The utility model content
The purpose of this utility model is to provide a kind of organic matter carbonizing device for catalytic treatment, and it is comparatively complicated to solve equipment and process of the prior art, and organic matter can not be effectively utilized, and has discharge of poisonous waste, affects the problem such as environment.
The technical solution of the utility model is:
A kind of organic matter carbonizing device for catalytic treatment, this device comprises organic matter carburizing reagent part, mixing portion and heating part, organic carbon reactive moieties inside arranges mixing portion, and by the mixing portion organic matter rubbish that mixes and the catalytic reaction agent that makes the organic matter rubbish carbonization, be set to the heating part of organic carbon reactive moieties heat supply on the organic carbon reactive moieties.
Described organic matter carbonizing device for catalytic treatment, this device is provided with the air draft part, and the air draft part communicates with the organic carbon reactive moieties.
Described organic matter carbonizing device for catalytic treatment, organic carbon reactive moieties are drum-type mixed structure or stirring-type mixed structure.
Described organic matter carbonizing device for catalytic treatment, heating part are heater or heating blower.
Described organic matter carbonizing device for catalytic treatment, this device is drum-type organic matter carbonizing device for catalytic treatment, be provided with: motor, sprocket wheel, bearing block, circulation air path, wind exhausting outlet, organic carbon reaction cylinder, cylinder internal partition, device housings, hot-flow flue, hermatic door, heater, pump drainage fan and rotating shaft, concrete structure is as follows:
The output of motor is by the rotating shaft on the sprocket wheel connecting axle bearing, organic carbon reaction cylinder in the one end connection device shell of rotating shaft, the inwall of organic carbon reaction cylinder arranges the cylinder internal partition along circumference, hot-flow flue and the heater communicate with blower fan is set at device housings, in the device housings front hermatic door is set, one end of pump drainage fan communicates with the device housings inner chamber, and the other end of pump drainage fan communicates with wind exhausting outlet by circulation air path.
Described organic matter carbonizing device for catalytic treatment, this device is stirring-type organic matter carbonizing device for catalytic treatment, be provided with: stirring rod, organic carbon reative cell, hermatic door, turning cylinder, air-valve, heater, exhaust duct, discharger, reative cell discharge door, reducing motor and driving chain, concrete structure is as follows:
The output of reducing motor connects the indoor turning cylinder of organic matter carburizing reagent by driving chain, the staggered stirring rod that is arranged with on the turning cylinder, the top of organic carbon reative cell arranges hermatic door, organic carbon reative cell bottom arranges heater, reative cell discharge door, and the reative cell discharge door connects discharger by pipeline.
Described organic matter carbonizing device for catalytic treatment also arranges blower fan, and blower fan communicates with the organic carbon reative cell.
Described organic matter carbonizing device for catalytic treatment also arranges exhaust duct, and exhaust duct communicates with the organic carbon reative cell, is provided with air-valve on the exhaust duct.
Described organic matter carbonizing device for catalytic treatment, discharger are spiral discharging device.
The beneficial effects of the utility model are:
1, the utility model organic matter carbonizing device for catalytic treatment mainly is that food garbage, daily life rubbish etc. is carried out carbonization treatment, has reached organic rubbish is become useful carbon dust.Organic matter carbonizing device for catalytic treatment (stirring-type) can be installed in the refuse depot, residential quarter, processes on the spot.Organic matter carbonizing device for catalytic treatment (drum-type) can be installed in the food and drink kitchen, just can process food garbage at any time.Its advantage is, rubbish need not be transported to garbage bury factory, saves transport power, need not take up an area (garbage bury ground), stops to bury the local pollution control on ground, and the organic matter carbonizing device for catalytic treatment self not have the pollution of discharging when disposal of refuse, do not have the peculiar smell discharge yet.
2, the utility model in use, have energy savings (with present waste incineration relatively), environmental protection (with garbage loading embeading relatively), pollution-free, noiselessness, the advantage such as easy to operate, be specially adapted to the uses such as family, residential quarter, office, school, dining room and restaurant.System rubbish disposal ability scope is large, and efficient is high, can process the rubbish in large, medium and small different scales city.
3, the utility model adopts drum-type organic matter carbonizing device for catalytic treatment and stirring-type organic matter carbonizing device for catalytic treatment, to stir the rubbish in the container, make it obtain biological fully reaction, the ability of the time of shortening disposal of refuse, raising disposal of refuse.
