TW201544162A - Gas-liquid-solid separator, gas-liquid separator and plasma desulphuration and denitration apparatus comprising same - Google Patents

Abstract

Provided are a gas-liquid-solid separator, a gas-liquid separator and a plasma desulphuration and denitration apparatus. The gas-liquid-solid separator comprises a cylindrical shell, a filter core nested in the shell and a water discharge valve, wherein a gas inlet having a flange and a gas outlet having a flange are provided on a side face of the shell, a cyclone channel is formed between the shell and the filter core, the filter core comprises three coaxially nested columnar filter barrels, which are a sintered filter, an inner filter barrel and an outer filter barrel successively from inside to outside, and a plurality of filter holes are arranged on both the inner filter barrel and the outer filter barrel, and can be aligned or staggered to each other when the inner filter barrel; and the outer filter barrel rotate relative to each other. The gas-liquid separator has two coaxially nested columnar filter barrels, and a plurality of filter holes are arranged on both the columnar filter barrels and can be aligned or staggered to each other when the inner filter barrel and the outer filter barrel rotate relative to each other. The plasma desulphuration and denitration apparatus comprises the gas-liquid-solid separator and the gas-liquid separator.

Description

Gas-liquid-solid separator, gas-liquid separator and plasma desulfurization and denitration equipment

The invention relates to the field of industrial exhaust gas purification, in particular to a gas-liquid solid separator, a gas-liquid separator and a plasma sulfur removal and denitration device.

Sulfide and nitrogen oxide emissions are the main causes of air pollution and acid rain.

According to national statistics, the sulfur dioxide emissions of coal-fired power plants account for about 50% of the total emissions of sulfur dioxide. Therefore, the control of sulfide and nitrogen oxide emissions is related to the realization of energy-saving emission reduction targets.

For the purpose of desulfurization and denitrification, the traditional wet limestone-gypsum flue gas desulfurization technology (CA-WFGD) and ammonia selective catalytic reduction (NH ₃ -SCR) are still used in the industry. Desulfurization and denitrification, but the simple superposition of the two systems results in complex process and system, large occupied area, high investment and operating costs, and difficult to promote and apply on a large scale. In the process of wet flue gas desulfurization and denitrification, NO _X The Henry's constant of 90% or more of water-insoluble NO and NO at room temperature (25 ° C) is only 1.94 × 10 ^-8 mol / L ‧ Pa, three orders of magnitude lower than SO ₂ , only by regulating pH and The method of temperature is difficult to significantly increase the solubility of NO in the liquid phase, thus seriously restricting the efficiency of desulfurization and denitrification.

In order to solve the above technical problem, the Chinese patent of the publication No. CN101940871A discloses a simultaneous desulfurization and denitration system based on photochemical advanced oxidation, which is understood in conjunction with Fig. 1, the desulfurization and denitration system (1) includes a burner (11) ), electrostatic precipitator (12), Heat exchanger (13), shower (14), atomizing nozzle (15), ultraviolet lamp (16), circulation pump (17), self-adding liquid column (18), separation tower (19) and chimney (110) ).

In use, the H ₂ O ₂ solution is input through the intake pipe (111) of the liquid addition tower (18), and the ultraviolet light excited by the ultraviolet lamp (16) is used to excite and decompose H ₂ O ₂ to generate a hydroxyl group having strong oxidizing property. group (OH ^-), and further oxidation of NO _X in the flue gas removal and SO _2, the reaction product of sulfuric acid and nitric acid solution to be resource utilization, to generate the ammonia is added agricultural fertilizer.

In order to ensure the radiated light power, the above-mentioned desulfurization and denitration system (1) needs to be provided with a plurality of ultraviolet lamps (16), on the one hand, a wind resistance is formed in the shower (14), and a plurality of circulating pumps (17) are required to pump gas. On the other hand, there is a problem that the photoelectric conversion efficiency and the absorption efficiency are low, that is, the conversion of electric energy into light energy has a loss of energy, and when light energy is absorbed by H ₂ O ₂ through the ash black smoke containing a large amount of particulate matter, light is present again. The problem of incomplete attenuation and absorption, the photoelectric energy loss after photoelectric conversion loss and absorption, the actual utilization of electric energy is still low, and it is difficult to improve.

In addition, in the coal-fired process of thermal power plants, different types and qualities of coal (such as lignite, bituminous coal or pulverized coal) and different combustion conditions (whether or not the oxygen combustion and combustion temperature) can produce soot particles with different center particle sizes.

Therefore, the screening of different particle size soot particles has become a technical problem in the field of desulfurization and denitrification. After investigation of the existing market, it is found that the gas-liquid separators sold in the market cannot screen different central particle sizes according to the coal-fired conditions of thermal power plants. Soot particles.

The present inventors have in view of the practical difficulties of the above-mentioned conventional desulfurization and denitration system and the lack of improvement, and hope to provide a breakthrough design to enhance the practical effect, which is devoted to research and design, and has been engaged for many years. The professional technical knowledge and practical experience of related product design and production, and the results obtained from the research and design, finally developed a gas-liquid-solid separator, gas-liquid separator and plasma removal. Sulfur denitration equipment to provide users.

The technical problem to be solved by the present invention is to overcome the defects that the prior art gas-liquid separator can not screen the soot particles of different central particle sizes according to the coal burning condition, and provide a gas-liquid solid separator, a gas-liquid separator and a plasma thereof. In addition to the sulfur denitration equipment, the gas-liquid-solid separator can screen soot particles of different center sizes according to the coal-burning condition.

The present invention solves the above technical problem by the following technical solution: a gas-liquid-solid separator, characterized in that the gas-liquid-solid separator comprises a cylindrical casing, a filter element embedded in the casing and a drain valve, the side of the casing is provided with a flanged air inlet and a flanged exhaust port, and a swirling air duct is formed between the casing and the filter core, the axis of the air inlet And the axis of the exhaust port is offset from the axis of the housing, the air inlet, the swirling air channel and the exhaust port are in communication with each other, and the drain valve is disposed on a bottom surface of the housing and the swirling air passage Interconnected, the filter element comprises three coaxially nested column filter barrels, which are a sintered filter, an inner filter barrel and an outer filter barrel from the inside to the outside, the inner filter barrel and the outer filter barrel The upper average array has a plurality of filter holes that are aligned or offset from each other when the inner filter barrel and the outer filter barrel rotate relative to each other.

Preferably, the air inlet is disposed at a lower portion of the housing, and the air outlet is disposed at an upper portion of the housing, and the air inlet is provided with a first pressure gauge for testing fluid pressure in the air inlet, the row A second pressure gauge for testing fluid pressure in the exhaust port is disposed on the air port, and the inner filter bucket is provided with a pallet, and the inner filter bucket is fixedly connected to the sintered filter through the pallet.

