CN102620527A - Drying system capable of realizing closed cycle, solvent recovery and atomizing granulation - Google Patents
Drying system capable of realizing closed cycle, solvent recovery and atomizing granulation Download PDFInfo
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- CN102620527A CN102620527A CN2012100995538A CN201210099553A CN102620527A CN 102620527 A CN102620527 A CN 102620527A CN 2012100995538 A CN2012100995538 A CN 2012100995538A CN 201210099553 A CN201210099553 A CN 201210099553A CN 102620527 A CN102620527 A CN 102620527A
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- 238000001035 drying Methods 0.000 title claims abstract description 45
- 239000002904 solvent Substances 0.000 title claims abstract description 18
- 238000005469 granulation Methods 0.000 title abstract description 10
- 230000003179 granulation Effects 0.000 title abstract description 10
- 238000011084 recovery Methods 0.000 title abstract description 9
- 238000007789 sealing Methods 0.000 claims abstract description 25
- 239000004744 fabric Substances 0.000 claims abstract description 21
- 239000007789 gas Substances 0.000 claims abstract description 12
- 230000007246 mechanism Effects 0.000 claims abstract description 12
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 12
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 38
- 229910052757 nitrogen Inorganic materials 0.000 claims description 19
- 239000000463 material Substances 0.000 claims description 14
- 239000007921 spray Substances 0.000 claims description 10
- 238000000034 method Methods 0.000 claims description 8
- 238000010924 continuous production Methods 0.000 claims description 6
- 229920006395 saturated elastomer Polymers 0.000 claims description 6
- 230000001174 ascending effect Effects 0.000 claims description 5
- 238000009826 distribution Methods 0.000 claims description 4
- 238000001914 filtration Methods 0.000 claims description 4
- 239000007788 liquid Substances 0.000 claims description 4
- 230000002787 reinforcement Effects 0.000 claims description 2
- 238000009835 boiling Methods 0.000 abstract description 6
- 239000011261 inert gas Substances 0.000 abstract description 4
- 230000000694 effects Effects 0.000 abstract description 3
- 238000005516 engineering process Methods 0.000 abstract description 3
- 238000004519 manufacturing process Methods 0.000 abstract description 3
- 239000008187 granular material Substances 0.000 abstract description 2
- 238000005245 sintering Methods 0.000 description 9
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 7
- 239000001301 oxygen Substances 0.000 description 7
- 229910052760 oxygen Inorganic materials 0.000 description 7
- 238000005507 spraying Methods 0.000 description 7
- 229910000831 Steel Inorganic materials 0.000 description 4
- 238000006073 displacement reaction Methods 0.000 description 4
- 239000010959 steel Substances 0.000 description 4
- 238000009833 condensation Methods 0.000 description 3
- 230000005494 condensation Effects 0.000 description 3
- 238000007599 discharging Methods 0.000 description 3
- 239000012530 fluid Substances 0.000 description 3
- 239000007787 solid Substances 0.000 description 3
- 238000010438 heat treatment Methods 0.000 description 2
- 239000000843 powder Substances 0.000 description 2
- 238000012216 screening Methods 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- 101000608752 Phytolacca americana Lectin-C Proteins 0.000 description 1
- 210000004712 air sac Anatomy 0.000 description 1
- 230000004888 barrier function Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000007664 blowing Methods 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000002826 coolant Substances 0.000 description 1
- 239000012809 cooling fluid Substances 0.000 description 1
- 238000004134 energy conservation Methods 0.000 description 1
- 238000004880 explosion Methods 0.000 description 1
- 230000002045 lasting effect Effects 0.000 description 1
- 239000003960 organic solvent Substances 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 238000007670 refining Methods 0.000 description 1
- 239000002912 waste gas Substances 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
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Abstract
The invention relates to a drying system applicable to realization of closed cycle, solvent recovery and atomizing granulation of inert gas, which comprises a boiling drying main unit. The boiling drying main unit comprises an upper cylinder, a boiling chamber and a lower cylinder which are hermetically connected sequentially from top to bottom, a bed plate is arranged at the bottom of the boiling chamber and comprises two plate bodies, adjacent edges of the two plate bodies are fixed on a rotary shaft and a shaft sleeve respectively, the rotary shaft is sleeved into the shaft sleeve, and ends, extending out of the boiling chamber, of the rotary shaft and the shaft sleeve are connected with pneumatic, hydraulic or electric driving mechanisms which are used for driving the rotary shaft and the shaft sleeve to rotate respectively. The bed plate is applicable to automatic discharge, fine in sealing effect, low in working strength, high in production efficiency and convenient in operation. A cloth bag adopting air bag sealing and combined with the cylinder jitter technology is applicable to sufficient recovery of fine granular materials. Heat exchangers are applicable to use of flash vapor and hot water generated by superheated water at the temperature of sufficiently 130 DEG C to preheat gas to be heated, so that heat use efficiency is greatly improved.
