CN215259242U - Jet ignition type methane treatment device - Google Patents
Jet ignition type methane treatment device Download PDFInfo
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- CN215259242U CN215259242U CN202120974882.7U CN202120974882U CN215259242U CN 215259242 U CN215259242 U CN 215259242U CN 202120974882 U CN202120974882 U CN 202120974882U CN 215259242 U CN215259242 U CN 215259242U
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Abstract
The jet ignition type methane treatment device comprises a methane pressurizing and conveying device, a bypass differential pressure type chemical injection and pollution discharge device and an injection type single-pipe combustion starting device. The bypass differential pressure type medicine injection and sewage discharge device comprises a magnetic turning plate ventilation electromagnetic valve, a magnetic turning plate reed pipe, a low-pressure end stop valve, a magnetic turning plate gas-phase electromagnetic valve, a high-pressure end stop valve, a magnetic turning plate gas-phase cutting hand valve, a magnetic turning plate body, a magnetic turning plate liquid-phase electromagnetic valve, a pH meter, a magnetic turning plate liquid-phase cutting hand valve, a magnetic turning plate sewage discharge hand valve, a desulfurization liquid barrel, a PU tee joint, a sewage discharge end stop valve and a sewage discharge electromagnetic valve; the methane pressurizing and conveying device comprises a methane pressurizing pump, a methane conveying regulating valve, a turbine air inlet switch valve, a storage tank body, a storage tank air pressure transmitter and a filler. The utility model is suitable for a marsh gas recovery comprehensive utilization behind the sewage anaerobic treatment, including marsh gas wet-type desulfurization, preliminary condensation dehydration, pressure boost transport, the function of burning energy supply.
Description
Technical Field
The utility model belongs to the technical field of methane recovery and comprehensive utilization, and relates to a jet ignition type methane treatment device.
Background
The marsh gas is a combustible mixed gas generated by organic substances through the fermentation of anaerobic microorganisms, and is mainly composed of 50% -80% of CH 420 to 40 percent of CO 20 to 5 percent of N2A small amount of H2、H2S、NH3And the like. The primary methane often carries a large amount of water, and is mixed with unavailable impurities and harmful gases, so that the primary methane cannot be directly combusted and discharged as fuel; the purified methane is a combustible gas with a high heat value and is about 20-25 MJ/m3The heat value of 1 cubic high-purity methane is equal to about 0.8kg of standard coal, and the antiknock property is better. The biogas purification system is generally divided into processes of water removal, desulfurization, pressurization, filtration, deamination and the like, wherein the desulfurization of biogas is a key technology.
In the general engineering application of sewage treatment, because the methane generation rate is unbalanced, a gas storage cabinet is required to be arranged for adjustment, and the pressure and the flow rate of the methane are stabilized by an external load. The prior art mainly comprises a floating roof type methane pressure stabilizing cabinet and a double-membrane type methane pressure stabilizing cabinet. The floating roof type methane pressure stabilizing cabinet has high manufacturing cost, and the condensed water in the gas storage air bag can influence the counterweight of the air bag and the service life of the whole methane pressure stabilizing cabinet; the outer membrane of the double-membrane type methane pressure stabilizing cabinet needs to be repeatedly ventilated and exhausted, so that the service life of a motor is influenced, and the membrane is easy to age and short in service life. In any kind of pressure stabilizing cabinet, the purpose is to stabilize the unbalanced gas production rate, and the pressure of the biogas is always maintained at a lower level.
In general engineering application of sewage treatment, an emergency torch is usually arranged at the periphery of a gas production pool and consists of a combustion chamber, an ejector nozzle, a supporting structure, an ignition and flame monitoring system, a flame arrester, a combustion-supporting fan, a main actuator, condensate water discharge, a PLC control cabinet and other main components, wherein the PLC controls the main actuator and the combustion-supporting fan to adjust the combustion amount.
In the engineering application with methane conveying requirement, in order to improve the phenomenon of insufficient methane pressure, the methane is more fully combusted, the firepower is larger, the methane is generally pressurized to a certain pressure, the numerical value is related to the type and the power of a used booster pump, and the methane can be more fully produced due to the negative pressure action of the pump, so that the methane-generating device is widely applied to various civil methane-generating tanks and methane is conveyed in a long distance.
In a common industrial methane treatment place, sodium carbonate is used as an alkali source for desulfurization liquid, the total alkalinity is controlled to be 0.3-0.6N, and NaHCO is3：Na2CO3Not less than 5 and the pH value is 8.2-8.5. Generally, two feeding modes, namely pump pressurization and differential pressure vacuum suction, are adopted, the former needs to consume electric power and needs to be provided with a set of control program capable of calculating the feeding proportion, and the latter needs to be provided with a pressure reducing device on a pipeline, so that large head loss is caused, the phenomenon of back suction is serious, the suction stroke is limited, and the stable use of the device is influenced.
