CN205223114U - Totally closed integrated continuous type refining equipment - Google Patents
Totally closed integrated continuous type refining equipment Download PDFInfo
- Publication number
- CN205223114U CN205223114U CN201520720095.4U CN201520720095U CN205223114U CN 205223114 U CN205223114 U CN 205223114U CN 201520720095 U CN201520720095 U CN 201520720095U CN 205223114 U CN205223114 U CN 205223114U
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- cracker
- outward turning
- sealed tube
- preheater
- reactor
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Abstract
Totally closed integrated continuous type refining equipment, relate to refining equipment technical field, its structure includes evolute reation kettle, be equipped with in the evolute reation kettle along with its pivoted pre -heater, cracker and combustion chamber, the material becomes the material sediment and gets into the combustion chamber behind the cracker scission reaction, the material sediment burn produced heat and is used for heating cracker and pre -heater in the combustion chamber, the process of reation kettle external heating and the process that material reation kettle preheats have just so been removed from outward, it is compacter to make the refining equipment structure, reduce shared installation space, and the heat just flows to the pre -heater after heating the cracker, multistage utilization heat like this, thermal utilization ratio has been improved, additionally, the combustible that the material sediment has contained not only utilized it again after the burning in, the outer expense of purchasing fuel has been saved, greatly reduces cost, and make the thorough grey scorification of material sediment, it is innoxious, and can do usage such as building material, and then reach energy -concerving and environment -protective mesh.
Description
Technical field
The present invention relates to refining equipment technical field, be specifically related to a kind of Full enclosed integrated continuous rendering equipment carrying out refining oil for greasy filth, oil-sand and organic waste material.
Background technology
Current, along with the fast development of society, the demand of the mankind to the energy gets more and more, and existing fewer and feweri for mankind's energy directly, and for solving energy problem, the mankind have to exploit potential energy source and utilize energy recovery.
In the exploitation of potential energy source, it is found that oil-sand, greasy filth, resinous shale be all containing in a large number can deep fat material and store content very large, be convenient to exploitation.These type of energy such as oil-sand, greasy filth, resinous shale are called potential energy source by people, by refining equipment by can produce after further for these potential energy sources scission reaction a large amount of can deep fat material, these can deep fat material by further distillation, decompose gasoline, the diesel oil equal energy source that can obtain the mankind and can directly use.In energy recovery utilizes, discarded organic materials collects by people, such as old tire or plastics, and these organic waste material is carried out oil plant and the coke of cracking and then recovery organic waste material by refining equipment.As can be seen here, in the exploitation of potential energy source and energy recovery utilize, the available energy could be obtained after all needing to adopt refining equipment to carry out scission reaction to cracking material, but there is following shortcoming in existing refining equipment: (1) heating fuel heats it in the outside of reactor, such heat will directly be discharged after reactor heating from smoke exhaust barrel, not only make the utilization ratio of fuel heat low, also result in the waste of amount of heat; (2) cracking material is carried out cracking last as need to carry out preheating to cracking material, to evaporate moisture in cracking material and then to accelerate the abundant decomposition of cracking material when scission reaction, but existing preheating procedure is located at outside reactor, namely outside reactor, cracking material is heated in addition, cracking material after preheating needs handling equipment to send in reactor, this adds increased equipment cost, and complicate refining equipment and operation; (3) the material slag after scission reaction is directly got rid of, and has so just slatterned the combustiblesubstance in material slag, and also result in the pollution of environment; (4) also there is structure comparison dispersion in existing refining equipment, take installing space larger, and the production capacity of separate unit reactor is very little, be difficult to the scale reaching thousands of tonnage, economic benefit is low, and the oil length of general cracking material is not high, only has the refining equipment of large production capacity to form scale and benefit.
Summary of the invention
The object of the invention is to for deficiency of the prior art and provide one to avoid external heat, outer preheating, heat energy Multi-class propagation, energy-conserving and environment-protective can be made, lysis efficiency is high, Full enclosed integrated continuous rendering equipment that production capacity is large.
Object of the present invention is achieved through the following technical solutions:
Full enclosed integrated continuous rendering equipment is provided, comprise outward turning reactor, the preheater rotated with described outward turning reactor is provided with in described outward turning reactor, cracker, material until cracking enters described cracker after described preheater preheats, material becomes material slag and enters the combustion chamber being positioned at described outward turning reactor after described cracker cracking, the heat that described combustion chambers burn material slag produces is for heating described cracker and described preheater, described cracker is connected with the escape pipe stretching out described outward turning reactor, the cracked gas that material produces after scission reaction in described cracker is discharged through described escape pipe.
