CN2861769Y - Hydrogen/oil mixed waste incinerator - Google Patents
Hydrogen/oil mixed waste incinerator Download PDFInfo
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- CN2861769Y CN2861769Y CN 200520127234 CN200520127234U CN2861769Y CN 2861769 Y CN2861769 Y CN 2861769Y CN 200520127234 CN200520127234 CN 200520127234 CN 200520127234 U CN200520127234 U CN 200520127234U CN 2861769 Y CN2861769 Y CN 2861769Y
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Abstract
The utility model relates to a hydrogen-oil mixed rubbish incinerator, comprising a pretreatment system, an auxiliary combustion system, a burning system, an exhaust processing system, a cinder disposal system and a computer control system. The pretreatment system is connected with the burning system, the burning system is connected with the exhaust processing system and the auxiliary combustion system separately, the exhaust processing system is connected with the cinder disposal system, the computer control system is connected with the pretreatment system, the burning system, the exhaust processing system, the cinder disposal system and the auxiliary combustion system respectively. The incinerator uses the hydrogen and oxygen released from the hydrogen-oxygen generator as combustion supporting agent. Hydrogen-oxygen treatment and industrial wastes incinerator are applicable to waste burning treatment from industries, hazardous domain and daily living. With the improved auxiliary combustion system, the utility model has the advantages of reduced secondary pollution, operation expense, operation cost, operation risk and treatment cost.
Description
Technical field
The utility model relates to a kind of hydrogen oil mixed waste incinerator.
Background technology
Oil, coal, natural gas burning product are carbon dioxide, are a kind of greenhouse gases, can cause the earth surface temperature to raise year by year.The influence that ecology is caused has obviously injured the existence of animal and plant.Simultaneously, contain impurity in the fossil fuel, particularly dredge, nitrogen, phosphorus, arsenic etc., the product after the burning be an acidity, can pollute and form acid rain to atmosphere.Acid rain not only can hurt the blade of crops and vegetables, and can reduce the germination percentage of crops and vegetable seeds, reduces soy proteinaceous content.Acid rain also can cause sedimentation, the accumulation of toxic metals elements such as a large amount of releases of Aluminium in Soil and magnesium, poisons thereby trees are formed, and the normal biochemical activity of microorganism is disturbed on the top layer that directly influences and endanger soil, makes the fertility decline of soil.Simultaneously, acid rain makes the lake acidifying, the activated aluminum in the soil is flushed in river, the lake, and then poisons fish, changes the ecosystem of whole water body.
State Bureau of Environmental Protection adds up the monitoring result of 2177 environmental monitoring stations in the whole nation 3 years (1991～1993), showing has 62.3% city sulfur dioxide mean annual concentration above national grade ii standard (0.06mg/m3), daily mean of concentration surpasses national grade III Standard (0.225mg/m3), cause year precipitation pH value to be lower than 5.6 acid rain coverage rate and account for 30% of territory, make and ecological environment and economic construction are affected the blast of dust and seriously polluted.At these situations, the environment-friendly type clean energy resource that we must find, and big, the follow-up property of a kind of reserves is strong, the thermal efficiency is high, storage form is many, and a kind of so just high-grade energy of hydrogen energy source.
MSW (MSW) is meant the solid waste that family, business activity, office and industrial department are produced, and must handle, but also can be used for generating and heat supply by the mode of burning or gasify, or produce byproduct---methane (biogas).
Now, MSW is still disposed with the mode of landfill, yet many MSWs can be used to produce electric energy or heat energy in some way, or as regrown material or mixed fertilizer, an only remaining seldom part is by buried processing.The gas that waste guaveyard produced also can be used for produce power, and all countries had carried out demonstration to this.The also obvious difference of calorific value that the home scrap of different regions is contained.The method of the processing solid waste of comparative maturity comprises: hybrid composting, recycling, burning, extract fuel, pyrolysis and hydrolysis from refuse.No matter any in the said method, all need to carry out sorting and preliminary treatment, so that reclaim useful material as far as possible.
