CN112880407A - Energy supply kiln based on multi-energy conversion - Google Patents

Abstract

The invention discloses an energy supply kiln based on multi-energy conversion, which comprises a kiln body and is characterized in that: the kiln comprises a kiln body, and is characterized in that a heavy oil inlet is formed in the left side of the kiln body, an air inlet is formed in the right side of the kiln body, an identification ball is arranged inside the kiln body, a multifunctional conversion shell is arranged above the kiln body, a waste gas treatment shell is arranged above the multifunctional conversion shell, a combustion judgment mechanism is arranged inside the identification ball, a multifunctional conversion mechanism is arranged inside the multifunctional conversion shell, a waste gas treatment mechanism is arranged inside the waste gas treatment shell, the combustion judgment mechanism comprises a judgment pipeline, the judgment pipeline is arranged inside the heavy oil inlet, an impeller is connected to the inner bearing of the judgment pipeline, judgment balls are evenly connected to the outer side of the impeller in a sliding mode, and friction factors between the judgment balls and the impeller are different.

Description

Energy supply kiln based on multi-energy conversion

Technical Field

The invention relates to the technical field of kilns, in particular to an energy supply kiln based on multi-energy conversion.

Background

The kiln or furnace means a furnace for firing ceramic ware and sculptures or fusing enamel to the surface of metal ware. Generally build with brick and stone, can make the various specifications of size as required, can adopt combustible gas, oil or electricity to come the operation, in the kiln of current burning heavy oil, most can't judge whether the burning in the kiln is abundant, and do not have temperature regulation and control device, and current kiln is low to the utilization ratio of energy, the exhaust treatment device of current kiln is comparatively simple simultaneously, purification waste gas that can not be fine leads to harmful gas to emit into in the air, consequently, it is very necessary to design the energy supply kiln based on many energy conversions that can discern the burning condition and energy utilization is higher.

Disclosure of Invention

The invention aims to provide an energy supply kiln based on multi-energy conversion, which solves the problems in the background technology.

In order to solve the technical problems, the invention provides the following technical scheme: an energy supply kiln based on multi-energy conversion comprises a kiln body and is characterized in that: the left side of the kiln body is provided with the heavy oil import, the right side of the kiln body is provided with air intlet, the inside of the kiln body is provided with the discernment ball, the top of the kiln body is provided with the multi-energy conversion shell, the top of multi-energy conversion shell is provided with the exhaust-gas treatment shell, the inside of discernment ball is provided with burning judgement mechanism, the inside of multi-energy conversion shell is provided with the multi-energy conversion mechanism, the inside of exhaust-gas treatment shell is provided with exhaust-gas treatment mechanism.

According to the above technical scheme, the mechanism is judged in burning is including judging the pipeline, judge the inside of pipeline setting at the heavy oil import, the inner bearing of judging the pipeline is connected with the impeller, the even sliding connection in the outside of impeller has the ball of judging, it is all different to judge the friction factor between ball and the impeller, the outside of judging the ball is provided with the control membrane, the downside of judging the pipeline is provided with the inflation bag, the inside of impeller is provided with friction portion, inflation bag pipe connection is in friction portion.

According to the technical scheme, the combustion judgment mechanism comprises an air inlet pipeline, the air inlet pipeline is arranged in an air inlet, an extension part is arranged on the outer side of the air inlet pipeline, a control cylinder is connected to a pipeline on one side of the extension part, a control shell is connected to a pipeline on one side of the control cylinder, an air speed part is arranged in the control shell, a speed control part is arranged on the inner side of the air speed part, a detection part is arranged on the inner side of the speed control part, and a temperature bag is arranged on one side of the control shell.

According to the technical scheme, one side pipe connection of friction portion has the pressure valve, the downside pipe connection of pressure valve has the output, the output is two upper and lower cavities, one side of output is provided with three hornblocks, three hornblocks's outside sliding connection has the temperature shell, the inside of temperature shell is filled with two kinds of liquids that thermal expansion coefficient is different, the outside of temperature shell is provided with flexible membrane, the outside of flexible membrane is provided with the set casing, set casing pipe connection is on the control shell.

According to the technical scheme, one side pipe connection of set casing has the balance chamber, the balance chamber divide into three cavity in the left side, middle and right sides, the inside of balance chamber is provided with the scissors valve, one side of scissors valve is provided with the control valve, one side pipe connection of control valve has the compression portion, one side of compression portion is provided with the explosion chamber, two upper and lower cavities of dividing into of explosion chamber, the inside of cavity is provided with the elastic membrane under the explosion chamber, the inside of cavity is provided with the adjustment ball on the explosion chamber.

