CN206739258U

CN206739258U - A kind of high-temp solid waste heat boiler

Info

Publication number: CN206739258U
Application number: CN201720435446.6U
Authority: CN
Inventors: 彭武星; 彭周雅柔
Original assignee: Individual
Current assignee: Individual
Priority date: 2017-03-02
Filing date: 2017-04-24
Publication date: 2017-12-12
Anticipated expiration: 2027-04-24

Abstract

The utility model discloses a kind of high-temp solid waste heat boiler, the waste heat boiler includes feed system, body of heater, heat-exchange system and discharge system；Heat-exchange system is mainly formed by connecting by heat exchanger and outside heat-storing device by pipeline, and outside heat-storing device is drum and/or boiler, and heat exchanger is arranged in the burner hearth of body of heater；Heat exchanger is at least made up of one group of heat exchanger tube and its water inlet union, water inlet pipe, water outlet union and outlet pipe；Level interval between adjacent heat exchange pipe outer wall is more than 1.5 times of material maximum particle diameter in burner hearth；Heat exchange area is divided in burner hearth, gas disturbance device is installed in heat exchange area.During work, in addition to setting heat exchange area is used in burner hearth and installs gas disturbance device, the operation thickness that also control material exchanges heat in burner hearth is not less than 2 meters；Speed is moved down no more than 20 meters per hour.The utility model has simple and reasonable, rapid cooling down high-temperature solid material while high efficiente callback high-temp solid material waste heat.

Description

A kind of high-temp solid waste heat boiler

Technical field

A kind of waste heat boiler is the utility model is related to, more particularly to one kind directly reclaims it by thermal source of high-temp solid material The high-temp solid waste heat boiler of waste heat.

Background technology

For the waste heat of caused high-temp solid material during remanufacture, conventional methods are all first to be consolidated with gas and high temperature Body material-heat-exchanging, high-temp solid material are cooled, and gas is heated to form high-temperature gas and enters back into gas waste-heat boiler；Its deficiency It is in high equipment cost, floor space is big, from power consumption is high, high-temp solid material utilization rate of waste heat is low, leaks out and can not keep away completely Exempt from.At present, the scheme of existing solid waste heat boiler proposes, such as " 201410265553.X high-temp solid heat recovery waste heat boilers And the method for recovery waste heat ", " a kind of 201220686983.5 solid heat transfer waste heat boiler ", its principle is in solid waste heat boiler High-temp solid material and heat exchanger tube in water direct heat-exchange, reclaim the waste heat of high-temp solid material；But all schemes are stopped Walk in experimental stage, and industrialization is not implemented, its basic reason has at 2 points：One is it is deposited in the high temperature in solid waste heat boiler When being moved from top to down by deadweight, the tube wall that the heat exchanger tube in solid material is burnt with being embedded in high temperature is only connect solid material Touch heat exchange and radiation heat transfer, the solid material being enclosed in around heat exchanger tube be cooled, be enclosed in gas around heat exchanger tube also by Cooling, just surrounds the cryogenic substance area that a floor is made up of low-temperature solid material and cryogenic gas so around heat exchanger tube, and The thermal conductivity factor of either gas or solid material is all extremely low, and this floor cryogenic substance area just hinders other high-temp solid materials Conducted heat to heat exchanger tube；And the gas in solid waste heat boiler is almost immobilising, is limited by device height, high-temp solid Material moves down that speed is very slow, and cryogenic substance area is not easy to be destroyed, so as to cause whole solid residual heat boiler for exchanging heat power low；Secondly It is the uniform water of solid material that all schemes do not solve same level in the solid waste heat boiler of big cross-sectional area really Flat the problem of declining discharging, the solid material for causing to have are imitated short in residing time in furnace, are not sufficiently cooled and are discharged, go out material temperature Spend height, it is impossible to the purpose of cooling down high-temperature solid material while reaching recovery high-temp solid material waste heat.

Utility model content

The purpose of this utility model is to overcome deficiency of the prior art, there is provided such a directly to reclaim height The high-temp solid waste heat boiler of warm solid material waste heat.

The purpose of this utility model is achieved by following technical proposals：

High-temp solid waste heat boiler technical scheme one：

The waste heat boiler includes feed system, body of heater, heat-exchange system and discharge system；The heat-exchange system is mainly by changing Hot device and outside heat-storing device are formed by connecting by pipeline, and outside heat-storing device is drum and/or boiler, and heat exchanger is arranged on In the burner hearth of body of heater；

The heat exchanger is at least made up of one group of heat exchanger tube and its water inlet union, water inlet pipe, water outlet union and outlet pipe；Often The water inlet of group heat exchanger tube is connected by the water inlet union of this group with the water inlet pipe of this group, and the delivery port of every group of heat exchanger tube passes through this The water outlet union of group is connected with the outlet pipe of this group；Level interval between adjacent heat exchange pipe outer wall is more than material in burner hearth most 1.5 times of big particle diameter；

At least one heat exchange area is divided into the burner hearth from top to down, a set of gas of installation is disturbed in each heat exchange area Dynamic device；The gas disturbance device includes warm-air pipe and hot blast pump, selects one of following arrangement：

Air entry and air-blowing mouth are set in heat exchange area, and air entry is connected by the air inlet of warm-air pipe and hot blast pump A, Connect, air-blowing mouth is connected by warm-air pipe with the air outlet of hot blast pump, partial hearth, warm-air pipe and hot blast where certain heat exchange area Pump forms hot air circulating system, and hot blast pump, which is extracted high-temperature gas out out of each heat exchange area and returned to again in this heat exchange area, enters promoting the circulation of qi Body circulation disturbance heat exchange；

Air entry is set in heat exchange area, and air entry is connected by warm-air pipe with the air inlet of hot blast pump, hot blast pump B, Air outlet lead to air, hot blast pump extracts the gas in each heat exchange area out row to air, and automatically from charging aperture or its He carries out gas disturbance heat exchange by place supplement air；

C, air-blowing mouth is arranged in heat exchange area, air-blowing mouth is connected by warm-air pipe with the air outlet of hot blast pump, hot blast pump Air inlet lead to air, hot blast pump is blown into each heat exchange area from the gas at normal temperature of outside suction, the gas in heat exchange area Body is discharged from discharging opening or elsewhere carries out gas disturbance heat exchange.

