Source: https://patents.google.com/patent/KR19990081315A/en
Timestamp: 2020-08-11 14:32:46+00:00
Document Index: 59902911

Matched Legal Cases: ['art 120', 'art, 161', 'art 130', 'art 110', 'art 120', 'art 110', 'art 110']

KR19990081315A - Rubber Recycling Facility - Google Patents
Rubber Recycling Facility Download PDF
KR19990081315A
KR19990081315A KR1019980015175A KR19980015175A KR19990081315A KR 19990081315 A KR19990081315 A KR 19990081315A KR 1019980015175 A KR1019980015175 A KR 1019980015175A KR 19980015175 A KR19980015175 A KR 19980015175A KR 19990081315 A KR19990081315 A KR 19990081315A
KR1019980015175A
KR100309880B1 (en
1998-04-28 Application filed by 정인태 filed Critical 정인태
1998-04-28 Priority to KR1019980015175A priority Critical patent/KR100309880B1/en
1999-11-15 Publication of KR19990081315A publication Critical patent/KR19990081315A/en
2001-12-28 Application granted granted Critical
2001-12-28 Publication of KR100309880B1 publication Critical patent/KR100309880B1/en
229920001971 elastomers Polymers 0.000 title claims abstract description 93
239000005060 rubber Substances 0.000 title claims abstract description 93
238000004064 recycling Methods 0.000 title claims abstract description 15
239000002699 waste material Substances 0.000 claims abstract description 91
239000007789 gases Substances 0.000 claims abstract description 59
238000000859 sublimation Methods 0.000 claims abstract description 58
239000003921 oil Substances 0.000 claims abstract description 38
XEEYBQQBJWHFJM-UHFFFAOYSA-N iron Chemical group data:image/svg+xml;base64,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 data:image/svg+xml;base64,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 [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 claims abstract description 20
150000002430 hydrocarbons Chemical class 0.000 claims abstract description 13
239000003054 catalyst Substances 0.000 claims abstract description 9
238000000354 decomposition Methods 0.000 claims description 22
239000002912 waste gas Substances 0.000 claims description 2
239000002245 particles Substances 0.000 claims 3
238000004089 heat treatment Methods 0.000 abstract description 6
229920003051 synthetic elastomers Polymers 0.000 abstract description 5
OKTJSMMVPCPJKN-UHFFFAOYSA-N carbon Chemical compound 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[C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 abstract description 4
-1 and at the same time Substances 0.000 description 1
The present disclosure relates to a rubber waste recycling facility for recycling synthetic rubber waste such as waste tires without pollution.
The recirculation facility of the rubber waste of the present invention, the input unit 110 to continuously operate the plurality of bend 111, 112 and the opening and closing valve 113, 114 of the chipped rubber waste alternately. Wow; A catalyst initiation unit 160 mixed with the injected rubber waste to promote gas sublimation of hydrocarbons; A hollow sublimation part 120 of the circulation spaces 121c and 122c and the sublimation spaces 121a and 122a for decomposing hydrocarbon gas during screw transfer while heating the rubber wastes at low temperature with fruit oil; A condensing device (200) connected to the sublimation spaces (121a, 122a) for reconverting the sublimed cracked gas into a predetermined oil; A fruit oil supply device 140 for circulating and supplying the rubber waste to the fruit oil circulation space at a low temperature of about 220 ° C .; It is composed of a discharge unit 130 for enabling continuous discharge of the transport waste in conjunction with the input unit 110, in particular a vacuum control means for controlling the discharge between the input unit 110 and the discharge unit 130 It is taken.
The present invention obtains a sublimation gas in the process of transporting the rubber waste and re-reduction to condensation oil, to provide a re-reduction facility of the rubber waste to separate the carbon black, iron core and the like.
In the present invention, in the process of transferring rubber waste such as waste tires and synthetic rubbers into chips, heating is carried out at a low temperature of about 220 ° C. to sublimate hydrocarbons to obtain a recyclable liquid oil, and at the same time, carbon black (C Black) / B, weak) and the rubber core (Beat Wire, hereinafter referred to as iron core) and other additives (Filler Additive, hereinafter referred to as an additive).