The burning solid refuse can cause atmosphere pollution, and some pollutant that is produced should be noted especially, because contain many harmful substances in the exhaust emission that is produced, comprising sulphur, chlorine, fluorine, nitrogen, chlorinated hydrocabon and heavy metal.The pollutant that one group of particular importance is arranged, promptly polychlorinated dibenzo-2 is disliked English (PCDD) and polychlorinated dibenzo (PCDF), may be the most dangerous carcinogenic composition.In the past 10 in the period of, scientists is being carried out a large amount of research work aspect the PCDD/PCDF mechanism of production inquiring into.The purpose of research is in order to seek a kind of method that can reduce or limit the PCDD/PCDF generation.Up to now, control method mainly focuses on: control burning condition, particularly ignition temperature preferably; The time that gas mixes and gas is detained in the combustion zone; The temperature of control boiler gas outlet; The removing of gas after the overheavy firing.
Present medical treatment, the industrial waste incineration stove has all adopted diesel oil, gasoline and natural gas are as single combustion adjuvant, not only in burning process, very easily form secondary pollution, also increased the weight of the operating load of exhaust gas processing device, the operating cost of equipment is also very high in addition, the hydrogen-oxygen medical treatment, the industrial waste incineration stove adopts electrolysis principle, water acts as a fuel, discharge hydrogen in the water outlet and oxygen new forms of energy by electrolysis as incinerator, burn by mixing the back with high-pressure atomization oil, solved various discarded objects with this and in burning process, can produce black smoke because of fuel oil or natural gas, the phenomenon of carbon monoxide and other pernicious gas, greatly reduce medical treatment simultaneously, the operating cost of industrial waste incineration stove, and realized the security and the feature of environmental protection of castoff burning technology.
The utility model content
In order to overcome above-mentioned deficiency, the utility model provides a kind of hydrogen oil mixed waste incinerator, hydrogen that this incinerator produces oxyhydrogen generator and oxygen are applicable to the burning disposal of aspect discarded objects such as industry, dangerous field, life, owing to improved combustion-supporting system as the burning disposal combustion adjuvant, reduce the generation of secondary pollution, thereby avoided second environmental pollution, but energy savings, the cost that reduces operation and handle, reduce operational risk, increase safety coefficient.
The technical solution adopted in the utility model is: above-mentioned hydrogen oil mixed waste incinerator includes preprocessing system, combustion-supporting system, CIU, exhaust treatment system, lime-ash treatment system and computer control system, described preprocessing system is connected with described CIU, this CIU is connected with described combustion-supporting system with described exhaust treatment system respectively, described then exhaust treatment system is connected with described lime-ash treatment system again, described computer control system respectively with described preprocessing system, described CIU, described exhaust treatment system, described lime-ash treatment system is connected with described combustion-supporting system.
Its technological process is: discarded object is stored in the rubbish negative pressure storage pit after collecting, under the Automatic Control of computer, solid waste can enter described CIU through automatic feeder and carry out burning disposal, its flue gas that burns the back generation enters described exhaust treatment system by exhaust gases passes, the lime-ash that burning process produces is handled by described lime-ash treatment system, carry out landfill after to be lime-ash by automatic deslagging device collect, after solidification equipment is handled, can be used for brickmaking at the discarded object that the neutralization reaction tower produces.The described computer control system of this incinerator system whole process using in operation is carried out control operation.
Described preprocessing system includes useless admittedly negative pressure cabin, pretreating device, feed arrangement, waste liquid tank, soil pick-up pump, air-introduced machine, described useless admittedly negative pressure cabin is connected with described air-introduced machine, described soil pick-up pump and described pretreating device respectively, described air-introduced machine is connected with dual firing chamber, described soil pick-up pump is connected to a combustion chamber by described waste liquid tank, described useless admittedly negative pressure cabin is when being connected to described pretreating device, also directly be connected with described feed arrangement, this feed arrangement also includes transmitting device, drying oven and pressure fan.