According to the technical scheme, the multi-energy conversion mechanism comprises a conversion shell, a floating shell is arranged inside the conversion shell, the floating shell is elastically connected to the conversion shell, a shrinkage bag is arranged inside the floating shell, the shrinkage bag is connected to the conversion shell through a pipeline, an eccentric valve is connected to one side of the shrinkage bag through a pipeline, a rotating needle is arranged inside the eccentric valve, a connecting portion is arranged inside the rotating needle, a connecting rod is connected to one side of the connecting portion through a bearing, and the connecting rod is connected to the floating shell through a bearing.

According to the technical scheme, one side pipe connection of eccentric valve has the recovery shell, the inner bearing of retrieving the shell is connected with wind-force and judges the shell, the inside of wind-force judgement shell is provided with the stock solution room, the outside of retrieving the shell is provided with the temperature membrane, the outside pipe connection of temperature membrane has the control room, two cavities about the control room divide into, the right cavity pipe connection of control room is on the stock solution room, the inside of control room is provided with torque switch.

According to the technical scheme, the exhaust-gas treatment mechanism includes the intake pipe, the outside of intake pipe evenly is provided with the absorption tube, the inside of absorption tube is provided with the density valve, the inside of density valve is provided with the density ball, one side of density valve is provided with the discernment bag, one side pipe connection of discernment bag has the balanced valve of anti-dress.

According to the technical scheme, the upper side of the reversely-installed balance valve is provided with a nitrogen oxide absorption shell, a solution ball is arranged inside the nitrogen oxide absorption shell, one side bearing of the solution ball is connected with a density rod, one side bearing of the density rod is connected with a centrifugal wheel, the inner side of the centrifugal wheel is elastically connected with a stopping plate, and the outer side of the stopping plate is clamped and provided with an air outlet pipeline.

According to the technical scheme, one side of nitrogen oxide absorption shell is provided with the colloid filter screen, one side of colloid filter screen is provided with the weight valve, one side pipe connection of weight valve has the gasbag, one side of gasbag is provided with shakes and beats the ball, one side of shaking and beating the ball is provided with the elasticity rope, the other end fixed mounting of elasticity rope is on the colloid filter screen.

Compared with the prior art, the invention has the following beneficial effects: in the invention, the raw materials are mixed,

(1) the combustion judgment mechanism is arranged, so that the combustion condition and the combustion effect in the kiln body can be judged, and corresponding treatment measures are taken;

(2) the multifunctional conversion mechanism is arranged, so that the energy which cannot be absorbed and is generated by combustion can be utilized secondarily;

(3) through being provided with exhaust-gas treatment mechanism for can carry out secondary treatment to the produced waste gas of heavy oil burning, and carry out secondary recycle to relevant energy.

Drawings

The accompanying drawings, which are included to provide a further understanding of the invention and are incorporated in and constitute a part of this specification, illustrate embodiments of the invention and together with the description serve to explain the principles of the invention and not to limit the invention. In the drawings:

FIG. 1 is a schematic overall perspective view of the present invention;

FIG. 2 is a schematic view of the structure of the combustion judging mechanism of the present invention;

FIG. 3 is a schematic structural view of the multi-energy conversion mechanism of the present invention;

FIG. 4 is a schematic structural view of an exhaust treatment mechanism of the present invention;

in the figure: 1. a kiln body; 2. heavy oil import; 3. an air inlet; 4. an identification ball; 5. a multifunctional conversion shell; 6. an exhaust gas treatment housing; 7. a combustion judgment mechanism; 71. a friction portion; 72. an impeller; 73. judging the ball; 74. an inflation bladder; 75. controlling a film; 76. a detection unit; 77. a speed control part; 78. a wind speed section; 79. a control cylinder; 710. an extension portion; 711. a temperature capsule; 712. an air intake duct; 713. a triangular block; 714. an output section; 715. a stationary case; 716. a flexible film; 717. a balancing chamber; 718. a scissor valve; 719. a control valve; 720. a compression section; 721. an elastic film; 722. adjusting the ball; 723. a pressure valve; 8. a multi-energy conversion mechanism; 81. a floating shell; 82. a contracting balloon; 83. a connecting portion; 84. rotating the needle; 85. an eccentric valve; 86. a conversion shell; 87. a wind power judging shell; 88. a liquid storage chamber; 89. a temperature film; 810. a control room; 811. a torque switch; 9. an exhaust gas treatment mechanism; 91. an air inlet pipe; 92. an absorber tube; 93. a density valve; 94. identifying a capsule; 95. reversely installing a balance valve; 96. a nitrogen oxide absorbing shell; 97. a solution ball; 98. a density rod; 99. an air outlet pipe; 910. a weight valve; 911. a colloid filter screen; 912. an air bag; 913. vibrating and hitting the ball; 914. an elastic cord.