The gas turbine belongs to a continuous work-doing machine with high rotating speed, and due to the working characteristics of the turbine, the efficiency is high only under the high rotating speed, and the rotating speed is generally more than 10000 r/min. Due to strict requirements of working conditions, in small-sized and civil engineering application, a gas turbine is high in manufacturing difficulty, complex in combustion control and high in cost.
SUMMERY OF THE UTILITY MODEL
The utility model aims at overcoming the discretization problem of prior art, providing a marsh gas processing apparatus that can concentrate realization marsh gas purification, combustion control, pressurization transport function, reduce marsh gas treatment facility's volume and cost.
The technical scheme of the utility model:
the jet ignition type methane treatment device comprises a bypass differential pressure type chemical injection and pollution discharge device, a methane pressurization conveying device and an injection type single-pipe combustion starting device.
Comprises a bypass differential pressure type chemical injection and pollution discharge device, a methane pressurization conveying device and an injection type single-pipe combustion starting device. The bypass differential pressure type medicine injection and sewage discharge device comprises a magnetic turning plate ventilation electromagnetic valve, a magnetic turning plate reed pipe, a low-pressure end stop valve, a magnetic turning plate gas-phase electromagnetic valve, a high-pressure end stop valve, a magnetic turning plate gas-phase cutting hand valve, a magnetic turning plate body, a magnetic turning plate liquid-phase electromagnetic valve, a pH meter, a magnetic turning plate liquid-phase cutting hand valve, a magnetic turning plate sewage discharge hand valve, a desulfurization liquid barrel, a PU tee joint, a sewage discharge end stop valve and a sewage discharge electromagnetic valve; the magnetic turning plate gas phase cutting hand valve and the magnetic turning plate liquid phase cutting hand valve are respectively connected into gas/liquid phase of the storage tank body through threads, the magnetic turning plate gas phase electromagnetic valve is connected with a gas phase interface of the magnetic turning plate body and the magnetic turning plate gas phase cutting hand valve, the magnetic turning plate liquid phase electromagnetic valve is connected with a liquid phase interface of the magnetic turning plate body and the magnetic turning plate liquid phase cutting hand valve, and the pH meter is vertically inserted into a middle pipe section of the magnetic turning plate liquid phase electromagnetic valve and the magnetic turning plate liquid phase cutting hand valve; the low-pressure end stop valve is vertically arranged in the middle pipe section of the gas phase interface of the magnetic turning plate body and the magnetic turning plate gas phase electromagnetic valve, and the high-pressure end stop valve is vertically arranged in the middle pipe section of the magnetic turning plate gas phase electromagnetic valve and the magnetic turning plate gas phase cutting hand valve; the magnetic turning plate ventilation electromagnetic valve is arranged at the top of the magnetic turning plate body, the magnetic turning plate blowdown hand valve is arranged at the bottom of the magnetic turning plate body, and the magnetic turning plate dry reed pipe is attached to the magnetic turning plate body through a steel hoop; the low pressure end stop valve is connected with the desulfurization liquid barrel through a desulfurization liquid barrel liquid outlet PU pipe, two end interfaces of the PU tee joint are respectively connected with the desulfurization liquid barrel and the high pressure end stop valve through a desulfurization liquid barrel air inlet PU pipe, the middle interface of the PU tee joint is connected with the bucket through a bucket air inlet PU pipe, and the sewage discharge electromagnetic valve is fixedly connected with a sewage discharge outlet at the bottommost part of the storage tank body.
The methane pressurizing and conveying device comprises a methane pressurizing pump, a methane conveying regulating valve, a turbine air inlet switch valve, a storage tank body, a storage tank air pressure transmitter and a filler; the biogas booster pump is fixedly connected between the primary biogas pipe connector and the gas inlet connector at the top of the storage tank body, the biogas conveying regulating valve is fixedly connected with the gas supply connector at the top of the storage tank body, and the turbine gas inlet switch valve is fixedly connected with the turbine gas inlet connector at the top of the storage tank body; the storage tank pressure transmitter is installed in a gas phase area of the storage tank body through stop valve threads, the filler is filled at the lower end of the storage tank body, and the height of the filler is controlled to be 1.1-1.2 times higher than the designed liquid level.
The injection type single-tube combustion starting device comprises a water bucket, a combustion chamber air-feeding electromagnetic valve, an injector, a combustion chamber, an ignition device, an injection type single-tube combustion starting device hearth, a slag discharge port, a water inlet ball valve, a water inlet nozzle, an exhaust port thermometer, a turbocharger driving wheel, a turbocharger driven wheel and a mixed alkali circulating pump; the combustion chamber air supply electromagnetic valve is connected between a gas phase interface of the storage tank body and the ejector, the combustion chamber is connected to an outlet of the ejector, the ignition device is inserted into a flame tube of the combustion chamber, and a hearth of the injection type single-tube combustion starting device is connected to an airflow outlet of the combustion chamber; the slag discharge port is arranged at the bottom of the hearth of the injection type single-tube combustion starting device, the water inlet ball valve is connected with the downstream pipe section of the blow-down electromagnetic valve, the water inlet spray head is embedded at the upper end of the hearth of the injection type single-tube combustion starting device and is not more than 45 degrees and is aligned to the position of sprayed air flow, and the exhaust port thermometer is arranged on an outlet pipeline of the hearth of the injection type single-tube combustion starting device; an outlet pipeline of a hearth of the injection type single-pipe combustion starting device is connected with a driving wheel of a turbocharger, the driving wheel of the turbocharger and a driven wheel of the turbocharger transmit motion through a shaft, the driving wheel of the turbocharger and a mixed alkali circulating pump transmit motion through a belt, and an inlet/outlet of the mixed alkali circulating pump is respectively connected with a gas phase/liquid phase of a storage tank body.
