CN102728604B - Organic matter carbonization catalysis processing device - Google Patents
Organic matter carbonization catalysis processing device Download PDFInfo
- Publication number
- CN102728604B CN102728604B CN201210195225.8A CN201210195225A CN102728604B CN 102728604 B CN102728604 B CN 102728604B CN 201210195225 A CN201210195225 A CN 201210195225A CN 102728604 B CN102728604 B CN 102728604B
- Authority
- CN
- China
- Prior art keywords
- organic matter
- carbon
- organic
- rubbish
- matter rubbish
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Active
Links
Landscapes
- Processing Of Solid Wastes (AREA)
Abstract
The invention relates to an organic matter processing technique, particularly an organic matter carbonization catalysis processing device for solving the problems of complicated devices and technology, inefficient application of organic matters, discharge of harmful matters, influence on the environment, etc. existing in the prior art. The device comprises an organic matter carbonization reaction unit, a mixing unit and a heating unit, wherein the mixing unit, organic waste mixed by the mixing unit and a catalytic reaction agent used for carbonizing the organic waste are arranged in the organic matter carbonization reaction unit, and the heating unit used for heating the organic matter carbonization reaction unit is arranged on the organic matter carbonization reaction unit. The device of the invention carries out carbonization on food residues, house refuse and the like, and turns organic waste into useful carbon powder. The device (stirring type) can be arranged in community garbage stations and process garbage on the spot. The device (roller type) can be arranged in restaurant kitchens and supermarkets, and can process food residues and agricultural product garbage at any time.
Description
Technical field
The present invention relates to organic matter treatment technology, be specially a kind of organic matter carbonizing device for catalytic treatment.
Background technology
At present, domestic rubbish disposal is, after being collected by family, be sent to refuse collecting mid point mostly, then delivers to garbage disposal plant process by sanitationman is concentrated.This processing mode not only will drop into a large amount of human and material resources, and dustbin, the easy contaminated environment in soot, and affects the appearance of the city.
Along with the quickening of urbanization process, the process of domestic waste has become the thorny difficult problem of countries in the world government, and countries in the world adopt the mode process domestic waste of landfill and burning.But, direct landfill meeting appropriation of land, contaminated environment and polluted underground water source; The greatest problem of sanitary landfill method is place election difficulty, is not that place Outskirts of City can find suitable landfill place.Exactly to the country adopting sanitary landfill method always, then it is also more and more difficult to find suitable landfill place.Although simple burning can process various house refuse, burning disposal investment is large, processing cost is high and there is the problem that can produce the harmful substances such as bioxin in organic matter Refuse Incineration Process, easily causes secondary pollution.And rubbish can not Thorough combustion, after burning, in stove, slag easily lumps, and not only can not effectively utilize, but also take a large amount of soil, contaminated environment, can not carry out recycling to rubbish, waste resource.
There is considerable part to be organic matter rubbish in domestic waste, in order to make full use of these organic matter rubbish, there has been proposed the resolving ideas of compost treatment, pile up by house refuse, store after insulation, ferment, by the ability of microbial decomposition in rubbish, organic substance decomposing is become inorganic nutrients.After compost treatment, house refuse becomes health, tasteless humus.So both solve the outlet of rubbish, can reach again the object of renewable resources, but consumer garbage compost amount is large, nutrient content is low, and Long-Time Service easily causes soil compaction and groundwater quality to degenerate.So the scale of house refuse is not easily too large, though composting mode can make rubbish become fertilizer, but the fertilizer efficiency of this garbage tankage is low, and is not accepted due to the existence of possibility of pollution.Composting technology can not process the organic matter being difficult to degrade, and only relies on compost treatment still thoroughly can not solve garbage problem.
