TW200836902A - Integrated compound-type pyrolysis system - Google Patents

Abstract

This invention relates to an integrated compound-type pyrolysis system, which includes a pyrolysis unit that has a pyrolysis furnace used to perform pyrolysis for recovered substance, a substance processing unit for post-processing the gaseous products created during the pyrolysis process according to whether the gaseous products are combustible or not, a dust-collecting unit for filtering suspended particles created during the pyrolysis process, a filtering and discharging unit used to filter and discharge unrecoverable substances created during pyrolysis, and a power-supplying unit for supplying power to each unit of the system during operation. This system is capable of completely processing all gaseous products and all solid and liquid residues created by the performance of a pyrolysis process on solid, liquid, combustible, and incombustible substances, and provides various functions of substance-recovering, refining/extracting, resource-recycling, and energy-renewing and features power saving and environment -friendliness, serving as a total solution for substance and energy transformation and extending the applications of pyrolysis technology.

Description

200836902 IX. INSTRUCTIONS: [Technical Field] The present invention relates to a composite material thermal cracking integration system, in particular to a complete recovery of 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 been mainly applied in the field of waste treatment, such as the treatment of waste tires. The recycling method of conventional waste tires can be roughly divided into two. In the first way, the first one is purely physically treated. 'The main thing is to cut the recovered waste tire into pieces by the coarse and fine crusher, and to separate the steel ring when it is. However, after the waste tire is cut into pieces, The recycling can be carried out in a limited manner and can no longer be used as a raw material for the production of tires. Therefore, the efficiency of recycling and recycling is not high, and it is not economical. The second type is chemically treated, mainly the recycling wheel. Month. Ik is cut into pieces by a coarse and fine crusher, and then subjected to a pyrolysis process, in which the above-mentioned pieces to be recovered are placed in a cracking furnace and mixed with a suitable proportion of catalyst. Reheating the cracking furnace to maintain the temperature between 23 and Celsius, and controlling the gas pressure in the furnace to maintain an environment of 1 to U times atmospheric pressure. Under the pressure environment, the pieces that are waiting for time will crack out products with economic value such as pyrolysis oil, carbon black, steel wire, etc., and distillate the gas 5 200836902, and the cracked oil can be further processed. The balance is separated into heavy oil, light oil, gasoline, kerosene, diesel and other products with high economic value, while carbon black is the raw material of activated carbon, and can also be used as a rubber and dye additive, and the steel wire can also be supplied. The steelmaking is used as a raw material. Although the technology of using the thermal cracking procedure to recover waste tires has matured, the gaseous products generated in the thermal cracking process, or suspended particles such as dust and smoke can not be made. Effective treatment, in addition to causing waste of resources, there is still a problem of polluting the environment. 'If the gaseous product contains toxic gas, it will cause harm to the human body; the current thermal cracking system for the thermal cracking second order is known. The architecture, including the power supply of the system, the thermal cracking process, the recovery of useful pyrolysis products, the discharge of unwanted pyrolysis products, etc. Complete and lack of good integration, is how to make the overall structure of the thermal cracking system more perfect, to make it more efficient and achieve more diversified applications, is an important topic in the field of thermal cracking recycling. The main purpose of the present invention is to provide a composite material thermal cracking integration system capable of recovering and refining a substance by a thermal cracking process, and solid, liquid, gaseous, flammable, non-flammable in a thermal cracking process. The product is a complete recovery or discharge treatment, and environmental protection. The present invention is a composite material thermal cracking integration system. The system architecture includes a thermal cracking unit, a material processing unit, a dust collecting unit, and a filtration. a discharge unit, and an energy supply unit. 6 200836902 = The thermal cracking unit comprises a cracking furnace, wherein the cracking furnace is provided for the pyrolysis process to be placed in the cracking chamber for the thermal cracking process; , the gaseous product produced when the material to be reclaimed is thermally cracked, according to whether it is flammable or not; The dust unit is connected to the cracking furnace for collecting the thermal cracking procedure 2:: particles, avoiding the scattering of the environment around it; _ 拼 茂 早 can be connected to the cleavage., _ . .盥Dust collection list=Used for non-recyclable substances generated in the pyrolysis process and attached to the energy supply unit to apply solar energy, wind power, natural energy of electricity Z and 'electrolyzed water to produce chlorine and oxygen mixture, after burning After the machine is ignited = the pollution-free oxy-oxygen flame energy is generated to supply the source of the operation of each unit, and it can be set at the exhaust pipe of the cracking furnace of the cracking furnace to generate electricity, and is matched with an external auxiliary power source, for example An internal combustion generator, t, the electrical energy required to operate the system. 2 The system can be used in a single cracking furnace or in parallel with multiple cracking furnaces for 敎:: sequence' and its cracking furnace can be an electric pyrolysis furnace or a hot gas cracking furnace. The U solution furnace uses a hot plate to pass current to generate bismuth cracking. Procedure = ΓΓ, and the gas cracking furnace uses an externally supplied flammable gas to form a liquid, and the hot gas generated after ignition is used as a heat source, although the source is different, both of which are heated through the cracking chamber. Pyrolysis in the chamber is a solid, liquid, flammable, or non-flammable material to be reconstituted for reconstitution. The bismuth material processing unit may comprise a vacuum pump connected to the cracking chamber, wherein if the refractory substance is flammable, the gaseous product generated by the pulverization process after the thermal cracking process is pumped through the vacuum pumping through a condensation 200836902, After being condensed into a flammable liquid, it is stored in a flammable liquid storage tank. The flammable liquid can also be separated from the pure flammable liquid by the A-oil separator, and then stored in the flammable liquid storage tank. If it is cooled by the condensation, it is not condensed into a liquid flammable gas. Then, the auxiliary burner that can be sent to a main burner or an auxiliary combustion device is ignited and burned into hot gas as a heat source of the gas cracking furnace. The right to-be-recycled material is non-flammable, and the gaseous product can be recycled after thermal cracking. The ruthenium is pumped out through a vacuum pump and condensed by a condenser, and then stored in a non-flammable liquid storage tank, and the gaseous state cannot be recycled. The product can be directly discharged to the filter unit after being exhausted in the cracking chamber, or can be burned and disinfected by the combustion chamber of the combustion device and the combustion chamber of the main burner, and then sent to the filter unit for discharge. After the thermal cracking process is completed, the remaining liquid material 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, and π is opened for taking out the solid matter. When the furnace cover of the cracking furnace is opened, the dust collection unit of the dust collecting unit can be started to prevent the powder # lf, the smoke, the steam from overflowing, and the cleared air is sent to the filter discharge and discharged again, and then the cracking furnace The hot gas used in the thermal cracking process may also be sent to the discharge unit for filtration and discharge after use. The ritual ware is used to electrolyze water into hydrogen and oxygen, and ignite the _ and Wang Ai's rolling and helium gas as the non-polluting enthalpy of the gas cracking furnace. The gas cracking furnace can also be combined with a main burner to burn fuel, for example, by externally inputting ... gas, combustible liquid, or hydrogen and oxygen produced by a hydrogen-oxygen generator to generate heat 8 200836902 Gas supply for (4) solution The heat energy required for the process. The composite material thermal cracking integrated system of the present invention can treat the material in a squeaking process and recycle the solid state generated in the thermal cracking process? Liquid ~, smoldering, flammable, non-combustible products for a complete recycling or disposal, i: choose the brake field account + /,, use the self-produced and natural energy supply system to operate:, also achieve energy saving The effect, and the useless mass produced in the thermal cracking process "(4) Dust collecting unit and the sputum discharge unit are filtered and discharged, and both: Baozhi 1 cheng's - is different from the traditional thermal cracking system, Will be: Determined:: The complete solution for the disposal of waste and the extraction of useful materials [Implementation] Please refer to the first to third figures and the fifth to the temporary ~ seven figures, the composite material thermal cracking integration of the present invention The system contains...

a thermal cracking unit (B) comprising a p X ^ cracking furnace (BS) (B }, the cracking furnace (BS) (BE), and the amp 埶 # 糸 糸 糸 糸 糸The program comprises an opening + a sneaker, an outer wall of the furnace body (B 1 3 ), and ~, β 1 3 having an opening, and a furnace (盍0) is disposed in the inner furnace body (Bl ( ^ J ) In the opening, the inner furnace body and the crucible 3) are a cracking chamber 1 ^ , k for accommodating the to-be-recycled material, and between the outer furnace body (B11) and the inner furnace body (Bl pa 丄d ) a heated air

