Summary of the invention
It is an object of the invention to provide one to prevent that pot furnace pressure is too high when there is accidental power failure, preventing from burning
Dry boiler safety production system, also will not produce steam contamination to working space when release aerofluxus.
For achieving the above object, the boiler of the present invention prevents that dryouting safety production system includes boiler, is provided with burning in boiler
Room and heating chamber;Heating chamber connects boiler water inlet pipe and boiler discharging tube, and boiler water inlet pipe connects softening water tank, softens water
The top of case connects soft water water inlet pipe, and soft water water inlet pipe connects water softener, and water softener connects external by soft water water inlet pipe
Water source;Boiler water inlet pipe is provided with for the feed pump of boiler water supply;
Described heating chamber is arranged over burn-out-proof solid carbon dioxide case, and burn-out-proof solid carbon dioxide case is arranged over water supply tank;
The top of heating chamber is connected by the top of the first pipeline with described burn-out-proof solid carbon dioxide case, the bottom of described burn-out-proof solid carbon dioxide case
It is connected with the middle part of heating chamber by the second pipeline;First pipeline is provided with the first valve, and the second pipeline is provided with the second valve
Door;The bottom of described burn-out-proof solid carbon dioxide case is higher than the top of described heating chamber;The sidewall bottom of described burn-out-proof solid carbon dioxide case connects useful
In the first transparent tube of instruction burn-out-proof solid carbon dioxide case middle water level, the upper end of the first transparent tube is connected with the top of burn-out-proof solid carbon dioxide case;
Burn-out-proof solid carbon dioxide box top connects atmospheric valve;Heating room side wall connects thermometer;
The bottom of described water supply tank is higher than the top of burn-out-proof solid carbon dioxide case;The bottom of water supply tank connects described burn-out-proof by the 3rd pipeline
The top of solid carbon dioxide case, the 3rd pipeline is provided with the 3rd valve;The top of water supply tank is connected by filling pipe to be had for for water supply tank
The small pump supplied water, the water inlet pipe of small pump connects external water source;
The sidewall bottom of described water supply tank connects the second transparent tube for showing water level, and the top of the second transparent tube is higher than mending
Water tank top and its open top;The connection that is inclined upwardly of the top of described second transparent tube has a pole, pole top connect have recessed
Ventricumbent arc lid, arc lid is positioned at the top of the second transparent tube;
Described heating room side wall is provided with the first Pressure gauge for showing heating room pressure, and described burn-out-proof solid carbon dioxide case sidewall is provided with
The second Pressure gauge of pressure within showing burn-out-proof solid carbon dioxide case;
Described heating chamber top is provided with safety and environmental protection releasing device;Safety and environmental protection releasing device includes relief valve, heat exchanger, use
In receiving tank and the cooling blower of steam, the import of relief valve connects the top of heating chamber by safety line;Tank
Inside fill water;
Heat exchanger includes housing, and in housing, the length direction along housing is provided with air-cooled heat exchanger tube, and air-cooled heat exchange pipe external surface is uniform
It is interval with some annulus fins;The entrance point of air-cooled heat exchanger tube connects the 4th pipeline, going out of the 4th pipeline connection safety valve
Mouthful;
The port of export of air-cooled heat exchanger tube connects has the 5th pipeline, the 5th pipeline to be passed through a side bottom of tank;Housing is in air-cooled
Connecting at heat exchanger tube entrance point has the 6th pipeline, the distal opening of the 6th pipeline to communicate with air;
Housing connects at the air-cooled heat exchanger tube port of export has the 7th pipeline, the distal opening of the 7th pipeline to communicate with air;6th
The distal opening of pipeline is higher than the distal opening at least 4 meters of the 7th pipeline;Described 7th pipeline is provided with described cooling blower.