Chinese invention patent (patent No. 20071014407.6) discloses one way of life temperature garbage negative pressure hot distilling process technique and equipment, it comprises hot furnace, cyclone separator, cooler, point flow container, blower fan and sealing feeding chamber, discharging bin, its hot furnace divides upper and lower two stoves, lower stove is combustion chamber, is provided with the gas outlet of flue gas above hot furnace; Upper stove is that heat heats up in a steamer room, is tightly connected with sealing feeding chamber, discharging bin, and form sealing transmission cavity, heat is heated up in a steamer room and is set in above hot furnace, and periphery is provided with flue and communicates with combustion chamber, is provided with heat and heats up in a steamer gas gas outlet, be connected with cyclone separator above side; Cyclone separator is sequentially connected with cooler, point flow container, another cyclone separator, blower fan; Combustion chambers burn produces heat and flue gas, respectively heat is heated up in a steamer to the rubbish negative pressure hot distilling in room, heat heats up in a steamer the temperature of room between 300 DEG C ~ 350 DEG C, rubbish becomes fuel gas, tar, carbon black through overheated cut solution, can recycle, effectively inhibit the generation of bioxin, solve the difficult problem producing secondary pollution in process house refuse process.Its weak point is, equipment and process is comparatively complicated, and cost is higher.
Summary of the invention
The object of the present invention is to provide a kind of organic matter carbonizing device for catalytic treatment, solve equipment and process of the prior art comparatively complicated, organic matter can not be effectively utilized, and there is discharge of poisonous waste, affects the problems such as environment.
Technical scheme of the present invention 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 mixed and the catalytic reaction agent making organic matter rubbish carbonization, organic carbon reactive moieties is set to the heating part of organic carbon reactive moieties heat supply.
Described organic matter carbonizing device for catalytic treatment, this device is provided with air exhaust part, and air exhaust part communicates with organic carbon reactive moieties.
Described organic matter carbonizing device for catalytic treatment, organic carbon reactive moieties is drum-type mixed structure or stirring-type mixed structure.
Described organic matter carbonizing device for catalytic treatment, heating part is 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: the reaction of motor, sprocket wheel, bearing block, circulation air path, wind exhausting outlet, organic carbon 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 in sprocket wheel connecting axle bearing, organic carbon reaction cylinder in one end connection device shell of rotating shaft, the inwall of organic carbon reaction cylinder circumferentially arranges cylinder internal partition, device housings arranges the hot-flow flue communicated with blower fan and heater, before device housings, hermatic door is set, one end of pump drainage fan communicates with device housings inner chamber, and the other end of pump drainage fan is communicated 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 turning cylinder of organic matter carburizing reagent indoor by driving chain, turning cylinder alternate has stirring rod, the top of organic carbon reative cell arranges hermatic door, arrange heater, reative cell discharge door bottom organic carbon reative cell, 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 organic carbon reative cell.
Described organic matter carbonizing device for catalytic treatment, also arranges exhaust duct, and exhaust duct communicates with organic carbon reative cell, and exhaust duct is provided with air-valve.
Described organic matter carbonizing device for catalytic treatment, discharger is spiral discharging device.
The invention has the beneficial effects as follows:
1, organic matter carbonizing device for catalytic treatment of the present invention, mainly carries out carbonization treatment to food garbage, daily life rubbish etc., has reached and organic rubbish is become useful carbon dust.Organic matter carbonizing device for catalytic treatment (stirring-type) can be arranged on refuse depot, community, treatment in situ.Organic matter carbonizing device for catalytic treatment (drum-type) can be arranged in food and drink kitchen, just can process food garbage at any time.Its advantage is, rubbish need not transport to garbage bury factory, saves transport power, and need not take up an area on (garbage bury ground), stop the local pollution control of burying ground, the pollution that organic matter carbonizing device for catalytic treatment self does not discharge when disposal of refuse, does not have peculiar smell to discharge yet.
2, the present invention in use, there is economize energy (comparing with current waste incineration), environmental protection (comparing with garbage loading embeading), pollution-free, noiselessness, the advantage such as easy to operate, be specially adapted to the uses such as family, community, office, school, dining room and restaurant.System rubbish disposal ability scope is large, and efficiency is high, can process the rubbish in large, medium and small different scales city.
3, the present invention 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 container, makes it obtain reaction biological fully, shortens the time of disposal of refuse, improves the ability of disposal of refuse.
