CN101886874A - Automatic constant temperature drying and automatic regulation material flow control device of light energy vertical dryer - Google Patents
Automatic constant temperature drying and automatic regulation material flow control device of light energy vertical dryer Download PDFInfo
- Publication number
- CN101886874A CN101886874A CN2009101172752A CN200910117275A CN101886874A CN 101886874 A CN101886874 A CN 101886874A CN 2009101172752 A CN2009101172752 A CN 2009101172752A CN 200910117275 A CN200910117275 A CN 200910117275A CN 101886874 A CN101886874 A CN 101886874A
- Authority
- CN
- China
- Prior art keywords
- control device
- adaptation module
- links
- vertical dryer
- automatic
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
Images
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E10/00—Energy generation through renewable energy sources
- Y02E10/40—Solar thermal energy, e.g. solar towers
- Y02E10/44—Heat exchange systems
Landscapes
- Drying Of Solid Materials (AREA)
Abstract
The invention discloses an automatic constant temperature drying and automatic regulation material flow control device of a light energy vertical dryer, aiming to solve the problems of environmental pollution caused by a great deal of harmful gas and dusts generated by drying the materials by the traditional vertical dryer through adopting a coal extracted heat in the production process and poor system automation degree in the control system of the traditional vertical dryer. The automatic constant temperature drying and automatic regulation material flow control device comprises a standard control device, an industrial control computer, a solar heat exchanger, a vertical dryer, an automatic constant temperature drying control device and a vertical dryer control device, wherein the standard control device is connected with the industrial control computer through a standard serial communication interface and is respectively connected with the solar heat exchanger and the vertical dryer, and the solar heat exchanger is connected with the vertical dryer. The invention has the advantages of simpleness, smooth flow and high automation degree, carries out automatic control by the industrial control computer, replaces fuel coals to dry the materials, improves the production efficiency and achieves the purposes of energy saving and emission reduction.
Description
Technical field
The present invention relates to a kind of material be carried out constant temperature drying and automatic and dried by the fire the control device of mass flow size according to the humidity regulation of material automatically.
Background technology
Along with the quickening of rapid economy development and process of industrialization, energy demand constantly increases, and China has become second production of energy state and the country of consumption in the world.But on the whole, China's high-grade energy relative deficiency, energy-consuming are based on coal, and resource and environmental pressure are big, and energy supply system is faced with significant challenge.Along with the back arriving of petroleum times, the basic outlet that solves China energy problem will change the economic development mode exactly, taps a new source of energy energetically and regenerative resource.We also are in the industrialization development initial stage, and industrial system is to rely on the high flow rate of conventional energy resource is realized that energy-saving and emission-reduction, environmental protection pressure are on the rise.Accelerate local regenerative resource development and use, walk the low-carbon (LC) path to economic development, the novel energy industrial structure of the diversification that construct fossil energy and regenerative resource balanced development, complements one another, fundamentally alleviate the pressure of economic growth to conventional energy resource resource and environment, alleviate the contradiction between resource and development and the environment, be to change the economic development mode, realize the sustainable development of socio-economy and the important selection of building a well-off society in an all-round way.
Traditional vertical dryer is to adopt the coal-fired caloric value of extracting that material is dried, and produces a large amount of pernicious gas NO
x, SO
2, CO, CO
2Deng and dust, contaminated environment; The more important thing is the energy " coal " that waste is non-renewable, its drying efficiency is low, and the pernicious gas of generation is big to equipment corrosion, causes the certain economic loss to manufacturer.
Because the pyrogen of traditional vertical dryer from medium-sized coal stove, is manually to burn stove in process of production mostly, operative employee's labour intensity is big, the equipment failure rate height of the low and coal stove of automaticity, and this mode of production can not adapt to the needs of present industry.
Only mention dryer system in the automatic control device of existing tower drier and comprised tower drier, Programmable Logic Controller, frequency converter, electricity shake machine, elevator, switch motor, temperature measurer, moisture apparatus, warning device, utilize the artificial stove that burns, undertaken the temperature bound is reported to the police by temperature measurer, by manually temperature being controlled, by Humidity Detection application switch motor material is returned oven dry and reach the oven dry purpose.
Summary of the invention
The purpose of this invention is to provide a kind of light energy vertical dryer automatic constant temperature drying and automatic regulation material flow control device, adopt the coal-fired heat that extracts material is dried to produce a large amount of pernicious gases in process of production and dust pollutes and have now the not high problem of vertical dryer control system automaticity to environment to solve existing vertical dryer.
