CN114263908A - Integrated heat energy recycling process for removing dust, sulfur and nitrate from garbage cutting preheating incineration steam - Google Patents

Integrated heat energy recycling process for removing dust, sulfur and nitrate from garbage cutting preheating incineration steam Download PDF

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CN114263908A
CN114263908A CN202111119138.XA CN202111119138A CN114263908A CN 114263908 A CN114263908 A CN 114263908A CN 202111119138 A CN202111119138 A CN 202111119138A CN 114263908 A CN114263908 A CN 114263908A
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water
garbage
steam
cylinder
heat energy
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崔学发
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Abstract

The invention provides a waste cutting preheating incineration steam dust removal and denitration integrated heat energy recycling process. Comprises the following steps: mechanical intelligent linear cutting garbage plastic bag wrapping and roller sorting garbage plastic recycling device. The recovered combustible garbage is preheated and dried in the furnace body and then is incinerated. The heat generated by burning the garbage is utilized to convert water and ammonia liquid into gaseous ammonia and water vapor in a heating mode. Under the condition of no catalyst, gaseous ammonia and steam are utilized to generate nitrogen oxide and sulfur dioxide by burning garbage, and the whole process is tracked and captured from the burning to the ending. The water vapor is converted into water body and water body wrapped with smoke particles through a cooling measure, so that the smoke particles are purified and dedusted indiscriminately. Filtering water body particles, and performing concentrated solidification treatment on waste residues; in the water body, the ammonia sulfite is oxidized into ammonium sulfate crystals as a byproduct. By utilizing the incineration heat energy, a device for pressing garbage plastics into brick and tile building materials and a device for converting the garbage plastics into heavy oil are arranged.

Description

Integrated heat energy recycling process for removing dust, sulfur and nitrate from garbage cutting preheating incineration steam
Technical Field
The invention relates to a waste cutting, preheating and burning steam dust removal and desulfurization nitrate integrated heat energy recycling process. The device is particularly suitable for household garbage of families and households in cities and villages, cutting, recovering and incinerating garbage plastic and combustible materials, cooling, dedusting, denitrating, desulfurizing smoke generated by incineration, adsorbing and purifying harmful gas particulate matter steam, and recycling the incineration heat energy of the garbage plastic and the combustible materials.
Background
The household garbage is produced by every household, and due to living habits of residents, various wastes are often wrapped by plastic bags, particularly kitchen residues wrapped by the garbage plastic bags, so that great difficulty and cost are increased for garbage plastic recycling and utilization. The current method for classifying, recycling and treating garbage plastics and combustible materials comprises the following steps: the garbage is mainly subjected to integral crushing, a large amount of plastic is crushed into small fragments, and the small plastic is often separated out and cannot be recycled in the screening process. Especially, sand, bricks, tiles and glass bottles in the garbage cause serious damage to machine equipment. The garbage is crushed integrally, so that a large amount of kitchen residues are adhered to the surfaces of garbage plastics and combustible materials, the water content and oil pollution impurities of the plastics are greatly increased, the load and cost of screening work are increased, and the incineration difficulty is increased. In addition, the heat generated by burning the garbage is not fully utilized, the recycling opportunity of garbage plastics is lost, and the carbon emission is increased. On the other hand, in the process of burning the garbage, a large amount of harmful gas can be generated. At present, the device for denitration, desulfurization and dust removal of flue gas by burning garbage has unsatisfactory effect and high operation cost.
Disclosure of Invention
In order to overcome the defects in the prior art, the invention provides a waste cutting, preheating and burning steam dedusting, desulfurization and nitre integrated heat energy recycling process. The related device comprises: (1) a mechanical intelligent linear cutting garbage plastic bag wrapping and roller sorting garbage plastic recycling combined device; (2) a waste preheating, drying and burning flue gas steam purification gas phase denitration and desulfurization integrated heat energy recycling device; (3) a device for purifying flue gas particles by cooling water body and desulfurizing by liquid phase steam; (4) a conical filter body dust removal centrifugal force dehydration device; (5) the anaerobic hot-melting garbage plastic pressing brick and tile building material heat energy recycling device; (6) an anaerobic cracking garbage plastic conversion heavy oil heat energy recycling device.
The garbage cutting preheating incineration steam dedusting and desulfurization nitre integrated heat energy recycling process relates to (1) contents related to mechanical intelligent linear cutting garbage plastic bag wrapping and roller combined recovery device:
comprises the following steps: the device comprises a roller, a fixed jacket, a fixed bolt, a push-pull rod, a power steel saw blade, a fixed steel saw blade, a torsion spring connecting rod rotating shaft, a connecting shaft, a floating wheel, a fan, a charging opening and a protective plate.
The method is characterized in that: the front end of the roller is provided with a charging opening, the lower end of the charging opening is provided with a fixed steel saw blade cutting tool, the fixed steel saw blade cutting tool is connected with a rotating shaft of a torsion spring connecting rod, and the fixed steel saw blade is provided with a guard plate at the upper part and the lower part; the push-pull rod is arranged in a jacket on the inner wall of the roller, a push-pull rod fixing bolt is arranged on the push-pull rod fixing jacket, two equivalent power steel saw blades are arranged on the inner wall of the roller in parallel, floating wheels are arranged at the bottoms of two ends of the roller, and the roller is provided with an inclination angle.
The garbage cutting preheating incineration steam dust removal desulfurization nitre integrated heat energy recycling process relates to (1) mechanical intelligent linear cutting garbage plastic bag wrapping and roller combined recovery device, and the technical scheme adopted for solving the technical problem is as follows:
in order to smoothly open the garbage plastic bag, various wastes are scattered from the plastic bag package, in particular to bricks, tiles, stones and glass bottles which do not need to be cut and crushed. The invention adopts a linear cutting garbage plastic bag device, which integrates the garbage plastic cutting and garbage plastic sorting and recycling. In order to prevent the garbage from winding machine equipment, in particular to solve the difficult problems of broken stones, tiles, glass bottles, hard objects and the like in the garbage. A mechanical automatic avoiding device is arranged on the cutting tool, and the automatic avoiding device can generate automatic avoiding capability when the cutting tool is used for cutting the hard objects. In order to achieve the automatic avoiding capability of the cutter, the cutting cutter is arranged at the feed inlet end of the roller, a push-pull rod and a steel saw blade are arranged on the wall of the roller by virtue of the rotary power generated when the roller is used for sorting and recovering the garbage plastic, and the garbage plastic bag is driven by the arranged steel saw blade and the push-pull rod to complete the linear cutting task. The steel saw blades are arranged in a double-row parallel structure, so that the damage resistance of cutting of the cutter is improved, and the garbage plastic bag is better driven to complete a linear cutting task. The garbage surface is linearly cut by utilizing the fixed steel saw blade arranged on the roller, and the garbage plastic bag is cut to scatter the wastes in the bag, so that the classification recycling task is completed. After the garbage plastic bags are driven out by the push-pull rod and the steel saw blade, the cut garbage plastic bags are blown away by wind power and recovered when the garbage plastic bags continuously and automatically slide off from the push-pull rod and the steel saw blade under the action of gravity along with the rotation of the roller, and garbage of other heavy objects is screened, classified and recovered by the roller. A fixed steel saw blade cutter for cutting plastic bags is installed on a shaft, and connecting rods are arranged at two ends of the shaft and are coaxially connected with torsion springs in a fixed and movable mode. When the push-pull rod and the steel saw blade push and pull the garbage out from the lower part of the fixed steel saw blade, if the fixed steel saw blade cutter touches a hard object, an upward thrust is generated on the steel saw blade cutter, when the thrust is greater than the torque force on the torque spring and the connecting rod arranged on the steel saw blade, the fixed steel saw blade drives the connecting rod to be lifted upwards, and after the hard object passes through, the fixed steel saw blade returns to the original position under the action of the torque spring and the gravity, and the garbage cutting task is continuously completed. The cutting tool who sets up has realized that the machinery is intelligent avoids hard object ability, has prevented that hard object from causing destruction to mechanical device. When the cutting tools meet hard objects such as broken stones, tiles and glass bottles which do not need to be cut, the hard objects can be removed through the set distance by the set distance between the tools. In order to fully utilize the effect of the acute-angle cutting surface of the steel saw blade cutter, the friction sheet is arranged on the steel saw blade rotating shaft, when the steel saw blade finishes a cutting task, the steel saw blade can rotate under the dragging of garbage, the acute angle is exposed to increase the cutting efficiency, the service life of the cutter is prolonged, and the garbage can be prevented from being wound or wrapping the acute angle of the cutter. The steel saw blade cutting tool who sets up can become the degree according to every steel saw blade wearing and tearing and just trades, sets up the push rod on the cylinder, can maintain or change every push rod through the bolt of adjustment setting at the push rod fixation clamp cover.
The garbage cutting, preheating, burning, steam dedusting, desulfurizing and nitre integrated heat energy recycling process relates to (1) a mechanical intelligent linear cutting garbage plastic bag wrapping and roller combined recovery device has outstanding advantages and beneficial and obvious effects.
1. The steel saw blade tool and the push-pull rod are not required to be manufactured and processed separately, so that the manufacturing cost is greatly reduced. 2. And carrying out linear cutting on the surface of the waste plastic by utilizing the acute angle of the steel saw blade. The minimal contact area of the acute angle of the cutter is utilized to generate strong penetrating power to the surface of an object. Greatly reducing the cutting friction resistance and saving the motor power. The production cost is reduced. Compared with the three-dimensional cutting and crushing, the cost and the electric energy are saved by more than sixty percent. 3. The linear cut maintains the integrity of the waste debris, particularly kitchen residue waste. The linear cutting is carried out on the garbage, and the advantages are provided for the subsequent screening, cracking and gasification of the garbage. Unnecessary loads of subsequent work of screening, pyrolysis and gasification are greatly reduced, and the water content of the garbage plastic is reduced. 4. The linear cutting machine can generate large cutting force, is time-saving and labor-saving, greatly improves the working efficiency, and has simple mechanical structure, easy manufacture and long service life. 5. By adopting linear cutting, the cutters have sufficient space, the movement resistance is reduced, the cutters move linearly, the problem of winding garbage is solved, and the cutting work efficiency is improved. 6. The cutter that sets up can avoid automatically to need cutting hard object, has realized the mechanical intelligent protection machine equipment ability, has improved equipment life, makes cutting efficiency obtain improving by a wide margin. 7. Through the distance of setting for between the cutter, equipment can not produce the extrusion force during the cutting rubbish, can make broken brick rubble glass bottle pass through cutting device smoothly again, has prevented that hard object from causing the destruction to cutting device. 8. The push-pull rod arranged on the roller is matched with the steel saw blade, so that the garbage sorting and cutting are integrated, the mechanical manufacturing cost is greatly saved, the structure is extremely simple, the manufacturing is easy, the power loss is low, the wear resistance and the fatigue resistance are realized, and the service life is long. 9. The arranged cutting steel saw blade and the push-pull rod can be adjusted and replaced at any time and any place, the maintenance is convenient, the cost is saved, and the energy consumption is greatly reduced.