4, organic matter rubbish is also known as wet refuse, refers to the discarded object of organic components in domestic waste, mainly pericarp, dish skin leaf, dish skin, kitchen vegetable slag etc.In domestic waste, more than 50% is organic waste, and increases year by year.The present invention processes organic matter rubbish, realizes the low-temperature carbonization at 60-150 DEG C, and the carbon dust weight of acquisition can reach the 6-10% of organic matter rubbish weight, and granularity can reach 20-200 order as required.Coarse fodder is as carbon raw material, and participate in next time and add reaction first, organic carbon catalyst can also reclaim, and continues to participate in lower secondary response.
5, the present invention adopts lower reaction temperature to make organic matter rubbish become carbon dust, and pyrolysis carbonization product qualities is better, can realize high value added utilization, have good economic benefit.The composition of the organic regenerative Tan bioxin after 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 the real harmless treatment realizing rubbish.
6, the present invention is in the process of process organic matter rubbish, and the discharge of this device unharmful substance, the harmless treatment for organic matter rubbish opens a Tiao Xin road.
Accompanying drawing explanation
Fig. 1 is organic matter carbonizing device for catalytic treatment (drum-type) structural representation of the present invention.In figure, 1, motor; 2, sprocket wheel; 3, bearing block; 4, circulation air path; 5, wind exhausting outlet; 6, organic carbon reaction cylinder (rotation); 7, cylinder internal partition; 8, device housings (insulation); 9, air channel; 10, hermatic door; 11, heater; 12, pump drainage fan; 13, rotating shaft.
Fig. 2 is organic matter carbonizing device for catalytic treatment (stirring-type) structural representation of the present invention.In figure, 14, blower fan; 15, stirring rod; 16, organic carbon reative cell; 17, hermatic door; 18, turning cylinder; 19, air-valve; 20, heater I; 21, exhaust duct; 22, discharger; 23, reative cell discharge door; 24, heater II; 25, reducing motor; 26, driving chain.
Fig. 3 is for adopting the present invention to food garbage organic matter carbonizing catalytic treatment FB(flow block).
Detailed description of the invention
As shown in Figure 1-2, organic matter carbonizing device for catalytic treatment of the present invention, 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 mixed and the catalytic reaction agent making organic matter rubbish carbonization, organic carbon reactive moieties is set to the heating part of organic carbon reactive moieties heat supply.This device is provided with air exhaust part, and air exhaust part communicates with organic carbon reactive moieties.Organic carbon reactive moieties is drum-type mixed structure or stirring-type mixed structure.
As shown in Figure 3, the technique of the present embodiment to the catalytic treatment of food garbage organic matter carbonizing is as follows:
(1) open reactor chamber door, in reative cell, first add the catalytic reaction agent of a certain proportion of carbon, organic matter rubbish and carbonization, off-response room door, carry out stirring and heating, temperature constant is at 60-150 DEG C.
Count by weight, organic matter rubbish 20-40 part; Carbon dust 5-10 part; Charing catalytic reaction agent 0.1-0.3 part.Catalytic reaction agent is: in selective oxidation of sulfur containing compounds in particular agent, 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:(10-30), the part by weight of granular active carbon and powdered carbon powder is 1:(1-10), under 150-200 DEG C of condition, Homogeneous phase mixing forms.Selective oxidation of sulfur containing compounds in particular agent is the concentrated sulfuric acid and sulfate; Or selective oxidation of sulfur containing compounds in particular agent is sulfur trioxide or sulphite.The granularity of granular active carbon is 40-80 order, and the granularity of powdered carbon powder is 150-200 order.
In the present invention, 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; Or 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 room door, proceed to stir and heat, temperature constant is at 60-150 DEG C.
(3) the same, circulation adds organic matter rubbish, and circular response.
(4) until in reative cell (the carbon capacity that reactant generates reaches rated limits), stop heating, ventilating and cooling reative cell, then open discharge door and sieve, fines is finished product carbon dust, coarse fodder, as carbon raw material, is participated in and is added reaction first next time.
