TWI353922B - - Google Patents

Description

1353922 IX. Description of the Invention: [Technical Field] The present invention relates to a composite material thermal cracking integration system, in particular to a method for completely recovering gaseous, liquid, and solid products generated during thermal cracking of a substance. , refining and processing composite material thermal cracking integration system. [Prior Art] The technology of thermal cracking has been developed for many years. In recent years, new developments have mainly been applied to waste treatment fields, such as the treatment of waste tires. Xi 2 The recycling method of waste tires can be roughly divided into two ways. The first one is purely and physically treated. The main waste tire is cut into pieces by coarse and fine crusher, and steel is separated. Circles, however, after the waste tires are cut into pieces, the recycling capacity that can be carried out subsequently is limited, and Yifa is used as a raw material for the production of tires, so the efficiency of recycling and reuse is utilized. The first '-seeds are treated in the chemical side-V 1 , 》 τβ» _ learning method, mainly to recycle the waste tires through the coarse and fine breaking machine ‘ 1V I β 1 cPvr. 】 After cutting into pieces, 're-cracking. (y iySls) program, the thermal cracking system is put into a cracking furnace, and mixed into the $u砰 block and mixed into a proper proportion of the catalyst to keep it in the image & 23 〇度", the temperature between the cracking furnace of 400 ° C, the pressure in the cracking furnace of the 抻 保持 system keeps the 2.5 2.5 2.5 2.5 2.5 2.5 2.5 2.5 2.5 2.5 2.5 2.5 2.5 2.5 2.5 2.5 2.5 2.5 2.5 2.5 2.5 2.5 2.5 2.5 2.5 2.5 2.5 2.5 2.5 2.5 2.5 2.5 2.5 2.5 2.5 2.5 2.5 2.5 2.5 2.5 2.5 2.5 2.5 2.5 2.5 2.5 2.5 2.5 2.5 2.5 2.5 2.5 2.5 2.5 In the middle, the copper wire field cracks out the steel wire with 4 economic value products, and the steaming crane out gas 5 丄 is 3922 iw: the raw material f in which the cracked oil can be further subjected to fractionation, separating the hydrazine and carbon hydrazine, gasoline, Kerosene, diesel and other products with high economic value, ... then activated carbon raw materials, can also be used as rubber, dyes and steel wire can also be supplied to steel mills as raw materials. The technology for recycling waste tires has been eliminated, 'but the gaseous products produced in the thermal cracking process, or the dust. 2 suspended particles are still unable to be effectively treated, except for the waste of resources. The product contains = Harm to the human body; currently known to carry out thermal cracking procedures:, the overall structure of the cracking system, including system power supply, thermal cracking process, useful thermal cracking product recovery, useless thermal cracking Matters: Emissions and other related processing equipment are not complete, and there is no good integration. Therefore, how to make the overall structure of the thermal cracking system more perfect, so that: better, more diversified Application 'is an important subject in the field of thermal cracking recovery. SUMMARY OF THE INVENTION The main object of the present invention is to provide a composite material thermal cracking integration system that can recover, analyze and thermally crack substances in a thermal cracking procedure. The solid, liquid, gaseous, flammable, non-flammable products produced in the program are complete or discharged, and environmentally friendly. The present invention is a composite material thermal cracking integration system. The system architecture includes There is a thermal cracking unit, a material processing unit, a dust collecting unit, a filter discharge unit, and an energy supply unit. 6 1353922

k V The thermal cracking early element contains a new secret ^, "solution furnace", the cracking furnace has - cracked to, it can be used for the recovery of the solution (4) #直入-cracking into the medium for thermal cracking procedure; The unit is connected to the cracking 榼^ — the furnace is used to generate the gaseous state generated when the to-be-recycled material is subjected to the orbital cracking process, and is flammable or not, and the dust collecting unit is connected to the cracking furnace. It is used to filter the suspended particles generated in the thermal cracking process, avoiding the four plates of the basin to avoid blood pollution and polluting the environment; the filter discharge unit can be connected to the cesium cracking single opening, such as..., the polymerization solution 70, the material processing unit And the dust collecting element is used to discharge and discharge non-recyclable substances generated in the thermal cracking process; the energy supply unit uses solar energy, wind power, hydropower natural energy to generate electricity, and generates hydrogen after electrolysis of water, children, and even people. The tail gas is combined with the pollution-free oxyhydrogen flame energy generated by the combustion engine to supply the energy required for the operation of each unit, and it can be used in the cracking chamber exhaust pipe of the cracking furnace. Mann set - gas turbine generator, and with an external auxiliary power source such as an engine generator power 'required for the operation of the supply system. The system can be used in a cracking furnace or a plurality of cracking furnaces in parallel, and the cracking furnace can be an electric pyrolysis furnace or a hot gas cracking furnace. The electrothermal cracking furnace uses a hot plate to pass current to generate thermal cracking. The heat energy required for the procedure' while the gas cracking furnace utilizes an externally supplied flammable gas or liquid 'heated gas generated by ignition as a heat source', although the source of heat energy is different 'both are transmitted through the cracking chamber Heating, so that the solid, liquid, flammable, or non-combustible material to be recovered in the cracking chamber is subjected to thermal cracking. The material processing unit may comprise a vacuum fruit pump connected to the cracking chamber, and the material to be recovered in the cracking chamber is flammable. Then, the gaseous product produced after the thermal cracking process can be condensed by a vacuum pump and condensed into a flammable liquid through a condensation 7 1353922, and then stored in a combustible liquid storage tank, and the combustible liquid can also be purely combustible by the oil water separator. The liquid is then stored in the flammable liquid storage tank; if it is not condensed into a liquid flammable gas after being condensed by the condenser, it can be sent to a main burner or an auxiliary The auxiliary burner of the combustion device is ignited and burned into hot gas as a heat source for the gas cracking furnace. If the to-be-recycled material is non-flammable, the gaseous product that can be recycled after thermal cracking can be pumped out through a vacuum pump and condensed through a condenser, and stored in a non-flammable liquid storage tank, which cannot be recycled. The gaseous product can be directly discharged to the filter unit after being exhausted in the cracking chamber, or sent to the combustion chamber of the auxiliary combustion device and the gas chamber of the main burner for combustion and disinfection, and then sent to the filter unit for discharge. After the completion of the thermal cracking process, the residual liquid substance can be transported to a liquid storage tank through a liquid material discharge pipe disposed at the bottom of the cracking chamber, and the remaining solid matter can be taken out through the take-out device to open the crack for removing the solid matter. When the furnace cover is used, the dust collection unit can be started to collect dust to prevent dust, smoke and steam from overflowing, and the filtered air is sent to the filter discharge unit for filtration and discharge; and the heat is generated in the cracking furnace. The hot gas used in the cracking process can also be sent to the filter discharge unit for disposal after use. ° In addition, a hydrogen-oxygen generator can be arranged in the energy supply unit to electrolyze water into hydrogen gas, A gas, and ignite the generated hydrogen gas and oxygen gas as a non-polluting hot gas source of the gas cracking furnace. . The gas cracking furnace can also be combined with a main burner to burn fuel, such as externally input flammable gas, flammable liquid or hydrogen and oxygen generated by the oxyhydrogen generator to generate heat 8 1353922 gas supply The thermal energy required to perform the thermal cracking procedure. The composite material thermal cracking integrated system of the invention can recover the material by a thermal cracking process, and complete the recovery of the solid, liquid, gaseous, combustible and non-combustible products generated in the thermal cracking process. Emission treatment, which uses the power supply required for the operation of the self-produced and natural energy supply system, and also achieves the energy-saving effect, and the useless substances generated in the thermal cracking process can be filtered and discharged through the dust suction unit and the filter discharge unit. With environmental protection effect, it is a complete solution that is different from the traditional thermal cracking system, which can recycle the waste to be recycled and extract the useful materials. [Embodiment] "Month Referring to Figures 1 to 2 and Figures 5 to 7, the composite material thermal cracking integration system of the present invention comprises: a thermal cracking unit (B) comprising a cracking furnace (BS) (BE) 'The cracking furnace (BS) (BE) is used to carry out the thermal cracking process of the to-be-recovered material, which comprises a furnace body with a - opening - (B 13) - the outer furnace body (B 1 1 ) is coated with The outer side wall of the inner furnace body (B 1 3) and the furnace cover (B〇) are disposed at the opening σ of the inner furnace body (B13), and the inner furnace body (Β 13) is a cracking t (Β3) for the capacity The retentate is set to be a heating space between the outer furnace body and the inner furnace body (Β丄3) for accommodating the heating element to heat the cracking chamber (B 3 to be reclaimed, wherein The heating element may be a hot gas, a hot plate, etc., on the inner side wall of the outer furnace body (B 1 1 ) and provided with a heat insulation layer (B丄2) to provide a heat insulation effect 9 1353922 The heat energy of the heating body is lost, and the surface temperature of the outer furnace body (B11) is prevented from being overheated;