The desulfurization liquid barrel, the water barrel, the low-pressure end stop valve, the high-pressure end stop valve and the sewage discharge end stop valve are in flexible connection through PU pipe materials, a desulfurization liquid barrel liquid outlet PU pipe communicated with the low-pressure end stop valve extends into the bottom of the desulfurization liquid barrel, and a desulfurization liquid barrel gas inlet PU pipe communicated with the high-pressure end stop valve is connected to a top cover of the desulfurization liquid barrel through a PU tee; in a similar way, a water barrel liquid outlet PU pipe communicated with the sewage discharge end stop valve extends into the bottom of the water barrel, and a water barrel air inlet PU pipe communicated with the high-pressure end stop valve is connected into the top cover of the water barrel through a PU tee joint.
The slag discharge port of the injection type single-pipe combustion starting device can be used for regularly cleaning the dust and the precipitated salt of the water after combustion.
The space of the injection type single-pipe combustion engine device is open, high-temperature gas transfers energy to steam, the temperature is reduced, the gas pressure cannot rise, but expands and flows out from a discharge port to push a driving wheel of a turbocharger to do work, because the gas expands in the open space, the gas can be discharged along a path with the minimum resistance, namely the direction of the driving wheel of the turbocharger, and the gas is transferred to a driven wheel of the turbocharger and a mixed alkali circulating pump through the driving wheel of the turbocharger;
the medium that injection formula single tube combustion engine device produced vapor is different according to the operating mode of blowdown, has 2 kinds of condition: during pollution discharge, desulfurization rich solution enters a hearth of the injection type single-tube combustion engine, water vapor is generated and crystallized to separate out salt, and the salt is left at a slag discharge port; when the sewage is not discharged, clean water pumped out by differential pressure in the water barrel enters the water barrel, and only water vapor is generated.
Before the device is used, all the electromagnetic valves and the hand valves are in a closed state, the biogas booster pump is started, the air pressure of the storage tank is increased, when a certain air pressure exists in the storage tank body, the reading of the air pressure transmitter of the storage tank exceeds 10kPa, and the device has a commissioning condition.
Starting the PLC, and enabling the device to enter a sequential control state: (1) opening a combustion chamber air supply electromagnetic valve, and discharging air in the storage tank through an ejector-combustion chamber pipeline by virtue of the air filling process of the storage tank; (2) delaying for 2min, automatically completing the actions of medicine injection and pollution discharge according to the steps, and synchronously executing ignition; (3) delaying for 5min, stopping the biogas booster pump after the turbocharging reaches a steady state, and only starting, exhausting and pressurizing when the air pressure of the storage tank is less than 10 kPa.
The utility model discloses improve the marsh gas recovery comprehensive utilization behind the sewage anaerobic treatment, adopt less control unit, retrench valve, fan quantity among the original marsh gas processing system, accomplished a series of functions including marsh gas wet flue gas desulfurization, preliminary condensation dehydration, pressure boost transport, burning energy supply. The biogas booster pump has few starting times, the pressure balance is realized by PLC control, the biogas can meet self-use, the pressurized purified biogas can be stably conveyed outwards, a native biogas generation area is maintained in a negative pressure state, and anaerobic reaction is promoted. Therefore, the utility model has the advantages that: the device overcomes the discretization problem in the prior art, provides a treatment device which can realize the functions of biogas purification, combustion control and pressurized conveying in a centralized way, and reduces the volume and the manufacturing cost of biogas treatment equipment.
Drawings
Fig. 1 is a schematic structural diagram of the utility model.
Fig. 2 is a flow chart of sequential control of injection and pollution discharge of the bypass differential pressure type injection and pollution discharge device.
FIG. 3 is a flow chart of ignition and water feeding sequential control of the injection type single-tube combustion engine.
FIG. 4 is a schematic view showing the connection of PU pipes of the desulfurization solution tank.
Fig. 5 is a schematic diagram of an ejector.
FIG. 6 is a gas path diagram of a single-tube combustor.
