CN216236866U - Novel conversion of abandonment organic matter energy device - Google Patents
Novel conversion of abandonment organic matter energy device Download PDFInfo
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- CN216236866U CN216236866U CN202123162751.8U CN202123162751U CN216236866U CN 216236866 U CN216236866 U CN 216236866U CN 202123162751 U CN202123162751 U CN 202123162751U CN 216236866 U CN216236866 U CN 216236866U
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Abstract
A novel conversion device for waste organic energy relates to the technical field of carburetion equipment. The discharge end of the melting extruder is provided with a melting material plug pipe, the melting extruder is connected with a thermal cracking reaction kettle through the melting material plug pipe, a slag discharge port at the tail end of the thermal cracking reaction kettle is connected with an inlet of the thermal cracking slag discharging kettle through a flange pipeline, the thermal cracking slag discharging kettle is connected with a powder material slag tank through a pipeline flange, the powder material slag tank is connected with a water-cooling screw machine through a flange, an outlet of the water-cooling screw machine is connected with an inlet of a carbon black storage tank, the thermal cracking reaction kettle is connected with a crude oil tank through a pipeline, the thermal cracking slag discharging kettle is connected with the crude oil tank through a pipeline, and the crude oil tank is connected with a dust remover through a pipeline. The purposes of continuous feeding, continuous deslagging, effective utilization of non-condensable gas, energy conservation and emission reduction are achieved, the whole system works under micro negative pressure, harmful gas and dust are effectively controlled, and the cleanness of a production plant area is kept.
Description
Technical Field
The utility model relates to a novel waste organic matter energy conversion device, and relates to the technical field of carburetion equipment.
Background
In the production process of modern enterprises, waste organic matters are often generated, the waste organic matters can cause environmental pollution if not properly treated, and in addition, the treated waste organic matters can be converted into energy sources for reutilization.
More small-size treatment facility among the prior art adopts small-size reation kettle basically, produces one cauldron, both can't carry out high temperature feeding, more can't carry out high temperature and arrange sediment, has not had the continuous oil device of abandonment organic matter of scale to put into use yet. After some equipment is improved, the problems of continuous feeding and high-temperature slag discharging are solved, however, the feeding cannot be carried out within one hour before the slag discharging, in the one hour, the oil in the slag is completely melted, and then the feeding can be carried out again after the slag is discharged, so that the continuous feeding is not absolutely necessary, and the production efficiency is not high.
SUMMERY OF THE UTILITY MODEL
The utility model aims to solve the problems in the prior art, and provides a novel waste organic matter energy conversion device, which realizes the purposes of continuous feeding, continuous deslagging, effective utilization of non-condensable gas, energy conservation and emission reduction, and simultaneously fully utilizes the heat energy of the device to achieve the purpose of energy conservation.
In order to achieve the purpose, the utility model adopts the following technical scheme: the device comprises a belt conveyer 1, a melting extruder 2, a thermal cracking reaction kettle 5, a thermal cracking slag discharging kettle 10, a powder slag tank 15, a water-cooling screw machine 16, a carbon black storage tank 17, a crude oil tank 19, a dedusting dechlorination device 21, a desulphurizing device 22, a gas compressor 23, a dehydration tower 24, a gas storage capsule 25, a gas generator set 26 and a crude oil storage 28, wherein the belt conveyer 1 is arranged at one side of the feeding end of the melting extruder 2, the discharging end of the melting extruder 2 is provided with a melting material plug pipe 4, the melting extruder 2 is connected with the thermal cracking reaction kettle 5 through the melting material plug pipe 4, a slag discharging port at the tail end of the thermal cracking reaction kettle 5 is connected with an inlet of the thermal cracking slag discharging kettle 10 through a flange pipeline, the thermal cracking slag discharging kettle 10 is connected with the powder slag tank 15 through a pipeline flange, the powder slag tank 15 is connected with