In particular, in the process of subliming hydrocarbons from such rubber wastes, it promotes the sublimation of rubber wastes, and forms a vacuum control line of several orders of about 5,000 mm to smoothly discharge the sublimated hydrocarbon gas as well as the remaining rubber wastes, The present invention relates to a reclaiming facility for rubber waste having a sublimation promotion structure for promoting sublimation at the beginning of rubber waste sublimation.
Rubber waste treatment facilities by pyrolysis and various methods for treating or recycling rubber waste are well known.
Most of the facilities have the problem of air pollution by treating residual gas in the atmosphere, or the rubber wastes are dry-treated according to the rubber component to obtain a predetermined recyclable material, but due to many problems of the regeneration treatment structure, Failed to achieve its purpose.
The waste tires contain about 26-30% synthetic rubber, about 26% -29% C / B, about 25-30% additives, about 1% latex, and about 10-12% iron core. Generally, synthetic rubber, C / B and other additives are main components. The double synthetic rubber can be recycled to hydrocarbon oils as is known.
Such discarded rubber wastes contain such renewable raw materials, and have been proposed to separate or remove them by various devices, but have not been effectively separated for recycling.
The present invention is to promote the gas decomposition of the rubber waste in consideration of the structural problems appearing in the existing devices for recycling the rubber waste as described above, to prevent the air pollution by obtaining oil through the decomposition gas Its purpose is to provide a reclaiming facility for rubber waste, which provides a pollution-free facility, and allows the remaining residues to be recollected with C / B and iron cores.
In particular, the present invention provides a sublimation promoting structure for inputting the catalyst material simultaneously with preheating in order to ensure the gas decomposition process of the rubber waste in the rubber waste recycling facility as described above, sublimation and separation of the overall rubber waste It is a main object to provide a vacuum control structure for controlling to maintain a predetermined vacuum state so that the process can be smoothly discharged.
1 is an overall schematic block diagram of the rubber waste recycling facility of the present invention
Figure 2 is a schematic side view of the present invention rubber waste reduction facility
Figure 3 is a schematic plan view of the rubber waste recycling facility of the present invention
4 is a block diagram of an exploded portion of the reclaiming equipment of the present invention rubber waste
5A is an enlarged sectional view taken along the line A-A of FIG.
5B is an enlarged cross-sectional view taken along the line B-B in FIG.
※ Explanation of code for main part of drawing
100: decomposition device,
110: inlet, 111, 112: feeder, 113, 114: opening and closing valve
115,137: sight glass, 116,117: cover, 118: power unit, 119: transport means
120: sublimation unit, 121: preheat chamber, 121a: gas sublimation space, 121b, 122b: transfer screw
121c: fruit oil circulation space, 122: sublimation chamber, 122a: gas sublimation space,
122c: refrigerant circulation space, 123: cooling chamber, 123a: gas sublimation space, 123c: cooling space,
123d, 124: flexible joint, 130: discharge portion, 131, 132: discharge curve,
133,134,135,136: Opening and closing valve, 140: Refrigerant oil supply device, 140a: Oil supply pipe,
140b: oil pipe, 150: gasoline collection head, 160: catalyst start, 161: power unit,
162: opening and closing valve, 170: switching valve,
200: condenser,
210: condenser, 20: non-condensable gas tank, 230: pumping means, 240: condensed oil tank,
300: iron core and C / B (carbon black) separator,
310: screw power unit, 320: feed screw, 330: iron feed conveyor,
340: Separating hopper, 340a: Water chamber, 340b: Cooling pipe, 350: Lifting bucket
The above object of the present invention is a rubber waste input means for supplying the rubber waste to the chip, sublimation means for separating the gas while heating and transferring the injected rubber waste chip at low temperature, gas collection and condensation means, waste gas decomposed It is achieved as a discharge means for separating and discharging the iron core and C / B in the rubber residue.