The air entry selects one of following arrangement or combination：

051：Air entry is arranged on the furnace wall of heat exchange area lower volume and/or on the bottom plate of body of heater；

052：Air entry is arranged on the tube wall of air intake duct, and air intake duct is arranged in the bottom of heat exchange area；The one of air intake duct Hold as air outlet；

053：Air entry is arranged in the suction plate of the induction chamber of heat exchange area bottom, and induction chamber is mainly by air-breathing The bottom plate composition of plate, the furnace wall of body of heater or side plate, air chamber bottom plate or body of heater, at least a discharge nozzle runs through induction chamber, induction chamber Upper setting air outlet；

The air-blowing mouth selects one of following arrangement or combination：

061：Air-blowing mouth is arranged on the furnace wall of heat exchange area upper furnace body and/or on the body of heater top of body of heater；

062：Air-blowing mouth is arranged in the aspiration tube on heat exchange area top, and one end of aspiration tube is air inlet；

063：Air-blowing mouth is arranged on the air-blowing plate of the air-blowing room on heat exchange area top, and air-blowing room is mainly by air-blowing At the top of the body of heater of plate, air chamber panel or body of heater, furnace wall or side plate composition, an at least discharge nozzle runs through air-blowing room, on air-blowing room Air inlet is set；

The A types gas disturbance device configuration is as follows：

In 051 type air entry and supporting 061 type air-blowing mouth, air entry and air-blowing mouth can also be in the whole of heat exchange area Arranged face-to-face on furnace wall；

In 052 type air entry and supporting 062 type air-blowing mouth, air intake duct can also be arranged in heat exchange area bottom or Top, aspiration tube are arranged in the middle part of heat exchange area；

The air entry is connected by warm-air pipe with the air inlet of hot blast pump, or air entry by air outlet through warm-air pipe It is connected with the air inlet of hot blast pump；Air-blowing mouth is connected by warm-air pipe with the air outlet of hot blast pump, or air-blowing mouth passes through air intake Mouth is connected through warm-air pipe with the air outlet of hot blast pump；

The Type B gas disturbance device configuration is as follows：

Air entry is connected by warm-air pipe with the air inlet of hot blast pump, or air entry by air outlet through warm-air pipe with heat The air inlet connection of air pump；

The c-type gas disturbance device configuration is as follows：

Air-blowing mouth is connected by warm-air pipe with the air outlet of hot blast pump, or air-blowing mouth by air inlet through warm-air pipe with heat The air outlet connection of air pump.

The air intake duct and aspiration tube are horizontally disposed and run through furnace wall；The warm-air pipe, air intake duct, aspiration tube, air-breathing Removing dust and clearing ash device can be installed, removing dust and clearing ash device is from ash-removing valve, cyclone dust collectors, pneumatic dust removal device, cloth bag on room, air-blowing room One of deduster and other dust arresters or combination；

Dust-proof blast cap or louvre type dust cover or other dust guards can be installed on air entry.

The pump housing and warm-air pipe of the hot blast pump can be arranged in heat exchange area or in the furnace wall of heat exchange area；The stove Lock wind feed arrangement can be installed on the charging aperture of body；It is rotary seal valve to lock wind feed arrangement, or is installed on burner hearth top close In closing plate, or the feed pipe insertion burner hearth of feed system；During using in feed pipe insertion burner hearth, high-temp solid material fills up and blocked up Live in expects pipe and realize self-sealed lock wind；Fin can be installed, the gap between fin is more than stove on the outer wall of the heat exchanger tube 1.5 times of the maximum particle diameter of material in thorax.

High-temp solid waste heat boiler technical scheme two：

The waste heat boiler includes feed system, body of heater, heat-exchange system and discharge system（10）；The heat-exchange system is main It is formed by connecting by heat exchanger and outside heat-storing device by pipeline, outside heat-storing device is drum and/or boiler, and heat exchanger is pacified In the burner hearth of body of heater；

When the cross section of the burner hearth is circular, ratio of height to diameter is more than 0.8, and when the cross section of burner hearth is rectangle, depth-width ratio is big In 0.8；

The discharging region no less than 3 is marked off on the bottom plate of the body of heater；

The discharge system is mainly made up of discharger and discharge controller, the quantity and the quantity in discharging region of discharger Equal, discharger is arranged on the lower section in discharging region；The electric control system of discharger electrically connects with discharge controller；It is described go out Glassware includes discharge nozzle and zone flow controller, and discharge nozzle connects through bottom plate with burner hearth, the lower section installation region of discharge nozzle Flow controller；Match as needed one of following：

101：The electric control part of the zone flow controller electrically connects with discharge controller；Discharge controller is according to going out The discharging speed of each discharger of temperature adjusting of material；The material of same level in burner hearth can be made uniformly to decline；

102：The outlet installation electronic-weighing storehouse of the zone flow controller；Electronic-weighing storehouse senses including electronic weight Device, warehouse and automatically controlled discharge door；I.e.：The outlet of zone flow controller is positioned at the top of the entrance of warehouse, automatically controlled discharge door peace Mounted in the lower section of the outlet of warehouse, electronic weight inductor is arranged on warehouse；Zone flow controller, electronic weight inductor Electrically connected with the electric control part of automatically controlled discharge door with discharge controller；Discharge controller respectively discharges according to the temperature adjusting of discharging The discharging speed of device；Each discharger can be made to discharge weight identical material within the work period of identical duration, made in burner hearth The material of same level uniformly declines；

103：Constant volume feed bin of the outlet installation with automatically controlled discharge door of the zone flow controller；I.e.：Zone flow The outlet of controller is positioned at the top of the entrance of constant volume feed bin；Each zone flow controller, the electric control part of automatically controlled discharge door are equal Electrically connected with discharge controller；Discharge controller is according to the discharging speed of each discharger of temperature adjusting of discharging；It can make respectively to go out Glassware discharge volume identical material within the work period of identical duration, under making the material of same level in burner hearth uniform Drop；

The high-temp solid material is entered in burner hearth from charging aperture by feed system and is stacked into not less than 2 meters work thickness Degree, heat exchanger tube is buried in high-temp solid material；Discharge system and the above-mentioned operation thickness of feed system linkage maintenance, high temperature are solid Body material is moved from top to down in burner hearth by conducting oneself with dignity with the speed less than 20 meters per hour, is changed with the water in heat exchanger tube Heat.

The area equation in each discharging region, discharge nozzle are arranged on the center in discharging region.

Bottom plate around the discharge nozzle raises up the funnel type chute to be formed and be connected with discharge nozzle, or each discharging The border installation riser in region forms the compartment being connected with discharge nozzle；Part on the discharge nozzle below the bottom plate and Being capable of installation and repairing valve between zone flow controller；The zone flow controller is automatically controlled flashboard, vibration discharger, bilayer Push-pull valve takes out terraced valve, and more than 3mm distances are kept with discharging opening when automatically controlled flashboard is installed；Installation constant volume material in the constant volume feed bin Level-sensing device each constant volume bin-level instrument in storehouse electrically connects with discharge controller；Fin, fin are installed on the outer wall of the heat exchanger tube Between gap be more than 1.5 times of maximum particle diameter of high-temp solid material in burner hearth.