The garbage cutting preheating incineration steam dedusting and desulfurization and denitration integrated heat energy recycling process relates to (2) the garbage preheating drying incineration flue gas steam purification gas phase denitration and desulfurization integrated heat energy recycling device relates to the following contents:
comprises the following steps: the incinerator charging opening, the automatic turnover cover plate, the automatic control turnover cover plate device, the turnover baffle plate, the automatic control turnover baffle plate device, the high-temperature gas heating channel, the reducing agent heater, the steam pipeline, the steam outlet, the gaseous ammonia pipeline, the gaseous ammonia outlet, the steam control valve, the steam water tank, the ammonia liquid control valve, the ammonia liquid water tank, hang frame automatic material conveying controlling means, hang frame net row, the trip shaft, hang frame upset connecting rod, the rope, the lantern ring, the furnace door, the fan, combustion-supporting gas pipeline, the gas control valve, the U-shaped grate, the incinerator body, the heat energy recycles the device, the high-temperature gas passageway.
The method is characterized in that: the upper end of the incineration furnace is provided with a charging hopper, and the upper end of the charging hopper is provided with an automatic overturning cover plate device; the automatic turnover cover plate device is provided with a motor, and a turnover cover plate is arranged on a motor transmission shaft; the lower end of the charging opening is provided with an automatic overturning baffle device, the automatic overturning baffle device is provided with a motor, and a motor transmission shaft is provided with an overturning baffle; a plurality of layers of hanging frames are arranged above the furnace body, and each hanging frame consists of two corresponding net rows; the net rows are formed by combining steel pipes or steel bars, and overturning shafts are arranged at two ends of the net rows of the hanging frame; a hanging frame overturning connecting rod is arranged on the overturning shaft and is arranged on the outer side of the incinerator body; the two overturning connecting rods are connected through a rope on the overturning connecting rods arranged on the two sides of the hanging frame, a lantern ring is arranged in the middle of the rope, and the lantern ring is connected with the rope on the motor concave wheel; a U-shaped fire grate is arranged below the incinerator body, an induced draft pipeline and a gas control valve are arranged below the U-shaped fire grate, and a furnace door is arranged at the corresponding position of the U-shaped fire grate; the reducing agent heater and the water vapor heater are arranged in the high-temperature gas channel; the reducing agent heater and the water vapor heater are both composed of a calandria; the reducing agent gaseous ammonia outlet is arranged at the flue gas outlet of the high-temperature gas channel and the bottom of the incinerator; the water vapor outlet is arranged in the flue gas pipeline at the bottom of the incinerator and behind the heat energy recycling device, and a fan is arranged in front of the water vapor outlet arranged in the flue gas pipeline; the ammonia water liquid tank and the steam water chamber are arranged above the high-temperature gas channel, and liquid flow control valve devices are arranged on the pipelines of the ammonia water liquid chamber and the steam water chamber; the outlet of the high-temperature gas channel is provided with a temperature measuring instrument, and the high-temperature gas channel is internally provided with a heat energy recycling device.
The technical scheme adopted by the garbage cutting preheating incineration steam dedusting and desulfurization and denitration integrated heat energy recycling process comprises the following steps of (2) garbage preheating drying incineration flue gas steam purification gas phase denitration and desulfurization integrated heat energy recycling device:
in order to reuse the heat energy of the garbage combustible. Especially, the high-temperature incineration of the garbage combustible materials with high water content is completed, the multilayer hanging frame is arranged above the furnace body, the garbage combustible materials with high water content are placed in the hanging frame, and the garbage combustible materials in the hanging frame are quickly evaporated by utilizing the heat generated by the incineration of the garbage, so that the combustible materials are preheated at high temperature. After the garbage combustible in the hanging frame is preheated and dried, the garbage combustible is thrown into a combustion area of the furnace body to be incinerated. The arrangement of the hanging frame solves the problem of high water content of the garbage combustible. Especially, the hanging frame is arranged at the lowest layer and is closest to flame, when the garbage combustible in the hanging frame at the lowest layer is subjected to high temperature and is about to reach the combustion degree, a power supply signal is input into the automatic unloading device of the hanging frame, the rope for controlling the turnover connecting rod is put down, the garbage combustible in the hanging frame automatically falls onto the U-shaped fire grate under the action of self gravity, and when the garbage plastic is put onto the U-shaped fire grate, the garbage plastic can be immediately combusted. And an overturning connecting rod arranged outside the furnace body on the hanging frame shaft plays a role in lever control. The garbage combustible is mainly plastic. The combustion of plastics is divided into two stages, namely a volatilization stage at about 200 ℃, the combustion is mainly completed by a delinking depolymerization reaction to release a large amount of heat, and the weight loss rate reaches 99% when the combustion is about 500 ℃. The hydrocarbons do not fix carbon. Only volatile components, a combustion stage and a burnout stage. Therefore, when the plastic is completely burned, the heat source is immediately lost, and the high temperature capability is difficult to form. In order to solve the problem of sustainable combustion of garbage combustible and increase the temperature accumulation capacity. The bottom of the incinerator is provided with a U-shaped fire grate as a combined body. On one hand, the U-shaped grate increases the incineration ventilation area; the ventilation area is increased by more than 50 percent compared with the plane grate. On the other hand, the U-shaped grate structure enables the garbage combustibles to be mutually gathered. The flames can mutually form radiation to generate high temperature to form accumulated temperature. The U-shaped grate structure makes up the problem that the garbage combustible does not have fixed carbon. The U-shaped grate structure provides conditions for continuous combustion of garbage combustible materials. The U-shaped furnace has large exhaust air volume, and provides guarantee for providing oxygen-enriched combustion of the garbage combustible. When the garbage plastic is burnt under the oxygen-rich condition, the generation of dioxin can be reduced firstly. Secondly, the gas components of the garbage putrefactive organic matters can be decomposed at high temperature. When the garbage combustible is burnt under the conditions of high temperature and oxygen enrichment, the generation of sulfur dioxide can be effectively reduced. When the temperature of the flue gas outlet reaches above 850 ℃, dioxin is prevented from being synthesized in the later combustion stage. In order to control the temperature condition of the furnace body, temperature monitors are arranged at different positions in the furnace body to provide data for controlling the waste incineration. Due to the combustible materials of the garbage, the garbage is combusted under the condition of oxygen enrichment. Therefore, the nitrogen oxide component in the smoke is greatly increased. In order to solve the problem, a selective catalytic reduction method is adopted for denitration and desulfurization of flue gas under the condition of not using a catalyst. Reducing agent: ammonia, urea. The advantages are that: no secondary pollution, and is nontoxic and pollution-free nitrogen and water. The sulfur dioxide in the flue gas can be removed by an ammonia method. In the prior art, ammonia method is used for denitration, and ammonia water liquid is atomized and mixed with flue gas after a high temperature window of 850 ℃ to 1200 ℃ is selected. By adopting the denitration method, the effect of reducing the nitrogen oxide by 50 to 60 percent can be achieved. In order to solve the problem that the prior denitration method is low in efficiency: the first method is to convert liquid ammonia into gaseous ammonia and water vapor by heating liquid reducing agent (ammonia water, urea liquid) with a heater. Secondly, a two-stage denitration measure is adopted for the waste incineration by utilizing gaseous ammonia and water vapor. The reducing agent heater is arranged in the high-temperature gas channel and is of a pipe arrangement structure. In order to prevent the waste from burning to generate excessive nitrogen oxides and sulfur dioxide from the source. The first section of ammonia method adopts the method that a reducing agent (gaseous ammonia and steam) outlet is arranged at the lower bottom of a U-shaped furnace exhaust, the gaseous ammonia and the steam enter a garbage combustion area, and the gaseous ammonia reducing agent, the steam and the garbage are burnt synchronously. When the gaseous ammonia reducing agent and the waste incineration are carried out synchronously, the reducing agent is enabled to capture the generation of the nitrogen oxides synchronously from the waste incineration source. Reducing agent and steam are added into the garbage for burning in the first time. When a large amount of water vapor and ammonia gas enter the garbage plastic combustion area, the generation conditions of nitrogen oxides and sulfur dioxide are fundamentally restrained. The ammonia steam and the water vapor enter a garbage combustion high-temperature area together, so that the gas-phase ammonia and the nitrogen oxide form a rapid reaction under the high-temperature condition of the reducing agent, and the utilization efficiency of the ammonia (urea) is improved. In order to solve the problem that the proportion of nitrogen oxide in flue gas is high (70 to 80 percent) in the oxygen-enriched incineration of garbage. In order to better improve the denitration efficiency of the ammonia process, a two-stage denitration method measure is adopted. And a second reducing agent outlet is arranged at the position of the high-temperature gas outlet of the incinerator. The flue gas outlet end of the incinerator is also provided with a gaseous ammonia reducing agent outlet. When the flue gas in the furnace body is concentrated at the flue gas outlet, the gaseous ammonia is utilized to form reduction reaction with the nitrogen oxide in the flue gas again. After the flue gas is subjected to secondary denitration, the denitration efficiency of the flue gas is greatly improved, and the nitrogen oxides in the flue gas are basically reduced. By utilizing the measures of gaseous ammonia (urea) two-stage denitration, the problem of low liquid-phase denitration efficiency of the ammonia process is effectively solved, and the ammonia process denitration achieves the best effect. The method for reducing nitrogen oxides by using an ammonia method provides favorable and convenient conditions for steam dust removal. In the process of burning the garbage, the reducing agent and the water vapor are added, which plays a key role in preventing the generation of dioxin. Especially, the reducing agent outlet is arranged at the position of the flue gas outlet of the incinerator, so that the secondary synthesis of dioxin is effectively prevented. The denitration and desulfurization liquid chamber and the steam water tank are arranged above the high-temperature gas channel. The denitration and desulfurization liquid (ammonia water and urea) tank and the steam water tank enable the ammonia water liquid (urea liquid) to automatically enter the heater to generate gaseous ammonia and water vapor through the control valve under the condition of no external force. The proportion of amine (urea) and water is according to the data fed back by nitrogen oxide monitor set at the back end of flue gas pipeline. The water vapor heater arranged in the high-temperature gas channel makes full use of the heat of burning garbage, removes dust by using water vapor, enables smoke particles and achieves the purpose of undifferentiated purification. In order not to influence the denitration and desulfurization by the ammonia process, the steam outlet is arranged at the rear end of the high-temperature gas channel, and in order to fully mix the steam and the flue gas, the fan is arranged at the steam outlet and automatically rotates under the driving of the flue gas, so that the flue gas and the steam are mixed. In order to perfect the furnace body in the initial stage of burning, the flue gas is purified. The reducing agent heater and the water vapor heater are provided with temporary heating devices to finish the tasks of dust removal, denitration and desulfurization of flue gas generated by combustion at the initial stage of the furnace body.
