PLASMA IGNITER WITH ASSEMBLED CATHODE

申请号 EP02703472.7 申请日 2002-02-27 公开(公告)号 EP1371905B1 公开(公告)日 2010-12-01
申请人 Yantai Longyuan Power Technology Co. Ltd.; 发明人 WANG, Aisheng; TANG, Hong; JI, Shuxin; WANG, Yupeng; TIAN, Dong; WANG, Gonglin; REN, Weiwu; CHEN, Xueyuan; SHAO, Ruihu; ZHANG, Xiaoyong; MA, Shuang;
摘要 This invention relates to a plasma igniter for directly igniting the coal-powder furnace. Said plasma igniter consists of a plasma generator which includes a composite anode, an assembled cathode, an electromagnetic coil and a transmitting coil; a coal powder burner which comprises mutt-stage pipes for conveying igniting coal, an equipment for adjusting thickness of coal powder and a four-stage burner canister; and a generator brace. Said assembled cathode consists of a cathode plate, a fixation nut, a conductive pipe, a inflooding pipe, a inflooding guiding pipe, a cathode lid and a sealing spacer. The lining for generatoring electric arc is assembled with the front of cathode. An alloy plate is used as the cathode plate. The nozzle that used for cooling the cathode is first convergent and then expansive, and is placed in the middle of the conductive pipe. The plasma igniter has the advantage of stableburning. It can be used as not only a main burner for the boiler but also a igniting burner. Since oil is not used, lots of petroleum source is saved.
权利要求 A plasma ignition device, comprising a pulverized coal burner (101), a plasma generator (102) for directly igniting the pulverized coal and a plasma generator bracket (103),
said plasma generator (102) comprising a dc power supply (508), a combined type cathode (602), a composite anode (604), an electromagnetic coil (603), an arc transporting coil (605) and a linear motor (601);
said plasma generator bracket (103) mounting the plasma generator (102) to said pulverized coal burner (101);
said combined type cathode (602) and said composite anode (604) being arranged on a same axis, said electromagnetic coil (603) and said arc transporting coil (605) surrounding a housing of the composite anode (604), said linear motor (601) serving to move said cathode (602) with respect to said anode (604);
said pulverized coal burner (101) comprising powder-air tubes (207), a primary air-powder tube (217), a first stage burning chamber (212) having an inlet tube (215), a second stage burning chamber (206) having an inlet tube (216), a third stage burning chamber (204), a fourth stage burning chamber (202), a burner nozzle (201) and a powder-concentration-adjusting guide plate (218),
wherein a mixture of the air and the pulverized coal enters said pulverized coal burner through said primary air-powder tube (217), is divided by the powder-concentration-adjusting guide plate (218) into three streams, which enter the first stage burning chamber (212) through the inlet tube (215) thereof, the second stage burning chamber (206) through the inlet tube (216) thereof and the third stage burning chamber (204) respectively, the resulting mixture then flowing to said fourth stage burning chamber (202) before exiting the pulverized coal burner through the burner nozzle (201) and
wherein the composite anode (604) is inserted into the first stage burning chamber (212) such that the stream entering the first stage burning chamber (212) through the inlet tube (215) thereof is ignited by the plasma, the resulting flame igniting the air-coal mixtures in the second stage burning chamber (206) and in the third stage burning chamber (204).
The plasma ignition device according to claim 1, characterized in that said combined type cathode (602) comprising a cathode head (301), an arc-starting bush (311) mounted on the cathode head (301), a cathode plate (302) surrounded by the are-starting bush (311), a cooling nozzle (303) for cooling the cathode plate (302) with water, an electrically conductive tube (304) connected at one end to the arc-starting bush (311), a water supply inlet tube (308) for supplying said water located at an opposite end of the electrically conductive tube (304), a water inlet pipe (305) in said electrically conductive tube (304) for supplying said water from said water supply inlet tube (308) to said cooling nozzle (303), a water outlet tube (307) for discharging said water mounted to the electrically conductive tube (304), and a cathode end cap (306) at said opposite end of the electrically conductive tube (304).The plasma ignition device according to claims 1 or 2, characterized in that said cathode plate (302) is in shape of a cylinder plus a cone, and is attached to the cathode head (301) through welding, and is made of Ag-based material, which is highly electrically conductive and highly thermally conductive, and the oxide of which is also conductive; the cooling nozzle (303) is constructed so that it is convergent first and then divergent.The plasma ignition device according to claim 1, characterized in that said composite anode (604) of said plasma generator (102) comprises sealing ring (401), cathode housing (402), cooling water (403), anode nozzle (404), anode body (405), anode base (406), water supply tube (407) and water outlet tube (408), said composite anode (604) is formed by welding a two nozzle tube structures, one end of said composite anode is welded to the anode nozzle (404), and the other end is welded to the anode base.The plasma ignition device according to claims 1 or 4, characterized in that said anode body (405) is made of Ag-based alloy, and the anode nozzle (404) is made of copper or Ag-based alloy.The plasma ignition device according to claims 1, 4 or 5, characterized in that said composite anode (604) is surrounded by an arc transporting coil (605).The plasma ignition device according to claim 1, characterized in that said pulverized coal burner (101) comprises burner nozzle (201), first stage burning chamber (212), second stage burning chamber (206), third stage burning chamber (204), fourth stage burning chamber (202), powder-air tubes (207), primary air-powder tube (217), auxiliary air inlet tube (209), primary powder-air guide plate (210), powder-concentration-adjusting guide plate (218), these components are assembled together through welded link board or through bolting, wherein, the pulverized coal flow coming through the primary air-powder tube (217) is divided into three streams, which respectively pass through guide plate (214) of the first stage burning chamber, guide plate (219) for the second stage burning chamber and primary powder-air guide plate (210), respectively into specified first stage burning chamber (212), second stage burning chamber (206) and third stage burning chamber (204); the auxiliary air coming from the auxiliary air inlet tube (209) is divided into three streams, which respectively cools the external cylinder (208) of the first stage burning chamber, third stage burning chamber (204) and the external wall of the fourth burning chamber (202), a portion of the auxiliary air enters into the inner wall of the fourth stage burning chamber (202) and the outer wall of the first stage burning chamber (212) so as to supplement oxygen for facilitating the combustion, the high concentration pulverized coal in the first stage burning chamber (212) is changed by the guide plate (214) of the first stage burning chamber from radial flow into axial flow, and the powder-concentration-adjusting guide plate (218) adjusts the concentration of the pulverized coal to a concentration facilitating the ignition.
说明书全文

