CN104789250A - Combined type internal rotation full-continuous refining equipment - Google Patents
Combined type internal rotation full-continuous refining equipment Download PDFInfo
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- CN104789250A CN104789250A CN201510222987.6A CN201510222987A CN104789250A CN 104789250 A CN104789250 A CN 104789250A CN 201510222987 A CN201510222987 A CN 201510222987A CN 104789250 A CN104789250 A CN 104789250A
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G1/00—Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal
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- Oil, Petroleum & Natural Gas (AREA)
- Life Sciences & Earth Sciences (AREA)
- Wood Science & Technology (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Screw Conveyors (AREA)
Abstract
The invention provides combined type internal rotation full-continuous refining equipment and relates to the technical field of refining equipment. The combined type internal rotation full-continuous refining equipment structurally comprises a plurality of reaction kettles which are flatly paved and are arranged in parallel, wherein a communication pipeline and a first packing auger shaft are arranged between every two adjacent reaction kettles, and the communication pipeline is used for communicating the two adjacent reaction kettles; each first packing auger shaft can be used for continuously feeding cracking materials into the other adjacent reaction kettle from one reaction kettle at a uniform speed, so that the blocking of each communication pipeline can be effectively prevented; with regard to sticky cracking materials, the equipment can be used for transforming the materials at a uniform speed, so that the cracking materials are prevented from coking and the cracking efficiency of the cracking materials is also improved. Compared with the up-down vertical and serial reaction kettles in the prior art, the plurality of reaction kettles which are serially connected in parallel can be conveniently assembled and overhauled, and a complicated supporting frame is not needed, so that the equipment cost is reduced; and meanwhile, the reaction kettles which are serially connected in parallel are not limited by heights and the relatively great capacity can be realized.
Description
Technical field
The present invention relates to refining equipment technical field, be specifically related to a kind of built-up type refining equipment for the oil refining of organic waste material.
Background technology
Current, the fast development of society makes the mankind create too much organic waste material, these waste materials abandoned not only cause the pollution of environment, and due to the energy containing a large amount of recoverable in waste material, also result in a large amount of wastes of the energy, thus in order to the recycling of environmental protection and the energy, people start design and can carry out cracking to organic waste material and obtain the refining equipment of energy recovery.
Traditional refining equipment is generally monomer-type reactor, monomer-type reactor is disposable can the limits throughput of cracking waste material, and fill too much waste material, extremely easily cause waste material cracking in reactor insufficient, and then cause energy recovery insufficient, and increase the volume of monomer-type reactor, the output value of refining equipment can be increased to a certain extent, but need very large power-equipment to go to drive the rotation of screw-conveyer-shaft in the rotation of reactor or reactor, and then add expending of the energy.For solving the problem, existing refining equipment is designed to knockdown, the energy recovery realizing waste material is combined by multiple reactor, the such as patent No. 2013201678342 discloses a kind of tire refining equipment, this refining equipment is cascaded from top to bottom by multiple reactor by connecting passage, multiple reactor is vertically arranged from top to bottom, due to the effect of gravity, be convenient to waste material falls to below reactor from the reactor of top to a certain extent, but, this exist following defect by waste material from the transfer mode that a reactor flows to another reactor by gravity: (1) this transfer mode is only adapted to non-toughness waste material, if waste material viscosity is higher or have coking phenomenon when scission reaction, just hold very much the blocking causing connecting passage, and then affect production process and production efficiency, (2) when waste material falls in another reactor from a reactor, waste material discontinuity is at the uniform velocity pounded on the waste material dropped that drops on above under universal gravity constant effect, be easy to cause waste material coking together, and then affect lysis efficiency, (3) vertical series multiple reactors together need more complicated bracing or strutting arrangement to support up and down, not only whole refining equipment to build engineering difficulty higher, and the stability of strutting system of whole refining equipment can not get effective guarantee, baroque bracing or strutting arrangement also adds additional equipment cost, (4) for ease of the at right angle setting up and down of reactor, the volume of reactor is traditionally arranged to be identical, and handiness is little, (5) vertical series built-up type refining equipment has certain limit height value up and down, that is, the production capacity value of the type refining equipment is also confined in certain volume range because of the restriction of height, and meanwhile, upper and lower vertically disposed reactor is also not easy to maintenance and the maintenance of equipment.(6) reactor overlaps, difficulty of heating, and the temperature of each reactor is different, causes reactor to expand with heat and contract with cold inconsistent, easily tears or be out of shape.