- the material handling unit (c), connected to the cracking furnace (BS) (BE), for subsequent treatment of the gaseous products produced in the thermal cracking process according to their flammability or not; a dust collection tg(D) , connected to a cracking furnace (BS) (BE) for taking into account the suspended particles generated in the thermal cracking process, - filtering the discharge unit (E), connecting to the thermal cracking unit (B), and the material handling unit ( C), and at least one of the three units, such as the dust collection unit, for filtering and discharging the non-recyclable material generated in the thermal cracking process; and - the energy supply unit (A) for opening From the supply of energy required for the operation of each early π, the above cracking 5) and one; the temperature of the external temperature delivered to the cracking too high can be cooled by the cracking, dust collecting unit step, one ~,, eight τ 阖Λ

Furnace (BS) (BE) is provided - the cracking chamber inlet pipe cracking chamber exhaust pipe (T6) is connected to the cracking chamber (B lower gas or liquid can be injected into the cracking chamber (τ chamber (Β3)) Moderately reduce the cracking chamber (6 j ; and the gaseous generating chamber exhaust pipe (T6) generated in the thermal cracking process is sent to the material processing unit (D) or the filtration discharge unit (ε) for clearing , recycling, or discharge treatment. Please refer to Figure 15 and Figure 22, A, Β, 16th Α The above cracking furnace (B s ) ' Β , twentieth (Β Ε ) still 10 1353922 comprises a helix leaf picking device (B 5 〇) comprising a drive motor (B52) and a helix leaf mechanism (B51) (B57) 'the drive motor ( B52) is disposed at an opening of the furnace body (B13) adjacent to the cracking furnace (BS) (BE), the spiral vane mechanism (B 5 ] ) (B 5 7 ) is disposed in the cracking chamber (b 3 ), and one end is connected To the drive motor (B 5 2 ) and to drive the rotation of the drive motor (3) 52) to agitate the material to be recovered in the cracking chamber so that it can be uniformly thermally cracked; (B5 1 ) may have a plurality of blade groups arranged side by side, each of which rotates around the same fixed axis to impart a to-be-recovered material. The spiral blade mechanism (B 5 7) may also have only a single blade group, and The blade group can be moved in the vertical direction in addition to the rotation of a certain axis to uniformly stir the to-be-recovered material. Referring to the twenty-third figure, the above-mentioned cracking furnace (BE) may or may not be provided with a spiral leaf mixing device. (B5〇), and a magnetic type two-way (B5〇') is provided, and the magnetic mixing device (B5〇 includes: an electric motor (B54), a magnetic steel piece (B55), and a magnetic stirring Dropper (B53), the motor (B54) is disposed under the inner furnace body 13), the magnet steel month (B55) is disposed under the inner furnace body and is connected to the power output of the motor (B54), which is an electric motor (B) 5 4) The rotation is driven, and a magnetic search is generated when rotating... 3) Set in the cracking chamber (B3) = the rotating magnetic field generated by the rotation of the magnetic steel sheet (B55), driven by stirring The material to be recovered in the chamber (B 3 ) is allowed to be uniformly pyrolyzed; the magnetic picker (B53) can be an ellipse Iron, covered with iron gas dragon 11 1353922 or other high temperature resistant, wear resistant, chemical resistant, plating. In a hurry, the monthly washing of dirty materials, please refer to Figure 14A, Β and twentieth - τ map, above The bottom of the cracking 姨 (BS ) ( ΒΕ ) can still be set to $ 煜

The material discharge tube (T) is connected to a liquid storage tank (S 1 ) for the completion of the hot distillation process of the acupoint to complete the discharge of the liquid substance remaining in Germany by the liquid substance. Answer rc , , , w , 1 7 ) Flow into the liquid storage tank (S 1 ) to facilitate subsequent recycling. Please refer to Figure 17A, B, 18th and 2nd + 4th Α, Β and 25th Α, Β 'The above cracking furnace (BS) (Β E) can also be equipped with a take-out device (B6 〇) (b device (Been (B70) has various implementations. "Remove, please refer to Figure 17A, only Fenchu-Kenting a, B and the first fourteen A, b, In the first embodiment of the extraction device (B6〇3 - 丄 丄 厶 厶 衮 衮 衮 衮 衮 衮 衮 衮 衮 衮 第一 第一 第一 第一 第一 第一 第一 第一 第一 第一 第一 第一 第一 第一 第一 第一 第一 第一 第一 第一 第一 第一 第一 第一 第一 第一 第一 第一 第一 第一 第一 第一(BS) (BE) outside the furnace body (Βι " sidewall with grooved inside the furnace H (B 1 3) side wall is also provided with a groove corresponding to the outer furnace body (B11) through the groove 'the removal 帛 ( B6 " can be laterally moved in the through groove of the outer furnace body (B11) in the inner furnace body (B13), and can selectively enter and exit the cracking chamber (B3), and the driving motor (B62) is connected to the take-out frame 1 ) - End 'provided the removal rack (B62) to remove the 'solid matter remaining in the cracking chamber after the completion of the thermal cracking procedure' operable extraction device (B6〇). See the eighteenth figure A, B and Twenty-fifth Figure A, B In the second embodiment of the take-out device (B 7 0, - ^ ', the take-up device (B7 12 1353922 0) includes a take-up frame (B7l) '-drive motor (b72), push frame (B73) , push-pull motor (B74), dust cover (B 75), and a dust suction pipe (D8), and the bottom of the furnace body (B1 3) in the cracking furnace (b E) is provided with a groove, the outer furnace The bottom of the body (B1) is also provided with a groove corresponding to the bottom of the inner furnace body, and the take-up frame (B 71) can be longitudinally moved to be worn in the inner furnace body (B13) and the outer furnace body (B11). In the tank, and selectively entering and leaving the cracking chamber, the driving motor (B72) is connected to the take-out "β7ι) end to provide: : the power of the rack (B 7 1 ) to move, the push frame (B 7 3 ) can be laterally = Grounded below the cracking furnace (BS) (BE), the pusher motor: 'b connected to the push frame (B73) - end, providing the power of the push frame (B73), when the 帛 (B71) is removed, Go, and when the main pre-south is south, ' = ( Β 7 4) can drive the push frame (M3) to traverse, and the material = Chuan's solid matter is pushed to the 1 car (shipped by the car (Β76) to him. In the process of progressing into the dust cover, the cover (B 7 5) Covered in the take-out frame (B 7 work) and the surrounding, to prevent the floating material in the process of removing the solid matter, etc.), the dust suction pipe (τ, , : containing flying dust, dust cover ( Β75”, the dust-proof military end can be extended into the anti-suction concentration; the cracking furnace (...(ΒΕ) below the ground: Π川, for take-out, (B71) when falling = flush with the ground, convenient push frame (B73) will take The solid material of the second set is pushed down to the transport vehicle (B 7 6). 7 1) Please refer to the twenty-sixth figure 'The cracking furnace (Η) (Μ) or 13 丄 353922

There is no take-out device (B60) (B7〇), but a lifting device (B8〇) is provided, and the lifting device (B8〇) includes a slide rail (b8 3), a one-day car (B81), and a Sheng a basket (b82), the moon rail (B83) is disposed above the cracking furnace (bs) (BE), and the crane (B81) is slidably disposed on the slide rail (B83). The basket (B82) passes through the basket The rope body (B84) is connected to the crane) and can be selectively raised and lowered by winding the rope body (B84) to hold the object to be reclaimed in the basket (B8 2) and pass through the container The blue (b, -) rise and fall will be placed in the cracking furnace (Bs) (BE) s cracking process, and will be left in the basket (B solid material hanged and transported to other places in the thermal cracking process) For further processing, please refer to the second + 4 · 闰 Δr, - seventeen diagrams A, B, C and D, the above cracking furnace (BE) or no extraction device (B 6 〇) (B 7 〇) And a lifting device (B8〇), which is provided with a support device (B92), a moving motor (B 9 1 , and a plurality of high temperature resistant hoses) (B93), the support frame (B92) · Stop from - positioned on the ground, for the cracking furnace (the BS (both sides via a respective pivot post (^ I) 921) pivoted thereon, the drive motor (

9 1) Set on the support frame (β 运 Q 21) to rotate to kiss the data and drive the tappet “9 ...... Furnace (BS) (BE); thereby, in the cracking furnace (BE), s After the angle is set, the solid matter remaining after the pyrolysis process & point can be temporarily poured into a milk product and dumped to a transport vehicle (Β 9 4 ) to another place for further processing; The high temperature resistant hoses (B9 salt are attached to the outer side wall of the cracking furnace (BE), and the high temperature resistant hose (b 14 u53922 3) functions as fuel, heat, electric energy, air, water: burning, non-flammable gas , liquid discharge, and through the resistance of two,: (B93) on the cracking furnace (BS) (BE) outside: soft officer

Reduce the cracking of the force motor (B91) applied to the column (B92lV\tension, channel, drive 1) with a weight of BE). It is easier to drive the cracking furnace (Μ). (B-Battery (BS) (BE) has various implementations. In the case, the company: = furnace (BS), can also be electric cracking furnace (be).