Detailed Description

The technical solutions in the embodiments of the present invention will be clearly and completely described below with reference to the drawings in the embodiments of the present invention, and it is obvious that the described embodiments are only a part of the embodiments of the present invention, and not all of the embodiments. All other embodiments, which can be derived by a person skilled in the art from the embodiments given herein without making any creative effort, shall fall within the protection scope of the present invention.

Referring to fig. 1-4, the present invention provides the following technical solutions: an energy supply kiln based on multi-energy conversion comprises a kiln body 1 and is characterized in that: a heavy oil inlet 2 is formed in the left side of the kiln body 1, an air inlet 3 is formed in the right side of the kiln body 1, an identification ball 4 is arranged inside the kiln body 1, a multifunctional conversion shell 5 is arranged above the kiln body 1, a waste gas treatment shell 6 is arranged above the multifunctional conversion shell 5, a combustion judgment mechanism 7 is arranged inside the identification ball 4, a multifunctional conversion mechanism 8 is arranged inside the multifunctional conversion shell 5, and a waste gas treatment mechanism 9 is arranged inside the waste gas treatment shell 6; the combustion judging mechanism is used for judging the combustion condition and the combustion effect inside the kiln body and making corresponding treatment measures, the multi-energy conversion mechanism is used for secondarily utilizing the energy which cannot be absorbed and is generated by combustion, and the waste gas treatment mechanism is used for secondarily treating the waste gas generated by the combustion of the heavy oil and secondarily recycling the related energy.

The combustion judgment mechanism 7 comprises a judgment pipeline, the judgment pipeline is arranged inside the heavy oil inlet 2, an impeller 72 is connected to an inner bearing of the judgment pipeline, a judgment ball 73 is evenly connected to the outer side of the impeller 72 in a sliding mode, friction factors between the judgment ball 73 and the impeller 72 are different, a control film 75 is arranged on the outer side of the judgment ball 73, an expansion bag 74 is arranged on the lower side of the judgment pipeline, a friction part 71 is arranged inside the impeller 72, and an expansion air bag pipeline is connected to the friction part 71; in the oil inlet process, the impeller rotates with constant torque continuously, the rotating speed of the impeller changes due to different viscosities of the entering heavy oil, friction factors among the judgment balls are different, different numbers of judgment balls can be thrown out at different rotating speeds, the size of a heavy oil inlet is controlled by a gap between the control membrane and the impeller, the smaller the gap is, the smaller the inlet is, and even the heavy oil inlet can be cut off, the expansion bladder expands when the temperature rises, pressure is transmitted to the friction part during expansion, the friction force between the friction part and the impeller is increased, the rotating speed of the impeller is reduced, the viscosity of the heavy oil is judged through centrifugal force, the higher the viscosity of the heavy oil is, the higher the heat value is, the rotating speed of the constant-torque impeller is reduced along with the increase of the viscosity of the heavy oil, the smaller the number of the thrown judgment balls is, the smaller the gap between the control membrane and the impeller is, the smaller the opening size of the heavy, the heavy oil with high heat value is fed in a small amount and the heavy oil with low heat value is fed in a large amount, so that the stability of the total heat value is ensured, the expansion bag at the lower side of the pipeline can be judged to identify the change of the temperature, when the injected heavy oil starts to burn, the expansion bag is caused to expand rapidly to transfer the pressure to the friction part, so that the friction force is increased steeply, the rotation of the impeller is stopped, the friction ball is retracted into the impeller, the heavy oil inlet is stopped at the moment, after the burning is finished, the friction force is reduced, the impeller can rotate, the viscosity condition of the heavy oil is judged through the difference of centrifugal force through the steps, corresponding feeding measures are taken, and meanwhile, the opening and closing of the opening are.

