CN204803012U - System for moisture organic matter pyrolysis production active carbon - Google Patents
System for moisture organic matter pyrolysis production active carbon Download PDFInfo
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- CN204803012U CN204803012U CN201520239842.2U CN201520239842U CN204803012U CN 204803012 U CN204803012 U CN 204803012U CN 201520239842 U CN201520239842 U CN 201520239842U CN 204803012 U CN204803012 U CN 204803012U
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Abstract
The utility model provides a system for moisture organic matter pyrolysis production active carbon, include: preprocessing device, radiant tube revolving bed pyrolysis oven, the oil -gas separation device, pyrolysis oil storage tank, pyrolysis gas buffer tank, wherein, radiant tube revolving bed pyrolysis oven links to each other with preprocessing device, and the oil -gas separation device links to each other with radiant tube revolving bed pyrolysis oven, and pyrolysis gas buffer tank links to each other with the oil -gas separation device, and pyrolysis oil storage tank links to each other with the oil -gas separation device. The utility model discloses the system for moisture organic matter pyrolysis production active carbon flow of above -mentioned embodiment is short, the running cost is low, and resourceization, the energyization are competent, and product economic benefits is good, and secondary pollution is few, easily realizes industrialization and scale.
Description
Technical field
The utility model belongs to organism recycling field, and specifically, the utility model relates to the system that gac is produced in water-bearing organic pyrolysis.
Background technology
Solid organic matters pyrolytic technique is high with its resource utilization rate, the advantage that environmental pollution is little and more and more favor by people.Pyrolysis primary product has following several: 1. inflammable gas, comprises some low-molecular-weight hydrocarbons as hydrogen, methane, carbon monoxide etc., generally uses as fuel gas, is the main products that pyrolysis produces economic worth; 2. pyrolysis oil, a part of pyrolysis oil is used by the refining oil fuel that can be used as; 3. pyrolytic carbon: rubbish charcoal major part with carbon black form exist, can be used as solid fuel use also can mix mud etc. of heating up water, but due to partial thermal decomposition charcoal calorific value not high, market value is lower, finds no sale.
The pyrolytic process flow process of current employing is generally and organism is obtained the dry pyrolysis feed with certain particle diameter through pre-treatment, pre-treatment comprises sorting, broken, drying, shaping etc., pyrolysis feed enters pyrolysis oven again and reacts, three kinds of products that reaction produces are collected respectively, again the product collected further is purified respectively, refining etc., finally obtain product.This technique overall flow is long, complex procedures, and product can not directly as product utilization, and process energy utilization rate is low.Especially for the organism of high-moisture percentage, high-moisture percentage organism comprises domestic refuse, mud, biomass, low-rank coal etc., its water ratio is generally between 20%-60%, if dry before carrying out pyrolytic reaction, shaping, require that stove is dried to water ratio outward and be less than 10%, process energy consumption is large, a large amount of water vapour of simultaneously drying generation are discharged in air the waste causing water vapour, if raw material is domestic refuse, and the solid waste such as mud, water vapor also can carry stink, and need carry out deodorizing process could qualified discharge.According to this technical process, be difficult to produce economic benefit, industrialization promotion difficulty.
Utility model content
The utility model is intended to solve one of technical problem in correlation technique at least to a certain extent.For this reason, an object of the present utility model is to propose the system that gac is produced in a kind of water-bearing organic pyrolysis.