High-temp solid waste heat boiler technical scheme three：

C, air-blowing mouth is arranged in heat exchange area, air-blowing mouth is connected by warm-air pipe with the air outlet of hot blast pump, hot blast pump Air inlet lead to air, hot blast pump is blown into each heat exchange area from the gas at normal temperature of outside suction, the gas in heat exchange area Body is discharged from discharging opening or elsewhere carries out gas disturbance heat exchange；

The air entry selects one of following arrangement or combination：

The air-blowing mouth selects one of following arrangement or combination：

063：Air-blowing mouth is arranged on the air-blowing plate of the air-blowing room on heat exchange area top, and air-blowing room is mainly by air-blowing Body of heater top, the furnace wall of body of heater or the side plate composition of plate, air chamber panel or body of heater, at least a discharge nozzle runs through air-blowing room, drum Air inlet is set on air chamber；

The A types gas disturbance device configuration is as follows：

When 052 type air entry is supporting in 062 type air-blowing mouth, air intake duct can also be arranged in heat exchange area bottom or Top, while aspiration tube can also be arranged in the middle part of heat exchange area；

The Type B gas disturbance device configuration is as follows：

The c-type gas disturbance device configuration is as follows：

Air-blowing mouth is connected by warm-air pipe with the air outlet of hot blast pump, or air-blowing mouth by air inlet through warm-air pipe with heat The air outlet connection of air pump；

The air intake duct and aspiration tube are horizontally disposed and run through furnace wall；The warm-air pipe, air intake duct, aspiration tube, air-breathing Removing dust and clearing ash device can be installed, removing dust and clearing ash device is from ash-removing valve, cyclone dust collectors, pneumatic dust removal device, cloth bag on room, air-blowing room One of deduster, other dust arresters or combination；Can be installed on air entry dust-proof blast cap or louvre type dust cover or other Dust guard；

The pump housing and warm-air pipe of the hot blast pump can be arranged in heat exchange area or in the furnace wall of heat exchange area；The stove Lock wind feed arrangement can be installed on the charging aperture of body；It is rotary seal valve to lock wind feed arrangement, or is installed on burner hearth top close In closing plate, or the feed pipe insertion burner hearth of feed system；During using feed pipe, high-temp solid material fill up feed pipe and block into Realize self-sealed lock wind in the outlet of expects pipe lower end；Fin can be installed, the gap between fin is big on the outer wall of the heat exchanger tube In 1.5 times of the maximum particle diameter of material in burner hearth；

The discharger being capable of configuration lock wind dust guard；

Suitable for the lock wind dust guard of the discharger of 101 type discharge systems：It is made up of sealing shell and rotary seal valve； The rotary seal valve is arranged on the lower section of zone flow controller；The exit portion of discharge nozzle, zone flow controller, rotation The entrance of sealing valve is all surrounded by sealing shell；

Suitable for the lock wind dust guard of the discharger of 102 type discharge systems：By sealing shell and automatically controlled sealing damper group Into；Automatically controlled sealing damper is installed, automatically controlled discharging is leaned in the outlet of warehouse between the outlet of zone flow controller and the entrance of warehouse Door lock wind is dust-proof；The exit portion of the discharge nozzle, zone flow controller, automatically controlled sealing damper, the entrance whole quilt of warehouse Sealing shell is surrounded；Each automatically controlled sealing damper electrically connects with discharge controller；

Suitable for the lock wind dust guard of the discharger of 103 type discharge systems：By sealing shell and automatically controlled sealing damper group Into；Automatically controlled sealing damper is installed, the outlet of constant volume feed bin is leaned between the outlet of zone flow controller and the entrance of constant volume feed bin Automatically controlled discharging door lock wind is dust-proof；The exit portion of the discharge nozzle, zone flow controller, automatically controlled sealing damper, constant volume feed bin Entrance all surrounded by sealing shell；Each automatically controlled sealing damper electrically connects with discharge controller；

Bottom plate around the discharge nozzle raises up the funnel type chute to be formed and be connected with discharge nozzle, or each discharging The border installation riser in region forms the compartment being connected with discharge nozzle；Part on the discharge nozzle below the bottom plate and Being capable of installation and repairing valve between zone flow controller；The zone flow controller is automatically controlled flashboard, vibration discharger, bilayer Push-pull valve takes out terraced valve, and more than 3mm distances are kept with discharging opening when automatically controlled flashboard is installed；Installation constant volume material in the constant volume feed bin Storehouse level-sensing device, each constant volume bin-level instrument electrically connect with discharge controller.

The utility model compared with prior art have it is simple and reasonable, by discharge control come improve heat exchange effect Rate, rapid cooling down high-temperature solid material while high efficiente callback high-temp solid material waste heat.

Brief description of the drawings

Fig. 1 is the example structure schematic diagram of the utility model one：Using A type gas disturbance devices, 051 type air entry with O61 type air-blowing mouths are supporting, the discharge system of 102 type dischargers.

Fig. 2 is Fig. 1 left view structural representations.

Fig. 3 is Fig. 1 B-B cross section structure diagrams.

Fig. 4 is Fig. 1 extended pattern structural representations.

Fig. 5 is the example structure schematic diagram of the utility model one, using A type gas disturbance devices, 052 type air entry with O62 type air-blowing mouths are supporting, the discharge system of 103 type dischargers.

Fig. 6 is the example structure schematic diagram of the utility model one, using A type gas disturbance devices, 052,053 type air entry Supporting, the discharge system of 103 type dischargers with O62 type air-blowing mouths.

Fig. 7 is the example structure schematic diagram of the utility model one, using A type gas disturbance devices, 052 type air entry with O62 type air-blowing mouths are supporting, the discharge system of 101 type dischargers.

Fig. 8 is Fig. 7 B-B cross section structure diagrams.

Fig. 9 is the example structure schematic diagram of the utility model one, using A type gas disturbance devices, 052,053 type air entry Supporting, the discharge system of 101 type dischargers with O62 type air-blowing mouths.

Figure 10 is the example structure schematic diagram of the utility model one, using A type gas disturbance devices, 053 type air entry with 061st, O62 types air-blowing mouth is supporting, the discharge system of 103 type dischargers.

Figure 11 is the example structure schematic diagram of the utility model one, and burner hearth is divided into a heat exchange area, using A type gases Disturbance device, 053 type air entry and O62 type air-blowing mouths are supporting, the discharge system of 103 type dischargers.

Figure 12 is Fig. 5 extended pattern structural representation.

Figure 13 is Fig. 3 extended pattern structural representation.

Figure 14 is the example structure schematic diagram of the utility model one, and burner hearth is divided into a heat exchange area, using Type B gas Disturbance device, 053 type air entry, the discharge system of 103 type dischargers.

Figure 15 is the example structure schematic diagram of the utility model one, and burner hearth is divided into a heat exchange area, using c-type gas Disturbance device, O61 type air-blowing mouths, the discharge system of 102 type dischargers.

Figure 16 is the example structure schematic diagram of the utility model one, and burner hearth is divided into a heat exchange area, using c-type gas Disturbance device, O63 type air-blowing mouths, the discharge system of 102 type dischargers.

Figure 17 is the example structure schematic diagram of the utility model one, the discharge system of 102 type dischargers.

Figure 18 is the example structure schematic diagram of the utility model one, the discharge system of 103 type dischargers.

Figure 19 is the example structure schematic diagram of the utility model one, the discharge system of 101 type dischargers.

Figure 20 is Figure 19 extended pattern structural representation.

Figure 21 is the A-A cross section structure diagrams of Fig. 1,5,7,12,15,16,17,18,19.

