CN207577106U - Useless solid powder regeneration roasting system - Google Patents
Useless solid powder regeneration roasting system Download PDFInfo
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- CN207577106U CN207577106U CN201721395452.XU CN201721395452U CN207577106U CN 207577106 U CN207577106 U CN 207577106U CN 201721395452 U CN201721395452 U CN 201721395452U CN 207577106 U CN207577106 U CN 207577106U
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Abstract
The utility model belongs to containing inflammable or have the solid waste regeneration treatment technical field of taste liquid, propose useless solid powder regeneration roasting system, including sequentially connected preheating device, liquid gasification desorption apparatus, calciner, cooling device, the preheating device, the cooling device includes inside for material cavity and is provided at both ends with the cylinder of axle bed, the upper and lower part of the cylinder is respectively arranged with inlet port and outlet port, rotation heat exchange structure is provided in the material cavity, the rotation heat exchange structure includes the swivel being rotatably arranged in the axle bed, it is the venting cavity for being passed through heat-exchange gas inside the swivel, the venting cavity of the preheating device is connected with the venting cavity closed loop of the cooling device.The disposal options that the utility model is solved in the prior art containing flammable liquid He the solid powder for having taste solution only have the drawbacks of incinerator disposition cannot recycle solid constituent, and solve the problems, such as that serialization and heat largely lose in production process.
Description
Technical field
The utility model belongs to containing inflammable or have the solid waste regeneration treatment technical field of taste liquid, is related to a kind of useless
The particularly useless atlapulgite of solid powder, waste diatomite, useless attapulgite, filter sand, greasy filth, sludge, useless footwear material, waste tyre material
With roasting regeneration system.
Background technology
In the prior art give up solid powder particularly regenerated atlapulgite, regeneration waste diatomite, regenerated attapulgite,
When filter sand, greasy filth, sludge, useless footwear material, waste tyre material are disposed, kiln is selected to be burned mostly, without recycling
Liquid therein, such as after oil-containing waste diatomite is burned by incinerator, the solid powder that gives up carries out landfill disposal, does not both have back
Oil content therein is received, does not also have recycled product diatomite, wastes resource, causes very high energy waste, while existing is contained
The processing of inflammable debirs can only burn, and be unable to regeneration, even if having oil gas desorption apparatus carry out using be letter
Single preliminary oil gas utilizes, and later stage solid powder does not make full use of, is not carried out serialization.
Utility model content
The utility model proposes useless solid powders to regenerate roasting system, solves and contains flammable liquid in the prior art and have
The disposal options of the solid powder of taste solution only have the drawbacks of incinerator disposition cannot recycle solid constituent, and solve and produced
The problem of serialization and heat largely lose in journey.
What the technical solution of the utility model was realized in：
Useless solid powder regeneration roasting system, including
Sequentially connected preheating device, liquid gasification desorption apparatus, calciner, cooling device,
The liquid gasification desorption apparatus includes at least two electromagnetic heating conveying devices set gradually, and the electromagnetism adds
Heat transfer apparatus includes tilting or horizontally disposed conveying cylinder, and the top of described conveying cylinder one end is provided with regeneration feed
Mouthful, the lower part of one end be provided with regeneration discharge port, steam port is provided with out on the conveying cylinder, is set in the transport tube body
There are the conveying screw rod of inclination or level, the regeneration discharge port of an electromagnetic heating conveying device and another adjacent described electricity
The regeneration feed mouth connection of magnetic heating conveyor, the transport tube are provided with electromagnetic heating coil, the conveying screw rod in vitro
Including the body of rod, the body of rod is pierced by the conveying cylinder and is connect with motor, and helical blade is provided on the body of rod,
The preheating device, the cooling device include inside for material cavity and are provided at both ends with the cylinder of axle bed, institute
The upper and lower part for stating cylinder is respectively arranged with inlet port and outlet port, and rotation heat exchange structure is provided in the material cavity,
The rotation heat exchange structure includes the swivel being rotatably arranged in the axle bed, is for being passed through heat exchange inside the swivel
The venting cavity of gas, the venting cavity of the preheating device are connected with the venting cavity closed loop of the cooling device.
As further technical solution, the swivel includes the shaft section across the axle bed and the shaft Duan Lian
The boundling section that connects is arranged in the boundling section and for several tube banks of heat exchange, several points are provided in the tube bank
It falls apart, the shaft section is connect with motor, and the both sides of the cylinder are respectively arranged with gas inlet pipe and gas outlet pipe, the gas
Inlet pipe and the gas outlet pipe are arranged in the shaft section.