Described relief valve includes tubular valve body, and valve body is provided with valve seat in entrance point, and valve seat center is provided with main pore, in valve seat
End is provided with horn mouth;Some secondary pores it are provided with between bell-mouthed sidewall and the outer face of valve seat;
Relief valve is provided with support orifice plate in outlet end, and supporting orifice plate has stage clip towards the connection of bell-mouthed side, and stage clip connects
Having the taper valve core suitable with described horn mouth, taper valve core is crimped on described bell-mouthed sidewall, and taper valve core
The described each secondary pore of sidewall closure;Support and be uniformly provided with multiple air-vent on orifice plate.
It is uniformly provided with multiple through hole on described annulus fin.
Present invention have the advantage that:
Use the present invention, when the heating room pressure of generation accident power-off, boiler is too high, by relief valve, soda pop can be mixed
Compound is discharged.Steam water interface is transferring heat to air through heat exchanger, so that major part steam is condensed into water.Vapour
Aqueous mixtures is finally passed through tank, and remaining a small amount of steam can be fully absorbed by the water in tank, thus avoids steam
Pollute.During accident power-off, staff can also utilize the heating chamber water filling to boiler of the water in burn-out-proof solid carbon dioxide case and water supply tank,
Thus prevent boiler from occurring dryouting phenomenon, both prevent the too high generation danger of pot furnace pressure, protected again boiler and do not dryouied, prevent
Only dryout rear equipment scrapping, extend the service life of boiler.
The setting of annulus fin can be greatly improved heat exchange efficiency, and the most too much affects air because of the existence of through hole
Flowing.
The distal opening of the 6th pipeline, higher than the distal opening at least 4 meters of the 7th pipeline, can play in cooling blower work
As time prevent the phenomenon of air flow shortcircuit (the 6th pipeline expellant gas is sucked by cooling blower again), it is ensured that cooling
Effect.Meanwhile, the distal opening position of the 6th pipeline is higher, it also avoid the air impact Ground Operation that temperature after heat exchange is higher
Personnel.
Pressure in heating chamber is the highest, and the distance that taper valve core leaves main pore and secondary pore is the most remote, taper valve core and loudspeaker
The current path formed between mouth sidewall is the widest, and vapour lock is the least, and the water and the steam that pass through in the unit interval are the most, reaches heating
The indoor technique effect that pressure is the highest, release speed is the fastest.The setting of secondary pore, it is possible to accelerate release speed, and strengthen
The technique effect that pressure in heating chamber is the highest, release speed is the fastest.
Detailed description of the invention
In Fig. 1 and Fig. 7, direction shown in arrow is the flow direction of fluid at this.
As shown in Figures 1 to 7, the boiler of the present invention prevents that dryouting safety production system includes boiler, is provided with burning in boiler
Room and heating chamber 1(combustor and heating chamber 1 are routine techniques, not shown combustor section);Heating chamber 1 connects has boiler to enter
Water pipe 2 and boiler discharging tube 3, boiler water inlet pipe 2 connects softening water tank 4, and the top of softening water tank 4 connects soft water water inlet pipe
5, soft water water inlet pipe 5 connects water softener 6, and water softener 6 connects external water source by soft water water inlet pipe 5;Water source can be city
Political affairs water system, it is also possible to be the river after precipitating, filtering and sterilize or lake water, not shown.Boiler water inlet pipe 2 is provided with use
In to the feed pump 7 of boiler water supply;
Described heating chamber 1 is arranged over burn-out-proof solid carbon dioxide case 8, and burn-out-proof solid carbon dioxide case 8 is arranged over water supply tank 9;
The top of heating chamber 1 is connected by the top of the first pipeline 10 with described burn-out-proof solid carbon dioxide case 8, described burn-out-proof solid carbon dioxide case 8
