CN106931422A

CN106931422A - A kind of method of heat exchange in high-temp solid waste heat boiler and stove

Info

Publication number: CN106931422A
Application number: CN201710272936.3A
Authority: CN
Inventors: 彭武星; 彭周雅柔
Original assignee: Individual
Current assignee: Hunan Xinghua Energy Technology Service Co ltd
Priority date: 2017-03-02
Filing date: 2017-04-24
Publication date: 2017-07-07

Abstract

A kind of method the invention discloses being exchanged heat in high-temp solid waste heat boiler and stove, the waste heat boiler includes feed system, body of heater, heat-exchange system and discharge system；Heat-exchange system is main to be formed by connecting by heat exchanger and outside heat-storing device by pipeline, and outside heat-storing device is drum and 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；1.5 times of level interval more than material maximum particle diameter in burner hearth between adjacent heat exchange pipe outer wall；Heat exchange area is divided in burner hearth, gas disturbance device is installed in heat exchange area.In addition to setting heat exchange area is used in burner hearth and gas disturbance device is installed, the operation thickness that also control material exchanges heat in burner hearth is not less than 2 meters to methods described；Move down speed and be not more than 20 meters per hour.The present invention 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 method of heat exchange in high-temp solid waste heat boiler and stove

Technical field

The present invention relates to a kind of waste heat boiler, more particularly to one kind directly reclaims its waste heat as thermal source with high-temp solid material High-temp solid waste heat boiler and stove in heat exchange method.

Technical background

It is the waste heat of the high-temp solid material of generation during remanufacture, conventional methods are all first to be consolidated with high temperature with gas Body material-heat-exchanging, high-temp solid material is cooled, and gas is heated to form high-temperature gas and enters back into gas waste-heat boiler；Its deficiency Place be high equipment cost, floor space it is big, from power consumption it is high, high-temp solid material utilization rate of waste heat is low, leak out and cannot keep away completely Exempt from.At present, the scheme proposition of existing solid waste heat boiler, 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 ", during its principle is 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 of scheme is stopped Walk in experimental stage, and industrialization is not implemented, its basic reason has at 2 points：One is the high temperature being deposited in solid waste heat boiler When being moved from top to down by deadweight, the tube wall with the heat exchanger tube being embedded in high temperature burning solid material is only connect solid material Touch heat exchange and radiation heat transfer, be enclosed in solid material around heat exchanger tube and 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 Either the thermal conductivity factor of 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 difficult 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 of scheme does not solve same level in the solid waste heat boiler of big cross-sectional area really The flat problem for declining discharging, causes the solid material having to be imitated in residing time in furnace short, is not sufficiently cooled and discharges, and goes out material temperature Spend height, it is impossible to reach the purpose of cooling down high-temperature solid material while reclaiming high-temp solid material waste heat.

The content of the invention

It is an object of the invention to overcome deficiency of the prior art, there is provided such a can be consolidated high temperature is directly reclaimed The method of heat exchange in the high-temp solid waste heat boiler and stove of body material waste heat.

The purpose of the present invention 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 main by heat exchanger It is formed by connecting by pipeline with outside heat-storing device, outside heat-storing device is one of drum and boiler and combinations thereof, heat exchanger 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；Every group is changed The water inlet of heat pipe is connected by the water inlet union of this group with the water inlet pipe of this group, and every group of delivery port of heat exchanger tube is by this group Water outlet union is connected with the outlet pipe of this group；Level interval between adjacent heat exchange pipe outer wall is more than material maximum grain in burner hearth 1.5 times of footpath；

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

A, setting air entry and air-blowing mouthful in heat exchange area, air entry are connected by warm-air pipe with the air inlet of hot blast pump, drum Gas port is connected by warm-air pipe with the air outlet of hot blast pump, partial hearth, warm-air pipe and hot blast pump structure where certain heat exchange area Into hot air circulating system, hot blast pump carries out gas and follows from being extracted out in each heat exchange area high-temperature gas returns to this heat exchange area again in Ring disturbance heat exchange；

B, air entry is set in heat exchange area, air entry is connected by warm-air pipe with the air inlet of hot blast pump, hot blast pump goes out Lead to air in air port, and hot blast pump extracts the gas in each heat exchange area out row to air, and automatically from charging aperture or other ground Side's supplement air carries out gas disturbance heat exchange；