The present invention includes standard control device, industrial computer, solar energy heat exchanger, vertical dryer, constant temperature drying and automatic control device, vertical dryer control device, standard control device links to each other with industrial computer by the standard serial communication interface, standard control device links to each other with solar energy heat exchanger and vertical dryer respectively, and solar energy heat exchanger links to each other with vertical dryer.
Described solar energy heat exchanger has temperature sensor No. one, flow transmitter, air intake valve and wind pipe, wind pipe is provided with the pipeline frequency conversion fan, described constant temperature drying and automatic control device comprises that being located at first on the described standard control device measures adaptation module, second measures adaptation module, the first control adaptation module, the second control adaptation module, first measures adaptation module links to each other with a described temperature sensor, second measures adaptation module links to each other with described flow transmitter, the first control adaptation module links to each other with described air intake valve, and the second control adaptation module links to each other with described pipeline frequency conversion fan.
Solar energy heat exchanger comprises that column type heat absorption vacuum tube, thermal-arrest change air compartment, air intake resistance dividing plate, pipeline heat collector, heat absorption cover plate, described air intake resistance dividing plate and pipeline heat collector are installed in thermal-arrest and change air compartment inside, the heat absorption cover plate is fixed on thermal-arrest and changes the air compartment top, and column type heat absorption vacuum tube is fixed on thermal-arrest and changes on air compartment and the heat absorption cover plate.
Described vertical dryer control device comprises that being located at the 3rd on the described standard control device controls adaptation module, the 4th control adaptation module, the 5th control adaptation module, the 3rd measures adaptation module, described vertical dryer top is provided with dedust air duct, dedust air duct is provided with temperature sensor No. two, dedust air duct links to each other with deduster, the deduster bottom is provided with motor, deduster links to each other with the dedusting fan motor, the vertical dryer bottom is provided with the remittance air compartment, the charging elevator is provided with the elevator motor, the 3rd control adaptation module links to each other with the elevator motor, the 4th control adaptation module links to each other with the dedusting fan motor, the 5th control adaptation module links to each other with motor, and the 3rd measures adaptation module links to each other with No. two temperature sensors.Described vertical dryer sidepiece is provided with the secondary hot-air pipe.
The present invention also comprises automatic adjusting material flow control device, automatically regulate material flow control device and comprise that being located at the 4th on the described standard control device measures adaptation module and the 6th control adaptation module, described vertical dryer is provided with moisture detection sensor and material adjuster, the 4th measures adaptation module links to each other with moisture detection sensor, and the 6th control adaptation module links to each other with the material adjuster.
Described material adjuster comprises regulates motor, power transmission shaft, power transmission shaft pillar, turbine box, elevating lever, cone governor, balance chain, spreading awl, sliding material basin awl, support, described adjusting motor is fixed on the support, regulating motor links to each other with turbine box by power transmission shaft, turbine box is fixed on the spreading awl, regulate motor and be provided with the power transmission shaft pillar outward, the two ends of power transmission shaft pillar are separately fixed to be regulated on motor and the turbine box, turbine box links to each other with cone governor by elevating lever, cone governor links to each other with the balance chain, and the balance chain is fixed on the sliding material basin awl.
The present invention has improved the automatization level of vertical dryer, adopt the control adaptation module and measure the course of work that adaptation module is controlled each equipment, the energy that utilizes luminous energy to produce becomes hot-air by heat exchanger and enters vertical dryer material is carried out constant temperature drying and automatic and dried by the fire the control device of mass flow size according to the humidity regulation of material automatically.
The heat converting to hot air that the present invention adopts the column type solar energy heat exchanger to produce, deliver to the remittance air compartment by pipeline fan, hot blast is bottom-up from the bottom of vertical dryer under the effect of deduster slowly evenly to flow, this moment, material was sent into the top of vertical dryer by the charging elevator, material is evenly landing formation and hot blast exchange from top to bottom, reach the purpose that automatic oven dry material substitution fire coal is dried material, the present invention is simple, flow process is smooth and easy, automaticity is high, has the advantage of energy savings.
Gansu Province's solar energy resources is very abundant, and the whole province's solar energy year total radiation is at 4800～6400MJ/m
2Between.Wherein Hexi Corridor and Gannan Plateau are the abundantest area of solar energy resources, Gansu Province, and a year total solar radiation amount is respectively 5800～6400MJ/m
2With 5800～6200MJ/m
2The Longnan Prefecture is relatively poorer, and a year total solar radiation amount only is 4800～5200MJ/m
2All the other areas are 5200～5800MJ/m
2, except that the Longnan Prefecture.