4, organic matter rubbish claims again wet refuse, refers to the discarded object of organic components in the domestic waste, mainly is pericarp, dish skin leaf, dish skin, kitchen vegetable slag etc.Be organic waste more than 50% in the domestic waste, and increase year after year.The utility model is processed organic matter rubbish, is implemented in the low-temperature carbonization under 60-150 ℃, and the carbon dust weight of acquisition can reach the 6-10% of organic matter rubbish weight, and granularity can reach the 20-200 order as required.Coarse fodder is participated in to add first and is reacted as the carbon raw material next time, and the organic carbon catalyst can also reclaim, and continues to participate in lower secondary response.
5, the utility model adopts lower reaction temperature to make organic matter rubbish become carbon dust, and pyrolysis carbonized product quality is better, can realize high value added utilization, has good economic benefit.The composition of the organic regenerative Tan bioxin after the carbonization is zero substantially, can be used as fuel and uses.From technological principle, thoroughly avoid generation and the diffusion of dioxin extremely toxic substance, be conducive to realize the real harmless treatment of rubbish.
6, the utility model is in the process of processing organic matter rubbish, and the discharging of this device unharmful substance is for a new road has been opened up in the harmless treatment of organic matter rubbish.
The specific embodiment
Shown in Fig. 1-2, the utility model organic matter carbonizing device for catalytic treatment, this device comprises organic matter carburizing reagent part, mixing portion and heating part, organic carbon reactive moieties inside arranges mixing portion, and by the mixing portion organic matter rubbish that mixes and the catalytic reaction agent that makes the organic matter rubbish carbonization, be set to the heating part of organic carbon reactive moieties heat supply on the organic carbon reactive moieties.This device is provided with the air draft part, and the air draft part communicates with the organic carbon reactive moieties.The organic carbon reactive moieties is drum-type mixed structure or stirring-type mixed structure.
As shown in Figure 3, present embodiment is as follows to the technique of food garbage organic matter carbonizing catalytic treatment:
(1) open reactor chamber door, in reative cell, at first add the catalytic reaction agent of a certain proportion of carbon, organic matter rubbish and carbonization, off-response chamber door stirs and heats, and temperature constant is at 60-150 ℃.
Count by weight organic matter rubbish 20-40 part; Carbon dust 5-10 part; Charing catalytic reaction agent 0.1-0.3 part.The catalytic reaction agent is: add granular active carbon and powdered carbon powder in the selective oxidation of sulfur containing compounds in particular agent, wherein: the part by weight of selective oxidation of sulfur containing compounds in particular agent and granular active carbon, powdered carbon powder sum is 1:(10-30), the part by weight of granular active carbon and powdered carbon powder is 1:(1-10), under 150-200 ℃ of condition, evenly mix.The selective oxidation of sulfur containing compounds in particular agent is the concentrated sulfuric acid and sulfate; Perhaps, the selective oxidation of sulfur containing compounds in particular agent is sulfur trioxide or sulphite.The granularity of granular active carbon is the 40-80 order, and the granularity of powdered carbon powder is the 150-200 order.
In the utility model, the selective oxidation of sulfur containing compounds in particular agent is the concentrated sulfuric acid and sulfate, and the concentrated sulfuric acid and sulfate are arbitrary proportion; Perhaps, the selective oxidation of sulfur containing compounds in particular agent is sulfur trioxide or sulphite.Sulphite is: sodium sulfite, sodium hydrogensulfite, potassium sulfite, potassium bisulfite, calcium sulfite, calcium bisulfite, magnesium sulfite or magnesium bisulfite etc.Sulfate is: sodium sulphate, niter cake, potassium sulfate, potassium acid sulfate, calcium sulfate, calcium bisulfate, magnesium sulfate or magnesium bisulfate etc.
(2) open reactor chamber door, continue and add a certain proportion of organic matter rubbish, off-response chamber door is proceeded to stir and heating, and temperature constant is at 60-150 ℃.
(3) the same, circulation adds organic matter rubbish, and circular response.
(4) until in the reative cell (the carbon capacity that reactant generates reaches specified limit), stopped heating ventilates and cools off reative cell, then opens discharge door and sieves, fines is the finished product carbon dust, and coarse fodder is as the carbon raw material, and next the participation adds reaction first.
