CN201832618U - Organic solid waste pyrolytic product gas-and-solid-phase continuous discharge device - Google Patents
Organic solid waste pyrolytic product gas-and-solid-phase continuous discharge device Download PDFInfo
- Publication number
- CN201832618U CN201832618U CN2010205611916U CN201020561191U CN201832618U CN 201832618 U CN201832618 U CN 201832618U CN 2010205611916 U CN2010205611916 U CN 2010205611916U CN 201020561191 U CN201020561191 U CN 201020561191U CN 201832618 U CN201832618 U CN 201832618U
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- China
- Prior art keywords
- rotary reactor
- solid
- reactor
- conveying worm
- rotary
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- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
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- 239000002910 solid waste Substances 0.000 title claims abstract description 21
- 239000007790 solid phase Substances 0.000 title claims abstract description 12
- 239000012071 phase Substances 0.000 claims abstract description 6
- 230000008093 supporting effect Effects 0.000 claims abstract description 5
- 239000007787 solid Substances 0.000 claims description 9
- 238000010079 rubber tapping Methods 0.000 claims description 7
- 230000008676 import Effects 0.000 claims description 3
- 238000000034 method Methods 0.000 abstract description 5
- 239000000047 product Substances 0.000 description 14
- 239000007789 gas Substances 0.000 description 8
- 238000000197 pyrolysis Methods 0.000 description 5
- 238000006243 chemical reaction Methods 0.000 description 3
- 239000002699 waste material Substances 0.000 description 3
- 238000004939 coking Methods 0.000 description 2
- 238000001816 cooling Methods 0.000 description 2
- 238000003912 environmental pollution Methods 0.000 description 2
- 239000002253 acid Substances 0.000 description 1
- 150000007513 acids Chemical class 0.000 description 1
- 239000006229 carbon black Substances 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000004033 plastic Substances 0.000 description 1
- 229920003023 plastic Polymers 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 230000002000 scavenging effect Effects 0.000 description 1
- 239000012265 solid product Substances 0.000 description 1
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- Processing Of Solid Wastes (AREA)
Abstract
The utility model discloses an organic solid waste pyrolytic product gas-and-solid-phase continuous discharge device which is characterized in that a spoon which can lift solid-phase products deposited on the wall of a rotary reactor to a collection hopper is arranged on the inner wall of the rotary reactor, the hopper is arranged in the cavity of the rotary reactor and a screw conveyer is arranged below the hopper; one part of the screw conveyer is arranged in the cavity of the rotary reactor, the other part of the screw conveyer is arranged outside the rotary reactor, the part of the screw conveyer arranged in the rotary reactor is supported through a sliding bearing, the outer sleeve of the sliding bearing is fixed on the rotary reactor, the inner sleeve of the sliding bearing is fixed on the screw conveyer, and the part of the screw conveyer arranged outside the rotary reactor is supported through a supporting member; and the rotary reactor is communicated with a gas-phase product discharge passage. Under the situation that the reactor runs normally, solid wastes in the reactor are continuously discharged separately according to gas phase and solid phase, the automatic control of the whole process can be realized, the environment is not polluted because the solid wastes are emitted under a closed environment, and the safety is high.
Description
Technical field:
The utility model relates to the continuous mutually tapping equipment of a kind of organic solid waste pyrolyze product gas-solid.
Background technology:
At present, organic solid waste such as waste plastics, scrap rubber, house refuse debirs and other organic solid wastes carry out minimizing, disposal of resources, generally adopt fixed reactor or rotary reactor pyrolysis.Adopt fixed reactor pyrolysis organic solid waste, generation solid waste can precipitate and condense upon on the reactor, and coking just generally will stop reaction, cooling back with the removing of ways such as steam, compress wind in reactor, carry out next round production again.Adopt rotary reactor pyrolysis organic solid waste, overcome the coking shortcoming, remove with methods such as machineries again but the solid waste after the cleaning pyrolysis still will stop reaction.There is following problem in these two kinds of modes: intermittent discharge generates the solid phase refuse, wastes energy, and reaction efficiency is low; Solid phase waste scavenging process pollutes the environment; Can not full process automatization operate the operating cost height; Rotary reactor is removed problem of environmental pollution equally, also will be at high temperature with the solid waste outlet and the outer conveying equipment interface of reactor of reactor, and the attended operation difficulty has major safety risks under the high temperature.
