CN104791840B - A kind of plant granule fuel combustion control method - Google Patents

A kind of plant granule fuel combustion control method Download PDF

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Publication number
CN104791840B
CN104791840B CN201510223822.0A CN201510223822A CN104791840B CN 104791840 B CN104791840 B CN 104791840B CN 201510223822 A CN201510223822 A CN 201510223822A CN 104791840 B CN104791840 B CN 104791840B
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gear
aerator
motor
microprocessor
temperature
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CN104791840A (en
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王新军
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Pingdu City Lin Yan Precision Machinery Factory
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Pingdu City Lin Yan Precision Machinery Factory
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Abstract

nullThe invention belongs to combustion apparatus and control technical field,Relate to a kind of plant granule fuel combustion control method,Circulating water temperature in the temperature sensor Real-time Collection arranged on water tank and transmission water tank,The reduced temperature pre-set is contrasted by microprocessor with circulating water temperature,To control motor respectively、Aerator and water pump simultaneously enter No. I gear、No. II gear or No. III gear operating,Under No. I gear, the rotating speed of driven by motor stirring cage is 100 130r/min、The rotating speed of aerator is 200 250r/min、The extraction speed of water pump is 0.3 0.5m/s,Under No. II gear, the rotating speed of driven by motor stirring cage is 70 99r/min、Blower speed is 150 200r/min、The extraction speed of water pump is 0.5 0.7m/s,Under No. III gear, the rotating speed of driven by motor stirring cage is 40 69r/min、The rotating speed of aerator is 100 150r/min、The extraction speed of water pump is 0.7 0.9m/s;The method design science, principle is simple, controls sensitive, and automaticity is high, and safety is good, and operating cost is low.

Description

A kind of plant granule fuel combustion control method
Technical field:
The invention belongs to combustion apparatus and control technical field, be specifically related to a kind of plant granule fuel combustion control method, According to the water temperature gathered, the inlet of fuel and wind-force can be automatically controlled, it is achieved the heating of energy-saving and environmental protection takes Warm effect.
Background technology:
The energy is the important substance basis that human society is depended on for existence and development, makes a general survey of the history of human social development, people The major progress each time of class civilization is all along with improvement and the replacement of the energy, and the exploitation of the energy greatly advance the world Economy and the development of human society.There is following characteristics in China's energy resources: energy resources total amount is relatively abundanter, per capita energy's money Source owning amount composes than relatively low, energy resources that to deposit skewness weighing apparatus, Energy Resources Exploitation difficulty bigger etc., along with economical quick Development energy resource consumption air especially is huge, the most seriously faces problem of energy crisis, particularly coal, oil etc. non-renewable Resource is the most in short supply, how to improve the significant problem that utilization of energy situation has become extremely urgent.There is the title of green energy resource Bioenergy, be not only different from the fossil energy of routine, but also be different from other new forms of energy, its feature having both concurrently and advantage, It it is one of topmost regenerative resource of the mankind;Bioenergy specifically refers to by biological activity, by biomass, water or other Inorganic matter is converted into the fuel gas such as biogas, hydrogen or ethanol, oils flammable liquid is the regenerative resource of carrier, and it is Big feature is to burn or do not cause environmental pollution after use, is conducive to maintaining ecological balance.
At present, relatively conventional bioenergy utilization means are mainly " burning ", miscellaneous biomass in prior art Combustor or biomass burner are broadly divided into air-cooled biomass combustion machine and water-cooled biomass combustion machine two types, all It is after scientific disposal, to recompress the biological particles made as fuel with raw materials such as waste wood and crops Radix Platycodonis waste materials, enters Row directly burning is to obtain biomass energy;Such as Chinese patent 201420675364.5,201420675124.5 and A kind of biomass dye vapour boiler disclosed in 201420674584.6, a kind of raw disclosed in Chinese patent 201420667752.9 Material thermal dye medium boiler, a kind of mixed biology matter burner etc. disclosed in Chinese patent 201420483726.0, all It is to utilize heat energy by biomass burning raw material, but the automaticity of the said equipment is the most relatively low, it is impossible to according to actual need The regulation of heat dissipation capacity to be carried out, still there is a large amount of fuel is waste combustion problem, research design one plant the most of the present invention Granular fuel method for controlling combustion, according to the entrance of the water temperature gathered admission velocity and wind-force to automatically control fuel Amount, thus realize efficient, energy-saving and environmental protection, automatic heat supply and heating.