Bottom be connected with the middle part of heating chamber 1 by the second pipeline 11;First pipeline 10 is provided with the first valve 46, the second pipeline
11 are provided with the second valve 12;The bottom of described burn-out-proof solid carbon dioxide case 8 is higher than the top of described heating chamber 1;Described burn-out-proof solid carbon dioxide case 8
Sidewall bottom connect and have the first transparent tube 13 for indicating burn-out-proof solid carbon dioxide case 8 middle water level, the upper end of the first transparent tube 13 with
The top of burn-out-proof solid carbon dioxide case 8 is connected;Burn-out-proof solid carbon dioxide case 8 top connects atmospheric valve 14;Heating chamber 1 sidewall connects thermometer
15;
The bottom of described water supply tank 9 is higher than the top of burn-out-proof solid carbon dioxide case 8;The bottom of water supply tank 9 connects institute by the 3rd pipeline 16
Stating the top of burn-out-proof solid carbon dioxide case 8, the 3rd pipeline 16 is provided with the 3rd valve 17;The top of water supply tank 9 is connected by filling pipe 18
Having the small pump 19 for supplying water for water supply tank 9, the water inlet pipe of small pump 19 connects external water source;
The sidewall bottom of described water supply tank 9 connects the second transparent tube 20 for showing water level, the top of the second transparent tube 20
Higher than water supply tank 9 top and its open top;Principle based on linker, in the second transparent tube 20 can show water supply tank 9
Water level.The connection that is inclined upwardly of the top of described second transparent tube 20 has a pole 21, and pole 21 top connects recessed ventricumbent arc
Lid 22, arc lid 22 is positioned at the top of the second transparent tube 20;The setting of arc lid 22, it is possible to avoid the process in long-term storage or use
Middle foreign body falls into the second transparent tube 20.
Described heating chamber 1 sidewall is provided with the first Pressure gauge 23 of pressure within showing heating chamber 1, described burn-out-proof solid carbon dioxide case
8 sidewalls are provided with the second Pressure gauge 24 of pressure within showing burn-out-proof solid carbon dioxide case 8;
Described heating chamber 1 top is provided with safety and environmental protection releasing device;Safety and environmental protection releasing device includes relief valve 25, heat exchange
Device, for receiving tank 26 and the cooling blower 27 of steam, the import of relief valve 25 connects heating chamber 1 by safety line 28
Top;Water is filled in tank 26;In order to avoid, lines are overlapping, drawing is chaotic, safety and environmental protection releasing device not shown in Fig. 1,
And safety line 28 is only shown.
Heat exchanger includes housing 29, and in housing 29, the length direction along housing 29 is provided with air-cooled heat exchanger tube 30, air-cooled heat exchange
Pipe 30 outer surface uniform intervals is provided with some annulus fins 31;The entrance point of air-cooled heat exchanger tube 30 connects the 4th pipeline 32, the
The outlet of four pipeline 32 connection safety valves 25;
The port of export of air-cooled heat exchanger tube 30 connects has the 5th pipeline 33, the 5th pipeline 33 to be passed through a side bottom of tank 26;Shell
Body 29 connects at air-cooled heat exchanger tube 30 entrance point has the 6th pipeline 34, the distal opening of the 6th pipeline 34 to communicate with air;
Housing 29 connects at air-cooled heat exchanger tube 30 port of export the 7th pipeline 35, the distal opening of the 7th pipeline 35 and big gas phase
Logical;The distal opening of the 6th pipeline 34 is higher than the distal opening at least 4 meters of the 7th pipeline 35;Described 7th pipeline 35 is provided with institute
State cooling blower 27.The distal opening of the 6th pipeline 34, higher than the distal opening at least 4 meters of the 7th pipeline 35, can play cold
But blower fan 27 prevents air flow shortcircuit (the 6th pipeline 34 expellant gas is sucked by cooling blower 27 again) when working
Phenomenon, it is ensured that cooling effect.Meanwhile, the distal opening position of the 6th pipeline 34 is higher, and after it also avoid heat exchange, temperature is higher
Air impact Ground Operation personnel.