The company can accommodate the heating element to add to the recyclables in the cracking chamber (B 敎ν β 3 ), wherein the heating element can be hot gas, electric heating # Ί Ί λ rebel, in the outer furnace The inner side wall of the body (Β 丄丄) is provided with a heat insulation layer (Β 1 24 C, to provide a heat insulation effect 200836902) to slow down the heat loss rate of the heating body in the heating space, and avoid the surface of the outer furnace body (B11) Temperature overheating;

a material processing unit (c), connected to the cracking furnace (BS) (BE) 'to carry out subsequent processing of the gaseous property produced in the thermal cracking process; /..., the B-dust collecting unit (D), connected to The cracking furnace (Bs) is used to collect the suspended particles generated in the thermal cracking process; the filter discharge unit (E) is connected to the pyrolysis single substance processing unit (C) and the dust collection unit (D), to > Early in the morning, used to filter the thermal cracking of 2 shells and discharge them; and harvest the source. An energy supply unit (the illusion, the energy required to supply each unit when operating, please refer to the furnace (BS) cracking chamber exhaust gas chamber (B 3 ) degree; and the hot chamber exhaust pipe ( (D), or For filtration and recovery, please refer to the figure and the above-mentioned 'cracking 5' and one; the external temperature is sent to the high temperature of the cracking, and the temperature can be cooled by the cracking and dust collecting unit, B, the twentieth BE is still ninth. Figures a, b and 19th, a, b (be) are provided with a cracking chamber inlet pipe (τ 笞 (T6) connected to the cracking chamber (B3) or liquid can be injected into the cracking chamber (D5) Moderately reduce the gaseous product produced in the cracking chamber (B 3 ) cracking process, T6) transport to the material handling unit (c) is the filter discharge unit (E), for further treatment or discharge treatment. The fifteenth figure A, B, the sixteenth figure a, the twenty-two figure, the above cracking furnace (BS) (10 200836902 includes - spiral leaf _ ^ (Β 5 〇), the spiral leaf transfer device (Β 50) The utility model comprises a driving stirrup (Β52) and a structure (Β51) (Β57), and the driving motor (Β52) is disposed at an opening of the furnace body (Β丄,) adjacent to the cracking furnace (BS) (,Β), the spiral blade The mechanism (B51) (B57) is located in the cracking chamber...) and its end is connected to the drive motor (B52) and rotated by the drive motor (B^2) to agitate the material to be recovered in the cracking chamber. It can be uniformly pyrolyzed; the spiral blade mechanism (B 5丄) can have a plurality of blade groups arranged side by side, and the blade groups rotate around the same fixed axis to stir the to-be-recovered material; the spiral leaf mechanism (B 5 7 ) It may have only a single-blade group, and the blade group may be moved in a vertical direction in addition to a certain axis rotation, to uniformly collect the to-be-recovered material. Motor (B54), a magnetic steel sheet (B55), see Figure 23, the above cracking furnace (BE) or may not have a spiral leaf mixing device (B5〇), but set a magnetic stirring; (B50 '), the magnetic stirring device (B5〇 includes, and a magnetic stirrer (B53), the motor (B54) is disposed under the inner furnace body (b13), and the magnetic steel sheet (B55) is set Under the inner furnace body (Bi3) and connected to the power output shaft of the motor (B54), the motor (B 5 4 ) is driven to rotate, and when rotated, generates a rotating magnetic field, the magnetic stirring rod (B 5 3 ) The manger is placed at the bottom of the cracking chamber (B 3 ) and is driven by the rotating magnetic field generated by the rotation of the magnetic steel sheet (B55) to stir the waste to be recovered in the cracking chamber (B 3 ) to make it uniformly heated. For cracking, the magnetic stirrer (B5 3) can be an elliptical magnet, coated with Teflon 11 200836902 or other materials that are resistant to high temperature, abrasion, chemical and chemical residues, and easy to clean and smudge. A, B and second Η - Figure, a liquid can be placed at the bottom of the above cracking furnace (BS) (BE) The discharge pipe (τ 7 ) is connected to a liquid storage tank (s丄), and the liquid substance remaining after the completion of the thermal cracking process flows through the liquid material discharge pipe (T 7 ) to the liquid storage tank (S 1 ) to The subsequent recycling. Twenty) (Β The removal of the Β, in the set (Β 5 2), the side wall of the outer furnace body is set, and 6 2) 2) the movement of the chamber, take (Β 7蚺翏读弟17图A, B, 18th figure A, B and 4A, B and 25th A, B, the above cracking furnace (Bs E) can still be equipped with - take-out device (B60 (B7〇), mourning (B60) (B7〇) has various implementations. Please refer to the seventeenth figure A, B and the twenty-fourth figure A, the take-up device (Bfin, -~) In an embodiment, the removal device 60) includes a removal frame (

^ 6 1 ) and a drive motor (R and the cracking furnace (B s) f R pB (there is a trough, the inner furnace body (BI outside the furnace body (Bll) (Βι" The groove is provided corresponding to the outer furnace n (Bl1 wood (Β61) can be moved laterally to selectively 妯, the mountain and the inner furnace body (Β 13) are selectively inserted into and out of the cracking chamber alveolar joint to be taken out Rack (Βθ 3), the drive motor (b power, this, at the second end) provides a take-up frame (B 6 state substance, can be operated after the completion of the cracking process remains in the cracking device f Ρ n, see The eighteenth w CB60) is taken out.

In the embodiment A, the "D out device (Β7〇) μ and the twenty-fifth figure A, the second embodiment, the take-out device 12 200836902 0) includes a take-out frame (B7 work), a drive motor - Pushing frame (B73), push-pull motor (b74) ..., and a dust suction pipe (T8), and the bottom of the furnace body (B13) in the cracking furnace (b=BE) is provided with a groove, and the bottom of the outer furnace is also provided It has a groove corresponding to the bottom of the inner furnace body") and can be longitudinally moved in the inner furnace body (Bl3) and the frame (: 1 1) in the socket, and can selectively enter and exit the cracking chamber drive motor (B72) ) is connected to the take-up rack (B 3), which is the power of the B-Mobile, which is connected to the push-pull (B7) 3 in the lateral direction of the push-pull (two-end 'provided to be placed in the cracking furnace (Bs)) Below B-E), the power of the push-pull motor is moved. When the take-up frame (B71) is lowered to 1 73), the push-pull motor (b74) can be used to push the frame (, & height, on the rack ("" The solid matter is pushed to the "3) traverse, and will be transported by the transport vehicle ("6) to him: the vehicle (...) on the dust cover ("5) is placed in the take-up frame, the step-by-step process, the defense Around, prevent taking The solid bear f) and the push frame (B73) smoke diffuse...etc.) are scattered around, and the dust suction pipe 7 pulls (including the dust and dust cover ("5), the dustproof single) can be extended into the defense with its end Absorption concentration; cracking furnace (BS) (Be) 5) Suspended particles of the towel - groove (B") for removal · (Β below the ground or can be set to be flush with the ground' convenient push frame (β 1 ) The solid material that can be contained when it descends is pushed down to the transport vehicle (Β76)) The take-up rack (Β71) Please refer to the twenty-sixth figure 'The cracking furnace (., ϋ b ) ( β £ ) or can be 13 200836902 There is no take-out device (B6〇) (b 7 π ^ sister / η, ΰ 70)' and a lifting device (B8〇) 5 ^ s ^ ^ ” is provided.) The lifting device (B") contains - slide rails (B8 crane (B81), and a container blue slide (B 8 3) are set at the cracking 煻f π 0, .... above the cracking furnace (BS) ( Β Ε ), the day

The vehicle (8 1 ) is slidably disposed on the slide rail (BR r R 〇0 , , the moon rail (B83), and the hopper basket (ΰ82) is connected to the rope body (brj, by # 〈8 4 ) to On the crane (Β 8 1 ), it can be selectively raised and lowered by winding the rope (Β84) 夕楼植二阳) to hold the objects to be reclaimed in the basket (Β

In Q 0 , 82), the to-be-recycled material is cut into the cracking furnace (B S ) ( Β E ) by the lifting of the basket (B 8 2 ).

The pyrolysis process is carried out, and the solid matter remaining on the basket (Β 8 2) is hoisted out in the hot cracking and ten; T ..., and the order is transported to Shaoguan Chuyu, and he is further advanced. Processing.芩月芩芩弟27十七, c Β Ο Λ r ρ , , , , C and D, the above cracking furnace C Β S } (BE) may not be set to drive to the month η shift, out Set (β60) (Β70) and the hanging device (Β80), and ## and set a pouring device (Β90), the pouring device (Β90) contains "(Β90) knowledge, decoction Bracket (Β92), a drive motor (Β 9 1 ), and dozens of 矜牟iRQ9, and several horse temperature resistant hoses (B 9 3 ), the set of wood (B 9 2 ) is set at 蚰;u , the upper part of the cracking furnace (BS) (BE) passes through a pivot column; ^ B b ; 1 ) the pivot is not above, the drive motor (Β) δ is placed on the support frame (Β9 2), ι 9 , z ) and can be rotated to pivot the column (B 9 2 1 ) to pivot the cracking furnace (New Zealand, fine, after the cracking furnace (Β E) is tilted to a certain angle and can be thermally cracked The solid matter remaining after the completion of the procedure is dumped, "main delivery vehicle (B94), transported to other places for further processing. One of the Nanwen temperature hoses (B 9 3) is attached to the cracking furnace ( β S) (BF, from yyd)