Description
Technical field
The present invention relates to the technical field of drying equipment, specifically is a kind of drying system that is suitable for realizing inert gas closed cycle, solvent recovery and spraying granulation.
Background technology
Chinese patent document CN101776372A discloses a kind of nitrogen closed cycle drying and solvent recovering system, has fluid bed dryer, condensing unit, solid and gas separator, circulating fan, heat exchanger, solvent recovery jar and nitrogen and supplies pipe; The exhaust outlet of fluid bed dryer is connected with the air inlet of said condensing unit through pipeline; The air outlet of condensing unit is connected with said solid and gas separator; The air outlet of solid and gas separator is connected with said circulating fan; The wind of circulating fan output is delivered to said heat exchanger heating, and the nitrogen after the heating is delivered in the drying machine; The solvent collection mouth of said condensing unit is connected with the solvent recovery jar, and said condensing unit and solvent recovery jar supply pipe that cooling medium is provided by cooling fluid; The charging aperture of said fluid bed dryer is equipped with material envelope type screw feeder.It has realized the fluidized drying and the Recovery of Organic Solvent of continuous charging and discharging, no waste gas discharge of wastewater.
Chinese patent document ZL200820041009.7 discloses a kind of closed cycle boiling drier, and it is the solvent in the recovered material effectively, and can in system, charge into inert gas, and makes its closed cycle.But the production process of its main frame is step, and every dry batch materials just must be pulled out discharging with hopper, not only wastes time and energy, and can cause the leakage of inert gas in the discharge process.
For realizing continuous production, Chinese patent document CN102022895A discloses a kind of closed cycle fluidized drying machine host, comprises hopper and orifice plate or the sintering web plate of making convertible structure, and orifice plate or sintering web plate are horizontally set at feed hopper bottom.Said convertible structure comprises: the rotating shaft that is fixedly linked with orifice plate or sintering web plate, be located at the external handwheel that is used to control of main barrel, the part that rotating shaft passes the main frame cylindrical shell cooperates with the rotary seal of main frame cylindrical shell.
The weak point of above-mentioned existing closed cycle fluidized drying machine host is: the upset of orifice plate or sintering web plate, need the artificial handwheel control of passing through, and waste time and energy.Orifice plate or sintering web plate be in level the time, can't guarantee the sealing at its edge to cause marginal existence to leak out, leak material, influence the fluidized drying effect; Even if sealing ring is set around orifice plate or sintering web plate, because handwheel can't provide lasting tensile force, it still can't keep sealing.
How being suitable for through a kind of that automatic continuous production, the higher closed cycle solvent of reliability reclaim, the spraying granulation drying system, is the technical barrier of this area.
Summary of the invention
The technical problem that the present invention will solve provide a kind of simple in structure, be suitable for the higher closed cycle of automatic continuous production, reliability, solvent reclaims and the spraying granulation drying system.
For solving the problems of the technologies described above, closed cycle provided by the invention, solvent reclaim and the spraying granulation drying system, and it comprises the fluidized drying main frame, and the fluidized drying main frame comprises upper shell 1.1, boiling-house 1.2 and the lower shell 1.3 of upper-lower seal connection successively; Boiling-house 1.2 bottoms are provided with bed board, it is characterized in that: said bed board is made up of two boards body 1.2.1, and the neighboring edge of this two boards body 1.2.1 is separately fixed on sheathed each other the rotating shaft 1.2.2 and axle sleeve 1.2.3; The end of extending boiling-house of this rotating shaft 1.2.2 and axle sleeve 1.2.3 with drive respectively that this rotating shaft 1.2.2 and axle sleeve 1.2.3 rotate pneumatic, surge or electric driving mechanism links to each other.