The combustion determination mechanism 7 includes an air intake duct 712, the air intake duct 712 is disposed inside the air inlet 3, an extension portion 710 is disposed outside the air intake duct 712, a control cylinder 79 is connected to a duct on one side of the extension portion 710, a control housing is connected to a duct on one side of the control cylinder 79, an air speed portion 78 is disposed inside the control housing, a speed control portion 77 is disposed inside the air speed portion 78, a detection portion 76 is disposed inside the speed control portion 77, and a temperature bag 711 is disposed on one side of the control housing; the detection part can quantitatively spray a small amount of hydrogen and starts to burn after being sprayed, the expansion size of the speed control part can be regulated and controlled by the combustion condition, so that the friction force applied to the speed control part is regulated, the speed of the speed control part is reduced, the rotating speed of the wind speed part is reduced, the pressure inside the control cylinder is controlled, the extension degree of the extension part and the extension length of the extension part can be controlled, the diameter of the outer wall of the air inlet pipeline can be controlled, the temperature bag is arranged inside the kiln body, when the temperature is overhigh, liquid inside the control shell can be sucked out, the pressure inside the control cylinder is reduced, the opening of the air inlet pipeline is reduced, even the opening is closed, when air starts to enter, the oxygen concentration in the air is judged through burning, when the concentration is higher, the burning intensity of the hydrogen of the detection part is high, and the friction force of the speed control part is increased, and then the rotating speed of the speed control part is reduced to drive the rotating speed of the outer wind speed part to be reduced, so that the blowing-in speed of air is reduced, when the oxygen concentration is lower, the combustion intensity is reduced, so that the friction force of the speed control part is reduced, and further the rotating speed of the wind speed part is reduced, so that the air inlet speed of the air inlet pipeline is reduced, the air inlet speed is different corresponding to different oxygen concentrations, the air exhaust speed is different, so that the exhaust oxygen amount is maintained at a certain stable value, the excessive air is prevented from entering or the exhaust oxygen amount is not enough, the temperature change in the kiln body can be identified by the temperature bag, when the temperature is too high, the heavy oil is judged to be combusting, at the moment, the temperature bag expands, the liquid in the control shell is sucked out, so that the hydraulic pressure in the control cylinder is reduced, the extension part is attached to the air inlet pipeline, the air inlet is cut off, and the concentration of the oxygen exhausted, and then the rate of discharging of air is controlled according to oxygen concentration, keeps the volume of the oxygen of letting in invariable, simultaneously, controls the size that opens of air inlet according to the inside temperature variation of kiln body, prevents that the inside heat from spilling over in the combustion process.

A pressure valve 723 is connected to a pipeline on one side of the friction part 71, an output part 714 is connected to a pipeline on the lower side of the pressure valve 723, the output part 714 is divided into an upper cavity and a lower cavity, a triangular block 713 is arranged on one side of the output part 714, a temperature shell is connected to the outer side of the triangular block 713 in a sliding mode, two kinds of liquid with different thermal expansion coefficients are filled in the temperature shell, a flexible membrane 716 is arranged on the outer side of the temperature shell, a fixed shell 715 is arranged on the outer side of the flexible membrane 716, and the fixed shell 715 is connected to; when the temperature is not at a certain value, two kinds of liquid in the temperature shell can generate pressure difference on two sides of the triangular block to drive the triangular block to rotate, the triangular block rotates and simultaneously extrudes the output part to lead out the pressure difference by the output part, the fixed shell has good thermal conductivity, the flexible membrane can not pass gas and the pressure is preset when the internal pressure of the flexible membrane is high, after combustion occurs, the pressure difference exists on two sides of the flexible membrane, the flexible membrane can expand or compress to output a pressure signal, the lower left channel is conducted when the pressure valve is in positive pressure, the lower right channel is conducted when the pressure valve is in negative pressure, the temperature change in the kiln body after heavy oil combustion is judged by the temperature shell, when the temperature is too high, the upper output part is extruded to generate positive pressure, the judgment that the introduction amount of the heavy oil is too much at the moment, the device can control the friction force in the friction part to adjust the introduction amount of the heavy oil, and when, when the temperature is too low, extrude the lower cavity of output portion, produce the negative pressure, the signal can be derived this moment, the device can combine oxygen concentration to judge that it leads to make the burning insufficient or because the feeding is too little to lead to, both sides pressure difference undersize after the burning, it is too little to judge oxygen input volume this moment, can make the device with hydraulic signal transmission to the control shell in, make extension portion extend, lead to the air opening to enlarge, put into more air, reach through above-mentioned step and judge the internal and external pressure difference of kiln after the burning through two kinds of liquid and the flexible membrane of different expansion coefficients and the pressure condition, and carry out real-time adjustment to the input volume of heavy oil and air.