the water-cooling screw machine 16 through a flange, an outlet of the water-cooling screw machine 16 is connected with an inlet of the carbon black storage tank 17, the thermal cracking reaction kettle 5 is connected with a crude oil tank 19 through a pipeline, the thermal cracking residue discharging kettle 10 is connected with the crude oil tank 19 through a pipeline, the crude oil tank 19 is connected with a dust removal dechlorination device 21 through a pipeline, and the dust removal dechlorination device 21, a sulfur removal device 22, a gas compressor 23, a dehydration tower 24, a gas storage capsule 25 and a gas generator set 26 are sequentially connected through pipelines; the top of the thermal cracking reaction kettle 5 is provided with two oil gas outlets, the oil gas outlets are provided with high-temperature sealing valves 30, the two oil gas outlets are respectively provided with a first catalytic tower 6 and a second catalytic tower 7, the first catalytic tower 6 and the second catalytic tower 7 are connected with the high-temperature sealing valves 30 through pipelines, the top of the thermal cracking residue discharging kettle 10 is provided with two oil gas outlets, the oil gas outlets are provided with high temperature sealing valves 30, the two oil gas outlets are respectively provided with a third catalytic tower 11 and a fourth catalytic tower 12, the third catalytic tower 11 and the fourth catalytic tower 12 are connected with the high temperature sealing valves 30 through pipelines, the first catalytic tower 6, the second catalytic tower 7, the third catalytic tower 11 and the fourth catalytic tower 12 are respectively connected with a first condenser 8, a second condenser 9, a third condenser 13 and a fourth condenser 14, and all the catalytic towers are connected with the condensers through thermal expansion corrugated pipes; the crude oil tank 19 is provided with a secondary condenser 18 and a tertiary condenser 20, the top of the secondary condenser 18 is connected with the first condenser 8, the second condenser 9, the third condenser 13 and the fourth condenser 14 through pipelines, and the top of the tertiary condenser 20 is connected with the dedusting dechlorination device 21 through a pipeline.
The melting extruder 2 is provided with a feeder 3 and a first electromagnetic heater 2-1, the feeder 3 is arranged below the belt conveyor 1, the outlet of the feeder 3 is connected with the inlet of the melting extruder 2, an extruder screw is also arranged in the melting extruder 2, the extruder screw is driven by a motor through a reduction box, the power of the motor is 45kw, and the power of a power supply of the first electromagnetic heater 2-1 is 40 kw.
The thermal cracking reaction kettle 5 is provided with second electromagnetic heaters 5-1, the second electromagnetic heaters 5-1 are provided with four groups, the power of the front two groups of second electromagnetic heaters 5-1 is 100kw, and the power of the rear two groups of second electromagnetic heaters 5-1 is 80 kw.
The thermal cracking residue discharging kettle 10 is provided with a third electromagnetic heater 10-1, the third electromagnetic heaters 10-1 are provided with four groups, and the power supply of the four groups of the third electromagnetic heaters 10-1 is 80 kw.
The thermal cracking reaction kettle 5 and the thermal cracking slag discharging kettle 10 are internally provided with screw feeders, and the power of a driving motor of the screw feeders is 11 kw.
The first catalytic tower 6, the second catalytic tower 7, the third catalytic tower 11 and the fourth catalytic tower 12 are respectively provided with a first standby catalytic tower 6-1, a second standby catalytic tower 7-1, a third standby catalytic tower 11-1 and a fourth standby catalytic tower 12-1, and the structures and connection modes of the first standby catalytic tower 6-1, the second standby catalytic tower 7-1, the third standby catalytic tower 11-1 and the fourth standby catalytic tower 12-1 are the same as those of the first catalytic tower 6, the second catalytic tower 7, the third catalytic tower 11 and the fourth catalytic tower 12.
One side of the crude oil tank 19 is provided with a crude oil pump 27, a crude oil reservoir 28 and a sales oil pump 29, the crude oil tank 19 is connected with the crude oil pump 27 through a pipeline, and the crude oil pump 27, the crude oil reservoir 28 and the sales oil pump 29 are connected through a pipeline.
The 2 bores of melting extruder be 250mm, length is 2800mm, thermal cracking reation kettle 5, thermal cracking slag discharging cauldron 10 diameter be 1400mm, length is 6000mm, high temperature seal valve 30 diameter be 300mm, valve body thickness is 100 mm.