Its technological process is: the discarded object of collecting is sent into described useless admittedly negative pressure cabin store, in storing process, the biogas of generation and other gas are sent into two burners by described air-introduced machine and are burned; Waste water is stored at described waste liquid tank after described soil pick-up pump is drawn, and sends into then and carries out burning disposal in the rotary kiln; Solid waste is carried out sorting through described pretreating device to solid waste, and discarded object is divided into three classes: the rubbish of the suitable burning disposal of high heating value, the waste product of recyclable utilization and building waste.The recyclable waste product that sorts out leaves salvage station in; The useless rubbish of building is sent into the brickmaking device and is carried out brickmaking; Combustible is transported in the incinerator through automatic feeder, has finished like this combustible is burned preceding pre-treatment.
Described combustion-supporting system includes water tank, electrolytic cell, moisture trap, the hydrogen-oxygen separator, flow regulator, air compressor machine, high-pressure pump, oil storage tank and atomizer, described water tank links to each other with described electrolytic cell by the pump group, described electrolyzer outlet end is connected to the described moisture trap that includes cooler, one end of this moisture trap is connected to described hydrogen-oxygen separator, and draw hydrogen simultaneously at two outputs of this hydrogen-oxygen separator, two gas exhaust pipings of oxygen, be connected respectively to described flow regulator again through the air compressor machine pressurization, be provided with multistage fireproof tempering device in this flow regulator; Described oil storage tank is connected to described atomizer by described high-pressure pump, and this atomizer and described flow regulator together are connected to the ignition device.
Its technological process is: described water tank is connected with described electrolytic cell by the pump group, described electrolyzer outlet end connects described moisture trap, one end of this moisture trap is communicated with described hydrogen-oxygen separator, and draw hydrogen, oxygen gas exhaust piping at two outputs of this hydrogen-oxygen separator, through pressure switch and appliance controller, automatically control air pressure inside, hydrogen-oxygen mixing ratio and gas flame temperature are through flow regulator adjustments of gas flow, after high-pressure atomization oil fully mixes on year-on-year basis, form combustion-supporting flame, control temperature in the stove with specific pressure by two-way.
Described CIU includes a described combustion chamber, described dual firing chamber, flue, automatic deslagging device, atomizer, pressure fan, ignition device.Described air compressor machine is connected respectively to described hydrogen-oxygen separator, in described hydrogen-oxygen seperator and the high-pressure atomization oil, this hydrogen-oxygen separator is connected respectively to a described combustion chamber and a described dual firing chamber by described ignition device, a described combustion chamber is also connected to described dual firing chamber, this combustion chamber is connected with described automatic feeder respectively, described atomizer and described pressure fan, described hydrogen-oxygen seperator and high-pressure atomization oil together are connected to the mixing gas tank, together be connected to described dual firing chamber through auxiliary combustion equipment and described pressure fan again, a described combustion chamber and described dual firing chamber also are connected to described automatic deslagging device together.
Its technological process is: solid waste is transferred to a described combustion chamber through described automatic feeder, and the indoor temperature of this combustion is between 650 ℃～800 ℃, in the oxygen debt roasting of a described indoor realization of combustion.Burning is not very abundant, in the flue gas that forms, just contain a large amount of combustibles that does not all burn like this, this flue gas enters described dual firing chamber by exhaust gases passes, further fully burn, the temperature of described dual firing chamber is between 850 ℃～1300 ℃, burning for the second time reaches the purpose of resolving harmful gas, reduce discharge of harmful gases, combustible in the flue gas is thoroughly burnt, not labile pernicious gas also at high temperature is cracked into gases such as fine solid particle, carbon compound, and PCDF and PCDD are destroyed fully.The biogas of drawing in the negative pressure storage silo and other gas mix the back and spray into by described auxiliary combustion equipment and carry out burning disposal in the described dual firing chamber with hydrogen or oxygen gas, after carrying out second-time burning through described dual firing chamber, enter described exhaust treatment system.