According to an aspect of the present utility model, the utility model proposes the system that gac is produced in a kind of water-bearing organic pyrolysis, comprising:
Pretreatment unit;
Radiator tube rotating bed pyrolysis oven, described radiator tube rotating bed pyrolysis oven comprises:
Housing, described housing forms ring-type furnace chamber;
Cloth stone or metal plate for standing a stove on as a precaution against fire, described cloth stone or metal plate for standing a stove on as a precaution against fire is positioned at the bottom of described ring-type furnace chamber rotationally;
Multiple radiator tube, multiple described radiator tube is arranged on the internal perisporium of described housing;
Drive unit, described drive unit is arranged on the below of described housing and is connected with described cloth stone or metal plate for standing a stove on as a precaution against fire, to drive described cloth stone or metal plate for standing a stove on as a precaution against fire to rotate;
Multiple partition wall, multiple described partition wall is stretched out downwards by the roof of described housing and keeps certain distance with described cloth stone or metal plate for standing a stove on as a precaution against fire, described ring-type furnace chamber is divided into dry chamber adjacent successively by multiple described partition wall, pyrolysis chamber and activation chamber, wherein, the bottom of two often adjacent chambers is connected, described dry chamber has opening for feed and high-temperature oil gas outlet, described activation chamber has activator entrance and gac outlet, wherein, described opening for feed is connected with described pretreatment unit, described radiator tube rotating bed pyrolysis oven is suitable for described raw material to carry out drying treatment, pyrolysis processing and activation treatment, so that the high-temperature oil gas obtained containing water vapour and gac,
Gas and oil separating plant, described gas and oil separating plant exports with described high-temperature oil gas and is connected, and is suitable for carrying out gas-oil separation process, to obtain pyrolysis oil and pyrolysis gas to the described high-temperature oil gas containing water vapour;
Pyrolysis oil storage tank, described pyrolysis oil storage tank is connected with described gas and oil separating plant and is suitable for storing described pyrolysis oil;
Pyrolysis gas surge tank, described pyrolysis gas surge tank is connected with described gas and oil separating plant and is suitable for storing described pyrolysis gas.
Discarded organism can be finally converted into recycling pyrolysis gas, gac and tar by the system adopting the water-bearing organic pyrolysis of the utility model above-described embodiment to produce gac, wherein pyrolysis gas calorific value is high, can do civilian and industrial fuel gas, the prosperity of gac mesopore can use in sewage disposal or gas sweetening.In whole system, major equipment is pyrolysis oven, only adopts pyrolysis oven to get final product a step and completes drying, pyrolysis, activation.Thus, the system adopting the water-bearing organic pyrolysis of the utility model above-described embodiment to produce gac processes organism, and technical process is short, running cost is low; resource utilization, energy level are high; product economy is profitable, and secondary pollution is few, is easy to realize industrialization and mass-producing.
In embodiments more of the present utility model, described pyrolysis gas surge tank is connected with the fuel inlet of described radiator tube rotating bed pyrolysis oven, so that using the fuel of described pyrolysis gas as described radiator tube rotating bed pyrolysis oven.
Accompanying drawing explanation
Fig. 1 is the structural representation producing the system of gac according to the water-bearing organic pyrolysis of an embodiment of the present utility model.
Fig. 2 is the structural representation producing the radiator tube rotating bed pyrolysis oven in the system of gac according to the water-bearing organic pyrolysis of an embodiment of the present utility model.
Fig. 3 is the structural representation producing the system of gac according to the water-bearing organic pyrolysis of another embodiment of the present utility model.
Fig. 4 is the schema producing the method for gac according to the water-bearing organic pyrolysis of an embodiment of the present utility model.
Embodiment
According to an aspect of the present utility model, the utility model proposes the system that gac is produced in a kind of water-bearing organic pyrolysis.As shown in Figure 1, comprise according to the system of the water-bearing organic pyrolysis production gac of the utility model specific embodiment: pretreatment unit 10, radiator tube rotating bed pyrolysis oven 20, gas and oil separating plant 30, pyrolysis oil storage tank 40, pyrolysis gas surge tank 50.
According to specific embodiment of the utility model, pretreatment unit 10 is suitable for carrying out sorting and break process to organism, to obtain median size not higher than the raw material of 20 millimeters.
According to specific embodiment of the utility model, as shown in Figure 2, radiator tube rotating bed pyrolysis oven 20 comprises: housing 21, cloth stone or metal plate for standing a stove on as a precaution against fire (not shown), multiple radiator tube (not shown), drive unit (not shown), multiple partition wall 22.Wherein, housing 21 forms ring-type furnace chamber, cloth stone or metal plate for standing a stove on as a precaution against fire is positioned at the bottom of ring-type furnace chamber rotationally, multiple radiator tube is arranged on the internal perisporium of housing 21, drive unit is arranged on the below of housing 21 and is connected with cloth stone or metal plate for standing a stove on as a precaution against fire, to drive cloth stone or metal plate for standing a stove on as a precaution against fire to rotate, multiple partition wall 22 is stretched out downwards by the roof of housing 21 and keeps certain distance with cloth stone or metal plate for standing a stove on as a precaution against fire, ring-type furnace chamber is divided into dry chamber 23 adjacent successively by multiple partition wall 22, pyrolysis chamber 24 and activation chamber 25, wherein, the bottom of two often adjacent chambers is connected, dry chamber 23 has opening for feed and 231 high-temperature oil gas outlet 232, activation chamber 25 has activator entrance 251 and gac outlet 252, wherein, opening for feed 231 is connected with pretreatment unit 10, radiator tube rotating bed pyrolysis oven 20 is suitable for raw material to carry out drying treatment, pyrolysis processing and activation treatment, so that the high-temperature oil gas obtained containing water vapour and gac.