Wherein, the direction of propulsion of material in described preheater, cracker is contrary with the material direction of propulsion of slag in described outward turning reactor, the material slag after burning before discharge successively through described cracker, preheater so that the heat of expecting entrained by slag is carried out second-heating to described cracker, preheater.
Wherein, the vergence direction of the spiral guide plate in described preheater, cracker and the vergence direction of described outward turning reactor internal screw guide plate are in oppositely arranging.
Wherein, dust plate is equipped with between any two adjacent spiral guide plates in the spiral guide plate in described preheater, cracker, outward turning reactor.
Wherein, the first sealed tube entering described cracker for the material after preheating is provided with between described preheater and described cracker.
Wherein, described first sealed tube is arranged in the shape of a spiral, and the vergence direction of described first sealed tube is identical with the vergence direction of the spiral guide plate of described preheater.
Wherein, the second sealed tube is provided with in described outward turning reactor, described cracker is stretched in described second sealed tube one end, and the described second sealed tube the other end is located in described outward turning reactor, part in described outward turning reactor to be sent in described cracker through the high temperature material slag of burning.
Wherein, described second sealed tube is arranged in the shape of a spiral, and the vergence direction of described second sealed tube is identical with the vergence direction of the spiral guide plate of described outward turning reactor.
Wherein, the 3rd sealed tube arranged in the shape of a spiral is provided with outside described outward turning reactor, the vergence direction of described 3rd sealed tube is identical with the vergence direction of the spiral guide plate of described cracker, described cracker is stretched in described 3rd sealed tube one end, and the described 3rd sealed tube the other end is inserted into the combustion chamber in described outward turning reactor.
Wherein, described combustion chamber is provided with the first fixed tube for fixed combustion device and the second fixed tube for fixing gas blower, and the air-out direction of the gas blower in described second fixed tube is towards described cracker.
Beneficial effect of the present invention:
Full enclosed integrated continuous rendering of the present invention equipment, by by preheater, cracker and combustion chamber are all located in outward turning reactor, material becomes material slag and enters combustion chamber after cracker scission reaction, the heat that material slag produces in combustion chamber combustion is for cracker and preheater heating, so just eliminate the operation of reactor external heat and the operation of the outer preheating of material reaction still, make refining equipment structure compacter, installing space shared by minimizing, and heat just flow to preheater to after cracker heating, such Multi-class propagation heat, improve the utilization ratio of heat, in addition, material slag has not only re-used combustiblesubstance contained in it after burning, eliminate the expense of outsourcing fuel, greatly reduce cost, and make the thorough grey scorification of material slag, innoxious, and can the purposes such as material of construction be done, and then reach the object of energy-conserving and environment-protective.
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 structural representation of Full enclosed integrated continuous rendering of the present invention equipment.
Fig. 2 is the sectional structure schematic diagram in A-A direction in Fig. 1.
Fig. 3 is the structural representation at another visual angle of Full enclosed integrated continuous rendering of the present invention equipment.
Fig. 4 is the propelling schematic diagram of material and material slag in Full enclosed integrated continuous rendering of the present invention equipment.
Fig. 5 is the structural representation of outward turning reactor of the present invention.
Fig. 6 is the structural representation of cracker of the present invention.
Fig. 7 is the structural representation of preheater of the present invention.
Include in Fig. 1 to Fig. 7:
1-outward turning reactor;
2-driving mechanism, 21-speed-changing transmission device, 22-transmitting gear, 23-revolving gear;
3-support roller, 31-support circle;
4-preheater, 41-web plate, 42-first feed bin, 43-second feed bin;
5-cracker;
6-spiral guide plate, 61-dust plate;
7-band supporting plate;
8-conveying auger, 81-feed-pipe, 82-draining steam pipe;
9-first sealed tube;
10-second sealed tube;
11-the 3rd sealed tube;
12-combustion chamber, 121-first fixed tube, 122-second fixed tube;
13-escape pipe;
14-treats cracking material;
15-expects slag;
16-scoops up flitch;
17-expects slag landing plate;
18-adiabator layer;
19-first seal cartridge, 191-smoke exhaust pipe, 192-scum pipe;
20-second seal cartridge;
30-the 3rd seal cartridge;
40-the 4th seal cartridge;
50-lock packing.
Embodiment
The invention will be further described with the following Examples.