Gansu Province's sun sunshine time reduces gradually from the north-westward southeast between 1700～3300h.The maximum area of year sunshine time is western part, Hexi Corridor, more than 3200h; Minimum area is the south of Gansu Province south, below 1800h; All the other areas are between 2000～3000h.Each season of sunshine time distributes irregular.Summer is maximum, and winter is minimum, and spring is greater than autumn.Summer (July), the whole province was between 170～320h; Be 120～230h winter (January); Be 130～280h spring (April); Be 110～280h autumn.
The present patent application people location is in the middle part, Hexi Corridor, and 5,280,000 square metres of floor spaces are the desert Gobi desert, has the good condition that solar energy development utilizes.Be calculated as follows for example:
(1) Q=CM Δ tQ: the heat C of absorption: specific heat capacity 4.2 * 103J/ (kg ℃) Δ t: temperature rise M: absorption area,
(2) A=mCp Δ T/Iy1 (1-y2) A: collector area m: water (hot water that needed in one day) Cp: specific heat (1Kg water improves the heat that was once needing)=4.187Kj/Kg ℃ I: the average exposure intensity Mj/m of the sun
2Y1: the efficient of heat collector (50%-55%) y2: the heat waste of system (10%-15%) is annotated: the evenly heat exposure intensity in Changzhou is 18-19Mj/m
2D (spring and autumn),
(3) for example: heat A=mCp Δ T/Iy1 (1-y2) Δ T=18 * 103Kj/m that the heat collector of 2 square meters absorbed in a day
2* 0.5 * 0.9/100kg * 4.187Kj/Kg ℃=19.34Q=CM Δ t * 100kg=4.2KJ/ (kg ℃) * 2m
2* 38.68 ℃ * 100kg=3249.12KJ
=4.182 joules on (4) 1 cards
Every square metre absorbs calorie value and is: A=1 * 4.187 * 6200 * 0.85=22065KJ, raw coal 20934 kilojoule/kilograms are equivalent to the caloric value of 1 kilogram of coal.Adopt light energy vertical dryer that material is dried and to save 6851.8 tons in raw coal every year.
Description of drawings
Fig. 1 is a structural representation of the present invention.
Fig. 2 is the control flow schematic diagram of column type solar energy heat exchanger of the present invention.
Fig. 3 is the structural representation of column type solar energy heat exchanger of the present invention.
Fig. 4 is the control flow schematic diagram of vertical dryer of the present invention.
Fig. 5 is the structural representation of material adjuster of the present invention.
The specific embodiment
The following examples can make those skilled in the art more fully understand light energy vertical dryer to constant temperature drying and automatic control device and automatic process characteristic and control procedure of regulating mass flow.
The present invention includes standard control device 2, industrial computer 1, solar energy heat exchanger 3, vertical dryer 4, constant temperature drying and automatic control device, vertical dryer control device, standard control device 2 links to each other with industrial computer 1 by the standard serial communication interface, standard control device 2 links to each other with solar energy heat exchanger 3 and vertical dryer 4 respectively, and solar energy heat exchanger 3 links to each other with vertical dryer 4.
Fig. 2 shows the control flow schematic diagram of invention column type solar energy heat exchanger.
Column type solar energy heat exchanger 3 has temperature sensor 15 No. one, flow transmitter 18, air intake valve 14 and wind pipe 16, wind pipe 16 is provided with pipeline frequency conversion fan 17, described constant temperature drying and automatic control device comprises that being located at first on the described standard control device 2 measures adaptation module A5, second measures adaptation module A7, the first control adaptation module A6, the second control adaptation module A8, first measures adaptation module A5 links to each other with a described temperature sensor 15, second measures adaptation module A7 links to each other with described flow transmitter 18, the first control adaptation module A6 links to each other with described air intake valve 14, and the second control adaptation module A8 links to each other with described pipeline frequency conversion fan 17.
Fig. 3 shows the structural representation of column type solar energy heat exchanger of the present invention, having summarized the basic structure of column type solar energy forms, solar energy heat exchanger 3 comprises that column type heat absorption vacuum tube T1, thermal-arrest change air compartment T2, air intake resistance dividing plate T3, pipeline heat collector T4, heat absorption cover plate T5, described air intake resistance dividing plate T3 and pipeline heat collector T4 are installed in thermal-arrest and change air compartment T2 inside, heat absorption cover plate T5 is fixed on thermal-arrest and changes air compartment T2 top, and column type heat absorption vacuum tube T1 is fixed on thermal-arrest and changes on air compartment T2 and the heat absorption cover plate T5.