C, air-blowing mouthful is arranged in heat exchange area, air-blowing mouthful is connected by warm-air pipe with the air outlet of hot blast pump, hot blast pump enters Lead to air in air port, and 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 from Discharging opening or elsewhere discharge carry 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 base 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；One end of air intake duct is 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 suction plate, stove The base plate composition of the furnace wall of body or side plate, air chamber base plate or body of heater, at least one discharge nozzle runs through induction chamber, is set on induction chamber Air outlet；

One of following arrangement of the air-blowing mouthful selection or combination：

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

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

063：Air-blowing mouthful is arranged on the air-blowing plate of the air-blowing room on heat exchange area top, and air-blowing room is main by air-blowing plate, gas The body of heater top of room panel or body of heater, furnace wall or side plate composition, at least one discharge nozzle run through air-blowing room, set on air-blowing room into Air port；

The A types gas disturbance device configuration is as follows：

In 051 type air entry and supporting 061 type air-blowing mouthful, air entry and air-blowing mouthful can also be in the whole furnace walls of heat exchange area Upper arrangement face-to-face；

When 052 type air entry and 062 type air-blowing are mouthful supporting, air intake duct can also be arranged in the bottom of heat exchange area or on Portion, aspiration tube is 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 passes through air outlet through warm-air pipe and heat The air inlet connection of air pump；Air-blowing mouthful is connected by warm-air pipe with the air outlet of hot blast pump, or air-blowing mouthful is passed through by air inlet Warm-air pipe is connected 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 passes through air outlet through warm-air pipe and hot blast pump Air inlet connection；

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

Air-blowing mouthful is connected by warm-air pipe with the air outlet of hot blast pump, or air-blowing mouthful passes through air inlet through warm-air pipe and hot blast pump Air outlet connection.

The air intake duct and aspiration tube are horizontally disposed and 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 selects 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；Lock wind feed arrangement is rotary seal valve, or installs close on burner hearth top 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 blocks 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 by changing Hot device and outside heat-storing device are formed by connecting by pipeline, and outside heat-storing device is one of drum and boiler and combinations thereof, is changed Hot device is arranged in the burner hearth of body of heater；

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

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

The discharge system is mainly made up of discharger and discharge controller, the quantity phase in the quantity of discharger and the region that discharges Deng lower section of the discharger installed in discharging region；The electric control system of discharger is electrically connected with discharge controller；The discharging Device includes discharge nozzle and zone flow controller, and discharge nozzle is connected through base plate with burner hearth, the lower section installation region stream of discharge nozzle Amount controller；Match as needed one of following：

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

102：Electronic-weighing storehouse is installed in the outlet of the zone flow controller；Electronic-weighing storehouse include electronic weight inductor, Warehouse and automatically controlled discharge door；I.e.：Positioned at the top of the entrance of warehouse, automatically controlled discharge door is arranged on for the outlet of zone flow controller The lower section of the outlet of warehouse, electronic weight inductor is arranged on warehouse；Zone flow controller, electronic weight inductor and electricity The electric control part for controlling discharge door is electrically connected with discharge controller；Discharge controller is according to each discharger of temperature adjusting of discharging Discharging speed；Can make each discharger that weight identical material is discharged within the work period of identical duration, make same in burner hearth The material of horizontal plane uniformly declines；

103：The constant volume feed bin with automatically controlled discharge door is installed in the outlet of the zone flow controller；I.e.：Zone flow is controlled The outlet of device is positioned at the top of the entrance of constant volume feed bin；Each zone flow controller, automatically controlled discharge door electric control part with go out Material controller electrical connection；Discharging speed of the discharge controller according to each discharger of temperature adjusting of discharging；Each discharger can be made The discharge volume identical material within the work period of identical duration, makes the material of same level in burner hearth uniformly decline；

The high-temp solid material by feed system from charging aperture into burner hearth in and be stacked into not less than 2 meters of operation thickness, Heat exchanger tube is buried in high-temp solid material；Discharge system maintains above-mentioned operation thickness, high-temp solid with feed system linkage Material is moved from top to down by deadweight in burner hearth with the speed less than 20 meters per hour, is exchanged heat with the water in heat exchanger tube.