E) On the outer side wall, the function of the high temperature resistant hose (B 14 200836902 9 3 ) is fuel, heat, electric energy, air, water, and flammable, non-flammable gas, liquid discharge, (T ... solution The furnace (... Reduced Ligong 4 solution furnace (β e ) weight is applied to the pivot column (B 9 2 1 channel, making the drive motor (Β 9丄) more susceptible to cracking =

E) pivoting. u W ( B above cracking furnace (BS) (BE) and female less ^ ^ ) has the embodiment of the evening, and is a gas cracking furnace (BS), but also Lei Xianjin electric pyrolysis furnace (BE ). In the second embodiment of the present invention, the cracking furnace (B s)

Q, Sun ^ You are a burning cracking furnace (B, eight heating space is a gas chamber (B said corpse ^, 丄) to accommodate the sorghum',, rolling to produce a heated inner furnace body (B 1 3) The required thermal energy.... The gas cracking furnace (BS) can be connected to the gas chamber (B 1 ) from the gas inlet pipe (T 〇).

n, recognition,, door / dish burning can be transported from the gas inlet pipe (T 〇) to the gas chamber (Β 1) in the oblique smell, 丄) in the inner furnace body (Β 13) heating. Please refer to the tenth figure Α盥Β, 兮μ > ^ 八 4 milk cracking furnace (BS) or input pipe (Τ〇), and set the fuel input pipe ((chuan, and the fuel wheel into the pipe ( Τι) Enter the setting of the fuel to the entrance of (Β 1 ) - You At 9, 疋 (1 8), gaseous or

η Λ VAi [1 8 ) Ignition in the gas chamber (B) after burning, 'become a high temperature gas to the inner furnace body. The gas cracking furnace...

0 , ^ ^ Set a main burner intake pipe (T Λ Λ main burner (1 8), so that the external air or non-combustible rolling body can be from the main burner intake pipe ( ^ ^ 1 , 1 2 ) to the main burner (1 15 200836902 8 ) to mix gaseous or liquid energy

The burning of w, igniting in the gas chamber (B for combustion sterilization; not to be secret # μ ^ & ", ^ ^ milk body, for example, the use of biological or mineral extracts of unwanted substances, to another Fan Xi A ^ The gas cracking furnace (BS) still contains the gas chamber injection tube (τ), which is produced by the medical treatment, toxic, special waste, etc. And the gas to the exhaust pipe (τ 4 ) is connected to the gas chamber (B 1 ), and the gas or liquid with a lower temperature can be transferred from the gas chamber inlet pipe (τ 3 ) to the gas to (Β 1 In the middle of the gas chamber (β 1 ), the gas in the combustion chamber (Β 1 ) can be output to the filter discharge unit via the gas chamber exhaust (Τ 4 ). (Ε) + for further cooling, filtration, or discharge treatment. Please refer to the tenth - figure A, B, c and D, the above gas cracking furnace BS) towel can be provided with at least one heat transfer tube (b 2 at least one pass & (B 2 ) extends from the gas chamber (B 1 ) into the cracking chamber (B 3 ), and both ends of the opening are connected to the gas chamber (B丄) to make the gas Room (bi) The gas can be penetrated into the cracking chamber (B 3 ) by flowing through the heat transfer tube (B 2 ). The heat transfer officer (B 2 ) can be designed according to the different material properties of the recycled material, and the different structures and quantities can be designed. The material to be recovered in the cracking chamber (B 3 ) is uniformly heated. Referring to Figures 12A and B and Figure 13A and B, the gas cracking furnace (BS) towel may still contain a baffle. (B4) is disposed between the Lu body (B 1 3 ) and the outer furnace body (B丄丄), and divides the space in the gas chamber (B 1 ) into a plurality of mutually connected flow passages to make the gas chamber (B丄) 16 The gas in 200836902 can flow along the flow path to the gas chamber exhaust pipe (T 4 ), so that the gas flow can be more evenly distributed throughout the gas chamber (B 1 ) to the cracking chamber ( B 3 ) uniform heating; the baffle (B 4 ) can be longitudinally disposed between the inner furnace body (B 1 3 ) and the outer furnace body (B 1 1 ), and the gas chambers (B丄) are spaced into a plurality of longitudinal flow passages ( As shown in Figure 12A), the deflector (B ^ ) can also be placed laterally between the inner furnace body (B 1 3) and the outer furnace body (B丄丄) to separate the gas chamber (B 1 ) a number of lateral flow paths (as shown in Figure 13a), none The baffles (B 4 ) are disposed laterally or vertically to achieve the effect of uniform heating. Please refer to the fifth to eighth figures and the nineteenth aspects of the eighth and sixth, in another preferred embodiment of the present invention, The cracking furnace (BE) is an electrothermal cracking furnace (β E ), and a heating plate (Η 1 ) is arranged in the heating space, and an electric winding (Η〇) is connected to the electric heating plate (hi), the electric heating plate (HI) is disposed around the outer side wall of the inner furnace body (Β 13) for generating heat energy to heat the inner furnace body (Β 13), and the cable (H0) is used to provide heating of the electric heating plate (η 1 ) The power. Referring to FIG. 20A and B, the electrothermal cracking furnace (BE) further comprises an electric heating tube (H2) extending from the electric heating plate (H 1 ) into the cracking chamber (B 3 ). The heat energy is evenly distributed in the cracking chamber (B 3 ), and the material to be recovered in the cracking chamber (B 3 ) is uniformly heated. Referring to the first to eighth figures, the above-mentioned substance processing unit (c) can have a vacuum pump (1 2), and the input end of the vacuum pump (丄2) is connected to the cracking furnace (BS) (Β E ) Cracking chamber exhaust pipe (τ 6 ), 17 200836902 = "Gaseous product generated in the thermal cracking process is extracted from the cracking chamber" to be transported to other places for processing; the output of the "3) 2) Or it can be connected to the fuel inlet pipe (τι). '/ 1 上=物. The mass processing unit (c) can still contain a condenser 6) (1 1) wheel end connected to the cracking chamber exhaust pipe (τ The second output is connected to the vacuum pump (12), and the gas is extracted from the cracking chamber (B3) by 2 (1). The cold state is sent to the vacuum pump (1 2 ). 仃(9) attack: object. Treatment early 7^ (C) can also contain - combustible liquid storage tank w combustible liquid storage tank (9) of the input end connected to the vacuum pump =) 'flammable gaseous products in the condenser (work i) After becoming a combustible liquid, it can be stored by direct air pumping μ^ μ r Q , /, industrial mercury (1 2 ) to flammable liquid \ ) storage; the output of flammable liquid (4) (9) is connected to the combustion ^^ & (T1), to transfer the combustible liquid stored therein to the main combustion unit (18) of the gas cracking furnace (BS) through the fuel input official (π), in the combustion chamber, in the gas chamber (B 1 ) forming a high-heat gas; in addition, the combustible liquid stored in the combustible liquid storage # ( 9 ) can be recycled through the fractionation process. 'flammable gaseous products such as waste tires, waste plastics, oily materials, etc., heat Gaseous product produced after the cleavage procedure. The above material processing unit (c) may further comprise a non-flammable liquid storage 2 (, 10), the input end of the non-flammable liquid storage tank (10) is connected to the true two pump (1 2 ), useful non-flammability After the gaseous product is condensed in the condenser (Work 1) and becomes a non-flammable liquid, it can be taken to the non-flammable liquid storage tank (1 〇) by vacuum pumping (work), and the non-flammable liquid is coming 18 200836902 The source may be a useful substance after biological or mineral extraction by a pyrolysis process, and the material processing unit (C) may further comprise an auxiliary combustion device (1, 'the auxiliary combustion device (16) is provided with an auxiliary burner (16 ^ combustion tank (162), the input end of the auxiliary burner (161) is connected to the straight space 1 〃 汞 mercury (1 2 ), produced in the thermal cracking process, and used for non-flammability The gaseous product can be pumped to the combustion tank (1 6 2 ) via vacuum pumping (1 2 ), burned and disinfected in the combustion chamber (i 6 2 ) via the auxiliary burner (i 6 2); The flammable gaseous product produced during the cracking process can also be condensed into flammable liquid after condensation (1 1 ) It is pumped by vacuum pumping (1 2) and sent to: the burning tank (ι 6 2 ) as fuel, and after combustion, the heat is generated. After the treatment by the condenser (1 ^ ), the flammable gas state of the flammable liquid is not condensed. The product can also be supplied to the main burner (18) as a fuel by means of a vacuum fruit pump (1 2 ) to a fuel inlet pipe (Ding), or a fuel-assisted burner (1 6 ) can be used as a fuel. After combustion, hot gas is generated. The output end of the combustion tank (1 62) is connected to the filter discharge unit (E), and the exhaust gas generated by the use of the non-flammable gaseous product after combustion sterilization and disinfection is filtered. The discharge unit (E) is filtered and discharged. The output of the mouth-fired k-tank (1 6 2) can still be connected to the gas input pipe (Ding) of the gas cracking furnace (BS) for the combustion tank ( 1 6 2) The hot gas generated after the combustion process is carried out, and is heated to the inner furnace body (b丄3) through the gas input pipe (T 〇) to the gas chamber (B work). The output of the combustion chamber (1 6 2 ) can still be connected to the main burner intake (T 2 )', thereby generating in the thermal cracking process Non-flammability 19 200836902 6 2 ) The combustion can be ignited by the auxiliary burner (1 6 1) in the combustion chamber (1 burner ΓΓΐ, Γ is delivered to the main _ via the main burner intake pipe (T2), It burns once to achieve the effect of full sterilization. 5Hai material processing unit f, the temporary description r% (C) still contains a temporary storage tank (13), for the input of the true *^ 13) is connected to the vacuum pump (12), can be:::^1 2) The flammable liquid is pumped to the temporary storage tank 3) T storage, the temporary storage sputum storage tank (9) is connected to the flammable tank through a bidirectional pipeline (9) a needle for transporting the flammable liquid temporarily stored therein to the flammable liquid reservoir; and supplying the flammable liquid in the flammable liquid storage tank (9) to ==) (:::; the temporary storage tank ( " Once the main combustion M h QM transports the flammable liquid temporarily stored in the machine: (18) or auxiliary combustion machine (161) as fuel, enters the enthalpy and generates hot gas. The material processing unit (<Γ, fire the oil water separator (14) to a water separator (14)' 4) input terminal is connected to the temporary storage tank, and the output end thereof is respectively connected to the auxiliary identification opening machine (161) and (4) Emissions: "The output can also be connected to the main burner (18) and connected to the flammable liquid storage tank (9) through the - bidirectional pipeline to the vehicle (1)' temporary storage tank ( 13) The temporary storage of the medium can be... The oil-water separation process is carried out in the oil-water separator (14) to separate the heart-burning liquid and the waste water, and the pure combustible liquid can be transported to the flammable liquid storage tank (9) for storage or transportation. To the main burner (18) and the auxiliary burner (1: for fuel, waste water is sent to the discharge unit (e) for discharge; oil-water separator (1 4 ) 柘ψ妯p σ, 丄 4 ) After the pure combustible liquid is precipitated, it can also be sent to the main burner (1 8), which is sent to the main combustion machine (1 8 ), and the auxiliary combustion machine (1 6 1 ) is used as a burning gas to separate the oil and water. (i 4) provides seven temporary storage of flammable liquids for the wheel 4), in the temporary storage tank (1 3 ) (ί 6 Ί ) ' burner (18) or auxiliary burner (1 6 1) as Burning ; -r ^ , if the right flammable liquid is directly transported from the temporary storage tank (1 3 ) to the sputable liquid, the QW material (9) stores the material in the flammable liquid storage tank C 9 , ", light transmission to the oil-water separator (1 4) precipitated pure combustible liquid and then delivered to the host burning, ~, heart machine (18) or auxiliary burner (] _ 6 1) as fuel.