A comparison: the actual two to four and the ninth figure ..., in the preferred P example of the present invention, the cracking furnace (BS) is a gas cracking furnace (B gas to the production system, for - gas The chamber (B1) is configured to accommodate the heat required to heat the inner furnace body (B 1 3 ). The gas cracking furnace (βςΐ ^ is connected to the gas chamber...), the second gas; T.)

n s ; ask 'the burning of the dish can be heated by the gas inlet pipe (T 〇): sent to the gas room (Chuanzhong to the inner furnace body...3). ...ΓSee the tenth figure... 'The gas_(bs) or K input s (TQ), and set a fuel input pipe (D1) p to gas to (Bl)' and on the fuel inlet pipe ( Tl) Entering the inlet of the combustion (Bl) - the main burner (18), the gaseous or = fuel can be sent to the main burner (18) to ignite in the gas chamber (Β after combustion, become a high temperature gas to the inner furnace ^ Gas cracking furnace (Bs) can also be set up: the intake pipe (Τ to the main burner (18), so that the external air or non-flammable gas can be sent from the main burner intake pipe (T2) To the main burner (1 1353922 8) 'In a mixed gaseous or liquid fuel, ignited in a gas chamber (Η) for combustion sterilization; non-flammable gases such as unwanted substances remaining after extraction of organisms or minerals, and A gaseous product produced by a pyrolysis process of a solid or liquid of a medical, toxic, or special waste that has been repeatedly burned.

The gas cracking furnace (BS) further includes a gas chamber inlet pipe (T 3 ) and a gas chamber exhaust pipe (T 4 ) connected to the gas chamber (B丄), and the dish is low. The gas or liquid can be transported by the gas chamber inlet pipe (T3), and the gas chamber (Β1) is used to moderately reduce the excessive temperature in the gas chamber (Β1); The gas in (至 1 ) can be output to the filter discharge unit (E) via the gas chamber drain “T4” for further cooling, filtration, or discharge treatment. Please refer to the eleventh round A. B, cw, the above gas cracking furnace S) may be provided with at least a heat transfer tube (B2), the at least one pass, S (B2) extending from the gas chamber (Bl) into the cracking chamber (B3) Medium: both ends of the opening are connected to the gas chamber (B1), so that the gas in the gas chamber (Η) can flow through the heat transfer tube (B2) in the deep cracking chamber (Μ) in the heat transfer tube, 15匕) According to the different material properties of the materials to be recycled, the structure and quantity design can be used to uniformly heat the materials to be recovered in the cracking chamber (B 3 ). Please refer to Figure 12 A and B and the tenth. Three pictures "B, above: gas cracking furnace The BS) may further include a baffle (B4) disposed between the 1) body I 1 3 ) and the outer furnace body (B 1 1 ), and the gas chamber (the two of the B chambers are separated into a plurality of mutually connected flow channels) , the gas in the gas chamber (Β 1 ) 16 1353922 can be distributed along the flow channel to the gas flow more uniformly distributed throughout the combustion (B3) uniform heating; the baffle (B13) and the outer furnace (B11 is divided into a number of longitudinal flow channels (such as the twelfth figure can also be set laterally in the inner furnace body (B 1 3 separates the gas chamber (B 1 ) into several horizontal directions, whether it is horizontal or vertical to set the heat of the baffle. Exhaust pipe (T 4 ), so that the gas chamber (Bl) can be disposed between the gas chamber (B 1 ) and the gas chamber (B 1 ) can be longitudinally disposed in the inner furnace body); Between the piece (B 4 )) and the outer body (B 1 1 ), the flow path (as shown in Figure 13A), (B 4 ) ' can be evenly added. Please refer to the fifth to eighth figures and 19 and A, in another preferred embodiment of the present invention, the cracking furnace (BE) is an electrothermal cracking furnace (BE), and a heating plate (H1) is provided in the heating space, and an electric heating device is provided. (H0) is connected to the hot plate (H1), the hot plate ( Hi) is placed around the outer side wall of the inner furnace (B 1 3) to generate heat energy to heat the inner furnace body (B 1 ?), 兮 · · succeed t f υ Π, m

1 01 ; ° Hai cable (Η 〇 ) to provide electric heating plate (H

1) The electrical energy required for fever.

Referring again to Figures 20 and 3, the electrothermal cracking furnace (BE) further comprises an electric heating tube (H2). The electric heating tube (H2) is extended from the electric heating fe(H i) into the cracking chamber (B3) to The heat energy sentence is distributed in the cracking chamber (B3), and the material to be recovered in the cracking chamber (B3) is uniformly formed into a crucible. & * **\ Referring to Figures 1 to 8, the above material handling unit (c) comprises a vacuum pump (12), the wheel end of which is connected to the cracking furnace (BS) ( BE) cracking chamber exhaust pipe (τ 6 ) 17 1353922 to take the gaseous money generated in the thermal cracking process from the cracking chamber (b sleeves are transported to other places for further processing; the vacuum fruit ( The output of 1 2) may be connected to the fuel input pipe (T1). The above material processing unit (C) may further comprise a condenser (work 1). The input end of the condensation benefit (1 1:) is connected to the cracking chamber. The exhaust pipe (Τ 6) 'its output is connected to a vacuum pump (12) for conveying the vacuum pump (1 2 ) from the gaseous product extracted from the cracking chamber (Β 3 ) to the vacuum pump (丄 2).

The above material processing unit (c) may further comprise a flammable liquid storage tank (9). The input end of the flammable liquid storage tank (9) is connected to a vacuum pumping (χ2) flammable gaseous product in the condenser (1 1 ) After the condensation process is performed and becomes a combustible liquid, it can be extracted by the vacuum pump (1 2) to the combustible liquid storage tank (9); the output of the combustible liquid storage # (9) is connected to the fuel input pipe f T 1 , )' The flammable liquid stored therein is sent to the main burner of the gas cracking furnace (Bs) through the fuel inlet pipe / D1 (the combustion process is performed, and the high-temperature gas is formed in the gas chamber (Β 1 ); , combustible liquid storage; flammable liquid stored in ff (9), can be returned to flammable gaseous products through fractionation procedures, such as waste tires, waste plastic knees, oil sludge 'from materials, etc., after thermal cracking procedures The gaseous product produced. The material processing unit (c) may further comprise a non-flammable liquid reservoir C 1 pv \ 'the input end of the non-flammable liquid storage tank (1 〇) is connected to the vacuum system f 1 〇, , 丄d), useful non-flammable gaseous product in the condenser (1 1 ) for condensation process After becoming a non-flammable liquid, it can be stored by vacuum pumping (1 2 ) ^ into a non-flammable liquid storage tank (1 〇); the source of the non-flammable liquid 18 1353922 may be a useful substance after biological or mineral extraction by thermal cracking process. μ The substance treatment unit C) may also include an auxiliary combustion device (16): the auxiliary combustion device (16) is provided with an auxiliary combustion machine (16 1) and a combustion chamber (162), the auxiliary The burner (the input of the 16 is connected to the vacuum fruit 2), the useless non-combustible gaseous product produced in the thermal cracking process can be pumped to the combustion chamber (16 2) via the vacuum pump (U). The auxiliary burner (16 η is ignited in the combustion chamber (162). The main genus of the genus 烧 烧 烧 烧 烧 烧 烧 ; ; ; ; ; ; ; ; ; ; ; ; ; ; ; ; ; ; ; ; ; ; ; ; ; ; ; ; ; ; ; After being combusted, it is pumped to the combustion tank (1 6 2 ) as a fuel by vacuum (4) (U) and generates hot gas after combustion; and after being treated by the condenser (1 1 ), it is not condensed into a combustible liquid. Flammable gaseous product °, can also be delivered to the fuel input pipe by vacuum pump (12) The burner (1 8) is proud of the rabbit, 嫉m ', 8) is used for burning, and can also be sent to auxiliary combustion as fuel, and generates hot gas after combustion; the output end of the combustion chamber 62) is connected The exhaust gas (E) is discharged, and the exhaust gas generated by the use of the non-flammable gaseous product after combustion sterilization and disinfection is filtered through the filter discharge unit (E) and discharged. The output end of the combustion tank (1 6 2 ) can still be connected to the gas input pipe (τ〇) of the gas cracking furnace (BS) for the combustion tank (the heat combustion generated after the combustion process is ordered) The gas 'is delivered to the inner furnace body (B 1 3) through the gas input pipe (Τ 0) to the Miao Weng 1 ... ceremony (B 1 ). ^ The output end of the combustion tank (16 2) is still available Connected to the main burner into the rolling officer (D) 2 'Inflammability generated by the thermal cracking process 1^53922 Gaseous product can be ignited in the combustion chamber via the auxiliary burner (i 6 i ) (丄6 2) After combustion, it is sent to the main burner (18) through the main burner intake pipe for secondary combustion to achieve sufficient sterilization effect. The substance processing unit (c) further includes a temporary storage tank (13), The input end of the temporary storage tank (13) is connected to the vacuum pump (12), and the vacuum pumping (1 2) can be used to pump the combustible liquid to the temporary storage tank (1 3) to store the '13⁄4 temporary storage tank (1 3) and Connected to the combustible liquid storage tank (9) through a bidirectional pipeline to transport the temporarily stored combustible liquid to the combustible liquid storage tank (9) for storage in the combustible liquid storage tank (9) The fuel liquid is transported to the temporary storage tank (13) for temporary storage; the output end of the temporary storage tank (13) is connected to the auxiliary combustion machine (161)' to transport the temporarily stored combustible liquid to the main combustion unit (1 8 Or the auxiliary burner (jl 6 i ) is used as fuel to carry out a combustion process and generate hot gas. The substance processing unit (c) further comprises a water separator (14), the oil water separator (14) The input end is connected to the temporary storage tank, and the output end is connected to the auxiliary combustion machine (16 χ ) and the filter discharge unit ^ (E), and the wheel end can be further connected to the main combustion machine (丄 8), and through - the bidirectional pipeline is connected to the flammable liquid storage tank (9) and the filtration discharge unit 70 (E), and the temporarily stored flammable liquid in the temporary storage tank (13) can be sent to the oil water separator (i 4 ) for oil water separation Procedure to precipitate pure combustible liquid and wastewater 'pure flammable liquid can be transported to flammable liquid storage# (9) to store or transport to main burner (1 8) and auxiliary burner (1 6 1) as fuel ' The waste water is sent to the filter discharge unit (E) and filtered to discharge the 'oil-water separator (1 4)# after the pure combustible liquid, or Wheel 20 1353922 is transported to the main burner (18) or the auxiliary burner (1 6 1) as fuel, so that the flammable liquid temporarily stored in the temporary storage tank (13) through the oil-water separator (14) It can be sent to the main burner (18) or the auxiliary burner (161) as fuel; in addition, if the flammable liquid is directly transported from the temporary storage tank (13) to the flammable liquid storage tank (9), The combustible liquid in the combustible liquid storage tank (9) is first sent to the oil water separator (丄4) to precipitate the pure combustible liquid, and then sent to the main combustion unit (18) or the auxiliary combustion unit (1 6 1) as fuel. In addition, a cleaning liquid column (17) is further included in the material processing unit (C), and the output end of the cleaning liquid column (17) is connected to the combustion chamber (162) of the auxiliary combustion device (16), and can be further connected to A gas chamber (bi) of a gas cracking furnace (BS) for injecting a cleaning liquid into a combustion tank (1 6 2 ) to clean the combustion chamber (i 6 2 ) or the gas chamber (B 1 ). The dust collecting unit (D) includes an exhaust dust collector (2 ◦), and the exhaust dust collecting state (2 〇) can be disposed in the furnace body (B 丄 3) adjacent to the cracking furnace (bs) (b E) The opening is used to absorb the cracking furnace (μ) (BE). When the furnace cover (B〇) is opened, the suspended particles generated in the thermal cracking process are scattered around; the exhaust dust collection _ (2〇) can also be Set in the vicinity of the cracking furnace (BS) (BE) outside the furnace body (Βΐι) through the slot J solution = set out · (Β 61) removed, scattered around the thermal particles generated in the sequence of suspended particles. The dust collecting unit (〇) of the upper sill also contains a cyclone dust collector (the input end of the cyclone dust collector (21) is connected to the venting chamber exhaust 21 1353922, the gas generating product generated in the cracking process is The cracking chamber (B 3 ) is extracted and separated by centrifugal force to separate the particles contained therein from the gas stream to filter the suspended particles; the cyclone dust collector (the input end of the '·, ^ can be connected to the exhaust set Dust collector (2 〇), the airborne dust collector (20) absorbs the suspended particles. ... The dust collecting unit (D) mentioned above still includes a cooler