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

Base plate around the discharge nozzle raises up the funnel type chute to be formed and be connected with discharge nozzle, or each discharging Riser is installed and forms the compartment being connected with discharge nozzle in the border in region；On the discharge nozzle be located at base plate below part 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；Constant volume material is installed in the constant volume feed bin Level-sensing device each constant volume bin-level instrument in storehouse is electrically connected with discharge controller；Fin, fin are installed on the outer wall of the heat exchanger tube Between 1.5 times of gap more than the maximum particle diameter of high-temp solid material in burner hearth.

High-temp solid waste heat boiler technical scheme three：

C, air-blowing mouthful is arranged in heat exchange area, air-blowing mouthful is connected by warm-air pipe with the air outlet of hot blast pump, hot blast pump enters Lead to air in air port, and 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 from Discharging opening or elsewhere discharge carry out gas disturbance heat exchange；

The air entry selects one of following arrangement or combination：

063：Air-blowing mouthful is arranged on the air-blowing plate of the air-blowing room on heat exchange area top, and air-blowing room is main by air-blowing plate, gas The body of heater top of room panel or body of heater, the furnace wall of body of heater or side plate composition, at least one 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：

When 052 type air entry is mouthful supporting in 062 type air-blowing, air intake duct can also be arranged in the bottom of heat exchange area or on Portion, 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 mouthful is connected by warm-air pipe with the air outlet of hot blast pump, or air-blowing mouthful passes through air inlet through warm-air pipe and hot blast pump Air outlet connection；

The air intake duct and aspiration tube are horizontally disposed and 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 selects 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 body of heater Lock wind feed arrangement can be installed on charging aperture；Lock wind feed arrangement is rotary seal valve, or installs coffer on burner hearth top, Or in the feed pipe insertion burner hearth of feed system；During using feed pipe, high-temp solid material fills up feed pipe and blocks feed pipe Self-sealed lock wind is realized in lower end outlet；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；

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 with rotary seal valve sealing shell；It is described Rotary seal valve is arranged on the lower section of zone flow controller；The exit portion of discharge nozzle, zone flow controller, rotatory sealing The entrance of valve is all surrounded by sealing shell；

Suitable for the lock wind dust guard of the discharger of 102 type discharge systems：It is made up of sealing shell and automatically controlled sealing damper；Area Automatically controlled sealing damper is installed, the outlet of warehouse is by automatically controlled discharging door lock wind between the outlet of domain flow controller and the entrance of warehouse It is dust-proof；The exit portion of the discharge nozzle, zone flow controller, automatically controlled sealing damper, the entrance of warehouse are all sealed outer Shell is surrounded；Each automatically controlled sealing damper is electrically connected with discharge controller；

Suitable for the lock wind dust guard of the discharger of 103 type discharge systems：It is made up of sealing shell and automatically controlled sealing damper；Area Automatically controlled sealing damper is installed between the outlet of domain flow controller and the entrance of constant volume feed bin, the outlet of constant volume feed bin by it is automatically controlled go out Bin gate lock wind is dust-proof；The exit portion of the discharge nozzle, zone flow controller, automatically controlled sealing damper, the entrance of constant volume feed bin All surrounded by sealing shell；Each automatically controlled sealing damper is electrically connected with discharge controller；

Base plate around the discharge nozzle raises up the funnel type chute to be formed and be connected with discharge nozzle, or the region that respectively discharges Border riser be installed form the compartment that is connected with discharge nozzle；Part and region below base plate are located on the discharge nozzle Being capable of installation and repairing valve between flow controller；The zone flow controller is automatically controlled flashboard, vibration discharger, double-deck plate Valve takes out terraced valve, and more than 3mm distances are kept with discharging opening when automatically controlled flashboard is installed；Constant volume feed bin material is installed in the constant volume feed bin Position instrument, each constant volume bin-level instrument is electrically connected with discharge controller.

The method of heat exchange in high-temp solid waste heat boiler stove：

Methods described includes the water in the heat and heat exchanger tube in high-temp solid material is carried out into heat by the way of radiation, conduction Exchange；

From any one waste heat boiler described in high-temp solid waste heat boiler stove technical scheme one, three；

Subregion heat exchange is carried out using setting heat exchange area in burner hearth；

The operation thickness that control high-temp solid material exchanges heat in burner hearth is not less than 2 meters；

The speed that moves down of high-temp solid material is controlled to be not more than 20 meters per hour；

Gas disturbance device is installed to improve the heat exchange efficiency of radiation and conduction, gas perturbation scheme is from one of following；

A, in heat exchange area high-temperature gas circulation disturbed, there is no thermal loss；

B, arranged to air from gas bleeding in each heat exchange area, fill into air and disturbed while automatic；

C, air is blasted on each heat exchange area top, while being disturbed to the unnecessary gas of airborne release.