The thermal-arrest principle is as follows: sunshine direct projection column type heat absorption vacuum tube T1, column type heat absorption vacuum tube T1 sends the heat that absorbs among the pipeline heat collector T4 to, changing air compartment T2 by thermal-arrest carries out heat and stores heat that the top board T5 that absorbs heat simultaneously also absorbs secondary and directly pass to thermal-arrest and change in the air compartment T2, because under the effect of air intake valve 14 and air intake resistance dividing plate T3, pipeline frequency conversion fan 17 changes the slow suction thermal-arrest of outdoor air among the air compartment T2 and exchanges the generation thermal current with pipeline heat collector T4.
Fig. 4 shows the control flow schematic diagram of vertical dryer of the present invention.
The vertical dryer control device comprises that being located at the 3rd on the described standard control device 2 controls adaptation module A1, the 4th control adaptation module A3, the 5th control adaptation module A4, the 3rd measures adaptation module A2, described vertical dryer 4 tops are provided with dedust air duct 13, dedust air duct 13 is provided with temperature sensor 10 No. two, dedust air duct 13 links to each other with deduster 5, deduster 5 bottoms are provided with motor 12, deduster 5 links to each other with dedusting fan motor 11, vertical dryer 4 bottoms are provided with remittance air compartment 19, charging elevator 6 is provided with elevator motor 7, the 3rd control adaptation module A1 links to each other with elevator motor 7, the 4th control adaptation module A3 links to each other with dedusting fan motor 11, the 5th control adaptation module A4 links to each other with motor 12, and the 3rd measures adaptation module A2 links to each other with No. two temperature sensors 10.Vertical dryer 4 sidepieces are provided with secondary hot-air pipe 20.
The present invention also comprises automatic adjusting material flow control device, automatically regulate material flow control device and comprise that being located at the 4th on the described standard control device 2 measures adaptation module A10 and the 6th control adaptation module A9, described vertical dryer 4 is provided with moisture detection sensor 8 and material adjuster 9, the 4th measures adaptation module A10 links to each other with moisture detection sensor 8, and the 6th control adaptation module A9 links to each other with material adjuster 9.
Introduce below and adopt the control adaptation module and measure the course of work that adaptation module is controlled each equipment.
Among the present invention, 1 pair of whole device of the industrial computer that use can have is controlled, and its control is divided into two parts, and first is the control of light energy vertical dryer constant temperature drying and automatic material.Second portion is the flow-control of being dried by the fire material according to humidity regulation automatically.They all use the form of image data feedback scan.
It is as follows that the present invention sends the hot blast operation principle:
Be through column type solar energy heat exchanger 3 among the present invention, thermal power transfer is become hot-air to be stored, when the stored air temperature reaches temperature sensor 15 setting values, standard control device 2 according to the address that receives select that the signal value gating links to each other with temperature sensor 15 first measure the address gating signal gating of adaptation module A5 after, the first measurement adaptation module A5 sends the temperature signal that records in the industrial computer 1 back to after A/D (modular converter) conversion.Industrial computer 1 compares according to the given data of internal temperature, when temperature greater than when setting value, send current controling signal and to the second control adaptation module A8 pipeline frequency conversion fan 17 is carried out speed regulating control, the electric current that speed is set along with temperature changes and changes.Industrial computer 1 sends a count signal and is transferred to standard control device 2 in 17 operations of pipeline frequency conversion fan, standard control device 2 with gating link to each other with flow transmitter 18 second measure the address gating signal gating of adaptation module A7 after, second measures adaptation module A7 sends the hot gas flow signal that records in the industrial computer 1 back to after A/D (modular converter) conversion.Industrial computer 1 compares according to the given data of inner stream flow, when flow greater than when setting value, send a simulation control current signal and to the first control adaptation module A6 valve opening of air intake valve 14 is automatically adjusted, the aperture of valve is along with the electric current of flow set changes and changes.Thereby make the heat energy in the column type solar energy heat exchanger 3 keep balance, under the setting value effect of a temperature sensor 15, the rotating speed of pipeline frequency conversion fan 17 keeps balance with the flow of hot blast and air intake valve 14 apertures again, reaches the purpose that constant temperature hot gas source is provided automatically.
The present invention adopts the rotating speed of the current signal control pipeline frequency conversion fan of temperature sensor output, utilizes the aperture of the current signal control air intake valve 14 of flow transmitter output, reaches the control procedure of automatic constant-temperature.Help vertical oven dry material is dried, play the requirement of energy-conservation and clean production.