The first catalytic tower 6, the second catalytic tower 7, the third catalytic tower 11 and the fourth catalytic tower 12 are identical in structure, the diameter of each catalytic tower is 800mm, and the height of each catalytic tower is 1000 mm.
The negative pressure in the crude oil tank 19 is 100mm water column.
The belt conveyor 1 and the melting extruder 2 are respectively provided with two groups.
And a radar level gauge 15-1 is arranged on the powder slag material plug tank 15.
After the technical scheme is adopted, the utility model has the beneficial effects that: the purposes of continuous feeding, continuous deslagging, effective utilization of non-condensable gas, energy conservation and emission reduction are achieved, meanwhile, the energy conservation purpose is achieved by fully utilizing self heat energy, the whole system works under micro negative pressure, harmful gas and dust are effectively controlled, the generation of harmful gas dioxin and the leakage of dust are effectively avoided, and the cleanness of a production plant area is kept.
Drawings
In order to more clearly illustrate the embodiments of the present invention or the technical solutions in the prior art, the drawings used in the description of the embodiments or the prior art will be briefly described below, and it is obvious that the drawings in the following description are only some embodiments of the present invention, and for those skilled in the art, other drawings can be obtained according to these drawings without creative efforts.
FIG. 1 is a schematic process flow diagram of the present invention;
FIG. 2 is a schematic flow diagram of the feed to condensing stage of the present invention;
FIG. 3 is a schematic diagram of a three stage condensation to storage sales process of the present invention.
Description of reference numerals: a belt conveyor 1, a melting extruder 2, a feeder 3, a melting material plug pipe 4, a thermal cracking reaction kettle 5, a first catalytic tower 6, a second catalytic tower 7, a first condenser 8, a second condenser 9, a thermal cracking slag discharging kettle 10, a third catalytic tower 11, a fourth catalytic tower 12, a third condenser 13, a fourth condenser 14, a powder slag tank 15, a water-cooling screw machine 16, a carbon black storage tank 17, a second-stage condenser 18, a crude oil tank 19, a third-stage condenser 20, a dedusting dechlorination device 21, a sulfur remover 22, a gas compressor 23, a dehydration tower 24, a gas storage capsule 25, a gas generator set 26, a crude oil storage 28, a sales oil pump 29, a high-temperature sealing valve 30, a first electromagnetic heater 2-1, a second electromagnetic heater 5-1, a third electromagnetic heater 10-1, a first standby catalytic tower 6-1, a second standby catalytic tower 7-1, a third standby catalytic tower 11-1, a first standby catalytic tower 2-1, a second electromagnetic heater 5-1, a second electromagnetic heater, a third electromagnetic heater 9, a third standby catalytic tower 11-1, a third catalytic tower, a second catalytic tower, a third catalytic tower 14-2-1, a third catalytic tower, a third condenser, a, The fourth spare catalytic tower 12-1.
Detailed Description
Referring to fig. 1 to fig. 3, the technical solution adopted by the present embodiment is: the device comprises a belt conveyer 1, a melting extruder 2, a thermal cracking reaction kettle 5, a thermal cracking slag discharging kettle 10, a powder slag tank 15, a water-cooling screw machine 16, a carbon black storage tank 17, a crude oil tank 19, a dedusting dechlorination device 21, a desulphurizing device 22, a gas compressor 23, a dehydration tower 24, a gas storage capsule 25, a gas generator set 26 and a crude oil storage 28, wherein the belt conveyer 1 is arranged at one side of the feeding end of the melting extruder 2, the discharging end of the melting extruder 2 is provided with a melting material plug pipe 4, the melting extruder 2 is connected with the thermal cracking reaction kettle 5 through the melting material plug pipe 4, a slag discharging port at the tail end of the thermal cracking reaction kettle 5 is connected with an inlet of the thermal cracking slag discharging kettle 10 through a flange pipeline, the thermal cracking slag discharging kettle 10 is connected with the powder slag tank 15 through a pipeline flange, the powder slag tank 15 is connected with the water-cooling screw machine 16 through a flange, an outlet of the water-cooling screw machine 16 is connected with an inlet of the carbon black storage tank 