The present invention with simple and reasonable, heat exchange efficiency is improved by discharging control compared with prior art, 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 one embodiment of the invention structural representation：Using A type gas disturbance devices, 051 type air entry and O61 types Supporting, the discharge system of 102 type dischargers of air-blowing mouthful.

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

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

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

Fig. 5 is one embodiment of the invention structural representation, using A type gas disturbance devices, 052 type air entry and O62 types Supporting, the discharge system of 103 type dischargers of air-blowing mouthful.

Fig. 6 is one embodiment of the invention structural representation, using A type gas disturbance devices, 052,053 type air entry with Supporting, the discharge system of 103 type dischargers of O62 types air-blowing mouthful.

Fig. 7 is one embodiment of the invention structural representation, using A type gas disturbance devices, 052 type air entry and O62 types Supporting, the discharge system of 101 type dischargers of air-blowing mouthful.

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

Fig. 9 is one embodiment of the invention structural representation, using A type gas disturbance devices, 052,053 type air entry with Supporting, the discharge system of 101 type dischargers of O62 types air-blowing mouthful.

Figure 10 is one embodiment of the invention structural representation, using A type gas disturbance devices, 053 type air entry and 061, Supporting, the discharge system of 103 type dischargers of O62 types air-blowing mouthful.

Figure 11 is one embodiment of the invention structural representation, and burner hearth is divided into a heat exchange area, is disturbed using A types gas Device, 053 type air entry and supporting, the discharge system of 103 type dischargers of O62 types air-blowing mouthful.

Figure 12 is the extended pattern structural representation of Fig. 5.

Figure 13 is the extended pattern structural representation of Fig. 3.

Figure 14 is one embodiment of the invention structural representation, and burner hearth is divided into a heat exchange area, is disturbed using Type B gas Device, 053 type air entry, the discharge system of 103 type dischargers.

Figure 15 is one embodiment of the invention structural representation, and burner hearth is divided into a heat exchange area, is disturbed using c-type gas Device, O61 types air-blowing mouthful, the discharge system of 102 type dischargers.

Figure 16 is one embodiment of the invention structural representation, and burner hearth is divided into a heat exchange area, is disturbed using c-type gas Device, O63 types air-blowing mouthful, the discharge system of 102 type dischargers.

Figure 17 is one embodiment of the invention structural representation, the discharge system of 102 type dischargers.

Figure 18 is one embodiment of the invention structural representation, the discharge system of 103 type dischargers.

Figure 19 is one embodiment of the invention structural representation, the discharge system of 101 type dischargers.

Figure 20 is the extended pattern structural representation of Figure 19.

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 mouthful, 7- warm-air pipes, 8- Base 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.

Specific embodiment

With reference to embodiment, the invention will be further described：

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 it is main by Heat exchanger and outside heat-storing device are formed by connecting by pipeline, and outside heat-storing device is one of drum 13 and boiler and its group Close, heat exchanger is arranged 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；Every group The water inlet of heat exchanger tube 12 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 12 passes through The water outlet union of this group is connected with the outlet pipe of this group；Level interval between the adjacent outer wall of heat exchanger tube 12 is more than in burner hearth 3 1.5 times of material maximum particle diameter；

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

A, setting air entry 5 and air-blowing mouthful 6 in heat exchange area 4, air entry 5 is by warm-air pipe 7 and the air inlet of hot blast pump 15 Connection, air-blowing mouthful 6 is connected by warm-air pipe 7 with the air outlet of hot blast pump 15, the partial hearth 3, hot blast where certain heat exchange area 4 Pipe 7 constitutes hot air circulating system with hot blast pump 15, and the extraction high-temperature gas from each heat exchange area 4 of hot blast pump 15 is returned to and originally changed again Gas circulation disturbance heat exchange is carried out in thermal region 4；