Embodiment 1
As shown in Figure 1, the utility model organic matter carbonizing device for catalytic treatment (drum-type) mainly comprises: motor 1, sprocket wheel 2, bearing block 3, circulation air path 4, wind exhausting outlet 5, organic carbon reaction cylinder (rotation) 6, cylinder internal partition 7, device housings (insulation) 8, air channel 9, hermatic door 10, heater 11, pump drainage fan 12 and rotating shaft 13 etc., and concrete structure is as follows:
The output of motor 1 is by the rotating shaft 13 on the sprocket wheel 2 connecting axle bearings 3, organic carbon reaction cylinder (rotation) 6 in the one end connection device shell (insulation) 8 of rotating shaft 13, the inwall of organic carbon reaction cylinder (rotation) 6 arranges cylinder internal partition 7 along circumference, make organic matter rubbish and promote the catalytic reaction agent of organic matter rubbish carbonization evenly fully to mix by cylinder internal partition 7, at device housings (insulation) 8 air channel 9 and the heater 11 that communicates with blower fan is set, in device housings (insulation) 8 fronts hermatic door 10 is set, one end of pump drainage fan 12 communicates with device housings (insulation) 8 inner chambers, and the other end of pump drainage fan 12 communicates with wind exhausting outlet 5 by circulation air path 4.
Adopt the treatment step of organic matter carbonizing device for catalytic treatment (drum-type) to be:
(1) opens hermatic door 10, add first 8 kilograms organic matter rubbish, 2 kilograms of carbon dusts and the agent of 0.05 kilogram of carbonization catalytic reaction; The catalytic reaction agent is: add granular active carbon and powdered carbon powder in liquid sulphur trioxide, wherein: the part by weight of liquid sulphur trioxide and granular active carbon, powdered carbon powder sum is 1:(10-20), the part by weight of granular active carbon and powdered carbon powder is 1:(1-3), under 150-200 ℃ of condition, evenly mix.The granularity of granular active carbon is the 40-80 order, and the granularity of powdered carbon powder is the 150-200 order.
Close hermatic door 10, rotate organic carbon reaction cylinder (rotation) 6, open air channel 9 and begin to ventilate, and open heater 11 and begin heating, organic carbon reaction cylinder (rotation) 6 interior temperature are controlled at (60-150 ℃), the interior normal pressure of reative cell;
(2) after 30 minutes reaction time, stop to stir, stop to ventilate, open hermatic door 10, the continuous organic matter rubbish that adds 8 kilograms, close hermatic door 10, rotate organic carbon reaction cylinder (rotation) 6, open air channel 9 and begin to ventilate, and open heater 11 and begin to heat, organic carbon reaction cylinder (rotation) 6 interior temperature are controlled at (60-150 ℃), continue reaction;
(3) after 30 minutes reaction time, repeat the processing step of (2).When rubbish is added to 48 kilograms, (repeat to add 6 times) and stop to stir, stopped heating, aeration-cooling, open hermatic door 10, discharging;
(4) reacted carbon dust carries out 200 mesh sieves and divides, and is subdivided into the finished product pack and preserves the carbon dust raw material that meal adds first as lower secondary response.
In the present embodiment, the carbon dust weight of acquisition can reach the 6-10% of organic matter rubbish weight.
Embodiment 2
As shown in Figure 2, the utility model organic matter carbonizing device for catalytic treatment (stirring-type) mainly comprises: blower fan 14, stirring rod 15, organic carbon reative cell 16, hermatic door 17, turning cylinder 18, air-valve 19, heater I 20, exhaust duct 21, discharger 22, reative cell discharge door 23, heater II 24, reducing motor 25 and driving chain 26 etc., and concrete structure is as follows:
The output of reducing motor 25 is by the turning cylinder 18 in the driving chain connection organic matter carburizing reagent chambers 16 26, the staggered stirring rod 15 that is arranged with on the turning cylinder 18, make organic matter rubbish and promote the catalytic reaction agent of organic matter rubbish carbonization evenly fully to mix by stirring rod 15, the top of organic carbon reative cell 16 arranges hermatic door 17, organic carbon reative cell 16 bottoms arrange heater (heater I 20 and heater II 24), reative cell discharge door 23, and reative cell discharge door 23 connects discharger 22 by pipeline.In the present embodiment, discharger 22 can be spiral discharging device.
Blower fan 14 communicates with organic carbon reative cell 16, and exhaust duct 21 communicates with organic carbon reative cell 16, is provided with air-valve 19 on the exhaust duct 21.
Adopt the treatment step of organic matter carbonizing device for catalytic treatment (stirring-type) to be:
(1) opens hermatic door 17, add first 25 kilograms organic matter rubbish, 6.5 kilograms of carbon dusts and the agent of 0.15 kilogram of carbonization catalytic reaction; The catalytic reaction agent is: add granular active carbon and powdered carbon powder in liquid sulphur trioxide, wherein: the part by weight of liquid sulphur trioxide and granular active carbon, powdered carbon powder sum is 1:(20-30), the part by weight of granular active carbon and powdered carbon powder is 1:(5-10), under 150-200 ℃ of condition, evenly mix.The granularity of granular active carbon is the 40-80 order, and the granularity of powdered carbon powder is the 150-200 order.