17, the thermal cracking reaction kettle 5 is connected with a crude oil tank 19 through a pipeline, the thermal cracking residue discharging kettle 10 is connected with the crude oil tank 19 through a pipeline, the crude oil tank 19 is connected with a dust removal dechlorination device 21 through a pipeline, and the dust removal dechlorination device 21, a sulfur removal device 22, a gas compressor 23, a dehydration tower 24, a gas storage capsule 25 and a gas generator set 26 are sequentially connected through pipelines; the top of the thermal cracking reaction kettle 5 is provided with two oil gas outlets, the oil gas outlets are provided with high-temperature sealing valves 30, the two oil gas outlets are respectively provided with a first catalytic tower 6 and a second catalytic tower 7, the first catalytic tower 6 and the second catalytic tower 7 are connected with the high-temperature sealing valves 30 through pipelines, the top of the thermal cracking residue discharging kettle 10 is provided with two oil gas outlets, the oil gas outlets are provided with high temperature sealing valves 30, the two oil gas outlets are respectively provided with a third catalytic tower 11 and a fourth catalytic tower 12, the third catalytic tower 11 and the fourth catalytic tower 12 are connected with the high temperature sealing valves 30 through pipelines, the first catalytic tower 6, the second catalytic tower 7, the third catalytic tower 11 and the fourth catalytic tower 12 are respectively connected with a first condenser 8, a second condenser 9, a third condenser 13 and a fourth condenser 14, and all the catalytic towers are connected with the condensers through thermal expansion corrugated pipes; the crude oil tank 19 is provided with a secondary condenser 18 and a tertiary condenser 20, the top of the secondary condenser 18 is connected with a first condenser 8, a second condenser 9, a third condenser 13 and a fourth condenser 14 through pipelines, the top of the tertiary condenser 20 is connected with a dedusting dechlorination device 21 through pipelines, the melting extruder 2 is provided with a feeder 3 and a first electromagnetic heater 2-1, the feeder 3 is arranged below the belt conveyor 1, the outlet of the feeder 3 is connected with the inlet of the melting extruder 2, the melting extruder 2 is also internally provided with an extruder screw rod which is driven by a motor through a reduction box, the power of the motor of the extruder screw rod is 45kw, the power of the first electromagnetic heater 2-1 is 40kw, the thermal cracking reaction kettle 5 is provided with a second electromagnetic heater 5-1, and the second electromagnetic heaters 5-1 are provided with four groups, the power of the front two groups of second electromagnetic heaters 5-1 is 100kw, the power of the rear two groups of second electromagnetic heaters 5-1 is 80kw, the thermal cracking residue discharging kettle 10 is provided with a third electromagnetic heater 10-1, the third electromagnetic heaters 10-1 are provided with four groups, and the power of the fourth electromagnetic heaters 10-1 is 80 kw.
Furthermore, screw feeders are arranged in the thermal cracking reaction kettle 5 and the thermal cracking slag discharging kettle 10 to coke on the walls of the thermal cracking reaction kettle and the thermal cracking slag discharging kettle, and the power of a driving motor of the screw feeders is 11 kw.
Further, a first standby catalytic tower 6-1, a second standby catalytic tower 7-1, a third standby catalytic tower 11-1 and a fourth standby catalytic tower 12 are respectively arranged on the first catalytic tower 6, the second catalytic tower 7, the third catalytic tower 11 and the fourth catalytic tower 12, and the structures and connection modes of the first standby catalytic tower 6-1, the second standby catalytic tower 7-1, the third standby catalytic tower 11-1 and the fourth standby catalytic tower 12-1 are the same as those of the first catalytic tower 6, the second catalytic tower 7, the third catalytic tower 11 and the fourth catalytic tower 12. The standby catalytic tower can continue to work when the main catalytic tower breaks down, and the operation continuity of the equipment is ensured.
Further, a crude oil pump 27, a crude oil reservoir 28 and a sales oil pump 29 are arranged on one side of the crude oil tank 19, the crude oil tank 19 is connected with the crude oil pump 27 through a pipeline, and the crude oil pump 27, the crude oil reservoir 28 and the sales oil pump 29 are connected through a pipeline.