The garbage cutting preheating incineration steam dedusting and desulfurization and denitration integrated heat energy recycling process relates to (2) a garbage preheating drying incineration flue gas steam purification gas phase denitration and desulfurization integrated heat energy recycling device, and has the outstanding advantages and the beneficial and obvious effects.
1. Utilize the space above the furnace body to set up multilayer multiunit and hang the frame, hang the frame with the rubbish combustible substance that water content is high packing into, before letting the rubbish combustible substance burn, preheat the dry mode in the furnace body in advance for rubbish plastics and combustible substance water content, contain miscellaneous quality and be difficult problem thoroughly to solve. 2. The garbage plastic and the combustible materials are sequentially fed in the incinerator through the hanging frame, the combustion effect reaches virtuous circle in the incinerator body, and the heat energy generated by combustion of the garbage combustible materials reaches the optimal ideal effect. The heat energy is fully reused for providing steam power generation, boiler heating, conversion of garbage plastics into heavy oil and garbage plastic hot-melting brick and tile building materials. 3. The incinerator charging hole is arranged above the furnace body, an automatic feeding control device is adopted, the smoke gas is prevented from leaking, and the labor intensity of workers is reduced. The automatic control system realizes an automatic capability and greatly saves labor force and cost. 4. Set up multilayer multiunit and hang the frame, orderly throw the material mode, be about to reach the combustion state when the rubbish combustible substance, at the reinforced mode that drops into, for the improvement burns rubbish combustible substance, the sustained combustion generates high temperature, has reached an optimum ideal effect. 5. The air intake is controlled by arranging the induced air pipeline and the valve at the bottom of the furnace, and favorable conditions are provided for oxygen required by waste incineration through induced air and fermented bean air. 6. The arrangement of the U-shaped fire grate increases the ventilation area by more than 50 percent compared with a plane furnace body, greatly improves the incineration efficiency, and meets the two characteristics of a volatilization stage and a burnout stage when plastics are combusted from solid to liquid. Namely, the phenomenon that the liquid is easy to accumulate when the temperature is low during combustion of the garbage plastic is prevented. But also solves the problem of ventilation required by the garbage plastics during combustion. The U-shaped fire grate can promote garbage plastics and combustible materials to complete the combustion task under the condition of oxygen enrichment, and lays a foundation for the reutilization of heat energy. 7. The arrangement structure of the U-shaped fire grate can gather loose garbage plastics, generate flames which radiate each other, and provide conditions for sustainable combustion of the plastics. The U-shaped grate structure makes up the problem of sustainable combustion of plastic under the condition that garbage plastic and combustible materials do not have fixed carbon and cannot form a stable heat source. The U-shaped grate ensures that the garbage combustible is always in a high-temperature state to complete the incineration task, and plays a key role in preventing the generation of dioxin. 8. Aiming at the problems of oxygen-enriched incineration of garbage and increase of nitrogen oxides, and in order to improve the problem of low denitration efficiency of an ammonia method, the method adopts the method that heat generated by incinerating the garbage is utilized to convert liquid ammonia into gaseous ammonia and water vapor in a heating mode. A two-stage method technical scheme is adopted for flue gas denitration by utilizing gas-phase ammonia and water vapor. Under the condition of no catalyst, gaseous ammonia and water vapor are utilized, and nitrogen oxides and sulfur dioxide are captured in the whole process from waste incineration to incineration. By utilizing the gas-phase ammonia two-stage denitration and desulfurization mode, the denitration efficiency is greatly improved. 9. The ammonia liquid urea liquid compartment is arranged at the upper end of the high-temperature gas channel, so that the ammonia liquid automatically enters the heater, the structure is simple, and the cost is greatly saved. 10. By adopting the method for denitration and desulfurization of gaseous ammonia and water vapor, the gaseous ammonia can be fully mixed with the flue gas nitrogen oxides, and the ammonia liquid is efficiently utilized. 11. The method for restraining nitrogen oxides and sulfides in the incineration waste by utilizing the gaseous ammonia and the water vapor is simple, effective and low in cost, and does not generate secondary pollution. 12. In the process of burning the garbage, gaseous ammonia and water vapor participate in the whole process of burning the garbage. Water vapor plays a critical role in preventing the generation of dioxin. Particularly, the reducing agent is arranged at the position of the flue gas outlet, and the water vapor prevents the chance of secondary synthesis of dioxin after the garbage is completely converted into flue gas after the garbage is burnt. 13. The method for wrapping harmful gas and fine particles in the flue gas by using the water vapor promotes the surfaces of dust, tar and harmful gas with various small molecular structure types in the flue gas to generate water, and the water promotes the surface area increase and the volume increase of the fine particles in the flue gas. The method for wrapping the smoke by the water body is utilized to enable all particles of the smoke to achieve the purpose of indiscriminate removal. 14. The self heat of the furnace body is utilized to convert water into steam for dedusting, the cost is low, the water is saved, and a steam dedusting method simulates a purification mode of flue gas in a natural state. 15 temporary heating devices are arranged on the reducing agent heater and the water vapor heater, so that the problems of smoke, denitration and desulfurization generated when the garbage is in a primary combustion state are solved.
The garbage cutting preheating incineration steam dedusting and desulfurizing nitre integrated heat energy recycling process relates to (3) the contents of the water body cooling liquid phase desulfurizing steam flue gas particulate matter purifying device, which relate to:
comprises the following steps: the device comprises a cooling box, an air inlet, an air outlet, a water body, a cooling water tank, a cooling calandria, a grid water blocking plate, a sealing door, a water storage tank, a cone filtering screen, an acid-base water body monitor, a water pump, a water outlet, a torsion spring hinge and a water baffle.
The method is characterized in that: the cooling box is provided with an air inlet and an air outlet, the upper end of the cooling box is provided with a cooling water tank, the lower end of the cooling water tank is provided with a cooling pipe communicated with the cooling water tank, and the middle position of the cooling pipe is provided with a grid water baffle; a lower water port is arranged at the bottom of the cooling box, and a torsion hinge is arranged at the lower water port to form sealing connection with the water baffle; below the breakwater, be provided with the tank, the tank is provided with the cone and crosses the screen of considering into, is provided with sour alkali water monitor in the tank, still is provided with the water pump in the filter, and the output pipeline on the water pump links to each other with the ammonium sulfite crystallization tank, and the cooling box is provided with sealing door.
The garbage cutting preheats and burns the integrated heat energy of steam dust removal desulfurization nitre and recycle process and involve (3) water cooling liquid phase desulfurization steam purification flue gas particulate matter device, the technical scheme that its solution technical problem adopted:
water is the best material for cooling. The cooling pipe is arranged in the cooling box body, and when a large amount of water vapor (ammonia gas) wraps various objects of flue gas and penetrates through the cooling exhaust pipe, the water vapor is cooled and then is converted into liquid from gas. When the water vapor is converted from gas to liquid, all objects in the flue gas are wrapped by the body of water. Various objects in the flue gas can be wrapped by the water body, and water body mixed aggregates are formed on the wall of the cooling pipe. The mixed aggregate that is wrapped up in by the water and is carried, the mouth of a river under the continuous entering cooling box, when a large amount of water gathers the mouth of a river under the entering cooling box, when water aggregate weight, exceeded when the mouth of a river sets up torque spring's power down, water aggregate will seal the breakwater and open and get into the tank, the tank has set up the multichannel and has crossed the worry, and water aggregate carries out deep level at the tank and crosses the worry. In order to increase the dust removal capacity, the grid water baffle plates are arranged between the cooling pipes, when steam enters the grid water baffle plates, the movement speed of the flue gas (steam) is accelerated, the water bodies collide with each other to form a large water body which is convenient to fall, and cement (sulfur dioxide reducing substances) in the flue gas is blocked. When the flue gas and the steam are cooled, the gaseous ammonia desulfurization is gradually changed into liquid ammonia desulfurization, and the liquid ammonia provides favorable conditions for flue gas desulfurization. The ammonia desulphurization participates in and tracks the whole process of the garbage incineration from the garbage incineration to the end of the incineration, and captures SO2 from a gas phase to a liquid phase, SO that the ammonia desulphurization achieves the best effect. When the liquid ammonia reacts with SO2 through physical absorption and chemical reaction, ammonia sulfite liquid is formed in the water body. In order to convert the ammonium sulfite in the water body into byproducts, the particles in the flue gas are subjected to harmless treatment, and the water body can be recycled. After the mixture is dedusted by the water body and enters the water storage tank, the water storage tank is provided with the cone filtering net, and the water body is deeply filtered through a plurality of cone filtering nets. After the filtered smoke dust particles are poured out from the cone filtering net, the cement solidification treatment is convenient to concentrate. The filtered water is input into an ammonia sulfite oxidation tank by a water pump, and air (oxygen) is pumped into the ammonia sulfite oxidation tank by an air pump, so that ammonium sulfate crystals are formed after the ammonia oxidation of the sulfurous acid. And the rest water is input into the cooling water tank to supplement the cooling water tank, and is recycled by the evaporated water body or the steam heater. The acid-base water body detector arranged in the water storage tank provides basis for the flow of ammonia liquid entering the heater for the denitration and desulfurization by the ammonia method. The cooling box body is provided with a sealing door for cleaning dirt on the cooling pipeline and on the grid water baffle.
The water body cooling liquid phase desulfurization steam purification flue gas particulate matter device that (3) water cutting preheating incineration steam dust removal desulfurization nitre integration heat energy reuse technology related to has outstanding advantage and beneficial effect that is showing.