In the figure: 1-a biogas booster pump, 2-a biogas conveying regulating valve, 3-a turbine air inlet switch valve, 4-a magnetic turning plate air inlet electromagnetic valve, 5-a magnetic turning plate reed pipe, 6-a low-pressure end stop valve, 7-a magnetic turning plate gas phase electromagnetic valve, 8-a high-pressure end stop valve, 9-a magnetic turning plate gas phase cutting hand valve, 10-a magnetic turning plate body, 11-a magnetic turning plate liquid phase electromagnetic valve, 12-a pH meter, 13-a magnetic turning plate liquid phase cutting hand valve, 14-a storage tank body, 15-a storage tank air pressure transmitter, 16-a filler, 17-a magnetic turning plate blow-off hand valve, 18-a desulfurization liquid barrel, a 19-PU tee joint, 20-a blow-off end stop valve, 21-a blow-off electromagnetic valve, 22-a water barrel, 23-a combustion chamber air inlet electromagnetic valve and a 24-ejector, 25-combustion chamber, 26-ignition device, 27-injection type single-tube combustion starting device hearth, 28-slag discharge port, 29-water inlet ball valve, 30-water inlet nozzle, 31-exhaust port thermometer, 32-turbocharger driving wheel, 33-turbocharger driven wheel, 34-mixed alkali circulating pump, 35-desulfurization liquid barrel liquid outlet PU pipe, 36-desulfurization liquid barrel air inlet PU pipe, 37-water barrel air inlet PU pipe and 38-water barrel liquid outlet PU pipe.
The specific implementation mode is as follows:
the following further describes the contents of the present invention with reference to the embodiments of the drawings.
FIG. 1 shows: the jet ignition type biogas treatment device comprises a biogas pressurization conveying device A, a bypass differential pressure type chemical injection and pollution discharge device B, an injection type single-pipe combustion starting device C and a matched control system.
The bypass differential pressure type medicine injection and sewage discharge device B consists of a magnetic turning plate ventilation electromagnetic valve 4, a magnetic turning plate reed pipe 5, a low-pressure end stop valve 6, a magnetic turning plate gas phase electromagnetic valve 7, a high-pressure end stop valve 8, a magnetic turning plate gas phase cutting hand valve 9, a magnetic turning plate body 10, a magnetic turning plate liquid phase electromagnetic valve 11, a pH meter 12, a magnetic turning plate liquid phase cutting hand valve 13, a magnetic turning plate sewage discharge hand valve 17, a desulfurization liquid barrel 18, a PU tee joint 19, a sewage discharge end stop valve 20 and a sewage discharge electromagnetic valve 21; the magnetic flap gas phase cutting hand valve 9 and the magnetic flap liquid phase cutting hand valve 13 are respectively connected into gas/liquid phase of a storage tank body 14 through threads, the magnetic flap gas phase electromagnetic valve 7 is connected with a gas phase interface of the magnetic flap body 10 and the magnetic flap gas phase cutting hand valve 9, the magnetic flap liquid phase electromagnetic valve 11 is connected with a liquid phase interface of the magnetic flap body 10 and the magnetic flap liquid phase cutting hand valve 13, the pH meter 12 is vertically inserted into a middle pipe section of the magnetic flap liquid phase electromagnetic valve 11 and the magnetic flap liquid phase cutting hand valve 13, the low-pressure end stop valve 6 is vertically arranged at the gas phase interface of the magnetic flap body 10 and the middle pipe section of the magnetic flap gas phase electromagnetic valve 7, the high-pressure end stop valve 8 is vertically arranged at the middle pipe section of the magnetic flap gas phase electromagnetic valve 7 and the magnetic flap gas phase cutting hand valve 9, the magnetic flap ventilation electromagnetic valve 4 is arranged at the top of the magnetic flap body 10, and the magnetic flap blowdown hand valve 17 is arranged at the bottom of the magnetic flap body 10, the magnetic turning plate reed pipe 5 is attached to the magnetic turning plate body 10 by a steel hoop; the low-pressure end stop valve 6 is connected with the desulfurization liquid barrel 18 through a desulfurization liquid barrel liquid outlet PU pipe 35, two end interfaces of the PU tee joint 19 are respectively connected with the desulfurization liquid barrel 18 and the high-pressure end stop valve 8 through a desulfurization liquid barrel air inlet PU pipe 36, the middle interface of the PU tee joint 19 is connected with the water barrel 22 through a water barrel air inlet PU pipe 37, the blow-off electromagnetic valve 21 is fixedly connected with a blow-off port at the bottommost part of the storage tank body 14, the blow-off end stop valve 20 is connected out from an outlet pipeline of the blow-off electromagnetic valve 21 and is connected with the water barrel 22 through a water barrel liquid outlet PU pipe 38.
The methane pressurizing and conveying device A consists of a methane pressurizing pump 1, a methane conveying regulating valve 2, a turbine air inlet switch valve 3, a storage tank body 14, a storage tank air pressure transmitter 15 and a filler 16; the biogas booster pump 1 is fixedly connected between a native biogas pipe connector and an air inlet connector at the top of the storage tank body 14, the biogas conveying regulating valve 2 is fixedly connected at the air inlet connector at the top of the storage tank body 14, the turbine air inlet switch valve 3 is fixedly connected at the turbine air inlet connector at the top of the storage tank body 14, the storage tank pressure transmitter 15 is installed in a gas phase area of the storage tank body 14 through a stop valve thread, the filler 16 is arranged at the lower end of the storage tank body 14, and the top is controlled to be 1.2 times as high as a designed liquid level.