Described exhaust treatment system includes cool-heat-exchanger, alkali lye pond, atomising device, neutralization reaction tower, dry type except that acid tower, deduster, air compressor machine, air-introduced machine, chimney, described alkali lye pond is connected to described neutralization reaction tower by described atomising device, described cool-heat-exchanger is connected to described dry type through this neutralization reaction tower and removes acid tower, this dry type is removed acid tower and described air compressor machine together is connected to described deduster, this deduster also is connected to ash discharging gear with described cool-heat-exchanger together when being connected to described chimney through described air-introduced machine.
Its technological process is: flue gas enters described cool-heat-exchanger from described flue, and rapid quench cools to 200 ℃, has avoided generation polychlorinated dibenzo-2 evil English (PCDD) and polychlorinated dibenzo (PCDF) to form vigorous warm area.The dust of larger particles begins to fall in the cinder catcher of described cool-heat-exchanger under the situation that temperature reduces.So just reduced the processing load of equipment subsequently.Alkali lye in the described neutralization reaction tower is by the abundant combination of the sour gas in described atomising device and the flue gas, and most sour gas has neutralized.Described dry type is removed in the acid tower and remaining sour gas and unnecessary alkali lye, is used for making flue gas to keep dry.Described deduster filters fine solid particle and the particle in the flue gas, and adopts pulsative oscillation that dust is shaken off at ash-collecting port.In the end again with the free from extraneous odour of allow compliance with emission standards, ordorless, smokeless gas through described air-introduced machine by described smoke stack emission to atmosphere.After the discarded object that described neutralization reaction tower produces is handled through solidification equipment, can be used for brickmaking.
Described computer control system not only is connected with described combustion-supporting system with described CIU, described exhaust treatment system, described lime-ash treatment system, also be connected with discarded object storage system, described feed system respectively, described discarded object storage system also is connected to described CIU simultaneously through described feed system and described combustion-supporting system, this CIU is connected to described exhaust treatment system, and this exhaust treatment system also is connected respectively to described lime-ash treatment system and gas emission device.Described computer control system adopts micro computer and fully integrated, total digitalization design, automaticity height, maintenance period are long, its monitoring system adopts infrared measure, the whole service process is comprehensively monitored, for the technology operation provides reliable data parameters, guarantee the stability and the continuation of technology.This monitor adopts the range soft, just can realize by software fully, and have functions such as report printing, status alert.
The disposal ability of this system can be for 15,25,50,100,200,400,500,1000Kg/h, and can do treatment system with coupling according to client's actual treatment amount.
The utility model is the combustion adjuvant that hydrogen that oxyhydrogen generator is produced and oxygen are handled as castoff burning.Can use water purification, and utilize alternating current to convert direct current to, the two poles of the earth with positive and negative polarities conducting electrolytic cell, by the hydrogen-oxygen molecule in the brine electrolysis, discharge hydrogen and oxygen, act as a fuel after the mixing, after mixing with high-pressure atomization oil (diesel oil or gasoline) again, form high pressure-temperature flame, thereby reach combustion-supporting purpose.Hydrogen-oxygen medical treatment, industrial waste incineration stove are applicable to the burning disposal of trade waste, danger wastes, domestic refuse.Owing to improved combustion-supporting system, reduce the generation of secondary pollution, also just reduced the expense of operation, reduced the cost of operation cost, operational risk and processing.
The beneficial effects of the utility model are:
(1) combustion-supporting to replace at present single fuel oil or combustion gas combustion-supporting for hydrogen and oxygen gas mixture that produces with oxyhydrogen machine and high-pressure atomization oil, as the combustion-supporting material of incinerator when discarded object is burned.
(2) adopt the combustion-supporting very big problem of energy resource consumption that has solved the combustion-supporting incinerator of fuel-firing gas-firing of hydrogen and oxygen gas mixture and high-pressure atomization oil.
(3) adopt the combustion-supporting secondary pollution that has realized that discarded object is brought when incinerating use fuel oil or combustion gas of hydrogen and oxygen gas mixture and high-pressure atomization oil, this mist can improve combustion rate 70%, minimizing sulfur dioxide, carbon dioxide reach 45%, save fuel oil 52.5%, can completing combustion and pollution-free, avirulence, nuisanceless, can not produce black smoke because of the situation of any burning and form carbon monoxide.