1. The method for removing the particulate matters in the flue gas by using the water vapor simulates a purification mode obtained by the flue gas under natural conditions. When the steam is converted into the water body, the water body achieves the effect of nondifferentiation dust removal on all particles in the flue gas, and particularly, the fine particles in the flue gas are purified. 2. Water is the best material for cooling, and when the flue gas and the steam pass through the cooling water pipe, the steam is immediately converted into the water body after being cooled. When the water body wraps and carries the flue gas to enter the grid water baffle, the speed is accelerated, collision is generated between the water bodies, the water bodies and the cementing material of the flue gas are gathered on the grid water baffle, and particulate matters in the flue gas are wrapped and carried by the water bodies. 3. Adopt steam to purify the flue gas, when steam cooling, the steam volume contracts fast, can make all particulate matter surface aggregation water in the flue gas, by the particulate matter of water parcel, under the effect of pipeline wind power, produces the collision each other and forms big water, concentrates the back downward flow through the cooling tube wall, convenient centralized processing. 4. The water vapor is utilized to ensure that the smoke is the most difficult to treat and has harmful effect on human bodies, and particulate matters smaller than PM2.5 can be well purified. 5. The ammonia desulphurization method comprises the steps of burning garbage, purifying flue gas, tracking the whole process, and tracking and capturing SO2 from a gas phase to a liquid phase, and is an efficient and energy-consumption-free desulphurization mode. 6. The gas-liquid phase desulfurization reaction has high reaction rate and high utilization efficiency of the absorbent, and can keep the desulfurization efficiency at 95-99 percent. 7. The steam dust removal and the ammonia denitration and desulfurization are integrated, so that the cost is greatly saved. 8. The filtering net of the water storage tank is set into a cone, and smoke particles are conveniently and intensively cleaned after being filtered by multiple layers of filtering materials. 9 after the water storage tank is purified, the ammonium sulfite liquid in the water body is input into the ammonium sulfite oxidation tank by a water pump, air or oxygen is pumped into the ammonium sulfite liquid by an air pump to be oxidized to form a byproduct ammonium sulfate crystal, and the energy is effectively utilized. 10. The steam is used for removing dust, the water body is recycled, secondary pollution is avoided, and water is saved. 11. The acid-base water body detector arranged in the filtering pond provides a basis for the flow of ammonia liquid entering the heater for the denitration and desulfurization by the ammonia method. 12. The sealing door arranged on the cooling box body provides convenience for cleaning dirt on the cooling pipeline and the grid water baffle.
The garbage cutting preheating incineration steam dust removal and desulfurization nitre integrated heat energy recycling process relates to (4) the contents of a conical filter body dust removal centrifugal force dehydration device:
comprises the following steps: cooling box, atomizing water nozzle, folding plate, sealing door, dust removing cylinder, cone filter, gas comprehensive detector, motor transmission device, shaft lever, bearing seat, fixing frame, water outlet, torsion spring hinge, water baffle, filtering water storage pool, cone filter screen and water pump.
The method is characterized in that: an atomized water spray head is arranged at the inlet of the cooling cylinder, and a folding plate is arranged in the cooling box; a sealing door is arranged outside the cooling box body; the dust removing cylinder is a cylinder, a conical filter is arranged in the cylinder, and a rope and thread filter material is arranged on the conical filter; the conical filter body is provided with a shaft lever, and the shaft lever is arranged on a bearing seat of the fixing frame; a motor is arranged on the shaft lever; the lower end of the dust removing cylinder is provided with a water outlet, the lower end of the water outlet is provided with a torsion spring hinge, and the torsion spring hinge is in sealing connection with the water baffle; and a filtering water storage tank is arranged below the water baffle and provided with a cone filtering net, a water pump is arranged in the tank, and an output pipeline arranged on the water pump is connected with the ammonium sulfite crystallization tank device. And a gas comprehensive detector is arranged at the position of a flue gas outlet of the dust removing cylinder.
Garbage cutting preheats (4) toper filter dust removal centrifugal force dewatering device that incineration steam dust removal desulfurization nitre integration heat energy recycling process involved, the technical scheme that its solution technical problem adopted:
in order to better purify the flue gas, a cooling box is arranged, and an atomized water spray head is arranged at the inlet of the cooling box. Through water atomization, the temperature of the flue gas is reduced, and steam is quickly converted into a water body. In the cooling box, set up the folded sheet, when the water wrapped up flue gas particulate matter and got into the folded sheet, the water formed the striking on the refracting surface of folded sheet, when through the refraction angle, produced the vortex. The water aggregate and the flue gas colloid are blocked by the vortex. In order to better purify the smoke particles, a conical filter device is arranged; on the conical body, a string filtering material is arranged. When the ropes are wound on the conical body, a narrow gap is formed between the ropes. When the water body wraps the smoke particles and passes through the rope line filter body, the rope line has strong water body adsorption capacity. After the rope absorbs the water, the filtering capacity is greatly enhanced. The filtering body adopts a cone body to reduce the resistance of the induced draft fan to the maximum extent, and the filtering area of the cone body is far larger than that of the plane. In order to better block the smoke particles and the water vapor, the motor is arranged on the conical filtering body, and the conical body is driven by the motor to rotate. When the toper filter body was rotatory, water and flue gas particulate matter just produced collision each other on filter body surface, just formed a large amount of water aggregates on filter body surface, on water aggregates was got rid of a dust removal section of thick bamboo in the effect of gravity and centrifugal force, got into the delivery port. When the weight of the water mass aggregates at the water outlet exceeds the torsion force of the torsion spring hinge, the water mass wraps the smoke particles, the water baffle is opened, and the smoke particles enter the filtering water storage tank. The filtering water storage tank is provided with a plurality of layers of cones and a filtering net, and when smoke particles enter the cones and filter the filtering net, the smoke particles can be concentrated at the tip part of the cones, so that the cement solidification can be conveniently and intensively cleaned. After the water in the water storage pool is deeply filtered, the ammonia sulfite water body contained in the water storage pool is pumped by a water pump to crystallize into ammonium sulfate. And the rest water is input into the cooling water tank to supplement the water body evaporated from the water tank or add the water body into the steam heater for recycling. And a gas comprehensive detector is arranged at the position of a flue gas outlet of the dust removal cylinder, so that ammonia liquid is provided for denitration and desulfurization, and feedback data is provided for the flow of the ammonia liquid entering the heater. In order to clean the dirt on the folding plate arranged on the dust removal box in time, a sealing door is arranged on the dust removal box body.
The (4) conical filter body dust removal centrifugal force dehydration device related to the garbage cutting preheating incineration steam dust removal and desulfurization nitrate integrated heat energy recycling process has outstanding advantages and beneficial and obvious effects.
1. The method for wrapping the particulate matters in the flue gas by using atomized water and steam ensures that large and small particulate matters in the flue gas obtain a nondifferential dust removal effect. 2. The vortex formed by the refraction surface and the refraction angle of the folding plate blocks the water aggregate and the glue liquid, so that the gas resistance is small, and the method is simple and effective. 3. The filtering adopts a conical body, the filtering area is increased to the maximum extent, the limited space of the dust removing cylinder is fully utilized, and the resistance of the induced draft fan is reduced. 4. The cone-shaped body is provided with technical measures, the movement speed of the smoke and the water vapor can be slowed down, the water aggregate can be easily stopped by the rope filtering material, and the water and smoke particles can be smoothly separated from the cone-shaped filtering body. 5. The conical body rotating method is adopted, so that the smoke and the water body mutually collide on the filtering material, the water body is gathered, and the working efficiency is improved for smoke dust removal. 6. The cone has good rotation stability, and the generated centrifugal force can easily throw away water and smoke aggregates from filter materials. And the dust removal task of the filter material can be continuously completed. 7. After the rope filtering material adsorbs water, the filtering and dedusting effect reaches the best state, and the flue gas purification effect is particularly obvious. 8. The cone that sets up at the tank filters the net, and the water is after the multilayer is filtered, and the flue gas particulate matter of filtering out gathers at cone point portion, convenient centralized processing, and solidification, innocent treatment are accomplished to cement. 9. The ammonia sulfite liquid in the water body is pumped into the ammonia oxidizing pond by a water pump, and air (oxygen) is pumped into the ammonia oxidizing pond by an air pump to form a byproduct ammonium sulfate crystal, so that the energy is recycled. 10. The residual water can be used for supplementing the water evaporated from the cooling water tank, or a heater is added to convert the water into steam, so that the water body is recycled. 11. The sealing door arranged on the cooling box body provides convenience for cleaning dirt on the folding plate. 12. A gas comprehensive detector is arranged at the position of a flue gas outlet of the dust removal cylinder, a heater control valve is provided, and the flow of the ammonia liquid is fed back.
The (5) anaerobic hot-melt garbage plastic pressing brick and tile building material heat energy recycling device related to the garbage cutting preheating incineration steam dedusting and desulfurizing nitre integrated heat energy recycling process comprises the following steps:
comprises the following steps: the device comprises a garbage feeding device, a feeding hopper, a feeding opening, a rotating device, a speed reducing motor, an air inlet, a conical spiral preheating extruder, a heat energy recycling high-temperature chamber, a transmission feeding device, a mold, a needle, a cutting tool, a pressing mold, a motor, a stamping device, a sand blasting hopper, a smoke outlet and a spiral blade;
the method is characterized in that: the cone spiral preheating extruder is arranged in the high-temperature heat energy utilization chamber; the speed regulating motor transmission device is connected with the large-diameter end of the cone spiral preheating extruder; a charging hole is arranged at the large-diameter end of the conical spiral preheating extruder; the small-diameter end of the conical spiral preheating extruder is provided with a garbage plastic and auxiliary material mixture outlet; a feeding transmission device is arranged at the outlet end of the garbage plastic mixture, a sand blasting hopper is arranged above the feeding transmission device, and a brick and tile mould for pressing the garbage plastic mixture is arranged behind the feeding transmission device; and a power device for pressing garbage plastic bricks and tiles is arranged above the die.
The technical proposal adopted by the anaerobic hot-melt garbage plastic pressing brick and tile building material heat energy recycling device for solving the technical problem is that the garbage cutting preheating incineration steam dedusting and desulfurizing nitre integrated heat energy recycling process relates to (5):
in order to fully utilize the heat energy generated by the waste plastics and convert a part of the waste plastics into the brick and tile building materials. In order to achieve the purpose that the garbage plastics have enough strength when being pressed into the brick and tile building materials, auxiliary materials such as sand and stone are added into the garbage plastics. In order to melt the garbage plastic without generating harmful substances, the garbage plastic is thermally melted into a liquid state under the condition of no oxygen to be used as an adhesive, and the sand and stone auxiliary material and the liquid garbage plastic are mixed and mutually connected to form firm connection. The conical spiral preheating extruder is placed in the high-temperature gas channel, so that heat is generated inside the conical spiral preheating extruder, and when loose plastics and auxiliary materials enter the conical spiral preheating extruder, the solid waste plastics and the auxiliary sand stones are converted into liquid under the action of temperature. The plastic liquid and the auxiliary sand stone are fully stirred and mixed through the spiral blades of the conical spiral preheating extruder, so that the plastic liquid and the auxiliary sand stone form a cementing state. As the volume of the waste plastics in the conical spiral preheating extruder is reduced, the volume of the conical spiral blade arranged in the extruder is also reduced. When rubbish plastics and auxiliary material are promoted forward by the spiral preheating extruder, the air of inside production also can move backward and discharge voluntarily, when rubbish plastics liquid and supplementary grit extrude from the toper preheating extruder screw, in order to prevent to produce smooth phenomenon on the briquetting brick surface to and let its surface produce the wholeization, set up the sandblast hopper at the exit end, to rubbish plastics liquid surface spraying sand immediately. After the surface of the mixture is coated with sand, the mixture enters a die under the drive of a feeding transmission device, a power device is arranged to press the waste plastic, a penetrating needle is arranged on the pressing die, on one hand, the penetrating needle releases air in the semi-liquid waste plastic, and on the other hand, the penetrating needle forms holes in the brick body, so that mortar between the bricks can be conveniently bonded.