As further technical solution, between the shaft section and the axle bed between the gas inlet pipe and institute
It states and is both provided with airtight and watertight padding between gas outlet pipe.
As further technical solution, the setting direction of the dispersion plate turns the tangential direction rotated, institute to be described
It states and several through-holes is provided on dispersion plate.
As further technical solution, the top of the cylinder of the preheating device is provided with oil gas vent, the oil gas
Exit is provided with dedusting condenser system.
As further technical solution, the calciner is connect by sifter with the cooling device, the sieve
Divide on device and be provided with gas wash tower.
As further technical solution, the liquid gasification desorption apparatus cracking still or electromagnetic heater or fluid bed.
As further technical solution, the liquid gasification desorption apparatus is connected with dedusting condenser system.
It the utility model use principle and has the beneficial effect that：
1st, in the utility model, useless solid powder first passes through preheating device and is preheated, and is then desorbed by liquid gasification
Device except oil regeneration, finally roasted by calciner and recombinate the microscopic void opening in powder, remaining in hole
Organic matter oxidation of coal removes, and then carries out classification packaging after cooling device cooling, the high temperature after being roasting as key point
After when cooling device cools down, heat is absorbed by hot gas, hot gas is sent to preheating device and is preheated material, therefore entire
The process energy gets the efficient use, and the design of preheating device is increased before useless solid powder roasting after regeneration,
Solve the problems, such as that all the more energy and rate of roasting are slow, efficiency is low completing to consume by kiln well, together
When preheating device venting cavity of the heat source by rotation heat exchange structure in be passed through hot gas realization, hot gas can be completed by roasting
Product cools down discharged heat process to provide, therefore save the great energy afterwards, the heat that material needs cool down after roasting
Amount has also obtained effective utilization, while whole process is also simple and efficient very much, and material is entered to the material of cylinder by feed inlet
After in chamber, send to rotation heat exchange structure, good heat exchange is realized during rotation, turns and is rotated in axle bed, heat
Gas is dispersed to boundling section by boundling section, and boundling section can disperse heat well so as to which heat conduction reaches material to be preheated,
Boundling section is more parallel tubules, and good heat conduction effect is set as more increasing heat transfer efficiency if waveform, restrain simultaneously
On be provided with several dispersion plates, material can constantly be carried out dispersion stirring, be provided well for heat exchange by dispersion plate
Condition, while dispersion plate is corrugated sets so that rotation can drive more materials, therefore practical preheating every time
Effect is very good, and the temperature by material that can be quickly is preheated to 300 DEG C by 100 DEG C, so as to meet well needed for production.
2nd, it in the utility model, is both provided between gas outlet pipe between gas inlet pipe between shaft section and axle bed
Airtight and watertight padding ensure that solid, gas are shown in the efficient progress of heat exchange, and being provided with several through-holes on dispersion plate can be very good to improve
Heat exchange effect.
3rd, in the utility model, the dedusting condenser system of oil gas vent on the cylinder of preheating device, the sieve on calciner
Divide device and gas wash tower, ensure that cleanly production so that it is cleaner in working environment, realize good clear production, liquid
Body gasifies desorption apparatus cracking still or electromagnetic heater or fluid bed, so as to meet various solid powder regenerated atlapulgites,
Regenerate waste diatomite, regenerated attapulgite, filter sand, greasy filth, sludge, useless footwear material, the regeneration of waste tyre material and roasting process.
Description of the drawings
The utility model is described in further detail with reference to the accompanying drawings and detailed description.
FIG. 1 is a schematic structural view of the utility model；
Fig. 2 is preheating device structure diagram in the utility model；
Fig. 3 is to disperse plate structure schematic diagram in the utility model；
Fig. 4 is one example structure schematic diagram of liquid gasification desorption apparatus in the utility model；
Fig. 5 is the another example structure schematic diagram of liquid gasification desorption apparatus in the utility model；
In figure：1- preheating devices, 10- oil gas vents, 11- material cavities, 12- axle beds, 13- cylinders, 14- feed inlets, 15- go out
Material mouth, 16- rotation heat exchange structures, 161- swivels, 162- venting cavities, 1611- shaft sections, 1612- boundling sections, 1613- tube banks,
1614- dispersion plates, 1615- through-holes, 17- gas inlet pipes, 18- gas outlet pipes, 19- airtight and watertight paddings, 2- liquid gasification desorption apparatus,
21- electromagnetic heating conveying devices, 211- conveying cylinders, 212- regeneration feed mouths, 213- regeneration discharge ports, 214- go out steam port,
215- conveying screw rods, the 2151- bodies of rod, 2152- helical blades, 216- electromagnetic heating coils, 22- frame bodies, 3- calciners, 4- are cold
But device, 5- dedusting condenser systems, 6- sifters, 7- gas wash towers.