The embodiment of Full enclosed integrated continuous rendering of the present invention equipment, as shown in Figure 1, Figure 2 and Figure 4, the driving mechanism 2 that its structure comprises outward turning reactor 1 and drives outward turning reactor 1 to rotate, the revolving gear 23 that driving mechanism 2 comprises speed-changing transmission device 21, transmitting gear 22 and is fixed on outward turning reactor 1, speed-changing transmission device 21 drives revolving gear 23 to rotate by transmitting gear 22, and then drives outward turning reactor 1 to rotate.The bottom of outward turning reactor 1 is also provided with the support roller 3 playing whole outward turning reactor 1 weight for support, support roller 3 is stable by the support circle 31 being fixed on outward turning reactor 1 circumference, reliably support play outward turning reactor 1.In the present embodiment, support roller 3 is provided with two groups, has four.
Be provided with preheater 4 and cracker 5 in outward turning reactor 1, preheater 4 and cracker 5 are all fixed in outward turning reactor 1 by band supporting plate 7.As shown in Figure 3, preheater 4 is provided with three, and three preheaters 4 are connected and fixed by web plate 41 each other, three preheater 4 settings triangular in shape, to increase the fixing stability of preheater 4 and stability.Meanwhile, three preheaters 4 can increase preheating in the unit time and treat the total amount of cracking material 14, and make preheating more all efficiently even.In the present embodiment, preheater 4 is tubular preheater.The right-hand member of three preheaters 4 is connected with the first feed bin 42, the right-hand member of three preheaters 4 is connected with the second feed bin 43, first feed bin 42 connects the one end for carrying outside to treat the conveying auger 8 of cracking material 14, the other end of conveying auger 8 is provided with feed-pipe 81, treats that cracking material 14 is delivered in the first feed bin 42 continuously through conveying auger 8.Second feed bin 43 connects the right-hand member of cracker 5 by the first sealed tube 9, and the left end of cracker 5 connects the escape pipe 13 stretching out outward turning reactor 1, and the especially oil gas that material produces after scission reaction in cracker 5 is got rid of from escape pipe 13.The left end of cracker 5 also extend into the combustion chamber 12 being positioned at outward turning reactor 1, the left end of cracker 5 is also connected with the 3rd sealed tube 11,3rd sealed tube 11 one end is stretched in cracker 5,3rd sealed tube 11 the other end stretches in combustion chamber 12, material slag 15 in cracker 5 after cracking enters in combustion chamber 12 by the 3rd sealed tube 11, and the heat that combustion chamber 12 comburant (-rent) slag 15 produces is for heating pyrolyze device 5 and preheater 4.The expense of outsourcing fuel is not only saved in the burning of material slag 15, greatly reduces cost, and makes the thorough grey scorification of material slag 15, innoxious, and can do the purposes such as material of construction, and then reaches the object of energy-conserving and environment-protective.In addition, combustion chamber 12 and preheater 4 are all located in outward turning reactor 1, heating in realization response still, decrease the waste of heat, and heat just flow to preheater 4, such Multi-class propagation heat after heating cracker 5, improve the utilization ratio of heat, eliminate the preheating of the outer material of reactor simultaneously, make refining equipment structure compacter, the installing space shared by minimizing.
As shown in Figure 1 and Figure 4, the second sealed tube 10 is provided with in outward turning reactor 1, the right-hand member of cracker 5 is stretched in second sealed tube 10 one end, second sealed tube 10 the other end is located in outward turning reactor 1, in outward turning reactor 1 rotation process, material slag 15 in outward turning reactor 1 is sent in the right-hand member of cracker 5 by the second sealed tube 10, the material slag 15 being also in the condition of high temperature after burning with entered by the first sealed tube 9 in preheating tube treat that cracking material 14 mixes, reach the object that cracking material 14 is treated in second-heating and inside and outside two heating, the temperature of material is made to reach scission reaction temperature fast, and then raising lysis efficiency.
In the present embodiment, as direction indicated by arrow in Fig. 4, the direction of propulsion of material in preheater 4, cracker 5 advances from right to left, and expect what the direction of propulsion of slag 15 in outward turning reactor 1 advanced from left to right, as shown in Figure 6 and Figure 7, the vergence direction of the spiral guide plate 6 in preheater 4, cracker 5 is tilted to the left, as figure 5 illustrates, the vergence direction of outward turning reactor 1 internal screw guide plate 6 is tilted to the right, and is equipped with dust plate 61 between two adjacent spiral guide plates 6 in preheater 4, cracker 5, outward turning reactor 1.Dust plate 61 can prevent material coking in preheater 4, cracker 5, also make material be heated more even simultaneously, accelerate the efficiency of preheating and cracking, and dust plate 61 not only has the effect preventing from expecting that slag 15 is bonded together in outward turning reactor 1, and material slag 15 starts and is conducive to expecting that the heat in slag 15 distributes, to make full use of the heat of material slag 15 by dust plate 61.