A balance chamber 717 is connected to a pipeline on one side of the fixed shell 715, the balance chamber 717 is divided into a left cavity, a middle cavity and a right cavity, a scissor valve 718 is arranged inside the balance chamber 717, a control valve 719 is arranged on one side of the scissor valve 718, a compression portion 720 is connected to a pipeline on one side of the control valve 719, an explosion chamber is arranged on one side of the compression portion 720 and divided into an upper cavity and a lower cavity, an elastic membrane 721 is arranged inside the lower cavity of the explosion chamber, and an adjusting ball 722 is arranged inside the upper cavity of the explosion chamber; when the temperature does not reach the required standard, negative pressure is introduced into the left chamber of the balance chamber, so that the pressure in the left force of the balance chamber is reduced, one side of the scissor valve is moved leftwards, the right chamber is connected with the fixed shell, when the internal pressure of the kiln body after combustion is greater than or equal to the preset pressure, the pressure of the balance chamber with the chambers towards the left direction is not changed or reduced, when the pressures of the left chamber and the right chamber of the balance chamber are reduced, the control valve is controlled to be opened, a hydraulic signal is introduced into the compression part, the left side and the right side of the lower chamber of the explosion chamber are respectively filled with hydrogen and oxygen, the expansion degree of the elastic membrane can be controlled by adjusting the size of the ball, when the temperature in the kiln body is judged to be not reach the desired temperature and the pressure difference does not exist between the two sides after combustion, the reason that the temperature is too low is judged to be caused by too little amount of the introduced heavy oil, at the, the friction force of the friction part is reduced. The rotating speed is increased to increase the input amount of the heavy oil, when the temperature is too low and the pressure difference at two sides is too small, the pressure at two sides of the balance chamber is reduced, the situation of insufficient combustion is judged to be generated at the moment, the insufficient combustion of the heavy oil with high viscosity can cause the carbon precipitation, the combustion efficiency is seriously influenced, at the moment, the control valve is opened, hydraulic pressure is led into the compression part from the control valve to cause the compression part to compress, the elastic die is driven to expand, hydrogen and oxygen are rapidly extruded out, the extruded hydrogen and oxygen are exploded under the condition of high temperature to generate severe high temperature, the precipitated carbon is shattered and oxidized, meanwhile, when the viscosity of the introduced heavy oil is too low, the expansion of the adjusting ball is controlled to offset the air pressure change generated by the compression of the compression bag, so that explosion is not generated, the method comprises the steps of judging the cause of the over-low temperature through the balance chamber, neutralizing the viscosity of the heavy oil and judging whether the insufficient combustion occurs to generate explosion or not to remove carbon deposition.

The multifunctional conversion mechanism 8 comprises a conversion shell 86, a floating shell 81 is arranged inside the conversion shell 86, the floating shell 81 is elastically connected to the conversion shell 86, a contraction bag 82 is arranged inside the floating shell 81, the contraction bag 82 is connected to the conversion shell 86 through a pipeline, an eccentric valve 85 is connected to one side of the contraction bag 82 through a pipeline, a rotating needle 84 is arranged inside the eccentric valve 85, a connecting part 83 is arranged inside the rotating needle 84, a connecting rod is connected to one side of the connecting part 83 through a bearing, and the connecting rod is connected to the floating shell 81 through a bearing; the gas exhausted from the kiln is introduced into the conversion shell, the conversion shell is filled with liquid with certain density, the floating shell can be maintained at the middle part under normal conditions, when the gas is introduced, the shrinkage bag expands, the density of the gas introduced into the shrinkage bag can be judged through the rising or falling of the floating shell, the floating shell rises or falls, the connecting rod connected to one side of the floating shell can be driven to rotate by the bearing, the connecting part connected to one side of the connecting rod is driven to rotate by the bearing, the rotating force is amplified and transmitted to the rotating needle by the connecting part, the on-off condition of the eccentric valve can be controlled through the rotation of the rotating needle, when the gas introduced into the conversion shell contains a large amount of heavy oil steam, the gas density is increased, the shrinkage bag is led to descend, the connecting rod is driven to rotate, the rotating needle is driven to rotate, the eccentric valve is opened to form a backflow passage, the gas introduced into the eccentric valve is introduced, the gas which is probably introduced into the shrinkage bag is maintained in a normal fluctuation range, which indicates that the gas in the shrinkage bag has no value of secondary utilization, the gas is directly introduced into the waste gas treatment mechanism and is discharged into the air after treatment, when the density of the gas in the shrinkage bag is smaller, the gas is judged to be caused by the excessive shrinkage bag due to the overhigh temperature of the gas in the shrinkage bag, at the moment, the floating shell moves upwards, the backflow channel is closed, the heat recovery channel is opened, the heat in the channel is recovered for the second time, and the gas is discharged into the waste gas treatment mechanism after the recovery is finished, and the purposes of judging whether the gas has the recovery value and how to recover the gas according to the density are achieved through the steps.