Summary of the invention:
It is an object of the invention to the shortcoming overcoming prior art to exist, seeking design provides a kind of plant granule fuel combustion Burn control method, it is possible to according to the temperature of the circulating water body collected, automatically control the inlet of fuel and the entrance of wind-force Amount, it is to avoid cross the waste of multi fuel.
To achieve these goals, the plant granule fuel combustion control method that the present invention relates to specifically includes following technique Step:
(1) water temperature collection and contrast: the microprocessor that the temperature sensor arranged on water tank is built-in with control chamber Electrical information connects, circulating water temperature in Real-time Collection and transmission water tank, is previously provided with and includes 20-50 in microprocessor DEG C, 51-70 DEG C and the reduced temperature of 71-90 DEG C, after microprocessor receives the circulating water temperature that temperature sensor is transmitted in real time Carry out contrast with the reduced temperature pre-set to compare, with control respectively motor enter No. I gear of motor, No. II gear of motor or No. III gear operating of motor;Aerator enters No. I gear of aerator, No. II gear of aerator or No. III gear fortune of aerator simultaneously Turn
(2) fuel inlet controls: microprocessor controls motor according to the comparing result of circulating water temperature with reduced temperature Entering No. I gear of motor, No. II gear of motor or No. III gear operating of motor, motor connects driving stirring cage and rotates so that by hopper In the fuel that leaks down in combustion furnace sent into by feed well, under No. I gear of motor, the rotating speed of driven by motor stirring cage is 100-130r/ Min, under No. II gear of motor, the rotating speed of driven by motor stirring cage is 70-99r/min, driven by motor stirring cage under No. III gear of motor Rotating speed is 40-69r/min;
(3) wind-force inlet controls: microprocessor regulates drum according to the comparing result of circulating water temperature with reduced temperature Blower fan little to TV university, enters No. I gear of aerator, No. II gear of aerator or No. III gear fortune of aerator controlling aerator Turning, under No. I gear of aerator, the rotating speed of aerator is 200-250r/min, and under No. II gear of aerator, blower speed is 150- 200r/min, under No. III gear of aerator, the rotating speed of aerator is 100-150r/min;
(4) water circulation speed controlling: motor and aerator respectively enter No. I gear of motor, No. II gear of motor simultaneously Or when No. III gear of motor and No. I gear of aerator, No. II gear of aerator or No. III gear of aerator, microprocessor is by control The water pump that water inlet processed is laid is to control injection and the velocity of discharge, No. I gear of motor and the aerator I of recirculated water in water tank Under gear, the extraction speed of water pump is 0.3-0.5m/s, the extraction speed of water pump under No. II gear of motor and No. II gear of aerator It is 0.7-0.9m/s for the extraction speed of water pump under 0.5-0.7m/s, No. III gear of motor and No. III gear of aerator.
Further, described step compares in (1) by contrast, if circulating water temperature is in the range of reduced temperature 20-50 DEG C, Then microprocessor controls motor and aerator respectively enters No. I gear of motor and No. I gear of aerator runs up;If recirculated water Temperature in the range of reduced temperature 51-70 DEG C, then microprocessor control motor and aerator respectively enter No. II gear of motor and No. II gear middling speed operating of aerator;If circulating water temperature is in the range of reduced temperature 71-90 DEG C, then microprocessor controls motor No. III gear of motor and No. III gear low-speed running of aerator is respectively enterd with aerator.