Embodiment 1
As shown in Figure 1, organic matter carbonizing device for catalytic treatment (drum-type) of the present invention 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 in sprocket wheel 2 connecting axle bearing 3, organic carbon reaction cylinder (rotation) 6 in one end connection device shell (insulation) 8 of rotating shaft 13, the inwall of organic carbon reaction cylinder (rotation) 6 circumferentially arranges cylinder internal partition 7, make organic matter rubbish by cylinder internal partition 7 and promote that the catalytic reaction agent of organic matter rubbish carbonization evenly fully mixes, device housings (insulation) 8 arranges the air channel 9 communicated with blower fan and heater 11, at device housings (insulation) 8, hermatic door 10 is set above, one end of pump drainage fan 12 communicates with device housings (insulation) 8 inner chamber, the other end of pump drainage fan 12 is communicated with wind exhausting outlet 5 by circulation air path 4.
The treatment step of employing organic matter carbonizing device for catalytic treatment (drum-type) is:
(1) open hermatic door 10, add the organic matter rubbish of 8 kilograms, 2 kilograms of carbon dusts and the agent of 0.05 kilogram of carbonization catalytic reaction first; Catalytic reaction agent is: in liquid sulphur trioxide, add granular active carbon and powdered carbon powder, 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 DEG C of condition, Homogeneous phase mixing forms.The granularity of granular active carbon is 40-80 order, and the granularity of powdered carbon powder is 150-200 order.
Close hermatic door 10, rotate organic carbon reaction cylinder (rotations) 6, open air channel 9 and start to ventilate, and open heater 11 and start heating, organic carbon reacts temperature in cylinder (rotation) 6 and controls at (60-150 DEG C), normal pressure in reative cell;
(2) after 30 minutes reaction time, stop stirring, stop ventilating, open hermatic door 10, the continuous organic matter rubbish adding 8 kilograms, close hermatic door 10, rotate organic carbon reaction cylinder (rotations) 6, open air channel 9 and start to ventilate, and open heater 11 and start to heat, in organic carbon reaction cylinder (rotation) 6, temperature controls at (60-150 DEG C), continues reaction;
(3), after 30 minutes reaction time, the processing step of (2) is repeated.When rubbish is added to 48 kilograms, (repeating to add 6 times) stops stirring, and stops heating, aeration-cooling, opens hermatic door 10, discharging;
(4) reacted carbon dust carries out 200 mesh sieves and divides, and is subdivided into 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, organic matter carbonizing device for catalytic treatment (stirring-type) of the present invention 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 connects the turning cylinder 18 in organic matter carburizing reagent room 16 by driving chain 26, turning cylinder 18 alternate has stirring rod 15, make organic matter rubbish by stirring rod 15 and promote that the catalytic reaction agent of organic matter rubbish carbonization evenly fully mixes, the top of organic carbon reative cell 16 arranges hermatic door 17, arrange heater (heater I 20 and heater II 24), reative cell discharge door 23 bottom organic carbon reative cell 16, 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, exhaust duct 21 is provided with air-valve 19.
The treatment step of employing organic matter carbonizing device for catalytic treatment (stirring-type) is:
(1) open hermatic door 17, add the organic matter rubbish of 25 kilograms, 6.5 kilograms of carbon dusts and the agent of 0.15 kilogram of carbonization catalytic reaction first; Catalytic reaction agent is: in liquid sulphur trioxide, add granular active carbon and powdered carbon powder, 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 DEG C of condition, Homogeneous phase mixing forms.The granularity of granular active carbon is 40-80 order, and the granularity of powdered carbon powder is 150-200 order.