The injection type single-tube combustion engine device consists of a water barrel 22, a combustion chamber air-feeding electromagnetic valve 23, an injector 24, a combustion chamber 25, an ignition device 26, an injection type single-tube combustion engine device hearth 27, a slag discharge port 28, a water inlet ball valve 29, a water inlet nozzle 30, an exhaust port thermometer 31, a turbocharger driving wheel 32, a turbocharger driven wheel 33 and a mixed alkali circulating pump 34; the combustion chamber air-feeding electromagnetic valve 23 is connected between a gas phase interface of the storage tank body 14 and the ejector 24, the combustion chamber 25 is connected to an outlet of the ejector 24, the ignition device 26 is inserted into a flame tube of the combustion chamber 25, the injection type single-tube combustion engine device hearth 27 is connected to an airflow jet port of the combustion chamber 25, the slag discharge port 28 is installed at the bottom of the injection type single-tube combustion engine device hearth 27 and is 0.5m away from the ground, the water inlet ball valve 29 is connected to a downstream pipe section of the blowdown electromagnetic valve 21, the water inlet nozzle 30 is embedded at the upper end of the injection type single-tube combustion engine device hearth 27 and jets airflow at an angle of less than or equal to 45 degrees, the exhaust port thermometer 31 is installed on an outlet pipeline of the injection type single-tube combustion engine device hearth 27, the outlet pipeline of the injection type single-tube combustion engine device hearth 27 is connected to the turbocharger driving wheel 32, and the turbocharger driving wheel 32 and the turbocharger driven wheel 33 transmit movement through a shaft, the turbocharger driving wheel 32 and the mixed alkali circulating pump 34 transmit motion through a belt, and the inlet/outlet of the mixed alkali circulating pump 34 is respectively connected to the gas phase/liquid phase of the storage tank body 14.
The desulfurization liquid barrel 18, the water barrel 22, the low-pressure end stop valve 6, the high-pressure end stop valve 8 and the sewage discharge end stop valve 20 are in flexible connection by adopting PU pipe materials, a desulfurization liquid barrel liquid outlet PU pipe 35 communicated with the low-pressure end stop valve 6 extends into the bottom of the desulfurization liquid barrel 18, and a desulfurization liquid barrel air inlet PU pipe 36 communicated with the high-pressure end stop valve 8 is connected to the top cover of the desulfurization liquid barrel 18 through a PU tee joint 19; similarly, a water barrel outlet PU pipe 38 communicated with the sewage discharge end stop valve 20 extends into the bottom of the water barrel 22, and a water barrel inlet PU pipe 37 communicated with the high pressure end stop valve 8 is connected into the top cover of the water barrel 22 through a PU tee joint 19.
As shown in fig. 2, the bypass differential pressure type medicine injection and sewage discharge device is composed of a magnetic turning plate ventilation electromagnetic valve 4, a magnetic turning plate reed pipe 5, a low-pressure end stop valve 6, a magnetic turning plate gas-phase electromagnetic valve 7, a high-pressure end stop valve 8, a magnetic turning plate gas-phase cutting hand valve 9, a magnetic turning plate body 10, a magnetic turning plate liquid-phase electromagnetic valve 11, a pH meter 12, a magnetic turning plate liquid-phase cutting hand valve 13, a magnetic turning plate sewage discharge hand valve 17, a desulfurization liquid barrel 18, a PU tee joint 19, a sewage discharge end stop valve 20 and a sewage discharge electromagnetic valve 21, and the process operations of medicine injection and pressurization are executed according to the sequence control flow shown in the figure.
FIG. 3 shows: the injection type single-tube combustion engine device consists of a water barrel 22, a combustion chamber air-feeding electromagnetic valve 23, an injector 24, a combustion chamber 25, an ignition device 26, a hearth 27, a slag discharge port 28, a water inlet ball valve 29, a water inlet spray head 30, an exhaust port thermometer 31, a turbocharger driving wheel 32, a turbocharger driven wheel 33 and a mixed alkali circulating pump 34, and the process operation of ignition and water addition is executed according to the sequence control flow shown in the figure.
FIG. 4 shows: the desulfurization liquid barrel 18 passes through a bypass differential pressure type pesticide injection and sewage disposal device.
FIG. 5 shows: and (3) air is introduced into the ejector 24, the pressurized biogas is fully mixed with air in the mixing chamber II through the Laval nozzle I, and the mixture is decelerated and stabilized in the diffuser III and enters the next section for combustion.
FIG. 6 shows: the combustion chamber 25 is composed of a swirler, a flame tube and a shell. The combustion chamber 25 is charged, the spark plug of the ignition device 26 extends into the flame tube, the airflow stirred by the vortex device is ignited to form a high-temperature area for stable combustion, the temperature of the shell is reduced by the airflow through the air gap of the flame tube, and the airflow is sprayed into the next section to generate steam.