Technical Field

The present invention relates to a a plasma ignition device for directly igniting a pulverized coal burner. The plasma ignition device can use a cathode. The plasma ignition device is used for directly starting a pulverized coal boiler. The plasma ignition device is used in the starting ignition stage and the low-load stable combustion stage of the pulverized coal boiler, and may serve as the primary burner of the pulverized coal boiler as well.

Background Art

The starting ignition and low-load stable combustion of the conventional industrial pulverized coal boiler rely on burning oil. In the year of 1999, me pulverized coal boilers of the state power system of China consumed about 2.87 million tons of oil, amounting to about 10 billion RMB yuan in value. Since the 1980's, the technologists of different countries focused on developing technologies adopting plasma technology in directly igniting the pulverized coal. An Australian has developed a plasma ignition device, in which the electrodes are protected with nitrogen gas and fat coal is burned. The former Soviet Union has made a large amount of fundamental research and made experiments in power plants in Baoji and Shaoguan in China respectively in 1996 and 1998, but the experiments were not successful. The Tsinghua University and Harerbin Boiler Factory in China have also made a large amount of research.

Various plasma ignition devices for directly igniting pulverized coal developed in different countries failed to achieve progress in some important technical problems such as ensuring the continuous operation of the generator and preventing the burner from coking, thus have not been adopted widely.

A patent of utility model of the applicant, no.99248829.x, has disclosed a plasma ignition device used in an axial flow type burner adopting bi-stage powder delivery. However, the burner has some shortcomings. To some extent, coking and ablation will occur. In addition, the coal type that can be burned in the burner is unique and the burner's operation is unstable. For example, the cathode of the burner is a graphite rod, which tends to drop scraps during operation and lead to short circuit and make the voltage unstable.

For overcoming said shortcomings, the applicant filed and was granted a patent for utility mode no. 00245 774.1, entitled as "metal electrodes used in plasma ignition device". The electrode disclosed in the patent still has some shortcomings: the anode tends to be damaged during arc starting, the voltage waves greatly, the cathode is short in life and expensive. Therefore, the wide application of the plasma ignition device is influenced adversely.

