Pyrolysis, gasification, dust removal, quality improvement and purification integrated process for carbon-containing energy
By combining pyrolysis gasification and catalytic reaction mechanisms, using gas-solid separators and dolomite catalysts, the problems of low energy utilization efficiency and difficult catalyst development in solid waste pyrolysis gasification are solved, efficient energy utilization and gas purification are achieved, and production costs and environmental hazards are reduced.
Patent Information
- Application Number
- CN202510086450.5
- Authority / Receiving Office
- CN · China
- Patent Type
- Applications(China)
- Current Assignee / Owner
- Filing Date
- 2025-01-20
- Publication Date
- 2025-04-11
AI Technical Summary
In the existing solid waste pyrolysis gasification technology, energy utilization efficiency is low, the quality of the generated combustible gases is low, and the catalyst development is difficult, environmental hazards after inactivation, and frequent replacements increase production costs.
A integrated process of carbon-containing energy pyrolysis gasification dust removal and quality purification is adopted. By combining the pyrolysis gasification mechanism and a catalytic reaction mechanism, high-temperature carbon particles are separated by a gas-solid separator, and re-introduced into the carbonization heating furnace as a heating source, and flue gas filtration is used in the catalytic filter box.
It improves energy utilization efficiency, reduces fuel loss, improves gas quality, reduces catalyst replacement frequency and environmental hazards, and reduces production costs.
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Figure CN119799371A_ABST
Abstract
Description
Technical Field
[0001] The invention relates to the technical field of pyrolysis and gasification, and specifically to an integrated process for pyrolysis and gasification of carbon-containing energy, dust removal, quality improvement and purification. Background Art
[0002] With the advancement of urbanization and the continuous improvement of the level of social development, based on the prevention and control principles of "reduction, resource utilization and harmlessness", the existing large-scale solid waste treatment methods mainly include landfill, composting and incineration. The solid waste composition is complex and contains many harmful substances. Long-term extensive storage and low-value utilization occupy a large amount of land.
[0003] However, the main problems of the existing direct incineration-based thermal disposal technology are low energy efficiency and difficulty in controlling the emission of key pollutants such as dioxins. Dust removal and purification and gas quality improvement are the key to clean and efficient use of raw gas and increase of product added value in the organic solid waste pyrolysis and gasification graded conversion process. In the past, solid heat carriers were used as heat sources to pyrolyze and gasify organic solid waste. Cyclone separators were used for dust removal, but experiments found that the separators could only separate carbon particles from oil and gas, while the remaining oil and gas still contained tar, which was easy to adhere to the inner wall of the pipeline during subsequent transportation;
[0004] At the same time, due to the heavy tar of rapid pyrolysis and the presence of pollutants and dust such as sulfur, nitrogen, and chlorine in the gasification gas of organic solid waste, the development of cheap, highly active, long-life, and renewable catalysts is extremely difficult, and existing catalysts cannot be used in industrial processes. On the other hand, the disposal of deactivated catalysts will cause the water-soluble transition metal ions contained in them to harm the environment. At the same time, the frequent replacement of catalysts in industrial applications also increases production costs and operational difficulties.
[0005] Therefore, an integrated process of pyrolysis, gasification, dust removal, quality improvement and purification of carbon-containing energy is designed to improve energy utilization efficiency and quality to solve such defects. Summary of the invention
[0006] In view of the shortcomings of the prior art, the present invention provides an integrated process for pyrolysis and gasification of carbon-containing energy, dust removal, quality improvement and purification, which solves the problems of low energy utilization efficiency and low quality of generated combustible gas during pyrolysis and gasification of existing solid waste.
[0007] To achieve the above objectives, the present invention is implemented through the following technical solutions: an integrated process for pyrolysis, gasification, dust removal, quality improvement and purification of carbon-containing energy, specifically comprising the following steps:
[0008] S1. Garbage feeding: Put the garbage into the feeding box in the pyrolysis gasification mechanism, and then turn the material transfer plate to pour the garbage into the pyrolysis gasification furnace;
[0009] S2. Heating in the furnace: using an igniter to heat the interior of the carbonization heating furnace;
[0010] S3, gasification decomposition: using the burning high-temperature flue gas to decompose the garbage inside the pyrolysis gasification furnace;
[0011] S4, flue gas filtration: filter the flue gas using the catalyst in the catalytic reaction mechanism;
[0012] S5. Lifting and replacing materials: Start the cylinder to pour the garbage inside the pyrolysis gasification furnace into the carbonization heating furnace, and replace the catalyst inside the catalyst box at the same time.