A gas-liquid separator, characterized in that the gas-liquid separator comprises a cylindrical casing, a filter element embedded in the casing and a drain valve, and a flange is arranged on a side of the casing An air inlet and a flanged exhaust port, a swirling air duct is formed between the housing and the filter element, and an axis of the air inlet and an axis of the air outlet are offset from an axis of the housing The air inlet, the swirling air passage and the exhaust port are in communication with each other in sequence. The drain valve is disposed on a bottom surface of the housing and communicates with the swirling air duct. The filter element comprises two coaxially nested columns. Filter barrels are arranged on the column filter barrels with a plurality of filter holes, which can be aligned or offset with each other when rotated relative to each other.

Preferably, the two coaxially nested column filter buckets are respectively an outer filter bucket and an inner filter bucket, and the inner filter bucket is nested in the outer filter bucket, and the outer filter bucket is provided with a spiral A drain plate for guiding the helical movement of gas within the swirling air passage.

Preferably, the air inlet and the air outlet are both disposed at an upper portion of the housing, and an upper portion of the outer filter bucket is provided with a baffle for blocking gas flowing in from the air inlet The drain plate is directed such that the drain plate directs the gas spiral into the bottom of the filter element.

Preferably, the inner filter bucket is provided with a plurality of annular fixing brackets and a plurality of swirlers, and the swirlers are fixed in the inner filter buckets by the annular fixing brackets, and the swirling directions of the swirlers The direction of drainage is the same as that of the drain plate.

Preferably, the gas-liquid separator further comprises a dish-shaped liquid collecting filter and a liquid guiding tube, and the casing, the liquid collecting filter, the liquid guiding tube and the drain valve are in communication with each other in sequence, and the collecting liquid The array on the filter has a plurality of collection filter holes, and the dish-shaped cavity of the liquid collection filter is used to collect soot particles.

A plasma desulfurization and denitration device, characterized in that the plasma desulfurization and denitration device comprises an ammonia supply system, a gas liquid solid separator as described above and a gas liquid separator as described above, the plasma removal The sulfur denitration apparatus further includes a first gas-solid separator, a gas-liquid separator, a first medium plasma, a reaction tank and a second gas-solid separator, the gas-liquid-solid separator, the first gas The solid separator, the gas-liquid separator, the first medium plasma, the reaction tank, and the second gas-solid separator are in communication with each other, and the ammonia supply system and the reaction tank are in communication with each other.

Preferably, the plasma sulfur removal and denitration device further comprises a nano plasma, the gas liquid The separator, the nano-plasma and the first dielectric plasma are connected to each other in turn, and the nano-plasma mainly functions to enhance the concentration of the radical. For the working condition requiring high emission index, the nano-plasma can be used.

Preferably, the first gas-solid separator comprises a first intake duct, a second intake duct, a first exhaust duct, a second exhaust duct, a filter core and a filter chamber, and the filter core is arranged In the filter chamber, the first intake duct is configured to pass fluid to the first exhaust duct through the filter core, and the second intake duct is configured to pass fluid to the second through the filter core An exhaust duct, the first intake duct and the second intake duct are oppositely disposed and capable of maintaining a direction of fluid relative to each other.

Preferably, the filter core is folded, and the filter chamber is provided with a plurality of fixing rods supported at the folded corners of the filter core to separate adjacent two folded layers.

Preferably, the first intake duct, the second intake duct, the first exhaust duct and the second exhaust duct communicate with the filter chamber through a diverging portion, the first intake duct The diverging portion and the diverging portion of the second intake duct are for distributing fluid and mitigating the flow rate, and the diverging portion of the first exhaust duct and the diverging portion of the second exhaust duct are used for collecting and filtering The fluid, the adjacent two folded layers of the filter core have an angle of 5° to 15°.

Preferably, the first gas-solid separator further comprises a soot temporary storage chamber having a rotating partition plate and a gate switch, and a partition plate is disposed between the soot temporary storage chamber and the filter chamber, the partition plate and the partition plate a gap is disposed between the inner wall surfaces of the first gas-solid separator, and the soot temporary storage chamber and the filter chamber communicate with each other through the nip, the gate switch is configured to control the rotation of the rotating partition plate to release the soot temporary storage chamber Soot particles inside.

Preferably, the first gas-solid separator further comprises a soot conveying vehicle, the soot conveying vehicle comprises a box body and a wheel disposed at an end of the box body, the soot temporary storage chamber is passed through a conveying pipe and The cabinets are connected to each other.

Preferably, the first gas-solid separator is provided with a first temperature control unit having a heat exchanger Equipment, the heat exchanger is a surface heat exchanger or a direct contact heat exchanger.

Preferably, both sides of the nano-plasma are provided with a thermostatic control system and form a structure for clamping the nano-plasma, and both sides of the first dielectric plasma are provided with a thermostatic control system and form a clamping first The structure of the dielectric plasma.

Preferably, the thermostatic control systems each include a hood that is comprised of a transfer tube, a diverging tube, and a rectangular adapter.

Preferably, the adapters each include an annular venting gap, and each venting gap includes an upper venting loop, a middle venting loop, and a lower venting loop that are in communication with each other. Circulating heating gas.

Preferably, the thermostatic control systems further comprise a temperature control box and a blower, wherein the exhaust port of the lower venting ring, the blower, the temperature control box and the air inlet of the upper venting ring are sequentially connected to each other. .

Preferably, the temperature control box is provided with a heater, and the temperature control box comprises a casing having an insulation layer, and the temperature sensor is provided with a temperature sensor.

Preferably, the reaction tank comprises a first reaction chamber, a particle temporary storage chamber and a second reaction chamber which are sequentially connected to each other, and a plurality of baffles are disposed in the first reaction chamber and the second reaction chamber. The baffles are used to block the fluid and change the flow direction so that the fluid is uniformly mixed, and the reaction tank is further provided with a discharge valve that communicates with the particle temporary storage chamber.

Preferably, the first reaction chamber, the particle temporary storage chamber and the inner wall surface of the second reaction chamber are covered with a polyurethane coating or a polytetrafluoroethylene coating.

The positive progressive effect of the invention is that the gas-liquid-solid separator of the invention can screen the soot particles of different central particle sizes according to the coal-burning condition, and the medium plasma and the nano-plasma have higher requirements on humidity, and the coal-fired power plant The exhaust pipe is long, and the flue gas is transported in the pipeline. There is moisture absorption and condensation phenomenon, which is particularly obvious in winter, so it is especially necessary for drying and dehumidifying the flue gas. The gas-liquid solid separator of the present invention can dehumidify and prevent plasma leakage.