In the present embodiment, first sealed tube 9, second sealed tube 10, the 3rd sealed tube 11 are arranged all in the shape of a spiral, because the first sealed tube 9 is treat that cracking material 14 is delivered in cracker 5, so the vergence direction of the first sealed tube 9 is tilted to the left by preheated in the second feed bin 43 with the rotation of outward turning reactor 1 automatically.Material slag 15 after outward turning reactor 1 combustion is sent in cracker 5 with the rotation of outward turning reactor 1 by the second sealed tube 10 automatically, and the vergence direction of the second sealed tube 10 is tilted to the right.Material slag 15 in cracker 5 is sent in combustion chamber 12 with the rotation of outward turning reactor 1 by the 3rd sealed tube 11 automatically, so the vergence direction of the 3rd sealed tube 11 is tilted to the left.3rd sealed tube 11 is around in outside outward turning reactor 1, effectively can prevent the coking in the 3rd sealed tube 11 of material slag 15, and the temperature that also can reduce material slag 15, to prevent from burning out the 3rd sealed tube 11, is also convenient to dredging and the maintenance of the 3rd sealed tube 11 simultaneously.
As shown in Figure 1 and Figure 4, the two ends, left and right of outward turning reactor 1 are equipped with the seal assembly for sealing outward turning reactor 1, the seal assembly being positioned at its right-hand member comprises the first seal cartridge 19 be connected with outward turning reactor 1 right-hand member and the second seal cartridge 20 be connected with the first seal cartridge 19, be filled with lock packing 50, first seal cartridge 19 with flexible sealing between first seal cartridge 19 and the outer wall of outward turning reactor 1 and be provided with the smoke exhaust pipe 191 for getting rid of the flue gas in outward turning reactor 1 and the scum pipe 192 for getting rid of the material slag 15 in outward turning reactor 1.Scum pipe 192 is connected with pinch flitch 16 being positioned at outward turning reactor 1 right-hand member by the material slag landing plate 17 be obliquely installed, scoop up flitch 16 and then the material slag in outward turning reactor 1 15 pinches is poured into material slag landing plate 17, material slag 15 enters scum pipe 192 along material slag landing plate 17 and then can expect that slag 15 be discharged.Conveying auger 8 enters in outward turning reactor 1 through the second seal cartridge 20, first seal cartridge 19 successively, also the effect that lock packing 50, second seal cartridge 20, first seal cartridge 19 reaches the double seal of rigidity and flexible sealing is filled with between second seal cartridge 19 and conveying auger 8.Conveying auger 8 is also provided with the draining steam pipe 82 for getting rid of the steam treated in lysate.
Outward turning reactor 1 left end is provided with connected 3rd seal cartridge 30 and the 4th seal cartridge the 40, three seal cartridge 30, the 4th seal cartridge 40 that are connected with the 3rd seal cartridge 30 also reach the effect of double seal.3rd seal cartridge 30 and and the outer wall of outward turning reactor 1 between be filled with lock packing 50.Escape pipe 13 passes combustion chamber 12, the 3rd seal cartridge 30, the 4th seal cartridge 40 successively and then stretches out between outward turning reactor the 1, four seal cartridge 40 and escape pipe 13 and is also filled with lock packing 50.Combustion chamber 12 is provided with the first fixed tube 121 for fixed combustion device and the second fixed tube 122 for fixing gas blower, first fixed tube 121, second fixed tube 122 is all fixed on the 3rd seal cartridge 30, wherein the air-out direction of gas blower is towards cracker 5, and then heat can be rushed at cracker 5, and then blow to preheater 4 again, realize the object of Multi-class propagation heat.
As shown in Figure 5, adiabator layer 18 is provided with in the barrel of outward turning reactor 1, spiral guide plate 6 in outward turning reactor 1 is fixed on the inner tube wall of outward turning reactor 1 through adiabator layer 18, and then adiabator layer 18 can be realized to be securely fixed on barrel simultaneously.
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. Full enclosed integrated continuous rendering equipment, comprise outward turning reactor, it is characterized in that: in described outward turning reactor, be provided with the preheater rotated with described outward turning reactor, cracker, material until cracking enters described cracker after described preheater preheats, material becomes material slag and enters the combustion chamber being positioned at described outward turning reactor after described cracker cracking, the heat that described combustion chambers burn material slag produces is for heating described cracker and described preheater, described cracker is connected with the escape pipe stretching out described outward turning reactor, the cracked gas that material produces after scission reaction in described cracker is discharged through described escape pipe.