Figure 22 is the A-A cross section structure diagrams of Fig. 6,9,10,11,14.

Figure 23 is Fig. 4,20 A-A cross section structure diagrams.

In figure：1- charging apertures, 2- furnace walls, 3- burner hearths, 4- heat exchange areas, 5- air entries, 6- air-blowing mouths, 7- warm-air pipes, 8- Bottom plate, 9- discharge nozzles, 10- discharge systems, 11- lock wind feed arrangements, 12- heat exchanger tubes, 13- drums, 14- rotary seal valves, 15- Hot blast pump, the 16- pump housings, 17- air intake ducts, 18- aspiration tubes, 19- removing dust and clearing ash devices, 20- induction chambers, 21- suction plates, 22- constant volumes Feed bin, 23- dischargings region, 24- service valves, 25- zone flow controllers, 26- sealing shells, 27- electronic weight inductors, 28- warehouses, the automatically controlled discharge doors of 29-, 30- constant volume bin-level instrument, the automatically controlled sealing dampers of 31-, 32- air-blowing room, 33- air-blowing plates, The dust-proof blast caps of 34-, 35- air outlets, 36- air inlets.

Embodiment

With reference to embodiment, the utility model is described in further detail：

High-temp solid waste heat boiler technical scheme one, refer to the attached drawing 1,2,3,4,5,6,7,8,9,10,11,12,13,14, 15,16,21,22,23.

The waste heat boiler includes feed system, body of heater, heat-exchange system and discharge system 10；The heat-exchange system mainly by Heat exchanger and outside heat-storing device are formed by connecting by pipeline, and outside heat-storing device is drum 13 and/or boiler, and heat exchanger is pacified In the burner hearth 3 of body of heater；

The heat exchanger is at least made up of one group of heat exchanger tube 12 and its water inlet union, water inlet pipe, water outlet union and outlet pipe； The water inlet of every group of heat exchanger tube 12 is connected by the water inlet union of this group with the water inlet pipe of this group, the delivery port of every group of heat exchanger tube 12 It is connected by the water outlet union of this group with the outlet pipe of this group；Level interval between the adjacent outer wall of heat exchanger tube 12 is more than burner hearth 1.5 times of material maximum particle diameter in 3；

At least one heat exchange area 4 is divided into the burner hearth 3 from top to down, a set of gas is installed in each heat exchange area 4 Body disturbance device；The gas disturbance device includes warm-air pipe 7 and hot blast pump 15, selects one of following arrangement：

Air entry 5 and air-blowing mouth 6 be set in heat exchange area 4, and air entry 5 is entered by warm-air pipe 7 and hot blast pump 15 A, Air port is connected, and air-blowing mouth 6 is connected by warm-air pipe 7 with the air outlet of hot blast pump 15, the partial hearth 3 at certain place of heat exchange area 4, Warm-air pipe 7 forms hot air circulating system with hot blast pump 15, and hot blast pump 15 is extracted high-temperature gas out out of each heat exchange area 4 and returned to again Gas circulation disturbance heat exchange is carried out in this heat exchange area 4；

Air entry 5 is set in heat exchange area 4 B, air entry 5 is connected by warm-air pipe 7 with the air inlet of hot blast pump 15, The air outlet of hot blast pump 15 leads to air, and hot blast pump 15 extracts the gas in each heat exchange area 4 out row to air, and automatically from entering Material mouth 1 supplements air progress gas disturbance heat exchange elsewhere；

C, air-blowing mouth 6 is arranged in heat exchange area 4, air-blowing mouth 6 is connected by warm-air pipe 7 with the air outlet of hot blast pump 15, The air inlet of hot blast pump 15 leads to air, and hot blast pump 15 is blown into each heat exchange area 4 from the gas at normal temperature of outside suction, is exchanged heat Gas in region 4 is discharged from discharging opening or elsewhere carries out gas disturbance heat exchange.

The air entry 5 selects one of following arrangement or combination：

051：Air entry 5 is arranged on the furnace wall 2 of the lower volume of heat exchange area 4 and/or on the bottom plate 8 of body of heater；

052：Air entry 5 is arranged on the tube wall of air intake duct 17, and air intake duct 17 is arranged in the bottom of heat exchange area 4；Air-breathing One end of pipe 17 is air outlet 35；

053：Air entry 5 is arranged in the suction plate 21 of the induction chamber 20 of the bottom of heat exchange area 4, and induction chamber 20 is main It is made up of the bottom plate 8 of suction plate 21, the furnace wall 2 of body of heater or side plate, air chamber bottom plate or body of heater, at least a discharge nozzle 9 is through suction Air chamber 20, air outlet 35 is set on induction chamber 20；

The air-blowing mouth 6 selects one of following arrangement or combination：

061：Air-blowing mouth 6 is arranged on the furnace wall 2 of the upper furnace body of heat exchange area 4 and/or on the body of heater top of body of heater；

062：Air-blowing mouth 6 is arranged in the aspiration tube 18 on the top of heat exchange area 4, and one end of aspiration tube 18 is air inlet 36；

063：Air-blowing mouth 6 is arranged on the air-blowing plate 33 of the air-blowing room 32 on the top of heat exchange area 4, and air-blowing room 32 is main It is made up of body of heater top, furnace wall 2 or the side plate of air-blowing plate 33, air chamber panel or body of heater, at least a discharge nozzle 9 runs through air-blowing room 32, air inlet 36 is set on air-blowing room 32；

The A types gas disturbance device configuration is as follows：

In 051 type air entry 5 and supporting 061 type air-blowing mouth 6, air entry 5 and air-blowing mouth 6 can also be in heat exchange areas 4 Whole furnace wall 2 on arrange face-to-face；

In 052 type air entry 5 and supporting 062 type air-blowing mouth 6, air intake duct 17 can also be arranged under heat exchange area 4 Portion or top, aspiration tube 18 are arranged in the middle part of heat exchange area 4；

The air entry 5 is connected by warm-air pipe 7 with the air inlet of hot blast pump 15, or air entry 5 passes through air outlet 35 It is connected through warm-air pipe 7 with the air inlet of hot blast pump 15；Air-blowing mouth 6 is connected by warm-air pipe 7 with the air outlet of hot blast pump 15, or Air-blowing mouth 6 is connected by air inlet 36 through warm-air pipe 7 with the air outlet of hot blast pump 15；

The Type B gas disturbance device configuration is as follows：

Air entry 5 is connected by warm-air pipe 7 with the air inlet of hot blast pump 15, or air entry 5 by air outlet 35 through heat Airduct 7 is connected with the air inlet of hot blast pump 15；

The c-type gas disturbance device configuration is as follows：

Air-blowing mouth 6 is connected by warm-air pipe 7 with the air outlet of hot blast pump 15, or air-blowing mouth 6 by air inlet 36 through heat Airduct 7 is connected with the air outlet of hot blast pump 15.

