CN110848698A - Solid waste treatment equipment - Google Patents
Solid waste treatment equipment Download PDFInfo
- Publication number
- CN110848698A CN110848698A CN201911014087.7A CN201911014087A CN110848698A CN 110848698 A CN110848698 A CN 110848698A CN 201911014087 A CN201911014087 A CN 201911014087A CN 110848698 A CN110848698 A CN 110848698A
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- China
- Prior art keywords
- solid waste
- pyrolysis
- waste treatment
- treatment apparatus
- cavity
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- 238000009270 solid waste treatment Methods 0.000 title claims abstract description 51
- 238000000197 pyrolysis Methods 0.000 claims abstract description 72
- 239000000463 material Substances 0.000 claims abstract description 48
- 239000002893 slag Substances 0.000 claims abstract description 12
- 238000005336 cracking Methods 0.000 claims abstract description 11
- 238000007599 discharging Methods 0.000 claims abstract description 7
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 6
- 238000004891 communication Methods 0.000 claims description 3
- 239000002910 solid waste Substances 0.000 abstract description 42
- 239000007789 gas Substances 0.000 abstract description 31
- 239000002341 toxic gas Substances 0.000 abstract description 6
- 238000004321 preservation Methods 0.000 description 14
- 210000000078 claw Anatomy 0.000 description 7
- 238000009434 installation Methods 0.000 description 4
- 239000000126 substance Substances 0.000 description 4
- 238000000034 method Methods 0.000 description 3
- KVGZZAHHUNAVKZ-UHFFFAOYSA-N 1,4-Dioxin Chemical compound O1C=COC=C1 KVGZZAHHUNAVKZ-UHFFFAOYSA-N 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- 229910052799 carbon Inorganic materials 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 239000010410 layer Substances 0.000 description 2
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 239000011241 protective layer Substances 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 1
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 229910002091 carbon monoxide Inorganic materials 0.000 description 1
- 239000003818 cinder Substances 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 201000010099 disease Diseases 0.000 description 1
- 208000037265 diseases, disorders, signs and symptoms Diseases 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 239000002737 fuel gas Substances 0.000 description 1
- 239000000295 fuel oil Substances 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000003345 natural gas Substances 0.000 description 1
- 239000003921 oil Substances 0.000 description 1
- 150000002894 organic compounds Chemical class 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000013589 supplement Substances 0.000 description 1
- 230000009466 transformation Effects 0.000 description 1
Images
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
- F23G5/02—Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment
- F23G5/027—Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment pyrolising or gasifying stage
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
- F23G5/44—Details; Accessories
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Gasification And Melting Of Waste (AREA)
- Processing Of Solid Wastes (AREA)
Abstract
The invention relates to the technical field of solid waste treatment, and discloses a solid waste treatment device, which comprises: the device comprises a high-temperature cracking cavity, a material inlet and a material outlet, wherein the two ends of the high-temperature cracking cavity are respectively provided with the material inlet and the material outlet; the power device is arranged at one end of the pyrolysis cavity and is used for driving the pyrolysis cavity to rotate; the spiral impeller is arranged inside the pyrolysis cavity; the gas treatment device is communicated with the pyrolysis cavity; and the slag discharging port is positioned below the high-temperature cracking cavity. This solid waste treatment equipment is provided with the pyrolysis chamber and carries out the pyrolysis treatment to solid waste, has very high pyrolysis efficiency, is provided with gas treatment device simultaneously and handles the gas that solid waste pyrolysis produced, avoids discharging toxic gas.
Description
Technical Field
The invention relates to the technical field of solid waste treatment, in particular to a solid waste treatment device.
Background
The solid waste refers to solid, semi-solid and gaseous articles, substances which are discarded or abandoned in a container and are generated in human production construction, daily life and other activities, and articles and substances which are regulated by laws and administrative laws and incorporated into solid waste management, wherein the articles and substances lose original utilization value or are not lost in use value. The solid waste has wide sources, various types, high yield, complex components, large workload and high difficulty in collection, transportation and disposal, and if the solid waste is not treated well, the solid waste pollutes the environment, spreads diseases, influences and hinders the development of the society. The main components of the solid waste are complex organic compounds, and are limited by the high cost of the separation of the converted materials, so that the energy utilization of the solid waste by a thermochemical method is the best way, namely, the solid waste is directly incinerated for utilization or converted into fuel gas and fuel oil. However, in the prior art, the pyrolysis efficiency of the solid waste is not high, so that toxic gases such as dioxin are generated, and secondary pollution is caused.