The top at the neighboring edge place of described two boards body 1.2.1 is provided with crossbeam 1.2.8; The lower surface of this crossbeam 1.2.8 is provided with sealing strip 1.2.9; Sealing bar 1.2.9 is suitable for when the bottom port of described two boards body 1.2.1 sealing boiling-house 1.2, making the neighboring edge of said two boards body 1.2.1 and said crossbeam 1.2.8 realize being sealed and matched; The bottom end face of boiling-house 1.2 is provided with sealing ring 1.2.0; Said sealing ring 1.2.0 is suitable for making the remaining edge of described two boards body 1.2.1 and the bottom port of said boiling-house 1.2 to be sealed and matched; Thereby ascending air is only passed through from the orifice plate or the sintering net that constitute bed board; Prevent the part from leaking out and cause the distinguished and admirable inequality on the bed board, and then cause uneven drying.
Embodiment as pneumatic drive mechanism; Said pneumatic drive mechanism comprises the connecting rod 1.2.6 of the end of extending boiling-house of being fixed in said rotating shaft 1.2.2 and axle sleeve 1.2.3, and this flexibly connects with the piston rod end of the first rotational lock cylinder 1.2.4, the second rotational lock cylinder 1.2.5 respectively the far-end of connecting rod 1.2.6; During work; First, second rotational lock cylinder is successively controlled its action by PLC; And then control said rotating shaft 1.2.2 and axle sleeve 1.2.3 alternately rotation successively, and make the alternately upset downwards successively of corresponding plate body, so that the material on the said bed board falls into said lower shell fully; And the realization automatic continuous production, and then enhance productivity.
Said rotating shaft 1.2.2 and axle sleeve 1.2.3 bearing cooperate, and said rotating shaft 1.2.2 and axle sleeve 1.2.3 constitute rotary seal with the auxiliary section of boiling-house wall body respectively and cooperate.
The bottom port of said boiling-house 1.2 is rounded, and described two boards body 1.2.1 is the semicircle 1.2.1 of symmetrical distribution.
The middle and upper part of said upper shell 1.1 interior, contiguous these upper shells 1.1 is provided with central dividing plate 1.1.0; And a plurality of cloth bags 1.6 of distribution and this central dividing plate 1.1.0 both sides; Bottom opening in each cloth bag of said central dividing plate 1.1.0 homonymy is fixed on the base fabric 1.6.0; Be distributed with the through hole 1.6.3 that links to each other with the bottom opening of said cloth bag 1.6 respectively on this base fabric 1.6.0; Each base fabric 1.6.0 is separately fixed on the waist shape ring 1.6.1 of the dividing plate 1.1.0 both sides that mediate; Be fixed with pressure bladder 1.6.2 around each waist shape ring 1.6.1, each the pressure bladder 1.6.2 after the inflation is suitable for making between each waist shape ring 1.6.1 and the central dividing plate 1.1.0 and between the inwall of each waist shape ring 1.6.1 and said upper shell 1.1 and is sealed and matched, so that the ascending air in the upper shell 1.1 is only discharged through each cloth bag 1.6.
Top in each cloth bag of said central dividing plate 1.1.0 homonymy is located on the lift bag frame 1.6.4, and this lift bag frame 1.6.4 links to each other with a locking cylinder 1.6.5
The bottom of contiguous said upper shell 1.1 is provided with spray gun 1.1.2, and the shower nozzle of this spray gun 1.1.2 is located at the bottom centre place of said upper shell 1.1.This spray gun 1.1.2 links to each other with the solvent carrier pipe with the elevated pressure nitrogen tracheae.The wall body of contiguous said upper shell 1.1 bottoms is provided with a plurality of pilot hole 1.1.3 that are used to be provided with said spray gun 1.1.2 that distribute up and down; Be used for selecting corresponding pilot hole for use according to the height of material in said boiling-house 1.2; And the material end face in the vaporific feed liquid that the makes said spray gun 1.1.2 ejection said boiling-house 1.2 that is suitable for covering just, and prevent that feed liquid is bonded at the inwall of said boiling-house 1.2.