The operation principle of material of the present invention and thermal current exchange oven dry is as follows:
The control procedure that the present invention regulates mass flow automatically is as follows:
Select signal value by standard control device 2 according to the address that receives, behind the address gating signal gating of the 4th measurement adaptation module A10 that gating links to each other with humidity sensor 8, the 4th measurement adaptation module A10 will record the moisture signal of material and send back in the industrial computer 1 after A/D (modular converter) conversion.Industrial computer 1 compares according to the given data of interior humidity, when humidity greater than when setting value, send current controling signal and material adjuster 9 automatically adjusted for the 6th control adaptation module A9, humidity is big more, material blanking amount is just more little.Humidity is more dried, and material blanking amount is just many more.Reach continous-stable constant temperature drying and automatic material and, whole production is in the energy-conservation and free of contamination environment automatically according to the blanking flow of humidity of materials control material.
Fig. 5 shows the structural representation of material adjuster of the present invention,
The operation principle of material adjuster is as follows:
The heat that the heat energy of vertical dryer 4 produces from solar energy, big under the inventory, can influence the degree of drying materials, material is bored H9 to cone governor H6 through sliding material basin, when just changeing, adjusting motor H1 can drive turbine box H4 motion by power transmission shaft H2, elevating lever H5 drives cone governor H6 and rises, the slit of back sliding material basin awl H9 and cone governor H6 diminishes because cone governor H6 rises, at this moment the flow velocity of material will descend, when regulating motor H1 counter-rotating, can drive turbine box H4 motion by power transmission shaft H2, elevating lever H5 drives cone governor H6 and descends, the slit of back sliding material basin awl H9 and cone governor H6 becomes big because cone governor H6 descends, at this moment the flow velocity of material will strengthen, thereby has guaranteed the uniformity and the quality that has improved drying materials of mass flow.
In the present invention, standard control device 2 can be selected the I/O 32 of (the MCGS built-in touch screen) of the production of the Kunlun, BeiJing, China configuration software company for use.Industrial computer 1 can be selected the main frame of the damp intelligent scientific ﹠ technical corporation of Chinese Shanghai flood for use, grinds magnificent industrial computer.All control adaptation module can adopt module or the similar A/D modular converter that grinds magnificent ADAM4000 series.All measure adaptation module can select for use in safe RM data acquisition module or grind magnificent data acquisition module, can also select similar D/F modular converter in addition.
Claims (7)
1. light energy vertical dryer automatic constant temperature drying and automatic regulation material flow control device, it is characterized in that: it comprises standard control device (2), industrial computer (1), solar energy heat exchanger (3), vertical dryer (4), constant temperature drying and automatic control device, vertical dryer control device, standard control device (2) links to each other with industrial computer (1) by the standard serial communication interface, standard control device (2) links to each other with solar energy heat exchanger (3) and vertical dryer (4) respectively, and solar energy heat exchanger (3) links to each other with vertical dryer (4).
2. according to the described light energy vertical dryer automatic constant temperature drying and automatic regulation material flow control device of claim 1, it is characterized in that: described solar energy heat exchanger (3) has a temperature sensor (15), flow transmitter (18), air intake valve (14) and wind pipe (16), wind pipe (16) is provided with pipeline frequency conversion fan (17), described constant temperature drying and automatic control device comprises that being located at first on the described standard control device (2) measures adaptation module (A5), second measures adaptation module (A7), the first control adaptation module (A6), the second control adaptation module (A8), first measures adaptation module (A5) links to each other with a described temperature sensor (15), second measures adaptation module (A7) links to each other with described flow transmitter (18), the first control adaptation module (A6) links to each other with described air intake valve (14), and the second control adaptation module (A8) links to each other with described pipeline frequency conversion fan (17).
3. according to claim 1 or 2 described light energy vertical dryer automatic constant temperature drying and automatic regulation material flow control devices, it is characterized in that: described vertical dryer control device comprises that being located at the 3rd on the described standard control device (2) controls adaptation module (A1), the 4th control adaptation module (A3), the 5th control adaptation module (A4), the 3rd measures adaptation module (A2), described vertical dryer (4) top is provided with dedust air duct (13), dedust air duct (13) is provided with No. two temperature sensors (10), dedust air duct (13) links to each other with deduster (5), deduster (5) bottom is provided with motor (12), deduster (5) links to each other with dedusting fan motor (11), vertical dryer (4) bottom is provided with remittance air compartment (19), charging elevator (6) is provided with elevator motor (7), the 3rd control adaptation module (A1) links to each other with elevator motor (7), the 4th control adaptation module (A3) links to each other with dedusting fan motor (11), the 5th control adaptation module (A4) links to each other with motor (12), and the 3rd measures adaptation module (A2) links to each other with No. two temperature sensors (10).
4. light energy vertical dryer automatic constant temperature drying and automatic regulation material flow control device according to claim 3 is characterized in that: the sidepiece of described vertical dryer (4) is provided with secondary hot-air pipe (20).