The present invention is characterized in that the rubber waste input means and the discharge means are a plurality of whistle is discharged while continuously operating alternately for smooth supply, discharge of the rubber waste.
The present invention provides a plurality of on-off valves disposed above and below the inlet and outlet to discharge the rubber waste decomposed into carbon gas in a vacuum balance atmosphere while being maintained at a predetermined low temperature during the transfer of the rubber waste sublimation means. By controlling the operation as a predetermined vacuum pressure control device, the continuous movement of the rubber waste is smooth, and it is characterized by promoting the gas decomposition action and eliminating the poor discharge during the discharge transfer process.
Hereinafter, described in detail with reference to the accompanying drawings a preferred embodiment of the present invention.
In the accompanying drawings, Fig. 1 is a schematic block diagram showing the entirety of the rubber waste recycling facility of the present invention, and Fig. 2 is a schematic side view of the rubber waste recycling facility of the present invention.
Rubber waste reduction facility of the present invention according to the above drawings is composed of a decomposition apparatus 100, a condensation apparatus 200, an iron core and a C / B separation apparatus 300 as largely divided in FIG.
The rubber waste decomposing device 100 includes a rubber waste injecting unit 110 for injecting the supplied rubber waste as shown in FIG. 4 and a sublimation for decomposing gas while transferring the injected rubber waste to a predetermined temperature. Discharging the portion 120, the fruit oil supply device 140 for circulating and supplying the fruit oil, and the remaining residue from which the gas is discharged by a predetermined vacuum control line formed between the input unit 110 and Discharge part 130 is divided into.
More specifically, as shown in FIG. 2 and FIG. 4, the input part 110 is composed of a plurality of bends 111 and 112 alternately continuously operated for smooth supply of rubber waste. The bends 111 and 112 are provided with covers 116 and 117 that open and close automatically according to the input of rubber waste.
Each of the bends 111 and 112 is installed at the bottom of the bends 111 and 112 and the sensors a and b for controlling the supply and discharge of chipped rubber waste. On / off valves 113 and 114 interlocked by sensors (a) (b) (a ') (b') are provided. Below the on / off valves 113 and 114 is driven as a motor power unit 119 and a conveying means 118 for conveying rubber waste continuously discharged through the plurality of bends 111 and 112 is provided. . Each bend 111 and 112 has a viewing window 115 for visually checking the internal waste.
In addition, the on-off valves 113 and 114 constitute a vacuum control line together with the on-off valves of the discharge unit 130 to be described later, and can be controlled together independently or through the entire control line. In addition, the input unit 110 is a flexible joint 124 for coping with the fine expansion and contraction error of the preheating chamber 121 that is expanded and contracted finely by heating at the boundary with the sublimation unit 120 to be described later. Connect it.
As shown in FIG. 4, when the first bend 111 is discharged (in the direction of the arrow ①), the second bevel 112 is made of rubber. When the waste is supplied and discharge in the first bend 111 is completed, the second bend 112 is operated (arrow ② direction) to discharge and at the same time a continuous discharge operation of injecting rubber waste into the first bend 111 is performed. Is done. In the continuous discharge operation, the discharge state is detected and controlled by the sensors (b) and (b ') for detecting the discharge state of the rubber waste in each of the bends 111 and 112, and the filling state after the injection is the sensor (a) (a). ') To detect the over state of the rubber waste to open and close the cover (116, 117).
The sublimation part 120 includes a preheating chamber 121 and a sublimation chamber 122 installed below the input part 110 as shown in FIGS. 2, 3, and 4.
The preheat chamber 121 installs a transfer screw 121b in the gas sublimation space 121a and forms a fruit oil circulation space 121c divided into the outer portion thereof. The preheating chamber 121 receives the continuous supply of rubber waste from the bottom conveying means 118 of the plurality of bends 111 and 112 and transfers the rubber waste through the conveying screw 121b. At this time, the transfer screw 121b is a shaftless transfer screw, and the fruit oil is circulated and supplied through the fruit oil circulation space 121c for initial preheating.