[0013] Preferably, the pyrolysis and gasification mechanism includes a slag dropping base, the top of the slag dropping base is fixedly connected to the carbonization heating furnace, the top of the carbonization heating furnace is fixedly connected to a dropping ring tube by opening an opening, the top of the dropping ring tube is fixedly connected to the pyrolysis and gasification furnace, the bottom of the inner cavity of the carbonization heating furnace is provided with a slag leakage net groove that penetrates into the interior of the slag dropping base, the bottom of the slag dropping base is fixedly connected to a motor through a bracket, the output shaft of the motor is fixedly connected to an inner groove rotating rod through a coupling, and the top end of the inner groove rotating rod sequentially penetrates the slag dropping base and the carbonization heating furnace and extends to the inner side of the pyrolysis and gasification furnace, and the surface of the inner groove rotating rod and the inner side of the slag dropping base are fixedly connected with an arc push plate.
[0014] Preferably, a polygonal vertical rod is slidably installed on the upper part of the inner side of the inner groove rotating rod, and the surface of the polygonal vertical rod is rotatably connected to a conical mesh frame used in conjunction with the blanking ring cylinder through a bearing, and the surface of the polygonal vertical rod is fixedly connected to a stirring rack used in conjunction with the conical mesh frame, and the surface of the carbonization heating furnace is fixedly installed with an igniter by opening an opening.
[0015] Preferably, a feed box is fixedly connected to the left side of the pyrolysis gasification furnace by opening a feed box, a material holding turn plate is rotatably connected between the front and rear parts of the inner cavity of the feed box by a rotating part, an isolation baffle used in conjunction with the material holding turn plate is rotatably connected to the upper part of the inner cavity of the feed box by a rotating part, and side shift openings are provided on the surface and rear part of the feed box and on the inner side of the pyrolysis gasification furnace.
[0016] Preferably, the surface and rear portion of the feed box and the outside of the pyrolysis gasification furnace are fixedly connected to a heat exchange frame through an opening, the top of the heat exchange frame is fixedly connected to a heat exchange conduit through an opening, and a plurality of heat exchange conduits are provided, the bottom end of the heat exchange conduit passes through the heat exchange frame and extends to the lower portion of the heat exchange frame, a gas-solid separator is fixedly installed on the top of the pyrolysis gasification furnace through an opening, a U-shaped air frame is installed on the left side of the gas-solid separator, and the top end of the heat exchange conduit is connected to the U-shaped air frame, the bottom end of the heat exchange frame is fixedly connected to a sloped return barrel, and the right end of the sloped return barrel passes through the carbonization heating furnace and extends to the inner side of the carbonization heating furnace.
[0017] Preferably, a cylinder is fixedly installed on the rear portion of the pyrolysis gasification furnace through a fixed seat, the top of the cylinder is fixedly connected to a lifting vertical rod through a fixed plate, and the bottom end of the lifting vertical rod passes through the pyrolysis gasification furnace and extends to the inner side of the pyrolysis gasification furnace, one end of the lifting vertical rod extending to the inside of the pyrolysis gasification furnace is fixedly connected to a polygonal lifting cylinder through a fixed plate, and the polygonal lifting cylinder is sleeved on the surface of the polygonal vertical rod.
[0018] Preferably, the bottom end of the lifting vertical rod is fixedly connected to a U-shaped lifting frame via a fixed plate, both ends of the U-shaped lifting frame are fixedly connected to a straight cylinder frame, a torsion spring rotating rod is rotatably connected between the two sides of the inner cavity of the straight cylinder frame via a bearing, and one side of the torsion spring rotating rod is fixedly connected to a rectangular pressure plate used in conjunction with the material holding rotating plate and the side shifting port.
[0019] Preferably, the catalytic reaction mechanism includes a catalytic filter box, which is fixedly installed on the right side of the pyrolysis gasification furnace through a fixing plate, and a catalytic box is provided on the inner side of the catalytic filter box, and the front and rear portions of the left side of the catalytic box are fixedly connected with rebound rods, and the left end of the rebound rod passes through the catalytic filter box and extends to the left side of the catalytic filter box, a spring is provided on the surface of the rebound rod and located on the outside of the catalytic filter box, and a pressure-bearing cross bar is fixedly connected to the right side of the catalytic box.
[0020] Preferably, the top of the cylinder is fixedly connected to an arc-shaped pressure frame used in conjunction with a pressure-bearing cross bar via a fixing plate, an air guide groove is provided on the lower side of the interior of the catalytic filter box, an air filter hole is provided on the top of the inner cavity of the air guide groove, and an air guide pipe is fixedly connected to the bottom of the air guide groove via an opening, an air supply pipe is installed on the right side of the gas-solid separator, and one end of the air supply pipe passes through the catalytic filter box and extends to the interior of the catalytic filter box.
[0021] Preferably, the front and rear sides of the top of the catalytic filter box are fixedly connected with a feeding elbow via an opening, the top of the feeding elbow is fixedly connected with a storage barrel, a solenoid valve is fixedly installed on the surface of the storage barrel, and a material receiving frame used in conjunction with the catalytic box is fixedly installed on the lower part of the right side of the catalytic filter box, a return material inclined pipe is fixedly installed on the bottom of the material receiving frame via an opening, and one end of the return material inclined pipe passes through the carbonization heating furnace and extends to the inner side of the carbonization heating furnace.
