CN205020091U - Integrative stove of petrochemical industry activation - Google Patents
Integrative stove of petrochemical industry activation Download PDFInfo
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- CN205020091U CN205020091U CN201520729651.4U CN201520729651U CN205020091U CN 205020091 U CN205020091 U CN 205020091U CN 201520729651 U CN201520729651 U CN 201520729651U CN 205020091 U CN205020091 U CN 205020091U
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- stove
- furnace
- petrochemical industry
- inner bag
- industry activation
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Abstract
The utility model relates to a production facility technical field, concretely relates to integrative stove of petrochemical industry activation, including the reacting furnace, the reacting furnace includes stove and lower stove, go up the stove and be equipped with the spout down between the stove, spout department is equipped with the slide, and go up the stove and include stove outer covering and inner bag, be equipped with resistance heater between stove outer covering and the inner bag, go up furnace roof portion and be equipped with feed inlet and gas vent, the stove lower part is equipped with steam inlet down, and lower stove upper portion is equipped with steam outlet, and the bottom is equipped with the toper discharge gate, simple structure, and reasonable in design, it is convenient to use.
Description
Technical field
The utility model relates to production equipment technical field, is specifically related to petrochemical industry activation integral furnace.
Background technology
Adsorbent is widely used in the numerous areas, particularly active carbon such as chemical industry, food, medicine, environmental protection, metallurgy, the development of demand along with society of absorbent charcoal material and the raising of living standards of the people, in the trend risen year by year.In the production process of active carbon, carbon containing matter obtains carbide after petrochemical industry, reactivation carbide thus obtain active carbon, petrochemical industry activation process plays vital effect to the output of active carbon and quality, at present, usually chemical method is utilized to produce active carbon, comprising following technique: one is that acid solution reclaims.In the recycling bin opened wide, normally use the acid soak active carbon semi-finished product of variable concentrations, with the acid solution of adsorbing in recovered carbon, this natural impregnation method, generally will through the lixiviate repeatedly of the gradient liquid 7 times of variable concentrations, just can reach the object of recovery, complex operation step, the cycle is long, labour intensity is high, and in recovery, produce a large amount of phosphoric acid steam, have impact on production environment.Two is rinsings, is normally sent in rinsing bath by the active carbon semi-finished product after reclaiming, allows water slowly flood, and makes acid solution discharging slowly, like this, and the deficiencies such as life period is long, labour intensity is high, water consumption is large.Three is boilings.In order to reduce ash content in active carbon and content of beary metal, need in active carbon, add hydrochloric acid or caustic soda, boiling is carried out in heating, is dissolved in by insoluble metallic salt wherein in hydrochloric acid solution or caustic soda, then with deionized water by its wash-out out.Boiling will be passed through heating, stirring, acid discharge, add water washing, and the operations such as charcoal, water separation, will complete above-mentioned steps in distinct device, operating process is cumbersome, adds workload.
Utility model content
The utility model object is to provide petrochemical industry activation integral furnace, to solve many defects that prior art deficiency causes.
Petrochemical industry activation integral furnace, comprise reacting furnace, described reacting furnace comprises stove and lower stove, is provided with chute between described upper stove and lower stove, and described chute place is provided with slide plate, upper stove comprises furnace shell and inner bag, be provided with resistance heater between described furnace shell and inner bag, upper furnace roof portion is provided with charging aperture and exhaust outlet, and described lower stove bottom is provided with steam inlet, lower stove top is provided with steam (vapor) outlet, and bottom is provided with conical discharge port.
Preferably, described inner bag adopts ceramic material to make.
Preferably, be provided with temperature sensor in described inner bag, described furnace shell is provided with controller, and described temperature sensor is electrically connected with controller, and described controller is electrically connected with resistance heater.
Preferably, described steam inlet place is provided with electric-air valve.
Preferably, described exhaust outlet is connected with recover.
The utility model has the advantage of, carbon containing matter enters upper stove from charging aperture, by resistive heater heats inner bag, and control temperature reaches between 500-600 degree, carbon containing matter heat drying is made it charing, the mist produced then is discharged by exhaust outlet, carbonization reaction terminates rear moving slide board makes carbide fall into lower stove, add high-temperature steam carry out the activation of carbide thus obtain finished product, finished product is collected via conical discharge port, inner bag adopts ceramic material to make, corrosion-and high-temp-resistant, increase the service life, temperature sensor and the convenient temperature of observing and controlling inner bag heating of controller, electric-air valve can control steam inlet and admission velocity, recover can recycling carbonization reaction produce mist and avoid environmental pollution, the utility model structure is simple, reasonable in design, easy to use, economic environmental protection.
Accompanying drawing explanation
Fig. 1 is the structural representation of petrochemical industry activation integral furnace described in the utility model.
Wherein, the upper stove of 1-, stove under 2-, 3-furnace shell, 4-inner bag, 5-charging aperture, 6-exhaust outlet, 7-resistance heater, 8-chute, 9-slide plate, 10-steam inlet, 11-steam (vapor) outlet, 12-conical discharge port, 13-recover, 14-electric-air valve, 15-temperature sensor, 16-controller.