In order to enable the reviewing committee to better understand the features of the present invention and its efficacy, it is described in detail with reference to the drawings.

(1)‧‧‧Desulfurization and denitration system

(10) ‧ ‧ ammonia source

(11)‧‧‧ Burners

(12)‧‧‧Electrostatic precipitator

(13)‧‧‧ Heat exchanger

(14)‧‧‧Sprinkler

(15)‧‧‧Atomizing nozzle

(16)‧‧‧UV lamp

(17) ‧ ‧ Circulating pump

(18)‧‧‧ Self-adding liquid tower

(19) ‧‧ ‧ separation tower

(110)‧‧‧ chimney

(111)‧‧‧Air intake pipe

(2) ‧ ‧ boiler

(20)‧‧‧Second medium plasma

(3) ‧ ‧ gas-liquid-solid separator

(31) ‧ ‧ barrel lid

(32)‧‧‧ fastening screws

(33)‧‧‧Sintering filter

(34) ‧ ‧ inner filter barrel

(35) ‧‧‧Shell

(36) ‧‧‧External filter bucket

(37) ‧‧‧Second pressure gauge

(38)‧‧‧Drain valve

(351)‧‧‧ Air intake

(352) ‧ ‧ vents

(4) ‧‧‧First gas-solid separator

(41) ‧‧‧Filter core

(42) ‧ ‧ fixed rod

(43) ‧‧‧Filter chamber

(44)‧‧‧Folding layer

(45) ‧ ‧ ash temporary storage chamber

(46)‧‧‧Rotating partition

(47)‧‧‧gate switch

(48)‧‧‧Transport pipeline

(49)‧‧‧ Ash truck

(410) ‧‧‧First intake duct

(420)‧‧‧First exhaust duct

(430)‧‧‧Second intake duct

(440) ‧‧‧Second exhaust duct

(450)‧‧‧ partition board

(460) ‧ ‧ gradual expansion

(5) ‧‧‧ gas-liquid separator

(51)‧‧‧ housing cover

(52) ‧ ‧ inner filter barrel

(53) ‧‧‧External filter bucket

(54)‧‧‧ catheter

(55) ‧‧‧Shell

(56) ‧ ‧ sump filter

(57)‧‧‧Drain valve

(58) ‧‧‧Fixed feet

(511)‧‧‧ linkage

(520) ‧ ‧ ring holder

(531)‧‧‧Baffles

(532)‧‧‧ Drainage board

(551)‧‧‧ Air inlet

(552)‧‧‧Exhaust port

(560)‧‧‧ dish-shaped cavity

(570)‧‧‧Water tank

(6) ‧‧‧ nano plasma

(60) ‧‧‧Second thermostat control system

(61) ‧ ‧ hood

(62) ‧‧‧Blowers

(63) ‧‧‧temperature control box

(611)‧‧‧Transfer tube

(612) ‧ ‧ gradual expansion

(613)‧‧‧Transfer

(614) ‧ ‧ upper ventilation loop

(615) ‧ ‧ venting loop

(616) ‧‧‧ ventilation loop

(661)‧‧‧ Shell

(65) ‧‧‧Blowers

(66) ‧‧‧temperature control box

(662)‧‧‧Temperature Sensor

(663)‧‧‧Resistive wire heater

(7) ‧‧‧First dielectric plasma

(70) ‧ ‧ Constant Temperature Control System

(8) ‧‧‧Reaction tank

(81)‧‧‧ intake manifold

(82)‧‧‧Exhaust nozzle

(83)‧‧‧First reaction chamber

(84) ‧‧‧Second reaction chamber

(85)‧‧‧Baffle

(86)‧‧‧Circular through holes

(87)‧‧‧Dumping valve

(88) ‧ ‧ granule temporary storage chamber

(89)‧‧‧Collection box

(9) ‧‧‧Second gas-solid separator

(90) ‧ ‧ chimney

Figure 1 is a schematic view showing the structure of a conventional desulfurization and denitration system.

2 is a schematic structural view of a gas-liquid-solid separator according to a preferred embodiment of the present invention.

3 is a schematic structural view of a gas-liquid separator according to a preferred embodiment of the present invention.

4 is a schematic structural view of a filter element of the gas-liquid separator of FIG. 3.

FIG. 5 is a schematic structural view of an inner filter barrel of the gas-liquid separator of FIG. 3. FIG.

Figure 6 is a schematic view showing the structure of the liquid collecting filter and the drain valve of the gas-liquid separator of Figure 3.

Figure 7 is a schematic view showing the structure of a first gas-solid separator according to a preferred embodiment of the present invention.

Figure 8 is a schematic view showing the structure of a reaction tank according to a preferred embodiment of the present invention.

FIG. 9 is a schematic structural view of a plasma sulfur removal and denitration apparatus according to a preferred embodiment of the present invention.

FIG. 10 is a partial structural schematic view of the plasma sulfur removal and denitration apparatus of FIG. 9. FIG.

11 is a schematic structural view of a hood and a temperature control box of the plasma desulfurization and denitration apparatus of FIG.

Figure 12 is a schematic view showing the structure of the temperature control box of Figure 11;

Figure 13 is a graph showing the effect of desulfurization and denitration of the plasma desulfurization and denitration equipment of Figure 9.

The invention will be described more clearly and fully hereinafter with reference to the accompanying drawings.

The structure of the gas-liquid-solid separator of this embodiment is as follows: 2, the gas-liquid-solid separator (3) of the present embodiment includes a bucket cover (31), a plurality of fastening screws (32), and a cylindrical casing (35), one embedded. a filter element in the housing (35) and a drain valve (38), the side of the housing (35) is provided with a flanged air inlet (351) and a flanged exhaust port ( 352), a swirling air duct is formed between the casing (35) and the filter element, and an axis of the air inlet (351) and an axis of the exhaust port (352) are both offset from an axis of the casing (35). The air inlet (351), the swirling air passage and the air outlet (352) are in communication with each other in sequence, and the drain valve (38) is disposed at a bottom of the housing (35) and communicates with the swirling air passage. The filter element comprises three coaxially nested column filter barrels, which are sintered filter (33), inner filter barrel (34) and outer filter barrel (36) from the inside to the outside, the inner filter A plurality of filter holes are arranged on the barrel (34) and the outer filter barrel (36), and the filter holes can be aligned or staggered when the inner filter barrel (34) and the outer filter barrel (36) rotate relative to each other. In order to change the effective area of the filter hole, Fine screening of droplets of different center particle diameter.