[0022] Beneficial Effects
[0023] The present invention provides an integrated process for pyrolysis, gasification, dust removal, quality improvement and purification of carbon-containing energy. Compared with the existing technology, it has the following beneficial effects:
[0024] (1) The integrated process of pyrolysis and gasification of carbon-containing energy for dust removal, quality improvement and purification uses a pyrolysis and gasification mechanism and a catalytic reaction mechanism in combination. The arrangement of these two mechanisms allows the oil and gas generated after the pyrolysis of garbage in the pyrolysis and gasification furnace to be separated by a gas-solid separator, thereby allowing the high-temperature carbon particles to be reintroduced into the inner side of the carbonization heating furnace. At the same time, by utilizing the upward drive of the cylinder and the linkage between the structures, the treated catalyst in the cylinder can be connected to the garbage for unloading, and the high-temperature catalyst enters the carbonization heating furnace as a heating source, thereby effectively improving the energy utilization efficiency and reducing fuel loss. At the same time, the gas filtered by the catalyst is purer and the quality is improved.
[0025] (2) The integrated process of pyrolysis and gasification of carbon-containing energy for dust removal, quality improvement and purification is provided with a conical mesh frame on the inner side of the blanking ring cylinder, and is used in combination with a straight cylinder frame and a material holding rotating plate. The arrangement of these structures can, after the pyrolysis and gasification of the garbage inside the pyrolysis and gasification furnace is completed and carbonized, use the lifting and lowering of the cylinder to drive the conical mesh frame to rise, so that the high-temperature carbonized garbage inside falls into the inner side of the carbonization heating furnace as a heating source. At the same time, after the cylinder is lowered, the rectangular pressing plate is used to press the material holding rotating plate to turn it over, and the garbage is poured into the inner side of the pyrolysis and gasification furnace for pyrolysis, thereby completing the transfer of the carbonized garbage and the dumping and loading of new garbage in turn, effectively improving the overall efficiency.
[0026] (3) The integrated process of pyrolysis, gasification, dust removal, quality improvement and purification of carbon-containing energy is achieved by installing a heat exchange frame on the surface and rear of the feed box, and installing a heat exchange duct on the inner side of the heat exchange frame, and using it in conjunction with a gas-solid separator. The arrangement of these structures can use the gas-solid separator to separate the high-temperature carbon particles in the oil and gas, and then let the heat exchange duct reintroduce them into the carbonization heating furnace as a heating source. In the process, the heat exchange frame will emit temperature to the inside of the feed box, thereby pre-heating and drying the garbage inside the feed box, thereby improving the efficiency of subsequent pyrolysis and gasification, and at the same time better utilizing energy.
[0027] (4) The integrated process of pyrolysis, gasification, dust removal, quality improvement and purification of carbon-containing energy is achieved by installing a catalytic filter box on the right side of the pyrolysis gasifier, and using it in combination with a catalytic box and a return inclined pipe. The arrangement of these structures can utilize dolomite catalyst to catalytically treat the oil and gas, thereby reducing the tar present in the oil and gas, ensuring that the inside of the pipeline will not stick during transportation, improving the quality of the fuel gas, and also avoiding the huge energy consumption of heating the oil and gas after condensation. In addition, the raw material price of dolomite catalyst is low, and it can be used directly as a heating source after the catalysis is completed, without the need for repeated and cumbersome regeneration, thereby reducing the catalytic cost and the cumbersomeness of replacing the catalyst. BRIEF DESCRIPTION OF THE DRAWINGS
[0028] Figure 1It is a schematic diagram of the process of the present invention;
[0029] Figure 2 It is a structural schematic diagram of the present invention;
[0030] Figure 3 It is a rear view of the structure of the present invention;
[0031] Figure 4 It is a schematic diagram of the pyrolysis gasification mechanism structure of the present invention;
[0032] Figure 5 It is a cross-sectional view of the slag dropping base, the carbonization heating furnace and the pyrolysis gasification furnace structure of the present invention;
[0033] Figure 6 It is a cross-sectional view of the feeding box structure of the present invention;
[0034] Figure 7 It is a schematic diagram of the structure of the cylinder, lifting vertical rod and multi-angle lifting cylinder of the present invention;
[0035] Figure 8 It is a schematic diagram of the straight tube frame, torsion spring rotating rod and rectangular pressing plate structure of the present invention;
[0036] Fig. 9 It is a schematic diagram of the inner groove rotating rod, the arc surface push plate and the multi-angle vertical rod structure of the present invention;
[0037] Fig.10 It is a schematic diagram of the catalytic reaction mechanism structure of the present invention;
[0038] Fig.11 It is a schematic diagram of the spring, pressure-bearing cross bar and arc-shaped pressure frame structure of the present invention;
[0039] Fig.12 It is a cross-sectional view of the catalytic filter box structure of the present invention.