Further, 2 bores of melting extruder be 250mm, length is 2800mm, thermal cracking reation kettle 5, thermal cracking slag discharging cauldron 10 diameter be 1400mm, length is 6000mm, high temperature seal valve 30 diameter be 300mm, valve body thickness is 100mm, valve body and flashboard adopt accurate lock to grind.
Further, the first catalytic tower 6, the second catalytic tower 7, the third catalytic tower 11 and the fourth catalytic tower 12 have the same structure, the diameter of the catalytic tower is 800mm, and the height of the catalytic tower is 1000 mm.
Further, the negative pressure in the crude oil tank 19 is 100mm water column. The crude oil tank 19 is provided with a pressure controller, and the compressor 23 is controlled by the pressure controller, so that the crude oil tank 19 and the whole reaction system are ensured to have negative pressure of 100mm water column, micro negative pressure control is realized, harmful gas dioxin is effectively prevented from being generated and dust is effectively prevented from leaking, and the cleanness of a production plant area is kept.
Furthermore, two groups of belt conveyors 1 and two groups of melting extruders 2 are respectively arranged.
Further, a radar level gauge 15-1 is arranged on the powder slag material plug tank 15. The material plug with a certain height in the tank can be kept, and the start and stop of the water-cooling screw machine 16 are controlled by the radar level gauge 15-1 to ensure the height of the material plug.
The working principle of the utility model is as follows: the waste organic matters are conveyed into a belt conveyor 1 by a forklift, conveyed into a feeder 3 by the belt conveyor 1 and then enter a melting extruder 2 through a hopper of the feeder 3, the heating temperature of electromagnetic heaters can be set and adjusted, at the moment, the melting extruder 2 is heated to the temperature required by the melting state of the waste organic matters, two groups of melting extruders 2 drive screws through motors to push molten materials to a melting material plug pipe 4 and further to a thermal cracking reaction kettle 5, at the moment, the thermal cracking reaction kettle 5 is heated to the temperature at which the materials can be cracked by four groups of electromagnetic heaters, the materials are immediately cracked into oil gas with corresponding temperature sections after entering the thermal cracking reaction kettle 5 and enter a first catalytic tower 6 and a second catalytic tower 7 through front and rear oil gas outlets, and oil gas reforming and reforming catalysts are filled in the first catalytic tower 6 and the second catalytic tower 7, oil gas generated by thermal cracking of organic matters is changed into light oil gas after passing through catalysts of a first catalytic tower 6 and a second catalytic tower 7, the light oil gas passes through a first condenser 8 and a second condenser 9 and is further sent into a second-stage condenser 18, crude oil obtained after condensation falls into the lower part of a crude oil tank 19, non-condensable gas is positioned at the upper part of the crude oil tank 19 and is cooled by a third-stage condenser 20, the crude oil falls into the crude oil tank 19, the non-condensable gas enters a dedusting dechlorination device 21 to be dedusted and dechlorinated, and then the non-condensable gas enters a dedusting dechlorination device 21 to be dedusted and dechlorinatedEnters a desulfurizer 22 to remove H2S, pressurizing the purified combustible non-condensable gas by the compressor 23, then dehydrating the combustible non-condensable gas in the dehydration tower 24, and then pressing the combustible non-condensable gas into the gas storage capsule 25, wherein the gas storage capsule 25 with certain pressure is connected with the gas generator set 26 through a pipeline to generate power; the crude oil in the crude oil tank 19 is pumped into a crude oil storage 28 by a crude oil pump 27 for sale. After the materials in the thermal cracking reaction kettle 5 are thermally cracked, oil gas flows out from an oil gas outlet at the upper part, the materials which are not cracked enter a thermal cracking slag discharging kettle 10 from a slag outlet of the thermal cracking reaction kettle 5, the materials have higher thermal cracking temperature and are further cracked, the oil gas flows out from the oil gas outlet, enters a third catalytic tower 11 and a fourth catalytic tower 12, then enters a third condenser 13 and a fourth condenser 14, and is further sent into a second-stage condenser 18, then enters a crude oil tank 19 to be subjected to oil-gas separation as the above parts, powder slag is finally discharged from a slag discharging hole of the thermal cracking slag discharging kettle 10 to a powder slag plug tank 15, the powder slag plug tank 15 is provided with a radar level gauge 15-1 to keep a material plug with certain height in the tank, air is blocked from entering the reaction kettle, a water-cooling screw machine 16 is controlled by the radar level gauge 15-1 to start and stop, in order to guarantee the height of the material plug, the crude oil tank 19 is provided with a pressure controller, and the compressor 23 is controlled by the pressure controller, so that the crude oil tank 19 and the whole reaction system are guaranteed to have a negative pressure of 100mm water columns, micro negative pressure control is realized, harmful gas dioxin is effectively prevented from being generated, dust is effectively prevented from leaking, and the cleanness of a production plant area is kept.