Close hermatic door 17, organic carbon reative cell 16 interior stirring rod 15 begin to stir, and open blower fan 14 and begin to ventilate, and open heater I 20 and heater II 24 begins heating, and the carburizing reagent indoor temperature is controlled at (60-150 ℃), normal pressure in the reative cell;
(2) after 30 minutes reaction time, stop to stir, stop to ventilate, open hermatic door 17, the continuous organic matter rubbish that adds 25 kilograms, close hermatic door 17, organic carbon reative cell 16 interior stirring rod 15 begin to stir, and continue to open blower fan 14 and begin to ventilate, and open heater I 20 and heater II 24 begins heating, the carburizing reagent indoor temperature is controlled at (60-150 ℃), repeats to continue reaction;
(3) after 30 minutes reaction time, repeat the processing step of (2).When rubbish is added to 250 kilograms, (repeat to add 10 times) and stop to stir, heater I 20 and heater II 24 stopped heatings, aeration-cooling, open reative cell discharge door 23 and spiral discharging device 22, discharging;
(4) reacted carbon dust carries out 200 mesh sieves and divides, and is subdivided into the finished product pack and preserves the carbon dust raw material that meal adds first as lower secondary response.
In the present embodiment, the carbon dust weight of acquisition can reach the 6-10% of organic matter rubbish weight.
Embodiment 3
As shown in Figure 1, the utility model organic carbon device for catalytic treatment (drum-type) mainly comprises: motor 1, sprocket wheel 2, bearing block 3, circulation air path 4, wind exhausting outlet 5, organic carbon reaction cylinder (rotation) 6, cylinder internal partition 7, device housings (insulation) 8, air channel 9, hermatic door 10, heater 11, pump drainage fan 12 and rotating shaft 13 etc., and concrete structure is as follows:
The output of motor 1 is by the rotating shaft 13 on the sprocket wheel 2 connecting axle bearings 3, organic carbon reaction cylinder (rotation) 6 in the one end connection device shell (insulation) 8 of rotating shaft 13, the inwall of organic carbon reaction cylinder (rotation) 6 arranges cylinder internal partition 7 along circumference, make organic matter rubbish and promote the catalytic reaction agent of organic matter rubbish carbonization evenly fully to mix by cylinder internal partition 7, at device housings (insulation) 8 air channel 9 and the heater 11 that communicates with blower fan is set, in device housings (insulation) 8 fronts hermatic door 10 is set, one end of pump drainage fan 12 communicates with device housings (insulation) 8 inner chambers, and the other end of pump drainage fan 12 communicates with wind exhausting outlet 5 by circulation air path 4.
Adopt the treatment step of organic carbon device for catalytic treatment (drum-type) to be:
(1) to food garbage by automatic forced formula oily-water seperating equipment (number of patent application: 201110195654.0) process, also can process with the grease trap of other type, waste oil is recyclable does other utilization again, to the waste residue of food garbage through the grease trap processing, carrying out processed, then add the organic carbon device for catalytic treatment.
(2) open hermatic door 10, add first waste residue, 3 kilograms of carbon dusts and the agent of 0.03 kilogram of carbonization catalytic reaction that 8 kilograms food garbage is processed through grease trap; The catalytic reaction agent is: in the selective oxidation of sulfur containing compounds in particular agent (in the present embodiment, the selective oxidation of sulfur containing compounds in particular agent is the mixture of the concentrated sulfuric acid and sulfate, the weight ratio of the concentrated sulfuric acid and sulfate is 3-6:1, sulfate is sodium sulphate, potassium sulfate, calcium sulfate or magnesium sulfate etc.) middle granular active carbon and the powdered carbon powder of adding, wherein: the part by weight of selective oxidation of sulfur containing compounds in particular agent and granular active carbon, powdered carbon powder sum is 1:(15-25), the part by weight of granular active carbon and powdered carbon powder is 1:(5-8), under 150-200 ℃ of condition, evenly mix.The granularity of granular active carbon is the 40-80 order, and the granularity of powdered carbon powder is the 150-200 order.