Detailed description of the invention
The technological means realized for making the utility model, creation characteristic, reaching object and effect is easy to understand, below in conjunction with detailed description of the invention, setting forth the utility model further.
Petrochemical industry activation integral furnace as shown in Figure 1, comprise reacting furnace, described reacting furnace comprises stove 1 and lower stove 2, chute 8 is provided with between described upper stove 1 and lower stove 2, described chute 8 place is provided with slide plate 9, upper stove 1 comprises furnace shell 3 and inner bag 4, resistance heater 7 is provided with between described furnace shell 3 and inner bag 4, upper stove 1 top is provided with charging aperture 5 and exhaust outlet 6, described lower stove 2 bottom is provided with steam inlet 10, lower stove 2 top is provided with steam (vapor) outlet 11, bottom is provided with conical discharge port 12, carbon containing matter enters upper stove 1 from charging aperture 5, by resistance heater 7 heating inner liner 2, and control temperature reaches between 500-600 degree, carbon containing matter heat drying is made it charing, the mist produced then is discharged by exhaust outlet 6, carbonization reaction terminates rear moving slide board 9 makes carbide fall into lower stove 2, add high-temperature steam carry out the activation of carbide thus obtain finished product, finished product is collected via conical discharge port 12.
It should be noted that described inner bag 4 adopts ceramic material to make, corrosion-and high-temp-resistant, increases the service life.
In the present embodiment, be provided with temperature sensor 15 in described inner bag 4, described furnace shell 3 is provided with controller 16, and described temperature sensor 15 is electrically connected with controller 16, and described controller 16 is electrically connected with resistance heater 7, the convenient temperature observed and control inner bag 4 and heat.
In the present embodiment, described steam inlet 10 place is provided with electric-air valve 14, controls steam inlet and admission velocity.
In addition, described exhaust outlet 6 is connected with recover 13, and the mist that recycling carbonization reaction produces also avoids environmental pollution.
Based on above-mentioned, petrochemical industry activation integral furnace of the present utility model, carbon containing matter enters upper stove 1 from charging aperture 5, by resistance heater 7 heating inner liner 4, and control temperature reaches between 500-600 degree, carbon containing matter heat drying is made it charing, the mist produced then is discharged by exhaust outlet 6, carbonization reaction terminates rear moving slide board 9 makes carbide fall into lower stove 2, add high-temperature steam carry out the activation of carbide thus obtain finished product, finished product is collected via conical discharge port 12, inner bag 4 adopts ceramic material to make, corrosion-and high-temp-resistant, increase the service life, temperature sensor 15 and the convenient temperature observed and control inner bag 4 and heat of controller 16, electric-air valve 14 can control steam inlet and admission velocity, recover 13 can recycling carbonization reaction produce mist and avoid environmental pollution, it is simple that this kind of all-in-one oven has structure, reasonable in design, easy to use, the advantage of economic environmental protection.
As known by the technical knowledge, the utility model can be realized by other the embodiment not departing from its Spirit Essence or essential feature.Therefore, above-mentioned disclosed embodiment, with regard to each side, all just illustrates, is not only.All within the scope of the utility model or be equal to the change in scope of the present utility model all comprise by the utility model.
Claims (5)
1. petrochemical industry activation integral furnace, it is characterized in that: comprise reacting furnace, described reacting furnace comprises stove and lower stove, is provided with chute between described upper stove and lower stove, and described chute place is provided with slide plate, upper stove comprises furnace shell and inner bag, be provided with resistance heater between described furnace shell and inner bag, upper furnace roof portion is provided with charging aperture and exhaust outlet, and described lower stove bottom is provided with steam inlet, lower stove top is provided with steam (vapor) outlet, and bottom is provided with conical discharge port.
2. petrochemical industry activation integral furnace according to claim 1, is characterized in that: described inner bag adopts ceramic material to make.
3. petrochemical industry activation integral furnace according to claim 1, it is characterized in that: be provided with temperature sensor in described inner bag, described furnace shell is provided with controller, and described temperature sensor is electrically connected with controller, and described controller is electrically connected with resistance heater.
4. petrochemical industry activation integral furnace according to claim 1, is characterized in that: described steam inlet place is provided with electric-air valve.
5. petrochemical industry activation integral furnace according to claim 1, is characterized in that: described exhaust outlet is connected with recover.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520729651.4U CN205020091U (en) | 2015-09-18 | 2015-09-18 | Integrative stove of petrochemical industry activation |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520729651.4U CN205020091U (en) | 2015-09-18 | 2015-09-18 | Integrative stove of petrochemical industry activation |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205020091U true CN205020091U (en) | 2016-02-10 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520729651.4U Expired - Fee Related CN205020091U (en) | 2015-09-18 | 2015-09-18 | Integrative stove of petrochemical industry activation |
Country Status (1)
| Country | Link |
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| CN (1) | CN205020091U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105126759A (en) * | 2015-09-18 | 2015-12-09 | 泰州市天平化工有限公司 | Petrifaction and activation integrated furnace |
-
2015
- 2015-09-18 CN CN201520729651.4U patent/CN205020091U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105126759A (en) * | 2015-09-18 | 2015-12-09 | 泰州市天平化工有限公司 | Petrifaction and activation integrated furnace |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20160210 Termination date: 20160918 |