CN204208567U - A kind of petrochemical industry reactor - Google Patents
A kind of petrochemical industry reactor Download PDFInfo
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- CN204208567U CN204208567U CN201420490588.9U CN201420490588U CN204208567U CN 204208567 U CN204208567 U CN 204208567U CN 201420490588 U CN201420490588 U CN 201420490588U CN 204208567 U CN204208567 U CN 204208567U
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- tank body
- helical blade
- lifting device
- steam discharge
- discharge pipe
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Abstract
The utility model discloses a kind of petrochemical industry reactor, comprise tank body, described tank interior is provided with lifting device, lifting device is made up of enhancing tube and helical blade, helical blade connects on the rotary shaft, and helical blade is arranged in enhancing tube, motor (11) is in transmission connection rotating shaft, and the outside of described tank body is provided with heater; The top of described tank body is connected with charge door and steam discharge pipe, described steam discharge pipe is connected to one end of U-shaped pipe, the other end of U-shaped pipe connects the input port of adsorbent bed by pipeline, the minimum point of described U-shaped pipe connects waste collection bottle, and steam discharge pipe periphery arranges condenser; The output of described adsorbent bed connects sterilizing chamber by pipeline, arranges actinolyte and ozone generator in described sterilizing chamber.Lifting device is set in tank body, is realized the circulation stirring daring to carry interior thick liquid by lifting device and inner helical blade, add fast response.
Description
Technical field
The utility model relates to a kind of reactor, specifically a kind of petrochemical industry reactor.
Background technology
The various organic compound from waste gas such as hydrocarbon, alcohol, aldehyde, ketone, ether, ester, amine carboxylic acid, aromatic hydrocarbon, phenols in the waste gas that the industries such as petrochemical industry are discharged, harmful, the common symptoms caused is fatigue and weak, dizziness headache, n and V, nervous asthma, blood change etc.The material such as aldehyde, amine also foul smelling.Organic exhaust gas can also cause photochemical fog, causes secondary pollution.The purifying treatment method of current organic exhaust gas mainly contains absorption method: utilize the surface force of adsorbent organic exhaust gas adsorption at adsorbent surface, to purify the waste gas of discharging in production process.The molecular weight of waste gas is larger, and boiling point is higher, and concentration is higher, and temperature is lower, then the adsorption capacity of adsorbent is larger, and adsorption cycle is longer.Absorption method is applicable to the purification of low-concentration organic exhaust gas, also can be used for high-concentration organic waste gas and reclaims.Conventional adsorbent has active carbon, silica gel, ion exchange resin etc.But cost is higher, application is less at present.Burning facture-organic exhaust gas, under the effect of temperature 200 ~ 400 DEG C with catalyst, is oxidized to carbon dioxide packing and water, releases the combustion heat simultaneously.Production by Catalytic Combustion Process is mainly used in the purification of organic exhaust gas of high temperature, high concentration, continuous blow-down, and under temperature is 600 ~ 800 DEG C and the holdup time is the condition of 0.3 ~ 0.5 second, organic gas can burn completely, becomes carbon dioxide packing and water.Direct combustion method is applicable to the organic waste-gas purification of high temperature, high concentration, and heat-recoverable.It is more that direct combustion method consumes the energy, should adopt heavy oil, natural gas makes pre-heat energy.During preheating, burning indoor temperature should be homogeneous, makes whole waste gas all be heated to predetermined temperature, otherwise can produce cacodorous intermediate product.If any the boiler of air volumematching, waste gas can be burnt in the boiler as air inducing.Absorption process: the method absorbing high-concentration organic waste gas with absorbing liquid.Absorbing liquid can simultaneous oxidation, neutralization part foul gas.Usual absorption process, as the pretreatment of organic exhaust gas, as dedusting, oil mist removing, except water soluble ingredient etc., and then to purify with additive method further.But general petrochemical enterprise, due to its exhaust gas constituents complexity, is difficult to it to purify completely by a kind of method, causes in the tail gas of discharge and also contain gas harmful in a large number, have a strong impact on the healthy of nearby residents.