70 (C) also includes a cleaning liquid tower 1 7 ) whose output is connected to the auxiliary combustion 162), and can be further connected to the combustion chamber (B 1 ) for injecting the cleaning liquid into the material processing unit (17). ), the cleaning liquid column (the combustion chamber of the device (1 6 ) (the gas combustion chamber (1 6 2 ) of the gas cracking furnace (BS) to put the combustion tank (丄6 2 ) or the gas chamber (b 1 The cleaning unit (D) includes an exhaust dust collector (2 〇), and the 忒 evacuation dust collector (20) can be placed in the furnace body adjacent to the cracking furnace (Bs) (b E) ( b 1 3) The opening is used to absorb the suspended particles generated by the pyrolysis furnace (Bs, (BE) when the furnace cover (b 〇) is opened, and is scattered in the thermal cracking process; the exhaust dust collector (2 〇) can also be placed in the groove of the furnace body (Β ί ί ) adjacent to the cracking furnace (BS ) ( BE ) to absorb the extraction frame ( B6 1 ) and then fly around in the thermal cracking process. The suspended dust particles (D) further comprise a cyclone (2丄), and the input end of the cyclone (2 1 ) is connected to the cracking chamber exhaust (Tr,, 21 200836902 to extract the gaseous products generated in the thermal cracking process from the cracking, and to separate the particles from the gas stream to collect the suspended particles by the action of centrifugal force; the cyclone dust collector At the input end, it can be connected to the exhaust dust collector (2〇) for the suspended particles sucked by the hurricane dust collector (20). The present dust collection unit (D) still contains one Cooler The input end of the cooler (19) is connected to the cracking chamber exhaust pipe (the output end of which is connected to the cyclone (21) for heat generation) to generate a gaseous product through a cooling process After being sent to the cyclone (2 1 ) to filter the suspended particles contained therein. 卞α〇 The above dust collection unit (D) still contains the net (the input end of the crossing net (22) is connected to the cyclone dust collector (21), used: Filtering the suspended particles remaining after the cyclone dust collector (2 1 ) (4)' is used for the above dust collecting unit (13), which also includes a bag type dust collector ((1)), the bag The input end of the dust collector (23) is connected to the filter screen (22) for filtering the filtered and meshed (2 2 ) collections. Suspended particles; the output end of the bag filter (23) is connected to the over discharge unit (e) to pass the gas remaining after the dust collection unit (D) has passed through the discharge unit ( E) Emission after filtration. Suspended particles collected by the extractor (2〇) can be further composed of cyclone (2 1 ), strainer (2 2 ) and baghouse (2 3 Filtering 'by this, when the gaseous product is transported to the sputum discharge unit TO ( E ) by the dust collecting unit (d ), the suspended particles are largely filtered out; and 3 the gaseous products of the suspended particles are also It can be directly discharged to the over-discharge unit (E) after being sucked by the suction dust collector (2 〇) 22 200836902. The filter discharge unit (E) includes a chimney (29), and the wheel end of the smoke 111 (29) is connected to the dust collecting unit (D) for discharging the dust collected by the dust collection unit (D). gas. The filter discharge unit (E) further includes an exhaust fan (28), the input end of the exhaust fan (28) is connected to the dust collection unit A (D), and the output end is connected to the smoke (2 9 ). It is used to extract the gas treated by the dust collection unit (D) and transport it to the smoke _ (29)#; the exhaust fan (2 input ^% can be connected to the exhaust dust collector (2 〇) or bag dust collection The device (23) can also be respectively connected to the two, and the useless gaseous product generated by the thermal cracking can be collected by the exhaust dust collection $ ( 2 Q ) and directly extracted by the pumping machine (2 8 ) to the smoke ( 2 9 ) Emissions, and if there are too many suspended particles in the gaseous product collected by the extracting dust «( 2 〇), you can enter: step by cyclone (2丄), filter • 罔 (2 2 ) with the bag