Being used for the dry heat exchanger 5 with gas of ebuillition of heated comprises: heat exchange unit 5.1 that the multilayer upper-lower seal connects and the preheating unit 5.2 that is sealedly attached to heat exchange unit 5.1 belows of bottom; This preheating unit 5.2 comprises the multilayer that upper-lower seal connects; The bottom air intake vent that is in the preheating unit 5.2 of the bottom links to each other with the air outlet of said explosion-proof circulating fan 4, and the top outlet inlet of the heat exchange unit 5.1 of top layer is the hot-blast outlet of said heat exchanger 5.
The thermal medium inlet of each heat exchange unit 5.1 links to each other with the saturated steam carrier pipe; The thermal medium outlet of each heat exchange unit 5.1 links to each other with the thermal medium inlet of each preheating unit 5.2 through a steam trap 11 backs; The thermal medium outlet output condensed water of each preheating unit 5.2; This condensed water is sent back to boiler, regenerates the said saturated steam that is not less than 130 ℃.
During use; 130 ℃ saturated steam send into each heat exchange unit 5.1 and fluidized drying with gas converting heat after the superheated water of 130 ℃ of outputs; This superheated water of 130 ℃ generates flash steam behind said steam trap 11; And be 100 ℃ vapour-liquid admixture, and send into each preheating unit 5.2 heat exchange, be used for the said fluidized drying of preheating and use gas; Successively heated through each heat exchange unit 5.1 again by the gas of preheating, finally reach required temperature.
In the heat transfer process of each heat exchange unit 5.1,130 ℃ saturated steam is emitted covert heat in the process that is condensed into 130 ℃ of water, makes the heat exchange coil in each heat exchange unit 5.1 remain at 130 ℃; And then make fluidized drying after heat exchange successively, reach 120 ℃ basically with gas.
Said 130 ℃ superheated water is sent into each preheating unit 5.2 behind said steam trap 11, use gas, be beneficial to the raising thermal energy conversion efficiency, with energy-conservation with the said fluidized drying of preheating.
The technique effect that the present invention has: (1) closed cycle of the present invention, solvent reclaim and the spraying granulation drying system, and the bed board of employing is suitable for automatic blanking, and sealing effectiveness is better, and working strength is low, and production efficiency is high, are convenient to operation.(2) cloth bag of the present invention adopts air sac sealing, in conjunction with the cylinder dither technique, is suitable for fully reclaiming fine granular materials.(3) heat exchanger of the present invention is suitable for utilizing flash steam, the hot water preheating gas to be heated of abundant 130 ℃ superheated water generation, has significantly improved utilization efficiency of heat energy.
Description of drawings
For content of the present invention is more clearly understood, below basis specific embodiment and combine accompanying drawing, the present invention is done further detailed explanation, wherein
Fig. 1 is the structural representation of drying system of the present invention;
Fig. 2 is the structural representation of boiling-house of the present invention;
Fig. 3 is the profile of the boiling-house among Fig. 2;
Fig. 4 is the partial enlarged drawing of the local I of said boiling-house;
Fig. 5 is the partial enlarged drawing of the local II of said boiling-house;
Fig. 6 is the vertical view of the boiling-house among Fig. 2;
Fig. 7 is the structural representation of each cloth bag in the upper shell of the present invention;
Fig. 8 is the A-A profile of Fig. 7.
The specific embodiment
Below in conjunction with accompanying drawing and embodiment the present invention is elaborated:
Like Fig. 1, the closed cycle of present embodiment, solvent reclaim and the spraying granulation drying system, and it comprises: fluidized drying main frame, fluidized drying main frame comprise upper shell 1.1, boiling-house 1.2 and the lower shell 1.3 of upper-lower seal connection successively.
The exhaust duct that is connected on the top exhaust outlet of said upper shell 1.1 links to each other with nitrogen filtering device 2, condensation and liquid-resisting device 3, explosion-proof circulating fan 4, heat exchanger 5 successively, and the hot-blast outlet of heat exchanger 5 links to each other with the air intake vent of said lower shell 1.3.
Condensation and liquid-resisting device 3 link to each other with solvent recovery jar 6, are provided with first Pneumatic butterfly valve 8 and displacement blow-down pipe 10 successively with the inlet upper reaches of explosion-proof circulating fan 4, and the displacement blow-down pipe is provided with second Pneumatic butterfly valve 9; The inlet of explosion-proof circulating fan 4 links to each other with nitrogen steel cylinder group 7.