A recycling shell is connected to a pipeline on one side of the eccentric valve 85, a wind power judging shell 87 is connected to an inner bearing of the recycling shell, a liquid storage chamber 88 is arranged in the wind power judging shell 87, a temperature film 89 is arranged on the outer side of the recycling shell, a control chamber 810 is connected to a pipeline on the outer side of the temperature film 89, the control chamber 810 is divided into a left cavity and a right cavity, a pipeline on the right cavity of the control chamber 810 is connected to the liquid storage chamber 88, and a torque switch 811 is arranged in the control chamber 810; after high-temperature gas discharged by the multifunctional conversion shell is discharged into the recovery shell, the wind power judgment shell is driven to rotate, power is generated to generate energy, the liquid in the temperature film can be heated, the liquid in the temperature film flows, the amount of the liquid flowing into the temperature film is equal to that of the liquid flowing out of the temperature film, when the pressure on two sides of the control chamber is reduced, the torque switch is opened under the action of the torque switch and discharges the liquid in the control chamber, power is generated through the flow rate of the discharged air, and when the flow rate is reduced to a certain speed, the liquid thrown out of the liquid storage chamber under the action of centrifugal force is reduced, so that the pressure on the left side of the control chamber is reduced, the liquid flowing through the temperature film can take away the heat in the high-temperature air, and because the total amount of the liquid in the temperature film is unchanged, when the temperature of the high-temperature air is reduced to a certain value, the expansion degree of the temperature, make the pressure on control room right side decline, the both sides pressure of controlling the membrane all descends this moment, leads to the torque switch to rotate, emits inside gas, reaches make full use of high-temperature gas's velocity of flow and heat through above-mentioned step to whether automatic judgement utilizes completely, independently will utilize the gas outgoing who finishes completely after utilizing completely.

The waste gas treatment mechanism 9 comprises an air inlet pipe 91, absorption pipes 92 are uniformly arranged on the outer side of the air inlet pipe 91, a density valve 93 is arranged inside the absorption pipes 92, a density ball is arranged inside the density valve 93, an identification bag 94 is arranged on one side of the density valve 93, and a reverse-mounted balance valve 95 is connected to one side of the identification bag 94 through a pipeline; the gas is discharged into the gas inlet pipe, the gas inlet pipe is stopped after entering a part of gas and continuously rotates after stopping, the interior of the absorption pipe is filled with aqueous solution, the density valve shell determines the opening and closing conditions of the absorption pipe according to the density of the flowing liquid, when the introduced liquid is aqueous solution, the density ball floats upwards, the density valve is stopped, when the introduced liquid is organic solution, the density ball sinks to open the density valve, the identification bag can identify the pressure and transmit the pressure to the reverse balance valve, the pressure transmitted by the identification bags on two sides can be mutually offset, the reverse balance valve identifies that the pressure exists on the outer side and is immediately stopped at the gas outlet pipeline, when the outer side has no pressure, the reverse balance valve is opened, after the gas is introduced, the organic matter contained in the gas is absorbed by the aqueous solution, the organic solution is dissolved in the water and continuously extruded to the density valve under the action of centrifugal force, when oil is extruded, the density valve is opened and is thrown away fluid to keep closing again after fluid is thrown away, fluid is thrown away on the discernment bag, discernment bag transmission pressure, and fluid is thrown away and is just slided and derive on the discernment bag, the pressure of judging arbitrary two corresponding discernment bags when the balanced valve of anti-dress is all the same, will open the pipeline of giving vent to anger, with gas outgoing, carry out follow-up operation, reach the water absorption organic matter and separate it with the density valve through above-mentioned step, and can judge whether the organic matter has been absorbed totally through whether there is the pressure differential between arbitrary two corresponding discernment bags.

A nitrogen oxide absorption shell 96 is arranged on the upper side of the reversely-mounted balance valve 95, a solution ball 97 is arranged inside the nitrogen oxide absorption shell 96, a density rod 98 is connected to a bearing on one side of the solution ball 97, a centrifugal wheel is connected to a bearing on one side of the density rod 98, a stop plate is elastically connected to the inner side of the centrifugal wheel, and an air outlet pipeline 99 is clamped and arranged on the outer side of the stop plate; after the gas is discharged organically, the gas is discharged into a nitrogen oxide absorption chamber, the nitrogen oxide absorption chamber is filled with sodium hydroxide solution, the nitrogen oxide in the waste gas can react with the gas to cause the density of the internal liquid to change, a solution ball can sink after the density changes to drive a density rod to rotate to drive a centrifugal rotation, so that a stop plate is thrown out to be matched with a gas outlet pipeline, the gas outlet pipeline is stopped, when the sodium hydroxide solution is completely consumed, the solution ball can sink to stop the gas from entering and start to update the internal solution, the nitrogen oxide in the waste gas is continuously absorbed and is judged whether to be completely absorbed, after the gas is completely absorbed, a centrifugal wheel does not rotate any more to separate the stop plate from the gas outlet pipeline, the internal gas is discharged, whether the sodium hydroxide solution is completely consumed can be judged through the density, when the sodium hydroxide solution is completely consumed, the gas inlet pipeline can be stopped and the internal solution can be, the removal condition of the nitrogen oxide is judged through the density through the steps, and the content of the sodium hydroxide in the solution can be judged through the change of the density.