The (5) anaerobic hot-melt garbage plastic pressed brick and tile building material heat energy recycling device related to the garbage cutting preheating incineration steam dedusting and desulfurizing nitre integrated heat energy recycling process has outstanding advantages and beneficial and obvious effects.
1. Compared with common bricks and tiles, the building material for making the bricks and the tiles by utilizing the heat energy generated by burning the garbage and then hot-melting and pressing the garbage plastics greatly improves the strength and realizes the recycling value of the garbage plastics. 2. The waste plastics can be converted into liquid under the condition of no oxygen by adopting the conical preheating screw extruder, the plastic liquid and the sandstone auxiliary material are fully mixed and cemented under the stirring of the screw extruder, and the pressed brick and tile show high density, high strength and very good corrosion resistance. 3. The bricks and tiles pressed by the waste plastics are added with a new building material, and the recycling value of the waste plastics is realized. 4. The sand and stone are sprayed on the surfaces of the bricks, so that mortar between the bricks can be conveniently cemented with each other, the attractiveness of the bricks is improved, and the waste plastic incineration amount is greatly reduced.
The integrated heat energy recycling process for removing dust and sulfur and nitre by cutting, preheating and burning the garbage relates to (6) the content of a device for converting garbage plastic into heavy oil heat energy and recycling the heavy oil heat energy by anaerobic cracking;
comprises the following steps: the device comprises a high-temperature gas channel, a charging opening, a charging hopper, a speed regulating motor, a driving wheel, a cone spiral preheating extruder, a gas-blocking cylinder, a liquid outlet, a cracking cylinder, a spiral scraper, a steam input electromagnetic valve, an oil-gas output pipeline, a temperature controller, a steam heater, a water body input valve, a spiral sealing discharger, a baffle, a torsion spring hinge, a transmission shaft, a liquid outlet, an oil-gas input and output pipeline, a combustible gas return pipeline, an oil storage tank and a condensing device.
The method is characterized in that: the cone spiral preheating extruder is arranged in the high-temperature gas channel and is provided with a transmission device; the charging hopper and the charging opening are arranged at the large-diameter end of the conical spiral preheating extruder; a plastic liquid outlet at the small diameter end of the conical spiral preheating extruder; an air blocking cylinder is arranged at the outlet end of the plastic liquid and is connected with the cracking cylinder; the cracking cylinder is provided with a temperature transition automatic control power switch, and a power signal output by the power switch is connected with an electromagnetic control valve of a steam inlet; the cracking cylinder is divided into an inner cylinder and an outer cylinder; holes and reinforcing strips with different sizes are arranged on an outer cylinder arranged on the cracking cylinder; the inner cylinder is a sealing cylinder, a transmission shaft is arranged in the inner cylinder, a speed regulating motor is arranged on the transmission shaft, and an arched spiral scraper is arranged on the transmission shaft of the speed regulating motor; an oil-gas pipeline arranged in the cracking cylinder is connected with a condenser, and a heavy oil pipeline of the condenser is connected with the storage cylinder. A combustible gas return pipeline is arranged on the heavy oil pipeline and is connected with the combustion furnace; a waste material cylinder is arranged at one end of the cracking cylinder, and a spiral sealing discharging machine is arranged at the lower end of the waste material cylinder; a torsion spring hinge is arranged at the outlet of the sealing and discharging machine and is in sealing connection with the baffle; and a steam heater is also arranged in the high-temperature gas channel, the water body input valve is connected with the heater, the heater is of a calandria structure, and the output port of the heater is connected with the steam input electromagnetic valve.
A garbage cutting preheating incineration steam dedusting and denitration integrated heat energy recycling process relates to (6) a device for recycling heat energy of converting garbage plastics into heavy oil by anaerobic cracking, and adopts the technical scheme for solving the technical problems that:
the waste plastic is converted into heavy oil by utilizing the heat energy of the waste incineration, and a conical spiral preheating extruder is arranged. The conical spiral preheating extruder is arranged in the high-temperature gas channel. The garbage plastic is cracked and converted into oil weight in a conical spiral preheating extruder under the anaerobic condition. When loose plastic enters the conical spiral preheating extruder, the plastic rises along with the temperature in the conical spiral preheating extruder, the solid is converted into liquid, the volume is continuously reduced, and the volume of the conical spiral preheating extruder is also reduced. When plastic liquid is preheated by the conical spiral extruder, the volume inside the spiral extruder is continuously reduced when the plastic liquid is continuously pushed forward by the spiral blades, the pressure generated inside the spiral extruder is continuously increased along with the continuous reduction of the volume of the spiral extruder, and the air inside the plastic liquid can automatically move backwards. To prevent air from entering the cracker cartridge, an air baffle is placed in front of the conical screw extruder. When the plastic liquid enters the air blocking cylinder, the diameter of the outlet of the air blocking cylinder is smaller than the inner diameter of the air blocking cylinder. Therefore, when the plastic liquid enters the gas resisting cylinder, the plastic liquid in the gas resisting cylinder is always in a sealed state, so that the space in the liquid cannot enter the gas resisting cylinder. When the toper spiral preheats the extruder and push plastics liquid from a choke section of thick bamboo into the schizolysis section of thick bamboo, in the pyrolysis gasification section of thick bamboo, be provided with arch spiral scraper blade, arch spiral scraper blade is driven under the speed regulating motor, evenly coats plastics liquid and evenly coats on the pyrolysis gasification section of thick bamboo surface, can convert the oil gas into fast after the liquid is heated. In order to convert the garbage plastics into high-quality heavy oil, the conversion efficiency of the garbage plastics and combustible materials is improved. The pyrolysis gasification device is characterized in that a temperature power supply automatic control switch is arranged in the pyrolysis cylinder, a power supply signal output by the switch is connected with a steam inlet electromagnetic control valve, the temperature in the pyrolysis gasification cylinder is regulated and controlled by steam, the internal pressure of the pyrolysis cylinder is improved, and the steam has a catalytic effect on oil steam to improve the quality of the oil steam. In order to solve the problem of uniform surface temperature inside the cracking cylinder, an inner cylinder and an outer cylinder are arranged, the cracking cylinder is of a double-layer structure, the outer cylinder is a temperature-balanced and stable cylinder, and the inner cylinder is a sealing cylinder and is a liquid cracking and gasifying separation cylinder. The outer cylinder is provided with small-diameter holes at the place where the cracking cylinder is close to the flame, and the outer cylinder is provided with large-diameter holes at the place where the cracking cylinder is far away from the flame, so that the temperature balance of the cracking cylinder is ensured; in addition, the reinforcing strip is arranged on the outer barrel to protect the inner barrel from deformation when heated. The garbage plastics can not be converted into liquid combustible gas in the process of converting heavy oil, and a special pipeline is arranged to return to the combustion furnace body again to provide a heat source. When the residual residue and waste materials are left after the oil vapor is converted in the cracking cylinder by the garbage plastic liquid, the residual residue and waste materials are automatically scraped into the other side of the cracking cylinder from one side by the spiral scraper and enter the waste discharge cylinder. In order to prevent air from entering the cracking cylinder to generate harmful gas, a spiral sealing discharging machine is arranged at the lower end of the waste material cylinder, and a torsion spring hinge is arranged at the outlet position of the lower end of the sealing discharging machine to be connected with a sealing baffle plate. When the spiral sealing discharging machine discharges waste materials, the sealing baffle can be opened, and the baffle is in a sealing state under the condition that the discharging cylinder does not discharge the waste materials. According to the waste discharge condition, whether rubbish plastics reach thorough gasification degree, regulate and control the motor revolution, make rubbish plastics in the schizolysis section of thick bamboo, the required time of complete gasification conversion oil gas. And a steam heater is also arranged in the high-temperature gas channel, and the generated steam is input into the electromagnetic valve through the steam to provide the steam required by the cracking cylinder.
The (6) anaerobic cracking garbage plastic conversion heavy oil heat energy recycling device related to the garbage cutting preheating incineration steam dedusting and denitration integrated heat energy recycling process has outstanding advantages and beneficial and obvious effects.
1. The conical screw preheating extruder makes the loose plastic enter from the large diameter end of the conical screw preheating extruder, and when the loose garbage plastic comes out from the small diameter end of the conical screw preheating extruder, the garbage plastic changes from solid to liquid by a preheating method and then enters the cracking cylinder. The oxygen and the nitrogen enter the cracking cylinder to be prevented from generating chemical reaction with the oil gas to generate harmful gas. Provides favorable guarantee conditions for the anaerobic cracking gasification of heavy oil by garbage plastics and combustible substances, realizes the purpose of automatic continuous production, improves the production efficiency, and achieves an ideal effect of converting garbage plastics into heavy oil by cracking. 2. The arched spiral scraper arranged in the cracking cylinder can convert garbage plastic liquid into oil gas on the surface of the cracking heating cylinder in a uniform mud flat manner; the garbage plastic is promoted to be quickly gasified in the cracking cylinder, the oil-gas conversion efficiency of the garbage plastic is improved, and the gasified waste can be automatically separated. 3. The sealing spiral discharging device is provided with the sealing baffle plate and the torsion spring hinge connection at the outlet end, so that air is prevented from entering the cracking cylinder, the automatic waste discharging device is realized, and conditions are provided for anaerobic cracking of garbage plastic conversion heavy oil. 4. The cracking cylinder adopts the design of the inner cylinder and the outer cylinder, and creates conditions for providing balanced surface temperature of the cracking cylinder, ensuring the stability of the inner cylinder body and leading the arched spiral scraper to smoothly complete the gasification of the plastic liquid. The heat is fully utilized, the conversion of the garbage plastics into oil gas in the cracking cylinder is accelerated, and the garbage gasification efficiency is improved. 5. The temperature control switch is utilized to ensure that the temperature of the cracking cylinder has automatic control capability, the steam is utilized to adjust the temperature and the pressure of the cracking cylinder, and the steam has catalytic action on oil gas, so that the oil gas leaves a high-temperature area quickly, and the oil gas quality is improved. 6. The calandria heater is arranged in the high-temperature gas channel, so that convenience is provided for solving the problem of steam required by the cracking cylinder. The method is simple and saves cost. 7. The speed regulating motor is used for controlling the garbage plastics, oil gas is converted in the cracking cylinder, the time required to be reached is shortened, and the recovery rate of the oil gas converted from the garbage plastics is improved. 8. In the process of converting heavy oil, the garbage plastic realizes automatic control from feeding to discharging waste.
Attached drawing description of devices involved in garbage cutting, preheating, incinerating, steam dedusting, desulfurizing and nitre integrated heat energy recycling process
FIG. 1 is a schematic view of the working principle of a combined device for mechanical intelligent linear cutting of garbage plastic bag wrapping and garbage plastic sorting by a roller.