According to specific embodiment of the utility model, gas and oil separating plant 30 and high-temperature oil gas export 232 and are connected, and are suitable for carrying out gas-oil separation process to the high-temperature oil gas containing water vapour, to obtain pyrolysis oil and pyrolysis gas.
According to specific embodiment of the utility model, pyrolysis oil storage tank 40 is connected with gas and oil separating plant 30 and is suitable for storing pyrolysis oil.
According to specific embodiment of the utility model, pyrolysis gas surge tank 50 is connected with gas and oil separating plant 30 and is suitable for store heat and vents one's spleen.
The water-bearing organic pyrolysis of the utility model above-described embodiment is adopted to produce the system of gac, first enter in radiator tube rotating bed pyrolysis oven after adopting pretreatment unit that organism is carried out simple pre-treatment and carry out pyrolysis, drying, pyrolysis and activation treatment is completed respectively by the dry chamber in radiator tube rotating bed pyrolysis oven, pyrolysis chamber and activation chamber, generate high-temperature oil gas and gac, further by the pyrolysis oil that utilizes gas and oil separating plant 30 high-temperature oil gas to be converted into can to recycle and pyrolysis gas.Discarded organism can be finally converted into recycling pyrolysis gas, gac and tar by said system of the present utility model, wherein pyrolysis gas calorific value is high, can do civilian and industrial fuel gas, the prosperity of gac mesopore can use in sewage disposal or gas sweetening.In whole system, major equipment is pyrolysis oven, only adopts pyrolysis oven to get final product a step and completes drying, pyrolysis, activation.Thus, the system adopting the water-bearing organic pyrolysis of the utility model above-described embodiment to produce gac processes organism, and technical process is short, running cost is low; resource utilization, energy level are high; product economy is profitable, and secondary pollution is few, is easy to realize industrialization and mass-producing.
According to specific embodiment of the utility model, as shown in Figure 3, the system of the water-bearing organic pyrolysis production gac of above-described embodiment can further include: gas collector 60, gas collector 60 exports 232 with the high-temperature oil gas being positioned at dry chamber 23 top and is connected, and is suitable for the high-temperature oil gas produced in pyrolysis chamber and activation chamber and water vapour by being collected after dry chamber.And then the temperature from pyrolysis chamber and activation chamber can be utilized to carry out heat treated higher than the high-temperature flue gas of drying chamber indoor and water vapour to the material of drying chamber indoor, part energy consumption can be saved thus.
According to specific embodiment of the utility model, the system of the water-bearing organic pyrolysis production gac of above-described embodiment can further include: recirculation blower 70, recirculation blower 70 is connected with activator entrance 251 with gas collector 60 respectively, so that the high-temperature oil gas of utilization containing water vapour is used for the activation treatment in activation chamber 25 as activator.The high-temperature oil gas component loops of collection can be passed back into rotating bed pyrolysis oven thus, both also used as the adjusting control agent improving gaseous constituent as activator, in order to make the high-temperature oil gas of circulation be uniformly distributed, the flitch of furnace bottom selects perforation plate.And then this part is passed into bottom body of heater flitch from the high-temperature oil gas of drying zone, through reaction mass, and with pyrolysis after the charcoal that generates react, form hole, there are methane steam reforming reaction, water-gas shift reaction, coke steam reforming reaction, Boudouard reaction etc. simultaneously, improve gas yield further.
According to specific embodiment of the utility model, pyrolysis gas surge tank 50 is connected with the fuel inlet of radiator tube rotating bed pyrolysis oven, using the fuel of pyrolysis gas as radiator tube rotating bed pyrolysis oven, can save part energy consumption thus.According to specific embodiment of the utility model, pyrolysis gas surge tank 50 is also connected with pyrolysis gas storage tank 51, so that using the fuel of a part of pyrolysis gas as radiator tube rotating bed pyrolysis oven, rest part is as production marketing.