[0040] In the figure: 1. pyrolysis and gasification mechanism; 2. catalytic reaction mechanism; 101. slag dropping base; 102. carbonization heating furnace; 103. drop ring cylinder; 104. pyrolysis and gasification furnace; 105. slag leakage net slot; 106. motor; 107. inner slot rotating rod; 108. arc push plate; 109. multi-angle vertical rod; 110. conical net frame; 111. stirring rack; 112. feeding box; 113. material rotating plate; 114. isolation baffle; 115. side shift port; 116. heat exchange frame; 117. heat exchange conduit; 118. gas-solid separator; 119. U-shaped air frame; 120. inclined return Barrel; 121, igniter; 122, cylinder; 123, lifting vertical rod; 124, multi-angle lifting cylinder; 125, U-shaped lifting frame; 126, straight cylinder frame; 127, torsion spring rotating rod; 128, rectangular pressure plate; 201, catalytic filter box; 202, catalytic box; 203, rebound rod; 204, spring; 205, pressure cross bar; 206, arc-shaped pressure frame; 207, air guide groove; 208, air filter hole; 209, air guide pipe; 210, air delivery pipe; 211, feeding elbow; 212, storage barrel; 213, solenoid valve; 214, material receiving frame; 215, return material inclined pipe. DETAILED DESCRIPTION
[0041] The following will be combined with the drawings in the embodiments of the present invention to clearly and completely describe the technical solutions in the embodiments of the present invention. Obviously, the described embodiments are only part of the embodiments of the present invention, not all of the embodiments. Based on the embodiments of the present invention, all other embodiments obtained by ordinary technicians in this field without creative work are within the scope of protection of the present invention.
[0042] See also Figure 1-12 The present invention provides a technical solution: an integrated process for pyrolysis, gasification, dust removal, quality improvement and purification of carbon-containing energy, which specifically includes the following steps:
[0043] S1. Garbage feeding: Garbage is fed into the feeding box 112 in the pyrolysis gasification mechanism 1, and then the material transfer plate 113 is turned over to pour the garbage into the pyrolysis gasification furnace 104;
[0044] S2, heating in the furnace: using the igniter 121 to first heat the interior of the carbonization heating furnace 102;
[0045] S3, gasification decomposition: using the high-temperature flue gas from combustion to decompose the garbage inside the pyrolysis gasification furnace 104;
[0046] S4, flue gas filtration: filtering the flue gas using the catalyst in the catalytic reaction mechanism 2;
[0047] S5. Lifting and replacing materials: Start the cylinder 122 to pour the garbage in the pyrolysis gasification furnace 104 into the carbonization heating furnace 102, and replace the catalyst in the catalyst box 202 at the same time.
[0048] The above-mentioned integrated process of pyrolysis, gasification, dust removal, quality improvement and purification of carbon-containing energy has the following more specific steps:
[0049] S1. Garbage feeding: First, organic solid garbage is put into the inner side of the feeding box 112, so that the garbage is piled on the top of the material holding rotating plate 113, and then the cylinder 122 uses the lifting vertical rod 123 to pull the U-shaped lifting frame 125 and the polygonal lifting cylinder 124 to rise together. After the polygonal lifting cylinder 124 rises, it will pull the polygonal vertical rod 109 to the inner side of the inner groove rotating rod 107, and drive the conical net frame 110 to rise and separate from the blanking ring cylinder 103. The frame 110 continues to rise. At this time, the rectangular pressing plate 128 enters the inner side of the side shift opening 115 and is squeezed by the material holding rotating plate 113. The rectangular pressing plate 128 flips downward and does not produce a hard pressure with the material holding rotating plate 113. When the conical screen frame 110 rises to the top, the rectangular pressing plate 128 moves to the upper part of the inner side of the side shift opening 115, and then rotates the rectangular pressing plate 128 under the torsion of the torsion spring rotating rod 127 to make it become a horizontal state, and then the cylinder 122 starts to bring The polygonal lifting cylinder 124 and the U-shaped lifting frame 125 slide down, and when the polygonal lifting cylinder 124 descends, the conical screen frame 110 will be lowered first. After the conical screen frame 110 is completely lowered to the inside of the blanking ring cylinder 103, the rectangular pressing plate 128 contacts the top of the material holding rotating plate 113. As the cylinder 122 continues to descend, the lifting vertical rod 123 will be used to press the straight cylinder frame 126 to descend. At this time, the rectangular pressing plate 128 presses the material holding rotating plate 113 to flip downward. Tilt, at this time, the garbage on the top of the material holding rotating plate 113 slides to the inner side of the pyrolysis gasification furnace 104 and is located on the top of the conical net frame 110, and the rectangular pressing plate 128 continues to descend and separates from the top of the material holding rotating plate 113. At this time, the material holding rotating plate 113 is flipped and reset by its own weight, and the isolation baffle 114 is reset to close the feeding box 112, and then a batch of garbage is put from the top of the feeding box 112 to the top of the material holding rotating plate 113, and then go to step S2;