Moreover, existing refining equipment is generally the screw-conveyer-shaft rotation in the drive shaft Direct driver reactor of power drill/driver, because the length of screw-conveyer-shaft is longer, and moment of torsion is larger, be difficult to ensure that drive shaft has identical right alignment with screw-conveyer-shaft, be thus easy to the wearing and tearing causing drive shaft, even fracture, cause the damage rate of equipment higher, and then cause the increase of production cost.
Summary of the invention
The object of the invention is to provide one to be convenient to assembling, maintenance and operation for deficiency of the prior art, cost is low, can push waste material at the uniform velocity continuously, and is applicable to the built-up type refining equipment of large production capacity value.
Object of the present invention is achieved through the following technical solutions:
A kind of built-up type inward turning Total continuity refining equipment is provided, comprise several reactors tiling and be arranged side by side, be provided with connecting pipe between two adjacent described reactors, in described connecting pipe, be provided with the first screw-conveyer-shaft for cracking material to be pushed at the uniform velocity, incessantly another reactor be adjacent from a reactor.
Wherein, described connecting pipe is located at the bottom of described reactor and is located at the end of described reactor.
Wherein, the direction of propulsion of the cracking material in two adjacent described reactors is contrary.
Wherein, the discharge port of described reactor is communicated with the opening for feed of the reactor be adjacent by described connecting pipe.
Wherein, described reactor is built-in with the second screw-conveyer-shaft promoting cracking material and advance, and described second screw-conveyer-shaft is connected with the driven unit for driving described second screw-conveyer-shaft to rotate.
Wherein, described driven unit comprises the coupling shaft of driving mechanism and the drive shaft and described second screw-conveyer-shaft that are connected described driving mechanism, the first shaft coupling is provided with between described coupling shaft and described second screw-conveyer-shaft, be provided with the second shaft coupling between described drive shaft and described coupling shaft, described coupling shaft is provided with drive axle seat.
Wherein, described first shaft coupling is any one among flange form shaft coupling, multi-claw type shaft coupling, bolt-type shaft coupling and chain coupling.
Wherein, described second shaft coupling is any one among flange form shaft coupling, multi-claw type shaft coupling, bolt-type shaft coupling and chain coupling.
Wherein, described second screw-conveyer-shaft and described coupling shaft junction are provided with seal assembly, described seal assembly comprises the first seal cartridge be coated on outside described first shaft coupling, the end of described reactor is fixed in one end of described first seal cartridge, the other end of described first seal cartridge is fixed with the second seal cartridge, is filled with sealed packing filler in described second seal cartridge.
Wherein, the vergence direction of the propelling fin of the second screw-conveyer-shaft in two adjacent described reactors is contrary.
Beneficial effect of the present invention:
Built-up type refining equipment of the present invention, comprise several reactors be arranged side by side that tiles, connecting pipe and the first screw-conveyer-shaft being built in connecting pipe is provided with between two adjacent reaction stills, connecting pipe is communicated with two adjacent reactors, cracking material can be pushed to another reactor be adjacent by the first screw-conveyer-shaft at the uniform velocity, incessantly from a reactor, and then effectively can prevent the blocking of connecting pipe, especially for thickness cracking material, reach the function at the uniform velocity transmitting material, not only prevent the coking of cracking material, also improve the lysis efficiency of cracking material.Relative to the reactor of the vertical series up and down of prior art, some reactors of side-by-side series of the present invention are assembled and are overhauled all very convenient, and do not need complicated bracing frame, reduce equipment cost, the reactor of side-by-side series is not subject to the restriction of height and volume simultaneously, can to connect flexibly the reactor of different volumes, to realize large production capacity value.
Built-up type refining equipment of the present invention, also comprise connection second screw-conveyer-shaft in the coupling shaft of the drive shaft of driving mechanism, because coupling shaft is provided with drive axle seat, drive axle seat guarantees that coupling shaft and drive shaft have approximately uniform right alignment, and then reduce the wearing and tearing of drive shaft, improve the work-ing life of drive shaft, and then reduce equipment cost, and right alignment is identical can also improve transmission efficiency, reduce the energy waste in transmission process.