The sublimation chamber 122 also forms a fruit oil circulation space 122c through which fruit oil circulates to the outside, and forms a sublimation space 122a in which a transfer screw 122b is installed on the inside, and a fruit oil circulation space 122c. The oil supply pipe 140a and the oil supply pipe 140b are connected to the fruit oil supply device 140 and are supplied while automatically controlling the temperature of the fruit oil at a predetermined temperature.
In addition, the cracked gas is transported along the gas pipe 152 in several exhaust holes 151 formed above the sublimation space 122a, as shown in FIGS. 4, 5A, and 5B. Is captured. The gas collecting head 150 collects a sublimation gas of hydrocarbon generated in each chamber of the sublimation unit 120 and is sent to a predetermined condenser 200 to be described later. The sublimation chamber 122 for such sublimation gas decomposition may be a multi-stage sublimation chamber of three or more stages.
As described above, the rubber waste being transported while being gas-decomposed through the sublimation unit 120 rises to about 50-60 ° C. from the initial input by the predetermined temperature of the fruit oil. Since the composite discharge of the iron core, C / B and other additives is cooled to a temperature around 160 ° C through the primary cooling unit 123 to the lower discharge 130.
The cooling unit 123 also has the form of a double tube. That is, the cooling space 123c is formed on the outside so that the outside air sucked from the blower is blown, and the conveying screw 123b is installed in the sublimation space 123a and the flexible joint 123d is installed at the bottom thereof. do.
Re-reduced materials of C / B, iron core, and other additives, which have been subjected to a predetermined gas separation through the sublimation unit 120, are lowered to a predetermined temperature through the cooling unit 123 and transferred to the discharge unit 130. .
The discharge unit 130 includes a plurality of discharge windows including a switching window 170 and several viewing windows 137 and a load detection sensor c) (d) (c ') (d'). 131, 132, and the on-off valves 133, 134, 135, 136, respectively installed in the upper and lower inlets and outlets of the discharge bend 131,132 to control the discharge continuously. Is done.
The complex structure of the on-off valves 133, 134, 135, 136 is by establishing a control line with the on-off valves 113, 114 of the input unit 110, a plurality of This is for alternating operation of the feeder and the chambers.
The on-off valves 133, 134, 135, and 136 have a series of rubber waste decomposition processes from the inlet unit 110 to the sublimation unit 120 and the outlet unit 130. Construct a series of control lines to achieve this.
The control line alternately opens and closes the outlet side on / off valves 113 and 114 of the plurality of feeders 111 and 112 on the input part 110 side, so that the continuous input of rubber waste is made. Together with the outlet side on-off valves 135 and 136, a predetermined vacuum discharge process is controlled together with the on-off valves.
At the same time, the loading height of the rubber waste re-reduced to the plurality of chambers by the sensors (c) (d) (c ') (d') for detecting the loading heights installed in the plurality of chambers (131, 132). Control.
For example, when the switching valve 170 is switched to flow in the discharge bend 131 direction, the on-off valve 133 is in the open position, the on-off valve 135 is in a closed state as the main decomposition cooling chamber ( Decomposed residues, C / B, iron core, and other substances discharged from 132a) continue to discharge toward the discharge curve 131, and form a cycle for receiving the residue until the upper sensor (a) is detected in the residue. At the same time, the other discharge bend 132 is the upper on-off valve 134 is closed and at the same time the lower on-off valve 136 is opened while the screw power unit 310 is installed at the bottom of the chamber to transfer the screw (320) While driving and discharging the residue to be discharged to the separator 300, the on-off valve 136 is closed by the detection of the lower chamber sensor (a ') and at the same time the upper on-off valve (134) by the closed state check sensor (d') ), And the upper switching valve 170 switches the discharge flow toward the discharge curve 132 as the opening state detection.
At the same time, the opening and closing valve 133 of the re-reduction materials positioned on the discharge bend 131 is closed while the opening and closing process of the lower opening and closing valve 135 is made, and at the same time, the transfer discharge is resumed as a transfer screw of the discharge bend 131. By taking the discharged residues alternately and allowing the discharged to be discharged by the continuous operation cycle to enable continuous operation to prevent backflow of the outside air.