The air intake duct 17 and aspiration tube 18 are horizontally disposed and run through furnace wall 2；The warm-air pipe 7, air intake duct 17, air-blowing Pipe 18, induction chamber 20, removing dust and clearing ash device 19 can be installed on air-blowing room 32, removing dust and clearing ash device 19 is from ash-removing valve, cyclone dust removal One of device, pneumatic dust removal device, sack cleaner and other dust arresters or combination；

Dust-proof blast cap 34 or louvre type dust cover or other dust guards can be installed on air entry 5.

The pump housing 16 and warm-air pipe 7 of the hot blast pump 15 can be arranged on the furnace wall 2 of in heat exchange area 4 or heat exchange area 4 In；Lock wind feed arrangement 11 can be installed on the charging aperture 1 of the body of heater；It is rotary seal valve to lock wind feed arrangement 11, or Installed on the top of burner hearth 3 in coffer, or the feed pipe insertion burner hearth 3 of feed system；It is high during using in feed pipe insertion burner hearth 3 Warm solid material, which fills up and blocks feed pipe, realizes self-sealed lock wind；Fin can be installed on the outer wall of the heat exchanger tube 12, Gap between fin is more than 1.5 times of the maximum particle diameter of material in burner hearth 3.

High-temp solid waste heat boiler technical scheme two, refer to the attached drawing 17,18,19,20,21,23.

When the cross section of the burner hearth 3 is circular, ratio of height to diameter is more than 0.8, when the cross section of burner hearth 3 is rectangle, depth-width ratio More than 0.8；

The discharging region 23 no less than 3 is marked off on the bottom plate 8 of the body of heater；

The discharge system 10 is mainly made up of discharger and discharge controller, quantity and the discharging region 23 of discharger Quantity is equal, and discharger is arranged on the lower section in discharging region 23；The electric control system of discharger electrically connects with discharge controller； The discharger includes discharge nozzle 9 and zone flow controller 25, and discharge nozzle 9 connects through bottom plate 8 with burner hearth 3, discharge nozzle 9 Lower section installation region flow controller 25；Match as needed one of following：

101：The electric control part of the zone flow controller 25 electrically connects with discharge controller；Discharge controller according to The discharging speed of each discharger of temperature adjusting of discharging；The material of same level in burner hearth 3 can be made uniformly to decline；

102：The outlet installation electronic-weighing storehouse of the zone flow controller 25；Electronic-weighing storehouse includes electronic weight sense Answer device 27, warehouse 28 and automatically controlled discharge door 29；I.e.：The outlet of zone flow controller 25 is located at the top of the entrance of warehouse 28, Automatically controlled discharge door 29 is arranged on the lower section of the outlet of warehouse 28, and electronic weight inductor 27 is arranged on warehouse 28；Zone flow The electric control part of controller 25, electronic weight inductor 27 and automatically controlled discharge door 29 electrically connects with discharge controller；Discharging control Device processed is according to the discharging speed of each discharger of temperature adjusting of discharging；Each discharger can be made within the work period of identical duration Weight identical material is discharged, the material of same level in burner hearth 3 is uniformly declined；

103：Constant volume feed bin 22 of the outlet installation with automatically controlled discharge door 29 of the zone flow controller 25；I.e.：Area The outlet of domain flow controller 25 is positioned at the top of the entrance of constant volume feed bin 22；Each zone flow controller 25, automatically controlled discharge door 29 electric control part electrically connects with discharge controller；Discharge controller is fast according to the discharging of each discharger of temperature adjusting of discharging Degree；Each discharger discharge volume identical material within the work period of identical duration can be made, make same level in burner hearth 3 Material uniformly decline；

The high-temp solid material is entered in burner hearth 3 from charging aperture 1 by feed system and is stacked into not less than 2 meters work Thickness, heat exchanger tube 12 is buried in high-temp solid material；Discharge system 10 maintains above-mentioned operation thickness with feed system linkage, High-temp solid material is moved in the burner hearth 3 from top to down by deadweight with the speed less than 20 meters per hour, and in heat exchanger tube 12 Water is exchanged heat.

The area equation in each discharging region 23, discharge nozzle 9 are arranged on the center in discharging region 23.

Bottom plate 8 around the discharge nozzle 9 raises up the funnel type chute to be formed and be connected with discharge nozzle 9, or respectively The border installation riser in discharging region 23 forms the compartment being connected with discharge nozzle 9；It is located on the discharge nozzle 9 under bottom plate 8 Being capable of installation and repairing valve 24 between the part of side and zone flow controller 25；The zone flow controller 25 is electric-controlled gate Plate, vibration discharger, double-deck push-pull valve take out terraced valve, and more than 3mm distances are kept with discharging opening when automatically controlled flashboard is installed；It is described fixed Hold installation constant volume bin-level instrument 30 in feed bin 22, each constant volume bin-level instrument 30 electrically connects with discharge controller；It is described to change Fin is installed, the gap between fin is more than 1.5 of the maximum particle diameter of high-temp solid material in burner hearth 3 on the outer wall of heat pipe 12 Times.

High-temp solid waste heat boiler technical scheme three, refer to the attached drawing 1,2,3,4,5,6,7,8,9,10,11,12,13,14, 15,16,21,22,23.

The burner hearth 3 is divided at least one heat exchange area 4 from top to down, and a set of gas is installed in each heat exchange area 4 Disturbance device；The gas disturbance device includes warm-air pipe 7 and hot blast pump 15, selects one of following arrangement：

C, air-blowing mouth 6 is arranged in heat exchange area 4, air-blowing mouth 6 is connected by warm-air pipe 7 with the air outlet of hot blast pump 15, The air inlet of hot blast pump 15 leads to air, and hot blast pump 15 is blown into each heat exchange area 4 from the gas at normal temperature of outside suction, is exchanged heat Gas in region 4 is discharged from discharging opening or elsewhere carries out gas disturbance heat exchange；

The air entry 5 selects one of following arrangement or combination：

The air-blowing mouth 6 selects one of following arrangement or combination：

063：Air-blowing mouth 6 is arranged on the air-blowing plate 33 of the air-blowing room 32 on the top of heat exchange area 4, and air-blowing room 32 is main It is made up of body of heater top, the furnace wall 2 of body of heater or the side plate of air-blowing plate 33, air chamber panel or body of heater, at least a discharge nozzle 9 runs through Air-blowing room 32, air inlet 36 is set on air-blowing room 32；

The A types gas disturbance device configuration is as follows：

When 052 type air entry 5 is supporting in 062 type air-blowing mouth 6, air intake duct 17 can also be arranged under heat exchange area 4 Portion or top, while aspiration tube 18 can also be arranged in the middle part of heat exchange area 4；

The Type B gas disturbance device configuration is as follows：

The c-type gas disturbance device configuration is as follows：

Air-blowing mouth 6 is connected by warm-air pipe 7 with the air outlet of hot blast pump 15, or air-blowing mouth 6 by air inlet 36 through heat Airduct 7 is connected with the air outlet of hot blast pump 15；