The slag discharge port 28 of the injection type single-pipe combustion starting device can be used for periodically cleaning the dust and the precipitated salt of the inlet water after combustion.
The space of the injection type single-pipe combustion engine device is open, high-temperature gas transfers energy to steam, the temperature is reduced, the gas pressure is not increased, but expanded and flows out from a discharge port to push a driving wheel 32 of the turbocharger to do work, because the gas is expanded in the open space, the gas is discharged along a path with the minimum resistance, namely the direction of the driving wheel 32 of the turbocharger, and is transferred to a driven wheel 33 of the turbocharger and a mixed alkali circulating pump 34 through the driving wheel 32 of the turbocharger;
the medium that injection formula single tube combustion engine device produced vapor is different according to the operating mode of blowdown, has two kinds of situations: during pollution discharge, desulfurization rich liquid enters a hearth 27 of the injection type single-tube combustion engine device from a water inlet nozzle 30, water vapor is generated and crystallized to separate out salt, and the salt is left at a slag discharge port 28; when the sewage is not discharged, clean water pumped out by differential pressure in the water barrel 22 enters, and only water vapor is generated.
The low-pressure end stop valve 6, the high-pressure end stop valve 8 and the sewage end stop valve 20 are all stop valves with quick insertion.
Before using, all solenoid valves, hand valve all are in the closed condition, start marsh gas booster pump 1, make the atmospheric pressure of storage tank rise, have had certain atmospheric pressure when storage tank body 14, and storage tank pressure transmitter 15 readings exceeds 10kPa, and the device possesses the condition of commissioning.
Starting the PLC, and enabling the device to enter a sequential control state:
1. opening the combustion chamber air-feeding electromagnetic valve 23, and discharging the air of the storage tank body 14 through pipelines of the ejector 24 and the combustion chamber 25 by virtue of the air-feeding process of the storage tank;
2. delaying for 2min, automatically completing the actions of medicine injection and pollution discharge according to the steps, and synchronously executing ignition;
3. delaying for 5min, stopping the biogas booster pump 1 after the turbocharging reaches a steady state, and only starting, exhausting and boosting when the air pressure of the storage tank is less than 10 kPa.
The program performs the automatic medicine injection and pollution discharge actions in the step 2 according to the following step specifications:
opening a magnetic flap gas-phase cutting hand valve 9 and a magnetic flap liquid-phase cutting hand valve 13, wherein the magnetic flap is communicated with the storage tank.
And secondly, opening the low-pressure end stop valve 6 and the high-pressure end stop valve 8, and communicating the magnetic turnover plate with the desulfurization liquid barrel.
Thirdly, the PLC controls the injection of the first desulfurization solution: and a PLC function key is switched to run, the system judges that the air pressure transmitter 15 of the storage tank meets the condition, the magnetic turning plate ventilation electromagnetic valve 4 is controlled to be opened, pressurized gas in the storage tank is injected into the desulfurization liquid barrel-18 through a PU pipe communicated with the high-pressure end stop valve 8, so that the air pressure in the desulfurization liquid barrel 18 is increased, and the pressurized desulfurization liquid is injected into the low-pressure end stop valve 6 from the bottom of the desulfurization liquid barrel-18 through another PU pipe and flows into the magnetic turning plate body 10.
Feeding back the desulfurization liquid level of the magnetic turning plate body 10 to the PLC by the magnetic turning plate reed pipe-5, and finishing the first medicine injection when the desulfurization liquid level reaches the set level value of 80 percent: and (3) closing the magnetic turning plate ventilation electromagnetic valve 4, opening the magnetic turning plate gas-phase electromagnetic valve 7, opening the magnetic turning plate liquid-phase electromagnetic valve 11, and enabling the desulfurization liquid of the magnetic turning plate body to flow into the storage tank body, wherein the feedback of the magnetic turning plate reed pipe 5 is below 3% due to the volume ratio of the desulfurization liquid to the storage tank body.
And fifthly, the sulfur-containing methane enters from the bottom of the storage tank and is fully mixed with the desulfurization solution under the action of the filler 16, so that the hydrogen sulfide is absorbed by the desulfurization solution.
Judging whether the desulfurization solution after absorbing the hydrogen sulfide becomes rich solution (the condition is that the pH value is less than 7.8) through a numerical value fed back by a pH meter 12, and controlling the injection operation of regulating the pH value by a PLC (programmable logic controller) when the pH value of the desulfurization solution is lower than a set value: closing the magnetic turning plate gas-phase electromagnetic valve 7 and the magnetic turning plate liquid-phase electromagnetic valve 11 to disconnect the magnetic turning plate body 10 from the storage tank body 14; and (3) opening the magnetic turnover plate ventilation electromagnetic valve 4, injecting pressurized gas in the storage tank into the desulfurization liquid barrel 18 through a PU pipe communicated with the high-pressure end stop valve 8, so that the internal air pressure of the desulfurization liquid barrel 18 is increased, and pressing desulfurization liquid to be injected from the bottom of the desulfurization liquid barrel-18 through another PU pipe and enter the low-pressure end stop valve 6 to converge into the magnetic turnover plate body 10.