FIG. 2 is a schematic view of the working principle of the gas phase denitration and desulfurization integrated heat energy recycling device for steam purification of waste preheating, drying and incineration flue gas.
FIG. 3 is a schematic view of the working principle of a device for purifying particulate matters in flue gas by water cooling and liquid-phase desulfurization steam.
FIG. 4 is a schematic view of the working principle of the conical filter dedusting centrifugal force dehydration device.
FIG. 5 shows a heat energy recycling device for oxygen-free hot-melt garbage plastic pressed brick and tile building materials.
FIG. 6 is a schematic view of the working principle of a device for converting waste plastics into heavy oil heat energy and recycling the heavy oil heat energy without oxygen cracking.
The abstract of the specification is as follows: FIG. 2 is a schematic view of the working principle of a steam purification, gas phase denitration and desulfurization integrated heat energy recycling device for waste preheating, drying and incineration flue gas.
The marks of all components in the schematic diagram of each device related to the garbage cutting preheating incineration steam dedusting and desulfurization nitrate integrated heat energy reutilization process are described as follows:
in the attached figure 1: 1, rolling a roller; 2, fixing a bolt by a push-pull rod; 3, fixing a jacket by a push-pull rod; 4, a push-pull rod; 5, a steel saw blade; 6 rubbing the shaft; 7, garbage; 8 connecting rods; 9 a torsion spring rotating shaft; 10 a steel saw blade; 11 a connecting rod; 12 torsion spring rotating shaft; 13 a steel saw blade; 14, protecting plates; 15 a floating wheel; 16 friction shaft; 17 a floating wheel; 18 connect the shafts.
In the attached fig. 2: 1. a heat energy recycling device; 2. a steam heater; 3. a gaseous nitrogen outlet, a 4 reducing agent heater; 5 ammonia liquid control valve; 6 steam control valve; 7, a water tank; 8 ammonia liquid water tank; 9 a feed inlet; 10, turning over the cover plate; 11 automatically controlling the turnover cover plate device; 12 automatically controlling the turnover baffle device; 13, an automatic material feeding control device of the hanging frame; 14 turning over the baffle; 15 a rope; 16 turning shaft; 17, a hanging frame turning connecting rod; 18, hanging frame net rows; 19 hanging the frame net row; 20 lifting frames and 21 turning shafts; 22 hanging frame turning connecting rod; 23, an automatic feeding control device of the hanging frame; 24, an automatic feeding control device of the hanging frame; 25 connecting rings; 26 a turning shaft; 27 hanging frame net rows; 28 hanging frame turning connecting rod; 29 hanging frame turning connecting rod; 30, hanging frame net rows; 31 a furnace door; 32 a gaseous ammonia outlet; 33 a water vapor outlet; 34 a gaseous ammonia outlet; 35 a fan; 36 a water vapor outlet; 37 a gaseous ammonia conduit; 38 a gaseous ammonia outlet; 39 a combustion supporting gas conduit; 40 gas control valves; a 41U-shaped grate; 42 the furnace body is burned.
In FIG. 3: 1. a flue gas inlet; 2, cooling a water tank; 3 cooling the water inlet of the calandria; 4, water body; 5, a smoke outlet; 6, a grid water retaining plate; 7, a water pump; 8, sealing the baffle; 9 filtering the screen; 10 torsion spring hinges; 11 a cooling tube; 12 water storage pool; acid-base liquid detector.
In fig. 4: 1, a flue gas inlet and 2, an atomized water spray head; 3, a dust removing cylinder; 4, a motor; 5, an air outlet; 6, a gas comprehensive detector; 7, a conical filter body; 8, folding the plate; 9 bearing seats; 10 shaft rod; 11 a fixing frame; 12 torsion spring hinges; 13 filtering the screen; 14 sealing the baffle plate; 15 a water storage tank.
In fig. 5: 1, a garbage feeding device; 2, a charging hopper; 3, a feed inlet; 4, a rotating device; 5, a speed reducing motor; 6, a high-temperature gas inlet; 7 a conical screw extruder; 8, a high-temperature gas channel; 9 driving the feeding device; 10, molding a tire mold; 11, threading a needle; 12 cutting tools; 13 pressing a mould; 14 speed regulating motor; 15 a stamping device; 16 grit blast hoppers; 17 a flue gas outlet; 18 helical blades.
In fig. 6: 1, an oil storage tank; 2 a condensing device; 3 oil gas output pipeline; 4, a smoke outlet; 5 oil gas output pipeline; 6, a cracking cylinder; 7 steam is input into the electromagnetic valve; 8, a temperature controller; 9 a steam heater; 10 high-temperature gas channel; 11 water body input valve; 12 a speed regulating motor; 13 spiral sealing discharge machine; 14 sealing the baffle plate; 15 torsion spring hinges; 16 a spiral flight; 17 a drive shaft; 18 gas resistance cylinder and liquid outlet; 19 a conical screw extruder; 20 a liquid outlet; 21 oil gas input and output pipelines; 22 a combustible gas return conduit; 23, garbage plastics; 24 a feed port; 25 a loading hopper; 26 a driving wheel; 27 speed regulating motor; 28 high temperature gas channel.
The integrated heat energy recycling process for cutting, preheating and incinerating garbage, removing dust, removing sulfur and nitre combines with the specification, the attached figure 1, and the specific implementation mode and the working principle of the combined device for mechanically and intelligently linearly cutting garbage plastic bag wrapping and recycling garbage plastic through roller separation are explained in detail.
In the embodiment shown in fig. 1: the garbage packaging machine is characterized in that a motor drives a lower roller (1) to rotate clockwise under the support of a floating wheel (15) and a floating wheel (17), a push-pull rod (4) is arranged on the wall of the roller, a steel saw blade (13) pushes and pulls garbage packages (7) out from the steel saw blade (10) to the steel saw blade (5), when the garbage packages (7) are pushed and pulled to a steel saw blade cutter (10) by the push-pull rod (4) and the steel saw blade (13), the garbage package surface can be cut by the steel saw blade cutter (10), the steel saw blade (10) slowly rotates backwards under the action of a friction sheet rotating shaft (16), acute angles are exposed, and the garbage plastic surface is cut by the acute angles. When push-and-pull rod (4), saw blade (13) drive rubbish parcel when saw blade (5), rubbish parcel (7) receive saw blade (5) repeated cutting again, saw blade (5) through at friction axle (6) slow backward movement, the continuous acute angle that shows increases cutting efficiency. Garbage parcel (7) is through saw blade (5) repeated cutting back, scatters out the discarded object of disposal bag parcel, and rubbish is under push-and-pull rod (4), saw blade (13) drive, along with the rotation of cylinder (1), and push rod (4), saw blade (13) angle are continuous to be changed into the vertical state, and rubbish plastics breaks away from push rod (4), saw blade (13) under gravity and air-blower are used. The cut garbage plastics enter a roller (1) for sorting and recycling. When the steel saw blade cutter (10) meets a large hard object, under the pushing of the push-pull rod (4) and the steel saw blade (13), when the upward resistance of the steel saw blade cutter (10) is greater than that of the torsion spring connecting rod rotating shaft (12), the torsion spring connecting rod (11) is lifted upwards, and the steel saw blade (10) is placed over the hard object which is not cut. When the steel saw blade cutter (5) meets a large hard object, the steel saw blade cutter (5) is pushed by the push-pull rod (4) and the steel saw blade (13), when upward resistance on the steel saw blade cutter (5) is greater than that on the torsion spring connecting rod rotating shaft (9), the torsion spring connecting rod (8) is lifted upwards, and the steel saw blade (5) is placed over the hard object which is not to be cut. When broken glass bottles, broken tiles and stones pass through the steel saw blade (10) and the steel saw blade (5), the cutting device adopts a linear motion mode, the glass bottles, broken tiles and stones set a distance between the cutting tools and can slide down along the lower surface of the roller, the roller is provided with an inclination angle, and the broken glass bottles and broken tiles and stones can roll downwards along the inclination angle of the roller and are discharged out of the screening cylinder. When the push-pull rod (4) and the steel saw blade (13) are abraded, the push-pull rod is replaced or repaired. When the steel saw blade (5) and the steel saw blade (10) are worn, the guard plate (14) is opened for replacement or repair.
The integrated heat energy recycling process for removing dust, sulfur and nitrate from steam in garbage cutting preheating incineration and the attached drawing 2 of the specification illustrate in detail the integrated heat energy recycling device for purifying gas phase sulfur removal and denitration from steam in garbage preheating drying incineration, the specific implementation mode and the working principle.
In the embodiment shown in fig. 2: before the incinerator (42) is ignited, a temporary heating device is arranged on the reducing agent heater (4) and the water vapor heater (2) and is used for steam dust removal and ammonia denitration and desulfurization. When the temperature of the incinerator body (42) rises, the reduction heater (4) and the steam heater (2) stop the temporary heating task. Transferring the heat of the high-temperature gas generated by the incinerator (42) to complete the tasks of heating the reducing agent (4) and heating the steam (2). When feeding materials to a charging port (9) of the incinerator, a power signal is input into the automatic control turnover cover plate device (11), the sealed turnover cover plate (10) is opened, when the charging materials are fed to the charging port (9), the automatic control turnover cover plate device (11) closes the sealed turnover cover plate (10), the self-control turnover baffle plate device (12) opens the turnover baffle plate (14), garbage plastics and combustible materials are fed into the incinerator body (42), after the turnover baffle plate (14) finishes feeding tasks, the turnover baffle plate (14) automatically returns to the original sealing position, and all hanging frames are filled with the materials by a repeated method. When garbage combustion objects in the hanging frame (20) need to be fed into the hanging frame (23), power signals are input into the automatic feeding control device (13), the automatic feeding control device (13) puts down the control ropes (15), the hanging frame overturning connecting rod (22) and the hanging frame overturning connecting rod (17), the hanging frame mesh rows (18) and the hanging frame mesh rows (19) are automatically opened, the garbage combustion objects automatically drop into the hanging frame (23), garbage plastics and the combustible objects are thrown into the hanging frame (24) by the hanging frame (23) in the same method, and the garbage plastics are thrown into the U-shaped fire grate (41) by the hanging frame (24) in the same method. After the U-shaped fire grate (41) is fully covered with garbage plastics, the garbage plastics on the U-shaped fire grate (41) are ignited, when the garbage plastics and combustible materials are ignited on the U-shaped fire grate (41), the generated temperature rises, the garbage plastics and the combustible materials in the hanging frame are arranged above the furnace body (42), water is evaporated and generates heat after the garbage plastics and the combustible materials are subjected to high temperature, when the garbage plastics and the combustible materials are about to finish combustion on the U-shaped fire grate (41), a power supply signal is input to the automatic feeding control device (24) in time, and the garbage combustible materials in the hanging frame (26) are put into the U-shaped fire grate (41). Because the garbage combustion objects in the hanging frame (26) are subjected to high temperature and reach a combustion state, when encountering the flame of the U-shaped fire grate (41), the garbage combustion objects can immediately generate combustion to form high temperature. The working personnel can continuously feed materials into the furnace body according to the garbage burning condition of each furnace door (31). The air intake quantity required by the furnace body is met by adjusting the induced air pipeline and the gas valve (40). When the furnace body is burnt, a reducing agent heater (4) arranged in a high-temperature gas channel generates heat, an ammonia liquid control valve (5) arranged in a desulfurization and denitrification liquid chamber (8) is opened, the reducing agent heater (4) heats and converts liquid ammonia into gaseous nitrogen and steam mixed gas, and the gaseous ammonia and steam mixed gas enters the bottom of a U-shaped fire grate (41) through a gaseous ammonia pipeline (37) to be arranged; the gaseous ammonia is sprayed out from an outlet (38); meanwhile, a gaseous ammonia outlet (3) arranged in the high-temperature gas channel sprays gaseous ammonia into the flue gas. When the incinerator burns to generate temperature, a valve (6) arranged on the water chamber (7) is opened, and water is input into the steam heater (2) and converted into steam; in order to utilize steam for dust removal, a steam outlet (36) is arranged in a flue gas outlet pipeline at the rear end of the heat energy recycling device, the steam is mixed with the flue gas, and a fan is arranged in front of the steam outlet (36). The other water vapor outlet (33) is arranged at the bottom of the U-shaped fire grate (41), so that the temperature in the furnace is adjusted by using the water vapor, and the condition that cutting gas is generated when garbage is completely eradicated to burn is avoided. A heat energy recycling device (1) is arranged in the high-temperature gas channel.