[0050] S2, heating in the furnace: after the garbage enters the pyrolysis gasification furnace 104, the igniter 121 is started to ignite and heat the interior of the carbonization heating furnace 102 with external fuel. After the temperature inside the carbonization heating furnace 102 rises, the heat will pass through the conical mesh frame 110 to pyrolyze and gasify the garbage inside the pyrolysis gasification furnace 104;
[0051] S3, gasification and decomposition: during the heating process, the garbage will produce derivative carbon. At this time, during the rising process of the air flow, the unreacted garbage, derivative carbon and volatiles will react with the hydrogen-rich atmosphere and water vapor in the middle and upper part of the pyrolysis gasification furnace 104 to undergo volatile reforming reaction to generate pyrolysis oil and gas. Then the gas-solid separator 118 draws in the oil and gas at the top and performs gas-solid separation. The separated high-temperature derivative carbon particles flow into the inner side of the heat exchange conduit 117 through the U-shaped air frame 119 and then pass through the heat exchange frame 116. At this time, the garbage inside the feeding box 112 will be heated and dried in advance by the temperature emitted by the heat exchange frame 116, until the high-temperature carbon particles enter the interior of the carbonization heating furnace 102 through the inclined return cylinder 120 as a heating source, and then the separated oil and gas enter the inner side of the catalytic filter box 201 through the gas pipe 210, and then go to step S4;
[0052] S4, flue gas filtration: After the oil gas enters the catalytic filter box 201, it passes through the dolomite catalyst in the catalytic box 202 to react, and the oil gas after the reaction and filtration becomes a sensible combustible gas, and then the combustible gas passes through the filter hole 208 and is led out through the air guide pipe 209 for separate use. After the pyrolysis and gasification of the garbage in the pyrolysis gasification furnace 104 is completed and highly carbonized, it goes to step S5;
[0053] S5, lifting and refueling: after the pyrolysis is completed, the cylinder 122 is started again to drive the conical net frame 110 to rise. After the conical net frame 110 rises to the top, the high-temperature carbonized garbage inside the pyrolysis gasification furnace 104 falls into the interior of the carbonization heating furnace 102 as a heating source. At this time, the igniter 121 is closed. During the rising process of the cylinder 122 at this time, the cylinder 122 will drive the arc pressure frame 206 to rise synchronously, so that the arc pressure frame 206 squeezes the pressure cross bar 205 to pull the catalyst box 202 out of the catalytic filter box 201. After the catalyst box 202 is moved out, the non-regenerated dolomite catalyst inside falls to the inner side of the receiving frame 214, and then the high-temperature heated catalyst enters the carbonization heating furnace 102 through the return material inclined pipe 215 as a heating source. After the cylinder 122 is lowered, the arc pressure frame 206 no longer squeezes the pressure cross bar 205, so that the catalyst box 202 is moved out of the spring 204 retracts to the inside of the catalytic filter box 201 under the elastic force of the arc pressure frame 206, and the top of the catalyst box 202 is pressed against and locked, and then the solenoid valve 213 is started to quantitatively add the dolomite catalyst in the storage barrel 212 into the inner side of the catalyst box 202 as a new catalyst material, and at the same time, the preheated garbage at the bottom of the material rotating plate 113 also falls to the top of the conical mesh frame 110 again. At this time, the carbon particles, carbonized garbage and high-temperature non-regenerative catalyst in the carbonization heating furnace 102 are used as heat sources to pyrolyze and gasify the garbage. At the same time, the carbon slag after combustion in the carbonization heating furnace 102 falls to the inside of the slag dropping base 101 through the slag leakage mesh groove 105. When the motor 106 drives the stirring rack 111 to rotate using the inner groove rotating rod 107, the arc push plate 108 pushes the carbon slag outward and discharges it from the slag dropping base 101, and at the same time, the stirring rack 111 turns the garbage to make it evenly heated.