(4) operating cost is low, utilizes power and water can obtain the combustion-supporting incinerator of hydrogen and oxygen gas mixture, greatly reduces the operating cost of offal treatment.
(5) adopt hydrogen and oxygen gas mixture and high-pressure atomization oil mist can make centralized heat energy, temperature is difficult for diffusion, and the maximum temperature interval is 800 ℃～3000 ℃, and can adjust and be fixed on required temperature.
(6) adopt the hydrogen-oxygen incinerator not need gas bomb, start aerogenesis during use, use automatic air pressure control, the design of multistage anti-backfire, absolute explosion-proof design, avoided traditional incinerator need set up a large-scale potential safety hazard that oil storage tank brought and an inconvenience.
(7) adopt programmable controller (PLC, English full name Programmable LogicController) intellectualizing system, can realize sorting in the past, pass in and out the Automatic Control of expecting burning, exhaust emissions, combustion-supporting system, auxiliary equipment.Its performance safety and stability, operation be reliable, the secondary pollution of having avoided whole system in operation, personnel and surrounding enviroment to be brought, thus increased safety coefficient.
Description of drawings
Fig. 1 is the utility model process flow diagram.
Fig. 2 is the device connection diagram of the utility model preprocessing system.
Fig. 3 is the device connection diagram of the utility model combustion-supporting system.
Fig. 4 is the device connection diagram of the utility model CIU.
Fig. 5 is the device connection diagram of the utility model exhaust treatment system.
Fig. 6 is the device connection diagram of the utility model computer control system.
Symbol description (nothing)
The specific embodiment
Embodiment of the present utility model provides a kind of hydrogen oil mixed waste incinerator, as shown in Figure 1, includes preprocessing system, combustion-supporting system, CIU, exhaust treatment system, lime-ash treatment system and computer control system.Preprocessing system is connected with CIU, and this CIU is connected to exhaust treatment system, imports electricity when water tank is connected to oxyhydrogen machine, in this oxyhydrogen machine, and then is connected to start-up burner.In addition, oil storage tank also is connected to start-up burner by the high-pressure atomization device, and this start-up burner is connected to CIU.Exhaust treatment system is connected to tapping equipment and lime-ash treatment system again simultaneously then.Computer control system is connected with combustion-supporting system with preprocessing system, CIU, exhaust treatment system, lime-ash treatment system respectively.
Discarded object is stored in the rubbish negative pressure storage pit after collecting, under the Automatic Control of computer, solid waste can enter CIU through automatic feeder and carry out burning disposal, its flue gas that burns the back generation enters exhaust treatment system by exhaust gases passes, the lime-ash that burning process produces is handled by the lime-ash treatment system, carry out landfill after to be lime-ash by automatic deslagging device collect, after solidification equipment is handled, can be used for brickmaking at the discarded object that the neutralization reaction tower produces.This incinerator system whole process using computer control system in operation is carried out control operation.
Preprocessing system includes useless admittedly negative pressure cabin, pretreating device, feed arrangement, waste liquid tank, soil pick-up pump, air-introduced machine, admittedly useless negative pressure cabin is connected with air-introduced machine, soil pick-up pump and pretreating device respectively, air-introduced machine is connected with dual firing chamber, the soil pick-up pump is connected to a combustion chamber by waste liquid tank, admittedly useless negative pressure cabin is when being connected to pretreating device, also directly be connected with feed arrangement, this feed arrangement also includes transmitting device, drying oven and pressure fan.The recyclable materials that produces in the pretreating device is deposited separately in addition, and the building waste of its generation is used for brickmaking, and the combustible of its generation is sent in the feed arrangement again.