The European Patent Application No. EP 0 303 522 A1 discloses a pulverized fuel burner that is suitable for use in combusting pulverized coal and which can be used as an igniter for igniting the main burners in a steam raising plant. The burner has an electrically powered torch that generates a continuous plasma, which expands into a devolatilisation zone of the burner, and primary conduits are provided for directing a primary supply of dense phase pulverized coal into the devolatilisation zone. The burner is constructed also to include a combustion zone that surrounds the devolatilisation zone, and secondary conduits are provided for directing a secondary supply of pulverized coal into the combustion zone along with a supply of combustion supporting air. In operation of the burner, the secondary supply of pulverized coal is entrained in the air and is carried into the combustion zone by way of a swirl device and, once in the combustion zone, the whole-air mixture is contacted by partially combusted volatiles and carbon particles that move radially outward from the devolatilisation zone.

The U.S. Patent US 5,156,100 discloses a method and apparatus for starting the boiler of a solid-fuel fired power plant and ensuring the burning process of the fuel. The main fuel of the boiler is ignited by entering an auxiliary fuel stream gasified and ignited with a plasma torch. Efficient mixing and safe ignition of the main fuel with the auxiliary fuel is ensured by a turbulent feed of the auxiliary fuel and a nozzle through which the auxiliary fuel is entered into the main fuel stream.

The International Patent Application No. WO 92/01194 features a method for reducing emissions of oxides of nitrogen in combustion of various kinds of fuel. It is a method for reducing of emissions of oxides of nitrogen in combustion processes burning a solid, liquid or gaseous fuel. The invention is based on an extremely staged combustion of the fuel. The fuel is first fed in an air-deficient form in order to attain reducing conditions into a flame of a plasma torch, where the fuel is gasified and force-ignited. Auxiliary air is fed in at least one stage of the partially gasified fuel flow for the purpose of further gasifying of said fuel, after which it is routed to the actual combustion chamber, for instance, a furnace, burner or similar space, where its combustion is completed. By virtue of the abrupt staging, the flame is subjected to reducing conditions, whereby oxides of nitrogen formed in the flame are reduced before they have a chance to exit with the flue gases.

The European Patent Application EP 0 303 522 A1 discloses a pulverized coal burner wherein a plasma torch is inserted in an inner cylinder to ignite a primary coal stream. The inner cylinder is inserted into an outer cylindrical casing which receives the secondary coal stream. The expanding plasma causes devolatilisation of the primary coal stream and provides a continuous source of ignition for the secondary coal stream.

Summary of the Invention

The object of the invention is to provide a plasma ignition device for directly igniting a pulverized coal burner, in which the plasma generator can operate continuously and stably, while ensuring that the pulverized coal burner is not easily subject to coking or burning loss, thus operates reliably.

Above object is realized by a plasma ignition device in accordance with the features of claim 1, for directly starting a pulverized coal boiler. Said plasma ignition device can comprise a plasma generator, pulverized coal burner and dc power supply, wherein said plasma generator comprises combined type cathode, composite anode, electromagnetic coil, arc-starting coil mounted surrounding the housing of the composite anode, and linear motor, and said pulverized coal burner can comprise burner nozzle, four stages of burning chambers, powder-air tubes, primary air-powder tube, guide plates, high-temperature plasma transporting pipe and powder-concentration-adjusting guide plate.

An additional object of the invention could be to provide a combined type cathode used in plasma ignition device.

A combined type cathode used in a plasma ignition device, can comprise cathode head, tight nuts, electrically conductive tube, water inlet tube, water inlet pipe, water outlet tube, cathode end cap and sealing cushion, said cathode head is welded to the tight nuts of copper, said electrically conductive, tube is jointed to the nuts by screwed connection, a water inlet tube is inserted into the other end of the electrically conductive tube, and is jointed thereto by welding or screwed connection, a water outlet tube is mounted by welding in the direction perpendicular to the electrically conductive tube, thereby a cooling system of the cathode is formed, characterized in that on the front end of the cathode is mounted a dedicated arc-starting bush, the cathode plate is made of alloy plate, and a cooling nozzle is adopted. Said cooling nozzle is constructed so that it is first convergent and then divergent.

Under normal operation condition, the inventive combined type cathode has the following properties:, self-contracting electric arc, stable voltage, long cycle-life, few burning loss of the anode during arc starting, considerably reduced cost. Therefore, the reliability of the plasma ignition device is improved.