Close hermatic door 17, in organic carbon reative cell 16, stirring rod 15 starts to stir, and opens blower fan 14 and starts to ventilate, and opens heater I 20 and heater II 24 and start heating, and carburizing reagent indoor temperature controls at (60-150 DEG C), normal pressure in reative cell;
(2) after 30 minutes reaction time, stop stirring, stop ventilating, open hermatic door 17, the continuous organic matter rubbish adding 25 kilograms, close hermatic door 17, in organic carbon reative cell 16, stirring rod 15 starts to stir, and continues to open blower fan 14 and starts to ventilate, and opens heater I 20 and heater II 24 starts heating, carburizing reagent indoor temperature controls at (60-150 DEG C), repeats to continue reaction;
(3), after 30 minutes reaction time, the processing step of (2) is repeated.When rubbish is added to 250 kilograms, (repeating to add 10 times) stops stirring, and heater I 20 and heater II 24 stop heating, 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 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, organic carbon device for catalytic treatment (drum-type) of the present invention 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 in sprocket wheel 2 connecting axle bearing 3, organic carbon reaction cylinder (rotation) 6 in one end connection device shell (insulation) 8 of rotating shaft 13, the inwall of organic carbon reaction cylinder (rotation) 6 circumferentially arranges cylinder internal partition 7, make organic matter rubbish by cylinder internal partition 7 and promote that the catalytic reaction agent of organic matter rubbish carbonization evenly fully mixes, device housings (insulation) 8 arranges the air channel 9 communicated with blower fan and heater 11, at device housings (insulation) 8, hermatic door 10 is set above, one end of pump drainage fan 12 communicates with device housings (insulation) 8 inner chamber, the other end of pump drainage fan 12 is communicated with wind exhausting outlet 5 by circulation air path 4.
The treatment step of employing organic carbon device for catalytic treatment (drum-type) is:
(1) automatic forced formula oily-water seperating equipment (number of patent application: 201110195654.0) process is passed through to food garbage, 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 grease trap process, carry out processed, then add organic carbon device for catalytic treatment.
(2) open hermatic door 10, add the food garbage of 8 kilograms first through the waste residue of grease trap process, 3 kilograms of carbon dusts and the agent of 0.03 kilogram of carbonization catalytic reaction; Catalytic reaction agent is: in selective oxidation of sulfur containing compounds in particular agent (in the present embodiment, 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.) 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:(15-25), the part by weight of granular active carbon and powdered carbon powder is 1:(5-8), under 150-200 DEG C of condition, Homogeneous phase mixing forms.The granularity of granular active carbon is 40-80 order, and the granularity of powdered carbon powder is 150-200 order.
Close hermatic door 10, rotate organic carbon reaction cylinder (rotations) 6, open air channel 9 and start to ventilate, and open heater 11 and start heating, organic carbon reacts temperature in cylinder (rotation) 6 and controls at (80-150 DEG C), normal pressure in reative cell;
(3) after 30 minutes reaction time, stop stirring, stop ventilating, open hermatic door 10, the continuous organic matter rubbish adding 8 kilograms, close hermatic door 10, rotate organic carbon reaction cylinder (rotations) 6, open air channel 9 and start to ventilate, and open heater 11 and start to heat, in organic carbon reaction cylinder (rotation) 6, temperature controls at (80-150 DEG C), continues reaction;
(4), after 30 minutes reaction time, the processing step of (2) is repeated.When rubbish is added to 48 kilograms, (repeating to add 6 times) stops stirring, and stops heating, aeration-cooling, opens hermatic door 10, discharging;
(5) reacted carbon dust carries out 200 mesh sieves and divides, and is subdivided into 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, organic carbon device for catalytic treatment (stirring-type) of the present invention 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 connects the turning cylinder 18 in organic matter carburizing reagent room 16 by driving chain 26, turning cylinder 18 alternate has stirring rod 15, make organic matter rubbish by stirring rod 15 and promote that the catalytic reaction agent of organic matter rubbish carbonization evenly fully mixes, the top of organic carbon reative cell 16 arranges hermatic door 17, arrange heater (heater I 20 and heater II 24), reative cell discharge door 23 bottom organic carbon reative cell 16, 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, exhaust duct 21 is provided with air-valve 19.
The treatment step of employing organic carbon device for catalytic treatment (stirring-type) is:
(1) automatic forced formula oily-water seperating equipment (number of patent application: 201110195654.0) process is passed through to food garbage, 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 grease trap process, carry out processed, then add organic carbon device for catalytic treatment.