5. light energy vertical dryer automatic constant temperature drying and automatic regulation material flow control device according to claim 4, it is characterized in that: described solar energy heat exchanger (3) comprises column type heat absorption vacuum tube (T1), thermal-arrest changes air compartment (T2), air intake resistance dividing plate (T3), pipeline heat collector (T4), heat absorption cover plate (T5), described air intake resistance dividing plate (T3) and pipeline heat collector (T4) are installed in thermal-arrest and change air compartment (T2) inside, heat absorption cover plate (T5) is fixed on the top that thermal-arrest changes air compartment (T2), and column type heat absorption vacuum tube (T1) is fixed on thermal-arrest and changes on air compartment (T2) and the heat absorption cover plate (T5).
6. light energy vertical dryer automatic constant temperature drying and automatic regulation material flow control device according to claim 4, it is characterized in that: it also comprises automatic adjusting material flow control device, automatically regulate material flow control device and comprise that being located at the 4th on the described standard control device (2) measures adaptation module (A10) and the 6th control adaptation module (A9), described vertical dryer (4) is provided with moisture detection sensor (8) and material adjuster (9), the 4th measures adaptation module (A10) links to each other with moisture detection sensor (8), and the 6th control adaptation module (A9) links to each other with material adjuster (9).
7. light energy vertical dryer automatic constant temperature drying and automatic regulation material flow control device according to claim 5, it is characterized in that: described material adjuster (9) comprises regulates motor (H1), power transmission shaft (H2), power transmission shaft pillar (H3), turbine box (H4), elevating lever (H5), cone governor (H6), balance chain (H7), spreading awl (H8), sliding material basin awl (H9), support (H10), described adjusting motor (H1) is fixed on the support (H10), regulating motor (H1) links to each other with turbine box (H4) by power transmission shaft (H2), turbine box (H4) is fixed on the spreading awl (H8), regulate the outer power transmission shaft pillar (H3) that is provided with of motor (H1), the two ends of power transmission shaft pillar (H3) are separately fixed to be regulated on motor (H1) and the turbine box (H4), turbine box (H4) links to each other with cone governor (H6) by elevating lever (H5), cone governor (H6) links to each other with balance chain (H7), and balance chain (H7) is fixed on the sliding material basin awl (H9).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2009101172752A CN101886874B (en) | 2009-05-12 | 2009-05-12 | Automatic constant temperature drying and automatic regulation material flow control device of light energy vertical dryer |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2009101172752A CN101886874B (en) | 2009-05-12 | 2009-05-12 | Automatic constant temperature drying and automatic regulation material flow control device of light energy vertical dryer |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN101886874A true CN101886874A (en) | 2010-11-17 |
| CN101886874B CN101886874B (en) | 2012-02-29 |
Family
ID=43072888
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2009101172752A Expired - Fee Related CN101886874B (en) | 2009-05-12 | 2009-05-12 | Automatic constant temperature drying and automatic regulation material flow control device of light energy vertical dryer |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN101886874B (en) |
Cited By (20)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104964544A (en) * | 2015-06-16 | 2015-10-07 | 苏州宏恒化工有限公司 | Hot air circulating drying machine |
| CN104990369A (en) * | 2015-08-14 | 2015-10-21 | 吉首大学 | Tower type penetrating reverse flow fluidized drier |
| CN104990367A (en) * | 2015-08-14 | 2015-10-21 | 吉首大学 | Penetrating reverse-flow type fluidization drying tower |
| CN105020986A (en) * | 2015-08-14 | 2015-11-04 | 吉首大学 | Thermal pump type tail heat recycling reverse flowing penetrating fluidized drying machine |
| CN105021012A (en) * | 2015-08-14 | 2015-11-04 | 吉首大学 | Hot-air drying machine capable of utilizing waste heat and achieving penetrating countercurrent fluidization |