Specific embodiment
The following is a combination of the drawings in the embodiments of the present utility model, and the technical scheme in the embodiment of the utility model is carried out
It clearly and completely describes, it is clear that the described embodiments are only a part of the embodiments of the utility model rather than whole
Embodiment.Based on the embodiment in the utility model, those of ordinary skill in the art are without creative efforts
All other embodiments obtained shall fall within the protection scope of the present invention.
As shown in fig. 1~fig. 5, the utility model proposes useless solid powder regenerate roasting system, including
Sequentially connected preheating device 1, liquid gasification desorption apparatus 2, calciner 3, cooling device 4,
Liquid gasification desorption apparatus 2 includes at least two electromagnetic heating conveying devices 21 set gradually, if Fig. 1 is all
Electromagnetic heating conveying device 21 is obliquely installed, if Fig. 2 is that an electromagnetic heating conveying device 21 is obliquely installed, electromagnetic heating conveying
Device 21 includes tilting or horizontally disposed conveying cylinder 211, the top of 211 one end of conveying cylinder are provided with regeneration feed mouth
212nd, the lower part of one end is provided with regeneration discharge port 213, conveys and steam port 214 is provided with out on cylinder 211, conveys cylinder 211
Inside be provided with the conveying screw rod 215 of inclination or level, the regeneration discharge port 213 of an electromagnetic heating conveying device 21 with it is adjacent another
The regeneration feed mouth 212 of one electromagnetic heating conveying device 21 connects, and electromagnetic heating coil 216 is provided with outside conveying cylinder 211,
Conveying screw rod 215 includes the body of rod 2151, and the body of rod 2151 is pierced by conveying cylinder 211 and is connect with motor, and spiral shell is provided on the body of rod 2151
Vane piece 2152,
Preheating device 1, cooling device 4 include inside for material cavity 11 and are provided at both ends with the cylinder 13 of axle bed 12, cylinder
The upper and lower part of body 13 is respectively arranged with feed inlet 14 and discharge port 15, and rotation heat exchange structure is provided in material cavity 11
16, rotation heat exchange structure 16 includes the swivel 161 being rotatably arranged in axle bed 12, and 161 inside of swivel is for being passed through hot friendship
The venting cavity 162 of ventilation body, the venting cavity 162 of preheating device 1 are connected with 162 closed loop of venting cavity of cooling device 4.
In the present embodiment, as shown in Fig. 4~Fig. 5, liquid gasification desorption apparatus 2 is good for continous way materials recycling equipment
It solves the industry issue that original oil refining furnace needs one stove of a stove to produce, conservation process is become very simple,
Less people is only needed to safeguard, need to only continue feed just can be uninterrupted, and production efficiency has obtained great promotion, and increases
Automatic feeding just can realize automated production, this process is held by several inclined electromagnetic heating conveying devices 21
Continuous heat what is realized in conveying, the conveying cylinder 211 that edge tilts upward during conveying is delivered up to ensure the effective of material
Heating makes the electromagnetic heating effect of electromagnetic heating coil 216 also arrive good guarantee, conveys and is provided with out steaming on cylinder 211
Steam ports 214 can discharge excess steam, also provide good heating environment for conveying heating process.
Further, swivel 161 includes the shaft section 1611 across axle bed 12, the boundling section being connect with shaft section 1611
1612nd, it is arranged in boundling section 1612 and for several tube banks 1613 of heat exchange, restrains and be provided with several dispersions on 1613
Plate 1614, shaft section 1611 are connect with motor,
The both sides of cylinder 13 are respectively arranged with gas inlet pipe 17 and gas outlet pipe 18, and gas inlet pipe 17 and gas outlet pipe 18 are equal
It is arranged in shaft section 1611.