Said lower shell 1.3 is turbination, and the bottom of this lower shell 1.3 links to each other with a screening machine 1.5 through the Blowing stopper 1.4 that is used for sealed discharging, is used to sieve out finished product and fine powder.
The bottom of contiguous said upper shell 1.1 is provided with the charging aperture 1.1.4 of band seal valve, and this charging aperture 1.1.4 links to each other with feeder, and the fine powder that said screening machine 1.5 sieves out is sent into this feeder.
Boiling-house 1.2 bottoms are provided with bed board, and said bed board is made up of two boards body 1.2.1, and the neighboring edge of this two boards body 1.2.1 is separately fixed on sheathed each other the rotating shaft 1.2.2 and axle sleeve 1.2.3; The end of extending boiling-house of this rotating shaft 1.2.2 and axle sleeve 1.2.3 is fixed with connecting rod 1.2.6 respectively, and this flexibly connects with the piston rod end of the first rotational lock cylinder 1.2.4, the second rotational lock cylinder 1.2.5 respectively the far-end of connecting rod 1.2.6; During work; First, second rotational lock cylinder is successively controlled its action by PLC; And then control said rotating shaft 1.2.2 and axle sleeve 1.2.3 alternately rotation successively, and make the alternately upset downwards successively of corresponding plate body, so that the material on the said bed board falls into said lower shell fully; And the realization automatic continuous production, and then enhance productivity.
The top at the neighboring edge place of described two boards body 1.2.1 is provided with crossbeam 1.2.8; The lower surface of this crossbeam 1.2.8 is provided with sealing strip 1.2.9; Sealing bar 1.2.9 is suitable for when the bottom port of described two boards body 1.2.1 sealing boiling-house 1.2, making the neighboring edge of said two boards body 1.2.1 and said crossbeam 1.2.8 realize being sealed and matched; The bottom end face of boiling-house 1.2 is provided with sealing ring 1.2.0; Said sealing ring 1.2.0 is suitable for making the remaining edge of described two boards body 1.2.1 and the bottom port of said boiling-house 1.2 to be sealed and matched; Thereby ascending air is only passed through from the orifice plate or the sintering net that constitute bed board; Prevent local leakage material, leak out, and cause the distinguished and admirable inequality on the bed board, and then cause uneven drying.
As preferred embodiment, sealing strip 1.2.9 comprises laterally arrange a pair of, and this laterally arranges with the edge of said two boards body 1.2.1 respectively to sealing strip 1.2.9.
When the bottom port of first, second this two boards body of rotational lock cylinder control 1.2.1 sealing boiling-house 1.2; Realize being sealed and matched in the edge of said two boards body 1.2.1; Ascending air is only passed through from the orifice plate or the sintering net that constitute bed board; Prevent the part from leaking out and cause the distinguished and admirable inequality on the bed board, and then cause uneven drying.
First, second Pneumatic butterfly valve 8,9 is controlled by said PLC; When first Pneumatic butterfly valve 8 is closed; Second Pneumatic butterfly valve 9 is opened, and with the nitrogen of nitrogen steel cylinder group 7 outputs through explosion-proof circulating fan 4, send into heat exchanger 5, fluidized drying main frame, nitrogen filtering device 2, condensation and liquid-resisting device 3 successively after; By said displacement blow-down pipe 10 air is discharged; When PLC recorded oxygen content and is lower than setting value through being located at first oxygen sensor in the said displacement blow-down pipe 10, the nitrogen control valve 7.1 that PLC controls on the output pipe of second Pneumatic butterfly valve 9, nitrogen steel cylinder group 7 was closed, and first Pneumatic butterfly valve 8 is opened; Can avoid the material of easy oxidation oxidized in the granulation dry run like this.
The air outlet of explosion-proof circulating fan 4 is provided with second oxygen sensor, in nitrogen closed cycle process, if when said PL C records oxygen content and exceeds standard through said second oxygen sensor, controls first Pneumatic butterfly valve 8 and closes, and nitrogen control valve 7.1 is opened; When PLC recorded oxygen content and is lower than setting value through being located at said first oxygen sensor, the nitrogen control valve of controlling on the output pipe of second Pneumatic butterfly valve 9, nitrogen steel cylinder group 7 7.1 was closed, and first Pneumatic butterfly valve 8 is opened; Thereby recover the nitrogen closed cycle.