Accompanying drawing explanation
The invention will be further described to utilize accompanying drawing, but the embodiment in accompanying drawing does not form any limitation of the invention, for those of ordinary skill in the art, under the prerequisite not paying creative work, can also obtain other accompanying drawing according to the following drawings.
Fig. 1 is the perspective view of a kind of built-up type inward turning Total continuity refining equipment of the present invention.
Fig. 2 is the plan structure schematic diagram of a kind of built-up type inward turning Total continuity refining equipment of the present invention.
Fig. 3 is the structural representation of the reactor be connected with apparatus for feeding of the present invention.
Fig. 4 is the structural representation of the reactor adjacent with Fig. 3.
Include in Fig. 1 to Fig. 4:
1-reactor, 12-feed-pipe, 13-backup line;
2-second screw-conveyer-shaft, 21-advance fin;
3-driving mechanism, 31-drive shaft;
4-coupling shaft;
5-drive axle seat;
6-first shaft coupling;
7-second shaft coupling;
8-is communicated with assembly, 81-connecting pipe, 82-first screw-conveyer-shaft;
9-first seal cartridge;
10-second seal cartridge, 101-sealed packing filler;
11-heating furnace body.
Embodiment
The invention will be further described with the following Examples.
The embodiment of a kind of built-up type inward turning Total continuity refining equipment of the present invention, as depicted in figs. 1 and 2, comprise several reactors 1 tiling and be arranged side by side, the bottom of reactor 1 is equipped with the heating furnace body 11 for impelling cracking material cracking reaction in reactor 1 to reactor 1 heating, be provided with between two adjacent reaction stills 1 and be communicated with assembly 8, logical assembly 8 comprise connection two adjacent reaction stills 1 connecting pipe 81 and be built in connecting pipe 81 for by cracking material from a reactor 1 at the uniform velocity, push to the first screw-conveyer-shaft 82 of another reactor 1 be adjacent incessantly.
Cracking material can be pushed to another reactor 1 be adjacent by the first screw-conveyer-shaft 82 at the uniform velocity, incessantly from a reactor 1, effectively can prevent the blocking of connecting pipe 81, especially for thickness cracking material, reach the function at the uniform velocity transmitting material, the coking of cracking material can not only be prevented, also can improve the lysis efficiency of cracking material.Relative to the reactor 1 of the vertical series up and down of prior art, some reactors 1 of side-by-side series of the present invention are assembled and overhaul all very convenient, and do not need complicated bracing frame, reduce equipment cost, the reactor 1 of side-by-side series is not subject to the restriction of height and volume simultaneously, industrial scale can not only be adjusted flexibly, and larger industrial scale can be realized.
In the present embodiment, the built-up type refining equipment that multiple reactors 1 that side-by-side series is arranged form, cracking material progressively moves to the reactor 1 of built-up type refining equipment end in the reactor 1 at built-up type refining equipment top, the reactor 1 being positioned at this built-up type refining equipment top is provided with feed-pipe 12 and backup line 13, feed-pipe 12 is connected with apparatus for feeding, can continuously to reactor 1 feed, backup line 13 can be used for the inner case in observing response still 1, the reactor 1 being positioned at this built-up type refining equipment wherein end is provided with pipeline of slagging tap, the pollution-free material slag produced after cracking material cracking is discharged.
As shown in Figure 3 and Figure 4, reactor 1 is built-in with the second screw-conveyer-shaft 2 promoting cracking material and advance, second screw-conveyer-shaft 2 is connected with the driven unit for driving the second screw-conveyer-shaft 2 to rotate, it is more even that the rotation of the second screw-conveyer-shaft 2 makes cracking material be heated in reactor 1, prevent the caking of cracking material, and then improve scission reaction efficiency, and the second screw-conveyer-shaft 2 is provided with and advances fin 21, second screw-conveyer-shaft 2 drives and advances fin 21 to rotate the discharge port that material can not only be pushed into reactor 1 from the opening for feed of reactor 1, and cracking material can be made further to be heated evenly.