B, the setting air entry 5 in heat exchange area 4, air entry 5 are connected by warm-air pipe 7 with the air inlet of hot blast pump 15, hot blast The air outlet of pump 15 leads to air, and hot blast pump 15 extracts the gas in each heat exchange area 4 out row to air, and automatic from charging aperture 1 or elsewhere supplement air carry out gas disturbance heat exchange；

C, the arrangement air-blowing mouthful 6 in heat exchange area 4, air-blowing mouthful 6 is connected by warm-air pipe 7 with the air outlet of hot blast pump 15, hot blast The air inlet of 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, heat exchange area Gas in 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 base 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 intake duct 17 One end be 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 by inhaling The base plate 8 of the furnace wall 2 of gas plate 21, body of heater or side plate, air chamber base plate or body of heater is constituted, and at least one discharge nozzle 9 runs through induction chamber 20, air outlet 35 is set on induction chamber 20；

One of following arrangement of the selection of air-blowing mouthful 6 or combination：

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

062：Air-blowing mouthful 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 mouthful 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 by rousing The body of heater top of gas plate 33, air chamber panel or body of heater, furnace wall 2 or side plate composition, at least one discharge nozzle 9 run 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 mouthful 6, air entry 5 and air-blowing mouthful 6 can also be in the whole of heat exchange area 4 Arranged face-to-face on individual furnace wall 2；

When 052 type air entry 5 and 062 type air-blowing mouthfuls 6 is supporting, air intake duct 17 can also be arranged in heat exchange area 4 bottom or Person top, aspiration tube 18 is 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 through heat Airduct 7 is connected with the air inlet of hot blast pump 15；Air-blowing mouthful 6 is connected by warm-air pipe 7 with the air outlet of hot blast pump 15, or air-blowing Mouth 6 is connected through warm-air pipe 7 by air inlet 36 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 passes through air outlet 35 through warm-air pipe 7 Air inlet with hot blast pump 15 is connected；

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

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

The air intake duct 17 and aspiration tube 18 are horizontally disposed and 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；Lock wind feed arrangement 11 is rotary seal valve, 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 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, 1.5 times of gap more than the maximum particle diameter of material in burner hearth 3 between fin.

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 for circle, ratio of height to diameter is more than 0.8, and when the cross section of burner hearth 3 is rectangle, depth-width ratio is more than 0.8；

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

The discharge system 10 is mainly made up of discharger and discharge controller, the quantity in the quantity of discharger and the region 23 that discharges Equal, discharger is arranged on the lower section in discharging region 23；The electric control system of discharger is electrically connected with discharge controller；It is described Discharger includes discharge nozzle 9 and zone flow controller 25, and discharge nozzle 9 is connected through base plate 8 with burner hearth 3, the lower section of discharge nozzle 9 Installation region flow controller 25；Match as needed one of following：

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

102：Electronic-weighing storehouse is installed in the outlet of the zone flow controller 25；Electronic-weighing storehouse includes electronic weight inductor 27th, warehouse 28 and automatically controlled discharge door 29；I.e.：The outlet of zone flow controller 25 is automatically controlled positioned at the top of the entrance of warehouse 28 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 is controlled The electric control part of device 25, electronic weight inductor 27 and automatically controlled discharge door 29 is electrically connected with discharge controller；Discharge controller The discharging speed of each discharger of temperature adjusting according to discharging；Each discharger can be made to be discharged within the work period of identical duration Weight identical material, makes the material of same level in burner hearth 3 uniformly decline；

103：The constant volume feed bin 22 with automatically controlled discharge door 29 is installed in the outlet of the zone flow controller 25；I.e.：Flow in region The outlet of amount 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 is electrically connected with discharge controller；Discharging speed of the discharge controller according to each discharger of temperature adjusting of discharging； 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 declines；

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

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

Base 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 compartment that the border installation riser formation in region 23 that discharges is connected with discharge nozzle 9；It is located under base plate 8 on the discharge nozzle 9 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 and constant volume bin-level instrument 30 is installed in feed bin 22, each constant volume bin-level instrument 30 is electrically connected with discharge controller；It is described to change Fin is installed, 1.5 of the gap between fin more than 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 disturbance is installed in each heat exchange area 4 Device；The gas disturbance device includes warm-air pipe 7 and hot blast pump 15, selects one of following arrangement：