The input of the cooler f 1 Ω^ y ; J 19) is connected to the cracking chamber exhaust pipe (the τ / middle output is connected to the cyclone (2 i ) for generating the gaseous state generated by the thermal cracking process After the cooling process, the product is sent to the cyclone 2 1 ' to filter the suspended particles contained therein. ° The above dust collecting unit (D) further comprises a filter (22), the input end of the I net (22) is connected to the cyclone (2ι) for collecting the cyclone dust collector (21) Suspended particles remaining after the transition. The dust collection unit (D) of the representative still includes a bag-type dust collector (2 3 ), and the input end of the bag dust collector (23) is connected to the data network (22), with, -set, star ; (2 2 ) suspended particles remaining after the crossing; the output end of the bag dust collector (23) is connected to the over-the-counter emission (E), and remains after being filtered. The gas is filtered through the filter discharge unit (E) and discharged. The suspended particles collected by the extractor (2 〇) can be further collected by the suspected dust collector (21), the filter (22) and the bag dust collector (23). The gaseous product is transported to the transitional discharge unit (E) by the dust collection unit (d), wherein the suspended particles have been substantially teared off; and the gaseous product containing the suspended particles can also pass through the stalk dust collector (2 〇) 22 ^^^922 Discharge directly to the filter discharge unit (E) after suction. The above-mentioned over-discharge unit (E) comprises a chimney (29) connected from the wheel-in end of the (29) to the dust collecting unit (d) for discharging after dust collection by the dust collecting unit (D) Gas. The filtering and discharging unit (E) further includes an exhaust fan (28), the input end of the exhaust fan (28) is connected to the dust collecting unit (D), and the output end thereof is connected to the chimney (29). The gas treated by the dust collection unit (D) is extracted and sent to the chimney (29) for discharge; the input end of the exhaust fan (28) can be connected to a wind collector (2 〇) or a bag dust collector. (23), can also be connected to the two separately, the unwanted gaseous products generated by thermal cracking can be collected by the exhaust dust collector (2〇), and directly through the exhaust fan (28) # to the smoke from (29 Emissions, and if there are too many suspended particles in the gaseous product collected by the extractor (20), it can be further circulated by a cyclone (2丄), a filter (2 2 ) and a bag set. The dust thief (2 3 ) filters the suspended particles, and then extracts the gaseous product through the exhaust fan (28) to the chimney (29) for discharge. The above filter discharge unit (E) further comprises a clean water/chemical scrubbing tower (25), and the input end of the clean water/chemical scrubbing tower (25) is connected to the collecting unit (D) for filtering the dust collecting sheet a (d) chemical substances contained in the gas remaining after the treatment, such as sulfur oxides, nitrogen oxides, etc.; the output of the clean water/chemical scrubbing tower (25) is connected to the exhaust fan (28) The gas that has passed through the exhaust fan (28) is extracted to the chimney (2 9 ) for discharge; the input end of the clean water/chemical scrubbing tower (25) is connected to the bag dust collector (23) or It is a suction dust collector (2 ^), 23 1353922 can also be connected to the two respectively. The useless gaseous products produced after thermal cracking can be directly collected by the exhaust dust collector (2〇) and sent to clean water/ The chemical washing tower (25) is further smashed, and if the gaseous product adsorbed by the extracting dust collector (2〇) entrains too much suspended particles, the cyclone (2 1 ) and the filter can be further used. (2 2 ) and the bag collector (2 3 ) will be suspended and then transported to the clean water/chemical scrubber 25) further over suddenly.