Described relief valve 25 includes tubular valve body 36, and valve body 36 is provided with valve seat 37 in entrance point, and valve seat 37 center is provided with master
Pore 38, valve seat 37 the inner is provided with horn mouth 39;Some secondary gas it is provided with between sidewall and the outer face of valve seat 37 of horn mouth 39
Hole 40;
Relief valve 25 is provided with support orifice plate 41 in outlet end, and support orifice plate 41 has stage clip towards the side connection of horn mouth 39
42, stage clip 42 connects the taper valve core 43 suitable with described horn mouth 39, and taper valve core 43 is crimped on described horn mouth 39
Sidewall on, and the described each secondary pore 40 of sidewall closure of taper valve core 43;Support and be uniformly provided with multiple air-vent on orifice plate 41
44。
Multiple through hole 45 it is uniformly provided with on described annulus fin 31, so that air flows more swimmingly in housing 29,
Improve the heat exchange efficiency between air and fin, thus more effectively reduce the water in air-cooled heat exchanger tube 30 and the temperature of steam.
The invention also discloses above-mentioned boiler and prevent dryouting the method for safe operation of safety production system, enter by the following method
OK:
Including operation method when properly functioning method and accidental power failure;
Properly functioning method is to start feed pump 7 and boiler, is become by the cool water heating that feed pump 7 is sent into after hot water continuously
Deliver to use heat unit from boiler discharging tube 3;Keep burn-out-proof solid carbon dioxide case 8 and water supply tank 9 to be in the state of full water simultaneously;
Operation method during accidental power failure is:
Staff observes thermometer the 15, first Pressure gauge 23 and the second Pressure gauge 24;When thermometer 15 shows the temperature of heating chamber 1
When degree is higher than 75 degree, in heating chamber 1, existing part water is vaporized;Now opening the first valve 46, the water vapour in heating chamber 1 leads to
Cross the first pipeline 10 and be passed through burn-out-proof solid carbon dioxide case 8, make to be in identical pressure between burn-out-proof solid carbon dioxide case 8 and heating chamber 1;
By the first Pressure gauge 23 and the second Pressure gauge 24, staff confirms that burn-out-proof solid carbon dioxide case 8 is in phase between heating chamber 1
Opening the second valve 12 and atmospheric valve 14 after same pressure, the water in burn-out-proof solid carbon dioxide case 8 flows into heating chamber 1, and at burn-out-proof solid carbon dioxide
In case 8 under the effect of hydraulic pressure, the most heated water and steam in heating chamber 1 flow to heat exchanger shell by after relief valve 25
29, finally flow into tank 26;When the pressure in heating chamber 1 is higher than the unlatching pressure of relief valve 25, the pressure in relief valve 25
Spring 42 is compressed, and taper valve core 43 leaves horn mouth 39, so that steam and water in heating chamber 1 by horn mouth 39 and support
Orifice plate 41, enters the bottom of tank 26 through the 5th pipeline 33 after flowing through the air-cooled heat exchanger tube 30 of heat exchanger, steam enters water storage
Absorbed by the water in tank 26 behind pond 26, from without working environment is produced steam contamination.Pressure in heating chamber 1 is more
Height, the distance that taper valve core 43 leaves main pore 38 and secondary pore 40 is the most remote, shape between taper valve core 43 and horn mouth 39 sidewall
The current path become is the widest, and vapour lock is the least, and the water and the steam that pass through in the unit interval are the most, reaches the pressure in heating chamber 1 more
Technique effect high, that release speed is the fastest.The setting of secondary pore 40, it is possible to accelerate release speed, and strengthen in heating chamber 1
The technique effect that pressure is the highest, release speed is the fastest.