C, the arrangement air-blowing mouthful 6 in heat exchange area 4, air-blowing mouthful 6 is connected by warm-air pipe 7 with the air outlet of hot blast pump 15, hot blast The air inlet of 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, heat exchange area Gas in 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：

063：Air-blowing mouthful 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 by rousing The body of heater top of gas plate 33, air chamber panel or body of heater, the furnace wall 2 of body of heater or side plate composition, at least one discharge nozzle 9 run through air-blowing Room 32, sets air inlet 36 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 mouthfuls 6, air intake duct 17 can also be arranged in heat exchange area 4 bottom or Person 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 mouthful 6 is connected by warm-air pipe 7 with the air outlet of hot blast pump 15, or air-blowing mouthful 6 passes through air inlet 36 through warm-air pipe 7 Air outlet with hot blast pump 15 is connected；

The air intake duct 17 and aspiration tube 18 are horizontally disposed and 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 in heat exchange area 4 or in the furnace wall 2 of heat exchange area 4；Institute State and can be installed on the charging aperture 1 of body of heater lock wind feed arrangement 11；Lock wind feed arrangement 11 is rotary seal valve, or in burner hearth 3 Installed on top in coffer, or the feed pipe insertion burner hearth 3 of feed system；During using feed pipe, high-temp solid material fill up into Expects pipe and block feed pipe lower end outlet realize self-sealed lock wind；Fin, wing can be installed on the outer wall of the heat exchanger tube 12 1.5 times of gap more than the maximum particle diameter of material in burner hearth 3 between piece；

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 14 groups of sealing shell 26 and rotary seal valve Into；The rotary seal valve 14 is arranged on the lower section of zone flow controller 25；The exit portion of discharge nozzle 9, zone flow control Device processed 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 damper 31 Composition；Automatically controlled sealing damper 31, the outlet of warehouse 28 are installed between the outlet of zone flow controller 25 and the entrance of warehouse 28 It is dust-proof by the lock wind of automatically controlled discharge door 29；The exit portion of the discharge nozzle 9, zone flow controller 25, automatically controlled sealing damper 31, The entrance of warehouse 28 is all surrounded by sealing shell 26；Each automatically controlled sealing damper 31 is electrically connected 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 damper 31 Composition；Automatically controlled sealing damper 31, constant volume feed bin are installed between the outlet of zone flow controller 25 and the entrance of constant volume feed bin 22 22 outlet is dust-proof by the lock wind of automatically controlled discharge door 29；It is the exit portion of the discharge nozzle 9, zone flow controller 25, automatically controlled close Envelope flashboard 31, the entrance of constant volume feed bin 22 are all surrounded by sealing shell 26；Each automatically controlled sealing damper 31 with discharging control Device is electrically connected；

Base plate 8 around the discharge nozzle 9 raises up the funnel type chute to be formed and be connected with discharge nozzle 9, or each discharging Riser is installed and forms the compartment being connected with discharge nozzle 9 in the border in region 23；The lower section of base plate 8 is located on the discharge nozzle 9 Being capable of installation and repairing valve 24 between part and zone flow controller 25；The zone flow controller 25 is automatically controlled flashboard, shakes Dynamic 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；The constant volume material Constant volume bin-level instrument 30 is installed, each constant volume bin-level instrument 30 is electrically connected with discharge controller in storehouse 22.

Heat-exchange method in high-temp solid waste heat boiler stove：

Methods described includes carrying out the water in the heat in high-temp solid material and heat exchanger tube 12 by the way of radiation, conduction Heat exchange；

Subregion heat exchange is carried out using setting heat exchange area 4 in burner hearth 3；

The operation thickness that control high-temp solid material exchanges heat in burner hearth 3 is not less than 2 meters；

A, in heat exchange area 4 high-temperature gas circulation disturbed, there is no thermal loss；

B, arranged to air from gas bleeding in each heat exchange area 4, fill into air and disturbed while automatic；

C, air is blasted on the top of each heat exchange area 4, while being disturbed to the unnecessary gas of airborne release.