The above-mentioned filter discharge unit (E) further includes a water tower (24), and the output end of the water tower (24) is connected to the clean water/chemical wash to provide the water/chemical wash (25) for the material. Working water. The above filter discharge unit (E) further comprises a wastewater/bioprocessing device 'the input end of the wastewater/bioprocessing device is connected to the oil water separator "4) 'to treat the wastewater discharged from the oil water separator (丄4) After the formation of fertilizer or waste material, the input end of the wastewater/biological treatment device (26) can also be connected to the clean water/chemical scrubbing tower (25) for water/chemical washing (2 5 ) The water used for operation after use is treated as fertilizer or waste. ^ The above-mentioned passing and discharging unit (E) may further include an activated carbon tower (2:)' the input end of the activated carbon tower (27) is connected to the clean water/chemical washing tower (25), and its output The end is connected to the exhaust fan (28 / used to deodorize the gas filtered through the water/chemical scrubber, and then discharged by the exhaust fan (2 'extracted to the smoke U (29). The above energy supply unit (A) contains There are at least - lightning _ knowing machine and; ', control device (6), the at least one generator is selected from β when too much energy 24 1353922 generator (l), wind power construction ο, motor (2) , the hydroelectric generator (3), and the internal combustion generator (4) constitute a group of ~ or a group, the input end of the power control device is connected to the at least - generator, providing a commutation 'transformed' power storage and points The function of electricity, the combination of the wheel composite material thermal cracking integration system of the power control device (6) is 7G early to supply the power required for the operation and control of each unit; the present invention is a composite material thermal cracking integrated Li The system is based on the geographical location of the place, the name and the climatic environment, and the right nature. The system 'can use solar generator r. *Motor (1), wind turbine (2), or hydro generator (3) 'For example, Dangyang generator (1) generates electricity, when rainy and windy = ... can use solar energy ^ ^ When the wind turbine (2) can be used to generate electricity, and the right place is close to the river, ~ humiliation of the seaport, etc., then the hydroelectric generator (3) can be used to generate electricity, the right eight... | electricity to make full use of natural resources; When the generator (1), the wind generator, the .s machine (2), and the hydroelectric generator (3) are unable to operate smoothly using the natural energy thunder helmet I can use the internal combustion generator (4) to generate electricity. The power supply required for each single operation is provided. The above energy supply unit (A彳..., ... includes a hydrogen-oxygen generator (7) and a damper (8), the hydrogen-oxygen generation „ ^ r 9 / 1 ^ The input of Wang An (7) is connected to the water tower (24) to electrolyze the water source provided by the water tower into a helium gas and oxygen rolling. The mixer (8) ..., 苴钤“The input is connected to the oxyhydrogen generator (7). The eight output 钿 is connected to the fuel wheel, ^ ^ a.as ( 7 \ D 1), in order to generate the oxygen and oxygen generated by the agricultural oxygen (7), and then send it to the main burner (18) for combustion, and in the gas chamber, the material is produced. The contaminated high-heat gas is heated to the furnace body of the heat-burning cracking furnace (BS), g8 (®13), and the output of the mixed sis (8) can also be connected to the auxiliary burner (1 6 1). 25 1353922 The fuel required for the combustion of the auxiliary burner (1 61) is provided. The above energy supply early (A) may also include a chilled wheel generator (5) 'the input of the gas turbine generator (5) Connected to the gas chamber exhaust pipe (T4), the output end of which is connected to the power control device (6), whereby the gas turbine generator (5) can generate electricity by using the gas discharged from the gas chamber exhaust pipe (T4) And generating the electrical energy to be used by the power control device (6); the input end of the gas turbine generator (5) may also be connected to the combustion chamber (162) of the auxiliary combustion device (16), thereby being non-flammable After the gas is burned and sterilized in the combustion tank (i 6 2 ), it can be discharged to the gas turbine generator for power generation; the input of the gas turbine generator (5) Lysis chamber may also be connected to the exhaust pipe (τ 6), to the use of exhaust gas of the exhaust pipe cracking chamber (T6) to generate electric power. Referring to the fourth and eighth figures, in another preferred embodiment of the composite material thermal cracking integration system of the present invention, the thermal cracking unit (b) may comprise a plurality of cracking furnaces (BS) connected in parallel with each other (Be). Each cracking furnace (BS) (BE) comprises a furnace body (B<13) having an opening, an outer furnace body (B11) covering the outer side wall of the inner furnace body (Bi3), and a furnace cover ( B 〇) is located at the opening of the inner furnace body (B i 3 ), and the inner furnace body (B13) is a cracking chamber (b3) for accommodating the to-be-recycled material, and the outer furnace body (B 1 1 ) and the inner The furnace body (B丄3) is a heating space for accommodating the heating element to heat the material to be recovered in the cracking chamber (B3), and is provided with heat insulation on the inner side wall of the outer furnace body (B i丄) Layer (B 12) to provide a thermal insulation effect to slow the heat loss rate of the heating body in the heating space and avoid overheating of the surface temperature of the outer furnace body (B1 1:); and 26 1353922 痣, liquid, flammable, and non-flammable The composite material thermal cracking integration system of materials can be recycled according to the characteristics of different kinds of materials to be recycled. It can be thermally cracked for solid, liquid, flammable, and non-flammable materials to be recycled, and various products obtained by thermal cracking procedures, including solid, liquid, gaseous, flammable, non-combustible products, can be transmitted through Various corresponding devices are processed for removal, condensation, purification, transition, sterilization, etc., and then recycled or discharged; and the same type of cracking furnace can be used according to the characteristics of the recovered materials to improve heat transfer and thermal cracking efficiency. 'At the same time, natural energy and self-produced electrical energy can be used as a source of energy supply for system operation, and self-produced fuel and pollution-free chlorine = and oxygen can be used as a gas source; in addition, the filter discharge unit can be permeable. The air pollution and wastewater treatment plant processes gaseous and liquid waste, and it can be combined with a biological treatment system to convert waste into fertilizer. The composite material thermal cracking integrated system of the invention has the functions of diversified material recovery, refining treatment, resource recycling, energy re-engineering, and has the characteristics of energy saving and environmental protection, and is a complete solution for processing composite materials, resulting in Thermal cracking technology is used in a wider range of applications. However, the above description is only a preferred embodiment of the present invention, and therefore, the equivalent changes of the patent specification and the patent application scope of the present invention should be included in the patent scope of the present invention. BRIEF DESCRIPTION OF THE EMBODIMENT: Fig.: is a circuit configuration diagram of a preferred embodiment of the composite material thermal cracking integration system of the present invention, which comprises a gas cracking furnace.

2S 1353922 The second figure is a circuit configuration diagram of a second preferred embodiment of the composite material disintegration system of the present invention, which comprises a _. 々, a 虱 虱 虱 cracking furnace and a The first auxiliary burner and a second auxiliary burner. Figure 3: Schematic diagram of the configuration of the first line. A fourth embodiment of a composite material, a pyrolysis integrated system integrated system, and a third parallel gas. FIG. 4 is a schematic diagram of a circuit configuration of a preferred embodiment of the composite material thermal cracking of the present invention, which comprises two cracking furnaces. .

Figure 5 is a circuit configuration diagram of a preferred embodiment of the thermal cracking of the composite material of the present invention, which comprises - a sixth embodiment: a preferred embodiment of the thermal cracking of the composite material of the present invention, which comprises an electrothermal cracking furnace The fourth electrothermal cracking furnace of the integrated system. The fifth and one auxiliary burner of the integrated system. Figure 7: The gas diagram of the pyrolysis furnace shown in the fifth figure is the eighth. Figure 8 is the sixth of the composite material thermal cracking integration system of the present invention.

A circuit configuration diagram of a preferred embodiment includes two electrothermal cracking furnaces connected in parallel with one another. Fig. 9A is a front cross-sectional view showing the gas cracking furnace of the composite material thermal cracking integrated system of the present invention. Figure 9B is a top view of the gas cracking furnace shown in Figure IX. Fig. A is a front cross-sectional view of a gas cracking furnace of a composite material pyrolysis integrated system of the present invention, which comprises a main burner. Figure 11B is a schematic view of the gas cracking furnace shown in Figure 11A. Fig. 11A is a front cross-sectional view showing the gas cracking furnace of the composite material thermal cracking integrated system of the present invention, in which a single heat transfer tube is provided. Figure 11B is a top plan view of the gas cracking furnace shown in Figure 11A. Eleventh Figure C is a front cross-sectional view of a gas cracking furnace of a composite material thermal cracking integrated system of the present invention, in which a plurality of heat transfer tubes are provided. Figure 11D is a top view of the gas cracking furnace shown in Figure 11C. Twelfth Figure A is a front cross-sectional view of a gas cracking furnace of a composite material thermal cracking integrated system of the present invention, in which a longitudinal baffle is provided. Twelfth Figure B: is a top view of the gas cracking furnace shown in Figure 12A. Thirteenth Figure A is a front cross-sectional view of a gas cracking furnace of a composite material thermal cracking integrated system of the present invention, in which a lateral deflector is provided. Thirteenth Figure B: A top view of the gas cracking furnace shown in Figure 13A. Fig. 14 is a front cross-sectional view showing the gas cracking furnace of the composite material pyrolysis integrated system of the present invention, in which a liquid storage tank is provided. Figure 14B is a top plan view of the gas cracking furnace shown in Figure 14A. Fig. 15 is a front cross-sectional view showing the gas cracking furnace of the composite material thermal cracking integration system of the present invention, wherein the spiral blade stirring device is provided with a plurality of blade groups. 30 1353922 Figure 15 B: A top view of the gas cracking furnace shown in Figure 15A. Fig. 16A is a front cross-sectional view of the gas cracking furnace of the composite material thermal cracking integrated system of the present invention. The spiral blade mixing device is provided with a single blade group. Figure 16B: The gas cracking furnace shown in Figure 16A is not intended. Fig. 17 is a front cross-sectional view showing the gas cracking furnace of the composite material pyrolysis integrated system of the present invention, which is provided with an open material removing device. Figure 17B is a top plan view of the gas cracking furnace shown in Figure 17A. Fig. 18 is a front cross-sectional view showing the gas cracking furnace of the composite material thermal cracking integrated system of the present invention, which is provided with a closed material removing device. Fig. 18B is a top plan view of the gas cracking furnace shown in Fig. 18A. Fig. 19 is a front cross-sectional view showing the electrothermal cracking furnace of the composite material pyrolysis integrated system of the present invention. Fig. 19B is a top view of the electrothermal cracking furnace shown in Fig. 19A. Fig. 20A is a front cross-sectional view showing the electrothermal cracking furnace of the composite material thermal cracking integrated system of the present invention, in which an electric heating tube is provided. Twenty-fifth Figure B is a schematic view of the above-mentioned electrothermal cracking furnace shown in Figure 20A. Figure 21 is a front cross-sectional view of the electrothermal cracking furnace of the composite material thermal cracking integrated system of the present invention, wherein the spiral blade stirring device is provided with a plurality of blade groups. " Twelfth Figure: Front view of the electrothermal cracking furnace of the composite material thermal cracking integrated system of the present invention. The spiral blade stirring device is provided with a single blade group. \ Figure 13: A schematic front cross-sectional view of the electrothermal cracking furnace of the composite material thermal cracking integrated system of the present invention, in which a magnetic stirring device is arranged. Twenty-fourth Figure A is a front cross-sectional view of an electrothermal cracking furnace of a composite material thermal cracking integration system of the present invention, in which an open material take-out device is provided. Twenty-fourth Figure B: is a top plan view of the electrothermal cracking furnace shown in Figure 14A. Twenty-fifth Figure A: A front cross-sectional schematic view of an electrothermal cracking furnace of a composite material thermal cracking integrated system of the present invention, in which a closed material take-out device is provided. Figure 25: Figure 25: A schematic cross-sectional view of the electrothermal cracking furnace that is not available under the solid. Figure 26 is a front view showing the material lifting device disposed above the cracking furnace of the composite material thermal cracking integration system of the present invention. Twenty-seventh Figure A: A front view of a cracking furnace of a composite material s post-type material thermal cracking integrated system of the present invention disposed on a pouring device.