Summary of the invention:
It is a kind of rational in infrastructure that the purpose of this utility model is to provide, the continuous mutually tapping equipment of the organic solid waste pyrolyze product gas-solid of under the state that reactor normally moves the discarded object gas in the reactor, solid phase-splitting being got rid of continuously.
Technical solution of the present utility model is:
The continuous mutually tapping equipment of a kind of organic solid waste pyrolyze product gas-solid, comprise rotary reactor, it is characterized in that: rotary reactor wall is provided with and rises to the scoop of bunker for collecting with being deposited on solid phase product on the rotary reactor wall, hopper is arranged in the rotary reactor inner chamber, and the hopper below is provided with conveying worm; Conveying worm partly is arranged in the rotary reactor inner chamber, part is arranged on outside the rotary reactor, the part of conveying worm in rotary reactor passed through sliding supported condition, the overcoat of sliding bearing is fixed on the rotary reactor, the interior cover of sliding bearing is fixed on the conveying worm, and conveying worm is positioned at the outer part of rotary reactor and passes through supporting members support; Rotary reactor communicates with gas phase product passing away.
Between hopper outlet and conveying worm import the pass air-valve is set, closing air-valve is the driving gear pair type of belt drive, and driving gear pair is connected with conveying worm screw rod main shaft.
The utility model is rational in infrastructure, by scoop, hopper, pass air-valve, the conveying worm that is provided with in the reactor, sliding bearing etc., under the state of the normal operation of reactor, under the condition of just identical temperature, pressure, operation, the solid waste gas in the reactor, solid phase-splitting are got rid of continuously.Parking, cooling, uneasy congruence shortcoming have been avoided.Can realize that full process automatization is controlled, airtight discharging is free from environmental pollution, degree of safety is high.Increase substantially operational efficiency, energy savings.
Description of drawings:
The utility model is described in further detail below in conjunction with drawings and Examples.
Fig. 1 is the configuration diagram of an embodiment of the utility model.
Fig. 2 is the cutaway view at scoop, hopper position.
The specific embodiment:
The continuous mutually tapping equipment of a kind of organic solid waste pyrolyze product gas-solid, comprise rotary reactor 1, rotary reactor wall is provided with and rises to the scoop 2 of bunker for collecting 3 with being deposited on solid phase product on the rotary reactor wall, hopper 3 is arranged in the rotary reactor inner chamber, and the hopper below is provided with conveying worm 5; Conveying worm partly is arranged in the rotary reactor inner chamber, part is arranged on outside the rotary reactor, the part of conveying worm in rotary reactor is by sliding bearing 6 supportings, the overcoat of sliding bearing is fixed on the rotary reactor, the interior cover of sliding bearing is fixed on the conveying worm, and conveying worm is positioned at the outer part of rotary reactor by support column (routine concrete foundation) 7 supportings; Rotary reactor and gas phase product passing away 8 communicate by the gap.
Be provided with between hopper outlet and conveying worm import and close air-valve 9, closing air-valve is driving gear pair 10 type of belt drive, and driving gear pair is connected with conveying worm screw rod main shaft 11.Also have motor, reductor 4 among the figure.