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 main to be formed by connecting by heat exchanger and outside heat-storing device by pipeline, and outside heat-storing device is vapour Bag（13）With one of boiler and combinations thereof, heat exchanger is 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 with the water inlet pipe of this group by the water inlet union 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）It is interior to install 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 mouthful（6）, air entry（5）By warm-air pipe（7）With hot blast pump （15）Air inlet connection, air-blowing mouthful（6）By 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）Constitute 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）In carry out gas circulation disturbance heat exchange；

B, in heat exchange area（4）Middle setting air entry（5）, air entry（5）By 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 extracts row out to big Gas, and it is automatic from charging aperture（1）Or supplement air carries out gas disturbance heat exchange elsewhere；

C, in heat exchange area（4）The air-blowing mouthful of middle arrangement（6）, air-blowing mouthful（6）By 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）The base plate of upper and/or body of heater（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 base plate of side plate, air chamber base 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 mouthful（6）Select one of following arrangement or combination：

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

062：Air-blowing mouthful（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 mouthful（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）, the body of heater top of air chamber panel or body of heater, 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 mouthful（6）When supporting, air entry（5）With air-blowing mouthful（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 mouthful（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）By warm-air pipe（7）With hot blast pump（15）Air inlet connection, or air entry（5）By air-out Mouthful（35）Through warm-air pipe（7）With hot blast pump（15）Air inlet connection；Air-blowing mouthful（6）By warm-air pipe（7）With hot blast pump（15） Air outlet connection, or air-blowing mouthful（6）By 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）By warm-air pipe（7）With hot blast pump（15）Air inlet connection, or air entry（5）By 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 mouthful（6）By warm-air pipe（7）With hot blast pump（15）Air outlet connection, or air-blowing mouthful（6）By 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 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. the waste heat boiler according to claim 1 or 2 or 3, 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）It is rotary seal valve, or in burner hearth（3）Installed on top closed Plate, or the feed pipe of feed system inserts burner hearth（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 main to be formed by connecting by heat exchanger and outside heat-storing device by pipeline, and outside heat-storing device is vapour Bag（13）With one of boiler and combinations thereof, heat exchanger is 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 is more than 0.8, burner hearth（3）Cross section be rectangle when, depth-width ratio More than 0.8；

The base 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 base 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 electronic-weighing storehouse is installed；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 go out Material controller electrical connection；Discharging speed of the discharge controller according to 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 install 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. the waste heat boiler according to claim 5 or 6, it is characterised in that：The discharge nozzle（9）The base 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 install riser formed with Discharge nozzle（9）The compartment being connected；The discharge nozzle（9）It is upper to be located at base 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）For automatically controlled flashboard, vibration discharger, bilayer are inserted 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 is 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 main to be formed by connecting by heat exchanger and outside heat-storing device by pipeline, and outside heat-storing device is vapour Bag（13）With one of boiler and combinations thereof, heat exchanger is 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）It is interior that a set of gas is installed 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）The air-blowing mouthful of middle arrangement（6）, air-blowing mouthful（6）By 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 combines：

063：Air-blowing mouthful（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）, the body of heater top of air chamber panel or body of heater, 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 mouthful（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 mouthful（6）By warm-air pipe（7）With hot blast pump（15）Air outlet connection, or air-blowing mouthful（6）By 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 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 anti- 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）It is rotation Turn sealing valve, or in burner hearth（3）Coffer is installed on top, or the feed pipe of feed system inserts burner hearth（3）It is interior；Using feed pipe When, high-temp solid material 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 be 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 Point, 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）Lock wind is dust-proof；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）Lock wind is dust-proof；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 base plate of surrounding（8）Raise up to be formed and discharge nozzle（9）The funnel type chute being connected, or Each discharging region（23）Border install riser formed and discharge nozzle（9）The compartment being connected；The discharge nozzle（9）On be located at Base 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 go out Material controller electrical connection.

The method of heat exchange in a kind of 11. high-temp solid waste heat boiler stoves, methods described is included height by the way of radiation, conduction Heat and heat exchanger tube in warm solid material（12）In water carry out heat exchange；It is characterized in that：

From claim 1-4, any one waste heat boiler described in 8-10；

In burner hearth（3）Middle use sets heat exchange area（4）Carry out subregion heat exchange；

Control high-temp solid material is in burner hearth（3）The operation thickness of middle heat exchange is not less than 2 meters；

A, in heat exchange area（4）Interior high-temperature gas circulation is disturbed, and does not have thermal loss；

B, from each heat exchange area（4）Interior gas bleeding is arranged to air, while fill into air automatically being disturbed；

C, in each heat exchange area（4）Top blasts air, while being disturbed to the unnecessary gas of airborne release.