Twenty-seventh Figure B: A side view of a cracking furnace that is not shown in Figure 27A, placed on a pouring device of 32 1353922. Figure 27 is a front view of the cracking furnace shown in Figure 27A for the pouring operation. Figure 27 is a side view of the cracking furnace shown in Figure 27A for the pouring operation.

[Main component symbol description] (A) Energy supply unit (BE) Electrothermal cracking furnace (B 〇) Furnace cover (B 2 ) Heat transfer tube (B 4 ) Guide vane (B12) Insulation layer (B 5 0 ) Spiral Leaf stirring equipment (50 ') magnetic stirring device (B 5 1) rotating leaf mechanism (B 5 3) magnetic stirring rod (B 5 5) magnetic steel sheet (B 6 0 ) take-out device (B 6 2 ) driving motor ( B 7 1) Take-out frame (B 7 3) push frame (B 7 5) dust cover (B 7 7) groove (B) thermal cracking unit (BS) gas cracking furnace (B 1 ) gas chamber (B 3 ) cracking chamber (B 1 1 ) outside furnace body (B 1 3 ) inside furnace body placement (B52) drive motor (B 5 4 ) motor (B 5 7 ) spiral blade mechanism (B 6 1 ) removal frame (B 7 0 ) take-out device (B 7 2 ) drive motor (B 7 4 ) push-pull motor (B 7 6 ) transport vehicle (B 8 0 ) lifting device 33 1353922

(b 8 1) Crane (B 8 3) slide rail (B 9 Ο) pouring device (B 9 2) support frame (B 9 3) high temperature resistant hose (C) material processing unit (E) filter discharge unit (Η 〇) cable (S 1 ) liquid storage tank (Τ 0) gas input pipe (Τ2) main burner intake pipe (Τ 4) combustion chamber exhaust pipe (Τ6) cracking chamber exhaust pipe (Τ 8) Dust suction pipe (2) Wind turbine (4) Internal combustion generator (6) Power control device (8) Mixer (1 0) Non-flammable liquid storage tank (1 2) Vacuum pump (1 4) Oil-water separator (1 6 Auxiliary combustion device (1 6 2 ) combustion tank (18) main burner (Β 8 2) basket (Β 8 4) rope body (Β 9 1 ) drive motor (Β 9 2 1 ) pivot column (Β 9 4) Conveyor (D) Dust collecting unit (Η 1) Electric heating plate (Η 2) Electric heating pipe (Τ 1) Fuel input pipe (Τ 3) Gas chamber inlet pipe (Τ5) Cracking chamber inlet pipe (Τ 7) Liquid material discharge pipe (1) Solar generator (3) Hydroelectric generator (5) Gas turbine generator (7) Hydrogen oxygen generator (9) Combustible liquid storage tank (1 1) Condenser (1 3 ) Storage tank (1 6 1) auxiliary burner (17) cleaning liquid tower (1 9) cooler 34

Claims (1)