The integrated heat energy recycling process for removing dust and sulfur and nitre by using garbage cutting preheating incineration steam combines with the specification of an attached figure 3 to describe a device for purifying flue gas particles by using water cooling liquid-phase sulfur removal steam, and the specific measures, modes and working principles are as follows:
in the embodiment shown in fig. 3: when mist (steam, gaseous ammonia, flue gas) got into the cooler bin from flue gas inlet (1), when the flue gas passed cooling tube (11), steam received the cooling back in the flue gas, was converted into liquid by gas, and liquid produced the flue gas particulate matter and condenses to cooling tube (11) wall on, when a large amount of water formed the gathering on cooling tube (11) wall, the water wrapped up the flue gas particulate matter and got into the bottom half. Following sealed breakwater (8) that set up, when the weight of water and particulate matter, when having exceeded the strength of the torsion spring that sealed breakwater (8) set up, breakwater (8) are opened to the water particulate matter and have got into tank (12), it blocks (6) breakwater to have set up the net between cooling tube (11), when steam gets into net breakwater (6), let flue gas (steam) velocity of motion accelerate, make collision each other between the water, form the convenient landing of big water, and stop the cementite in the flue gas. And in the cooling process of the flue gas and the steam, the gaseous ammonia desulfurization is gradually changed into liquid ammonia desulfurization. A plurality of layers of filtering nets (9) are arranged in the water storage tank (12); after the water storage tank (12) is filtered deeply, a water pump (7) pumps water containing the sub-flowing acid liquid into a sulfurous acid ammonia oxidation tank, and the sub-flowing acid ammonia is oxidized into a byproduct, namely ammonium flowing acid crystal. An acid-base detector (13) is arranged in the filtering water tank (12) to provide feedback data for the flow of the ammonia liquid entering the heater.
The integrated heat energy recycling process for removing dust, sulfur and nitrate from the garbage by cutting, preheating and burning steam, and the attached drawing 4 of the specification are combined to explain the conical filter body dust removal centrifugal force dehydration device in detail, and the specific measures, modes and working principles are adopted.
In the embodiment shown in fig. 4: when the cooled flue gas mixture is removed by taking the flue gas, the flue gas enters the dust removing cylinder (3) from the flue gas inlet (1), and the atomized water spray heads (2) further cool the mixed flue gas to increase the water content of the flue gas. When flue gas and aqueous vapor get into folded sheet (8), produce the collision between flue gas and water and folded sheet (8), produce the vortex in folded sheet (8) refraction angle department, make the water wrap up and hold flue gas particulate matter and form the aggregation and subside. When flue gas and aqueous vapor mixture, dust removal cylinder (3) get into by motor (4) drive, when rotatory toper filter (7), flue gas and water mixture produce the collision on the rope line that toper filter (7) set up, and flue gas particulate matter and water are intercepted by the rope line. The smoke particles and the water body are thrown to the wall of the dust removing cylinder (3) under the centrifugal force action of the cone filtering body (7). The water mixture enters a sealing water baffle (14), when the weight of the water mixture exceeds the force of a torsion spring hinge, the sealing baffle (14) is opened by the water mixture, the water mixture enters a water storage tank (15), and the water mixture is deeply filtered through a plurality of filtering nets (13), then the water mixture containing ammonia sulfite is input into a sulfite ammonia oxidation tank through a water pump. At the flue gas outlet end of the dust removing cylinder (3), a gas comprehensive detector (6) is arranged to provide a basis for ammonia denitration and desulfurization.
The waste cutting preheating incineration steam dedusting and desulfurization nitre integrated heat energy recycling process combines with the specification, the attached figure 5, and the detailed description of the specific measure mode and the working principle of the oxygen-free hot-melt waste plastic pressing brick and tile building material heat energy recycling device.
In the embodiment shown in fig. 5: when the conical screw extruder (7) reaches heat in the high-temperature gas channel, the conical screw extruder (7) is driven by the speed reducing motor (5); the conical screw extruder (7) is rotated. When the garbage plastics (1) and the auxiliary materials enter the charging opening (3) from the charging hopper (2), the garbage plastics (1) and the sand and stone auxiliary materials are heated in the conical screw extruder (7) and then are converted into liquid from solid under the pushing of the screw blades (18). When the liquid plastic and the sand form a cementing mixture in the conical screw extruder (7), the cementing mixture is pushed out by the screw blade (18) to the transmission feeding device (9); a sand blasting hopper (16) is arranged above the transmission feeding device (9) to spray sand coatings on the cemented object, and when the cemented object finishes spraying the sand coatings, the cemented object automatically enters the moulding bed (10); the punching device (15), the punching device (15) utilizes the pressing die (13) that sets up under the drive of buncher (14), and the brick and tile building material is suppressed to the plastics cementate.
The integrated heat energy recycling process for removing dust and sulfur and nitre by using steam for cutting, preheating and burning garbage and the attached figure 6 of the specification explain the concrete measure mode and the working principle of the device for converting anaerobic cracking garbage plastic into heavy oil heat energy in detail:
in the embodiment shown in fig. 6: the cone screw extruder (19) is arranged in the high-temperature gas channel (28), when the cone screw extruder (19) generates heat, the speed-adjustable motor (27) is started to drive the cone screw extruder (19) to rotate under the drive of the transmission device (26), the garbage plastics (23) are added into the hopper (24), when the garbage plastics enter the cone screw extruder (19) from the inlet (25), the cone screw extruder (19) continuously pushes the garbage plastics forwards, and the garbage plastics are changed from solid into liquid, because the liquid outlet arranged at the front end of the cone screw extruder (19) is small, the gas resistance cylinder (18) forms resistance to the air in the plastic liquid after the space of the gas resistance cylinder (18) is completely filled by the plastic liquid, and the air in the plastic liquid cannot enter the gas resistance cylinder (18), the plastic liquid enters the cracking cylinder (6) under the condition of no air. When the cone spiral preheating extruder (19) pushes the plastic liquid into the cracking cylinder (6), the arched spiral scraper (16) coats the plastic liquid from one side of the cracking cylinder (6) to the other side, and the plastic liquid is cracked and converted into oil gas at a high temperature; oil gas enters the condensing device (2) through the oil gas output pipeline (21) and the oil gas output pipeline (5), and oil gas forms heavy oil liquid and then enters the oil storage tank (1). The waste material of production is driven simultaneously by arch scraper blade (16) to the waste material section of thick bamboo of setting in, and waste material section of thick bamboo lower extreme is provided with spiral discharging machine (13), and when spiral discharging machine (13) promoted sealed striker plate (14) with the waste material, the thrust that the waste material produced is greater than when torsion spring hinge (15) that sealed striker plate (14) set up, and sealed baffle (14) are opened to the waste material, discharges the waste material under spiral discharging machine (13) encapsulated situation. The staff regulates and control adjustable motor (27) and the speed governing motor rotational speed that the arch spiral scraping plate set up through whether the inspection waste material changes totally and changes the oil vapour condition. When the garbage plastic is cracked in the cracking cylinder (6), the temperature automatic control power switch (8) exports power signal input/output steam electromagnetic valve (7), steam enters the cracking cylinder (6), the steam promotes the inside pressure that produces of the cracking cylinder (6), carry out catalytic action to oil gas, make oil gas leave the high temperature area of cracking cylinder (6) fast, obtain high quality oil gas, oil gas passes through pipeline (5), pipeline (21), get into condensing equipment (2), can not cool for the combustible gas of liquid, it provides the heat source to return the incinerator again through combustible gas pipeline (22). The staff can monitor whether the waste plastics and combustible materials reach the complete gasification degree according to the spiral sealing discharging machine (14) and the discharged waste material condition, timely adjust the speed regulating motor (27) arranged on the cone spiral preheating extruder (19) and the speed regulating motor arranged on the transmission shaft arch spiral scraper (16), adjust the rotating speed of the speed regulating motor, and discharge the waste materials outwards after the waste plastics are completely cracked, so that the waste plastics conversion heavy oil reaches the best effect.