(2) open hermatic door 17, add the food garbage of 20 kilograms first through the waste residue of grease trap process, 5 kilograms of carbon dusts and the agent of 0.1 kilogram of carbonization catalytic reaction; Catalytic reaction agent is: in selective oxidation of sulfur containing compounds in particular agent (in the present embodiment, 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 DEG C of condition, Homogeneous phase mixing forms.The granularity of granular active carbon is 40-80 order, and the granularity of powdered carbon powder is 150-200 order.
Close hermatic door 17, in organic carbon reative cell 16, stirring rod 15 starts to stir, and opens blower fan 14 and starts to ventilate, and opens heater I 20 and heater II 24 and start heating, and carburizing reagent indoor temperature controls at (80-150 DEG C), normal pressure in reative cell;
(2) after 30 minutes reaction time, stop stirring, stop ventilating, open hermatic door 17, the continuous organic matter rubbish adding 25 kilograms, close hermatic door 17, in organic carbon reative cell 16, stirring rod 15 starts to stir, and continues to open blower fan 14 and starts to ventilate, and opens heater I 20 and heater II 24 starts heating, carburizing reagent indoor temperature controls at (80-150 DEG C), repeats to continue reaction;
(3), after 30 minutes reaction time, the processing step of (2) is repeated.When rubbish is added to 250 kilograms, (repeating to add 10 times) stops stirring, and heater I 20 and heater II 24 stop heating, 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 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.
Claims (5)
1. an organic matter carbonizing catalysis treatment method, the method adopts organic matter carbonizing device for catalytic treatment to process organic matter rubbish, it is characterized in that: this device comprises organic matter carburizing reagent part, mixing portion and heating part, organic carbon reactive moieties inside arranges mixing portion, and the organic matter rubbish to be mixed by mixing portion, carbon dust and make the catalytic reaction agent of organic matter rubbish carbonization, organic carbon reactive moieties is set to the heating part of organic carbon reactive moieties heat supply;
This device is drum-type organic matter carbonizing device for catalytic treatment, be provided with: the reaction of motor, sprocket wheel, bearing block, circulation air path, wind exhausting outlet, organic carbon 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 in sprocket wheel connecting axle bearing, organic carbon reaction cylinder in one end connection device shell of rotating shaft, the inwall of organic carbon reaction cylinder circumferentially arranges cylinder internal partition, make organic matter rubbish by cylinder internal partition and promote that the catalytic reaction agent of organic matter rubbish carbonization evenly fully mixes, device housings arranges the hot-flow flue communicated with blower fan and heater, before device housings, hermatic door is set, one end of pump drainage fan communicates with device housings inner chamber, the other end of pump drainage fan is communicated with wind exhausting outlet by circulation air path,
The described organic matter rubbish, the carbon dust that are mixed by mixing portion and make the catalytic reaction agent of organic matter rubbish carbonization, counted, organic matter rubbish 20-40 part by weight; Carbon dust 5-10 part; Charing catalytic reaction agent 0.1-0.3 part; Catalytic reaction agent is: in selective oxidation of sulfur containing compounds in particular agent, 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:(10-30), the part by weight of granular active carbon and powdered carbon powder is 1:(1-10), under 150-200 DEG C of condition, Homogeneous phase mixing forms; Selective oxidation of sulfur containing compounds in particular agent is the concentrated sulfuric acid and sulfate; Or selective oxidation of sulfur containing compounds in particular agent is sulfur trioxide or sulphite; The granularity of granular active carbon is 40-80 order, and the granularity of powdered carbon powder is 150-200 order;
This device processes organic matter rubbish, realizes the low-temperature carbonization at 60-150 DEG C, and the carbon dust weight of acquisition reaches the 6-10% of organic matter rubbish weight, and granularity reaches 20-200 order as required.