Its technological process as shown in Figure 2, for: the discarded object of collecting is sent into admittedly useless negative pressure cabin store, in storing process, the biogas of generation and other gas are sent into two burners by air-introduced machine and are burned; Waste water is stored at waste liquid tank after the soil pick-up pump is drawn, and sends into then and carries out burning disposal in the rotary kiln; Solid waste is carried out sorting through pretreating device to solid waste.Discarded object is divided into three classes: the rubbish of the suitable burning disposal of high heating value, the waste product of recyclable utilization and building waste, the recyclable waste product that sorts out leaves salvage station in, the useless rubbish of building is sent into the brickmaking device and is carried out brickmaking, combustible is transported in the incinerator through automatic feeder, has finished like this combustible is burned preceding pre-treatment.
Combustion-supporting system includes water tank, electrolytic cell, moisture trap, hydrogen-oxygen separator, flow regulator, air compressor machine, high-pressure pump, oil storage tank and atomizer, water tank links to each other with electrolytic cell by centrifugal pump, the electrolyzer outlet end is connected to the moisture trap that includes cooler, one end of this moisture trap is connected to the hydrogen-oxygen separator, and draw hydrogen, two gas exhaust pipings of oxygen simultaneously at two outputs of this hydrogen-oxygen separator, be connected respectively to flow regulator again through the air compressor machine pressurization, also be provided with multistage fireproof tempering device in this flow regulator; Oil storage tank is connected to atomizer by high-pressure pump, and this atomizer and flow regulator together are connected to the ignition device.
Its technological process as shown in Figure 3, for: water tank is connected with electrolytic cell by the pump group, the electrolyzer outlet end connects moisture trap, one end of this moisture trap is communicated with the hydrogen-oxygen separator, and draw hydrogen, oxygen gas exhaust piping at two outputs of this hydrogen-oxygen separator, through pressure switch and appliance controller, automatically control air pressure inside, hydrogen-oxygen mixing ratio and gas flame temperature are through flow regulator adjustments of gas flow, after high-pressure atomization oil fully mixes on year-on-year basis, form combustion-supporting flame, control temperature in the stove with specific pressure by two-way.
CIU includes a combustion chamber, dual firing chamber, flue, automatic deslagging device, atomizer, pressure fan, ignition device.Air compressor machine is connected respectively in hydrogen-oxygen separator, hydrogen-oxygen seperator and the high-pressure atomization oil, and this hydrogen-oxygen separator is connected respectively to a combustion chamber and a dual firing chamber after by the ignition device, and this combustion chamber is connected with automatic feeder, atomizer and pressure fan respectively.Hydrogen-oxygen seperator and high-pressure atomization oil together are connected to the mixing gas tank, together are connected to dual firing chamber through auxiliary combustion equipment and pressure fan again.One combustion chamber is also connected to dual firing chamber, combustion chamber and a dual firing chamber and be connected to automatic deslagging device together, and waste material is carried out landfill.Dual firing chamber also is connected to exhaust treatment system by flue.
Its technological process as shown in Figure 4, for: solid waste is transferred to a combustion chamber through automatic feeder, the indoor temperature of this combustion is between 650 ℃～800 ℃, in the oxygen debt roasting of an indoor realization of combustion; Burning is not very abundant, in the flue gas that forms, just contain a large amount of combustibles that does not all burn like this, this flue gas enters dual firing chamber by exhaust gases passes, further fully burn, the temperature of dual firing chamber is between 850 ℃～1300 ℃, burning for the second time reaches the purpose of resolving harmful gas, reduced discharge of harmful gases, combustible in the flue gas is thoroughly burnt, not labile pernicious gas also at high temperature is cracked into gases such as fine solid particle, carbon compound, and PCDF and PCDD are destroyed fully; The biogas of drawing in the negative pressure storage silo and other gas mix the back and spray into by auxiliary combustion equipment and carry out burning disposal in the dual firing chamber with hydrogen or oxygen gas, after carrying out second-time burning through dual firing chamber, enter exhaust treatment system.