The air intake duct 17 and aspiration tube 18 are horizontally disposed and run through furnace wall 2；The warm-air pipe 7, air intake duct 17, air-blowing Pipe 18, induction chamber 20, removing dust and clearing ash device 19 can be installed on air-blowing room 32, removing dust and clearing ash device 19 is from ash-removing valve, cyclone dust removal One of device, pneumatic dust removal device, sack cleaner, other dust arresters or combination；Can be installed on air entry 5 dust-proof blast cap 34 or Louvre type dust cover or other dust guards；

The pump housing 16 and warm-air pipe 7 of the hot blast pump 15 can be arranged on the furnace wall 2 of in heat exchange area 4 or heat exchange area 4 In；Lock wind feed arrangement 11 can be installed on the charging aperture 1 of the body of heater；It is rotary seal valve to lock wind feed arrangement 11, or Installed on the top of burner hearth 3 in coffer, or the feed pipe insertion burner hearth 3 of feed system；During using feed pipe, high-temp solid material plug Expire feed pipe and block the outlet of feed pipe lower end and realize self-sealed lock wind；Wing can be installed on the outer wall of the heat exchanger tube 12 Piece, the gap between fin are more than 1.5 times of the maximum particle diameter of material in burner hearth 3；

The discharger being capable of configuration lock wind dust guard；

Suitable for the lock wind dust guard of the discharger of 101 type discharge systems 10：By sealing shell 26 and rotary seal valve 14 compositions；The rotary seal valve 14 is arranged on the lower section of zone flow controller 25；The exit portion of discharge nozzle 9, region stream Amount controller 25, the entrance of rotary seal valve 14 are all surrounded by sealing shell 26；

Suitable for the lock wind dust guard of the discharger of 102 type discharge systems 10：By sealing shell 26 and automatically controlled sealing lock Plate 31 forms；Automatically controlled sealing damper 31 is installed between the outlet of zone flow controller 25 and the entrance of warehouse 28, warehouse 28 Outlet is dust-proof by automatically controlled discharge door 29 lock wind；The exit portion of the discharge nozzle 9, zone flow controller 25, automatically controlled sealing lock Plate 31, the entrance of warehouse 28 are all surrounded by sealing shell 26；Each automatically controlled sealing damper 31 electrically connects with discharge controller；

Suitable for the lock wind dust guard of the discharger of 103 type discharge systems 10：By sealing shell 26 and automatically controlled sealing lock Plate 31 forms；Automatically controlled sealing damper 31, constant volume are installed between the outlet of zone flow controller 25 and the entrance of constant volume feed bin 22 The outlet of feed bin 22 is dust-proof by automatically controlled discharge door 29 lock wind；The exit portion of the discharge nozzle 9, zone flow controller 25, electricity Control sealing damper 31, the entrance of constant volume feed bin 22 are all surrounded by sealing shell 26；Each automatically controlled sealing damper 31 with discharging Controller electrically connects；

Bottom plate 8 around the discharge nozzle 9 raises up the funnel type chute to be formed and be connected with discharge nozzle 9, or respectively The border installation riser in discharging region 23 forms the compartment being connected with discharge nozzle 9；It is located on the discharge nozzle 9 under bottom plate 8 Being capable of installation and repairing valve 24 between the part of side and zone flow controller 25；The zone flow controller 25 is electric-controlled gate Plate, vibration discharger, double-deck push-pull valve take out terraced valve, and more than 3mm distances are kept with discharging opening when automatically controlled flashboard is installed；It is described fixed Hold installation constant volume bin-level instrument 30 in feed bin 22, each constant volume bin-level instrument 30 electrically connects with discharge controller.

Claims

1. a kind of high-temp solid waste heat boiler, the waste heat boiler includes feed system, body of heater, heat-exchange system and discharge system （10）；The heat-exchange system is mainly formed by connecting by heat exchanger and outside heat-storing device by pipeline, and outside heat-storing device is vapour Bag（13）And/or boiler, heat exchanger are arranged on the burner hearth of body of heater（3）It is interior；It is characterized in that：

The heat exchanger is at least by one group of heat exchanger tube（12）And its water inlet union, water inlet pipe, water outlet union and outlet pipe composition；Often Group heat exchanger tube（12）Water inlet be connected by the water inlet union of this group with the water inlet pipe of this group, every group of heat exchanger tube（12）Water outlet Mouth is connected by the water outlet union of this group with the outlet pipe of this group；Adjacent heat exchanger tube（12）Level interval between outer wall is more than Burner hearth（3）1.5 times of interior material maximum particle diameter；

The burner hearth（3）At least one heat exchange area is inside divided into from top to down（4）, each heat exchange area（4）Interior installation is a set of Gas disturbance device；The gas disturbance device includes warm-air pipe（7）With hot blast pump（15）, select one of following arrangement：

A, in heat exchange area（4）Middle setting air entry（5）With air-blowing mouth（6）, air entry（5）Pass through warm-air pipe（7）With hot blast pump （15）Air inlet connection, air-blowing mouth（6）Pass through warm-air pipe（7）With hot blast pump（15）Air outlet connection, certain heat exchange area（4） The partial hearth at place（3）, warm-air pipe（7）With hot blast pump（15）Form hot air circulating system, hot blast pump（15）From each heat transfer zone Domain（4）Interior extraction high-temperature gas returns to this heat exchange area again（4）Middle progress gas circulation disturbance heat exchange；

B, in heat exchange area（4）Middle setting air entry（5）, air entry（5）Pass through warm-air pipe（7）With hot blast pump（15）Air inlet Connection, hot blast pump（15）Air outlet lead to air, hot blast pump（15）By each heat exchange area（4）Interior gas, which is extracted out, to be arranged to big Gas, and automatically from charging aperture（1）Or air is supplemented elsewhere and carries out gas disturbance heat exchange；

C, in heat exchange area（4）Middle arrangement air-blowing mouth（6）, air-blowing mouth（6）Pass through warm-air pipe（7）With hot blast pump（15）Air outlet Connection, hot blast pump（15）Air inlet lead to air, hot blast pump（15）Each heat transfer zone is blown into from the gas at normal temperature of outside suction Domain（4）In, heat exchange area（4）Interior gas is discharged from discharging opening or elsewhere carries out gas disturbance heat exchange.

