CN102009060A - Device for continuously discharging gas-solid phase products of pyrolyzed organic solid wastes - Google Patents
Device for continuously discharging gas-solid phase products of pyrolyzed organic solid wastes Download PDFInfo
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- CN102009060A CN102009060A CN 201010508090 CN201010508090A CN102009060A CN 102009060 A CN102009060 A CN 102009060A CN 201010508090 CN201010508090 CN 201010508090 CN 201010508090 A CN201010508090 A CN 201010508090A CN 102009060 A CN102009060 A CN 102009060A
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- rotary reactor
- reactor
- conveying worm
- rotary
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Abstract
The invention discloses a device for continuously discharging gas-solid phase products of pyrolyzed organic solid wastes. In the device, a material scoop for lifting 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 inner cavity of the rotary reactor; a screw conveyor is arranged under the hopper; one part of the screw conveyor is arranged in the inner cavity of the rotary reactor, and the other part of the screw conveyor is arranged outside the rotary reactor; the part of the screw conveyor arranged in the rotary reactor is supported by a sliding bearing; the outer housing of the sliding bearing is fixed on the rotary conveyor; the inner housing of the sliding bearing is fixed on the screw conveyor; the part of the screw conveyor positioned outside the rotary reactor is supported by a support piece; and the rotary reactor is communicated with a gas-phase product discharge channel. By the device, the solid wastes in the reactor can be continuously discharged in gas and solid split phases when the reactor runs normally; and the whole process can be automatically controlled, the emission is performed in a closed atmosphere, the environment is not polluted, and the safety is high.
Description
Technical field:
The present invention 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:
The object of the present invention is to provide a kind of rational in infrastructurely, the organic solid waste pyrolyze product gas-solid of under the state of the normal operation of reactor the discarded object gas in the reactor, solid phase-splitting being got rid of continuously is tapping equipment continuously mutually.
Technical solution of the present invention 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 present invention is rational in infrastructure, by scoop, hopper, pass air-valve, the conveying worm that is provided with in the reactor, sliding bearing etc. are 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 invention will be further described below in conjunction with drawings and Examples.
Fig. 1 is the configuration diagram of one embodiment of the invention.
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 |
|---|---|---|---|
| CN 201010508090 CN102009060A (en) | 2010-09-30 | 2010-09-30 | Device for continuously discharging gas-solid phase products of pyrolyzed organic solid wastes |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201010508090 CN102009060A (en) | 2010-09-30 | 2010-09-30 | Device for continuously discharging gas-solid phase products of pyrolyzed organic solid wastes |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN102009060A true CN102009060A (en) | 2011-04-13 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201010508090 Pending CN102009060A (en) | 2010-09-30 | 2010-09-30 | Device for continuously discharging gas-solid phase products of pyrolyzed organic solid wastes |
Country Status (1)
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| CN (1) | CN102009060A (en) |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4308103A (en) * | 1980-06-02 | 1981-12-29 | Energy Recovery Research Group, Inc. | Apparatus for the pyrolysis of comminuted solid carbonizable materials |
| US4439209A (en) * | 1982-08-25 | 1984-03-27 | Wilwerding Carl M | Thermal decomposition apparatus |
| WO1999018170A1 (en) * | 1997-10-02 | 1999-04-15 | Mannesmann Ag | Method and installation for extracting a fraction of a carbon-containing valuable product |
| CN201832618U (en) * | 2010-09-30 | 2011-05-18 | 赵旭荣 | Organic solid waste pyrolytic product gas-and-solid-phase continuous discharge device |
-
2010
- 2010-09-30 CN CN 201010508090 patent/CN102009060A/en active Pending
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4308103A (en) * | 1980-06-02 | 1981-12-29 | Energy Recovery Research Group, Inc. | Apparatus for the pyrolysis of comminuted solid carbonizable materials |
| US4439209A (en) * | 1982-08-25 | 1984-03-27 | Wilwerding Carl M | Thermal decomposition apparatus |
| WO1999018170A1 (en) * | 1997-10-02 | 1999-04-15 | Mannesmann Ag | Method and installation for extracting a fraction of a carbon-containing valuable product |
| CN201832618U (en) * | 2010-09-30 | 2011-05-18 | 赵旭荣 | Organic solid waste pyrolytic product gas-and-solid-phase continuous discharge device |
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Application publication date: 20110413 |