Disclosure of Invention
The invention aims to solve the problem that toxic gas is generated due to low pyrolysis efficiency of solid waste in the prior art, and provides solid waste treatment equipment.
In order to achieve the above object, an embodiment of the present invention provides a solid waste treatment apparatus including:
the device comprises a high-temperature cracking cavity, a material inlet and a material outlet, wherein the two ends of the high-temperature cracking cavity are respectively provided with the material inlet and the material outlet;
the power device is arranged at one end of the pyrolysis cavity and is used for driving the pyrolysis cavity to rotate;
the spiral impeller is arranged inside the pyrolysis cavity;
the gas treatment device is communicated with the pyrolysis cavity;
and the slag discharging port is positioned below the high-temperature cracking cavity.
Preferably, the solid waste treatment equipment further comprises a reverse conveying device arranged on the outer wall of the pyrolysis cavity, the reverse conveying device is used for conveying the materials flowing out of the material outlet to one side of the material inlet, and the slag discharge port is located on one side of the material inlet.
Preferably, the reverse conveying device comprises a plurality of hooks which are annularly and uniformly distributed along the outer wall of the pyrolysis cavity and are closely arranged along the length direction of the pyrolysis cavity.
Preferably, the hook claw has an installation inclination angle opposite to the advancing direction of the material in the pyrolysis cavity, and the hook claw has a bearing surface for bearing the material.
Preferably, the material outlet of the solid waste treatment apparatus comprises a plurality of overflow holes opened on the pyrolysis chamber.
Preferably, the solid waste treatment equipment further comprises a heat preservation cavity, and the heat preservation cavity is formed by surrounding a heat preservation outer cover arranged around the pyrolysis cavity.
Preferably, the gas treatment device comprises a gas discharge pipeline and a gas return pipeline, and the gas return pipeline is communicated with the heat preservation cavity.
Preferably, the outlet of the gas discharge conduit is in communication with a water vapour container.
Preferably, an electric ignition device is arranged in the heat preservation cavity, and the solid waste treatment equipment further comprises an air supplement pipeline communicated with the heat preservation cavity.
Preferably, the inside of the solid waste treatment apparatus is further provided with a reverse spiral impeller having a reverse spiral direction opposite to the spiral direction of the spiral impeller.
Through the technical scheme, the solid waste treatment equipment provided by the embodiment of the invention is provided with the pyrolysis cavity for carrying out pyrolysis treatment on the solid waste, has high pyrolysis efficiency, and is also provided with the gas treatment device for treating gas generated by pyrolysis of the solid waste, so that toxic gas is prevented from being discharged.
Drawings
Figure 1 shows a perspective view of a solid waste treatment apparatus provided in accordance with an embodiment of the present invention;
figure 2 shows a cross-sectional view of a solid waste treatment apparatus provided in accordance with an embodiment of the present invention;
FIG. 3 illustrates a schematic configuration of a reverse conveying apparatus of a solid waste treatment facility provided according to an embodiment of the present invention;
fig. 4 illustrates a schematic structural view of a claw of a solid waste treatment apparatus according to an embodiment of the present invention.
Description of the reference numerals
1 pyrolysis chamber 2 Material Inlet
3 material outlet 4 power device
5 helical impeller 6 gas treatment device
7 arrange cinder notch 8 and collude claw
9 heat preservation chamber 10 heat preservation dustcoat
11 air supply pipe 12 reverse-spiral impeller
61 gas discharge line 62 gas return line
81 bearing surface
Detailed Description
The following detailed description of embodiments of the invention refers to the accompanying drawings. It should be understood that the detailed description and specific examples, while indicating the present invention, are given by way of illustration and explanation only, not limitation.
Fig. 1 illustrates a perspective view of a solid waste treatment apparatus provided according to an embodiment of the present invention, showing a sectional view of the solid waste treatment apparatus provided according to an embodiment of the present invention. An embodiment of the present invention provides a solid waste treatment apparatus, as shown in fig. 1 or 2, which may include:
the device comprises a high-temperature cracking cavity 1, wherein a material inlet 2 and a material outlet 3 can be respectively arranged at two ends of the high-temperature cracking cavity 1;
the power device 4 can be arranged at one end of the pyrolysis chamber 1, and the power device 4 can be used for driving the pyrolysis chamber 1 to rotate;
the spiral impeller 5, the spiral impeller 5 can be arranged inside the pyrolysis chamber 1;
the gas treatment device 6, the gas treatment device 6 can be communicated with the pyrolysis chamber 1;
the slag discharge port 7, the slag discharge port 7 can be positioned below the pyrolysis cavity 1.