2. an organic matter carbonizing catalysis treatment method, the method adopts organic matter carbonizing device for catalytic treatment to process organic matter rubbish, it is characterized in that: this device comprises organic matter carburizing reagent part, mixing portion and heating part, organic carbon reactive moieties inside arranges mixing portion, and the organic matter rubbish to be mixed by mixing portion, carbon dust and make the catalytic reaction agent of organic matter rubbish carbonization, organic carbon reactive moieties is set to the heating part of organic carbon reactive moieties heat supply;
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 turning cylinder of organic matter carburizing reagent indoor by driving chain, turning cylinder alternate has stirring rod, make organic matter rubbish by stirring rod and promote that the catalytic reaction agent of organic matter rubbish carbonization evenly fully mixes, the top of organic carbon reative cell arranges hermatic door, arrange heater, reative cell discharge door bottom organic carbon reative cell, reative cell discharge door connects discharger by pipeline;
The described organic matter rubbish, the carbon dust that are mixed by mixing portion and make the catalytic reaction agent of organic matter rubbish carbonization, counted, organic matter rubbish 20-40 part by weight; Carbon dust 5-10 part; Charing catalytic reaction agent 0.1-0.3 part; Catalytic reaction agent is: in selective oxidation of sulfur containing compounds in particular agent, 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:(10-30), the part by weight of granular active carbon and powdered carbon powder is 1:(1-10), under 150-200 DEG C of condition, Homogeneous phase mixing forms; Selective oxidation of sulfur containing compounds in particular agent is the concentrated sulfuric acid and sulfate; Or selective oxidation of sulfur containing compounds in particular agent is sulfur trioxide or sulphite; The granularity of granular active carbon is 40-80 order, and the granularity of powdered carbon powder is 150-200 order;
This device processes organic matter rubbish, realizes the low-temperature carbonization at 60-150 DEG C, and the carbon dust weight of acquisition reaches the 6-10% of organic matter rubbish weight, and granularity reaches 20-200 order as required.
3. according to organic matter carbonizing catalysis treatment method according to claim 2, it is characterized in that: also arrange blower fan, blower fan communicates with organic carbon reative cell.
4. according to organic matter carbonizing catalysis treatment method according to claim 2, it is characterized in that: also arrange exhaust duct, exhaust duct communicates with organic carbon reative cell, and exhaust duct is provided with air-valve.
5. according to organic matter carbonizing catalysis treatment method according to claim 2, it is characterized in that: discharger is spiral discharging device.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201210195225.8A CN102728604B (en) | 2012-06-13 | 2012-06-13 | Organic matter carbonization catalysis processing device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201210195225.8A CN102728604B (en) | 2012-06-13 | 2012-06-13 | Organic matter carbonization catalysis processing device |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN102728604A CN102728604A (en) | 2012-10-17 |
| CN102728604B true CN102728604B (en) | 2015-07-15 |
Family
ID=46985302
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201210195225.8A Active CN102728604B (en) | 2012-06-13 | 2012-06-13 | Organic matter carbonization catalysis processing device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN102728604B (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113307663B (en) * | 2020-02-27 | 2024-05-03 | 陕西博瑞新环保科技有限公司 | Distributed harmless carbon fertilizer preparation device by cracking garbage organic matters |
| CN112299887A (en) * | 2020-10-16 | 2021-02-02 | 陕西博瑞新环保科技有限公司 | Device for preparing carbon fertilizer by cracking harmless superconducting garbage with mixed heat source |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH11335670A (en) * | 1998-05-22 | 1999-12-07 | Nisshin Kogyo Kk | Apparatus for carbonizing treatment |