| CN105020985A (en) * | 2015-08-14 | 2015-11-04 | 吉首大学 | Heat pump type tail heat utilization penetrating reverse flow fluidized drying machine |
| CN105020984A (en) * | 2015-08-14 | 2015-11-04 | 吉首大学 | Hot-air drying machine capable of utilizing waste heat and achieving penetrating countercurrent fluidization |
| CN105066652A (en) * | 2015-08-14 | 2015-11-18 | 吉首大学 | Tail heat recovery hot air type penetrating counterflow fluidized drying machine |
| CN105066653A (en) * | 2015-08-14 | 2015-11-18 | 吉首大学 | Heat pump type tail heat recovery and penetrating counterflow fluidized drying machine |
| CN105115279A (en) * | 2015-08-14 | 2015-12-02 | 吉首大学 | Heat-pump type exhaust heat utilization penetration counter-flow fluidized drying machine |
| CN105110416A (en) * | 2015-10-06 | 2015-12-02 | 吉首大学 | Vibrating motor vibration and rubber pad shock absorption fluidized bed type ion exchange water treatment device |
| CN105135826A (en) * | 2015-08-14 | 2015-12-09 | 吉首大学 | Tail heat recovery hot wind type penetration countercurrent fluidized dryer |
| CN105174376A (en) * | 2015-10-06 | 2015-12-23 | 吉首大学 | Fluid bed type ion exchange water treatment device adopting electromagnetic vibration and provided with foam cushions for damping |
| CN105651024A (en) * | 2016-03-11 | 2016-06-08 | 安徽新生力生物科技有限公司 | Grain dryer with automatic drying-layer constant-temperature control device |
| CN105737546A (en) * | 2016-03-11 | 2016-07-06 | 安徽新生力生物科技有限公司 | Constant-temperature control system used for drying layer of grain dryer |
| CN105758167A (en) * | 2016-03-11 | 2016-07-13 | 安徽新生力生物科技有限公司 | Constant-temperature control method of drying layer of grain drying machine |
| CN106546091A (en) * | 2015-12-24 | 2017-03-29 | 广东展翠食品股份有限公司 | A kind of bergamot fruit drying equipment and its drying meanss |
| CN111566428A (en) * | 2017-12-15 | 2020-08-21 | 芝浦机械电子株式会社 | Organic film forming apparatus |
| CN113251783A (en) * | 2021-06-21 | 2021-08-13 | 山东新迪医疗科技有限公司 | Traditional chinese medicine drying storage equipment |
| CN113803968A (en) * | 2021-09-03 | 2021-12-17 | 江苏悦谷农业科技发展有限公司 | Grain drier and control method of drying layer flow and heat supply quantity thereof |
-
2009
- 2009-05-12 CN CN2009101172752A patent/CN101886874B/en not_active Expired - Fee Related
Cited By (28)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104964544A (en) * | 2015-06-16 | 2015-10-07 | 苏州宏恒化工有限公司 | Hot air circulating drying machine |
| CN105021012B (en) * | 2015-08-14 | 2018-03-13 | 吉首大学 | Tail heat utilization hot air type penetrates adverse current fluidized dryer |
| CN105020986B (en) * | 2015-08-14 | 2018-03-13 | 吉首大学 | Heat-pump-type tail recuperation of heat penetrates adverse current fluidized dryer |
| CN104990369A (en) * | 2015-08-14 | 2015-10-21 | 吉首大学 | Tower type penetrating reverse flow fluidized drier |
| CN105021012A (en) * | 2015-08-14 | 2015-11-04 | 吉首大学 | Hot-air drying machine capable of utilizing waste heat and achieving penetrating countercurrent fluidization |
| CN105020985A (en) * | 2015-08-14 | 2015-11-04 | 吉首大学 | Heat pump type tail heat utilization penetrating reverse flow fluidized drying machine |
| CN105020984A (en) * | 2015-08-14 | 2015-11-04 | 吉首大学 | Hot-air drying machine capable of utilizing waste heat and achieving penetrating countercurrent fluidization |
| CN105066652A (en) * | 2015-08-14 | 2015-11-18 | 吉首大学 | Tail heat recovery hot air type penetrating counterflow fluidized drying machine |
| CN105066653A (en) * | 2015-08-14 | 2015-11-18 | 吉首大学 | Heat pump type tail heat recovery and penetrating counterflow fluidized drying machine |
| CN105115279A (en) * | 2015-08-14 | 2015-12-02 | 吉首大学 | Heat-pump type exhaust heat utilization penetration counter-flow fluidized drying machine |
| CN104990367A (en) * | 2015-08-14 | 2015-10-21 | 吉首大学 | Penetrating reverse-flow type fluidization drying tower |
| CN105135826A (en) * | 2015-08-14 | 2015-12-09 | 吉首大学 | Tail heat recovery hot wind type penetration countercurrent fluidized dryer |
| CN105020985B (en) * | 2015-08-14 | 2018-02-09 | 吉首大学 | Heat-pump-type tail heat utilization penetrates adverse current fluidized dryer |
| CN105020986A (en) * | 2015-08-14 | 2015-11-04 | 吉首大学 | Thermal pump type tail heat recycling reverse flowing penetrating fluidized drying machine |
| CN105020984B (en) * | 2015-08-14 | 2017-12-19 | 吉首大学 | A kind of tail heat utilization hot air type penetrates adverse current fluidized dryer |
| CN105135826B (en) * | 2015-08-14 | 2017-11-10 | 枣阳市灵鹿酒业有限公司 | A kind of tail recuperation of heat hot air type penetrates adverse current fluidized dryer |