The air inlet (351) may be disposed at a lower portion of the casing (35), the exhaust port (352) is disposed at an upper portion of the casing (35), and the air inlet (351) is provided with a test interior thereof a first pressure gauge of fluid pressure, the exhaust port (352) is provided with a second pressure gauge (37) for testing the internal fluid pressure thereof, and the inner filter bucket (34) is provided with a pallet, the inner filter bucket ( 34) being fixedly coupled to the sintered filter (33) by the pallet so as to keep the two relatively stationary, thereby relatively rotating the inner filter bucket (34) and the outer filter bucket (36) to cause the inner filter The filter holes on the tub (34) and the filter holes on the outer filter bucket (36) are aligned or offset from each other.

The structure of the gas-liquid separator of the present embodiment is as follows: Please understand with reference to FIG. 3, the embodiment further provides a gas-liquid separator (5) including a connecting rod (511). Housing cover (51), An inner filter barrel (52), an outer filter barrel (53), a liquid guiding tube (54), a cylindrical casing (55), a dish-shaped liquid collecting filter (56), and a drain valve (57) and three fixed legs (58), the housing (55), the liquid collection filter (56), the liquid guiding tube (54) and the drain valve (57) are in turn in communication with each other.

3 and FIG. 4, the inner filter barrel (52) and the outer filter barrel (53) are column filter barrels having a plurality of filter holes in a surface array, and the inner filter barrel (52) is nested in The outer filter barrel (53) is formed with a filter element, and the filter holes can be aligned or offset with each other when the inner filter barrel (52) and the outer filter barrel (53) are relatively rotated, so as to change the effective area of the filter hole. Furthermore, fine screening of droplets of different center particle sizes, using an adjustable pore separation water and gas structure, can reduce the relative humidity by 30%-60%, and the outer filter barrel (53) is provided with a spiral drain plate. (532), the drain plate (532) is for guiding the helical movement of the gas within the swirling air passage.

As understood with reference to Figure 3, the side of the housing (55) is provided with a flanged air inlet (551) and a flanged exhaust port (552), the air inlet (551) and The exhaust port (552) is disposed at an upper portion of the casing (55), and a swirling air passage is formed between the casing (55) and the filter element, an axis of the air inlet (551) and the exhaust port The axes of (552) are all offset from the axis of the housing (55), and the intake port (551), the swirling air passage, and the exhaust port (552) are in communication with each other in sequence.

An upper portion of the outer filter bucket (53) is provided with a baffle (531) for blocking gas flowing in from the air inlet (551) toward the drain plate (532) so as to The drain plate (532) directs the gas spiral into the bottom of the filter element.

As understood from FIG. 5, the inner filter barrel (52) is provided with a plurality of annular fixing frames (520) and a plurality of swirlers (not shown) through which the cyclones pass. The fixing brackets (520) are fixed in the inner filter barrel, and the swirling directions of the swirlers are the same as the drainage direction of the draining plate (532).

As understood with reference to Figure 6, the liquid collection filter (56) has a plurality of liquid collection filter holes in the array, and the dish-shaped cavity (560) of the liquid collection filter (56) is used to collect soot particles, the drainage valve The water storage tank (570) of (57) is capable of storing the filtered wastewater.

The structure of the first gas-solid separator of the present embodiment is as follows: Please understand with reference to FIG. 7 , the embodiment further provides a first gas-solid separator (4), the first gas-solid separator (4) includes the first An intake duct (410), a second intake duct (430), a first exhaust duct (420), a second exhaust duct (440), a filter core (41), and a filter chamber (43), a filter cartridge (41) is disposed in the filter chamber (43) for passing fluid to the first exhaust conduit (420) through the filter cartridge (41), a second intake duct (430) for passing fluid through the filter core (41) to the second exhaust duct (440), the first intake duct (410) and the second intake duct (430) Relatively arranged and capable of keeping the flow direction of the fluid opposite.

The filter core (41) is folded, and a plurality of fixing rods (42) are disposed in the filter chamber (43), and the fixing rods (42) are supported at the folded corners of the filter core (41) to The two adjacent folded layers (44) are separated, and an angle of between 5 and 15 is preferably formed between adjacent two folded layers (44).

The first intake duct (410), the second intake duct (430), the first exhaust duct (420) and the second exhaust duct (440) each pass through a diverging portion (460) and the The filter chambers (43) are in communication with each other, and the outer contour of the diverging portion (460) may be a truncated cone or a trumpet shape, the diverging portion (460) of the first intake duct (410) and the second intake duct ( The diverging portion (460) of 430) is used to evenly distribute fluid and relieve flow rate, The diverging portion (460) of the first exhaust conduit (420) and the diverging portion (460) of the second exhaust conduit (440) are used to collect the filtered fluid.

The first gas-solid separator (4) further includes a soot temporary storage chamber (45) having a rotating partition plate (46) and a gate switch (47), the soot temporary storage chamber (45) and the filter chamber (43) Between the partition plate (450), a gap between the partition plate (450) and the inner wall surface of the first gas-solid separator (4) is provided, the soot temporary storage chamber (45) and the filter The chambers (43) are in communication with each other through the nip, and the gate switch (47) is for controlling the rotation of the rotating partition plate (46) to release the soot particles in the soot temporary storage chamber (45).

The first gas-solid separator (4) further includes a soot transport truck (49) including a tank body and wheels disposed at the end of the tank body, the soot temporary storage chamber ( 45) communicating with the tank through a conveying pipe (48) to transport the soot particles to the soot conveying vehicle (49), thereby avoiding the soot flying during the process of directly filling the plastic bag with the soot, to the cleaning personnel Eye damage and contamination of the external environment, the collected soot particles can be used as a chemical raw material (for example, making black shoe polish or rubber tires).

In addition, the first gas-solid separator (4) is provided with a first temperature control device having a heat exchanger (13), and the heat exchanger (13) is a surface heat exchanger or a direct contact heat exchanger. In order to reduce the temperature of the flue gas.

The structure of the reaction tank of this embodiment is as follows: Please understand with reference to Fig. 8, this embodiment further provides a reaction tank (8) including an intake nozzle (81) which is in communication with each other in sequence, first The reaction chamber (83), the particle temporary chamber (88) and the second reaction chamber (84) and the exhaust nozzle (82), specifically in the first reaction chamber (83) and the second reaction chamber (84) a circular through hole (86) is formed in the lower partition plate, and a plurality of baffles (85) are disposed in the first reaction chamber (83) and the second reaction chamber (84), and the guides are provided The flow plate (85) is used to block fluids and change the flow direction, The fluid is uniformly mixed, and the reaction tank (8) is further provided with a discharge valve (87) communicating with the particle temporary storage chamber (88), the reaction tank (8) further comprising a collecting box (89). The collection box (89) is used to collect fertilizer particles discharged from the discharge valve (87).