| JP2002129165A (en) * | 2000-10-25 | 2002-05-09 | Yamamoto Kiyokazu | Carbonization apparatus for waste |
| JP2003201481A (en) * | 2002-01-08 | 2003-07-18 | Masayuki Matsui | Carbonizing oven |
| CN201288111Y (en) * | 2008-07-09 | 2009-08-12 | 密西西比国际水务有限公司 | Apparatus for treating sewage sludge and/or waste slag |
| CN102307681A (en) * | 2008-07-21 | 2012-01-04 | S·Y·维尔奇科 | Method for processing materials in a drum-type apparatus and a device for carrying out said method |
| CN202667236U (en) * | 2012-06-13 | 2013-01-16 | 沈阳金利洁科技有限公司 | Organic matter carbonization catalytic treatment device |
-
2012
- 2012-06-13 CN CN201210195225.8A patent/CN102728604B/en active Active
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH11335670A (en) * | 1998-05-22 | 1999-12-07 | Nisshin Kogyo Kk | Apparatus for carbonizing treatment |
| JP2002129165A (en) * | 2000-10-25 | 2002-05-09 | Yamamoto Kiyokazu | Carbonization apparatus for waste |
| JP2003201481A (en) * | 2002-01-08 | 2003-07-18 | Masayuki Matsui | Carbonizing oven |
| CN201288111Y (en) * | 2008-07-09 | 2009-08-12 | 密西西比国际水务有限公司 | Apparatus for treating sewage sludge and/or waste slag |
| CN102307681A (en) * | 2008-07-21 | 2012-01-04 | S·Y·维尔奇科 | Method for processing materials in a drum-type apparatus and a device for carrying out said method |
| CN202667236U (en) * | 2012-06-13 | 2013-01-16 | 沈阳金利洁科技有限公司 | Organic matter carbonization catalytic treatment device |
Also Published As
| Publication number | Publication date |
|---|---|
| CN102728604A (en) | 2012-10-17 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN105855275B (en) | A kind of processing method of sludge and kitchen garbage | |
| CN101797578B (en) | Garbage microwave pyrolysis comprehensive treatment system and method and equipment used by same | |
| CN101844859B (en) | Complete steam low-temperature thermally tempering and drying device and method for sludge | |
| CN103240264B (en) | Have the low emission solid organic castoff treatment system of biogas and Activated Carbon Production concurrently | |
| CN2905782Y (en) | Kitchen refuse compost treating system | |
| CN102249508B (en) | Method for comprehensively utilizing sludge in recycling mode | |
| CN102808000B (en) | Recycling grading utilization and carbon sequestration treatment method for municipal solid waste | |
| CN201999838U (en) | Sludge treatment system | |
| CN105057307B (en) | Domestic rubbish treatment system | |
| CN102504843B (en) | Heat accumulation type fuel gas radiation pipe rotary hearth furnace domestic garbage dry distillation method | |
| CN204999815U (en) | Vertical spiral discharge's domestic waste fermenting installation | |
| CN107460111A (en) | Organic solid castoff processing system and its method of disposal based on subcritical hydrolysis | |
| CN102728603B (en) | Organic matter carbonization catalysis processing technology | |
| CN101289637A (en) | Method for preparing clean fuel derived from sludge | |
| CN104178185A (en) | Kitchen waste pyrolysis treatment technique | |
| CN108911802A (en) | Household composting device | |
| CN201753303U (en) | Steam low-temperature quenching and tempering complete sludge drying device | |
| CN102776123A (en) | Waste continuous solid fermenting reacting device and solid fermenting method | |
| CN208907086U (en) | Household composting device | |
| CN102728604B (en) | Organic matter carbonization catalysis processing device | |
| CN102786997A (en) | Method for preparing solid molding fuel by biogas residues, municipal sludge and straw powder | |
| CN202667236U (en) | Organic matter carbonization catalytic treatment device | |
| CN207514920U (en) | A kind of high-efficiency low-pollution rural garbage disposal plant | |
| CN204769852U (en) | Domestic waste processing system | |
| CN205347174U (en) | Utilize plus sludge drying of living beings and processing apparatus that carbomorphism combined together |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C56 | Change in the name or address of the patentee | ||
| CP03 | Change of name, title or address |
Address after: 110179 Liaoning city of Shenyang Province Hunnan high yinglu No. 8-5 Patentee after: Shenyang Jin Lijie environmental protection Science and Technology Co., Ltd. Address before: 110179 Liaoning Province, Shenyang Hunnan high yinglu No. 8 Patentee before: Shenyang Jinlijie Technology Co., Ltd. |