Be provided with shake cylinder 1.1.5 in the top of each cloth bag of said central dividing plate 1.1.0 homonymy, be used to control the alternately shake of cloth bag of said central dividing plate 1.1.0 both sides, the action of shake cylinder 1.1.5 is controlled by PLC.
Said upper shell 1.1 tops are connected with the two-way exhaust duct that is distributed in said central dividing plate 1.1.0 both sides; This two-way exhaust duct links to each other with nitrogen filtering device 2 through collecting pipe; Be respectively equipped with Pneumatic butterfly valve on the said two-way exhaust duct; When a described shake cylinder 1.1.5 began to move, the said Pneumatic butterfly valve of homonymy was closed, with the fine grained on each cloth bag of conveniently shaking off side.
Two semicircular plate body 1.2.1 that constitute said bed board are as the rotation Dump gate; It comprises: stacked up and down seat shape net 1.2.10 and punched-plate 1.2.11, the edge of seat shape net 1.2.10 and punched-plate 1.2.11 is fixed in the stacked closed semicircular ring of a pair of symmetry up and down.The closed semicircular ring that is in the below is connected on said rotating shaft 1.2.2 or the axle sleeve 1.2.3 through a plurality of reinforcement 1.2.7.
The top of said bed board is provided with the rabbling mechanism 1.2.0 that is used for refining, with homogeneous material, guarantees dry uniformity, and improves drying efficiency.
The middle part of contiguous said upper shell 1.1 is provided with a plurality of rupture pressure disc 1.1.1, to shift to an earlier date explosion when the superpressure, guarantees the security of whole system equipment.
Said electric driving mechanism preferred driven by servomotor mechanism or step motor drive mechanism.The structural principle of driving mechanism of surging is identical with pneumatic drive mechanism.
Claims (10)
1. a drying system comprises the fluidized drying main frame, and the fluidized drying main frame comprises upper shell, boiling-house and the lower shell of upper-lower seal connection successively; The boiling-house bottom is provided with bed board, it is characterized in that:
Said bed board is made up of the two boards body, and the neighboring edge of this two boards body is separately fixed in the sheathed each other rotating shaft and axle sleeve; The end of extending boiling-house of this rotating shaft and axle sleeve with drive respectively that this rotating shaft and axle sleeve rotate pneumatic, surge or electric driving mechanism links to each other.
2. drying system according to claim 1; It is characterized in that: the top at the neighboring edge place of described two boards body is provided with crossbeam; The lower surface of this crossbeam is provided with sealing strip; The sealing bar is suitable for when the bottom port of described two boards body sealing boiling-house, making the neighboring edge of said two boards body and said crossbeam realize being sealed and matched; The bottom end face of boiling-house is provided with sealing ring, and said sealing ring is suitable for making the remaining edge of described two boards body and the bottom port of said boiling-house to be sealed and matched.
3. drying system according to claim 1 is characterized in that: said rotating shaft and axle sleeve bearing cooperate, and said rotating shaft and axle sleeve constitute rotary seal with the auxiliary section of boiling-house wall body respectively and cooperate.
4. according to the described drying system of one of claim 1 to 3, it is characterized in that: the bottom port of said boiling-house is rounded, and described two boards body is the semicircle of symmetrical distribution.
5. drying system according to claim 4; It is characterized in that: two semicircular plate bodys that constitute said bed board comprise: stacked up and down seat shape net and punched-plate, the edge of seat shape net and punched-plate are fixed in the stacked closed semicircular ring of a pair of symmetry up and down; The closed semicircular ring that is in the below is connected on said rotating shaft or the axle sleeve through a plurality of reinforcements.
6. according to the described drying system of one of claim 1 to 3; It is characterized in that: the middle and upper part of interior, contiguous this upper shell of said upper shell is provided with central dividing plate; And a plurality of cloth bags of distribution and these central dividing plate both sides; Bottom opening in each cloth bag of said central dividing plate homonymy is fixed on the base fabric; Be distributed with the through hole that links to each other with the bottom opening of said cloth bag respectively on this base fabric, each base fabric is separately fixed on the waist shape ring of the dividing plate both sides that mediate, and is fixed with pressure bladder around each waist shape ring; Each pressure bladder after the inflation is suitable for making between each waist shape ring and the central dividing plate and between the inwall of each waist shape ring and said upper shell and is sealed and matched, so that the ascending air in the upper shell is only discharged through each cloth bag.