The solid waste treatment equipment provided by the embodiment of the invention is provided with the pyrolysis cavity 1 with the temperature of 200-300 ℃, the pyrolysis cavity 1 is driven by the power device 4 to rotate, the spiral impeller 5 is arranged in the pyrolysis cavity 1 to convey the solid waste to advance in a spiral manner, and the solid waste is subjected to pyrolysis reaction at high temperature. This solid waste treatment equipment has very high pyrolysis efficiency, is provided with gas treatment device 6 simultaneously and handles the gas that the solid waste pyrolysis produced, avoids discharging toxic gas.
In the embodiment of the present invention, the pyrolysis chamber 1 of the solid waste treatment apparatus is an oxygen-free environment, the solid waste after pyrolysis in the pyrolysis chamber 1 is gradually converted into combustible gas and incompletely converted solid waste, if directly discharged, the partially incompletely converted solid waste is carbonized in the pile, and a carbon protective layer is formed on the outside of the material, so that the material cannot be further converted. In view of the above technical problems, in an embodiment of the present invention, the solid waste treatment apparatus may further include a reverse conveying device disposed on an outer wall of the pyrolysis chamber 1, the reverse conveying device being rotatable along with the pyrolysis chamber 1 and conveying the incompletely converted solid waste flowing out of the material outlet 3 to one side of the material inlet 2, the reverse conveying device being an aerobic environment in which the incompletely converted solid waste is secondarily pyrolyzed, thereby further improving pyrolysis efficiency and preventing a carbonized layer from being formed on a surface of the incompletely converted solid waste. The slag discharging opening 7 of the solid waste treatment equipment is positioned at one side of the material inlet 2, and the completely converted solid waste slag conveyed by the reverse conveying device is discharged from the slag discharging opening 7 for further utilization.
Fig. 3 illustrates a schematic configuration view of a reverse conveying device of a solid waste treatment apparatus according to an embodiment of the present invention. As shown in fig. 3, in one embodiment of the present invention, the reverse conveying device of the solid waste treatment apparatus may include a plurality of hooks 8, the plurality of hooks 8 may be annularly and uniformly distributed along an outer wall of the pyrolysis chamber 1 and closely arranged along a length direction of the pyrolysis chamber 1, and the hooks 8 have an installation inclination angle opposite to an advancing direction of the material in the pyrolysis chamber 1. A plurality of hooks 8 are distributed from the material outlet 3 to the material inlet 2, so that the reverse conveying process is completed. And in the reverse conveying process, the hook claw 8 can strip a carbon protective layer possibly formed by the incompletely converted solid waste to realize the further conversion of the solid waste.
Fig. 4 illustrates a schematic structural view of a claw of a solid waste treatment apparatus according to an embodiment of the present invention. In one embodiment of the invention, as shown in fig. 4, the claw 8 of the solid waste treatment apparatus may have a receiving surface 81 for receiving the material. The receiving surfaces 81 of all the hooks 8 form a rotary housing (as shown in fig. 3) arranged outside the pyrolysis chamber 1 for receiving the incompletely converted solid waste slag flowing out of the material outlet 3, and the hooks 8 have an installation inclination angle opposite to the advancing direction of the material in the pyrolysis chamber 1, so that the incompletely converted solid waste slag spirally advances in the direction opposite to the advancing direction of the material in the pyrolysis chamber 1, thereby realizing reverse conveying.
In one embodiment of the present invention, as shown in fig. 2, the material outlet 3 of the solid waste treatment apparatus may include several overflow holes opened on the pyrolysis chamber 1. Specifically, referring to fig. 3, each overflow hole may correspond to one hook 8, the incompletely transformed solid waste flowing out from the overflow hole falls onto a receiving surface 81 of one hook 8, after the hook 8 rotates to the highest point, the solid waste on the receiving surface 81 of the hook 8 falls onto the outer wall of the pyrolysis chamber 1, and the solid waste is located above the receiving surface 81 of the hook 8 at the lower oblique position due to the installation inclination angle of the hook 8, so that after the hook 8 rotates continuously, the solid waste falls onto the receiving surface 81 of the hook 8 at the lower oblique position, and thus the incompletely transformed solid waste flowing out from the material outlet 3 is reversely conveyed to one side of the material theft inlet 2 in one step.
As shown in fig. 2, in one embodiment of the present invention, the solid waste treatment apparatus may further include a thermal insulating chamber 9, and the thermal insulating chamber 9 is surrounded by a thermal insulating housing 10 disposed around the pyrolysis chamber 1. The internal temperature of the heat preservation cavity 9 is about 450 ℃, and the heat preservation cavity 9 can be used for maintaining the high temperature inside the pyrolysis cavity 1 and also used for secondary pyrolysis of incompletely converted solid waste.