In the present embodiment, useless solid powder first passes through preheating device 1 and is preheated, then by liquid gasification desorption apparatus
2 except oil regeneration, finally roasted by calciner 3 and recombinate the microscopic void opening in powder, remaining in hole to have
Machine matter oxidation of coal remove, then cooling device 4 cooling after carry out classification packaging, as key point be roasting after high temperature object
After expecting that heat is absorbed by hot gas when cooling device 4 cools down, hot gas is sent to preheating device 1 and is preheated, therefore entire
The process energy gets the efficient use, and the design of preheating device is increased before useless solid powder roasting after regeneration,
Solve the problems, such as that all the more energy and rate of roasting are slow, efficiency is low completing to consume by kiln well, together
When preheating device heat source by be passed through in the venting cavity 162 of rotation heat exchange structure 16 hot gas realize, hot gas can be by roasting
Product cools down discharged heat process to provide, therefore save the great energy after the completion of burning, and material needs to drop after roasting
The heat of temperature has also obtained effective utilization, while whole process is also simple and efficient very much, and material enters to cylinder by feed inlet 14
After in the material cavity 11 of body 13, send to rotation heat exchange structure 16, good heat exchange is realized during rotation, turn
161 rotate in axle bed 12, and hot gas is dispersed to boundling section 1612 by boundling section 1612, and boundling section 1612 can be fine by heat
Dispersion reach material to be preheated so as to heat conduction, boundling section 1612 is more parallel tubules, and good heat conduction effect is set as wave
Heat transfer efficiency can more be increased if shape wave, while restrain and be provided with several dispersion plates 1614 on 1613, dispersion plate 1614 can
Material is constantly carried out dispersion stirring, good condition is provided, while dispersion plate 1614 is waveform for heat exchange
Setting to rotate every time and can drive more materials, therefore practical pre-heat effect is very good, can be quickly by object
The temperature of material is preheated to 300 DEG C by 100 DEG C, so as to meet well needed for production.
Further, it is respectively provided between gas outlet pipe 18 between gas inlet pipe 17 between shaft section 1611 and axle bed 12
There is airtight and watertight padding 19.
Further, the setting direction of dispersion plate 1614 is to turn the tangential direction of 161 rotations, is provided on dispersion plate 1614
Several through-holes 1615.
It is equal between gas outlet pipe 18 between gas inlet pipe 17 between shaft section 1611 and axle bed 12 in the present embodiment
Airtight and watertight padding 19 is provided with, ensure that solid, gas are shown in the efficient progress of heat exchange, several through-holes are provided on dispersion plate 1614
1615 can be very good to improve heat exchange effect.
Further, the top of the cylinder 13 of preheating device 1 is provided with oil gas vent 10, and dedusting is provided at oil gas vent 10
Condenser system 5.
Further, calciner 3 is connect by sifter 6 with cooling device 4, and gas wash tower 7 is provided on sifter 6.
Further, 2 cracking still of liquid gasification desorption apparatus or electromagnetic heater or fluid bed.
Further, liquid gasification desorption apparatus 2 is connected with dedusting condenser system 5.Connect the pre- of liquid gasification desorption apparatus 2
The conveying heating cage of thermal 1 can also connect dedusting condenser system 5, while keep it in normal pressure, negative pressure, the condition of tiny structure
It is lower carry out steam condensation, not only solve desorption out gas get into the air pollution environment the problem of, also completely recycling
Liquid component realizes resource regeneration.
In the present embodiment, the dedusting condenser system 5 of oil gas vent 10 on the cylinder 13 of preheating device 1, on calciner 3
Sifter 6 and gas wash tower 7, ensure that cleanly production so that it is cleaner in working environment, it realizes clean raw well
Production, 2 cracking still of liquid gasification desorption apparatus or electromagnetic heater or fluid bed, so as to meet various solid powder regenerated activity
The regeneration and roasting of carclazyte, regeneration waste diatomite, regenerated attapulgite, filter sand, greasy filth, sludge, useless footwear material, waste tyre material
Process.
The above is only the preferred embodiment of the utility model only, is not intended to limit the utility model, all at this
Within the spirit and principle of utility model, any modification, equivalent replacement, improvement and so on should be included in the utility model
Protection domain within.