When the pressure in heating chamber 1 is less than the unlatching pressure of relief valve 25, at the elastic force effect inferior pyramidal valve of stage clip 42
Core 43 compresses horn mouth 39, the closure main pore 38 of institute and each secondary pore 40, thus closed safe valve 25;
If the most first opening the first valve 46 and directly opening the second valve 12, may cause the water in heating chamber 1 and steam because of
Pressure raises (water in boiler can vaporize because not flowing, and causes pressure to raise) and flows backwards to burn-out-proof solid carbon dioxide case 8, so will
Cause the water in burn-out-proof solid carbon dioxide case 8 cannot flow downwardly into heating chamber 1, until the water in heating chamber 1 dryouies, steam pressure is less than anti-
Dryout the hydraulic pressure of water tank 8, thus cause safety problem and steam contamination problem in the process.
In running when accidental power failure, staff persistently carries out following two operation:
1. observe thermometer 15, after thermometer 15 shows that the water temperature of heating chamber 1 is less than 50 degree, close the second valve 12;Heating
Water temperature in room 1 is gone up after more than 75 degree, reopens the second valve 12;This operation is prevented from burn-out-proof solid carbon dioxide case 8
Water too fast inflow heating chamber 1, to such an extent as to do not fully absorb the heat energy in heating chamber 1 and just spilt out by boiler discharging tube 3.This
The meaning of operation is when having a power failure that making full use of water in burn-out-proof solid carbon dioxide case 8 absorbs the ability of heat energy.
2. the liquid level in burn-out-proof solid carbon dioxide case 8 is observed by the first transparent tube 13, when in burn-out-proof solid carbon dioxide case 8, liquid level is less than burn-out-proof
Solid carbon dioxide case 8 height 1/3 time, open the 3rd valve 17 and atmospheric valve 14, make water in water supply tank 9 be injected by the 3rd pipeline 16
Burn-out-proof solid carbon dioxide case 8, burn-out-proof solid carbon dioxide case 8 fills the water in water or water supply tank 9 when using up, closes the 3rd valve 17 and atmospheric valve
14。
In operation method during accidental power failure, staff observes the pressure of the first Pressure gauge 23, when the first Pressure gauge 23
Registration more than or equal to the unlatching pressure of relief valve 25 time, open cooling blower 27, cooling blower 27 draw ambient air general
Surrounding air sends into the housing 29 of heat exchanger along the 7th pipeline 35, flows through after each annulus fin 31 through the 6th pipeline in housing 29
Flow out after 34, thus cool down rapidly the water by air-cooled heat exchanger tube 30 and steam, prevent the water temperature over-high in tank 26, steam
Overflow from tank 26 and form steam contamination.
During use, boiler discharging tube 3 connection heat unit.In heating chamber 1 during hypertonia, the steam water interface temperature of outflow
Spend higher, as by after relief valve 25 directly discharge will produce substantial amounts of steam, pollute working environment, make plant area's wall because of for a long time
Moist and impaired.In the present invention, the steam water interface flowed out from relief valve 25 sends into housing 29, by the air-cooled heat exchange of housing 29
During pipe 30, with pipe outside cooling air-flow generation heat exchange.The setting of annulus fin 31 can be greatly improved heat exchange efficiency, and because of
The flowing of cooling air is the most too much affected for the existence of through hole 45.Most of steam after heat exchange, in vaporization mixture
It is condensed into water, injects the bottom of tank 26 finally by the 5th pipeline 33.
If the 5th pipeline 33 is not passed through the bottom of tank 26, but opening is at tank 26 ullage, then
Still can flow out some vapor from the 5th pipeline 33, environment is caused a small amount of steam contamination;5th pipeline 33 is passed through tank 26
Bottom, then steam can be avoided completely to permeate into the phenomenon in air.
Above example is only in order to illustrative not limiting technical scheme, although with reference to above-described embodiment to this
Bright be described in detail, it will be understood by those within the art that: still the present invention can be modified or etc.
With replacing, any modification or partial replacement without departing from the spirit and scope of the present invention, it all should contain the power in the present invention
In the middle of profit claimed range.