According to specific embodiment of the utility model, the temperature of the drying chamber indoor in radiator tube rotating bed pyrolysis oven 20 is 300-400 degree Celsius, and then can dry raw material organism fully, temperature in pyrolysis chamber is 600-800 degree Celsius, and then pyrolysis can be carried out to the raw material organism after oven dry further, and generate high-temperature oil gas and fixed carbon, temperature in activation chamber is 850-950 degree Celsius, can activate the fixed carbon that pyrolysis obtains further thus, obtain the gac of mesopore prosperity, according to specific embodiment of the utility model, said system can further include gac collection device 80, for collecting and storing activated carbon product.
According to specific embodiment of the utility model, be can 50-250 millimeter by the thickness of raw material cloth in radiator tube rotating bed pyrolysis oven.Specifically suitably can adjust according to concrete pending organic type, the efficiency of drying, pyrolysis and activation treatment can be improved thus further.According to specific embodiment of the utility model, the time that cloth stone or metal plate for standing a stove on as a precaution against fire rotates a circle in described radiator tube rotating bed pyrolysis oven is 1.5-3.5 hour.The time of namely carrying out drying treatment, pyrolysis processing and activation treatment in radiator tube rotating bed pyrolysis oven is total up to 1.5-3.5 hour.Therefore, above-mentioned system cycle organism being produced activated carbon of the present utility model is short, and efficiency is high, and energy consumption is low, can significantly reduce costs.
Describing in detail below with reference to Fig. 4 adopts the water-bearing organic pyrolysis of the utility model embodiment to produce the system of gac by the method for water-bearing organic pyrolysis production gac.
The method of producing gac according to the water-bearing organic pyrolysis of the utility model specific embodiment comprises: organism is carried out sorting, break process, to obtain median size not higher than the raw material of 20 millimeters; Described raw material is carried out drying treatment, pyrolysis processing and activation treatment in radiator tube rotating bed pyrolysis oven, so that the high-temperature oil gas obtained containing water vapour and gac; The described high-temperature oil gas containing water vapour is carried out gas-oil separation process, to obtain pyrolysis oil and pyrolysis gas.
The water-bearing organic pyrolysis of the utility model above-described embodiment is adopted to produce the method for gac, enter after organism is carried out simple pre-treatment in radiator tube rotating bed pyrolysis oven and carry out pyrolysis, drying, pyrolysis and activation treatment is completed respectively by the drying zone in radiator tube rotating bed pyrolysis oven, pyrolysis zone and region of activation, generate high-temperature oil gas and gac, high-temperature oil gas is converted into the pyrolysis oil that can recycle and pyrolysis gas further.Above-mentioned processing method the finished product of the present utility model are pyrolysis gas, gac and tar, and wherein pyrolysis gas calorific value is high, can do civilian and industrial fuel gas, and the prosperity of gac mesopore can use in sewage disposal or gas sweetening.Whole technique, mainly carrying out in same pyrolysis oven, completes the object of drying, pyrolysis, activation, raising gas yield.Thus, the method technical process of the water-bearing organic pyrolysis production gac of the utility model above-described embodiment is short, running cost is low, and resource utilization, energy level are high, and product economy is profitable, and secondary pollution is few, are easy to realize industrialization and mass-producing.
The employing water-bearing organic pyrolysis describing the utility model embodiment below with reference to Fig. 4 in detail produces the system of gac by the method for water-bearing organic pyrolysis production gac.
First organism is carried out pre-treatment, pre-treatment comprises sorting and break process.According to specific embodiment of the utility model; the pending organism of the utility model can be at least one in domestic refuse, mud, biomass and low-rank coal; all there is the higher moisture of 20-65%; high-moisture percentage organic matter pyrolysis technique due to overall energy utilization rate low, deficiency in economic performance and be difficult to realize industrialization and mass-producing.The existing organism for these high-moistures, more the pretreatment mode adopted first adopt repeatedly to dehydrate at present, such as, high pressure pyrolysis, expansion drying and mummification etc.If but dry in pre-treatment, need to consume a large amount of heat smoke, and the steam vapour amount of drying generation is also very large, also the smell is awful for some, and needing to remove stink could discharge, and therefore make whole pretreated process energy consumption large, running cost is high.And the utility model only adopts simple sorting and fragmentation in preprocessing process, oven dry part is put in rotating bed pyrolysis oven and carries out, effectively can solve drying course thus and need a large amount of heat smoke, and extra setting removes the problem of stink facility, and then significantly save energy consumption.