1353922 May 10, 2010, apply for a patent garden: 1. A composite material thermal cracking integration system, comprising: a thermal cracking unit, comprising a cracking furnace, the cracking furnace is used to enter the body to be recycled The thermal cracking process comprises a furnace having an opening - the outer furnace body is coated on the outer side wall of the inner furnace, and a furnace cover is arranged in the inner furnace; the inner chamber is a cracking chamber for the capacity The retentate is disposed, and the: between the body and the inner furnace body is heated to accommodate the heating element to heat the material to be recovered in the cracking chamber, and the side wall of the outer furnace body is provided with a barrier layer. - a material handling unit, connected to the cracking crucible, which is produced in the thermal cracking process: the gaseous precursors are subsequently treated according to their flammability or not; - the dust collecting unit is connected to the cracking furnace for filtering thermal cracking Suspended particles produced in the process; - a filter discharge unit 'connected to the thermal cracking unit, the material processing unit and the dust collecting unit' for clarifying and discharging the non-recyclable material generated in the thermal cracking process; and an energy supply unit , loaded & people κ . The flat 7L includes at least one generator and a power control device. The input end of the power control device is connected to the at least one generator, and the power control device is connected to the composite The single 7L of the material thermal cracking integration system supplies the energy required for each unit to operate. 2 The composite material thermal cracking integration system described in the first paragraph of the patent application is in which the cracking furnace is provided with a cracking chamber inlet pipe and a cracking chamber exhaust pipe connected to the cracking chamber. 3:3⁄4申, the composite material thermal cracking integration system described in the second paragraph of the patent scope of the 'in which the cracking furnace comprises a spiral blade stirring device, the 36 1353922 100 January 1 i £ g? Tgg ¥ ~ spiral The blade stirring device comprises a driving motor and a spiral blade mechanism. The gas driving motor is disposed adjacent to the furnace body opening in the cracking furnace. The spiral blade mechanism is disposed in the cracking chamber, and one end thereof is connected to the driving motor and driven by the driving motor. Rotate. 4. The composite material thermal cracking integration system according to claim 1, wherein the cracking furnace comprises a magnetic stirring device comprising an electric motor, a magnetic steel sheet, and a magnetic mixing machine. The motor is disposed under the inner furnace body, and the magnetic steel piece is disposed under the inner furnace body and connected to the power output shaft of the motor to rotate by the motor and generate a rotating magnetic field when rotating, the magnetic stirring The sub-unit is disposed at the bottom of the cracking chamber and is driven by the rotating magnetic field generated when the magnetic steel sheet rotates. 5. The composite material thermal cracking integration system of claim 1, wherein a liquid material discharge pipe is disposed at a bottom of the cracking furnace to be connected to a liquid storage tank. 6. The composite material pyrolysis Lu integration system according to the above-mentioned patent scope, wherein the cracking furnace is further provided with a take-out device, the take-up device comprising a take-up rack and a drive motor, and the cracking furnace The side wall of the outer furnace body is provided with a through groove, and the side wall of the inner furnace body is also provided with a through groove corresponding to the through hole of the outer furnace body. The take-out frame can be laterally moved in the through hole of the outer furnace body and the inner furnace body, and Optionally entering and exiting the cracking chamber, the drive motor is coupled to one end of the take-up rack to provide power to remove the rack. 37 1 · The composite material thermal cracking 2 integrated system according to claim 1, wherein the cracking furnace is further provided with a take-out device, the removal device 1353922 100 years 8 θ 12 days correction replacement page • i contains - The take-up frame, the drive motor '-pushing frame', a push-pull motor, a dust cover, and a dust suction f, and the bottom of the furnace body of the cracking furnace is provided with a groove, and the bottom of the outer furnace body is also provided with a groove. Corresponding to the groove of the bottom of the inner furnace body, the take-up frame can be longitudinally moved in the through groove of the inner furnace body and the outer furnace body, and can selectively enter and exit the cracking chamber, and the driving motor is connected to one end of the take-up rack Providing power for removing the frame, the push frame is laterally movable under the cracking furnace, and the push-pull motor is connected to the push-frame end to provide power for pushing the frame, and the dust cover is disposed on the take-up frame and the push frame Around the dust pipe, one end of the pipe is extended into the dust cover. 8. The composite material thermal cracking 1 system according to claim i, wherein the S-base cracking furnace is provided with a lifting device, the lifting device comprising a slide rail, a crane, and a Sheng a basket, the slide rail is arranged above the cracking furnace, the crane is slidably arranged on the slide rail, and the basket is connected to the crane through a rope body, and can be selectively selected by winding the rope body Lifting and lowering. 9. The composite material pyrolysis I-integration system according to claim 1, wherein the cracking furnace is provided with a pouring device, which comprises a support frame, a drive motor, and a number Treasury high-temperature hose, the truss is set on the ground 'for each side of the cracking furnace, which is pivoted through a pivot post. 'The drive motor is arranged on the support frame and can drive the pivot post to rotate the cracking furnace' The high temperature resistant hoses are attached to the outer side wall of the cracking furnace. 10. The composite material thermal cracking integration system as described in the second paragraph of the patent scope, wherein the cracking furnace is a gas cracking furnace, and the heating space is a gas chamber for accommodating high heat combustion. The gas is used to generate the heat energy required to heat the inner furnace body. 38 1353922 Aug. 12, pp. 12, pp. 1 1 1. The composite material thermal cracking integrated system of claim 1, wherein the gas cracking furnace is provided with a gas input pipe connected to the gas room. The composite material thermal cracking integration system of claim 1, wherein the gas cracking furnace is provided with a fuel input pipe connected to the gas chamber and enters the gas chamber at the fuel inlet pipe. A main burner is placed at the entrance. A composite material thermal cracking integration system as described in claim 1 wherein the gas cracking furnace is provided with a main burner inlet pipe connected to the main burner. The composite material thermal cracking integration system according to any one of claims 1 to 3, wherein the gas cracking furnace comprises a gas chamber injection pipe and a gas chamber The exhaust pipe is connected to the gas chamber. The composite material thermal cracking integration system of claim 1, wherein the gas cracking furnace is provided with at least one heat transfer tube, the at least one heat transfer tube extending from the gas chamber In the cracking chamber, both ends of the opening are connected to the gas chamber. 1 6 · The composite material thermal cracking integration system as described in the scope of claim 1 'where the gas cracking furnace contains a baffle disposed between the inner furnace body and the outer furnace body' The space in the middle is divided into a number of mutually connected flow paths. The composite material thermal cracking integration system according to claim 2, wherein the cracking furnace is an electrothermal cracking furnace, wherein a heating plate is provided in the heating space and a cable is connected to the electric heating plate. The electric heating 39 1353922 August 12, 100, the replacement of the slab is disposed around the outer side wall of the inner furnace body for generating thermal energy to heat the inner furnace body, and the electric cable is used to provide electric energy required for heating the electric heating plate. 18. The composite material pyrolysis integration system of claim 17, wherein the electrothermal cracking furnace comprises an electric heating tube that extends from the electric heating plate into the cracking chamber. 19. The composite material thermal cracking integration system of claim 2, wherein the material processing unit comprises a vacuum pump, the vacuum pump input being coupled to the cracking chamber exhaust of the cracking furnace. Φ 2 ◦ · The composite material thermal cracking integration system of claim 19, wherein the material processing unit comprises a condenser, the input end of the condenser is connected to the cracking chamber exhaust pipe, and the output thereof The input end connected to the vacuum pump and the vacuum pump is connected to the cracking chamber exhaust pipe of the cracking furnace through a condenser. The composite material thermal cracking integration system of claim 2, wherein the material processing unit comprises a combustible liquid reservoir, the input end of the combustible liquid storage tank being connected to the vacuum pump. _ 22. The composite material thermal cracking integration system as described in claim 2, wherein the gas cracking furnace is provided with a fuel input pipe connected to the gas chamber, the material processing unit includes a temporary storage tank, a oil water separator and a combustible liquid storage tank, wherein the input end of the temporary storage tank is connected to the vacuum pump, and the input end of the oil water separator is connected to the temporary storage tank. The combustible liquid storage tank is respectively connected to the temporary through the bidirectional pipeline The storage tank and the water separator have an output end connected to the fuel input pipe. 2 3. The composite material heat 40 1353922 (~Ϊ55~Aug. 12a) cracking integration system as described in claim 2, wherein the material processing unit contains a __not (four) storage tank, which is not The input end of the flammable liquid storage tank is connected to the vacuum pump. _ 24. The composite material heat according to claim 19, wherein the material processing unit comprises an auxiliary combustion device, wherein one is provided An auxiliary burner and a combustion chamber, the input end of which is connected to a vacuum pump, and the output end of the combustion chamber is connected to the filter discharge unit. 25, for example, the compound material thermal cracking integration system described in claim 11 of the patent dry circumference, the material processing unit comprises a vacuum pump and an auxiliary combustion device [the input end of the vacuum pump is connected to the cracking of the cracking furnace) The chamber exhaust f' the auxiliary combustion device is provided with an auxiliary burner and a combustion chamber, and the input end of the auxiliary burner is connected to the vacuum pump, and the output end of the combustion chamber is respectively connected to the filter discharge unit and the gas cracking furnace Gas input pipe. The composite material thermal cracking integration system according to claim 3, wherein the material processing unit comprises a vacuum pump and an auxiliary combustion device, wherein the input end of the vacuum pump is connected to the cracking of the cracking furnace a chamber exhaust pipe, the auxiliary combustion device is provided with an auxiliary combustion machine and a combustion tank, the input end of the auxiliary combustion machine is connected to the vacuum pump, and the output end of the combustion tank is respectively connected to the filter discharge unit and the main burner intake pipe . The composite material thermal cracking integration system of claim 23, wherein the material processing unit comprises an auxiliary combustion device, wherein an auxiliary combustion machine and a combustion chamber are provided, the auxiliary combustion 41 1353922 August 12, 2014 The input end of the machine is connected to the vacuum pump filter discharge unit. The output end of the combustion chamber is connected to the 28. The composite material thermal cracking integration system described in claim 27, Wherein, the material processing unit further comprises a temporary storage tank, the input end of the temporary storage tank is connected to the vacuum pump, and the output end thereof is connected to the auxiliary combustion machine 1 temporary storage tank and is connected to the flammable liquid storage tank through the bidirectional pipeline The input end of the flammable liquid storage tank is connected to the vacuum pump through the temporary storage tank. 2 9 \ The composite material thermal cracking integration system according to claim 28, wherein the material processing unit further comprises a water separator [the oil water separator input terminal is connected to the temporary storage tank, the wheel thereof The outlets are connected to the auxiliary burner and the filter discharge unit respectively, and are connected to the combustible liquid storage tank and the filter discharge unit through a bidirectional tube. j. For example, the patent ~m ’5, the material thermal cracking integration system, the material processing unit of the material also includes a cleaning liquid tower, and the output end of the cleaning liquid tower is connected to the combustion chamber of the auxiliary combustion device. 