According to a preferred embodiment of the invention, said composite anode is in form of double nozzle tubes. Said anode body is made of material having high thermal conductivity and high electrical conductivity and the oxide of which is also electrically conductive, preferably Ag-based alloy, and the anode nozzle may be made of Ag-based alloy or red copper. Said combined type cathode comprises cathode head, arc-starting bush, tight nuts, cathode plate, cooling nozzle, electrically conductive tube, water inlet tube, water inlet pipe, water outlet tube , electrically conductive tube and cathode end cap. Said cathode plate is in shape of a cylinder plus a cone, and is attached to the cathode head through welding, and is made of Ag-based material, the cooling nozzle is constructed so that it is convergent first and then divergent.

Since the combined type cathode adopts high-velocity nozzle with forced cooling, the heat transmission of the cathode is accelerated and the life of the cathode is lengthened. The life of the cathode is further improved through adopting good electrically conductive and good thermally conductive material, preferably Ag-based material as cathode plate.

Through adopting the composite anode, the flow field of the plasma in the inner cavity of the anode is changed In particular, at the nozzle, the axial component of the flow is dominant, and thus the anode is prevented from being contaminated by the pulverized coal. In addition, since the receiving area of the anode is increased on the basis of the conventional nozzle, the electrons are received within the anode nozzle tube, and thus will not be disturbed by any external dynamic field, and thus the output power of the equipment is very stable. The are-transporting coil coated outside of the composite anode increases the length of the plasma flame, and thus improve the ability of igniting the pulverized coal.

Furthermore, adopting multi-stage axial powder delivery and gas film cooling techniques, and performing ignition through stage-by-stage amplification, which increase greatly the output power of the burner with lower power consumption, the burner has functions of ignition and stable combustion, as well as serving as primary burner. Specifically, auxiliary air is adopted to perform air film cooling of the first, second, third and fourth burning chambers, so that the wall temperature of the burning chambers is decreased below the ash fusion temperature and coking is prevented. In the third stage burning chamber, the oxygen is supplemented by the low concentration powder flow; in the fourth burning chamber, the oxygen is supplemented by the auxiliary air, so that the burning is enhanced and the rigidity of the flame is improved.

Therefore, the inventive plasma ignition device has advantages of great power, no coking, high burning efficiency, strong rigidity of flame, and various coals can be burned therein. Since the inventive equipment solves the key techniques relating to the continuous and stable operation of high power plasma ignition device, the inventive plasma ignition device may be widely applied in industrial pulverized coal boiler. The conventional method of starting and igniting industrial boiler and making it stably operating with oil will be replaced, and a large amount of petroleum will be saved.

Brief Description of the Drawings

The preferred embodiments of the present invention will be discussed in details with reference to the accompanying drawings, in which,

  • Fig.1 is a diagram illustrating the structure of a plasma ignition device for directly igniting a pulverized coal boiler according to the present invention;
  • Fig.2 is a diagram illustrating the structure of a pulverized coal burner of the plasma ignition device for directly igniting a pulverized coal boiler according to the present invention;
  • Fig.3 is a diagram illustrating the structure of a combined type cathode of the plasma ignition device for directly igniting a pulverized coal boiler according to the present invention;
  • Fig. 4 is a diagram illustrating the structure of a composite anode of the plasma ignition device for directly igniting a pulverized coal boiler according to the present invention;
  • Fig.5 is a diagram illustrating the operating principle of the plasma ignition device for directly igniting a pulverized coal boiler according to the present invention;
  • Fig.6 is a diagram illustrating the structure of a plasma generator of a plasma ignition device for directly igniting a pulverized coal boiler according to the present invention;
  • Fig.7 is a diagram illustrating the operating principle of the plasma generator shown in fig.6.

Detailed Description of the Invention

Now the preferred embodiment of the present invention will be described in details with reference to the accompanying drawings.

First all the reference signs in the figures will be described in the following table.