[0054] The above-mentioned integrated process of pyrolysis, gasification, dust removal, quality improvement and purification of carbon-containing energy is implemented through the following structure:
[0055] Please refer to Figure 4 , Figure 5 , Figure 6 , Figure 7 , Figure 8 and Fig. 9, showing the overall structure of the pyrolysis and gasification mechanism 1, the pyrolysis and gasification mechanism 1 includes a slag dropping base 101, the top of the slag dropping base 101 is fixedly connected to a carbonization heating furnace 102, the top of the carbonization heating furnace 102 is fixedly connected to a blanking ring tube 103 through an opening, the top of the blanking ring tube 103 is fixedly connected to a pyrolysis and gasification furnace 104, the bottom of the inner cavity of the carbonization heating furnace 102 is provided with a slag leakage net groove 105 that penetrates into the interior of the slag dropping base 101, the bottom of the slag dropping base 101 is fixedly connected to a motor 106 through a bracket, the motor 106 is a servo motor, the output shaft of the motor 106 is fixedly connected to an inner groove rotating rod 107 through a coupling, and the top of the inner groove rotating rod 107 sequentially penetrates the slag dropping base 101 and the carbonization heating furnace 102 and extends to the hot On the inner side of the pyrolysis gasification furnace 104, the surface of the inner groove rotating rod 107 and the inner side of the slag dropping base 101 are fixedly connected with an arc push plate 108, and the upper part of the inner side of the inner groove rotating rod 107 is slidably installed with a polygonal vertical rod 109, and the surface of the polygonal vertical rod 109 is rotatably connected with a conical net frame 110 used in conjunction with the blanking ring tube 103 through a bearing, and the inner wall of the blanking ring tube 103 is provided with an annular convex strip for receiving the conical net frame 110, and the surface of the polygonal vertical rod 109 is fixedly connected with a stirring rack 111 used in conjunction with the conical net frame 110, and the surface of the carbonization heating furnace 102 is fixedly installed with an igniter 121 through an opening, and the fuel of the igniter 121 is gas, and the left side of the pyrolysis gasification furnace 104 is fixedly connected with a feeding box 112 through an opening. A material holding rotating plate 113 is rotatably connected between the front and rear parts of the inner cavity of the feeding box 112 through a rotating member, and an isolation baffle 114 used in conjunction with the material holding rotating plate 113 is rotatably connected to the upper part of the inner cavity of the feeding box 112 through a rotating member. The isolation baffle 114 can be turned vertically by its own gravity after the material holding rotating plate 113 is reset. A side shift opening 115 is provided on the surface and rear part of the feeding box 112 and on the inner side of the pyrolysis gasification furnace 104. A heat exchange frame 116 is fixedly connected to the surface and rear part of the feeding box 112 and on the outside of the pyrolysis gasification furnace 104 through an opening. A heat exchange conduit 117 is fixedly connected to the top of the heat exchange frame 116 through an opening, and a plurality of heat exchange conduits 117 are provided, and the bottom end of the heat exchange conduit 117 passes through the heat exchange conduit 117. The heat frame 116 extends to the lower part of the heat exchange frame 116. A gas-solid separator 118 is fixedly installed on the top of the pyrolysis gasification furnace 104 through an opening. A U-shaped air frame 119 is installed on the left side of the gas-solid separator 118, and the top of the heat exchange pipe 117 is connected to the U-shaped air frame 119. The bottom end of the heat exchange frame 116 is fixedly connected to an inclined return barrel 120, and the right end of the inclined return barrel 120 penetrates the carbonization heating furnace 102 and extends to the inner side of the carbonization heating furnace 102. A cylinder 122 is fixedly installed on the rear part of the pyrolysis gasification furnace 104 through a fixed seat, and the top of the cylinder 122 is fixedly connected to a lifting vertical rod 123 through a fixed plate, and the bottom end of the lifting vertical rod 123 penetrates the pyrolysis gasification furnace 104 and extends to the inner side of the pyrolysis gasification furnace 104.One end of the lifting vertical rod 123 extending to the inside of the pyrolysis gasification furnace 104 is fixedly connected to a polygonal lifting cylinder 124 through a fixed plate, and the polygonal lifting cylinder 124 is sleeved on the surface of the polygonal vertical rod 109. The bottom end of the lifting vertical rod 123 is fixedly connected to a U-shaped lifting frame 125 through a fixed plate. Both ends of the U-shaped lifting frame 125 are fixedly connected to a straight cylinder frame 126. A torsion spring rotating rod 127 is rotatably connected between the two sides of the inner cavity of the straight cylinder frame 126 through a bearing. A rectangular pressing plate 128 used in conjunction with the material rotating plate 113 and the side shifting port 115 is fixedly connected to one side of the torsion spring rotating rod 127.