2. Full enclosed integrated continuous rendering according to claim 1 equipment, it is characterized in that: the direction of propulsion of material in described preheater, cracker is contrary with the material direction of propulsion of slag in described outward turning reactor, the material slag after burning before discharge successively through described cracker, preheater so that the heat of expecting entrained by slag is carried out second-heating to described cracker, preheater.
3. Full enclosed integrated continuous rendering according to claim 1 equipment, is characterized in that: the vergence direction of the spiral guide plate in described preheater, cracker and the vergence direction of described outward turning reactor internal screw guide plate are in oppositely arranging.
4. Full enclosed integrated continuous rendering according to claim 1 equipment, is characterized in that: be equipped with dust plate between any two adjacent spiral guide plates in the spiral guide plate in described preheater, cracker, outward turning reactor.
5. Full enclosed integrated continuous rendering according to claim 1 equipment, is characterized in that: be provided with the first sealed tube entering described cracker for the material after preheating between described preheater and described cracker.
6. Full enclosed integrated continuous rendering according to claim 5 equipment, it is characterized in that: described first sealed tube is arranged in the shape of a spiral, the vergence direction of described first sealed tube is identical with the vergence direction of the spiral guide plate of described preheater.
7. Full enclosed integrated continuous rendering according to claim 1 equipment, it is characterized in that: in described outward turning reactor, be provided with the second sealed tube, described cracker is stretched in described second sealed tube one end, the described second sealed tube the other end is located in described outward turning reactor, to be sent in described cracker by the high temperature material slag of part after burning in described outward turning reactor.
8. Full enclosed integrated continuous rendering according to claim 7 equipment, is characterized in that: described second sealed tube is arranged in the shape of a spiral, the vergence direction of described second sealed tube is identical with the vergence direction of the spiral guide plate of described outward turning reactor.
9. Full enclosed integrated continuous rendering according to claim 1 equipment, it is characterized in that: outside described outward turning reactor, be provided with the 3rd sealed tube arranged in the shape of a spiral, the vergence direction of described 3rd sealed tube is identical with the vergence direction of the spiral guide plate of described cracker, described cracker is stretched in described 3rd sealed tube one end, and the described 3rd sealed tube the other end is inserted into the combustion chamber in described outward turning reactor.
10. Full enclosed integrated continuous rendering according to claim 1 equipment, it is characterized in that: described combustion chamber is provided with the first fixed tube for fixed combustion device and the second fixed tube for fixing gas blower, the air-out direction of the gas blower in described second fixed tube is towards described cracker.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520720095.4U CN205223114U (en) | 2015-09-17 | 2015-09-17 | Totally closed integrated continuous type refining equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520720095.4U CN205223114U (en) | 2015-09-17 | 2015-09-17 | Totally closed integrated continuous type refining equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205223114U true CN205223114U (en) | 2016-05-11 |
Family
ID=55898191
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520720095.4U Withdrawn - After Issue CN205223114U (en) | 2015-09-17 | 2015-09-17 | Totally closed integrated continuous type refining equipment |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205223114U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105087038B (en) * | 2015-09-17 | 2016-08-24 | 湖南奔骥环保能源科技有限责任公司 | Full enclosed integrated continuous rendering equipment |
| CN110756152A (en) * | 2019-11-29 | 2020-02-07 | 青岛伊克斯达再生资源有限公司 | External rotation type pyrolysis reaction kettle supporting wheel traveling mechanism and traveling method |
| CN110756152B (en) * | 2019-11-29 | 2024-05-31 | 十堰伊克斯达再生资源有限公司 | Supporting wheel traveling mechanism and traveling method of external rotation type pyrolysis reaction kettle |
-
2015
- 2015-09-17 CN CN201520720095.4U patent/CN205223114U/en not_active Withdrawn - After Issue
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105087038B (en) * | 2015-09-17 | 2016-08-24 | 湖南奔骥环保能源科技有限责任公司 | Full enclosed integrated continuous rendering equipment |
| CN110756152A (en) * | 2019-11-29 | 2020-02-07 | 青岛伊克斯达再生资源有限公司 | External rotation type pyrolysis reaction kettle supporting wheel traveling mechanism and traveling method |
| CN110756152B (en) * | 2019-11-29 | 2024-05-31 | 十堰伊克斯达再生资源有限公司 | Supporting wheel traveling mechanism and traveling method of external rotation type pyrolysis reaction kettle |
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|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| AV01 | Patent right actively abandoned |
Granted publication date: 20160511 Effective date of abandoning: 20160824 |
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| C25 | Abandonment of patent right or utility model to avoid double patenting |