After collecting the dust particles (2 3 ) W suspended particles, the gaseous products are extracted into the chimney (2 9 ) through the exhaust fan (2 8 ). The above-mentioned over-discharge unit (E) further comprises a clean water/chemical scrubbing tower (=5), and the input end of the clean water/chemical scrubbing tower (25) is connected to the dust collecting early element (D) for passing through the collection. The chemical substances contained in the gas remaining after the dust sheet a (D) treatment, such as sulfur oxides, nitrogen oxides, etc.; the round/out ends of the water/chemical washing material (25) are connected to the exhaust fan (2) 8) 'Extract the gas after filtering it through the exhaust fan (28) to the cigarette (2 9 ) Emission '·Shaw clear water / chemical wash tower (2 5 ) input terminal f is connected to the bag dust collector (23) or extracting dust H (2〇), 23 200836902 can also be connected to the two, after thermal cracking ==_ (2〇) suction, transport = progressive filtration, and if the wind collection Dust collector (2 夹 气 之 之 气 气 气 气 气 气 气 气 气 气 气 气 气 气 气 气 气 气 气 气 气 气 气 气 气 气 气 气 气 气 气 气 气 气 气 气 气 气 气 气 气 气 气 气 气 气The gas-based raw water wash 2 5) further transition " to - "Chemical filter discharge single it (E) still contains - water tower (2) The output of the water tower (2 4) is connected to clean water /Chemical washing, the working water required for filtration in the clean water/chemical washing tower (2 5 ). /, The above-mentioned filtration 'emission unit (E) still contains - waste "biological treatment device" the wastewater / biological treatment The input end of the device is connected to the oil-water separation and crying: 1 4) 'After treating the wastewater separated by the oil-water separator (14): discharging after forming fertilizer or waste material; the wastewater/bioprocessing device (2 6 ) The input end can also be connected to the clean water/chemical scrubbing tower (25), and the working water used after the clean water/chemical washing tower (25) is used:: into fertilizer or waste material discharge. y The above-mentioned filter discharge unit (E) may further comprise an activated carbon column (27), and the input end of the activated carbon column (27) is connected to the clean water/chemical wash tower (25)' The exhaust fan (28) is used to: deodorize the gas filtered by the clean water/chemical scrubber, and then pump it to the cigarette (2 9 ) for discharge by the exhaust fan (28). The above energy supply unit (A) comprises at least one generator and a power control device (6) selected from the group consisting of solar energy 24 200836902 generator (1), wind power generator (2), hydroelectric generator (3), and a group of internal combustion generators (4), the input end of the power control device (6) is connected to the at least one generator to provide functions of switching, voltage transformation, power storage, and power distribution The output of the power control device (6) is connected to each unit of the composite material thermal cracking integration system to supply the power required for operation and control of each unit; the composite material thermal cracking integration system of the present invention is borrowed The geographical and climatic environment of the installation location can be matched with a suitable self-strain system that can use solar generators (1), wind turbines (2), or hydroelectric generators (3), such as parasols ☆ gnshi J When the Tianxian first is sufficient, the solar generator can be used (1). When the wind is rainy, the wind turbine (2) can be used to generate electricity. If the installation location is close to the river, the reservoir, the estuary, etc., the water can be used. The machine (3) mines, dies, and makes full use of natural resources; while solar generators (1), wind power planting machines (2), and hydroelectric generators (3) use natural energy. When the generator cannot operate smoothly, the internal combustion generator (4) can be used to generate electricity, and the power supply required for each single connection can be provided. The energy supply unit (A) g may be -, A) may further comprise a hydrogen-oxygen generator (7) and a mixture (8), the input end of the hydrogen-oxygen-producing glutinous milk-birth (7) is connected to a water tower (24) for electrolyzing the water source provided by the water tower (?, κ producing κ2) into hydrogen and oxygen'. The input end of the mixer (8) singapore (n, ^^t) is connected to The oxyhydrogen generator (7)' has its output connected to the 烨 仏 r r r r r r r r r r r r r r r r r r r r r r r r r r r r r r r r r r r r r r r r r ^ A ceremony and milk mixing are transferred to the main burner (18) IX, L, and in the gas chamber (only - ^ ^ 1) to generate a pollution-free high heat igniting to the thermal combustion cracking furnace (B s ^^ QX ^ 円 furnace body (B 1 3 ) heating; the output end of the a (8) can also be connected to the auxiliary burner (1 6 1), 25 200836902 to provide an auxiliary burner (1 61) The fuel required for combustion. The above energy supply unit (A) may further comprise a 々(5) 'the input of the ternary wheel generator (5) is eight), and its output is connected to the power control device (a ^, the gas turbine is in the thunder By means of the wheel generator (5), the gas discharged from the gas chamber exhaust gas can be used to generate electricity, and the generated electric energy is sent to the power control device for use; the use of the gas turbine generator (5) It can also be connected to the combustion tank of the auxiliary combustion (16) ("non-combustible gas is burned and sterilized in the ^ 梓 ' ^ ^ ^ ^, 钇 钇 (1 6 2), can be discharged to the ^ wheel generator Power generation; the turbine generator (the end can also be connected to the cracking official _ #, the gas discharged from the sputum and the material inlet pipe (T6) to generate electricity. The ritual «month see the fourth and eighth figures' in the composite of the present invention In another preferred embodiment of the thermal decomposition integrated system of the formula, the above-mentioned thermal cracking unit (the B coating may comprise a plurality of cracking furnaces (BS) (BE) connected in parallel with each other, and each column furnace (BS) (Be) comprises There is a furnace body (b 13) having an opening, and an outer furnace body (B11) covering the inner furnace body (B13) The outer side wall and a furnace (B 〇) are arranged in the inner furnace body (B 1 3 port, and the inner furnace body (B13) is a cracking chamber (B3) for accommodating the to-be-recycled material] (B 1 1 ) The inner furnace body (B 1 3 ) is - the heating space 'can accommodate the heating element to heat the to-be-recovered material in the cracking t (B 3)': the outer furnace body (B i 1 The inner side wall is provided with a heat insulating layer (B 12) to provide a heat insulating effect to slow the heat loss rate of the heating body in the heating space '1 to avoid overheating of the surface temperature of the outer furnace body (B11); 26 200836902 • The above substances The processing unit (c) is connected to each cracking furnace (B s) (BE ), respectively, and the dust collecting unit (d) is also connected to each cracking furnace (B s) (be); ), whether it is a gas cracking furnace (BS) or an electric pyrolysis furnace (be), the material to be recovered can be simultaneously subjected to a thermal cracking process in each cracking furnace (BS) (BE), and the material processing unit (C) is shared, The dust collection unit (d), the over-discharge unit, and the energy supply unit (A) perform the refining of useful substances and the filtration and discharge of unwanted substances. Please refer to the second figure. In another preferred embodiment of the present invention, the substance processing unit (B) includes an interconnected first auxiliary combustion chamber (31) and a second auxiliary combustion device (32), the first auxiliary The combustion device (3 1 ) is provided with a first auxiliary combustion machine (3 1 1 ) and a combustion tank (3 1 2) 'the second auxiliary combustion device (3 2) ^: one brother and one auxiliary combustion machine (3 2 1 And a combustion chamber (32 2 2), the first auxiliary combustion device (31) and the second auxiliary combustion device (32) are connected to the gas cracking furnace at the output end of the combustion chamber (312) (322) In the gas chamber (B 1 ) of (BS), in addition to igniting the combustible gas or combustible liquid through the first auxiliary combustor (31) and the second auxiliary combustor (32) in the combustion chamber (312) (322) ) It is burned into high temperature gas and then sent to the gas chamber (B 1 ). It can also be combined with the main burner (1 8 ) installed in the gas cracking furnace (b S ) to incombust the non-flammable gas state. The product is subjected to three-time high-temperature combustion sterilization and is then sent to the filtration discharge unit (E) for discharge. According to the description of the above embodiments, the present invention is a composite material thermal cracking integrated system capable of simultaneously processing solid 27, 200836902 two liquid, flammable, and non-combustible substances, and can be applied according to different types of materials to be recycled. The process of recycling can be used for thermal cracking of solid, liquid, flammable, and non-flammable materials to be recycled, and various products obtained by thermal cracking procedures, including solid, liquid, gaseous, combustible, and non-service The product is produced by various kinds of clothes corresponding to the library, such as taking out, condensing, purifying, filtering, sterilizing, etc., and then adding ^ ^ ^ ^ to identify the group, and depending on the recyclables: different use of the temple The design of the cracking furnace of the type is to use the natural energy and self-produced electric energy as the source of energy supply for the system operation, and to use the self-produced fuel and the pollution-free hydrogen emulsion as the oxygen-burning, The al*, deficient and μ/over-drainage units can be used to treat gaseous and liquid wastes through a wastewater treatment plant, which can be used to convert waste into fertilizers. discharge. Composite substance of the invention