In addition to the function of changing the flow direction of the waste, the switching valve 170 also serves to prevent the pinch of residues during the opening and closing valves 133 and 134 of the opening and closing valves 131 and 132.
Such a control system by evacuating the rubber waste is characterized by facilitating the transfer of the rubber waste in the sublimation unit 120, as well as the decomposition of hydrocarbons. In the vacuum discharge section, a separate vacuum pumping means (not shown) is installed to maintain and control a predetermined vacuum pressure, and at the same time to block backflow of external air.
On the other hand, the condensation structure after the decomposition gas generated in the gas decomposition process is as follows.
The trapped gas of the gas collecting head 150 is connected to a predetermined condenser 200 consisting of the condenser 210 and the non-condensable gas tank 220, the oil generated by the condensation in the condensing oil tank 240 Stored. At this time, the non-condensable gas is returned to a predetermined pressure condition to recondensate or reburn. The condenser 200 condenses the recovered hydrocarbons by making a vacuum to a plurality of condensers 210 through the vacuum turbine pumping means 230, and condensed hydrocarbons are not condensed or not condensed. Some of the condensation is condensed through the recondenser 210 and the remaining non-condensable gas flows into the combustion gas through the non-condensable gas tank 220.
The present invention is composed of a drive motor 161 and the open-opening valve 162 in order to start the gas decomposition of the rubber waste in the initial stage of the rubber waste input, the transfer path of the lower preheating unit 110 receives a predetermined decomposition promoting material The catalyst starter 160 for supplying the gas is installed. The catalyst initiation unit 160 is possible by mixing an appropriate amount of the catalyst material consisting of a predetermined component to the rubber waste being transported and mixed with the initial rubber waste.
This addition of catalyst material will promote the gas sublimation with the start of the sublimation of the gas in the gas decomposition process.
Residue discharged in such a vacuum atmosphere is separated into iron core and C / B through a predetermined recovery device. That is, the residues alternately discharged through the outlet valves 135 and 136 of the valve of the discharge unit 130 are separated into the iron core and the C / B through the iron core and the C / B separation device 300.
Iron core and C / B separation device 300 is composed of a screw power unit 310, the transfer screw 320, the auxiliary conveyor 330, the separating hopper 340 and the transfer bucket 350.
That is, the gas-resolved decomposition residue is transferred to the screw power unit 310 and the conveying screw 320 so that the C / B is sucked by the suction ventilation force of the separator 340 so that the conveying screw 320 is inlet side. As the outside air is sucked through the air supply hole formed in the cooling air, the C / B is transferred through the upper outlet while being cooled through the cooling space 340b between the water pipes 340a. This C / B is recycled through a predetermined process.
At the same time, the remaining residues (mainly iron cores) which are not lifted up are separated and transported as they are and are contained in the lifting bucket 350 through the iron transfer conveyor 330 and are transferred for a predetermined recycling process.
As described above, the present invention sublimes the cracked gas of rubber waste under a stable low temperature heating atmosphere, and thus, a conventional and complicated apparatus for treating rubber waste, which requires a complicated and difficult facility to remove slag in the second and third times at a high temperature of at least 450 ° C. The problems of the operation, and at the same time there is almost no problem of operation interruption due to frequent mechanical failures, especially the installation of the blast furnace, etc. improved the problems of the high heat treatment structure, the facilities of the pollution prevention structure due to the combustion of rubber waste Problems have been solved and rubber waste has been recycled and recycled in a clean state.