According to specific embodiment of the utility model, the raw material with certain particle diameter is obtained by sorting and pre-treatment, pre-treatment adopts different pretreatment modes according to the difference of raw material, if domestic refuse then needs to carry out sorting and fragmentation, by bulk inorganics wherein, metals etc. separate, if biomass or low-rank coal then only need break process, if mud does not then need process can yet.Eventually pass pre-treatment to need to obtain the raw material that particle diameter is not more than 20 millimeters.
According to specific embodiment of the utility model, further, above-mentioned raw materials is carried out drying treatment, pyrolysis processing and activation treatment in radiator tube rotating bed pyrolysis oven, so that the high-temperature oil gas obtained containing water vapour and gac.According to specific embodiment of the utility model, above-mentioned radiator tube rotating bed pyrolysis oven has dry district, pyrolysis zone and region of activation, the above-mentioned raw materials obtained through pre-treatment is fed by front end, drying zone, and along with the rotation of radiator tube rotating bed pyrolysis oven, successively drying treatment, pyrolysis processing and activation treatment are carried out to raw material, so that the high-temperature oil gas obtained containing water vapour and gac.
According to specific embodiment of the utility model, the temperature in drying zone is 300-400 degree Celsius, and Main Function is dried by the moisture in raw material, and the origin of heat of oven dry is radiator tube radiative transfer, the high-temperature oil gas in stove in radiant heat and stove.Pyrolysis zone temperature 600-800 degree Celsius has been the main reaction region of pyrolysis, and the raw material through drying continues to be warmed reaction and generates high-temperature oil gas and solid carbon; Region of activation temperature 850-950 degree Celsius, the solid carbon that pyrolysis zone generates completes the gac that priming reaction generates mesopore prosperity in this region.
According to specific embodiment of the utility model, be can 50-250 millimeter by the thickness of raw material cloth in radiator tube rotating bed pyrolysis oven.Specifically suitably can adjust according to concrete pending organic type, the efficiency of drying, pyrolysis and activation treatment can be improved thus further.According to concrete example of the present utility model, the time of carrying out drying treatment, pyrolysis processing and activation treatment in radiator tube rotating bed pyrolysis oven is total up to 1.5-3.5 hour, and the time that namely radiator tube rotating bed pyrolysis oven rotates a circle is 1.5-3.5 hour.Therefore, the above-mentioned method cycle of organism being produced activated carbon of the present utility model is short, and efficiency is high, and energy consumption is low, can significantly reduce costs.
According to specific embodiment of the utility model, the high-temperature flue gas that pyrolysis processing and activation treatment can also be produced and water vapour are used for drying treatment.Particularly, high-temperature oil gas outlet can be only set on the top of drying zone, be discharged after the high-temperature flue gas produced in pyrolysis zone and region of activation thus and water vapour need to enter drying zone, and then the temperature from pyrolysis zone and region of activation can be utilized to carry out heat treated higher than the high-temperature flue gas in drying zone and water vapour to the material in drying zone.Part energy consumption can be saved thus.
According to specific embodiment of the utility model, the high-temperature oil gas containing water vapour of generation in drying zone can also be utilized as activator for the activation treatment in region of activation.Particularly, circulation gas entrance can be set at the furnace wall of the bottom being positioned at region of activation, the high-temperature oil gas component loops of collection is passed back into rotating bed pyrolysis oven, both also used as the adjusting control agent improving gaseous constituent as activator, in order to make the high-temperature oil gas of circulation be uniformly distributed, the flitch of furnace bottom selects perforation plate.And then this part is passed into bottom body of heater flitch from the high-temperature oil gas of drying zone, through reaction mass, and with pyrolysis after the charcoal that generates react, form hole, there are methane steam reforming reaction, water-gas shift reaction, coke steam reforming reaction, Boudouard reaction etc. simultaneously, improve gas yield further.
According to specific embodiment of the utility model, in pyrolysis oven, oven dry and stove are dried energy consumption difference outward and are mainly the energy Q that water vapour consumes
water vapour, because the gasification latent heat of water is very large, Q
water vapourheat only accounts for about 25% of total energy consumption.Therefore, after this part water vapour produced drying zone is collected, part is used for high-temperature activation section, not only reduce the intensification energy consumption of activated water steam, eliminate a large amount of flue gas of extra process simultaneously and carry out deodorizing process to flue gas, therefore aforesaid method overall operation expense of the present utility model is lower.