Due to, the discharge port of reactor 1 is communicated with the opening for feed of the reactor 1 be adjacent by connecting pipe 81, for making the length of connecting pipe 81 the shortest, be convenient to cracking material enters in another reactor 1 of being adjacent in a reactor 1, in reactor 1, the turning direction of the second screw-conveyer-shaft 2 is identical, the vergence direction of the propelling fin 21 of the second screw-conveyer-shaft 2 in two adjacent reaction stills 1 is contrary, thus makes the direction of propulsion of the cracking material in two adjacent reaction stills 1 contrary.
Push completely in a reactor 1 in another reactor 1 be adjacent for making cracking material, connecting pipe 81 is located at the end of reactor 1, and is located at the bottom of reactor 1, the still wall of connecting pipe 81 evagination bottom reactor 1.
As shown in Figure 3 and Figure 4, driven unit comprises the coupling shaft 4 of driving mechanism 3 and the drive shaft 31 and the second screw-conveyer-shaft 2 that are connected driving mechanism 3, be provided with the first shaft coupling 6 between coupling shaft 4 and the second screw-conveyer-shaft 2, be provided with the second shaft coupling 7 between drive shaft 31 and coupling shaft 4, coupling shaft 4 is provided with drive axle seat 5.
Drive shaft 31 is connected by coupling shaft 4 indirectly with the second screw-conveyer-shaft 2, because coupling shaft 4 is provided with drive axle seat 5, drive axle seat 5 can guarantee that coupling shaft 4 and drive shaft 31 have approximately uniform right alignment, and then reduce the wearing and tearing of drive shaft 31, improve the work-ing life of drive shaft 31, thus reduction equipment cost, and highly coaxially can also improve transmission efficiency, reduce the energy waste in transmission process.
Concrete, the first shaft coupling 6, second shaft coupling 7 all can be among flange form shaft coupling, multi-claw type shaft coupling, bolt-type shaft coupling and chain coupling any one.
Concrete, second screw-conveyer-shaft 2 is provided with seal assembly with coupling shaft 4 junction, seal assembly comprises the first seal cartridge 9 be coated on outside the first shaft coupling 6, the end of reactor 1 is fixed in one end of first seal cartridge 9, the other end of the first seal cartridge 9 is fixed with in the second seal cartridge 10, second seal cartridge 10 and is filled with sealed packing filler 101.The positiver sealing of the first seal cartridge 9 and the second seal cartridge 10 realization response still 1, and the flexible sealing having sealed packing filler 101 realization response still 1 of the second seal cartridge 10, the double seal that positiver sealing and flexible sealing combine, good seal performance, effectively can guarantee that the gas of reactor 1 does not leak.
Finally should be noted that; above embodiment is only in order to illustrate technical scheme of the present invention; but not limiting the scope of the invention; although done to explain to the present invention with reference to preferred embodiment; those of ordinary skill in the art is to be understood that; can modify to technical scheme of the present invention or equivalent replacement, and not depart from essence and the scope of technical solution of the present invention.
Claims (10)
1. a built-up type inward turning Total continuity refining equipment, it is characterized in that: comprise several reactors tiling and be arranged side by side, be provided with connecting pipe between two adjacent described reactors, in described connecting pipe, be provided with the first screw-conveyer-shaft for cracking material to be pushed at the uniform velocity, incessantly another reactor be adjacent from a reactor.
2. a kind of built-up type inward turning Total continuity refining equipment according to claim 1, is characterized in that: described connecting pipe is located at the bottom of described reactor and is located at the end of described reactor.
3. a kind of built-up type inward turning Total continuity refining equipment according to claim 1, is characterized in that: the direction of propulsion of the cracking material in two adjacent described reactors is contrary.
4. a kind of built-up type inward turning Total continuity refining equipment according to claim 1, is characterized in that: the discharge port of described reactor is communicated with the opening for feed of the reactor be adjacent by described connecting pipe.
5. a kind of built-up type inward turning Total continuity refining equipment according to claim 1, it is characterized in that: described reactor is built-in with the second screw-conveyer-shaft promoting cracking material and advance, described second screw-conveyer-shaft is connected with the driven unit for driving described second screw-conveyer-shaft to rotate.