= (4) When the system has diversified substances, refining treatment, and resources I: use: energy re-engineering, and it has the characteristics of energy saving and environmental protection, and it is more comprehensive for the treatment of composite materials. The use of the above-mentioned patents for the application of the invention is only a preferred embodiment of the present invention. Therefore, the equivalent structure of the patent scope of the invention is included in the patent application. Within the scope of the patent of the present invention. [Simple description of the drawing] The figure is a circuit configuration diagram of the first car mussel embodiment of the complex 热 物质 substance thermal cracking integration system of the present invention, and the 畀 contains a gas cracking 28 200836902 FIG. 2 is a circuit configuration diagram of a first preferred embodiment of the composite material thermal cracking integration system of the present invention, comprising a gas cracking furnace and a first auxiliary combustion machine and a second auxiliary combustion The third figure is a schematic diagram of the circuit configuration of the composite material hot crack shown in the first figure. The fourth figure of the σ system is the third preferred embodiment of the composite material thermal cracking integration system of the present invention. A circuit configuration diagram comprising two fuel cracking furnaces connected in parallel with each other. A fifth diagram: a circuit configuration diagram of a fourth preferred embodiment of the composite material thermal cracking integration system of the present invention, comprising electrothermal pyrolysis ▲The sixth figure is an embodiment of the composite material thermal cracking integration system of the present invention, which comprises an electrothermal cracking furnace and an auxiliary burner. The seventh figure is one of the fifth figures.婵翕 “,, and the schematic diagram of the line configuration of the hole table. Figure 8 is a circuit diagram of a sixth preferred embodiment of the composite material thermal cracking integration system of the present invention, wherein the package ^ ^ A 匕 3 has two electrothermal cracking furnaces connected in parallel. Fig. 9A is a schematic cross-sectional view of a gas cracking furnace of a composite material of the present invention. Figure IX Figure B: shows the top of the gas cracking furnace shown in Figure 9A. Figure A is the composite of the invention, the combustion of the #, ,, Qiaowubei pyrolysis integrated system; 4, the schematic diagram of the sodium view of the furnace, the straight kg (5) η eight packs each have a main burner. Ten Ten Diagrams: For the operation shown in the tenth figure a < β «I cracking furnace above the schematic diagram 29 200836902 figure. Fig. 11A is a front cross-sectional view showing the gas cracking furnace of the composite material thermal cracking whole body system of the present invention, wherein 覃i... π is obtained. Η 图Η: It is a top view of the gas ρ private cracking furnace shown in Figure 11. Eleventh Figure C: is a schematic cross-sectional view of a gas cracking furnace of a composite material of the present invention, which is provided with a "disintegration system", in which a plurality of heat transfer tubes are provided. / Tenth - Figure D: is the tenth - Fig. C is a top view of the gas cracking furnace shown in Fig. C. Fig. 12 is a front cross-sectional view of the gas cracking furnace of the composite material thermal cracking integrated system of the present invention, in which a longitudinal deflector is provided. Twelve Figure B: is a top view of the gas cracking furnace shown in Figure 12A. Figure 13A is a front cross-sectional view of the gas cracking furnace of the composite material thermal cracking integrated system of the present invention, wherein There is a horizontal deflector. Fig. 11B is a top view of the gas cracking furnace shown in Fig. 13A. The schematic diagram of the gas in the furnace of the material thermal cracking integration system is provided with a liquid storage tank. The tenth figure B 4 shows the top view of the gas cracking furnace shown in Figure 14A. ·Before the cup + person x month complex & material thermal cracking integrated system gas cracking furnace Illustrated ~ Figure 'The spiral blade stirring device is provided with a plurality of blade sets. 30 200836902 The fifteenth figure B · is a top view of the gas cracking furnace shown in the fifteenth figure A. Figure 16: A A schematic cross-sectional view of a gas cracking furnace for inventing a composite material thermal cracking integrated system, wherein a spiral blade stirring device is provided with a single blade group. "" Figure 16: Burning as shown in Fig. 16A The gas cracking furnace is top view. Qin No. 17: A: The front view of the gas cracking furnace of the composite material thermal cracking integration system of the present invention, which is provided with an open material removal device. Figure B ·· is a top view of the gas cracking furnace shown in Figure 17A. Figure 18: A front cross-sectional view of the gas cracking furnace of the composite material thermal cracking integrated system of the present invention, which is designed There is a closed material removal device. 帛18Fig. B: is a top view of the gas cracking furnace shown in Fig. 18A. Fig. 19A is a composite material thermal cracking integration system of the present invention Front section of electrothermal cracking furnace Figure 19B is a top view of the electrothermal cracking furnace shown in Fig. 19A. Fig. 20A: Shovel section of the gas thermal cracking furnace of the composite material thermal cracking integrated system of the present invention Schematic diagram, in which an electric heating tube is provided. The tenth figure B· is a schematic diagram of the electrothermal cracking furnace shown in the twenty-first diagram a, see 31 200836902. The twenty-first figure is the composite material thermal cracking integration system of the invention The front view of the electrothermal cracking furnace is schematicly arranged, wherein the spiral blade stirring device is provided with a plurality of blade groups. The twenty-second figure: a single blade group for the front view of the electrothermal cracking furnace. The surface of the composite material thermal cracking integrated system of the present invention The schematic diagram is provided with a spiral blade stirring device/23rd view: a schematic front cross-sectional view of the electrothermal melting furnace of the composite material thermal cracking integrated system of the present invention, wherein a magnetic type transfer device is provided. Figure 14A is a schematic cross-sectional view of the composite material pyrolysis integrated cracking furnace of the present invention, wherein an open type: mass take-up device is provided. Twenty-fourth Figure B: Schematic diagram of the top view. It is the front view of the electrothermal cracking furnace of the electric pyrolysis furnace shown in Fig. 14A. The schematic diagram of the thermal decomposition integrated system of the composite material of the present invention is shown in the upper cross-sectional view of the twenty-fifth figure B. It is the electrothermal cracking furnace shown in Figure 25A.

Figure 26: Setting above the cracking furnace The cracking furnace of Figure 27A is placed in a twenty-seventh figure. Figure B is a front view of the mass lifting device of the composite material thermal cracking integrated system of the present invention. It is a schematic view of the composite material thermal cracking integration system of the present invention on the device. The pyrolysis furnace shown in Fig. 5 and Fig. 7 is set on the side view of 32 200836902. 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 (B55) 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 Room (B 1 1 ) The outer furnace body (B 1 3 ) is placed in the furnace body (B 5 2 ) The drive motor (B 5 4 ) The motor (B 5 7 ) The spiral blade mechanism (B 6 1 ) is taken out (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 200836902 (B 8 1 ) Crane (B 8 3) slippery ( B 9 0 ) pouring device (B 9 2) support frame (B 9 3) high temperature resistant hose (C) material handling unit (E) filter discharge unit (Η 〇) cable (S1) liquid storage tank (Τ 0 ) Gas input pipe (Τ 2 ) Main burner intake pipe (Τ 4 ) Combustion chamber exhaust pipe (Τ 6 ) Cracking chamber exhaust pipe (Τ 8 ) Dust pipe (2) Wind turbine (4) Internal combustion Motor (6) Power control device (8) Mixer (10) Non-flammable liquid storage tank (1 2) Vacuum pump (1 4) Oil-water separator (1 6) Auxiliary combustion unit (1 6 2 ) Combustion tank (1 8) Main burner (Β 8 2) Basket (Β 8 4) Rope body (Β91) Drive motor (Β 9 2 1 ) Pivot (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 (Τ 5 ) 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 ) Temporary storage tank (1 6 1) Auxiliary burner (1 7 ) Cleaning liquid tower (1 9 ) cooler 34 200836902 (20) extractor dust collector (21) cyclone dust collector (2 2 ) filter screen (2 3 ) bag type dust collector (2 4 ) water tower (2 5 ) water /Chemical scrubber (2 6 ) Wastewater / biological treatment unit (2 7 ) Activated carbon tower (28) Exhaust fan (29) Chimney (3 1 ) First auxiliary combustion unit (3 1 1 ) First auxiliary burner (3 1 2 ) combustion tank (3 2 ) second auxiliary combustion device (3 2 1 ) second auxiliary combustion machine (3 2 2 ) combustion tank 35

Claims (1)