In the rubber waste recycling facility,
A rubber waste inlet which forms an on / off valve on the bottom of each bend such that rubber waste processed into chips is alternately supplied and discharged through a plurality of bends, and the rubber waste is continuously discharged through any one of the on / off valves;
In order to decompose and sublimate the predetermined hydrocarbon gas while preheating the injected rubber waste, the outside has a circulation space through which the circulating fruit oil is circulated, and the inside has a sublimation space connected to the gas collection line while the gas decomposition is performed. Sublimation part formed in a hollow;
An external air sucked from the blower is blown to form a predetermined cooling condition, and an inner side of the cooling unit is provided with a conveying screw to cool down to a predetermined temperature while transferring the rubber waste after sublimation; And
Recirculation of the rubber waste which includes a plurality of discharge bends for opening and closing the residues cooled and transferred from the cooling unit with the on / off valves of the inlet part, and each of the discharge bends includes upper and lower discharge parts respectively provided with opening and closing valves. equipment.
And a catalyst initiation unit connected to a predetermined catalyst material on the sublimation space of the preheating unit so as to promote gas decomposition during the sublimation action of the rubber waste.
And a vacuum control line for vacuum-controlling a series of rubber waste gas decomposition processes from the input part to the sublimation part, the cooling part, and the discharge part under a predetermined vacuum pressure.
Re-reduction of rubber waste material, characterized in that further comprising a decomposition gas condensation treatment device for connecting to the gas collection line of the sublimation unit for collecting and transporting the sublimed decomposition gas from the rubber waste and re-reduction treatment to a predetermined carbonized gas crude oil equipment.
Low temperature fruit oil is circulated along the circulation space of each chamber of the preheater and sublimation part, and the fruit is composed of a predetermined fruit oil supply structure, and a fuel pipe and an oil pipe connected thereto so that the rubber waste being transported is appropriately heated. Rubber waste reduction facility further comprises an oil supply device.
In order to separate the iron core and C / B from the residual rubber waste after gas decomposition discharged to atmospheric pressure from the discharge portion under the vacuum pressure,
A transfer screw for forming the C / B particles so that they can be lifted through the process of sucking the outside air;
A blower for sucking C / B particles along the sublimation space communicated from the inlet of the transfer screw;
Separating hopper which is installed at the upper end of the one side of the transfer screw, and formed a cooling tube through which the water chamber and the rising C / B particles pass through the sealed inside;
Re-reduction facility for rubber waste, characterized in that it further comprises an iron core and a C / B separation device made of iron core transfer means for transferring the residue, that is, the iron core to a predetermined place from which the C / B was removed.
The sublimation unit, the preheating chamber having a sublimation space having a preheating space and a transfer screw at the inlet side of the sublimation unit for the first preheating, sublimation of the rubber waste introduced into the input unit; And
It is connected to the exit of the preheat chamber to separate the gas from the rubber waste while transporting the rubber waste transferred from the preheating chamber to the second heat transfer, and surrounds the outside with a fruit oil circulation space and installs a transfer screw inside the rubber waste. A sublimation chamber for reclaiming rubber waste, characterized in that the sublimation chamber is formed to form a sublimation space in which an exhaust pipe for collecting decomposed gas is communicated while causing a sublimation action to be carried out.
Recycling equipment for rubber waste, characterized in that the sublimation chamber of the sublimation unit is at least two stages or more
The cracked gas condensation treatment device, Gas collecting head for temporarily storing the hydrocarbon gas decomposed from the sublimation unit;
A primary condenser for condensing hydrocarbon gas transferred from the gas collecting head to a predetermined pressure and converting the oil into oil;
A secondary condenser for condensing the gas having no primary condensation again;
A condensation oil tank for storing primary condensed oil;
A non-condensable gas tank for temporarily storing the non-condensable gas that has not been condensed through the secondary condenser and the condensing oil tank; And
And a pumping means for condensing the first and second condensers to a predetermined pressure.
KR1019980015175A 1998-04-28 1998-04-28 Recycling device for waste rubber KR100309880B1 (en)
KR1019980015175A KR100309880B1 (en) 1998-04-28 1998-04-28 Recycling device for waste rubber
KR19990081315A true KR19990081315A (en) 1999-11-15
KR100309880B1 KR100309880B1 (en) 2001-12-28
ID=37530871
KR (1) KR100309880B1 (en)
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