The first reaction chamber (83), the particle temporary storage chamber (88) and the inner wall surface of the second reaction chamber (84) are coated with a polyurethane coating (polyurethane) or polytetra Polytetrafluoroethylene (PTFE) coating, the researchers found that after the inner wall of the reaction chamber is coated with polyurethane or polytetrafluoroethylene, the synthetic fertilizer particles will not adsorb or adhere to the inner wall surface of the reaction chamber, and will easily crystallize to form 0.2- 5mm particle size fertilizer particles, large particles of fertilizer particles will automatically fall into the particle temporary storage cavity (88) for easy collection, smaller particles of ammonium sulfate and ammonium nitrate can be separated using a second gas-solid separator (9) collect.

The structure of the plasma sulfur removal and denitration device of the present embodiment is as follows: Please understand that the plasma sulfur removal and denitration device of the present embodiment includes an ammonia supply system, a gas-liquid-solid separator as described above (3). a first gas-solid separator (4) as described above, a gas-liquid separator (5) as described above, and a reaction tank (8) as described above, the plasma sulfur removal and denitration device further comprising a nanometer a plasma (6), a first dielectric plasma (7), a second gas-solid separator (9) and a chimney (90), the gas-liquid-solid separator (3), the first gas-solid separator (4) the gas-liquid separator (5), the nano-plasma (6), the first dielectric plasma (7), the reaction tank (8), the second gas-solid separator (9), and the The chimneys (90) are in communication with each other in sequence, and the ammonia supply system and the reaction tank (8) are in communication with each other to introduce ammonia into the reaction tank (8), and FIG. 9 only schematically shows a coal-fired power plant boiler ( 2) The actual boiler (2) is relatively bulky. Figure 10 shows the pipe connection structure of the first gas-solid separator (4) and the gas-liquid-solid separator (3) and the gas-liquid separator (5).

Please understand again in conjunction with FIG. 9. Specifically, the ammonia supply system includes an ammonia gas source (10) and a second dielectric plasma (20), and the ammonia gas source (10) may be an ammonia gas cylinder or A device for synthesizing ammonia gas, the second dielectric plasma (20) is for causing an ammonia gas molecule to adsorb a charge, and supplying an adsorbed ammonia gas molecule into the reaction tank (8).

The nano plasma (6) is provided with a constant temperature control system (70) on both sides thereof and forms a structure for holding the nano plasma (6), and the first dielectric plasma (7) is provided with constant temperature control on both sides thereof. System (70) and forming a structure for holding the first dielectric plasma (7), the use of a sandwich structure in a bulky plasma system, such that the heating rate is increased and the temperature control is more precise, and the reaction temperature is maintained at 65 ° C. The ionization efficiency is improved up to 70 °C.

The above four constant temperature control systems (70) have the same structure, so only the second constant temperature control system (60) is taken as an example. Please understand with reference to FIG. 11. In actual production, the second constant temperature control system (60) includes a ventilation cover. (61), a blower (62) and a temperature control box (63).

The venting cover (61) is composed of an adapter tube (611), a diverging tube (612) and a rectangular adapter (613). The adapter (613) includes an annular ventilation gap for ventilation. The gap includes an upper venting loop (614), a middle venting loop (615), and a lower venting loop (616) that are in communication with each other, the venting gap being used to circulate the heated gas. The intake port of the lower venting ring (616), the blower (62), the temperature control box (63), and the exhaust port of the upper venting ring (614) are in turn in communication with each other.

As will be understood from FIG. 12, the temperature control box (66) includes a housing (661) having an insulating layer, and a resistor wire heater (663) is disposed in the housing (661), and the insulating layer is provided with A temperature sensor (662) for pumping gas into the inner cavity of the outer casing (661).

The working principle of the gas-liquid-solid separator and the plasma desulfurization and denitration device of the present embodiment is as follows: Please understand that, in use, the boiler (2) exhaust gas flows through the system in sequence. a gas-liquid-solid separator (3), the first gas-solid separator (4), the gas-liquid separator (5), the nano-plasma (6), the first dielectric slurry (7), the reaction tank (8) The second gas-solid separator (9) and the chimney (90) are discharged to the external environment.

In the gas-liquid-solid separator (3), the moisture and soot particles in the exhaust gas of the boiler (2) are initially filtered. Table 1 shows the gas-liquid-solid separator (3) for the capture efficiency of particles of different particle sizes.

It can be seen from the data in Table 1 that the gas-liquid-solid separator (3) has an electrostatic precipitating effect on dust particles having a particle diameter of 10 μm or more.

In the first gas-solid separator (4), the moisture and soot particles in the exhaust gas of the boiler (2) are filtered again, and the first gas-solid separator (4) (also referred to as a stainless steel mesh filter) adopts 2.5. The micron stainless steel filter is used as the filter element to achieve high separation effect. The stainless steel mesh filter is designed to be washed repeatedly every day, not afraid of heat, once every six months, saving energy and completely solving the problem of PM2.5 failure to meet the standard. Table 2 The capture efficiency of the first gas-solid separator (4) for particles of different particle sizes is given.

It can be seen from the data in the above Table 2 that the first gas-solid separator (4) has an effect of electrostatically removing dust particles having a particle diameter of 2.5 μm or more.

Industrial implementation results show that, according to the gas liquid-solid separator (3) and the first gas-solid separator (4), the treatment advantages of different particle size dust particles are achieved by cascading the gas-liquid-solid separator (3) and the The first gas-solid separator (4), the particle separation rate of particle size greater than 10um is almost 100%, the particle separation rate of particle size greater than 2.5um is more than 80%, and the double filtration treatment method can control the content of soot particles in PM2. .5 emission standards (less than 0.075 mg / cubic meter).

Therefore, the exhaust gas body after the double dust removal treatment by the gas-liquid-solid separator (3) and the first gas-solid separator (4) can completely satisfy the nano-plasma produced by Suzhou Wangde Technology Co., Ltd. in terms of dust content (6) And the first dielectric plasma (7) does not require a relative humidity (RH) higher than 65%, so there is no damage to the plasma.

In addition, the heat exchanger (13) in the first gas-solid separator (4) can also cool the boiler (2) exhaust gas (100 ° C to 200 ° C) to 45 ° C to 80 ° C to avoid gas temperature over The high-level damage to the nano-plasma (6) and the first dielectric plasma (7), as well as the efficiency of desulfurization and denitrification (the sulfur removal, denitrification thermochemical reaction is temperature-critical).