According to specific embodiment of the utility model, further, the above-mentioned high-temperature oil gas containing water vapour of discharging in radiator tube rotating bed pyrolysis oven is carried out gas-oil separation process, to obtain pyrolysis oil and pyrolysis gas.And then effective recycling can be carried out to the high-temperature oil gas containing water vapour.According to concrete example of the present utility model, can also using the fuel of pyrolysis gas obtained above as radiator tube rotating bed pyrolysis oven.Part energy consumption can be saved thus, reduce costs.
The water-bearing organic pyrolysis of the utility model above-described embodiment is adopted to produce the method for gac, enter after organism is carried out simple pre-treatment in radiator tube rotating bed pyrolysis oven and carry out pyrolysis, complete drying, pyrolysis and activation treatment respectively by drying zone, pyrolysis zone and region of activation, generate high-temperature oil gas and gac.High owing to entering the organic matter raw material water ratio after stove, be rich in water vapour in the high-temperature oil gas of generation, this gas part circulation melted down, the activator as region of activation uses, and a part of cooling and purifying obtains high heating value pyrolysis gas and tar.A high heating value pyrolysis gas part provides the energy as the fuel gas of pyrolysis oven for pyrolysis, and remainder is as production marketing.Above-mentioned processing method the finished product of the present utility model are pyrolysis gas, gac and tar, and wherein pyrolysis gas calorific value is high, can do civilian and industrial fuel gas, and the prosperity of gac mesopore can use in sewage disposal or gas sweetening.Whole technique, mainly carrying out in same pyrolysis oven, completes the object of drying, pyrolysis, activation, raising gas yield.Thus, the method technical process of the water-bearing organic pyrolysis production gac of the utility model above-described embodiment is short, running cost is low, and resource utilization, energy level are high, and product economy is profitable, and secondary pollution is few, are easy to realize industrialization and mass-producing.
According to specific embodiment of the utility model, discarded organism is prepared into pyrolytic carbon by existing technical matters usually, and pyrolytic carbon is low as fuel value, and price is low, and market outlet is bad.Middle for discarded organism preparation is generated the gac of mesopore prosperity by the utility model, can be used for waste water, off gas treatment, and then effectively transforms organic waste in order to the higher gac of economic value added.
The system adopting the water-bearing organic pyrolysis of the utility model above-described embodiment to produce gac can reach following technique effect:
(1) adopt radiator tube rotating bed pyrolysis oven as main equipment, in same stove, complete drying, pyrolysis, the process of activation, flow process is short, and energy utilization rate is high, is easy to amplify simultaneously, realizes mass-producing;
(2) only carry out simple pre-treatment, oven dry part be put in radiator tube rotating bed pyrolysis oven and carry out, solving drying course needs a large amount of heat smoke, needs separately to establish the problem removing stink facility;
(3) pyrolytic carbon directly activates in stove, two steps of activation is completed in same stove, generates the gac of mesopore prosperity, this gac can be used for waste water, off gas treatment, solve pyrolytic carbon low as fuel value, the predicament that price is low, improve its economic value added;
(4) effectively utilize the water vapour of drying and producing, while carrying out activating, improve the output of pyrolysis gas;
(5) solve high-moisture percentage organic matter pyrolysis deficiency in economic performance, be difficult to a difficult problem for industrialization and mass-producing.