3 1 . The compound as described in claim 2 The de-integration system, the middle, the 兮隹_麻留; the ‘人 ‘ ' ', the middle β 集 dust collection early 兀 contains an exhaust dust collector, the exhaust dust collector is placed adjacent to the furnace opening in the cracking furnace. Λ 3 2 · The composite material according to the sixth paragraph of the patent scope is cleaved and integrated, wherein the dust collecting unit comprises an exhaust dust collector, which is disposed adjacent to the furnace body outside the cracking furnace. When the tank is removed by the take-out frame, it is scattered around the thermal cracking procedure:: Particles. < The core sweat is as described in the patent scope of the composite material heat 42 100 years for j rotation: m", the dust collection The unit comprises a cyclone dust collector, ', and the input end is connected to the cracking chamber exhaust pipe, and the cyclone dust collector 1 inlet is connected to the pomelo wind dust collector at the same time. Cracking n · such as the towel, please patent (4) the compound material heat described in item 3 3: wide system 'where, 1 Xuan dust collecting unit contains a - cooler, the cold: the input end is connected to the cracking chamber exhaust pipe 'The output is connected to the cyclone duster. , ύ b • The composite material pyrolysis integration system of claim 4, wherein the 'fourth dust unit still includes a screen, and the input end of the screen is connected to the cyclone. 3 6. The composite material thermal cracking integration system as described in claim 35, wherein the dust collecting unit further includes a bag type dust collector, and the input end of the Xuanyi type dust collector is connected to Filter_, its output is connected to the filter discharge unit. 37. The composite material thermal cracking integration system of claim 2, wherein the filter discharge unit comprises a chimney, and the input end of the smoke solid is connected to the dust collection unit. 3 8. The composite material thermal cracking integration system according to claim 37, wherein the filter discharge unit further comprises an exhaust fan, wherein the input end of the exhaust fan is connected to the dust collecting unit, and the output thereof The input end connected to the cigarette letter 's Xuanyan 13⁄4 is connected to the dust unit through the exhaust fan. The composite material thermal cracking integration system of claim 3, wherein the filter discharge unit further comprises a clean water/chemical scrubber tower. The input end of the clean water/chemical scrubber tower is connected to the dust collection. Unit, 43 1353922 August 12, 100 rev. Replacement page with its output connected to the pomelo fan. 4. The composite material thermal cracking integration system as described in claim 39, wherein the filter discharge unit further comprises a water tower, and the output end of the water tower is connected to a clean water/chemical scrubber. The composite material thermal cracking integration system of claim 29, wherein the filtration discharge unit comprises a wastewater/bioprocessing device, the input of the wastewater/bioprocessing device being coupled to the water separator. The composite material thermal cracking integration system of claim 4, wherein the filtration discharge unit comprises a wastewater/bioprocessing device, and the input end of the wastewater/bioprocessing device is connected to clean water/chemistry Wash > tower. 4 3 · The composite material thermal cracking integration system of claim 4, wherein the filtration discharge unit further comprises an activated carbon column, wherein the input end of the activated carbon column is connected to the clean water/chemical scrubber, The output is connected to an exhaust fan, and the output of the clean water/chemical scrubber is connected to the exhaust fan through an activated carbon tower. 4. The composite material thermal cracking integration system of claim 2, wherein the at least one generator of the energy supply unit is selected from the group consisting of a solar generator, a wind power generator, a hydroelectric generator, and an internal combustion A group of generators. 4. The composite material thermal cracking integration system of claim 12, wherein the at least one generator is selected from the group consisting of a solar generator, a wind power generator, a hydroelectric generator, and an internal combustion generator. 1353922 100 years Μ 12-day repair group, the energy supply unit still includes a hydrogen-oxygen generator and a mixer. The input end of the hydrogen-oxygen generator is connected to a water tower, and the input end of the mixer is connected to the hydrogen and oxygen The generator has an output connected to the fuel input pipe. 46. The composite material thermal cracking integration system of claim 24, wherein the at least one generator is selected from the group consisting of a solar generator, a wind power generator, a hydroelectric generator, and an internal combustion generator. The group 'source supply unit further includes a digital oxygen generator and a mixer. The input end of the hydrogen-oxygen generator is connected to a water tower, and the input end of the mixer is connected to the wind oxygen generator, and the output end is connected. To the auxiliary burner. 4 7. The composite material thermal cracking integration system according to claim 14, wherein the at least power generation (four) is selected from the group consisting of a solar generator, a wind power generator, a hydroelectric generator, and an internal combustion generator. In the group, the energy supply unit further comprises a full-wheel generator, the input end of the gas turbine generator is connected to the gas chamber exhaust pipe, and the output end is connected to the power control device. 4 8. The composite material thermal cracking integration system of the patent scope of claim 24, the +, the at least generator is selected from the group consisting of a solar generator, a wind power generator, a hydroelectric generator, and an internal combustion generator The group of source 'source supply unit still includes a chilled wheel generator, the input end of the chilled wheel generator is connected to the combustion of the auxiliary blasting device (4), and the output end thereof is connected to the power control device. 4 9 . The patented range cracking integration system, wherein the composite material heat source supply unit of the electric motor of the gas turbine generator includes a gas turbine inlet end connected to the cracking chamber exhaust Tube, its 45 1353922 August 12, 100 correction replacement page output is connected to the power control device. 5 〇. A composite material thermal cracking integration system, comprising: a thermal cracking single it, comprising a plurality of pyrolysis furnaces connected in parallel, the cracking furnaces are used for performing a thermal cracking process of the materials to be recovered, And a furnace body having an opening, an outer furnace body covering the outer side wall of the inner furnace, and a furnace cover disposed at an opening of the inner furnace body, wherein the inner furnace body is a cracking chamber for accommodating the to-be-recycled material. Between the furnace body and the inner furnace body is a heating space for accommodating the heating body to heat the material to be recovered in the cracking chamber, and a heat insulating layer is arranged on the side wall of the outer furnace body; - a material processing unit, respectively connected To each cracking furnace, the gaseous products generated in the thermal cracking process are followed up according to whether they are flammable or not; - the dust collecting unit is distributed to each of the furnaces, and (4) the heat cracking sequence is used. The generated suspended particles; a filtered discharge unit connected to the thermal cracking unit, the material processing unit u and the dust collecting unit' for filtering and discharging the non-recyclable substances generated in the thermal cracking process; and - the energy supply unit, Include At least one generator and a power control device, the input end of the power control device is connected to the at least one power generation=, and the output end of the power control device is connected to each unit of the composite material thermal cracking integration system to supply each unit operation The energy needed. 5. The composite material thermal cracking integration system described in claim 5, wherein the cracking furnaces are gas cracking furnaces, and the heating space of each gas cracking furnace is used for gas chambers. In order to accommodate the high-heat gas, the heat required to heat the inner furnace body is corrected by 46 1353922. 5 2 · The composite material heat as described in claim 50. The cracking integration system 'where' The pyrolysis furnaces are electrothermal cracking furnaces, and the heating space of each electrothermal cracking furnace is provided with a heating plate, and an electric environment is connected to the electric heating plate, and the electric heating plate is disposed around the outer side wall of the inner furnace body for generating The heat energy is used to heat the inner furnace body, and the cable is used to provide electric energy required for heating the electric heating plate. 5 3 . The composite material heat as described in claim 5, wherein the electrothermal cracking furnace comprises an electric heating tube extending from the electric heating plate into the cracking chamber. 5 4 - The composite material thermal cracking integration system as described in claim 5, wherein the material processing unit comprises a first auxiliary combustion device and a second auxiliary combustion device connected to each other, the first auxiliary combustion The device is provided with a first auxiliary combustion machine and a first combustion chamber, the second auxiliary combustion device is provided with a second auxiliary combustion machine and a second combustion chamber, and the first combustion chamber and the second auxiliary unit of the first auxiliary combustion device The second output of the combustion unit is connected to the gas chamber of the gas cracking furnace. 5. The composite material thermal cracking integration system of claim 5, wherein the cracking chamber of the cracking furnace has a cracking chamber exhaust pipe, the material processing unit including a vacuum pump, the vacuum pumping The input is connected to the cracking chamber exhaust pipe of the cracking furnace. 5. The composite material thermal cracking integration system of claim 5, wherein the material processing unit comprises a condenser, the input end of the condensation Is connected to the cracking chamber exhaust pipe, and the output thereof Connected to 47 1353922 Vacuum pumping,. The input of the vacuum pump is connected to the cracking chamber exhaust pipe of the furnace through a condenser. 5 7. The composite material loading and disintegrating system according to claim 56, wherein the cracking furnace is provided with a fuel input pipe connected to the gas chamber, and the helium material processing unit comprises a combustible liquid storage tank. The input end of the flammable liquid storage tank is connected to the vacuum pump, and the output end thereof is connected to the fuel input pipe. 5 8. The composite material thermal and pyrolysis integrated system according to claim 56, wherein the cracking furnace is provided with a fuel input pipe connected to the gas chamber, and the material processing unit comprises a temporary storage tank, The oil water separator and an input end of the flammable liquid storage tank 'β temporary storage tank are connected to the vacuum fruit pump. The input end of the oil water separator is connected to the temporary storage tank. The flammable liquid storage tank is respectively connected to the through the bidirectional pipeline. A temporary storage tank and a water separator, the output end of which is connected to the fuel inlet pipe. 5 9 · The composite material thermal cracking integration system according to claim 57, wherein the material processing unit comprises a non-flammable liquid φ storage tank. The input end of the non-flammable liquid storage tank is connected to the vacuum pump Pu. The composite material thermal cracking integration system of claim 59, wherein the material processing unit comprises an auxiliary combustion device. The device is provided with an auxiliary combustion machine and a combustion chamber. The input end is connected to a vacuum pump, and the output end of the combustion tank is connected to the filter discharge unit and the main burner intake pipe, respectively. 6 1 · The composite material thermal cracking integration system according to claim 60, wherein the material processing unit further comprises a temporary storage tank, 48 1353922 ____ the input end of the temporary storage tank is connected to the vacuum pump, The output end is connected to the auxiliary combustion machine; the temporary storage tank is connected to the flammable liquid storage tank through a bidirectional pipeline, and the input end of the flammable liquid storage tank is connected to the vacuum fruit through the temporary storage tank. 62. The composite material thermal " cracking integration system of claim 61, wherein the material processing unit further comprises a water separator, the input end of the oil water separator being connected to the temporary storage tank, The output ends are connected to the main burner, the auxiliary burner and the filter discharge unit, respectively, and are connected to the combustible liquid storage tank and the filter discharge unit through a bidirectional pipeline. Lu 63. The composite material hot furnace of claim 62, wherein the material processing unit further comprises a cleaning liquid, and the output end of the cleaning liquid column is respectively connected to the auxiliary combustion device. The combustion chamber and the gas chamber of the gas cracking furnace. 6 4 . The composite material pyrolysis 1 ° system of claim 6 wherein the vacuum pump output is connected to a fuel input pipe. Η---图: 如次页 49 1353922 Correction replacement page on August 12, 100 <J) T-OJVCNJCSIVCOCNI 1353922 PAGE CHANGE 曰 February 8 00 U l-CNIvCSICNvC0CNI Combustible liquid k fractionation I 1 \ 1] / ίχΐ- M- ^h- H- ¢4- ¢0- ΐ>φ^ 1 1 幸 t 1 Ϋ ΜΠ 濉 f, 1353922 • · 1353922 Corrected replacement page on August 12, 100 I created J BS moved ί Igg»^艄醛辉实留 i (4) 谨—味 1353922 Corrected replacement page on August 12, 100丨 1353922 6 August 12, 100 revised replacement page 1353922 0[ 1 survey 0V0 1353922 • · August 12, 100 revised replacement page 凾 < move 1353922 Ninth Figure A Ninth Figure B Tenth Figure A Tenth Picture B 1353922 Figure 11B Figure 11 C Figure 11 D 1353922 1353922 Thirteenth Figure A Thirteenth Picture B Fourteenth Figure B Fourteenth Figure A 1353922 Picture 15 Figure 16A Figure 16 B 1353922 Figure 17A Figure 17 B 1353922 Eighteenth figure B 1353922 B11 B12 19th Figure A 19th Picture B SS should be this _yO/ 1353922 Twenty-two 匮 1353922 1353922 1353922 Twenty-fifth Figure B 1353922 B83 BE.BS B11 rI353922 Picture 27 A 1353922