CN205640938U - Platinum catalyst tail washings processing apparatus who retrieve, purification process produces - Google Patents
Platinum catalyst tail washings processing apparatus who retrieve, purification process produces Download PDFInfo
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- CN205640938U CN205640938U CN201620297294.3U CN201620297294U CN205640938U CN 205640938 U CN205640938 U CN 205640938U CN 201620297294 U CN201620297294 U CN 201620297294U CN 205640938 U CN205640938 U CN 205640938U
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- tail washings
- incinerator
- sludge pump
- purification process
- platinum catalyst
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Abstract
The utility model discloses a platinum catalyst tail washings processing apparatus who retrieve, purification process produces, including the clarification storage tank, stir sludge pump, the spiral shell centrifuge and burn burning furnace of crouching certainly, catalyst tail washings dress deposits at the clarification storage tank, and clarification tank outlet connects from stirring the sludge pump, stirs the sludge pump exit linkage spiral shell centrifuge that crouches certainly, and the spiral shell centrifuge exit linkage that crouches burns burning furnace burn the charging tray that is provided with the liftable in the burning furnace. The utility model discloses a platinum catalyst tail washings processing apparatus who retrieve, purification process produces to the great catalyst tail washings of viscosity, adopts earlier and stirs from stirring the sludge pump, then handles through the spiral shell centrifuge that crouches for the water content reduces, and entering is at last burnt burning furnace and is carried out incineration disposal, and this equipment structure is reasonable, and is efficient, and the treatment effect is good, moreover reducing pollutants.
Description
Technical field
This utility model relates to catalyst tail washings processing technology field, the platinum catalyst tail washings processing means produced particularly to a kind of recovery, purification process.
Background technology
The tail washings viscosity of platinum catalyst is higher, and traditional equipment processing tail washings and technique slag liquid moisture content are high, and subsequent treatment environmental pollution is bigger, it is impossible to be up to state standards.Traditional handicraft is: the clarification storage tank slag liquid of 40% (aqueous >=)--------steel charging tray--------pusher furnace burning-------exhaust treatment system.Feed liquid is fast to charging tray corrosion, and pusher furnace treatment effeciency is low, pollutes big, and processes not thorough, weak effect.
Accordingly, it would be desirable to a kind of new equipment, and the catalyst tail washings that viscosity is bigger is processed by new technological process, to reduce environmental pollution, improves efficiency and effect.
Utility model content
This utility model technical issues that need to address are that the processing equipment of the existing catalyst tail washings higher to viscosity pollutes weight, and efficiency is low, weak effect.
For solving above-mentioned technical problem, the platinum catalyst tail washings processing means that this utility model provides a kind of recovery, purification process produces, including clarification storage tank, certainly stir sludge pump, horizontal screw centrifuge and incinerator, catalyst tail washings is contained in clarification storage tank and precipitates, clarification outlet connects from stirring sludge pump, connecting horizontal screw centrifuge from stirring sludge pump outlet, horizontal screw centrifuge outlet connects incinerator, is provided with liftable charging tray in described incinerator.The platinum catalyst tail washings processing means that recovery of the present utility model, purification process produce, for the catalyst tail washings that viscosity is bigger, first uses and is stirred from stirring sludge pump, then process through horizontal screw centrifuge, water content being reduced, finally enters incinerator and carry out burning disposal, charging tray is set to liftable charging tray, convenient charging, and the efficiency of burning ratio can be made to maximize, whole device structure is reasonable, and efficiency is high, high treating effect, and reduce pollution.
Further, also include that emission-control equipment, described emission-control equipment are connected to the air exit of incinerator.Incinerator is processed the tail gas produced and carries out purified treatment, reduce further pollution.
Optimal technical scheme is, clarification storage tank, certainly stirs between sludge pump, horizontal screw centrifuge and incinerator and all to carry out material transmission by auger connection.Owing to the viscosity of tail washings is higher, thus the material of tail washings transmits to use and carries dynamic auger to realize, and can improve efficiency, is equivalent to tail washings is carried out pre-stirring during transmitting simultaneously, kills two birds with one stone.