As shown in fig. 1, in one embodiment of the present invention, the gas treatment means 7 of the solid waste treatment apparatus may include a gas exhaust pipe 61 and a gas return pipe 62, and the gas return pipe 61 may communicate with the soak chamber 9. Further, an electric ignition device (not shown) is provided in the insulated chamber 9, and the solid waste treatment apparatus may further include an air supply pipe 11 communicating with the insulated chamber 9. The primary preheating of heat preservation chamber 9 is that the combustion-supporting thing (oil, coal, natural gas etc.) is lighted to the electricity ignition device, after heat preservation chamber 9 and pyrolysis chamber 1 reached predetermined temperature after the pyrolysis chamber 1 schizolysis, no longer need supply the combustion-supporting thing, but the combustible gas that solid waste produced after the pyrolysis chamber 1 schizolysis partly can get into heat preservation chamber 9 from gas return line 62, continuously burn as supplementary heat source, thereby for heat preservation chamber 9 with pyrolysis chamber 1 improvement heat in order to maintain high temperature, air supply pipeline 11 can be for combustion process supplementary oxygen, and provide the aerobic environment for the secondary pyrolysis of the solid waste residue of the complete transformation of not flowing out from material export 3. Through the ingenious and unique design, on one hand, the secondary pyrolysis of the incompletely converted solid waste is realized, the pyrolysis efficiency is improved, and the formation of a carbonized layer on the surface of the incompletely converted solid waste is avoided; on the other hand, the full utilization of energy and the continuous operation performance of the equipment are ensured, and the solid waste treatment equipment does not need to add combustion-supporting substances after primary preheating, so that the energy consumption is saved. Because the solid waste is fully pyrolyzed, the generation of toxic gases such as dioxin and the like is further avoided, and the aims of reducing, recycling and harmlessness of the solid waste are fulfilled.
Further, in one embodiment of the present invention, an outlet of the gas exhaust duct 61 of the solid waste treatment apparatus may be communicated with a water vapor container (not shown), and another portion of the combustible gas generated from the solid waste after the solid waste is cracked by the pyrolysis chamber 1 is introduced into the water vapor container through the gas exhaust duct 61, and the combustible gas reacts with the water vapor at a high temperature to generate combustible water gas, the main components of which are carbon monoxide and hydrogen. By the mode, the utilization rate of energy is further improved, and harmful gas emission and secondary pollution are avoided.
In one embodiment of the present invention, as shown in fig. 1, the inside of the solid waste treatment apparatus may be further provided with a reverse-spiral impeller 12 opposite to the rotation direction of the spiral impeller 5. The reverse-spiral impeller 12 can reduce the conveying pressure at one side of the material outlet 3 of the pyrolysis chamber 1, and improve the operation stability and safety of the solid waste treatment equipment.
The preferred embodiments of the present invention have been described in detail above with reference to the accompanying drawings, but the present invention is not limited thereto. Within the scope of the technical idea of the invention, numerous simple modifications can be made to the technical solution of the invention, including combinations of the individual specific technical features in any suitable way. The invention is not described in detail in order to avoid unnecessary repetition. Such simple modifications and combinations should be considered within the scope of the present disclosure as well.
Claims (10)
1. A solid waste treatment apparatus, comprising:
the device comprises a high-temperature cracking cavity, a material inlet and a material outlet, wherein the two ends of the high-temperature cracking cavity are respectively provided with the material inlet and the material outlet;
the power device is arranged at one end of the pyrolysis cavity and is used for driving the pyrolysis cavity to rotate;
the spiral impeller is arranged inside the pyrolysis cavity;
the gas treatment device is communicated with the pyrolysis cavity;
and the slag discharging port is positioned below the high-temperature cracking cavity.
2. The solid waste treatment apparatus of claim 1, further comprising a reverse conveyor disposed on an outer wall of the pyrolysis chamber, the reverse conveyor being configured to convey material flowing from the material outlet to a side of the material inlet, the slag discharge port being located at a side of the material inlet.
3. The solid waste treatment apparatus of claim 2, wherein the reverse conveyor comprises a plurality of hooks annularly and evenly spaced along an outer wall of the pyrolysis chamber and closely arranged along a length of the pyrolysis chamber.
4. The solid waste treatment apparatus of claim 3, wherein the hook has a mounting inclination opposite to the advancing direction of the material in the pyrolysis chamber, the hook having a receiving surface to receive the material.