Seventhly, feeding the doctor solution level of the magnetic turning plate body 10 back to the PLC by a magnetic turning plate reed pipe 5, and adjusting pH to finish medicine injection when the doctor solution level reaches a set level value of 80 percent: and closing the magnetic turning plate ventilation electromagnetic valve 4, opening the magnetic turning plate gas-phase electromagnetic valve 7, opening the magnetic turning plate liquid-phase electromagnetic valve 11, and enabling the desulfurization liquid of the magnetic turning plate body 10 to flow into the storage tank body 14.
And allowing the PLC to repeatedly execute the medicine injection action for adjusting the pH value, and keeping the desulfurization solution in the storage tank to be normally used within a period of time.
Ninthly, when the dosing step is not executed, the system simultaneously meets the conditions that the pH value is less than 7.8, the liquid level of the magnetic turning plate is higher than 50 percent, and the sewage discharge action of the doctor solution (rich solution) in the PLC operation storage tank is performed: and (3) opening the sewage discharge electromagnetic valve 21 until the liquid level fed back by the magnetic turning plate reed pipe 5 is lower than 5%, closing the sewage discharge electromagnetic valve 21, and ending sewage discharge.
At this time, the execution condition of step (c) is satisfied again, the system executes the drug injection action for adjusting the pH value, and the doctor solution in the storage tank is kept to be normally used.
⑪ designing desulfurizing liquid barrels 22 with different volumes according to different yields of hydrogen sulfide, and controlling the replenishment of the desulfurizing liquid in 2-3 days: closing the low-pressure end stop valve 6 and the high-pressure end stop valve 8, and disconnecting the magnetic turnover plate from the desulfurization liquid barrel 18; pulling out the two PU pipes on the end cover of the desulfurization liquid barrel 18, discharging the air pressure (purified methane) of the desulfurization liquid barrel 18, opening the end cover of the desulfurization liquid barrel 18, and adding fresh desulfurization liquid; recovering two PU pipes on the end cover, and opening a low-pressure end stop valve 6 and a stop valve 8; similarly, the high-pressure end stop valve 8 and the sewage discharge end stop valve 20 can be used in cooperation to supplement clean water to the water bucket 22.
The program performs the auto-ignition operation of step 2 according to the following step specification:
firstly, the PLC opens the combustion chamber air supply electromagnetic valve 23, and low-pressure methane is mixed with air by the ejector and enters the combustion chamber.
Secondly, starting the ignition device 26, igniting for 10s, feeding back the temperature of the exhaust port thermometer 31 to be greater than 80 ℃ (the maximum possible ambient temperature), entering the next step, and otherwise, sending out an ignition failure alarm by the program.
Thirdly, the water inlet ball valve 29 is opened manually to a certain opening degree after ignition is successful, and the opening degree of the ball valve is adjusted according to whether the slag discharging port 28 is wet or drips within a period of time, so that the inlet water can be completely evaporated.
And fourthly, in the running process, the feedback temperature of the exhaust port thermometer 31 is less than 95 ℃, the program sends out flameout alarm, the ignition device is automatically started, the interval is 3 seconds, the ignition is carried out for 5 times, the feedback is still less than 95 ℃, and the program sends out alarm of ignition failure.
Claims (4)
1. The jet ignition type methane treatment device is characterized in that: the device comprises a bypass differential pressure type chemical injection and sewage discharge device, a methane pressurization conveying device and an injection type single-pipe combustion starting device, wherein the bypass differential pressure type chemical injection and sewage discharge device comprises a magnetic turning plate ventilation electromagnetic valve, a magnetic turning plate reed pipe, a low-pressure end stop valve, a magnetic turning plate gas-phase electromagnetic valve, a high-pressure end stop valve, a magnetic turning plate gas-phase cutting hand valve, a magnetic turning plate body, a magnetic turning plate liquid-phase electromagnetic valve, a pH meter, a magnetic turning plate liquid-phase cutting hand valve, a magnetic turning plate sewage discharge hand valve, a desulfurization liquid barrel, a PU tee joint, a sewage discharge end stop valve and a sewage discharge electromagnetic valve; the magnetic turning plate gas phase cutting hand valve and the magnetic turning plate liquid phase cutting hand valve are respectively connected into gas/liquid phase of the storage tank body through threads, the magnetic turning plate gas phase electromagnetic valve is connected with a gas phase interface of the magnetic turning plate body and the magnetic turning plate gas phase cutting hand valve, the magnetic turning plate liquid phase electromagnetic valve is connected with a liquid phase interface of the magnetic turning plate body and the magnetic turning plate liquid phase cutting hand valve, and the pH meter is vertically inserted into a middle pipe section of the magnetic turning plate liquid phase electromagnetic valve and the magnetic turning plate liquid phase cutting hand valve; the low-pressure end stop valve is vertically arranged in the middle pipe section of the gas phase interface of the magnetic turning plate body and the magnetic turning plate gas phase electromagnetic valve, and the high-pressure end stop valve is vertically arranged in the middle pipe section of the magnetic turning plate gas phase electromagnetic valve and the magnetic turning plate gas phase cutting hand valve; the magnetic turning plate ventilation electromagnetic valve is arranged at the top of the magnetic turning plate body, the magnetic turning plate blowdown hand valve is arranged at the bottom of the magnetic turning plate body, and the magnetic turning plate dry reed pipe is attached to the magnetic turning plate body through a steel hoop; the low pressure end stop valve is connected with the desulfurization liquid barrel through a desulfurization liquid barrel liquid outlet PU pipe, two end interfaces of the PU tee joint are respectively connected with the desulfurization liquid barrel and the high pressure end stop valve through a desulfurization liquid barrel air inlet PU pipe, the middle interface of the PU tee joint is connected with the bucket through a bucket air inlet PU pipe, and the sewage discharge electromagnetic valve is fixedly connected with a sewage discharge outlet at the bottommost part of the storage tank body.