The above description is only for the purpose of illustrating the technical solutions of the present invention and not for the purpose of limiting the same, and other modifications or equivalent substitutions made by those skilled in the art to the technical solutions of the present invention should be covered within the scope of the claims of the present invention without departing from the spirit and scope of the technical solutions of the present invention.
Claims (10)
1. The utility model provides a novel abandonment organic matter energy conversion device which characterized in that: the device comprises a belt conveyor (1), a melting extruder (2), a thermal cracking reaction kettle (5), a thermal cracking slag discharging kettle (10), a powder slag tank (15), a water-cooling screw machine (16), a carbon black storage tank (17), a crude oil tank (19), a dust removal dechlorination device (21), a sulfur removal device (22), a gas compressor (23), a dehydration tower (24), a gas storage capsule (25), a gas generator set (26) and a crude oil storage tank (28), wherein the belt conveyor (1) is arranged on one side of the feeding end of the melting extruder (2), the discharging end of the melting extruder (2) is provided with a melting material plug pipe (4), the melting extruder (2) is connected with the thermal cracking reaction kettle (5) through the melting material plug pipe (4), a slag discharging port at the tail end of the thermal cracking reaction kettle (5) is connected with an inlet of the thermal cracking reaction kettle (10) through a flange pipeline, the thermal cracking slag discharging kettle (10) is connected with the powder slag tank (15) through a pipeline flange, the powder slag pot (15) is connected with a water-cooling screw machine (16) through a flange, the outlet of the water-cooling screw machine (16) is connected with the inlet of a carbon black storage tank (17), a thermal cracking reaction kettle (5) is connected with a crude oil tank (19) through a pipeline, a thermal cracking slag discharging kettle (10) is connected with the crude oil tank (19) through a pipeline, the crude oil tank (19) is connected with a dust removal dechlorination device (21) through a pipeline, and the dust removal dechlorination device (21), a sulfur removal device (22), a gas compressor (23), a dehydration tower (24), a gas storage capsule (25) and a gas generator set (26) are sequentially connected through pipelines; the top of the thermal cracking reaction kettle (5) is provided with two oil gas outlets, a high-temperature sealing valve (30) is arranged on the oil gas outlets, a first catalytic tower (6) and a second catalytic tower (7) are respectively arranged on the two oil gas outlets, the first catalytic tower (6) and the second catalytic tower (7) are connected with the high-temperature sealing valve (30) through pipelines, two oil gas outlets are arranged on the top of the thermal cracking slag discharging kettle (10), the high-temperature sealing valve (30) is arranged on the oil gas outlets, a third catalytic tower (11) and a fourth catalytic tower (12) are respectively arranged on the two oil gas outlets, the third catalytic tower (11) and the fourth catalytic tower (12) are connected with the high-temperature sealing valve (30) through pipelines, and a first condenser (8) and a second condenser (7), the third catalytic tower (11) and the fourth catalytic tower (12) are respectively connected with the first catalytic tower (6), the second catalytic tower (7), the third catalytic tower (11) and the fourth catalytic tower (12), The catalytic tower comprises a second condenser (9), a third condenser (13) and a fourth condenser (14), wherein all the catalytic towers are connected with the condensers through thermal expansion corrugated pipes; and a secondary condenser (18) and a tertiary condenser (20) are arranged on the crude oil tank (19), the top of the secondary condenser (18) is connected with the first condenser (8), the second condenser (9), the third condenser (13) and the fourth condenser (14) through pipelines, and the top of the tertiary condenser (20) is connected with the dust removal dechlorination device (21) through pipelines.