200836902 X. Patent Application Range: 1 · A composite material thermal cracking integration system comprising: - a thermal cracking unit comprising a cracking furnace for injecting a thermal cracking process for the recovered material The furnace body has an opening, an outer furnace body is coated on the outer wall of the inner furnace body, and a < isolated 'temperature generation δ is in the inner furnace In the body opening, the inner furnace body is a cracking chamber for accommodating the to-be-recycled material, and the furnace body and the inner furnace body are a heating space for accommodating the heating body to be recovered in the cracking chamber. Heating the material on the side wall of the outer furnace body and providing a heat insulation layer; a material processing unit is connected to the cracking furnace to carry out subsequent processing according to the flammability of the gaseous product generated in the thermal cracking process The dust unit is connected to the cracking furnace for filtering the suspended particles generated in the thermal cracking process; a filtering and discharging unit is connected to at least one of the three units of the thermal cracking unit, the material processing unit, and the dust collecting unit to The non-recyclable substances generated in the thermal cracking private sequence are filtered and discharged; and the monthly b source supply unit supplies the energy required for each unit to operate. 2. The composite material thermal cracking integration system of claim 2, wherein the cracking furnace is provided with a cracking chamber inlet pipe and a pumping chamber exhaust pipe connected to the cracking chamber. The compound material thermal cracking integration system according to claim 1, wherein the cracking furnace comprises a spiral blade stirring device, and the fan blade stirring device comprises a driving motor and a spiral blade mechanism, and the crucible driving The motor is disposed adjacent to the furnace opening in the cracking furnace. The spiral vane mechanism is not in the cracking chamber, and one end thereof is connected to the driving motor and is rotated by the drive motor belt 36200836902. 4. The composite material thermal cracking integration system according to claim 1, wherein the cracking furnace comprises a magnetic stirring stirrer, and the magnetic stirring device comprises a motor, a magnetic steel sheet, a ri door M and a magnetic stirrer, the motor is disposed under the inner furnace body, the magnetic steel piece is disposed under the inner pity body and is connected to the power output shaft of the motor, and is rotated by the motor to be rotated and generated when rotating a rotating magnetic field, the magnetic stirrer is set in the column The bottom of the chamber is detonated by the rotating magnetic field generated by the rotation of the magnetic steel sheet. The moving material thermal cracking integrated system as described in claim i, wherein the bottom of the cracking furnace is provided with a The liquid substance discharge pipe is connected to a liquid storage tank. & 6 · The application integration system includes a take-out wall, a slot, a slot, and an optional one end, and is provided with a 7-integrated system, the device includes a take-out dust cover, and In the trough, the outer furnace bottom τ M month rfW, the crucible cracking furnace is further provided with a take-out device, the take-out rack and a drive motor, and the side wall of the furnace body on the side of the furnace outside the cracking furnace is also provided with a trough Corresponding to the outer furnace body, the outer furnace body and the inner furnace body are arranged to move laterally into and out of the cracking chamber, and the driving motor is connected to the power of the take-out rack. The composite material thermal cracking described in the first paragraph of the patent range is also provided with a take-out device for removing the wood-loading drive motor, a push frame, a push-pull motor, a * s ' and the cracking furnace The bottom of the furnace body is provided with a wearing portion and a trough corresponding to the bottom of the inner furnace body, and the 37 200836902 removal frame can be longitudinally swayed in the inner furnace body and the outer furnace body. In the middle, 廿7 selectively enters and exits the dream nucleus and can be used to remove the stalker who moves the rigging and lifts the power. The push frame can be moved laterally to the cleavage side of the 'Pushing frame 1» 4杳, 击下下" Connected to one end of the push frame, the movement of the push frame is provided. The dust cover is now covered by Yushan, and the dust suction pipe is reinserted into the dust cover. /, Wei Shen as claimed in the scope of patent application i. 0, *,,,,, ~ ~ τ and mouth; milk stomach pyrolysis Positively, wherein the cracking furnace is provided with a lifting device, the lifting device comprises a slippery, a one-day car, and a basket, the stomach slide is arranged above the cracking furnace, and the crane is slidably disposed on the In the sliding, the basket is connected to the crane through a rope body, and can be selectively raised and lowered by winding the rope. 9 · The composite material thermal cracking as described in the scope of the patent application The integrated system, wherein the cracking furnace is provided with a pouring device, the pouring device comprises a supporting frame, a driving motor, and a plurality of high temperature resistant hoses, the supporting frame is arranged on the ground for each of the two sides of the cracking furnace to pass through The pivoting column is pivoted thereon, the driving motor is disposed on the support frame, and the pivoting column can be rotated to pivot the cracking furnace. The high temperature resistant hoses are attached to the outer side wall of the cracking furnace. The composite material thermal cracking integration system according to Item 2, wherein the cracking furnace is a gas cracking furnace, and the heating space is a burning chamber for accommodating high-heat gas to generate a heated inner furnace body. Required heat. 1 1 · If applying for a patent The composite material thermal cracking integration system of the first aspect, wherein the gas cracking furnace is provided with a gas input pipe connected to the gas chamber. 38 200836902 1 2 · as described in claim 1 The composite material thermal cracking integration system, wherein the gas cracking furnace is provided with a fuel input pipe connected to the gas chamber' and a main burner is arranged at the inlet of the fuel inlet pipe into the gas chamber. 1 3 · If applying The composite material thermal cracking integration system according to Item 12, wherein the gas cracking furnace is provided with a main burner inlet pipe connected to the main burner. 1 4 · As claimed in the first section of the patent The composite material thermal cracking integration system according to any one of the items 1 to 3, wherein the gas cracking furnace comprises a gas chamber inlet pipe and a gas chamber exhaust pipe connected to the gas chamber. The composite material thermal cracking integration system according to claim 1, wherein the gas cracking furnace is provided with at least one heat transfer tube, and the at least one heat transfer tube extends from the gas chamber into the cracking chamber Medium, two of them The opening is connected to the gas chamber. 1 6 · The composite material thermal cracking integration system according to the first aspect of the patent application, wherein the gas cracking furnace comprises a baffle disposed inside the inner furnace body and outside Between the furnace bodies, the space in the gas chamber is divided into a plurality of mutually connected flow channels. 1 7 · The composite material thermal cracking integration system according to the second aspect of the patent application scope, wherein the cracking furnace is electrothermal cracking The furnace is provided with a heating plate in the heating space, and is provided with a cable connected to the electric heating plate. The electric heating plate is disposed around the outer side wall of the inner furnace body for generating heat energy to heat the inner furnace body, and the electric power is used for providing The electric energy required for heating the electric heating plate. 1 8 · The composite material heat as described in claim 17 of the patent scope 39 200836902 The cracking integration system 'where, the electrothermal cracking furnace comprises an electric heating pipe, which is extended by the electric heating plate Into the lysis chamber. [19] The composite material thermal cracking integration system of claim 2, wherein the material processing unit comprises a vacuum pump, and the input end of the vacuum fruit is connected to a cracking chamber exhaust pipe of the cracking furnace. 2 0. The composite material thermal cracking integration system of the invention of claim 19, wherein the material processing unit comprises a condenser, and the input end of the condensation is connected to the cracking chamber exhaust pipe, and the output thereof The end is connected to a vacuum pump, and the input end of the vacuum pump is connected to the cracking chamber exhaust pipe of the cracking furnace through a condenser. 2 1 The composite material pyrolysis integration system of the invention of claim 2, wherein the substance treatment unit comprises a combustible liquid storage tank, the input end of which is connected to a vacuum pump. / 2 2 · The composite material thermal cracking integrated system of claim 2, wherein the material processing unit comprises a temporary storage tank, a water separator, and a combustible liquid storage tank, the temporary storage The input end of the tank is connected to the vacuum pump, and the input end of the oil water separator is connected to the temporary storage tank, and the combustible liquid storage tank is respectively connected to the temporary storage tank and the oil water=offer through the bidirectional pipeline, and the output end thereof is connected To the fuel input pipe. 2 3 . The composite material pyrolysis integration system of claim 2, wherein the material processing unit comprises a non-flammable liquid storage tank, and the input end of the non-flammable liquid storage tank is connected to the vacuum fruit. 2 4 · The composite material 埶 cracking integration system as described in claim 19, wherein the material treatment unit has an auxiliary combustion 40 200836902 device, wherein an auxiliary gas turbine input is provided The end is connected to a straight-burning tank, which assists in the exhaust unit. "Lipu" The output end of the combustion tank is connected to over 2 5 · As claimed in the patent scope, the compound material is called the system of the compound substance, which is described in the article 1. The product and the auxiliary combustion device 1 The straight empty bag 3 has a vacuum pumping cracking chamber exhaust pipe, the auxiliary inlet end is connected to the cracking furnace A, and the auxiliary burner and the output end of the .f burning tank are respectively connected to the vacuum pump , the gas input pipe. The fuel discharge unit and the gas cracking furnace of the fuel cracking = two applications: the benefit of the range of material referred to in item 13 of the heat of the second:, the material handling unit contains - vacuum pumping chamber of the Lipu pump, the auxiliary person to the cracking furnace _ ", 70 waves are provided with an auxiliary burner and a fire two burning tank, the auxiliary burner is connected to the inlet, the machine, and the input port Vacuum pumping, the output end of the fuel is connected to the exhaust unit of the main combustion unit and the main combustion unit respectively. 7. The composite material hot lifting 'integration system' as described in item 2 of the patent 5f patent, wherein the material processing unit Contains an auxiliary combustion II Wherein the auxiliary burner is provided with a groove and a combustion, the combustion of the auxiliary wheel the end connected to the vacuum pump, an output terminal connected to the combustion of the filtration tank discharge unit rose.斤2 8 such as the composite material thermal 4 solution integration system described in claim 27 of the patent scope, wherein the material processing unit further includes a temporary storage tank, 41 200836902 The input end of the temporary storage tank is connected to the vacuum pump The burner is connected to the flammable liquid through a bidirectional pipe. The input end of the flammable liquid storage tank is connected to the vacuum pump through the temporary storage tank.曰 ' 2 9 . As in the patent application scope 2 8 f cracking integrated system, wherein, (4) p = weight * combined material hot matter shell treatment early 兀 still contains a oil-water separation state 'the oil-water separation crying people * mountain The knife is separated from the input and connected to the temporary storage slot. The output is connected to the auxiliary dance machine and the filter discharge unit, and connected to the flammable liquid storage tank and the filter discharge unit through a bidirectional pipe. Column 3 Q · The composite number described in item 29 of the patent scope: deconstruction: system, wherein the substance processing unit still includes-cleaning; the output end of the 〇β washing tower is connected to the auxiliary combustion device Burning tank. 3 j. The composite material thermal cracking integration system according to claim 2, wherein the dust collection unit comprises an exhaust dust collector disposed at an opening of the furnace body adjacent to the cracking furnace . 