2. The injection ignition type biogas processing apparatus according to claim 1, characterized in that: the methane pressurizing and conveying device comprises a methane pressurizing pump, a methane conveying regulating valve, a turbine air inlet switch valve, a storage tank body, a storage tank air pressure transmitter and a filler; the biogas booster pump is fixedly connected between the native biogas pipe connector and the gas inlet connector at the top of the storage tank body, the biogas conveying regulating valve is fixedly connected with the gas supply connector at the top of the storage tank body, and the turbine gas inlet switch valve is fixedly connected with the turbine gas inlet connector at the top of the storage tank body; the storage tank pressure transmitter is installed in a gas phase area of the storage tank body through stop valve threads, the filler is filled at the lower end of the storage tank body, and the height of the filler is controlled to be 1.1-1.2 times higher than the designed liquid level.
3. The injection ignition type biogas processing apparatus according to claim 1, characterized in that: the injection type single-tube combustion starting device comprises a water bucket, a combustion chamber air-feeding electromagnetic valve, an injector, a combustion chamber, an ignition device, an injection type single-tube combustion starting device hearth, a slag discharge port, a water inlet ball valve, a water inlet nozzle, an exhaust port thermometer, a turbocharger driving wheel, a turbocharger driven wheel and a mixed alkali circulating pump; the combustion chamber air supply electromagnetic valve is connected between a gas phase interface of the storage tank body and the ejector, the combustion chamber is connected to an outlet of the ejector, the ignition device is inserted into a flame tube of the combustion chamber, and a hearth of the injection type single-tube combustion starting device is connected to an airflow outlet of the combustion chamber; the slag discharge port is arranged at the bottom of the hearth of the injection type single-tube combustion starting device, the water inlet ball valve is connected with the downstream pipe section of the blow-down electromagnetic valve, the water inlet spray head is embedded at the upper end of the hearth of the injection type single-tube combustion starting device and is not more than 45 degrees and is aligned to the position of sprayed air flow, and the exhaust port thermometer is arranged on an outlet pipeline of the hearth of the injection type single-tube combustion starting device; an outlet pipeline of a hearth of the injection type single-pipe combustion starting device is connected with a driving wheel of a turbocharger, the driving wheel of the turbocharger and a driven wheel of the turbocharger transmit motion through a shaft, the driving wheel of the turbocharger and a mixed alkali circulating pump transmit motion through a belt, and an inlet/outlet of the mixed alkali circulating pump is respectively connected with a gas phase/liquid phase of a storage tank body.
4. A jet ignition type biogas processing apparatus according to claim 1 or claim 2 or claim 3, characterized in that: the desulfurization liquid barrel, the water barrel, the low-pressure end stop valve, the high-pressure end stop valve and the sewage discharge end stop valve are in flexible connection through PU pipe materials, a desulfurization liquid barrel liquid outlet PU pipe communicated with the low-pressure end stop valve extends into the bottom of the desulfurization liquid barrel, and a desulfurization liquid barrel gas inlet PU pipe communicated with the high-pressure end stop valve is connected to a top cover of the desulfurization liquid barrel through a PU tee; in a similar way, a water barrel liquid outlet PU pipe communicated with the sewage discharge end stop valve extends into the bottom of the water barrel, and a water barrel air inlet PU pipe communicated with the high-pressure end stop valve is connected into the top cover of the water barrel through a PU tee joint.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202120974882.7U CN215259242U (en) | 2021-05-09 | 2021-05-09 | Jet ignition type methane treatment device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202120974882.7U CN215259242U (en) | 2021-05-09 | 2021-05-09 | Jet ignition type methane treatment device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN215259242U true CN215259242U (en) | 2021-12-21 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202120974882.7U Active CN215259242U (en) | 2021-05-09 | 2021-05-09 | Jet ignition type methane treatment device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN215259242U (en) |
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2021
- 2021-05-09 CN CN202120974882.7U patent/CN215259242U/en active Active
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