In the gas-liquid separator (5), it should be understood in conjunction with FIG. 3 that the boiler (2) containing water vapor sequentially passes through the intake port (551), the swirling air passage, and the inner filter barrel (52). After the cavity is discharged from the exhaust port (552), since the axis of the air inlet (551) deviates from the axis of the casing (55), the exhaust gas of the boiler (2) forms a vortex in the swirling air passage. The water vapor condenses into water droplets and slams into the inner wall surface of the casing (55) under the action of centrifugal force. After opening the drain valve (57), the water can be drained, and the dry boiler (2) exhaust gas passes through the filter element, and Discharged through the exhaust port (552).

The baffle (531) functions as a reflective fluid, and the gas flowing from the air inlet is blocked toward the drainage plate (532), so that the drainage plate (532) guides the gas spiral motion and collides with the filter element. bottom of. Although the intake port (551) and the exhaust port (552) are both disposed at the upper portion of the casing (55), after the synergy of the baffle (531) and the deflector (532), the boiler (2) exhaust gas It is possible to obtain a uniform distribution in the axial direction of the filter element, so that the filter function of the filter element can be effectively used.

Another benefit of using the deflector (532) to spiral the flow is that the airflow is not only subjected to radial centrifugal forces, but also to the axial guiding force, so that the water vapor quickly condenses into water droplets and slantes downwardly and evenly toward the casing ( The inner wall surface of 55) avoids the problem of only the upper portion of the inner wall surface of the casing (55), resulting in uneven impact force (too much noise).

According to the coal-fired condition of the thermal power plant, the inner filter barrel (52) and the outer filter barrel (53) can be relatively rotated to change the effective area of the filter hole, thereby finely screening the droplets of different center particle diameters, and experimentally found that When using lignite in a thermal power plant, the effective radius of the filter hole can be set at 10 micrometers to 15 micrometers, and at a swirling speed of more than 25 meters per second, more than 85% of the moisture in the exhaust gas can be removed, and the swirling speed is improved. This inner filter bucket can be used (52) The internal swirlers are to ensure that the swirlers rotate in the same direction as the drain (532).

As can be understood from Fig. 6, the liquid collecting filter holes of the array on the dish-shaped liquid collecting filter (56) can collect the liquid and collect the soot particles in the dish (560), thereby avoiding direct boiler ( 2) The effluent discharged to the external environment causes water pollution, and the water discharged by the drain valve (57) reaches the standard.

As will be understood in conjunction with FIG. 11, in the hood (61), the mixed gas is slid into the diverging tube (612) through the transfer tube (611) to achieve gas uniformity, and the venting grooves are used to circulate the heated gas. The temperature of the mixed gas can be maintained at 65 ° C to 70 ° C by sequential heating of the lower venting loop (616), the intermediate venting loop (615), and the upper venting loop (614). The blower (62) is for providing a circulating power to the heating gas to maintain the rotation of the heating gas, and the resistance wire heater (663) is for electrically heating the circulating gas to maintain the temperature of the heating gas at 70 °C. In this embodiment, a resistance wire heater (663) is provided, and in actual production, a gas heat exchanger or a water heater can also be used.

Please understand with reference to Figure 9, in the nano-plasma (6) and the first dielectric plasma (7), the main chemical reactions of the desulfurization and denitration processes are:

H ₂ O+e → H ⁺ +OH ^-

O ₂ +e → 2O ^-

O ₂ +O ^- → O ₃

O+H ₂ O → OH ^- +OH ^-

H+O ₂ → HO ₂ ^3-

After nano plasma (6) and a first plasma medium (7) of the high pressure discharge reaction, a large amount of _{^{O -, O 3, OH -}} , HO 2 3- radical.

SO ₂ +O ^- → SO ₃

SO ₃ +H ₂ O → H ₂ SO ₄

SO ₂ +OH ^- → HSO ₃ ^-

HSO ₃ ^- +OH ^- → H ₂ SO ₄

Similarly, nitric acid is also produced. As understood with reference to Figure 9, the ammonia gas source (10) and the second dielectric plasma (20) are capable of supplying the adsorbed ammonia molecules to the reaction tank (8). The ammonia gas source (10) is provided with a flow valve on the exhaust pipe, which can adjust the injection flow rate of the ammonia gas to be close to the measurement of the chemical reaction, and the following chemical reaction occurs in the reaction tank (8):

H ₂ SO ₄ +2NH ₃ → (NH ₄ ) ₂ SO ₄

HNO ₃ +NH ₃ → NH ₄ NO ₃

To test the concentration of NO _X concentration of SO _2, the boiler (2) exhaust gas flow rate, impact, plasma voltage of NO _X removal rate, SO ₂ removal rate and the energy consumption, the sulfur removal thus performed denitrification experiments: Experiment When controlling the boiler (2), the exhaust gas flow rate is 40L/H, and the total power of the nano-plasma (6) and the first dielectric plasma (7) is changed (the voltage is controlled at 36KV). The experimental results are shown in Fig. 13, and it is known through experiments. , NO _X and SO ₂ removal rate and energy consumption is not a linear relationship, in the coal chemical industry, the electric power control 50W can be removed more than 90% of the NO _X and SO _2, this time the average power consumption is only 1.25W /L, in addition, the plasma voltage can be adjusted to 100KV to 150KV for better desulfurization and denitration.

The gas-liquid-solid separator and the plasma desulfurization and denitration device of the present embodiment have the following technical effects:

First, the gas-liquid-solid separator (3) of the present invention can screen the soot particles of different center particle sizes according to the coal-burning condition. Specifically, the inner filter barrel can be relatively rotated according to the coal-fired condition of the thermal power plant (34). And the outer filter barrel (36) to change the filter hole Effective area, and then fine screening of droplets of different center particle sizes.

Second, the swirling air passage utilizes the kinetic energy of the original fluid to rotate the centrifugal water, and the swirling wind speed can be measured by the first pressure gauge and the second pressure gauge (37), since the air inlet is disposed in the casing (35) In the lower part, the exhaust port is disposed at an upper portion of the casing (35). During the swirling process, the water droplets and the flue gas are separated in the middle of the outer filter tank (36), and the water droplets are subjected to gravity and centrifugal force. Sliding downwardly downward toward the inner wall surface of the casing (35), and converges along the inner wall surface of the casing (35) to the bottom of the casing (35), the flue gas exhaust gas swirls upwardly and sequentially passes through the outer a filter barrel (36), the inner filter barrel (34) and the sintered filter (33), the filter barrel formed by the outer filter barrel (36) and the inner filter barrel (34), capable of finely screening the droplets, The sintered filter (33) is capable of adsorbing soot particles in the flue gas to achieve coarse filtration of the soot particles.