3 2 · The composite material thermal cracking 5 system according to claim 6 wherein the dust collecting unit comprises a draft dust collector, the exhaust dust collector being disposed adjacent to the furnace body outside the cracking furnace At the groove, when the suction frame is removed, the suspended particles generated in the thermal cracking process are scattered around. u As claimed in the patent scope, item 31, the composite material thermal cracking whole person &#, ..... ^ 糸 , system, wherein the dust collecting unit comprises a cyclone dust collector, wind The input end of the wood dust person is connected to the cracking chamber exhaust pipe, and the wheel end of the cyclone dust collector is simultaneously connected to the exhaust dust collector. 3 4 · The composite material heat as described in claim 3 of the patent scope 42 200836902 cracking integrated system, wherein the dust collecting unit comprises a cooler, the input end of the cooler is connected to the cracking chamber exhaust pipe The output is connected to the = dust collector. 5 · The composite material thermal cracking integration system described in the patent specification "4, wherein the Xiao dust collection unit further comprises a filter screen, and the input end of the filter mesh is connected to the cyclone dust collector. ^ 3 6 . The composite material thermal cracking integration system according to claim 35, wherein the dust collecting unit further comprises a bag type dust collecting crying, and the input end of the bag type dust collector is connected to the filter The net has an output connected to the filter discharge unit. The composite material thermal cracking integration system of claim 2, wherein the filter discharge unit comprises a smoke _, and the input end of the smoke 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, the input end of the exhaust fan is connected to the dust collecting unit, and the output end is connected To the chimney's input to the smoker is connected to the dust collection 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 wash tower, and the input end of the clean water/chemical scrubber is connected to the set The dust unit has an output connected to the exhaust fan. The composite material thermal cracking integration system of claim 39, wherein the filtration discharge unit further comprises a water tower, the output end of which is connected to the clean water/chemical scrubber. 43 200836902 歹]. In the case of the scope of the patent, the composite material is described in item 29, where the filter discharge unit comprises a waste water/bio-processing device, the wastewater 7 biological treatment device The end is connected to the oil-water separation state. 4 2. The composite material 敎 cracking integration system according to the fourth aspect of the patent, wherein the filtration discharge unit comprises a wastewater/bioprocessing device. The input end of the I-type is connected to the clean water/chemical scrubber. 4 3 · The composite material thermal cracking integration system according to claim 4, wherein the filter discharge unit further comprises an activated carbon column, The input end of the activated carbon tower is connected to the clean water/chemical washing material, and the output end thereof is connected to the exhaust fan, and the output end of the clean water/chemical scrubbing tower is connected to the exhaust fan through the activated carbon tower. 4 4 · If the patent application scope The composite material thermal cracking integration system of item 2, wherein the energy supply unit comprises at least one generator and a power control device, the at least one generator being selected from the sun a group of generators, wind turbines, hydroelectric generators, and internal combustion generators. The input of the power control device is coupled to the at least one generator, and the output of the power control device is coupled to the composite material for thermal cracking The unit of the composite material thermal cracking integrated system as described in claim 2, wherein the energy supply unit comprises at least a generator and a power control device, the at least one The motor is selected from the group consisting of a solar generator, a wind power generator, a hydroelectric generator, and an internal combustion generator 44 200836902, and an input end of the power control device is connected to the at least one generator, and the output of the power control device The end is connected to each unit of the composite material thermal cracking integration system; in addition, the energy supply unit further comprises a hydrogen-oxygen generator and a mixer, the input end of the hydrogen-oxygen generator is connected to a water tower, the input of the mixer The end is connected to the oxyhydrogen generator, and the output end thereof is connected to the fuel input pipe. 46. The composite material heat and cracking integrated system, wherein the energy supply unit comprises at least one power generation, a machine, and a power control device selected from the group consisting of a solar generator, a wind power generator, and a hydroelectric generator And a group of internal combustion generators, wherein an input end of the power control device is connected to the at least one generator, and an output end of the power control device is connected to each unit of the composite material thermal cracking integration system; The supply unit further comprises a hydrogen-oxygen generator and a mixer, the input end of the hydrogen-oxygen generator being connected to a water tower. The input end of the mixer is connected to the hydrogen-oxygen generator, and the output end is connected to the auxiliary burner. 4 7 · The composite material thermal cracking integration system as described in claim 4, wherein the energy supply unit comprises at least one generator and a power control device, the at least one generator is selected from the group consisting of solar energy a group of motors, wind turbines, hydroelectric generators, and internal combustion generators, the wheel of the power control device The input end is connected to the at least one generator, and the output end of the power control device is connected to each unit of the composite material thermal cracking integration system; furthermore, the energy supply unit further comprises a gas full-wheel generator, the gas turbine generator The input is connected to the gas chamber exhaust, 45 200836902 The output is connected to the power control unit. 4 8 · If the patent application scope is the 24th cracking integration season, the 're-amp; mass-type material hot-coating solution, first, wherein the energy supply unit includes at least a machine and a power control device, At least one generator is selected from the group consisting of a generator, a wind generator, a hydraulic unit, a hydraulic unit, a unit, and an internal combustion generator. The input end of the power control unit is connected to the at least one power generation unit: The output of the power control device is connected to the composite material thermal cracking: each unit of the 5th system; in addition, the energy supply unit further includes a gas turbine generator, and the input end of the gas turbine generator is connected to the combustion of the auxiliary combustion device The slot has an output connected to the power control unit. Acoustic solution ^ Li Wei, please refer to the composite material thermal motor described in Patent No. 44; wherein 'the energy supply unit still includes a gas turbine generator, and the input end of the gas turbine generator is connected to the cracking chamber exhaust pipe, The basin output is connected to the power control unit. 5 〇. A composite material thermal cracking integration system, comprising: a thermal cracking unit comprising a plurality of pyrolysis furnaces connected in parallel, the cracking furnaces being used for performing a thermal cracking process of the materials to be recovered, each of which comprises - the furnace body inside the opening, an outer furnace body coated on the outer side wall of the inner furnace, and the furnace cover is arranged at the opening of the inner furnace body, wherein the inner furnace body is a cracking chamber for the capacity to be recovered 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 is provided with a heat insulating layer on the side wall of the outer furnace body; Connected to each cracking furnace separately, and the gaseous products generated in the thermal cracking process are carried out according to their flammability or not. The dust collecting unit is connected to each cracking furnace for filtering heat. a suspended particle generated in the cracking process; a filter discharge unit connected to at least one of the three units of the thermal cracking unit, the material processing unit, and the dust collecting unit for clarifying the non-recyclable substance generated in the pyrolysis spear , And emit it; and an energy supply unit that supplies the energy needed to operate each unit. 5 1 · The composite material thermal cracking integration system according to claim 50, wherein the cracking furnaces are gas cracking furnaces, and the heating space of each gas cracking furnace is a gas chamber It is used to house high-heat gas to generate the heat energy needed to heat the inner furnace. 5 2 · The composite material thermal cracking integrated system described in claim 50, wherein the cracking furnaces are electrothermal cracking furnaces, and the heating spaces of the electric thermal cracking furnaces are provided with electric heating plates, and one is provided The cable is connected to the electric heating plate. The electric heating plate is disposed around the outer side wall of the inner furnace body for generating heat energy for heating the inner furnace body, and the electric cable is used for supplying electric energy required for heating the electric heating plate. 5. The composite material thermal cracking integration system of claim 5, wherein each of the electrothermal cracking furnaces comprises an electric heating tube that extends from the electric heating plate into the cracking chamber. The composite material thermal cracking integration system of claim 1, 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 device A first auxiliary combustion machine and a combustion chamber are provided, and the second auxiliary combustion device is in the gas chamber of the auxiliary combustion cracking furnace of the "..." and the second auxiliary combustion device. The output ends are connected to the gas cracking 1 series: Shen: The compound material heat according to the patent scope item 12 is vacuum pumped pine. The material processing unit contains - vacuum pumping, 56. If the end is connected to the cracking furnace The cracking chamber exhaust pipe. The cracking and integrating system, the complex material of the condenser according to item 5 of Liweiwei, heats the LI of the condenser, the material processing unit comprises a condenser, vacuum pumping, the straight space ==Solution chamber exhaust pipe' The output end is connected to the cracking chamber of the furnace. The exhaust pipe is connected to the cracking crack through the condenser: System: 利: The composite material heat described in item 5 of the range... , the substance handling unit contains There is a sump, the input end of the flammable liquid storage tank is connected to the fuel inlet pipe. H, the wheel "connected, 5 8 · The compound material thermal cracking integration system described in the 56th patent scope, The towel processing device comprises a temporary storage tank, a water separation H and a flammable (four) tank. The input end of the temporary storage tank is connected to the vacuum pump. The wheel end of the oil water separator is connected to the temporary storage tank. The combustible liquid storage tank is respectively connected to the temporary storage tank and the oil water separator's output end through a bidirectional pipeline and connected to the fuel inlet pipe. The composite material thermal cracking integration system of claim 57, wherein the material processing unit comprises a non-flammable liquid storage tank. The input end of the non-flammable liquid storage tank is connected to a vacuum pump. 48 200836902 6 Q. The composite material thermal cracking integration system of claim 59, wherein the material processing unit comprises an auxiliary combustion device, wherein an auxiliary combustion machine and a combustion chamber are provided, the auxiliary combustion The input end of the machine 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. ^丄^ τ 寻 刊 干 第 第 60 60 60 60 60 60 60 60 60 60 60 60 60 60 60 60 60 60 60 60 60 60 60 60 60 60 60 60 60 60 60 60 60 60 60 60 60 60 60 60 60 60 60 60 60 60 60 60 60 60 60 60 60 60 60 60 60 60 60 60 60 60 60 60 60 60 60 60 60 60 60 60 60 60 60 60 60 60 60 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 pump through the temporary storage tank. 6 2. The composite material thermal cracking mentioned in the scope of patent patent item 61: integrated system 'where' the material processing unit still contains a water separation benefit, the input end of the oil water separator is connected to the temporary storage tank The transmission line connects the main burner, the auxiliary burner and the filter discharge unit, and is connected to the combustible liquid storage tank and the (4) discharge unit through the two-way official road. The solution of the composite material described in Item 62 of the patent scope is the 敎, 充电, its towel, and the material processing unit still contains the cleaning; the output of the tower m liquid tower is connected to the auxiliary teacher respectively. The tank and the gas chamber of the gas cracking furnace. “Combustion of clothing” 6 4 • As in the patent application, item 63 of the cracking integration system, where the true material = material heat input tube. 甩 < 翻出鳊 still connected to fuel 49