7. drying system according to claim 6; It is characterized in that: said upper shell top is connected with the two-way exhaust duct that is distributed in said central dividing plate both sides; This two-way exhaust duct links to each other with the nitrogen filtering device through collecting pipe, is respectively equipped with Pneumatic butterfly valve on the said two-way exhaust duct.
8. according to the described drying system of one of claim 1 to 3, it is characterized in that: the bottom of said upper shell is provided with spray gun, and the shower nozzle of this spray gun is located at the bottom centre place of said upper shell; This spray gun links to each other with the solvent carrier pipe with the elevated pressure nitrogen tracheae; The wall body of contiguous said upper shell bottom is provided with a plurality of pilot holes that are used to be provided with said spray gun that distribute up and down; Be used for selecting corresponding pilot hole for use, and the feed liquid that said spray gun is sprayed out is suitable for the interior material end face of said boiling-house of covering just according to the height of material in said boiling-house.
9. according to the described drying system of one of claim 1 to 3, it is characterized in that: be used for the dry heat exchanger of ebuillition of heated and comprise: the preheating unit of heat exchange unit that the multilayer upper-lower seal connects and the heat exchange unit below that is sealedly attached to bottom with gas; This preheating unit comprises the multilayer that upper-lower seal connects; The bottom air intake vent that is in the preheating unit of the bottom links to each other with the air outlet of said explosion-proof circulating fan;
The thermal medium inlet of each heat exchange unit links to each other with the saturated steam carrier pipe; The thermal medium outlet of each heat exchange unit is through linking to each other with the thermal medium inlet of each preheating unit behind the steam trap; The thermal medium outlet output condensed water of each preheating unit; This condensed water is sent back to boiler, regenerates the said saturated steam that is not less than 130 ℃.
10. according to the method for work of the described drying system of one of claim 1 to 3; It is characterized in that: said pneumatic drive mechanism comprises the connecting rod of the end of extending boiling-house of being fixed in said rotating shaft and axle sleeve, and this flexibly connects with the piston rod end of first, second rotational lock cylinder respectively the far-end of connecting rod;
The method of work of this drying system comprises: first, second rotational lock cylinder is successively controlled its action by PLC; And then control the alternately rotation successively of said rotating shaft and axle sleeve; And corresponding plate body is successively alternately overturn downwards; So that the material on the said bed board falls into said lower shell fully, and realize automatic continuous production.
Priority Applications (4)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410146923.8A CN103954098B (en) | 2012-04-06 | 2012-04-06 | Closed cycle, solvent are reclaimed and the method for work of spraying granulation drying system |
| CN201410144879.7A CN103954096B (en) | 2012-04-06 | 2012-04-06 | The method of work of drying system |
| CN201210099553.8A CN102620527B (en) | 2012-04-06 | 2012-04-06 | Drying system capable of realizing closed cycle, solvent recovery and atomizing granulation and working method thereof |
| CN201410146911.5A CN103954097B (en) | 2012-04-06 | 2012-04-06 | A kind of method of work of drying system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201210099553.8A CN102620527B (en) | 2012-04-06 | 2012-04-06 | Drying system capable of realizing closed cycle, solvent recovery and atomizing granulation and working method thereof |
Related Child Applications (3)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201410144879.7A Division CN103954096B (en) | 2012-04-06 | 2012-04-06 | The method of work of drying system |
| CN201410146923.8A Division CN103954098B (en) | 2012-04-06 | 2012-04-06 | Closed cycle, solvent are reclaimed and the method for work of spraying granulation drying system |
| CN201410146911.5A Division CN103954097B (en) | 2012-04-06 | 2012-04-06 | A kind of method of work of drying system |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN102620527A true CN102620527A (en) | 2012-08-01 |