2. waste heat boiler according to claim 1, it is characterised in that：The air entry（5）Select one of following arrangement Or combination：

051：Air entry（5）It is arranged on heat exchange area（4）The furnace wall of lower volume（2）Upper and/or body of heater bottom plate（8）On；

052：Air entry（5）It is arranged on air intake duct（17）Tube wall on, air intake duct（17）It is arranged in heat exchange area（4）Bottom； Air intake duct（17）One end be air outlet（35）；

053：Air entry（5）It is arranged in heat exchange area（4）The induction chamber of bottom（20）Suction plate（21）On, induction chamber （20）Mainly by suction plate（21）, body of heater furnace wall（2）Or the bottom plate of side plate, air chamber bottom plate or body of heater（8）Composition, at least one Discharge nozzle（9）Through induction chamber（20）, induction chamber（20）Upper setting air outlet（35）；

The air-blowing mouth（6）Select one of following arrangement or combination：

061：Air-blowing mouth（6）It is arranged on heat exchange area（4）The furnace wall of upper furnace body（2）On at the top of upper and/or body of heater body of heater；

062：Air-blowing mouth（6）It is arranged in heat exchange area（4）The aspiration tube on top（18）On, aspiration tube（18）One end be into Air port（36）；

063：Air-blowing mouth（6）It is arranged in heat exchange area（4）The air-blowing room on top（32）Air-blowing plate（33）On, air-blowing room （32）Mainly by air-blowing plate（33）, air chamber panel or body of heater body of heater at the top of, furnace wall（2）Or side plate composition, at least one discharging Pipe（9）Through air-blowing room（32）, air-blowing room（32）Upper setting air inlet（36）；

The A types gas disturbance device configuration is as follows：

In 051 type air entry（5）With 061 type air-blowing mouth（6）When supporting, air entry（5）With air-blowing mouth（6）Can also be in heat transfer zone Domain（4）Whole furnace wall（2）Upper arrangement face-to-face；

In 052 type air entry（5）With 062 type air-blowing mouth（6）When supporting, air intake duct（17）Heat exchange area can also be arranged in（4） Bottom or top, aspiration tube（18）It is arranged in heat exchange area（4）Middle part；

The air entry（5）Pass through warm-air pipe（7）With hot blast pump（15）Air inlet connection, or air entry（5）Pass through air-out Mouthful（35）Through warm-air pipe（7）With hot blast pump（15）Air inlet connection；Air-blowing mouth（6）Pass through warm-air pipe（7）With hot blast pump（15） Air outlet connection, or air-blowing mouth（6）Pass through air inlet（36）Through warm-air pipe（7）With hot blast pump（15）Air outlet connection；

The Type B gas disturbance device configuration is as follows：

Air entry（5）Pass through warm-air pipe（7）With hot blast pump（15）Air inlet connection, or air entry（5）Pass through air outlet （35）Through warm-air pipe（7）With hot blast pump（15）Air inlet connection；

The c-type gas disturbance device configuration is as follows：

Air-blowing mouth（6）Pass through warm-air pipe（7）With hot blast pump（15）Air outlet connection, or air-blowing mouth（6）Pass through air inlet （36）Through warm-air pipe（7）With hot blast pump（15）Air outlet connection.

3. waste heat boiler according to claim 2, it is characterised in that：The air intake duct（17）And aspiration tube（18）Horizontal cloth Put and run through furnace wall（2）；The warm-air pipe（7）, air intake duct（17）, aspiration tube（18）, induction chamber（20）, air-blowing room（32）Upper energy Removing dust and clearing ash device is enough installed（19）, removing dust and clearing ash device（19）From ash-removing valve, cyclone dust collectors, pneumatic dust removal device, bag-type dust One of device and other dust arresters or combination；

Air entry（5）On dust-proof blast cap can be installed（34）Or louvre type dust cover or other dust guards.

4. according to 1 or 2 or 3 waste heat boiler of claim, it is characterised in that：The hot blast pump（15）The pump housing（16）And heat Airduct（7）Heat exchange area can be arranged on（4）Interior or heat exchange area（4）Furnace wall（2）In；The charging aperture of the body of heater（1）On Lock wind feed arrangement can be installed（11）；Lock wind feed arrangement（11）For rotary seal valve, or in burner hearth（3）Installed on top closed Plate, or the feed pipe insertion burner hearth of feed system（3）It is interior；Burner hearth is inserted using feed pipe（3）When interior, high-temp solid material fills up And block feed pipe and realize self-sealed lock wind；The heat exchanger tube（12）Outer wall on fin can be installed, between fin between Gap is more than burner hearth（3）1.5 times of the maximum particle diameter of interior material.

5. a kind of high-temp solid waste heat boiler, the waste heat boiler includes feed system, body of heater, heat-exchange system and discharge system （10）；The heat-exchange system is mainly formed by connecting by heat exchanger and outside heat-storing device by pipeline, and outside heat-storing device is vapour Bag（13）And/or boiler, heat exchanger are arranged on the burner hearth of body of heater（3）It is interior；It is characterized in that：

The burner hearth（3）Cross section for it is circular when, ratio of height to diameter be more than 0.8, burner hearth（3）Cross section when being rectangle, depth-width ratio More than 0.8；

The bottom plate of the body of heater（8）On mark off discharging region no less than 3（23）；

The discharge system（10）Mainly it is made up of discharger and discharge controller, quantity and the discharging region of discharger（23）'s Quantity is equal, and discharger is arranged on discharging region（23）Lower section；The electric control system of discharger is electrically connected with discharge controller Connect；The discharger includes discharge nozzle（9）With zone flow controller（25）, discharge nozzle（9）Through bottom plate（8）With burner hearth（3） Connection, discharge nozzle（9）Lower section installation region flow controller（25）；Match as needed one of following：

101：The zone flow controller（25）Electric control part electrically connected with discharge controller；Discharge controller is according to going out The discharging speed of each discharger of temperature adjusting of material；Burner hearth can be made（3）The material of interior same level uniformly declines；

102：The zone flow controller（25）Outlet installation electronic-weighing storehouse；Electronic-weighing storehouse senses including electronic weight Device（27）, warehouse（28）With automatically controlled discharge door（29）；I.e.：Zone flow controller（25）Outlet be located at warehouse（28）Entrance Top, automatically controlled discharge door（29）Installed in warehouse（28）Outlet lower section, electronic weight inductor（27）Installed in warehouse （28）On；Zone flow controller（25）, electronic weight inductor（27）With automatically controlled discharge door（29）Electric control part with going out Expect controller electrical connection；Discharge controller is according to the discharging speed of each discharger of temperature adjusting of discharging；Each discharger can be made Weight identical material is discharged within the work period of identical duration, makes burner hearth（3）The material of interior same level uniformly declines；

103：The zone flow controller（25）Outlet installation carry automatically controlled discharge door（29）Constant volume feed bin（22）；I.e.： Zone flow controller（25）Outlet be located at constant volume feed bin（22）Entrance top；Each zone flow controller（25）, electricity Control discharge door（29）Electric control part electrically connected with discharge controller；Discharge controller respectively discharges according to the temperature adjusting of discharging The discharging speed of device；Each discharger discharge volume identical material within the work period of identical duration can be made, make burner hearth（3） The material of interior same level uniformly declines；

The high-temp solid material is by feed system from charging aperture（1）Into burner hearth（3）It is interior and be stacked into not less than 2 meters work Thickness, by heat exchanger tube（12）It is buried in high-temp solid material；Discharge system（10）Above-mentioned work is maintained with feed system linkage Thickness, high-temp solid material is in burner hearth（3）It is interior to be moved from top to down with the speed less than 20 meters per hour by conducting oneself with dignity, with heat exchanger tube （12）In water exchanged heat.

6. waste heat boiler according to claim 5, it is characterised in that：Each discharging region（23）Area equation, discharging Pipe（9）It is arranged on discharging region（23）Center.