The agent structure of the device realizing plant granule fuel combustion control method in the present invention includes mainframe box, water inlet Mouth, outlet, water tank, combustion furnace, chimney, hopper, stirring cage, motor, aerator, Dust Storage Room, control chamber, display floater, fire door, Water pump, cover plate, feed well, sensor and microprocessor, in the inner chamber of the mainframe box of hollow type body structure, a side bottom is fixed Being provided with combustion furnace, the outside jacket formula of combustion furnace is provided with the junction of the water tank of temperature sensor, water tank and mainframe box Block form offers water inlet and the outlet of tubular structure up and down, and water inlet is provided with the water pump electrically connected with control chamber, Being arranged in the control chamber on mainframe box wall body and be provided with microprocessor and integral control circuit, the positive side of control chamber is provided with Display floater, for display circulating water body temperature, intake velocity and charging rate in real time;Offer on the rear side wall body of mainframe box It is used for discharging flue dust with the chimney of combustion furnace pipeline communication, is docked by feed well between combustion furnace with stirring cage, helical form pillar The stirring cage of structure is realized driving by motor electrical connection, and the operating of motor is controlled to adjust by microprocessor in control chamber, and stirring cage is just Top jacket formula is provided with the hopper of funnel-shaped structure for adding fuel, the fuel that hopper leaks down by the rotation of stirring cage through entering Hopper enters in combustion furnace, hopper is equipped with and is provided with cover plate in order to seal;The lower end of combustion furnace seals with aerator and docks, drum The operating of blower fan is controlled to adjust by microprocessor in control chamber, and the bottom of combustion furnace is equipped with the sealed Dust Storage Room of drawing structure Dust after collecting burning, the position of mainframe box correspondence combustion furnace offers locking-type fire door with handles, is used for looking into See and/or clear up combustion furnace.
Preferably, display floater being provided with water temperature display meter, wind speed display and fuel and enters speed display, water temperature shows Count and connect the temperature sensor in water tank by microprocessor electrical information, for the temperature of display circulating water body in real time;Wind speed shows Show that device passes through microprocessor electrical information and connects aerator, for real-time Display Drum blower fan rotating speed under different gears;Fuel enters Speed display connects motor by microprocessor electrical information, for the rotating speed of stirring cage under different gears of display motor in real time.
Compared with prior art, microprocessor built-in in clearance control chamber and control circuit realize setting entirety the present invention Standby Automated condtrol, the temperature automatic adjustment of the circulating water body transmitted in real time according to the sensor on water tank controls motor and drum The rotating speed of blower fan, thus realize under different heating demand fuel and the control of intake, it is achieved more efficient energy-conservation, ring Protect;The method design science, principle is simple, controls sensitive, and automaticity is high, and safety is good, and operating cost is low.
Accompanying drawing illustrates:
Fig. 1 is the flow process schematic block diagram of the control method that the present invention relates to.
Fig. 2 is the agent structure principle schematic of the plant granule fuel burner that the present invention relates to.
Fig. 3 is the outward appearance front view of the plant granule fuel burner that the present invention relates to.
Detailed description of the invention:
Below in conjunction with the accompanying drawings and by embodiment the present invention made further description, but the present invention is not limited in Implementation below.
Embodiment:
The plant granule fuel combustion control method that the present embodiment relates to specifically includes following processing step:
(1) water temperature collection and contrast: micro-place built-in in the temperature sensor 18 arranged on water tank 4 and control chamber 12 Reason device 19 electrical information connects, circulating water temperature in Real-time Collection and transmission water tank 4, is previously provided with bag in microprocessor 19 Including the reduced temperature of 20-50 DEG C, 51-70 DEG C and 71-90 DEG C, what microprocessor 19 received that temperature sensor 18 transmits in real time follows Carry out contrast with the reduced temperature pre-set after ring coolant-temperature gage to compare, enter motor No. I gear, electricity controlling motor 9 respectively No. II gear of machine or No. III gear operating of motor, aerator 10 enters No. I gear of aerator, No. II gear of aerator or drum simultaneously No. III gear operating of blower fan;