A colloid filter screen 911 is arranged on one side of the nitrogen oxide absorption shell 96, a weight valve 910 is arranged on one side of the colloid filter screen 911, an air bag 912 is connected to one side of the weight valve 910 through a pipeline, a vibration ball 913 is arranged on one side of the air bag 912, an elastic rope 914 is arranged on one side of the vibration ball 913, and the other end of the elastic rope 914 is fixedly arranged on the colloid filter screen 911; the gas is finally dedusted after coming out of the nitrogen oxide absorption chamber, the rapping ball is fixed on the colloid filter screen by the elastic rope, the weight valve can identify the amount of dust remaining on the colloid filter screen and can convert the dust into a hydraulic signal to be transmitted to the air bag, the air bag expands to extrude the rapping ball, the rapping ball can be separated from the original position under the extrusion of the air bag and quickly knocked off to the colloid filter screens at two sides of the air bag under the action of the elastic rope to knock off the dust and knock off the dust deposited on the weight valve, at the moment, the pressure signal received by the air bag disappears, the air bag starts to recover, the rapping ball recovers under the action of the elastic rope because of the colloid filter screen, when the rapping ball is pulled out by the elastic rope, the filter screen vibrates secondarily, the dust deposited on the filter screen is judged, and when the amount is accumulated to a certain amount, the rapping ball is used for hitting the filter screen, and when the device is reset, the filter screen is hit secondarily to enable dust deposited on the filter screen to be shaken down, and the purpose of preventing the filter screen from being blocked by hitting the filter screen automatically and secondarily is achieved through the steps.

It is noted that, herein, relational terms such as first and second, and the like may be used solely to distinguish one entity or action from another entity or action without necessarily requiring or implying any actual such relationship or order between such entities or actions. Also, the terms "comprises," "comprising," or any other variation thereof, are intended to cover a non-exclusive inclusion, such that a process, method, article, or apparatus that comprises a list of elements does not include only those elements but may include other elements not expressly listed or inherent to such process, method, article, or apparatus.

Finally, it should be noted that: although the present invention has been described in detail with reference to the foregoing embodiments, it will be apparent to those skilled in the art that changes may be made in the embodiments and/or equivalents thereof without departing from the spirit and scope of the invention. Any modification, equivalent replacement, or improvement made within the spirit and principle of the present invention should be included in the protection scope of the present invention.

Claims (10)

1. An energy supply kiln based on multi-energy conversion comprises a kiln body (1), and is characterized in that: the left side of the kiln body (1) is provided with heavy oil import (2), the right side of the kiln body (1) is provided with air intlet (3), the inside of the kiln body (1) is provided with discernment ball (4), the top of the kiln body (1) is provided with multipotency conversion shell (5), the top of multipotency conversion shell (5) is provided with exhaust-gas treatment shell (6), the inside of discernment ball (4) is provided with burning judgement mechanism (7), the inside of multipotency conversion shell (5) is provided with multipotency conversion mechanism (8), the inside of exhaust-gas treatment shell (6) is provided with exhaust-gas treatment mechanism (9).

2. The multi-energy conversion based energy supply kiln as recited in claim 1, wherein: mechanism (7) is judged in burning is including judging the pipeline, judge the inside of pipeline setting at heavy oil import (2), the inner bearing of judging the pipeline is connected with impeller (72), the even sliding connection in outside of impeller (72) has judgement ball (73), the friction factor between judgement ball (73) and impeller (72) is all inequality, the outside of judgement ball (73) is provided with control membrane (75), the downside of judging the pipeline is provided with inflation bag (74), the inside of impeller (72) is provided with friction portion (71), inflation bag pipe connection is on friction portion (71).