Third, the positive and negative rotation of the filtered soot particles, as understood in conjunction with Figure 7, at the first time, open the first intake duct (410) and the valve on the first exhaust duct (420), close the first a valve on the two intake ducts (430) and the second exhaust duct (440), such that the flue gas is blown toward the filter core (41) in a first direction, and the first one is closed at a second time. a gas pipe (410) and a valve on the first exhaust pipe (420) open a valve on the second intake pipe (430) and the second exhaust pipe (440), so that the flue gas flows along the first Blowing the filter core (41) in both directions, the positive and negative rotation of the soot particles is advantageous in that the soot particles are blown in the first direction and embedded in the folded corners of the filter core (41) in the second direction Under the action of the wind, it is blown out and re-filtered, and alternately filtered in the forward and reverse directions to avoid the problem that the soot particles are embedded in the folded corners to form scale.

Fourth, the filtering effect is excellent and can be automatically detected. Please continue to understand in conjunction with FIG. 7 , in view of the fact that the adjacent two folded layers (44) of the filter core (41) have an angle of 5° to 15°, the flue gas can Effectively blowing a nip between adjacent two folded layers (44), and The component has a component perpendicular to the folded layer (44) to facilitate separation of the soot particles, and the filtered soot particles fall into the soot temporary storage chamber (45), and the soot temporary storage chamber (45) is divided into two juxtaposed soots. In the area, under the condition of positive and negative rotation filtering soot particles, the amount of coal ash in the two soot temporary storage areas remains basically equal. If there is a large difference in the amount of coal ash, it can be judged that the coal ash filtration channel is faulty.

Fifth, the mixture is uniform and the synthesis reaction is sufficient. The baffles (85) can block the fluid and change the flow direction, so that the fluid is uniformly mixed, and the gas path is further extended, so that the synthesis reaction is fully performed, and the chemical fertilizer particles are synthesized. The inclined baffle plate (85) rolls off and falls into the particle temporary storage chamber (88). After using the polyurethane coating or the polytetrafluoroethylene coating, it is found that the fertilizer particles do not adsorb or stick. On the inner wall surface of the reaction chamber and the reaction tank (8).

Sixth, the heating rate is fast and the temperature control is precise. The two sides of the nano plasma (6) and the two sides of the first dielectric plasma (7) are provided with a constant temperature control system (70), and the constant temperature control system (70) Set on both sides, the nano-plasma (6) and the first dielectric plasma (7) are sandwiched in the middle to form a sandwich structure, which has a fast heating rate and precise temperature control, and is convenient to maintain the reaction temperature in the range of 65 ° C to 70 ° C. .

Seventh, the plasma desulfurization and denitration device has high energy utilization efficiency and high sulfur removal and denitration efficiency, and the nano plasma (6) voltage and the first dielectric plasma (7) can generate a high of 10KV-200KV. Piezoelectric, the high-voltage electrode inside the plasma can instantly ionize the molecules in the soot exhaust gas into ions in the free state, so the energy utilization efficiency is high and the sulfur removal and denitration efficiency is strong, and the catalyst coating inside the plasma can guide the free ions. The state of the ion chemical reaction, so there is no ozone, in addition, the energy consumption is only a few tenths to one percent of other sulfur removal and denitration equipment.

Eighth, the plasma desulfurization and denitration device adopts a modular stacking design, and has the advantages of small volume, compact structure and strong expansion capability, for example, a plurality of first dielectric plasmas (7) can The plurality of first dielectric plasma units are laterally stacked into a first dielectric plasma module, and the plurality of first dielectric plasma modules are vertically stacked into a plasma sulfur removal and denitration device. Therefore, it has the advantages of small volume, compact structure and strong expansion capability.

Ninth, multi-layer insulation and prevention of leakage, the outer surface of each first dielectric plasma (7) is insulated by a polyvinyl chloride material, after the first dielectric plasma (7) is laterally stacked into a first dielectric plasma unit, The outer surface of each first dielectric plasma unit is insulated by a polyvinyl chloride material, and the outer surface of each first dielectric plasma module is assembled after the first dielectric plasma unit is laterally stacked into the first dielectric plasma module. Insulation is made of polyvinyl chloride material, so multi-layer insulation can prevent leakage of plasma and achieve power saving and safety.

While the invention has been described with respect to the specific embodiments of the present invention, it should be understood that the scope of the invention is defined by the scope of the appended claims. A person skilled in the art can make various changes or modifications to the embodiments without departing from the spirit and scope of the invention, and such changes and modifications fall within the scope of the invention.

(10) ‧ ‧ ammonia source

(2) ‧ ‧ boiler

(20)‧‧‧Second medium plasma

(3) ‧ ‧ gas-liquid-solid separator

(4) ‧‧‧First gas-solid separator

(5) ‧‧‧ gas-liquid separator

(8) ‧‧‧Reaction tank

(6) ‧‧‧ nano plasma

(60) ‧‧‧Second thermostat control system

(7) ‧‧‧First dielectric plasma

(70) ‧ ‧ Constant Temperature Control System

(9) ‧‧‧Second gas-solid separator

(90) ‧ ‧ chimney

Claims (22)