Exhaust treatment system includes cool-heat-exchanger, alkali lye pond, atomising device, neutralization reaction tower, dry type except that acid tower, deduster, air compressor machine, air-introduced machine, chimney.The alkali lye pond is connected to the neutralization reaction tower by atomising device, cool-heat-exchanger is connected to dry type through this neutralization reaction tower and removes acid tower, this dry type is removed acid tower and air compressor machine together is connected to sack cleaner, this sack cleaner also is connected to ash discharging gear with described cool-heat-exchanger together when being connected to chimney through air-introduced machine.The neutralization reaction tower is sent into reacted discarded object in the solidification equipment again, and the refuse that this solidification equipment is produced can be used for brickmaking with building waste again.
Its technological process as shown in Figure 5, for: flue gas enters cool-heat-exchanger from flue, and rapid quench cools to 200 ℃, has avoided the generation polychlorinated dibenzo-2 to dislike English (PCDD) and polychlorinated dibenzo (PCDF) forms vigorous warm area; The dust of larger particles begins to fall in the cinder catcher of cool-heat-exchanger under the situation that temperature reduces, and has so just reduced the processing load of equipment subsequently; Alkali lye in the neutralization reaction tower is by the abundant combination of the sour gas in atomising device and the flue gas, and most sour gas has neutralized; Dry type is removed in the acid tower and remaining sour gas and unnecessary alkali lye, is used for making flue gas to keep dry; Deduster filters fine solid particle and the particle in the flue gas, and adopts pulsative oscillation that dust is shaken off at ash-collecting port; In the end again with the free from extraneous odour of allow compliance with emission standards, ordorless, smokeless gas through air-introduced machine by smoke stack emission to atmosphere.After the discarded object that the neutralization reaction tower produces is handled through solidification equipment, can be used for brickmaking.
Computer control system is connected with combustion-supporting system with discarded object storage system, feed system, CIU, exhaust treatment system, lime-ash treatment system respectively, the discarded object storage system also is connected to CIU simultaneously through feed system and combustion-supporting system, this CIU is connected to exhaust treatment system, this exhaust treatment system also is connected respectively to lime-ash treatment system and gas emission device, as shown in Figure 6.Computer control system adopts micro computer and fully integrated, total digitalization design, automaticity height, maintenance period are long, its monitoring system adopts infrared measure, the whole service process is comprehensively monitored, for the technology operation provides reliable data parameters, guarantee the stability and the continuation of technology.This monitor adopts the range soft, just can realize by software fully, and have functions such as report printing, status alert.
The disposal ability of this incinerator can be for 15,25,50,100,200,400,500,1000Kg/h, and can do treatment system with coupling according to client's actual treatment amount.
Though with specific embodiment the present invention is described, have the knack of this skill person will know clearly can claims define below not breaking away from spirit of the present invention and scope in implement variations and modifications.No matter but it does any variation on shape or structure, the modification that every employing present technique is made all drops within the protection domain of the present utility model.
Claims (6)
1. hydrogen oil mixed waste incinerator, it is characterized in that, include preprocessing system, combustion-supporting system, CIU, exhaust treatment system, lime-ash treatment system and computer control system, described preprocessing system is connected with described CIU, this CIU is connected with described combustion-supporting system with described exhaust treatment system respectively, described then exhaust treatment system is connected with described lime-ash treatment system again, described computer control system respectively with described preprocessing system, described CIU, described exhaust treatment system, described lime-ash treatment system is connected with described combustion-supporting system.
2. hydrogen oil mixed waste incinerator as claimed in claim 1, it is characterized in that, described preprocessing system includes useless admittedly negative pressure cabin, pretreating device, feed arrangement, waste liquid tank, the soil pick-up pump, air-introduced machine, described useless admittedly negative pressure cabin respectively with described air-introduced machine, described soil pick-up pump and described pretreating device connect, described air-introduced machine is connected with dual firing chamber, described soil pick-up pump is connected to a combustion chamber by described waste liquid tank, described useless admittedly negative pressure cabin is when being connected to described pretreating device, also be connected with described feed arrangement, this feed arrangement also includes transmitting device, drying oven and pressure fan.