6. a kind of built-up type inward turning Total continuity refining equipment according to claim 5, it is characterized in that: described driven unit comprises the coupling shaft of driving mechanism and the drive shaft and described second screw-conveyer-shaft that are connected described driving mechanism, the first shaft coupling is provided with between described coupling shaft and described second screw-conveyer-shaft, be provided with the second shaft coupling between described drive shaft and described coupling shaft, described coupling shaft is provided with drive axle seat.
7. a kind of built-up type inward turning Total continuity refining equipment according to claim 6, is characterized in that: described first shaft coupling is any one among flange form shaft coupling, multi-claw type shaft coupling, bolt-type shaft coupling and chain coupling.
8. a kind of built-up type inward turning Total continuity refining equipment according to claim 6, is characterized in that: described second shaft coupling is any one among flange form shaft coupling, multi-claw type shaft coupling, bolt-type shaft coupling and chain coupling.
9. a kind of built-up type inward turning Total continuity refining equipment according to claim 5, it is characterized in that: described second screw-conveyer-shaft and described coupling shaft junction are provided with seal assembly, described seal assembly comprises the first seal cartridge be coated on outside described first shaft coupling, the end of described reactor is fixed in one end of described first seal cartridge, the other end of described first seal cartridge is fixed with the second seal cartridge, is filled with sealed packing filler in described second seal cartridge.
10. a kind of built-up type inward turning Total continuity refining equipment according to claim 5, is characterized in that: the vergence direction of the propelling fin of the second screw-conveyer-shaft in two adjacent described reactors is contrary.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510222987.6A CN104789250A (en) | 2015-05-05 | 2015-05-05 | Combined type internal rotation full-continuous refining equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510222987.6A CN104789250A (en) | 2015-05-05 | 2015-05-05 | Combined type internal rotation full-continuous refining equipment |
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| CN104789250A true CN104789250A (en) | 2015-07-22 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201510222987.6A Pending CN104789250A (en) | 2015-05-05 | 2015-05-05 | Combined type internal rotation full-continuous refining equipment |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107537435A (en) * | 2016-06-24 | 2018-01-05 | 湖南力健机械有限公司 | A kind of Assembled rotary continuously cracks automatically and carbonizing apparatus |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN202226821U (en) * | 2011-06-09 | 2012-05-23 | 李艺 | Multi-stage combined electromagnetic heating pipe type continuous cracking refining reactor |
| CN202246580U (en) * | 2011-06-09 | 2012-05-30 | 李艺 | Electromagnet and fuel combined heating reactor for solid or liquid cracking |
| CN203295438U (en) * | 2012-12-17 | 2013-11-20 | 蔡民宝 | Tyre oil refining equipment |
| CN104327877A (en) * | 2013-07-22 | 2015-02-04 | 李艺 | Double-heating efficient energy-saving equipment possessing internal and external double kettles and used for cracking waste tyres, waste plastic and waste engine oil |
| CN204824733U (en) * | 2015-05-05 | 2015-12-02 | 湖南奔骥环保能源科技有限责任公司 | Modular internal rotation is continuous refining equipment entirely |
-
2015
- 2015-05-05 CN CN201510222987.6A patent/CN104789250A/en active Pending
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN202226821U (en) * | 2011-06-09 | 2012-05-23 | 李艺 | Multi-stage combined electromagnetic heating pipe type continuous cracking refining reactor |
| CN202246580U (en) * | 2011-06-09 | 2012-05-30 | 李艺 | Electromagnet and fuel combined heating reactor for solid or liquid cracking |
| CN203295438U (en) * | 2012-12-17 | 2013-11-20 | 蔡民宝 | Tyre oil refining equipment |
| CN104327877A (en) * | 2013-07-22 | 2015-02-04 | 李艺 | Double-heating efficient energy-saving equipment possessing internal and external double kettles and used for cracking waste tyres, waste plastic and waste engine oil |
| CN204824733U (en) * | 2015-05-05 | 2015-12-02 | 湖南奔骥环保能源科技有限责任公司 | Modular internal rotation is continuous refining equipment entirely |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107537435A (en) * | 2016-06-24 | 2018-01-05 | 湖南力健机械有限公司 | A kind of Assembled rotary continuously cracks automatically and carbonizing apparatus |
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Application publication date: 20150722 |