(2) fuel inlet controls: microprocessor 19 controls electricity according to the comparing result of circulating water temperature with reduced temperature Machine 9 enters No. I gear of motor, No. II gear of motor or the operating of No. III gear of motor, motor 9 connect drive stirring cage 8 to rotate so that By the fuel leaked down in hopper 7 in combustion furnace 5 sent into by feed well 17, under No. I gear of motor, motor 9 drives the rotating speed of stirring cage 8 For 100-130r/min, under No. II gear of motor, motor 9 drives the rotating speed of stirring cage 8 to be 70-99r/min, under No. III gear of motor Motor 9 drives the rotating speed of stirring cage 8 to be 40-69r/min;
(3) wind-force inlet controls: microprocessor 19 is right with the regulation of the comparing result of reduced temperature according to circulating water temperature Aerator 10 little to TV university, enters No. I gear of aerator, No. II gear of aerator or aerator III controlling aerator 10 Gear operates, and under No. I gear of aerator, the rotating speed of aerator 10 is 200-250r/min, aerator 10 under No. II gear of aerator Rotating speed is 150-200r/min, and under No. III gear of aerator, the rotating speed of aerator 10 is 100-150r/min;
(4) water circulation speed controlling: motor 9 and aerator 10 respectively enter No. I gear of motor, No. II shelves of motor simultaneously When position or No. III gear of motor and No. I gear of aerator, No. II gear of aerator or No. III gear of aerator, microprocessor 19 leads to Cross the water pump 15 controlling to lay at water inlet 2 to control injection and the velocity of discharge of recirculated water in water tank 4, No. I gear of motor and Under No. I gear of aerator, the extraction speed of water pump 15 is 0.3-0.5m/s, water under No. II gear of motor and No. II gear of aerator The extraction speed of pump 15 is 0.5-0.7m/s, and under No. III gear of motor and No. III gear of aerator, the extraction speed of water pump 15 is 0.7-0.9m/s。
The step (1) related in the present embodiment compares by contrast, if circulating water temperature is in reduced temperature 20-50 DEG C scope In, then microprocessor 19 controls motor 9 and aerator 10 respectively enters No. I gear of motor and No. I gear of aerator runs up; If circulating water temperature is in the range of reduced temperature 51-70 DEG C, then microprocessor 19 controls motor 9 and aerator 10 respectively enters electricity No. II gear of machine and No. II gear middling speed operating of aerator;If circulating water temperature is in the range of reduced temperature 71-90 DEG C, the most micro-place Reason device 19 controls motor 9 and aerator 10 respectively enters No. III gear of motor and No. III gear low-speed running of aerator.
The plant granule fuel combustion control method that the present embodiment relates to is specifically real in plant granule fuel burner Existing, described plant granule fuel burner agent structure include mainframe box 1, water inlet 2, outlet 3, water tank 4, combustion furnace 5, Chimney 6, hopper 7, stirring cage 8, motor 9, aerator 10, Dust Storage Room 11, control chamber 12, display floater 13, fire door 14, water pump 15, Cover plate 16, feed well 17, sensor 18 and microprocessor 19, a side bottom in the inner chamber of the mainframe box 1 of hollow type body structure Being installed with combustion furnace 5, the outside jacket formula of combustion furnace 5 is provided with the water tank 4 of temperature sensor 18, water tank 4 and main frame The upper and lower block form in junction of case 1 offers water inlet 2 and the outlet 3 of tubular structure, is provided with and control chamber at water inlet 2 The water pump 15 of 12 electrical connections, is arranged in the control chamber 12 on mainframe box 1 wall body and is provided with microprocessor 19 and integrating control electricity Road, the positive side of control chamber 12 is provided with display floater 13, for display circulating water body temperature in real time, intake velocity and charging speed Degree;Offer the chimney 6 with combustion furnace 5 pipeline communication on the rear side wall body of mainframe box 1 for discharging flue dust, combustion furnace 5 with stir Being docked by feed well 17 between cage 8, the stirring cage 8 of helical form pole structure is electrically connected realization by motor 9 and drives, the fortune of motor 9 Turning and controlled to adjust by microprocessor 19 in control chamber 12, the surface jacket formula of stirring cage 8 is provided with the hopper 7 of funnel-shaped structure and uses In adding fuel, the fuel that hopper 7 leaks down, in feed well 17 enters combustion furnace 5 hopper 7 is equipped with by the rotation of stirring cage 8 Cover plate 16 is installed in order to seal;The lower end of combustion furnace 5 seals with aerator 10 and docks, and the operating of aerator 10 is by control chamber 12 Middle microprocessor 19 controls to adjust, and the bottom of combustion furnace 5 is used for collecting burning equipped with the sealed Dust Storage Room 11 of drawing structure After dust, the position of the corresponding combustion furnace 5 of mainframe box 1 offers locking-type fire door 14 with handles, is used for checking and/or clearly Reason combustion furnace 5;When this plant granule fuel burner uses, chimney 6 is installed and pick out outdoor, in hopper 7, add plant Grain fuel, then plug in control chamber 12 to electricity.