| CN105174376A (en) * | 2015-10-06 | 2015-12-23 | 吉首大学 | Fluid bed type ion exchange water treatment device adopting electromagnetic vibration and provided with foam cushions for damping |
| CN105110416A (en) * | 2015-10-06 | 2015-12-02 | 吉首大学 | Vibrating motor vibration and rubber pad shock absorption fluidized bed type ion exchange water treatment device |
| CN106546091A (en) * | 2015-12-24 | 2017-03-29 | 广东展翠食品股份有限公司 | A kind of bergamot fruit drying equipment and its drying meanss |
| CN106546091B (en) * | 2015-12-24 | 2022-03-22 | 广东展翠食品股份有限公司 | Bergamot fruit drying equipment and drying method thereof |
| CN105651024A (en) * | 2016-03-11 | 2016-06-08 | 安徽新生力生物科技有限公司 | Grain dryer with automatic drying-layer constant-temperature control device |
| CN105758167A (en) * | 2016-03-11 | 2016-07-13 | 安徽新生力生物科技有限公司 | Constant-temperature control method of drying layer of grain drying machine |
| CN105737546A (en) * | 2016-03-11 | 2016-07-06 | 安徽新生力生物科技有限公司 | Constant-temperature control system used for drying layer of grain dryer |
| CN111566428A (en) * | 2017-12-15 | 2020-08-21 | 芝浦机械电子株式会社 | Organic film forming apparatus |
| CN111566428B (en) * | 2017-12-15 | 2022-03-29 | 芝浦机械电子株式会社 | Organic film forming apparatus |
| CN113251783A (en) * | 2021-06-21 | 2021-08-13 | 山东新迪医疗科技有限公司 | Traditional chinese medicine drying storage equipment |
| CN113251783B (en) * | 2021-06-21 | 2021-09-17 | 山东新迪医疗科技有限公司 | Traditional chinese medicine drying storage equipment |
| CN113803968A (en) * | 2021-09-03 | 2021-12-17 | 江苏悦谷农业科技发展有限公司 | Grain drier and control method of drying layer flow and heat supply quantity thereof |
Also Published As
| Publication number | Publication date |
|---|---|
| CN101886874B (en) | 2012-02-29 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN101886874B (en) | Automatic constant temperature drying and automatic regulation material flow control device of light energy vertical dryer | |
| CN101655319B (en) | System for regulating and optimizing smoke by power generation and recycle of residual heat of sintering ring cold machine | |
| CN105604599B (en) | A kind of solar energy air pump self tunnel natural ventilation system and method | |
| CN104061698B (en) | Salar light-gathering formula thermal-arrest baking oven | |
| CN105156144A (en) | Complementary tunnel natural ventilation system with solar air pump and method | |
| CN106196948A (en) | A kind of simple solar drying apparatus | |
| CN101884425B (en) | Energy-saving food drying baking room | |
| CN202955607U (en) | Street lamp capable of generating power by using upflow and flywheel battery | |
| CN201811130U (en) | Active server pages (ASP) light-emitting diode (LED) road tunnel lighting system | |
| CN206176960U (en) | Drying device provides multiple forms of energy to complement each other | |
| CN207716757U (en) | material drying device | |
| CN201397023Y (en) | Light energy vertical drying machine automatic constant temperature drying automatic regulation material flow capacity control device | |
| CN102437221B (en) | Automatically cleaning cooling type solar cell panel | |
| CN102329061B (en) | Energy-saving and emission-reduction star-wheel sludge drying tower with common application of wind energy and solar energy | |
| Wang et al. | Combination of waste-heat-recovery heat pump and auxiliary solar-energy heat supply priority for tobacco curing. | |
| CN102396769A (en) | Full natural energy air stream drying cabin for processing marine food products | |
| CN209706022U (en) | A kind of energy-saving, environmental protection boiler | |
| CN201621868U (en) | Solar air preheater of vacuum tube | |
| CN104295450A (en) | Ground tower furnace type renewable energy heating and refrigerating power generation device | |
| CN109020146A (en) | A kind of sludge automatic fuel device and method based on solar energy greenhouse | |
| CN214463015U (en) | Solar plant with solar heat collection roof and sunlight room | |
| CN103629061A (en) | Comprehensive solar photovoltaic hot-air-flow utilization power generation device | |
| CN208982218U (en) | It is a kind of using solar chimney as the wind power plant of tower | |
| CN206572425U (en) | A kind of power generating streetlamp | |
| CN206118049U (en) | Food production firing equipment |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20120229 Termination date: 20210512 |