[0056] Please refer to Fig.10 , Fig.11 and Fig.12 , showing the overall structure of the catalytic reaction mechanism 2, the catalytic reaction mechanism 2 includes a catalytic filter box 201, the catalytic filter box 201 is fixedly installed on the right side of the pyrolysis gasification furnace 104 through a fixing plate, a catalytic box 202 is arranged inside the catalytic filter box 201, a dolomite catalyst is placed inside the catalytic box 202, the front and rear of the left side of the catalytic box 202 are fixedly connected with a rebound rod 203, and the left end of the rebound rod 203 penetrates the catalytic filter box 201 and extends to the catalytic filter box 201. On the left side of the filter box 201, a spring 204 is sleeved on the surface of the rebound rod 203 and located outside the catalytic filter box 201. A pressure cross bar 205 is fixedly connected to the right side of the catalytic box 202. The top of the cylinder 122 is fixedly connected to an arc-shaped pressure frame 206 used in conjunction with the pressure cross bar 205 through a fixed plate. An air guide groove 207 is opened on the lower side of the interior of the catalytic filter box 201. A filter hole 208 is opened on the top of the inner cavity of the air guide groove 207. The filter hole 208 can block dolomite. The catalyst falls, and the bottom of the air guide groove 207 is fixedly connected with an air guide pipe 209 through an opening, and an air delivery pipe 210 is installed on the right side of the gas-solid separator 118, and one end of the air delivery pipe 210 passes through the catalytic filter box 201 and extends to the inside of the catalytic filter box 201. The front and rear sides of the top of the catalytic filter box 201 are fixedly connected with a feed elbow 211 through an opening, and the top of the feed elbow 211 is fixedly connected with a storage barrel 212, and the inside of the storage barrel 212 is pre- Dolomite catalyst particles are put in, and a solenoid valve 213 is fixedly installed on the surface of the storage barrel 212. The solenoid valve 213 is pre-set and can feed quantitatively each time it is started. A material receiving frame 214 used in conjunction with the catalyst box 202 is fixedly installed on the lower part of the right side of the catalytic filter box 201, and a return material inclined pipe 215 is fixedly installed on the bottom of the material receiving frame 214 through an opening, and one end of the return material inclined pipe 215 passes through the carbonization heating furnace 102 and extends to the inner side of the carbonization heating furnace 102.
[0057] Meanwhile, the contents not described in detail in this specification belong to the prior art known to those skilled in the art.
Claims
1. An integrated process for pyrolysis, gasification, dust removal, quality improvement and purification of carbon-containing energy, characterized by: The specific steps include: S1. Garbage feeding: Garbage is fed into the inner side of the feeding box (112) in the pyrolysis gasification mechanism (1), and then the material holding rotating plate (113) is turned over to pour the garbage into the interior of the pyrolysis gasification furnace (104); S2, heating in the furnace: using the igniter (121) to first heat the interior of the carbonization heating furnace (102); S3, gasification decomposition: using the high-temperature flue gas from combustion to decompose the garbage inside the pyrolysis gasification furnace (104); S4, flue gas filtration: filtering the flue gas using the catalyst in the catalytic reaction mechanism (2); S5. Lifting and replacing materials: Start the cylinder (122) to pour the garbage inside the pyrolysis gasification furnace (104) into the carbonization heating furnace (102), and replace the catalyst inside the catalyst box (202) at the same time.
2. According to claim 1, a carbon-containing energy pyrolysis gasification dust removal and purification integrated process is characterized by: The pyrolysis gasification mechanism (1) comprises a slag dropping base (101), the top of the slag dropping base (101) is fixedly connected to a carbonization heating furnace (102), the top of the carbonization heating furnace (102) is fixedly connected to a material dropping ring cylinder (103) via an opening, the top of the material dropping ring cylinder (103) is fixedly connected to a pyrolysis gasification furnace (104), and the bottom of the inner cavity of the carbonization heating furnace (102) is provided with a slag leakage net groove (105) penetrating to the interior of the slag dropping base (101). The bottom of the slag dropping base (101) is fixedly connected to a motor (106) via a bracket, the output shaft of the motor (106) is fixedly connected to an inner groove rotating rod (107) via a coupling, and the top end of the inner groove rotating rod (107) sequentially penetrates the slag dropping base (101) and the carbonization heating furnace (102) and extends to the inner side of the pyrolysis gasification furnace (104), and a curved push plate (108) is fixedly connected to the surface of the inner groove rotating rod (107) and located on the inner side of the slag dropping base (101).
3. The integrated process for pyrolysis, gasification, dust removal, quality improvement and purification of carbon-containing energy according to claim 2, characterized in that: A polygonal vertical rod (109) is slidably mounted on the upper inner side of the inner groove rotating rod (107); a conical mesh frame (110) used in conjunction with the blanking ring tube (103) is rotatably connected to the surface of the polygonal vertical rod (109) via a bearing; a stirring rack (111) used in conjunction with the conical mesh frame (110) is fixedly connected to the surface of the polygonal vertical rod (109); an igniter (121) is fixedly mounted on the surface of the carbonization heating furnace (102) via an opening.
4. The integrated process for pyrolysis, gasification, dust removal, quality improvement and purification of carbon-containing energy according to claim 3 is characterized by: A feeding box (112) is fixedly connected to the left side of the pyrolysis gasification furnace (104) by opening a feed box, a material holding rotating plate (113) is rotatably connected between the front and rear parts of the inner cavity of the feeding box (112) by a rotating member, an isolation baffle (114) used in conjunction with the material holding rotating plate (113) is rotatably connected to the upper part of the inner cavity of the feeding box (112) by a rotating member, and a side shift opening (115) is provided on the surface and rear part of the feeding box (112) and located on the inner side of the pyrolysis gasification furnace (104).