Claims (7)

1. The garbage cutting preheating incineration steam dedusting and desulfurizing nitre integrated heat energy recycling process relates to the following devices and components: a) mechanical intelligent linear cutting rubbish plastic bag parcel and cylinder are selected separately rubbish plastics and are retrieved integrated device, including: the device comprises a roller, a fixed jacket, a fixed bolt, a push-pull rod, a power steel saw blade, a fixed steel saw blade, a torsion spring connecting rod rotating shaft, a connecting shaft, a floating wheel, a fan, a charging opening and a protective plate; b) the garbage preheats dry incineration flue gas steam and purifies gaseous phase denitration desulfurization integration heat energy and recycles the device, including: the device comprises a charging hole, an automatic overturning cover plate, an automatic control overturning cover plate device, an overturning baffle plate, an automatic control overturning baffle plate device, a high-temperature gas heating channel, a reducing agent heater, a steam pipeline, a steam outlet, a gaseous ammonia pipeline, a gaseous ammonia outlet, a steam control valve, a steam water tank, an ammonia liquid control valve, an ammonia liquid water tank, a hanging frame automatic charging control device, a hanging frame mesh row, an overturning shaft, a hanging frame overturning connecting rod, a rope, a lantern ring, a furnace door, a fan, a combustion-supporting gas pipeline, a gas control valve, a U-shaped fire grate, an incinerator body, a heat energy recycling device and a high-temperature gas channel; c) water cooling liquid phase desulfurization steam purifies particulate matter device of flue gas, including: the device comprises a cooling box, an air inlet, an air outlet, a water body, a cooling water tank, a cooling calandria, a grid water blocking plate, a sealing door, an acid-base water body monitor, a water pump, a water outlet, a torsion spring hinge, a water baffle, a cone filtering net and a water storage pool; d) the centrifugal dewatering device for dust removal of the conical filter comprises: the device comprises a cooling box, an atomized water spray head, a folding plate, a sealing door, a dust removing cylinder, a cone filter, a motor transmission device, a shaft lever, a bearing seat, a fixing frame, a gas comprehensive detector, a water outlet, a torsion spring hinge, a water baffle, a cone filter screen, a water storage tank and a water pump; e) the utility model provides a device is recycled to anaerobic hot melt rubbish plastics suppression brick tile building material heat energy, including: the device comprises a garbage feeding device, a feeding hopper, a feeding opening, a rotating device, a speed reducing motor, an air inlet, a conical spiral preheating extruder, a heat energy recycling high-temperature chamber, a transmission feeding device, a mold, a penetrating needle, a cutting tool, a pressing mold, a motor, a stamping device, a sand blasting hopper and a spiral blade; f) anaerobic cracking garbage plastic conversion heavy oil heat energy recycling device, including: the device comprises a high-temperature gas channel, a charging opening, a charging hopper, a speed regulating motor, a driving wheel, a cone screw extruder, a gas resisting cylinder, a cracking cylinder, a spiral scraper, a steam input electromagnetic valve, an oil gas output pipeline, a temperature control switch, a steam heater, a water body input valve, a spiral sealing discharging machine, a baffle, a torsion spring hinge, a transmission shaft, a liquid outlet, an oil gas input and output pipeline, a combustible gas return pipeline, a condensing device and an oil storage tank.
2. The garbage cutting preheating incineration steam dedusting and desulfurization nitre integrated heat energy recycling process according to claim 1 relates to a) a mechanical intelligent linear cutting garbage plastic bag wrapping and roller sorting garbage plastic recycling combined device, which is characterized in that: the front end of the roller is provided with a feed inlet, the lower end of the feed inlet is provided with a fixed steel saw blade cutting tool, the fixed steel saw blade cutting tool is connected with a rotating shaft of a torsion spring connecting rod, and the fixed steel saw blade is provided with a guard plate at the upper part and the lower part; the push-pull rod is arranged in a jacket on the inner wall of the roller, a push-pull rod fixing bolt is arranged on the push-pull rod fixing jacket, a power steel saw blade is arranged on the inner wall of the roller, floating wheels are arranged at the bottoms of two ends of the roller, and the roller is provided with an inclination angle.
3. The garbage cutting preheating incineration steam dedusting and desulfurization and denitration integrated heat energy recycling process as claimed in claim 1, relates to b) a garbage preheating drying incineration flue gas steam purification gas phase denitration and desulfurization integrated heat energy recycling device, and is characterized in that: the upper end of the incinerator is provided with a charging hopper, and the upper end of the charging hopper is provided with an automatic turnover cover plate device; the automatic turnover cover plate device is provided with a motor, and a motor transmission shaft is connected with the turnover cover plate; an automatic overturning baffle device is arranged at the lower end of the charging opening, a motor is arranged on the automatic overturning baffle device, and a motor transmission shaft is connected with the overturning baffle; a plurality of layers of hanging frames are arranged above the furnace body, and each hanging frame consists of two corresponding net rows; the net rows are formed by combining steel pipes or steel bars, and overturning shafts are arranged at two ends of the net rows of the hanging frame; a hanging frame overturning connecting rod is arranged on the overturning shaft and is arranged outside the incinerator body; the turning connecting rods arranged on the two sides of the hanging frame are provided with ropes to connect the two turning connecting rods, and the middle position of each rope is provided with a lantern ring which is connected with the ropes on the motor concave wheel; a U-shaped fire grate is arranged below the incinerator body, an induced draft pipeline and a gas control valve are arranged below the U-shaped fire grate, and a furnace door is arranged at the corresponding position of the U-shaped fire grate; the reducing agent heater and the water vapor heater are arranged in the high-temperature gas channel; the reducing agent heater and the water vapor heater are both composed of a calandria; the reducing agent gaseous ammonia outlet is arranged at the position of the flue gas outlet of the furnace body and the bottom of the incinerator; the water vapor outlet is arranged in the flue gas pipeline at the bottom of the incinerator and at the rear end of the heat energy recycling device, and a fan is arranged in front of the water vapor outlet; the ammonia water liquid tank and the steam water tank are arranged above the high-temperature gas channel, and liquid flow control valve devices are arranged on the ammonia water liquid tank and the steam water tank; the outlet of the high-temperature gas channel is provided with a temperature measuring instrument, and the high-temperature gas channel is internally provided with a heat energy recycling device.
4. The garbage cutting preheating incineration steam dedusting and desulfurizing nitre integrated heat energy recycling process according to claim 1, c) water body cooling liquid phase desulfurizing steam smoke particulate matter purifying device, which is characterized in that: the cooling box is provided with an air inlet and an air outlet, and the upper end of the cooling box is provided with a cooling water tank; the lower end of the cooling water tank is communicated with a cooling pipe; a grid water baffle is arranged in the middle of the cooling pipe; a water outlet is arranged at the bottom of the cooling tank; a torsion hinge is arranged at the position of the water outlet and is in sealing connection with the water baffle; a water storage tank is arranged below the water baffle and is provided with a cone filtering net; an acid-base water body monitor is arranged in the water storage tank, a water pump is also arranged in the filtering tank, and an output pipeline on the water pump is connected with the sulfurous acid ammonia oxidation crystallization tank; and a sealing door is arranged on the cooling box body.
5. The garbage cutting preheating incineration steam dust removal and desulfurization nitrate integrated heat energy recycling process d) conical filter body dust removal centrifugal force dehydration device related to the garbage cutting preheating incineration steam dust removal and desulfurization nitrate integrated heat energy recycling process according to the claim 1, and is characterized in that: an atomized water spray head is arranged at the inlet of the cooling box, a folding plate is arranged in the cooling box, and a sealing door is arranged on the outer side of the cooling box; the dust removing cylinder is a cylinder, and a conical filter body is arranged in the cylinder; the rope and thread filtering material is arranged on the conical filtering body; the conical filter body is provided with a shaft lever, and the shaft lever is arranged on a bearing seat of the fixing frame; a motor is arranged on the shaft lever; the lower end of the dust removing cylinder is provided with a water outlet; a torsion spring hinge is arranged at the position of the water outlet and is in sealing connection with the water baffle; a filtering water storage tank is arranged below the water baffle; the filtering water storage tank is provided with a cone filtering net, a water pump is arranged in the filtering water storage tank, and an output pipeline arranged on the water pump is connected with the ammonium sulfite crystallization tank device; and a gas comprehensive detector is arranged at the position of a flue gas outlet of the dust removing cylinder.
6. The waste cutting preheating incineration steam dedusting and desulfurizing nitre integrated heat energy recycling process as claimed in claim 1 relates to e) an oxygen-free hot-melt waste plastic pressing brick and tile building material heat energy recycling device, which is characterized in that: the cone spiral preheating extruder is arranged in the high-temperature gas channel; the transmission device of the speed regulating motor is connected with the large-diameter end of the cone spiral preheating extruder; a charging hole is arranged at the large-diameter end of the conical spiral preheating extruder; the small-diameter end of the conical spiral preheating extruder is provided with a garbage plastic and auxiliary material mixture outlet; the garbage and plastic mixture brick and tile pressing mold is set behind the feeding transmission device, and the brick and tile pressing power unit is set over the mold.
7. The garbage cutting preheating incineration steam dedusting and denitration integrated heat energy recycling process as claimed in claim 1 relates to f) a device for recycling heat energy of converting waste plastics into heavy oil by anaerobic cracking, and is characterized in that: the cone spiral preheating extruder is arranged in the high-temperature gas channel and is provided with a transmission device; the charging hopper and the charging opening are arranged at the large-diameter end of the conical spiral preheating extruder; the small-diameter end of the conical spiral preheating extruder is a plastic liquid outlet; an air blocking cylinder is arranged at the outlet end of the plastic liquid and is connected with the cracking cylinder; the cracking cylinder is provided with a temperature transition automatic control power switch, and a power signal output by the power switch is connected with an electromagnetic control valve of a steam inlet; the cracking cylinder is divided into an inner cylinder and an outer cylinder; holes and reinforcing strips with different sizes are arranged on an outer cylinder arranged on the cracking cylinder; the inner cylinder is a sealing cylinder, a transmission shaft is arranged in the inner cylinder, a speed regulating motor is arranged on the transmission shaft, and an arched spiral scraper is arranged on the transmission shaft of the speed regulating motor; an oil-gas pipeline arranged in the cracking cylinder is connected with a condenser, and a heavy oil pipeline of the condenser is connected with a storage cylinder; a combustible gas return pipeline is arranged on the heavy oil pipeline and connected with the combustion furnace; a waste material cylinder is arranged at one end of the cracking cylinder, and a spiral sealing discharging machine is arranged at the lower end of the waste material cylinder; a baffle is arranged at the outlet of the sealing and discharging machine and is in sealing connection with the torsion spring hinge; and a steam heater is also arranged in the high-temperature gas channel, the water body input valve is connected with the heater, the heater is of a calandria structure, and the output port of the heater is connected with the steam input electromagnetic valve.
CN202111119138.XA 2021-09-16 2021-09-16 Integrated heat energy recycling process for removing dust, sulfur and nitrate from garbage cutting preheating incineration steam Withdrawn CN114263908A (en)

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN117029002A (en) * 2023-08-28 2023-11-10 云南绿色能源有限公司 Cloud computing-based intelligent control system and method for garbage incineration
CN117250133A (en) * 2023-11-16 2023-12-19 国建大数据科技(辽宁)有限公司 Smart city large-scale data acquisition method and system

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN117029002A (en) * 2023-08-28 2023-11-10 云南绿色能源有限公司 Cloud computing-based intelligent control system and method for garbage incineration
CN117029002B (en) * 2023-08-28 2023-12-29 云南绿色能源有限公司 Cloud computing-based intelligent control system and method for garbage incineration
CN117250133A (en) * 2023-11-16 2023-12-19 国建大数据科技(辽宁)有限公司 Smart city large-scale data acquisition method and system
CN117250133B (en) * 2023-11-16 2024-02-20 国建大数据科技(辽宁)有限公司 Smart city large-scale data acquisition method and system

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Application publication date: 20220401