It is provided with water temperature display meter 20, wind speed display 21 and fuel on the display floater 13 related in the present embodiment and enters speed Display 22, water temperature display meter 20 connects the temperature sensor 18 in water tank 4 by microprocessor 19 electrical information, for the most aobvious Show the temperature of circulating water body;Wind speed display 21 connects aerator 10 by microprocessor 19 electrical information, for real-time Display Drum The blower fan 10 rotating speed under different gears;Fuel enters speed display 22 and connects motor 9 by microprocessor 19 electrical information, for real Time show motor 9 rotating speed of stirring cage 8 under different gears.

Claims (4)

1. a plant granule fuel combustion control method, it is characterised in that specifically include following processing step:
(1) water temperature collection and contrast: the microprocessor telecommunications that the temperature sensor arranged on water tank is built-in with control chamber Breath connects, circulating water temperature in Real-time Collection and transmission water tank, is previously provided with and includes 20-50 DEG C, 51-in microprocessor The reduced temperatures of 70 DEG C and 71-90 DEG C, microprocessor receives after the circulating water temperature that temperature sensor is transmitted in real time with in advance The reduced temperature arranged carries out contrast and compares, to control motor entrance No. I gear of motor, No. II gear of motor or motor III respectively The operating of number gear, aerator enters No. I gear of aerator, No. II gear of aerator or No. III gear operating of aerator simultaneously;
(2) fuel inlet controls: microprocessor controls motor according to the comparing result of circulating water temperature with reduced temperature and enters No. I gear of motor, No. II gear of motor or No. III gear operating of motor, motor connects driving stirring cage and rotates will to leak in hopper Under fuel send in combustion furnace through feed well, under No. I gear of motor, the rotating speed of driven by motor stirring cage is 100-130r/min, electricity Under No. II gear of machine, the rotating speed of driven by motor stirring cage is 70-99r/min, and under No. III gear of motor, the rotating speed of driven by motor stirring cage is 40-69r/min;
(3) wind-force inlet controls: microprocessor regulates aerator according to the comparing result of circulating water temperature with reduced temperature Little to TV university, enter No. I gear of aerator, No. II gear of aerator or the operating of No. III gear of aerator controlling aerator, Under No. I gear of aerator, the rotating speed of aerator is 200-250r/min, and under No. II gear of aerator, blower speed is 150- 200r/min, under No. III gear of aerator, the rotating speed of aerator is 100-150r/min;
(4) water circulation speed controlling: motor and aerator respectively enter No. I gear of motor, No. II gear of motor or electricity simultaneously When No. III gear of machine and No. I gear of aerator, No. II gear of aerator or No. III gear of aerator, microprocessor is entered by control The water pump laid at the mouth of a river is to control injection and the velocity of discharge, No. I gear of motor and No. I gear of aerator of recirculated water in water tank The extraction speed of lower water pump is 0.3-0.5m/s, and under No. II gear of motor and No. II gear of aerator, the extraction speed of water pump is 0.5-0.7m/s, under motor No. III gear of No. III gear aerator, the extraction speed of water pump is 0.7-0.9m/s.
Plant granule fuel combustion control method the most according to claim 1, it is characterised in that in step (1) by contrast than Relatively, if circulating water temperature is in the range of reduced temperature 20-50 DEG C, then microprocessor controls motor and aerator respectively enters motor No. I gear and No. I gear of aerator run up;If circulating water temperature is in the range of reduced temperature 51-70 DEG C, then microprocessor Control motor and aerator respectively enters No. II gear of motor and No. II gear middling speed operating of aerator;If circulating water temperature is right In the range of temperature 71-90 DEG C, then microprocessor controls motor and aerator respectively enters No. III gear of motor and aerator III Number gear low-speed running.