101

pulverized coal burner

308

water supply tube

102

plasma generator

310

sealing washer

103

bracket

311

are-starting bush

201

burner nozzle

312

conductor sheet

202

fourth stage burning chamber

401

sealing ring

203

burner external cylinder

402

cathode housing

204

third stage burning chamber

403

cooling water

205

auxiliary air inner cylinder

404

anode nozzle tube

206

second stage burning chamber

405

anode body

207

powder-air tubes

406

anode base

208

external cylinder of the first stage burning chamber

407

water supply tube

209

auxiliary air inlet tube

408

water outlet tube

210

primary air guide plate

501

pulverized coal burner

211

the flange of the first stage burning chamber

502

auxiliary air tube

212

first stage burning chamber

503

electromagnetic coil

213

high-temperature plasma transporting pipe

504

anode

214

guide plate of the first stage burning chamber

505

compressed air inlet tube

215

inlet tube of the first stage burning chamber

506

cathode

216

inlet tube of the second stage burning chamber

507

dc power supply

217

primary air-powder tube

508

primary air inlet tube

218

adjustable guide plate for adjusting the powder concentration

601

linear induction motor

219

guide plate for the second stage burning chamber

602

combined type cathode

220

powder channel for the third stage burning chamber

603

electromagnetic coil

221

link board

604

composite anode

222

auxiliary air channel

605

arc transporting coil

223

auxiliary air channel

606

anode water inlet tube

301

cathode head

607

anode water outlet tube

302

cathode plate

608

cathode air inlet tube

303

cooling nozzle

609

cathode water outlet tube

304

cathode external cylinder

610

cathode water inlet tube

305

water inlet pipe

12

are-starting coil

306

cathode end cap

14

compressed air outlet

307

water outlet tube

15

insulating cylinder

As shown in fig.3, a combined type cathode used in a plasma ignition device, comprises cathode head 301, tight nuts, electrically conductive tube 304, water inlet tube 308, water inlet pipe 305, water outlet tube 307, cathode end cap 306 and sealing cushion 310, said cathode head 301 is welded to the tight nuts of copper, said electrically conductive tube 304 is jointed to the nuts by screwed connection, a water inlet tube 308 is inserted into the other end of the electrically conductive tube 304, and is jointed thereto by welding or screwed connection, a water outlet tube 307 is mounted by welding in the direction perpendicular to the electrically conductive tube 304, thereby a cooling system of the cathode is formed, characterized in that on the front end of the cathode is mounted a dedicated arc-starting bush 311, the cathode plate 302 is made of alloy plate, and a cooling nozzle 303 for cooling the cathode plate is jointed to the water inlet tube 308 through welding and is arranged in the center of the electrically conductive tube 304, said cooling nozzle is constructed so that it is first convergent and then divergent.

According to a preferred embodiment, the are-starting bush 311 is made of graphite rod, which has high fusion temperature and high electrical conductivity, the arc-starting bush 311 is fastened on the front end of the cathode head 301 through screwed connection, and is flush with the cathode plate 302.

According to another preferred embodiment, the cathode plate 302 is made of Ag-based alloy plate, which has high thermal conductivity and high electrical conductivity, the cathode plate 302 is jointed to the cathode head 301 through brazing, and is flush with the arc-starting bush 311. Adopting plate-type cathode enables the self-contracting of the arc starting point.

During the operation of the plasma ignition device adopting above combined type cathode, as shown in fig.7, when the combined type cathode 602 has been in contact with the anode 603, the dc power supply 507 is powered on and the current load is set. When the combined type cathode 602 departs slowly from the anode 603, an electric arc is first formed between the anode 603 and the arc-starting bush 311. Due to the effects of mechanical compression, magnetic compression and thermal compression, the electric arc is quickly transferred from the arc-starting bush 311 to the central cathode plate 302. The revolving air-flow coming from the compressed air outlet 14 become plasma under the action of the energy of the electric arc. Experiments show that the burning loss of the anode during arc starting is much fewer and the life of the node is extended.

In addition, since the cooling nozzle of the cooling system of the cathode adopts a nozzle tube has a structure that is first convergent and then divergent, the liquid is accelerated in the throat portion of the nozzle, so that the efficiency of the heat exchange of the cathode is improved and the life of the cathode is lengthened.

As shown in fig. 1, the plasma ignition device for directly igniting a pulverized coal boiler of the invention comprises a plasma generator 102, a pulverized coal burner 101, and a plasma generator bracket 103.

Through flange connection, the plasma generator 102 has its composite anode 604 inserted into the first stage burning chamber 212 of the pulverized coal burner. As shown in fig. 6, said plasma generator comprises composite anode 604, combined type cathode 602, linear motor 601, electromagnetic coil 603 and arc transporting coil 605 mounted surrounding the housing of the composite anode 604. The composite anode 604 and the combined type cathode 602 are arranged in the same axis. The composite anode is connected to the positive pole of the dc power supply 508, and the combined type cathode 602 is connected to the negative pole of the dc power supply 508. The linear motor serves for making said cathode and said anode to contact each other and then pulling them apart from each other so that a plasma electric arc could be established.

As shown in fig.4, the composite anode is constructed as double nozzle tubes, that is, the composite anode is formed by welding a pair of nozzle tubes. One end of the composite anode is welded to the anode nozzle 404, and the other end is welded to the anode base 406. Said anode body 405 is made of material of high thermal conductivity and high electrical conductivity and the oxide of which is also electrically conductive, such as Ag-based material. The anode nozzle 404 may be made of cu-based or Ag-based material.