Claims (7)
1. useless solid powder regenerates roasting system, which is characterized in that is taken off including sequentially connected preheating device (1), liquid gasification
Adsorption device (2), calciner (3), cooling device (4),
The liquid gasification desorption apparatus (2) includes at least two electromagnetic heating conveying devices (21) set gradually, the electricity
Magnetic heating conveyor (21) includes inclination or horizontally disposed conveying cylinder (211), described to convey the upper of cylinder (211) one end
Portion is provided with regeneration feed mouth (212), the lower part of one end is provided with regeneration discharge port (213), is set on the conveying cylinder (211)
Steam port (214) is equipped with out, the conveying screw rod (215) of inclination or level is provided in the conveying cylinder (211), described in one
The regeneration discharge port (213) of electromagnetic heating conveying device (21) and another adjacent described electromagnetic heating conveying device (21) are again
Raw feed inlet (212) connects, and electromagnetic heating coil (216), the conveying screw rod are provided with outside the conveying cylinder (211)
(215) including the body of rod (2151), the body of rod (2151) is pierced by the conveying cylinder (211) and is connect with motor, the body of rod
(2151) helical blade (2152) is provided on,
The preheating device (1), the cooling device (4) include inside for material cavity (11) and are provided at both ends with axle bed (12)
Cylinder (13), the upper and lower part of the cylinder (13) is respectively arranged with feed inlet (14) and discharge port (15), the material
Rotation heat exchange structure (16) is provided in chamber (11), the rotation heat exchange structure (16) is including being rotatably arranged on the axle bed
(12) swivel (161) in, the internal venting cavity (162) for for being passed through heat-exchange gas of swivel (161), the preheating
The venting cavity (162) of device (1) is connected with venting cavity (162) closed loop of the cooling device (4).
2. useless solid powder regeneration roasting system according to claim 1, which is characterized in that the swivel (161) includes
Shaft section (1611) across the axle bed (12), is arranged on institute at the boundling section (1612) being connect with the shaft section (1611)
It states in boundling section (1612) and for several tube banks (1613) of heat exchange, described restrain is provided with several dispersions on (1613)
Plate (1614), the shaft section (1611) connect with motor,
The both sides of the cylinder (13) are respectively arranged with gas inlet pipe (17) and gas outlet pipe (18), the gas inlet pipe (17) and
The gas outlet pipe (18) is arranged in the shaft section (1611).
3. useless solid powder regeneration roasting system according to claim 2, which is characterized in that the shaft section (1611) with
Sealing is both provided between the axle bed (12) between the gas outlet pipe (18) between the gas inlet pipe (17) to fill out
Expect (19).
4. useless solid powder regeneration roasting system according to claim 2, which is characterized in that the dispersion plate (1614)
Setting direction is the tangential direction for turning (161) rotation, and several through-holes (1615) are provided on the dispersion plate (1614).
5. useless solid powder regeneration roasting system according to claim 1, which is characterized in that the preheating device (1)
The top of cylinder (13) is provided with oil gas vent (10), and dedusting condenser system (5) is provided at the oil gas vent (10).
6. useless solid powder regeneration roasting system according to claim 1, which is characterized in that calciner (3) warp
It crosses sifter (6) to connect with the cooling device (4), gas wash tower (7) is provided on the sifter (6).
7. useless solid powder regeneration roasting system according to claim 1, which is characterized in that the liquid gasification desorption dress
It puts (2) and is connected with dedusting condenser system (5).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721395452.XU CN207577106U (en) | 2017-10-25 | 2017-10-25 | Useless solid powder regeneration roasting system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721395452.XU CN207577106U (en) | 2017-10-25 | 2017-10-25 | Useless solid powder regeneration roasting system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207577106U true CN207577106U (en) | 2018-07-06 |
Family
ID=62729290
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201721395452.XU Active CN207577106U (en) | 2017-10-25 | 2017-10-25 | Useless solid powder regeneration roasting system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN207577106U (en) |
-
2017
- 2017-10-25 CN CN201721395452.XU patent/CN207577106U/en active Active
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| Date | Code | Title | Description |
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| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20180706 Address after: 073000 No. 063, No. 5 road, renewable resources industrial base, North (Dingzhou), Dingzhou, Baoding, Hebei Patentee after: Hebei pecno limited use of renewable resources Address before: 050000 room 4, unit 2, 30 Huaxin Road, Qiaodong District, Shijiazhuang, Hebei, 401. Co-patentee before: Wei Shubin Patentee before: Kang Yongli |