5. The integrated process for pyrolysis, gasification, dust removal, quality improvement and purification of carbon-containing energy according to claim 4, characterized in that: The surface and rear of the feeding box (112) and the outside of the pyrolysis gasification furnace (104) are fixedly connected to a heat exchange frame (116) through an opening, and the top of the heat exchange frame (116) is fixedly connected to a heat exchange conduit (117) through an opening, and a plurality of heat exchange conduits (117) are provided, and the bottom end of the heat exchange conduit (117) passes through the heat exchange frame (116) and extends to the lower part of the heat exchange frame (116). The pyrolysis gasification furnace (104) 04) is fixedly installed with a gas-solid separator (118) on the top by opening an opening, a U-shaped air frame (119) is installed on the left side of the gas-solid separator (118), and the top end of the heat exchange pipe (117) is connected to the U-shaped air frame (119), and the bottom end of the heat exchange frame (116) is fixedly connected with a sloped return barrel (120), and the right end of the sloped return barrel (120) passes through the carbonization heating furnace (102) and extends to the inner side of the carbonization heating furnace (102).
6. The integrated process for pyrolysis, gasification, dust removal, quality improvement and purification of carbon-containing energy according to claim 5, characterized in that: A cylinder (122) is fixedly mounted on the rear of the pyrolysis gasification furnace (104) via a fixed seat, and a top end of the cylinder (122) is fixedly connected to a lifting vertical rod (123) via a fixed plate, and a bottom end of the lifting vertical rod (123) passes through the pyrolysis gasification furnace (104) and extends to the inner side of the pyrolysis gasification furnace (104), and one end of the lifting vertical rod (123) extending to the inside of the pyrolysis gasification furnace (104) is fixedly connected to a polygonal lifting cylinder (124) via a fixed plate, and the polygonal lifting cylinder (124) is sleeved on the surface of the polygonal vertical rod (109).
7. The integrated process for pyrolysis, gasification, dust removal, upgrading and purification of carbon-containing energy according to claim 6, characterized in that: The bottom end of the lifting vertical rod (123) is fixedly connected to a U-shaped lifting frame (125) via a fixing plate, and both ends of the U-shaped lifting frame (125) are fixedly connected to a straight cylinder frame (126). A torsion spring rotating rod (127) is rotatably connected between the two sides of the inner cavity of the straight cylinder frame (126) via a bearing member, and one side of the torsion spring rotating rod (127) is fixedly connected to a rectangular pressing plate (128) used in conjunction with the material holding rotating plate (113) and the side shifting port (115).
8. The integrated process for pyrolysis, gasification, dust removal, upgrading and purification of carbon-containing energy according to claim 1, characterized in that: The catalytic reaction mechanism (2) comprises a catalytic filter box (201), the catalytic filter box (201) is fixedly installed on the right side of the pyrolysis gasification furnace (104) through a fixing plate, a catalytic box (202) is arranged on the inner side of the catalytic filter box (201), the front and rear parts of the left side of the catalytic box (202) are fixedly connected with a rebound rod (203), and the left end of the rebound rod (203) passes through the catalytic filter box (201) and extends to the left side of the catalytic filter box (201), a spring (204) is sleeved on the surface of the rebound rod (203) and located outside the catalytic filter box (201), and a pressure-bearing cross bar (205) is fixedly connected to the right side of the catalytic box (202).
9. The integrated process for pyrolysis, gasification, dust removal, quality improvement and purification of carbon-containing energy according to claim 8, characterized in that: The top of the cylinder (122) is fixedly connected to an arc-shaped pressure frame (206) used in conjunction with a pressure-bearing cross bar (205) via a fixing plate; an air guide groove (207) is provided on the lower side of the interior of the catalytic filter box (201); an air filter hole (208) is provided on the top of the inner cavity of the air guide groove (207); an air guide pipe (209) is fixedly connected to the bottom of the air guide groove (207) via an opening; an air supply pipe (210) is installed on the right side of the gas-solid separator (118), and one end of the air supply pipe (210) passes through the catalytic filter box (201) and extends to the interior of the catalytic filter box (201).
10. The integrated process for pyrolysis, gasification, dust removal, quality improvement and purification of carbon-containing energy according to claim 9, characterized in that: The front side and the rear side of the top of the catalytic filter box (201) are fixedly connected to a feed elbow (211) through openings, the top of the feed elbow (211) is fixedly connected to a material storage barrel (212), and a solenoid valve (213) is fixedly installed on the surface of the material storage barrel (212). A material receiving frame (214) used in conjunction with the catalytic box (202) is fixedly installed at the lower part of the right side of the catalytic filter box (201), and a return material inclined pipe (215) is fixedly installed at the bottom of the material receiving frame (214) through an opening, and one end of the return material inclined pipe (215) passes through the carbonization heating furnace (102) and extends to the inner side of the carbonization heating furnace (102).