Because of the solid phase product under gravity and the centrifugal action utilization is deposited on the reactor wall, rely on the rotation of rotational response device to drive the scoop that is fixed on the reactor wall, refuse is risen to bunker for collecting; Bunker for collecting is installed on the conveying worm with reactor rotary middle spindle same position; Relevant air-valve between hopper and conveying worm separates solid phase product and gas phase product; The solid phase product is got rid of outside the reactor with conveying worm.Organic solid waste can be got rid of in conveying worm at carbon black, silt, other solid waste that continuous pyrolysis, solid product contain the condition of high temperature; The gas product that is blocked has oil gas, acids gas etc. to get rid of continuously outside conveying worm.
Claims (2)
1. organic solid waste pyrolyze product gas-solid continuous tapping equipment mutually, comprise rotary reactor, it is characterized in that: rotary reactor wall is provided with and rises to the scoop of bunker for collecting with being deposited on solid phase product on the rotary reactor wall, hopper is arranged in the rotary reactor inner chamber, and the hopper below is provided with conveying worm; Conveying worm partly is arranged in the rotary reactor inner chamber, part is arranged on outside the rotary reactor, the part of conveying worm in rotary reactor passed through sliding supported condition, the overcoat of sliding bearing is fixed on the rotary reactor, the interior cover of sliding bearing is fixed on the conveying worm, and conveying worm is positioned at the outer part of rotary reactor and passes through supporting members support; Rotary reactor communicates with gas phase product passing away.
2. the continuous mutually tapping equipment of organic solid waste pyrolyze product according to claim 1 gas-solid, it is characterized in that: between hopper outlet and conveying worm import, the pass air-valve is set, closing air-valve is the driving gear pair type of belt drive, and driving gear pair is connected with conveying worm screw rod main shaft.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010205611916U CN201832618U (en) | 2010-09-30 | 2010-09-30 | Organic solid waste pyrolytic product gas-and-solid-phase continuous discharge device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010205611916U CN201832618U (en) | 2010-09-30 | 2010-09-30 | Organic solid waste pyrolytic product gas-and-solid-phase continuous discharge device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201832618U true CN201832618U (en) | 2011-05-18 |
Family
ID=44002713
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2010205611916U Expired - Lifetime CN201832618U (en) | 2010-09-30 | 2010-09-30 | Organic solid waste pyrolytic product gas-and-solid-phase continuous discharge device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201832618U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102009060A (en) * | 2010-09-30 | 2011-04-13 | 赵旭荣 | Device for continuously discharging gas-solid phase products of pyrolyzed organic solid wastes |
| CN104075330A (en) * | 2014-06-30 | 2014-10-01 | 辽宁工程技术大学 | Medical waste rotary kiln pyrolytic reaction device |
-
2010
- 2010-09-30 CN CN2010205611916U patent/CN201832618U/en not_active Expired - Lifetime
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102009060A (en) * | 2010-09-30 | 2011-04-13 | 赵旭荣 | Device for continuously discharging gas-solid phase products of pyrolyzed organic solid wastes |
| CN104075330A (en) * | 2014-06-30 | 2014-10-01 | 辽宁工程技术大学 | Medical waste rotary kiln pyrolytic reaction device |
| CN104075330B (en) * | 2014-06-30 | 2016-04-20 | 辽宁工程技术大学 | A kind of medical waste rotary kiln pyrogenation reaction unit |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| ASS | Succession or assignment of patent right |
Owner name: NANTONG TIANYI ENVIRONMENTAL TECH-ENERGY CO., LTD. Free format text: FORMER OWNER: ZHAO XURONG Effective date: 20111104 Free format text: FORMER OWNER: LI JIANGUO |
|
| C41 | Transfer of patent application or patent right or utility model | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20111104 Address after: 345 No. 226011 Jiangsu city of Nantong province tongNing Avenue Patentee after: Nantong Tianyi Environmental Protection Energy Equipment Co., Ltd. Address before: 345 No. 226011 Jiangsu city of Nantong province tongNing Avenue Co-patentee before: Li Jianguo Patentee before: Zhao Xurong |
|
| CX01 | Expiry of patent term | ||
| CX01 | Expiry of patent term |
Granted publication date: 20110518 |