3. hydrogen oil mixed waste incinerator as claimed in claim 1, it is characterized in that, described combustion-supporting system includes water tank, electrolytic cell, moisture trap, the hydrogen-oxygen separator, flow regulator, air compressor machine, high-pressure pump, oil storage tank and atomizer, described water tank links to each other with described electrolytic cell by the pump group, described electrolyzer outlet end is connected to the described moisture trap that includes cooler, one end of this moisture trap is connected to described hydrogen-oxygen separator, and draw hydrogen simultaneously at two outputs of this hydrogen-oxygen separator, two gas exhaust pipings of oxygen, be connected respectively to described flow regulator again through the air compressor machine pressurization, be provided with multistage fireproof tempering device in this flow regulator; Described oil storage tank is connected to described atomizer by described high-pressure pump, and this atomizer and described flow regulator together are connected to the ignition device.
4. hydrogen oil mixed waste incinerator as claimed in claim 1, it is characterized in that, described CIU includes a described combustion chamber, described dual firing chamber, flue, automatic deslagging device, atomizer, pressure fan, the ignition device, described air compressor machine is connected respectively to described hydrogen-oxygen separator, in described hydrogen-oxygen seperator and the high-pressure atomization oil, this hydrogen-oxygen separator is connected respectively to a described combustion chamber and a described dual firing chamber by described ignition device, a described combustion chamber is also connected to described dual firing chamber, this combustion chamber is connected with described automatic feeder respectively, described atomizer and described pressure fan, described hydrogen-oxygen seperator and high-pressure atomization oil together are connected to the mixing gas tank, together be connected to described dual firing chamber through auxiliary combustion equipment and described pressure fan again, a described combustion chamber and described dual firing chamber also are connected to described automatic deslagging device together.
5. hydrogen oil mixed waste incinerator as claimed in claim 1, it is characterized in that, described exhaust treatment system includes cool-heat-exchanger, the alkali lye pond, atomising device, the neutralization reaction tower, dry type is removed acid tower, deduster, air compressor machine, air-introduced machine, chimney, described alkali lye pond is connected to described neutralization reaction tower by described atomising device, described cool-heat-exchanger is connected to described dry type through this neutralization reaction tower and removes acid tower, this dry type is removed acid tower and described air compressor machine together is connected to described deduster, and this deduster is connected to described chimney through described air-introduced machine.
6. hydrogen oil mixed waste incinerator as claimed in claim 1, it is characterized in that, described computer control system is connected with discarded object storage system, described feed system respectively, described discarded object storage system also is connected to described CIU simultaneously through described feed system and described combustion-supporting system, this CIU is connected to described exhaust treatment system, and this exhaust treatment system is also connected to described lime-ash treatment system.
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200520127234 CN2861769Y (en) | 2005-10-12 | 2005-10-12 | Hydrogen/oil mixed waste incinerator |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200520127234 CN2861769Y (en) | 2005-10-12 | 2005-10-12 | Hydrogen/oil mixed waste incinerator |
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| CN2861769Y true CN2861769Y (en) | 2007-01-24 |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103353116A (en) * | 2013-07-01 | 2013-10-16 | 广东博海昕能环保有限公司 | Automatic combustion control system |
| CN105114958A (en) * | 2015-09-28 | 2015-12-02 | 长沙卡特尔环保科技有限公司 | Garbage incinerator using hydrogen and oxygen mixed gas |
| WO2020118756A1 (en) * | 2018-12-13 | 2020-06-18 | 中国电子科技集团公司第十三研究所 | Inflammable waste combustion and disposal device |
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2005
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103353116A (en) * | 2013-07-01 | 2013-10-16 | 广东博海昕能环保有限公司 | Automatic combustion control system |
| CN105114958A (en) * | 2015-09-28 | 2015-12-02 | 长沙卡特尔环保科技有限公司 | Garbage incinerator using hydrogen and oxygen mixed gas |
| WO2020118756A1 (en) * | 2018-12-13 | 2020-06-18 | 中国电子科技集团公司第十三研究所 | Inflammable waste combustion and disposal device |
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