Close hermatic door 10, rotate organic carbon reaction cylinder (rotation) 6, open air channel 9 and begin to ventilate, and open heater 11 and begin heating, organic carbon reaction cylinder (rotation) 6 interior temperature are controlled at (80-150 ℃), the interior normal pressure of reative cell;
(3) after 30 minutes reaction time, stop to stir, stop to ventilate, open hermatic door 10, the continuous organic matter rubbish that adds 8 kilograms, close hermatic door 10, rotate organic carbon reaction cylinder (rotation) 6, open air channel 9 and begin to ventilate, and open heater 11 and begin to heat, organic carbon reaction cylinder (rotation) 6 interior temperature are controlled at (80-150 ℃), continue reaction;
(4) after 30 minutes reaction time, repeat the processing step of (2).When rubbish is added to 48 kilograms, (repeat to add 6 times) and stop to stir, stopped heating, aeration-cooling, open hermatic door 10, discharging;
(5) reacted carbon dust carries out 200 mesh sieves and divides, and is subdivided into the finished product pack and preserves the carbon dust raw material that meal adds first as lower secondary response.
In the present embodiment, the carbon dust weight of acquisition can reach the 6-10% of organic matter rubbish weight.
Embodiment 4
As shown in Figure 2, the utility model organic carbon device for catalytic treatment (stirring-type) mainly comprises: blower fan 14, stirring rod 15, organic carbon reative cell 16, hermatic door 17, turning cylinder 18, air-valve 19, heater I 20, exhaust duct 21, discharger 22, reative cell discharge door 23, heater II 24, reducing motor 25 and driving chain 26 etc., and concrete structure is as follows:
The output of reducing motor 25 is by the turning cylinder 18 in the driving chain connection organic matter carburizing reagent chambers 16 26, the staggered stirring rod 15 that is arranged with on the turning cylinder 18, make organic matter rubbish and promote the catalytic reaction agent of organic matter rubbish carbonization evenly fully to mix by stirring rod 15, the top of organic carbon reative cell 16 arranges hermatic door 17, organic carbon reative cell 16 bottoms arrange heater (heater I 20 and heater II 24), reative cell discharge door 23, and reative cell discharge door 23 connects discharger 22 by pipeline.In the present embodiment, discharger 22 can be spiral discharging device.
Blower fan 14 communicates with organic carbon reative cell 16, and exhaust duct 21 communicates with organic carbon reative cell 16, is provided with air-valve 19 on the exhaust duct 21.
Adopt the treatment step of organic carbon device for catalytic treatment (stirring-type) to be:
(1) to food garbage by automatic forced formula oily-water seperating equipment (number of patent application: 201110195654.0) process, also can process with the grease trap of other type, waste oil is recyclable does other utilization again, to the waste residue of food garbage through the grease trap processing, carrying out processed, then add the organic carbon device for catalytic treatment.
(2) open hermatic door 17, add first waste residue, 5 kilograms of carbon dusts and the agent of 0.1 kilogram of carbonization catalytic reaction that 20 kilograms food garbage is processed through grease trap; The catalytic reaction agent is: in the selective oxidation of sulfur containing compounds in particular agent (in the present embodiment, the selective oxidation of sulfur containing compounds in particular agent is sulphite, sulphite can be sodium sulfite, potassium sulfite, calcium sulfite or magnesium sulfite etc.) in add granular active carbon and powdered carbon powder, wherein: the part by weight of selective oxidation of sulfur containing compounds in particular agent and granular active carbon, powdered carbon powder sum is 1:(25-30), the part by weight of granular active carbon and powdered carbon powder is 1:(8-10), under 150-200 ℃ of condition, evenly mix.The granularity of granular active carbon is the 40-80 order, and the granularity of powdered carbon powder is the 150-200 order.
Close hermatic door 17, organic carbon reative cell 16 interior stirring rod 15 begin to stir, and open blower fan 14 and begin to ventilate, and open heater I 20 and heater II 24 begins heating, and the carburizing reagent indoor temperature is controlled at (80-150 ℃), normal pressure in the reative cell;
(2) after 30 minutes reaction time, stop to stir, stop to ventilate, open hermatic door 17, the continuous organic matter rubbish that adds 25 kilograms, close hermatic door 17, organic carbon reative cell 16 interior stirring rod 15 begin to stir, and continue to open blower fan 14 and begin to ventilate, and open heater I 20 and heater II 24 begins heating, the carburizing reagent indoor temperature is controlled at (80-150 ℃), repeats to continue reaction;
(3) after 30 minutes reaction time, repeat the processing step of (2).When rubbish is added to 250 kilograms, (repeat to add 10 times) and stop to stir, heater I 20 and heater II 24 stopped heatings, aeration-cooling, open reative cell discharge door 23 and spiral discharging device 22, discharging;
(4) reacted carbon dust carries out 200 mesh sieves and divides, and is subdivided into the finished product pack and preserves the carbon dust raw material that meal adds first as lower secondary response.
In the present embodiment, the carbon dust weight of acquisition can reach the 6-10% of organic matter rubbish weight.