Further improvement is that, described charging tray is provided in round, center is rotationally connected with rotary shaft, whole charging tray even partition is multiple region, rotary shaft is rotatably connected on incinerator crown center position, incinerator top is provided with charging aperture, and the outlet of the auger being connected with horizontal screw centrifuge is connected to charging aperture, and the region of each separation of charging tray all can be turned to below charging aperture.Charging tray can be steel charging tray, the card subregion of charging tray, the contact surface of burning can be improved, improve efficiency, and charging tray charging is convenient and swift, can first charging tray be promoted near charging aperture, auger rotates charging, one region rotates charging tray after having fed, subsequent region is fed, charging tray is down in incinerator after having fed suitably region burn, materials from spattering when avoiding feeding, fall into bottom incinerator, it is difficult to clear up, and the position that charging tray is in incinerator can be adjusted according to the incineration temperature that material needs, efficiency is high, and energy-conserving and environment-protective.
The platinum catalyst tail washings processing means that recovery of the present utility model, purification process produce, device efficiency is high, energy-conserving and environment-protective, and process technique the most more high-efficiency environment friendly, the aqueous >=slag liquid of 40% was precipitated by clarification storage tank before this, after by underflow through from stirring sludge pump stirring, after horizontal screw centrifuge processes, slag liquid is aqueous is down to about 10%, then enters incinerator and burns, and the waste gas that incinerator produces also enters air after exhaust treatment system processes.The platinum catalyst tail washings processing means that recovery of the present utility model, purification process produce, processing through horizontal screw centrifuge after first stirring from stirring sludge pump, solid-liquid separation effect is the best, and discharging Slag treatment puts in place again, for finally burning the basis established, making incinerator firing efficiency high, slag loss is few, and the charging tray life-span is long, greatly reduce environmental pollution simultaneously, the reasonable in design of incinerator, can improve efficiency, extension device service life.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model；
Fig. 2 is the top view of this utility model charging tray；
Wherein, 1-clarifies storage tank, and 2-is from stirring sludge pump, 3-horizontal screw centrifuge, 4-incinerator, 5-charging tray, 6-exhaust treatment system, 7-auger, 8-rotary shaft, 9-charging aperture.
Detailed description of the invention
Describe optimal technical scheme of the present utility model below in conjunction with the accompanying drawings in detail.
As shown in the figure, the platinum catalyst tail washings processing means that recovery of the present utility model, purification process produce, including clarification storage tank 1, from stirring sludge pump 2, horizontal screw centrifuge 3 and incinerator 4, catalyst tail washings is contained in clarification storage tank 1 and precipitates, clarification storage tank 1 outlet connects from stirring sludge pump 2, horizontal screw centrifuge 3 is connected from stirring sludge pump 2 outlet, horizontal screw centrifuge 3 outlet connects incinerator 4, liftable charging tray 5 it is provided with in described incinerator 4, also include that emission-control equipment 6, described emission-control equipment 6 are connected to the air exit of incinerator 4.
Wherein, clarify storage tank 1, from stirring sludge pump 2, all carrying out material transmission by auger 7 connection between horizontal screw centrifuge 3 and incinerator 4, described charging tray 5 is provided in round, center is rotationally connected with rotary shaft 8, whole charging tray 5 even partition is multiple region, rotary shaft 8 is rotatably connected on incinerator 4 crown center position, incinerator 4 top is provided with charging aperture 9, the outlet of the auger 7 being connected with horizontal screw centrifuge 3 is connected to charging aperture 9, and the region of each separation of charging tray 5 all can be turned to below charging aperture 9.
The platinum catalyst tail washings processing means that recovery of the present utility model, purification process produce, for the catalyst tail washings that viscosity is bigger, first uses and is stirred from stirring sludge pump, then process through horizontal screw centrifuge, water content being reduced, finally enters incinerator and carry out burning disposal, charging tray is set to liftable charging tray, convenient charging, and the efficiency of burning ratio can be made to maximize, whole device structure is reasonable, and efficiency is high, high treating effect, and reduce pollution.
Incinerator is processed the tail gas produced and carries out purified treatment, reduce further pollution.
Owing to the viscosity of tail washings is higher, thus the material of tail washings transmits to use and carries dynamic auger to realize, and can improve efficiency, is equivalent to tail washings is carried out pre-stirring during transmitting simultaneously, kills two birds with one stone.