2. The novel waste organic energy conversion device according to claim 1, wherein: the melting extruder (2) is provided with a feeding machine (3) and a first electromagnetic heater (2-1), the feeding machine (3) is arranged below the belt conveyor (1), an outlet of the feeding machine (3) is connected with an inlet of the melting extruder (2), an extruder screw is further arranged in the melting extruder (2), the extruder screw is driven by a motor through a reduction gearbox, the power of the motor is 45kw, and the power of a power supply of the first electromagnetic heater (2-1) is 40 kw.
3. The novel waste organic energy conversion device according to claim 1, wherein: the slag tapping device is characterized in that a second electromagnetic heater (5-1) is arranged on the thermal cracking reaction kettle (5), four groups of the second electromagnetic heaters (5-1) are arranged, the power of two groups of the second electromagnetic heaters (5-1) at the front end is 100kw, the power of two groups of the second electromagnetic heaters (5-1) at the rear end is 80kw, a third electromagnetic heater (10-1) is arranged on the thermal cracking reaction kettle (10), four groups of the third electromagnetic heaters (10-1) are arranged, the power of the three electromagnetic heaters (10-1) in the four groups is 80kw, screw feeders are arranged in the thermal cracking reaction kettle (5) and the thermal cracking slag tapping kettle (10), and the power of a screw feeder driving motor is 11 kw.
4. The novel waste organic energy conversion device according to claim 1, wherein: the device is characterized in that a first standby catalytic tower (6-1), a second standby catalytic tower (7-1), a third standby catalytic tower (11-1) and a fourth standby catalytic tower (12) are respectively arranged on the first catalytic tower (6), the second catalytic tower (7), the third catalytic tower (11-1) and the fourth catalytic tower (12-1), and the structures and connection modes of the first standby catalytic tower (6-1), the second standby catalytic tower (7-1), the third standby catalytic tower (11-1) and the fourth standby catalytic tower (12-1) are the same as those of the first catalytic tower (6), the second catalytic tower (7), the third catalytic tower (11) and the fourth catalytic tower (12).
5. The novel waste organic energy conversion device according to claim 1, wherein: a crude oil pump (27), a crude oil reservoir (28) and a sales oil pump (29) are arranged on one side of the crude oil tank (19), the crude oil tank (19) is connected with the crude oil pump (27) through a pipeline, and the crude oil pump (27), the crude oil reservoir (28) and the sales oil pump (29) are connected through a pipeline.
6. The novel waste organic energy conversion device according to claim 1, wherein: the bore of the melting extruder (2) is 250mm, the length is 2800mm, the diameter of the thermal cracking reaction kettle (5) and the thermal cracking slag discharging kettle (10) is 1400mm, the length is 6000mm, the diameter of the high-temperature sealing valve (30) is 300mm, and the thickness of the valve body is 100 mm.
7. The novel waste organic energy conversion device according to claim 1, wherein: the first catalytic tower (6), the second catalytic tower (7), the third catalytic tower (11) and the fourth catalytic tower (12) are identical in structure, the diameter of each catalytic tower is 800mm, and the height of each catalytic tower is 1000 mm.
8. The novel waste organic energy conversion device according to claim 1, wherein: the belt conveyor (1) and the melting extruder (2) are respectively provided with two groups.
9. The novel waste organic energy conversion device according to claim 1, wherein: the negative pressure in the crude oil tank (19) is 100mm water column.
10. The novel waste organic energy conversion device according to claim 1, wherein: and a radar level gauge (15-1) is arranged on the powder slag tank (15).
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| CN202123162751.8U CN216236866U (en) | 2021-12-16 | 2021-12-16 | Novel conversion of abandonment organic matter energy device |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114106866A (en) * | 2021-12-16 | 2022-03-01 | 广西海鸥能源装备有限公司 | Novel conversion of abandonment organic matter energy device |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114106866A (en) * | 2021-12-16 | 2022-03-01 | 广西海鸥能源装备有限公司 | Novel conversion of abandonment organic matter energy device |
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