Plant granule fuel combustion control method the most according to claim 1, it is characterised in that the plant granule combustion related to Material burner agent structure include mainframe box, water inlet, outlet, water tank, combustion furnace, chimney, hopper, stirring cage, motor, Aerator, Dust Storage Room, control chamber, display floater, fire door, water pump, cover plate, feed well, sensor and microprocessor, hollow type case In the inner chamber of the mainframe box of body structure, a side bottom is installed with combustion furnace, and the outside jacket formula of combustion furnace is provided with temperature The upper and lower block form in junction of the water tank of sensor, water tank and mainframe box offers water inlet and the outlet of tubular structure, enters Be provided with the water pump electrically connected with control chamber at the mouth of a river, be arranged in the control chamber on mainframe box wall body be provided with microprocessor and Integral control circuit, the positive side of control chamber is provided with display floater, in real time display circulating water body temperature, intake velocity and Charging rate;Offer the chimney with combustion furnace pipeline communication on the rear side wall body of mainframe box for discharging flue dust, combustion furnace with Docked by feed well between stirring cage, the stirring cage of helical form pole structure by motor electrical connection realize drive, the operating of motor by Microprocessor control and regulation in control chamber, the surface jacket formula of stirring cage is provided with the hopper of funnel-shaped structure for adding combustion Material, the fuel that hopper leaks down by the rotation of stirring cage in feed well enters combustion furnace, hopper is equipped be provided with cover plate in order to Seal;The lower end of combustion furnace seals with aerator and docks, and the operating of aerator is controlled to adjust by microprocessor in control chamber, burning The bottom of stove is used for the dust after collecting burning, the position of mainframe box correspondence combustion furnace equipped with the sealed Dust Storage Room of drawing structure The place of putting offers locking-type fire door with handles, is used for checking and/or clearing up combustion furnace.
Plant granule fuel combustion control method the most according to claim 1, it is characterised in that be provided with on display floater Water temperature display meter, wind speed display and fuel enter speed display, and water temperature display meter is connected in water tank by microprocessor electrical information Temperature sensor, in real time showing the temperature of circulating water body;Wind speed display connects air blast by microprocessor electrical information Machine, for real-time Display Drum blower fan rotating speed under different gears;Fuel is entered speed display and is connected by microprocessor electrical information Motor, for the rotating speed of stirring cage under different gears of display motor in real time.
CN201510223822.0A 2015-05-05 2015-05-05 A kind of plant granule fuel combustion control method Active CN104791840B (en)

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Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101576271A (en) * 2009-06-10 2009-11-11 王义红 Automatic biological material combusting multipurpose furnace
CN101725999A (en) * 2009-12-11 2010-06-09 中国电力科学研究院 Method for controlling load of biomass vibration grate boiler
JP2011064402A (en) * 2009-09-17 2011-03-31 Hanshin Electric Co Ltd Method of controlling combustion of combustion device
KR101261150B1 (en) * 2011-07-28 2013-05-06 린나이코리아 주식회사 Method for controlling heated water supply in hot-water supply device
CN104214826A (en) * 2014-09-25 2014-12-17 无锡昊瑜节能环保设备有限公司 Energy-saving control system for mini-boiler
CN204240403U (en) * 2014-11-06 2015-04-01 胥洪武 Efficient biomass boiler control system

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101576271A (en) * 2009-06-10 2009-11-11 王义红 Automatic biological material combusting multipurpose furnace
JP2011064402A (en) * 2009-09-17 2011-03-31 Hanshin Electric Co Ltd Method of controlling combustion of combustion device
CN101725999A (en) * 2009-12-11 2010-06-09 中国电力科学研究院 Method for controlling load of biomass vibration grate boiler
KR101261150B1 (en) * 2011-07-28 2013-05-06 린나이코리아 주식회사 Method for controlling heated water supply in hot-water supply device
CN104214826A (en) * 2014-09-25 2014-12-17 无锡昊瑜节能环保设备有限公司 Energy-saving control system for mini-boiler
CN204240403U (en) * 2014-11-06 2015-04-01 胥洪武 Efficient biomass boiler control system

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