprehensive processing system, it is characterised in that: described system includes the first breaker, sorting unit, the first drying device, the second breaker, the second drying device, anaerobic cracker and combustion furnace；
Described first breaker is used for putting into house refuse and house refuse carrying out break process, and described first breaker, sorting unit and the first drying device are sequentially connected with, and described sorting unit is used for sub-electing plastics；Described second breaker is used for putting into agriculture and forestry organic waste material and agriculture and forestry organic waste material being carried out break process, described second drying device is connected on the second breaker, and described first drying device and the second drying device are both connected on anaerobic cracker, described anaerobic cracker is connected to combustion furnace, for being delivered in combustion furnace by combustible gas, described combustion furnace is for heating the first drying device；
Described system also includes cooling down storehouse and composting guiding device, and described cooling storehouse is connected on described anaerobic cracker, for receiving the charcoal from anaerobic cracker；Described composting guiding device is connected to cool down on storehouse, for charcoal is made charcoal base manure.
One way of life rubbish the most according to claim 1 and agriculture and forestry organic waste material carbonization circulation comprehensive processing system, it is characterised in that: described anaerobic cracker includes pyrolysis furnace, feed appliance, degasifier, reformer, heater and multipass sort device；
Described degasifier is arranged on the exit of described feed appliance, and described feed appliance is for pyrolysis furnace internal feeding raw material；
Described heater is arranged on the side of pyrolysis furnace, it is provided that the heat of pyrolysis furnace reaction；
Described reformer is arranged on pyrolysis furnace top, and described multipass sort device is connected on reformer, described multipass sort device is provided with an air vent, is provided with a pressure valve between described air vent and multipass sort device；
Described pyrolysis furnace lower end has slag charge mouth.
One way of life rubbish the most according to claim 2 and agriculture and forestry organic waste material carbonization circulation comprehensive processing system, it is characterized in that: described anaerobic cracker also includes circulating fan and heating rod, described heating rod is arranged on inside pyrolysis furnace, one end of described circulating fan is connected on multipass sort device, and the other end of circulating fan is connected on heating rod；
Described anaerobic cracker also includes that pressure relief device, described pressure relief device are arranged on described degasifier.
One way of life rubbish the most according to claim 1 and agriculture and forestry organic waste material carbonization circulation comprehensive processing system, it is characterized in that: described system also includes molding apparatus processed and heat energy circulating device, described molding apparatus processed is for making plastic material by isolated for sorting unit plastics, described heat energy circulating device is arranged between described anaerobic cracker and the second drying device, for the heat that anaerobic cracker produces is sent to the second drying device；
Being also associated with proportioner on described composting guiding device, this proportioner is for adding composting dispensing to composting guiding device；Described composting dispensing is bio-bacterial manure.
One way of life rubbish the most according to claim 1 and agriculture and forestry organic waste material carbonization circulation comprehensive processing system, it is characterised in that: the baking temperature in described first drying device is 250-350 DEG C.
One way of life rubbish the most according to claim 5 and agriculture and forestry organic waste material carbonization circulation comprehensive processing system, it is characterised in that: the baking temperature in described first drying device is 300 DEG C.
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105710114A (en) * | 2016-04-08 | 2016-06-29 | 深圳市卫力生物能源发展有限公司 | Carbonization circulation overall treatment system and method for household refuse and forestry and agricultural residues |
| CN108435754A (en) * | 2018-03-05 | 2018-08-24 | 于继林 | The technique that rural urbanization house refuse and agriculture and forestry organic waste material prepare biomass fuel |
| CN108570339A (en) * | 2018-01-25 | 2018-09-25 | 李加利 | A kind of multi-functional agriculture and forestry organic waste material harmless treatment with utilize equipment |
| CN111815338A (en) * | 2019-04-11 | 2020-10-23 | 深圳市家家分类科技有限公司 | Garbage source classification and reduction comprehensive service platform and related products |
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2016
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Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105710114A (en) * | 2016-04-08 | 2016-06-29 | 深圳市卫力生物能源发展有限公司 | Carbonization circulation overall treatment system and method for household refuse and forestry and agricultural residues |
| CN105710114B (en) * | 2016-04-08 | 2024-01-12 | 深圳卫力集团有限公司 | Domestic garbage and agricultural and forestry waste carbonization cycle comprehensive treatment system and method |
| CN108570339A (en) * | 2018-01-25 | 2018-09-25 | 李加利 | A kind of multi-functional agriculture and forestry organic waste material harmless treatment with utilize equipment |
| CN108570339B (en) * | 2018-01-25 | 2021-10-26 | 李加利 | Multifunctional agricultural and forestry waste harmless treatment and utilization equipment |
| CN108435754A (en) * | 2018-03-05 | 2018-08-24 | 于继林 | The technique that rural urbanization house refuse and agriculture and forestry organic waste material prepare biomass fuel |
| CN108435754B (en) * | 2018-03-05 | 2021-09-17 | 于继林 | Process for preparing biomass fuel from rural urban household garbage and agricultural and forestry waste |
| CN111815338A (en) * | 2019-04-11 | 2020-10-23 | 深圳市家家分类科技有限公司 | Garbage source classification and reduction comprehensive service platform and related products |
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