Embodiment 1
Employing Domestic Waste In Beijing is raw material, msw water content 54%, becomes to be grouped into as table 1:
Table 1 domestic refuse becomes to be grouped into (wt%)
The rubbish entering factory removes bulk inorganics and metal through simple sorting, then carries out fragmentation, the refuse pyrolysis raw material particle size < 20mm that fragmentation obtains;
Broken rubbish is evenly carried out cloth in radiator tube rotating bed pyrolysis oven, fabric thickness is 100mm, in stove, rubbish completes reaction with the rotation of furnace bottom through super-dry, pyrolysis, activation, wherein drying zone temperature 350 degrees Celsius, pyrolysis zone temperature 800 degrees Celsius, region of activation temperature 900 degrees Celsius, overall treatment time is 2 hours;
Radiator tube rotating bed pyrolysis oven is the main equipment realizing this process, and it comprises housing, cloth stone or metal plate for standing a stove on as a precaution against fire, multiple radiator tube, drive unit, multiple partition wall.Its furnace bottom is rotating ring-shaped furnace bottom, and radiant tube burner is arranged on the internal perisporium of housing, and being vented one's spleen by the combustion heat provides refuse pyrolysis institute heat requirement in thermal-radiating mode, and the flue gas in radiator tube and the atmosphere in rotating bed completely cut off.Pyrolysis oven is divided into three chambers by partition wall, and be dry chamber, pyrolysis chamber and activation chamber respectively, material is fed by dry chamber front end, arranges pneumatic outlet at the furnace roof place of dry chamber, for collecting the steam-laden oil gas of high temperature; The bottom furnace wall of activation chamber arranges circulation gas entrance, the high-temperature oil gas component loops of collection is passed back into rotating bed, both also used as the adjusting control agent improving gaseous constituent as activator, be uniformly distributed to make the high-temperature oil gas of circulation, the flitch of furnace bottom selects perforation plate, in region of activation, end sets out materials device, collects activated carbon product;
The high-temperature oil gas part of the moisture vapor collected is recycled the activator entrance that blower fan is back to activation chamber and uses as activator, another part is after cooling and purifying, obtain pyrolysis oil and pyrolysis gas, wherein pyrolysis oil is stored in pyrolysis oil storage tank, as production marketing.Pyrolysis gas is stored in pyrolysis gas surge tank, and wherein a part is as being connected with radiant tube burner with pipeline by press device, and as the postcombustion of radiant tube burner, rest part is as production marketing;
The sealed discharging machine of the gac generated through being positioned at activation chamber end is discharged, and obtains activated carbon product after cooling.
The product yield obtained is in table 2, and wherein pyrolysis gas calorific value is 4600kcal/Nm
3:
Table 2 product yield (wt% butt)
The Properties of Activated Carbon parameter obtained is in table 3
Table 3 Properties of Activated Carbon parameter
Embodiment 2
Adopt Beijing's dewatered sludge to be raw material, moisture percentage in sewage sludge 60%, its technical analysis and calorific value are in table 4:
Table 4 Beijing sludge industrial is analyzed and calorific value
Enter factory's mud not need in radiator tube rotating bed pyrolysis oven, to carry out cloth with carrying out pre-treatment Direct Uniform, fabric thickness 200mm, in stove, mud completes reaction with the rotation of furnace bottom through super-dry, pyrolysis, activation, wherein drying zone temperature 400 degrees Celsius, pyrolysis zone temperature 700 degrees Celsius, region of activation temperature 850 degrees Celsius, 3 hours reaction times;
Radiator tube rotating bed pyrolysis oven is the main equipment realizing this process, and concrete structure and function apply the description with embodiment 1.Material is fed by front end, drying zone, arranges pneumatic outlet at the furnace roof place of drying zone, for collecting the steam-laden oil gas of high temperature; In the body of heater side of bottom, region of activation, circulation gas entrance is set, the high-temperature oil gas component loops of collection is passed back into rotating bed, both also used as the adjusting control agent improving gaseous constituent as activator, be uniformly distributed to make the high-temperature oil gas of circulation, the flitch of furnace bottom selects perforation plate, in region of activation, end sets out materials device, collects activated carbon product;
The high-temperature oil gas part of the moisture vapor collected is recycled the gas inlet that blower fan is back to region of activation and uses as activator, and another part, after cooling and purifying, obtains pyrolysis oil and pyrolysis gas, and wherein pyrolysis oil is stored in oil tank, as production marketing.Pyrolysis gas is stored in gas tank, and wherein a part is as being connected with radiant tube burner with pipeline by press device, and as the postcombustion of radiant tube burner, rest part is as production marketing;
The sealed discharging machine of the gac generated through being positioned at region of activation end is discharged, and obtains activated carbon product after cooling.
The product production obtained is in table 5, and wherein the calorific value of pyrolysis gas is 4300kcal/Nm
3:
Table 5 product yield (wt% butt)
The Properties of Activated Carbon parameter obtained is in table 6.
Table 6 Properties of Activated Carbon parameter
In the utility model, unless otherwise clearly defined and limited, the term such as term " installation ", " being connected ", " connection ", " fixing " should be interpreted broadly, and such as, can be fixedly connected with, also can be removably connect, or integral; Can be mechanical connection, also can be electrical connection; Can be directly be connected, also indirectly can be connected by intermediary, can be the connection of two element internals or the interaction relationship of two elements.For the ordinary skill in the art, the concrete meaning of above-mentioned term in the utility model can be understood as the case may be.