3. The multi-energy conversion based energy supply kiln as claimed in claim 2, wherein: burning judges mechanism (7) and includes admission line (712), admission line (712) set up the inside in air intlet (3), the outside of admission line (712) is provided with extension portion (710), one side pipe connection of extension portion (710) has control cylinder (79), one side pipe connection of control cylinder (79) has the control shell, the inside of control shell is provided with wind speed portion (78), the inboard of wind speed portion (78) is provided with accuse fast portion (77), the inboard of accuse fast portion (77) is provided with detection portion (76), one side of control shell is provided with temperature bag (711).

4. The multi-energy conversion based energy supply kiln as claimed in claim 3, wherein: the pipeline connection of one side of friction portion (71) has pressure valve (723), the downside pipeline connection of pressure valve (723) has output portion (714), two upper and lower cavities are divided into in output portion (714), one side of output portion (714) is provided with triangle piece (713), the outside sliding connection of triangle piece (713) has the temperature shell, the inside of temperature shell is filled with two kinds of liquid that the coefficient of thermal expansion is different, the outside of temperature shell is provided with flexible membrane (716), the outside of flexible membrane (716) is provided with set casing (715), set casing (715) pipe connection is on the control shell.

5. The multi-energy conversion based energy supply kiln as claimed in claim 4, wherein: the utility model discloses a hydraulic pressure regulating device, including fixed shell (715), balancing chamber (717) are connected to one side pipe connection of fixed shell (715), balancing chamber (717) divide into three cavities of left side, middle and right side, the inside of balancing chamber (717) is provided with scissors valve (718), one side of scissors valve (718) is provided with control valve (719), one side pipe connection of control valve (719) has compression portion (720), one side of compression portion (720) is provided with the explosion room, the division of explosion room is two upper and lower cavities, the inside of cavity is provided with elastic membrane (721) under the explosion room, the inside of cavity is provided with adjustment ball (722) on the explosion room.

6. The multi-energy conversion based energy supply kiln as recited in claim 5, wherein: multipotency conversion mechanism (8) are including converting shell (86), the inside of converting shell (86) is provided with floating shell (81), floating shell (81) elastic connection is on converting shell (86), the inside of floating shell (81) is provided with shrink bag (82), shrink bag (82) pipe connection is on converting shell (86), one side pipe connection of shrink bag (82) has eccentric valve (85), the inside of eccentric valve (85) is provided with commentaries on classics needle (84), the inside of commentaries on classics needle (84) is provided with connecting portion (83), one side bearing of connecting portion (83) is connected with the connecting rod, the connecting rod bearing is connected on floating shell (81).

7. The multi-energy conversion based energy supply kiln as recited in claim 6, wherein: the utility model discloses a wind power generation device, including eccentric valve (85), one side pipe connection of retrieving the shell, retrieve the shell, the inner bearing of retrieving the shell is connected with wind-force and judges shell (87), the inside of shell (87) is judged to wind-force is provided with stock solution room (88), the outside of retrieving the shell is provided with temperature membrane (89), the outside pipe connection of temperature membrane (89) has control room (810), two cavities about control room (810) divide into, the right cavity pipe connection of control room (810) is on stock solution room (88), the inside of control room (810) is provided with torque switch (811).

8. The multi-energy conversion based energy supply kiln as recited in claim 7, wherein: exhaust-gas treatment mechanism (9) are including intake pipe (91), the outside of intake pipe (91) evenly is provided with absorbent tube (92), the inside of absorbent tube (92) is provided with density valve (93), the inside of density valve (93) is provided with the density ball, one side of density valve (93) is provided with discernment bag (94), one side pipe connection of discernment bag (94) has anti-equilibrium valve (95) of adorning.

9. The multi-energy conversion based energy supply kiln as recited in claim 8, wherein: the upside of reverse balance valve (95) of adorning is provided with nitrogen oxide and absorbs shell (96), the inside of nitrogen oxide absorption shell (96) is provided with solution ball (97), one side bearing of solution ball (97) is connected with density pole (98), one side bearing of density pole (98) is connected with the centrifugal wheel, the inboard elastic connection of centrifugal wheel has the shutoff board, the outside card of shutoff board with have outlet duct (99).

10. The multi-energy conversion based energy supply kiln as recited in claim 9, wherein: one side of nitrogen oxide absorption shell (96) is provided with colloid filter screen (911), one side of colloid filter screen (911) is provided with weight valve (910), one side pipe connection of weight valve (910) has gasbag (912), one side of gasbag (912) is provided with shakes and beats ball (913), one side of shaking and beating ball (913) is provided with elasticity rope (914), the other end fixed mounting of elasticity rope (914) is on colloid filter screen (911).

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