7. according to the waste heat boiler of claim 5 or 6, it is characterised in that：The discharge nozzle（9）The bottom plate of surrounding（8）Upwards Convex to form and discharge nozzle（9）The funnel type chute being connected, or the region that respectively discharges（23）Border installation riser formed with Discharge nozzle（9）The compartment being connected；The discharge nozzle（9）It is upper to be located at bottom plate（8）The part of lower section and zone flow controller （25）Between being capable of installation and repairing valve（24）；The zone flow controller（25）Inserted for automatically controlled flashboard, vibration discharger, bilayer Plate valve takes out terraced valve, and more than 3mm distances are kept with discharging opening when automatically controlled flashboard is installed；The constant volume feed bin（22）Interior installation constant volume Bin-level instrument（30）, each constant volume bin-level instrument（30）Electrically connected with discharge controller；The heat exchanger tube（12）Outer wall Upper installation fin, the gap between fin are more than burner hearth（3）1.5 times of the maximum particle diameter of interior high-temp solid material.

8. a kind of high-temp solid waste heat boiler, the waste heat boiler includes feed system, body of heater, heat-exchange system and discharge system （10）；The heat-exchange system is mainly formed by connecting by heat exchanger and outside heat-storing device by pipeline, and outside heat-storing device is vapour Bag（13）And/or boiler, heat exchanger are arranged on the burner hearth of body of heater（3）It is interior；It is characterized in that：

The burner hearth（3）At least one heat exchange area is divided into from top to down（4）, each heat exchange area（4）The interior a set of gas of installation Body disturbance device；The gas disturbance device includes warm-air pipe（7）With hot blast pump（15）, select one of following arrangement：

C, in heat exchange area（4）Middle arrangement air-blowing mouth（6）, air-blowing mouth（6）Pass through warm-air pipe（7）With hot blast pump（15）Air outlet Connection, hot blast pump（15）Air inlet lead to air, hot blast pump（15）Each heat transfer zone is blown into from the gas at normal temperature of outside suction Domain（4）In, heat exchange area（4）Interior gas is discharged from discharging opening or elsewhere carries out gas disturbance heat exchange；

9. waste heat boiler according to claim 8, it is characterised in that：The air entry（5）Select following arrangement it One or combination：

063：Air-blowing mouth（6）It is arranged in heat exchange area（4）The air-blowing room on top（32）Air-blowing plate（33）On, air-blowing room （32）Mainly by air-blowing plate（33）, air chamber panel or body of heater body of heater at the top of, the furnace wall of body of heater（2）Or side plate composition, at least one Root discharge nozzle（9）Through air-blowing room（32）, air-blowing room（32）Upper setting air inlet（36）；

The A types gas disturbance device configuration is as follows：

In 052 type air entry（5）In 062 type air-blowing mouth（6）When supporting, air intake duct（17）Heat exchange area can also be arranged in（4） Bottom or top, while aspiration tube（18）Heat exchange area can also be arranged in（4）Middle part；

The Type B gas disturbance device configuration is as follows：

The c-type gas disturbance device configuration is as follows：

Air-blowing mouth（6）Pass through warm-air pipe（7）With hot blast pump（15）Air outlet connection, or air-blowing mouth（6）Pass through air inlet （36）Through warm-air pipe（7）With hot blast pump（15）Air outlet connection；

Each discharging region（23）Area equation, discharge nozzle（9）It is arranged on discharging region（23）Center.

10. waste heat boiler according to claim 8 or claim 9, it is characterised in that：The air intake duct（17）And aspiration tube（18） It is horizontally disposed and run through furnace wall（2）；The warm-air pipe（7）, air intake duct（17）, aspiration tube（18）, induction chamber（20）, air-blowing room （32）On removing dust and clearing ash device can be installed（19）, removing dust and clearing ash device（19）From ash-removing valve, cyclone dust collectors, pneumatic dust removal device, One of sack cleaner, other dust arresters or combination；Air entry（5）On dust-proof blast cap can be installed（34）Or louvre type is prevented Dust hood or other dust guards；

The hot blast pump（15）The pump housing（16）And warm-air pipe（7）Heat exchange area can be arranged on（4）Interior or heat exchange area（4）'s Furnace wall（2）In；The charging aperture of the body of heater（1）On can install lock wind feed arrangement（11）；Lock wind feed arrangement（11）For rotation Turn sealing valve, or in burner hearth（3）Coffer, or the feed pipe insertion burner hearth of feed system are installed on top（3）It is interior；Using feed pipe When, high-temp solid material, which fills up feed pipe and blocks the outlet of feed pipe lower end, realizes self-sealed lock wind；The heat exchanger tube（12） Outer wall on fin can be installed, the gap between fin is more than burner hearth（3）1.5 times of the maximum particle diameter of interior material；

The discharger being capable of configuration lock wind dust guard；

Suitable for 101 type discharge systems（10）Discharger lock wind dust guard：By sealing shell（26）With rotary seal valve （14）Composition；The rotary seal valve（14）Installed in zone flow controller（25）Lower section；Discharge nozzle（9）Export department Divide, zone flow controller（25）, rotary seal valve（14）Entrance all by sealing shell（26）Surrounded；

Suitable for 102 type discharge systems（10）Discharger lock wind dust guard：By sealing shell（26）With automatically controlled sealing lock Plate（31）Composition；Zone flow controller（25）Outlet and warehouse（28）Entrance between automatically controlled sealing damper is installed（31）, Warehouse（28）Outlet lean on automatically controlled discharge door（29）It is dust-proof to lock wind；The discharge nozzle（9）Exit portion, zone flow controller （25）, automatically controlled sealing damper（31）, warehouse（28）Entrance all by sealing shell（26）Surrounded；Each automatically controlled sealing damper （31）Electrically connected with discharge controller；

Suitable for 103 type discharge systems（10）Discharger lock wind dust guard：By sealing shell（26）With automatically controlled sealing lock Plate（31）Composition；Zone flow controller（25）Outlet and constant volume feed bin（22）Entrance between automatically controlled sealing damper is installed （31）, constant volume feed bin（22）Outlet lean on automatically controlled discharge door（29）It is dust-proof to lock wind；The discharge nozzle（9）Exit portion, region Flow controller（25）, automatically controlled sealing damper（31）, constant volume feed bin（22）Entrance all by sealing shell（26）Surrounded；Respectively Automatically controlled sealing damper（31）Electrically connected with discharge controller；

The discharge nozzle（9）The bottom plate of surrounding（8）Raise up and to be formed and discharge nozzle（9）The funnel type chute being connected, or Each discharging region（23）Border installation riser formed and discharge nozzle（9）The compartment being connected；The discharge nozzle（9）On be located at Bottom plate（8）The part of lower section and zone flow controller（25）Between being capable of installation and repairing valve（24）；The zone flow control Device（25）For automatically controlled flashboard, vibration discharger, double-deck push-pull valve or terraced valve is taken out, 3mm is kept with discharging opening when automatically controlled flashboard is installed Above distance；The constant volume feed bin（22）Interior installation constant volume bin-level instrument（30）, each constant volume bin-level instrument（30）With going out Expect controller electrical connection.