In the utility model, unless otherwise clearly defined and limited, fisrt feature second feature " on " or D score can be that the first and second features directly contact, or the first and second features are by intermediary indirect contact.And, fisrt feature second feature " on ", " top " and " above " but fisrt feature directly over second feature or oblique upper, or only represent that fisrt feature level height is higher than second feature.Fisrt feature second feature " under ", " below " and " below " can be fisrt feature immediately below second feature or tiltedly below, or only represent that fisrt feature level height is less than second feature.
In the description of this specification sheets, specific features, structure, material or feature that the description of reference term " embodiment ", " some embodiments ", " example ", " concrete example " or " some examples " etc. means to describe in conjunction with this embodiment or example are contained at least one embodiment of the present utility model or example.In this manual, to the schematic representation of above-mentioned term need not for be identical embodiment or example.And the specific features of description, structure, material or feature can combine in one or more embodiment in office or example in an appropriate manner.In addition, when not conflicting, the feature of the different embodiment described in this specification sheets or example and different embodiment or example can carry out combining and combining by those skilled in the art.
Although illustrate and described embodiment of the present utility model above, be understandable that, above-described embodiment is exemplary, can not be interpreted as restriction of the present utility model, those of ordinary skill in the art can change above-described embodiment, revises, replace and modification in scope of the present utility model.
Claims (2)
1. a system for gac is produced in water-bearing organic pyrolysis, it is characterized in that, comprising:
Pretreatment unit;
Radiator tube rotating bed pyrolysis oven, described radiator tube rotating bed pyrolysis oven comprises:
Housing, described housing forms ring-type furnace chamber;
Cloth stone or metal plate for standing a stove on as a precaution against fire, described cloth stone or metal plate for standing a stove on as a precaution against fire is positioned at the bottom of described ring-type furnace chamber rotationally;
Multiple radiator tube, multiple described radiator tube is arranged on the internal perisporium of described housing;
Drive unit, described drive unit is arranged on the below of described housing and is connected with described cloth stone or metal plate for standing a stove on as a precaution against fire, to drive described cloth stone or metal plate for standing a stove on as a precaution against fire to rotate;
Multiple partition wall, multiple described partition wall is stretched out downwards by the roof of described housing and keeps certain distance with described cloth stone or metal plate for standing a stove on as a precaution against fire, described ring-type furnace chamber is divided into dry chamber adjacent successively by multiple described partition wall, pyrolysis chamber and activation chamber, wherein, the bottom of two often adjacent chambers is connected, described dry chamber has opening for feed and high-temperature oil gas outlet, described activation chamber has activator entrance and gac outlet, and wherein, described opening for feed is connected with described pretreatment unit;
Gas and oil separating plant, described gas and oil separating plant exports with described high-temperature oil gas and is connected;
Pyrolysis oil storage tank, described pyrolysis oil storage tank is connected with described gas and oil separating plant;
Pyrolysis gas surge tank, described pyrolysis gas surge tank is connected with described gas and oil separating plant.
2. the system of gac is produced in water-bearing organic pyrolysis according to claim 1, and it is characterized in that, described pyrolysis gas surge tank is connected with the fuel inlet of described radiator tube rotating bed pyrolysis oven.
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| CN201520239842.2U CN204803012U (en) | 2015-04-20 | 2015-04-20 | System for moisture organic matter pyrolysis production active carbon |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105665423A (en) * | 2016-03-22 | 2016-06-15 | 北京神雾环境能源科技集团股份有限公司 | System and method for disposing household waste |
| CN105861013A (en) * | 2016-06-22 | 2016-08-17 | 北京神雾环境能源科技集团股份有限公司 | Pulverized coal pyrolysis dust collecting system internally provided with cyclone dust collector and particle sortable particle bed |
| CN106391673A (en) * | 2016-11-30 | 2017-02-15 | 北京神雾环境能源科技集团股份有限公司 | System and method for treating household garbage |
-
2015
- 2015-04-20 CN CN201520239842.2U patent/CN204803012U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105665423A (en) * | 2016-03-22 | 2016-06-15 | 北京神雾环境能源科技集团股份有限公司 | System and method for disposing household waste |
| CN105861013A (en) * | 2016-06-22 | 2016-08-17 | 北京神雾环境能源科技集团股份有限公司 | Pulverized coal pyrolysis dust collecting system internally provided with cyclone dust collector and particle sortable particle bed |
| CN106391673A (en) * | 2016-11-30 | 2017-02-15 | 北京神雾环境能源科技集团股份有限公司 | System and method for treating household garbage |
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