A gas-liquid-solid separator, characterized in that the gas-liquid-solid separator comprises a cylindrical casing, a filter element embedded in the casing and a drain valve, and a side of the casing is provided with a a flange inlet and a flanged exhaust port, and a swirling air passage is formed between the housing and the filter element, the axis of the inlet and the axis of the exhaust port are offset from the axis of the housing The air inlet, the swirling air passage and the exhaust port are in communication with each other in sequence. The drain valve is disposed on a bottom surface of the housing and communicates with the swirling air passage. The filter element comprises three coaxially nested columns. a filter barrel, which is a sintered filter, an inner filter barrel and an outer filter barrel from the inside to the outside, and the inner filter barrel and the outer filter barrel are arranged with a plurality of filter holes, and the filter holes can The inner filter barrel and the outer filter barrel are aligned or staggered when rotated relative to each other. The gas-liquid-solid separator according to claim 1, wherein the air inlet is disposed at a lower portion of the casing, and the air outlet is disposed at an upper portion of the casing, and the air inlet is provided with a first pressure gauge for testing fluid pressure in the air inlet, wherein the exhaust port is provided with a second pressure gauge for testing fluid pressure in the air outlet, and the inner filter bucket is provided with a pallet, and the inner filter bucket passes the The pallet is fixedly coupled to the sintered filter. A gas-liquid separator, characterized in that the gas-liquid separator comprises a cylindrical casing, a filter element embedded in the casing and a drain valve, and a flange is arranged on a side of the casing An air inlet and a flanged exhaust port, a swirling air duct is formed between the housing and the filter element, and an axis of the air inlet and an axis of the air outlet are both offset from an axis of the housing. The air inlet, the swirling air channel and the exhaust port are in communication with each other. The drain valve is disposed on a bottom surface of the housing and communicates with the swirling air channel. The filter element comprises two coaxially nested column filter barrels. The plurality of filter holes are arrayed on the columnar filter barrels, and the filter holes can be aligned or offset with each other when rotated relative to each other. The gas-liquid separator according to claim 3, characterized in that the two coaxial inserts The cylindrical filter barrels of the sleeve are respectively an outer filter barrel and an inner filter barrel, and the inner filter barrel is nested in the outer filter barrel, and the outer filter barrel is provided with a spiral drainage plate, and the drainage plate is used for Guide the spiral motion of the gas in the swirling duct. The gas-liquid separator according to claim 4, wherein the air inlet and the air outlet are both disposed at an upper portion of the casing, and an upper portion of the outer filter bucket is provided with a baffle. A baffle is used to block gas flowing in from the intake port toward the drain plate such that the drain plate directs the gas spiral to strike the bottom of the filter element. The gas-liquid separator according to any one of claims 4 to 5, wherein the inner filter barrel is provided with a plurality of annular fixing frames and a plurality of cyclones, and the cyclones pass The annular fixing brackets are fixed in the inner filter barrel, and the swirling directions of the swirlers are the same as the drainage direction of the drainage board. The gas-liquid separator according to any one of claims 4 to 5, wherein the gas-liquid separator further comprises a dish-shaped liquid collection filter and a liquid guiding tube, the housing, The liquid collecting filter, the liquid guiding tube and the drain valve are in communication with each other in sequence, and the liquid collecting filter has a plurality of liquid collecting filtering holes arranged on the array, and the dish-shaped cavity of the liquid collecting filter is used for collecting soot particles. A plasma desulfurization and denitration device, characterized in that the plasma desulfurization and denitration device comprises an ammonia supply system, a gas-liquid solid separator according to any one of claims 1-2, and a patent application The gas-liquid separator according to any one of the items 3-7, wherein the plasma sulfur removal and denitration device further comprises a first gas-solid separator, a gas-liquid separator, a first dielectric plasma, and a a reaction tank and a second gas-solid separator, the gas-liquid-solid separator, the first gas-solid separator, the gas-liquid separator, the first medium plasma, the reaction tank, and the second gas-solid separator The ammonia supply system and the reaction tank are in communication with each other in sequence. The plasma desulfurization and denitration device according to Item 8 of the patent application, characterized in that the plasma The sulfur removal and denitration apparatus further includes a nano-plasma, and the gas-liquid separator, the nano-plasma, and the first dielectric plasma are sequentially connected to each other. The plasma desulfurization and denitration apparatus according to claim 8, wherein the first gas-solid separator comprises a first intake duct, a second intake duct, a first exhaust duct, and a second An exhaust duct, a filter cartridge and a filter chamber, the filter cartridge being disposed in the filter chamber, the first intake duct for passing fluid to the first exhaust duct through the filter core, the first A second intake duct is configured to pass fluid to the second exhaust duct through the filter core, the first intake duct and the second intake duct being disposed opposite to each other and capable of maintaining a direction of fluid relative to each other. The plasma desulfurization and denitration device according to claim 10, wherein the filter core is folded, and the filter chamber is provided with a plurality of fixing rods, and the fixing rods are supported by the filter core. The folded corners of the child are separated to separate the adjacent two folded layers. The plasma desulfurization and denitration apparatus according to claim 11, wherein the first intake duct, the second intake duct, the first exhaust duct, and the second exhaust duct are both The diverging portion of the first intake duct and the diverging portion of the second intake duct are used to evenly distribute the fluid and relieve the flow rate, and the first exhaust duct is gradually The flared portion and the diverging portion of the second exhaust conduit are used to collect the filtered fluid, the adjacent two folded layers of the filter cartridge having an included angle of 5° to 15°. The plasma desulfurization and denitration device according to claim 10, wherein the first gas-solid separator further comprises a soot temporary storage chamber having a rotating partition plate and a gate switch, and the soot is temporarily stored. A partitioning plate is disposed between the cavity and the filtering chamber, and a gap is disposed between the partitioning plate and the inner wall surface of the first gas-solid separator, and the soot temporary storage cavity and the filtering cavity communicate with each other through the nip. A gate switch is used to control the rotation of the rotating partition to release soot particles in the soot temporary storage chamber. The plasma desulfurization and denitration device according to claim 13 of the patent application, characterized in that A gas-solid separator further includes a soot transport cart including a tank and wheels disposed at an end of the tank, the soot temporary chamber being in communication with the tank through a feed conduit. The plasma desulfurization and denitration device according to claim 8, wherein the first gas-solid separator is provided with a first temperature control device having a heat exchanger, and the heat exchanger is a surface type Heat exchanger or direct contact heat exchanger. The plasma desulfurization and denitration device according to claim 9, wherein the nano plasma is provided with a constant temperature control system on both sides thereof and forms a structure for holding the nano plasma, the first medium Both sides of the plasma are provided with a thermostatic control system and form a structure for holding the first dielectric plasma. The plasma desulfurization and denitration device according to claim 9, wherein the thermostatic control systems each include a ventilating cover, each of which comprises a transfer tube, a diverging tube and a Rectangular adapters. The plasma desulfurization and denitration device according to claim 17, wherein the adapters each comprise an annular ventilation gap, and each of the ventilation gaps comprises an upper ventilation loop that is in communication with each other in turn. A medium venting loop and a lower venting loop for circulating the heated gas. The plasma desulfurization and denitration device according to claim 18, wherein the thermostatic control systems further comprise a temperature control box and a blower, the exhaust port of the lower ventilation loop, the blower The temperature control box and the air inlet of the upper air circulation loop are in communication with each other in sequence. The plasma desulfurization and denitration device according to claim 19, wherein the temperature control box is provided with a heater, and the temperature control box comprises an outer casing having an insulation layer. A temperature sensor is provided. The plasma desulfurization and denitration apparatus according to claim 8, wherein the reaction tank comprises a first reaction chamber, a particle temporary storage chamber and a second reaction chamber which are sequentially connected to each other, and the first reaction A plurality of baffles are disposed in the cavity and the second reaction chamber, the baffles are configured to block the fluid and change the flow direction, so that the fluid is uniformly mixed, and the reaction tank is further provided with the particulate temporary cavity. Discharge valve. The plasma desulfurization and denitration device according to claim 21, wherein the first reaction chamber, the particle temporary storage chamber and the inner wall surface of the second reaction chamber are covered with polyurethane. Coating or Teflon coating.