Charging tray can be steel charging tray, the card subregion of charging tray, the contact surface of burning can be improved, improve efficiency, and charging tray charging is convenient and swift, can first charging tray be promoted near charging aperture, auger rotates charging, one region rotates charging tray after having fed, subsequent region is fed, charging tray is down in incinerator after having fed suitably region burn, materials from spattering when avoiding feeding, fall into bottom incinerator, it is difficult to clear up, and the position that charging tray is in incinerator can be adjusted according to the incineration temperature that material needs, efficiency is high, and energy-conserving and environment-protective.
The platinum catalyst tail washings processing means that recovery of the present utility model, purification process produce, device efficiency is high, energy-conserving and environment-protective, and processing technique the most more high-efficiency environment friendly, the aqueous >=slag liquid of 40% was precipitated by clarification storage tank before this, by from stirring sludge pump stirring, after horizontal screw centrifuge processes, slag liquid is aqueous about 10%, then enters incinerator and burns, and the waste gas that incinerator produces also enters air after exhaust treatment system processes.The platinum catalyst tail washings processing means that recovery of the present utility model, purification process produce, processing through horizontal screw centrifuge after first stirring from stirring sludge pump, solid-liquid separation effect is the best, and discharging Slag treatment puts in place again, for finally burning the basis established, making incinerator firing efficiency high, slag loss is few, and the charging tray life-span is long, greatly reduce environmental pollution simultaneously, the reasonable in design of incinerator, can improve efficiency, extension device service life.
Claims (4)
1. the platinum catalyst tail washings processing means that a recovery, purification process produce, it is characterized in that: include clarifying storage tank, certainly stirring sludge pump, horizontal screw centrifuge and incinerator, catalyst tail washings is contained in clarification storage tank and precipitates, clarification outlet connects from stirring sludge pump, horizontal screw centrifuge is connected from stirring sludge pump outlet, horizontal screw centrifuge outlet connects incinerator, is provided with liftable charging tray in described incinerator.
The platinum catalyst tail washings processing means that recovery the most as claimed in claim 1, purification process produce, it is characterised in that: also include that emission-control equipment, described emission-control equipment are connected to the air exit of incinerator.
Reclaim the most as claimed in claim 1 or 2, platinum catalyst tail washings processing means that purification process produces, it is characterised in that: clarification storage tank, certainly stir between sludge pump, horizontal screw centrifuge and incinerator and all to carry out material transmission by auger connection.
The platinum catalyst tail washings processing means that recovery the most as claimed in claim 3, purification process produce, it is characterized in that: described charging tray is provided in round, center is rotationally connected with rotary shaft, whole charging tray even partition is multiple region, rotary shaft is rotatably connected on incinerator crown center position, incinerator top is provided with charging aperture, and the outlet of the auger being connected with horizontal screw centrifuge is connected to charging aperture, and the region of each separation of charging tray all can be turned to below charging aperture.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620297294.3U CN205640938U (en) | 2016-04-12 | 2016-04-12 | Platinum catalyst tail washings processing apparatus who retrieve, purification process produces |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620297294.3U CN205640938U (en) | 2016-04-12 | 2016-04-12 | Platinum catalyst tail washings processing apparatus who retrieve, purification process produces |
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| CN205640938U true CN205640938U (en) | 2016-10-12 |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106287750A (en) * | 2016-10-20 | 2017-01-04 | 湖南野森环保科技有限责任公司 | A kind of environment-friendly type mud-processing equipment |
| CN107520239A (en) * | 2017-09-21 | 2017-12-29 | 航天环境工程有限公司 | Plasma dangerous waste processing method |
| CN107559838A (en) * | 2017-09-21 | 2018-01-09 | 航天环境工程有限公司 | The control method of plasma smelting furnace |
-
2016
- 2016-04-12 CN CN201620297294.3U patent/CN205640938U/en active Active
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106287750A (en) * | 2016-10-20 | 2017-01-04 | 湖南野森环保科技有限责任公司 | A kind of environment-friendly type mud-processing equipment |
| CN107520239A (en) * | 2017-09-21 | 2017-12-29 | 航天环境工程有限公司 | Plasma dangerous waste processing method |
| CN107559838A (en) * | 2017-09-21 | 2018-01-09 | 航天环境工程有限公司 | The control method of plasma smelting furnace |
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