| CN102620527B CN102620527B (en) | 2014-04-09 |
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Family Applications (4)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201410146923.8A Expired - Fee Related CN103954098B (en) | 2012-04-06 | 2012-04-06 | Closed cycle, solvent are reclaimed and the method for work of spraying granulation drying system |
| CN201210099553.8A Active CN102620527B (en) | 2012-04-06 | 2012-04-06 | Drying system capable of realizing closed cycle, solvent recovery and atomizing granulation and working method thereof |
| CN201410144879.7A Expired - Fee Related CN103954096B (en) | 2012-04-06 | 2012-04-06 | The method of work of drying system |
| CN201410146911.5A Expired - Fee Related CN103954097B (en) | 2012-04-06 | 2012-04-06 | A kind of method of work of drying system |
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| CN201410146911.5A Expired - Fee Related CN103954097B (en) | 2012-04-06 | 2012-04-06 | A kind of method of work of drying system |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105014063A (en) * | 2015-07-17 | 2015-11-04 | 中国兵器科学研究院宁波分院 | Spray granulation device suitable for active powder and granulation method thereof |
| CN105674698A (en) * | 2016-03-28 | 2016-06-15 | 全越 | Highly-sealed dehumidification drying mechanism |
| US11492300B2 (en) | 2016-12-27 | 2022-11-08 | Sabic Global Technologies B.V. | Drying a coating using electromagnetic radiation or heating of drum |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106214807A (en) * | 2016-08-04 | 2016-12-14 | 余庆县黔龙民族药业有限责任公司 | The processing technique of Fructus Evodiae |
| CN112556368B (en) * | 2020-12-07 | 2022-07-15 | 万川环境科技(广东)有限公司 | High-efficient drying equipment of quartz sand is used in optical lens piece production |
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| US4670993A (en) * | 1984-08-16 | 1987-06-09 | E.C.C. America Inc. | Method for fluidizing fine kaolin particles |
| CN101195147A (en) * | 2006-12-05 | 2008-06-11 | 亨特尔(天津)科技开发有限公司 | Movable self-tipping type quantitative sand charging device |
| CN102022895A (en) * | 2009-09-23 | 2011-04-20 | 吕江强 | Main machine of closed cycle boiling dryer |
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| US4601113A (en) * | 1985-04-26 | 1986-07-22 | Westinghouse Electric Corp. | Method and apparatus for fluidized steam drying of low-rank coals |
| JP4660150B2 (en) * | 2004-09-29 | 2011-03-30 | 中央化工機株式会社 | Vibration flow device |
| CN201281534Y (en) * | 2008-07-10 | 2009-07-29 | 吕江强 | Closed cycle boiling and drying unit |
| CN101776372B (en) * | 2010-01-28 | 2011-11-30 | 常州市星干干燥设备有限公司 | Nitrogen closed cycle drying and solvent recovery system |
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2012
- 2012-04-06 CN CN201410146923.8A patent/CN103954098B/en not_active Expired - Fee Related
- 2012-04-06 CN CN201210099553.8A patent/CN102620527B/en active Active
- 2012-04-06 CN CN201410144879.7A patent/CN103954096B/en not_active Expired - Fee Related
- 2012-04-06 CN CN201410146911.5A patent/CN103954097B/en not_active Expired - Fee Related
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4670993A (en) * | 1984-08-16 | 1987-06-09 | E.C.C. America Inc. | Method for fluidizing fine kaolin particles |
| CN101195147A (en) * | 2006-12-05 | 2008-06-11 | 亨特尔(天津)科技开发有限公司 | Movable self-tipping type quantitative sand charging device |
| CN102022895A (en) * | 2009-09-23 | 2011-04-20 | 吕江强 | Main machine of closed cycle boiling dryer |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105014063A (en) * | 2015-07-17 | 2015-11-04 | 中国兵器科学研究院宁波分院 | Spray granulation device suitable for active powder and granulation method thereof |
| CN105014063B (en) * | 2015-07-17 | 2017-03-29 | 中国兵器科学研究院宁波分院 | Suitable for the spray granulation plant of active powder |
| CN105674698A (en) * | 2016-03-28 | 2016-06-15 | 全越 | Highly-sealed dehumidification drying mechanism |
| US11492300B2 (en) | 2016-12-27 | 2022-11-08 | Sabic Global Technologies B.V. | Drying a coating using electromagnetic radiation or heating of drum |
Also Published As
| Publication number | Publication date |
|---|---|
| CN103954098A (en) | 2014-07-30 |
| CN103954096B (en) | 2015-11-25 |
| CN103954098B (en) | 2015-11-25 |
| CN103954097A (en) | 2014-07-30 |
| CN103954096A (en) | 2014-07-30 |
| CN103954097B (en) | 2015-11-25 |
| CN102620527B (en) | 2014-04-09 |
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