As shown in fig.3, said combined type cathode comprises cathode head 301, arc-starting bush 311, tight nuts, cathode plate 302, cooling nozzle 303, electrically conductive tube 304, water inlet tube 308, water inlet pipe 305, water outlet tube 307 and cathode end cap 306. The cathode plate 302 is in form of an inversed cone, and is made of Ag-based alloy. The cooling nozzle 303 is constructed so that it is convergent first and then divergent.

As shown in fig.2, said pulverized coal burner 101 comprises burner nozzle 201, fourth stage burning chamber 202, third stage burning chamber 204, inlet tube 216 of the second stage burning chamber, primary air-powder tube 217, auxiliary air inlet tube 209, guide plate 214 of the first stage burning chamber, guide plate 219 for the second stage burning chamber and powder channel 220 for the third stage burning chamber. The mixture of the air and the pulverized coal flow coming through the primary air-powder tube 217 is divided by the powder-concentration-adjusting guide plate 218 into three streams, which respectively enter into said three stages of burning chambers and burn therein. The auxiliary air coming through the auxiliary air inlet tube 209 is divided into three streams, which respectively cool and supplement oxygen to the outer wall of the first stage burning chamber 212, the outer wall of the third stage burning chamber 204 and the inner and outer walls of the fourth stage burning chamber 202.

The principle and the operation of the invention will be described below with reference to fig.5. When the dc power supply 508 is powered on, the linear motor 507 is started and advances, so that the cathode 506 contacts the anode 504. At the same time, the output current and the air pressure of the compressed air inlet tube 505 are set. With the cathode departing slowly from the anode, an electric arc voltage is established. Since arc voltage is a function of the distance between the two electrodes, the distance shall be determined depending on the type of the coal, so that the power of the art and the voltage may be determined. The ionized air carrying energy form a plasma flambeau and enters into the first stage burning chamber 212 of the pulverized coal burner, thereby ignite the high concentration pulverized coal passing through the inlet tube 215 of the first stage burning chamber.

At the same time, the pulverized coal introduced by the primary air-powder tube 217 is divided by the coal-concentration-adjusting guide plate into three streams, which enters into the burner body. A first portion of 20% of the high concentration pulverized coal enters into the first stage burning chamber through the inlet tube 215 of the first stage burning chamber and the guide plate of the first stage burning chamber, and is ignited by said plasma flambeau. The second stream, 60% of the high concentration pulverized coal enters into the second stage burning chamber through the inlet tube 216 of the second stage burning chamber and the guide plate of the second stage burning chamber. The third stream, 20% of the high concentration pulverized coal enters into the third stage burning chamber through the primary air-powder guide plate and the powder channel for the third stage burning chamber.

Wherein, the auxiliary air passes through the auxiliary air inlet tube of the powder-air tube and enters into the burner by two ways. The air of one way passes through the upper inlet of the external cylinder of the first stage burning chamber to cool the outer wall of the first stage burning chamber, and then supplements oxygen for burning. The air of the other way passes through the auxiliary air channel to cool the outer wall of the third stage burning chamber, and then is further divided into two streams, one of which enters into the fourth stage burning chamber to supplement oxygen for burning, the other of which passes through the auxiliary air channel to cool the fourth stage burning chamber, then enters into the burner hearth.

Thus, when the high-temperature plasma transporting tube provides a high-temperature plasma, as described above, the first portion of 20% of the high concentration pulverized coal is ignited immediately, the flame thereof further ignites the second portion of 60% of the pulverized coal, the rest 20% of the pulverized coal passes though the pulverized coal channel of the third stage burning chamber and mixes with above said flambeau and burns. The last portion of the powder-air flow also serves to cool the second stage burning chamber.

Experiments show that when the amount of pulverized coal in the burning chambers is 500kg/h, the shape of the flame is ϕ700× 3000mm. The flame ignites the pulverized coal in the second stage burning chamber 206 and the third stage burning chamber 204. When the total amount of the pulverized coal is 5000kg/h, the temperature of the flame is greater than 1200 °C, the jetting velocity at the nozzle is about 45-55m/s, and the shape of the flame is approximately ϕ1000× 7000mm. When adopting four plasma ignition devices in straight-flow burner, tangential firing may be maintained, thus starting ignition and stable combustion may be realized.

QQ群二维码
意见反馈