5. The solid waste treatment apparatus of claim 1, wherein the material outlet of the solid waste treatment apparatus comprises a plurality of overflow holes provided in the pyrolysis chamber.
6. The solid waste treatment apparatus of claim 1, further comprising a holding chamber defined by a holding enclosure disposed about the pyrolysis chamber.
7. The solid waste treatment apparatus of claim 6, wherein the gas treatment device comprises a gas exhaust line and a gas return line, the gas return line communicating with the holding chamber.
8. The solid waste treatment apparatus of claim 7, wherein the outlet of the gas discharge conduit is in communication with a water vapor container.
9. The solid waste treatment apparatus of claim 6, wherein an electric lighter is disposed within the insulated chamber, and further comprising an air supply line in communication with the insulated chamber.
10. The solid waste treatment apparatus of claim 1, wherein the inside of the solid waste treatment apparatus is further provided with a reverse-spiral impeller having a rotation direction opposite to that of the spiral impeller.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201911014087.7A CN110848698A (en) | 2019-10-23 | 2019-10-23 | Solid waste treatment equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201911014087.7A CN110848698A (en) | 2019-10-23 | 2019-10-23 | Solid waste treatment equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN110848698A true CN110848698A (en) | 2020-02-28 |
Family
ID=69597781
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201911014087.7A Pending CN110848698A (en) | 2019-10-23 | 2019-10-23 | Solid waste treatment equipment |
Country Status (1)
| Country | Link |
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| CN (1) | CN110848698A (en) |
Citations (12)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| ES8609667A1 (en) * | 1985-06-21 | 1986-07-16 | Lago Lucia Jose Manue | Installation for the treatment of solid residues. |
| JP2004277551A (en) * | 2003-03-14 | 2004-10-07 | Ngk Insulators Ltd | Pyrolysis gas piping |
| CN104059685A (en) * | 2014-06-09 | 2014-09-24 | 青岛东方循环能源有限公司 | Waste cracking furnace |
| CN203889523U (en) * | 2014-06-09 | 2014-10-22 | 青岛东方循环能源有限公司 | After-treatment device for solid products produced after cracking |
| CN104910930A (en) * | 2014-03-14 | 2015-09-16 | 上海金匙环保科技股份有限公司 | Organic solid waste pyrolysis treatment device, system and method |
| CN105087038A (en) * | 2015-09-17 | 2015-11-25 | 湖南奔骥环保能源科技有限责任公司 | All-closed integrated continuous refining device |
| CN205241605U (en) * | 2015-12-11 | 2016-05-18 | 青岛伊诺威能源化工新技术有限公司 | Hot type solid organic matter pyrolysis furnace in succession |
| CN206375857U (en) * | 2016-10-18 | 2017-08-04 | 湖南省君鹏环保科技有限公司 | Cracking of waste plastics equipment for gasification |
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| CN208535998U (en) * | 2018-04-20 | 2019-02-22 | 河南天泰网安信息技术有限公司 | A kind of waste energy regeneration pyrolysis treatment systems |
| CN109531812A (en) * | 2019-01-07 | 2019-03-29 | 河北联众谊诚混凝土有限公司 | A kind of concrete process equipment |
| CN211625262U (en) * | 2019-10-23 | 2020-10-02 | 安徽省华冠生态科技有限公司 | Solid waste treatment equipment |
-
2019
- 2019-10-23 CN CN201911014087.7A patent/CN110848698A/en active Pending
Patent Citations (12)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| ES8609667A1 (en) * | 1985-06-21 | 1986-07-16 | Lago Lucia Jose Manue | Installation for the treatment of solid residues. |
| JP2004277551A (en) * | 2003-03-14 | 2004-10-07 | Ngk Insulators Ltd | Pyrolysis gas piping |
| CN104910930A (en) * | 2014-03-14 | 2015-09-16 | 上海金匙环保科技股份有限公司 | Organic solid waste pyrolysis treatment device, system and method |
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| CN203889523U (en) * | 2014-06-09 | 2014-10-22 | 青岛东方循环能源有限公司 | After-treatment device for solid products produced after cracking |
| CN105087038A (en) * | 2015-09-17 | 2015-11-25 | 湖南奔骥环保能源科技有限责任公司 | All-closed integrated continuous refining device |
| CN205241605U (en) * | 2015-12-11 | 2016-05-18 | 青岛伊诺威能源化工新技术有限公司 | Hot type solid organic matter pyrolysis furnace in succession |
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