Utility model content
The purpose of this utility model is to provide a kind of petrochemical industry reactor, to solve the problem proposed in above-mentioned background technology.
For achieving the above object, the utility model provides following technical scheme:
A kind of petrochemical industry reactor, comprise sterilizing chamber, adsorbent bed, U-shaped pipe, condenser, steam discharge pipe, charge door, tank body, heater, lifting device, helical blade, motor, discharging opening, waste collection bottle, actinolyte and ozone generator, described tank interior is provided with lifting device, lifting device is made up of enhancing tube and helical blade, helical blade connects on the rotary shaft, and helical blade is arranged in enhancing tube, motor 11 is in transmission connection rotating shaft, and the outside of described tank body is provided with heater; The top of described tank body is connected with charge door and steam discharge pipe, described steam discharge pipe is connected to one end of U-shaped pipe, the other end of U-shaped pipe connects the input port of adsorbent bed by pipeline, the minimum point of described U-shaped pipe connects waste collection bottle, and steam discharge pipe periphery arranges condenser; The output of described adsorbent bed connects sterilizing chamber by pipeline, arranges actinolyte and ozone generator in described sterilizing chamber.
As further program of the utility model: the bottom of described tank body is provided with discharging opening.
As the utility model further scheme: fill active carbon in described adsorbent bed.
Compared with prior art, the beneficial effects of the utility model are: in tank body, arrange lifting device, the circulation stirring daring to carry interior thick liquid is realized by lifting device and inner helical blade, add fast response, and steam discharge pipe is set at tank body prevents the excessive device damage caused of internal pressure, steam discharge pipe connects U-shaped pipe outward successively simultaneously, adsorbent bed and sterilizing chamber, the organic compounds produced in petrochemical industry being produced thoroughly processes, avoid exhaust emission air and cause air peculiar smell, at the leading portion of U-shaped pipe, condenser is set, effectively devil liquor recovery is entered waste collection bottle, prevent waste reflux from causing reactant contaminated, avoid waste liquid equally and flow into adsorbent bed with steam, pollute inner active carbon, make the life of equipment of this use more lasting, and improve follow-up exhaust treatment efficiency.This practicality adopts ultraviolet beam irradiation to carry out cracking, adopt ozone simultaneously, ozone is polymerized with in free state polluter atom, generate new, harmless or low harmful substances, as CO2, H2O etc., Pre-Ozonation on Organic Matter has extremely strong oxidation simultaneously, has to foul gas and other excitant peculiar smell the elimination effect got instant result, and finally reaches the object of thoroughly purification.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model.
Detailed description of the invention
Below in conjunction with the accompanying drawing in the utility model embodiment, be clearly and completely described the technical scheme in the utility model embodiment, obviously, described embodiment is only the utility model part embodiment, instead of whole embodiments.Based on the embodiment in the utility model, those of ordinary skill in the art are not making the every other embodiment obtained under creative work prerequisite, all belong to the scope of the utility model protection.
Refer to Fig. 1, in the utility model embodiment, a kind of petrochemical industry reactor, comprise sterilizing chamber 1, adsorbent bed 2, U-shaped pipe 3, condenser 4, steam discharge pipe 5, charge door 6, tank body 7, heater 8, lifting device 9, helical blade 10, motor 11, discharging opening 12, waste collection bottle 13, actinolyte 14 and ozone generator 15, described tank body 7 inside is provided with lifting device 9, lifting device 9 is made up of enhancing tube and helical blade 10, helical blade 10 connects on the rotary shaft, and, helical blade 10 is arranged in enhancing tube, to be in transmission connection rotating shaft by motor 11, make helical blade 10 that the reactant of thickness bottom tank body 7 is promoted to the top of tank body 7, in lifting process, helical blade 10 pairs of reactants stir, thus realize the overall circulation stirring of reactant in tank body 7, the outside of described tank body 7 is provided with heater 8, heater 8 pairs of reactants carry out temperature control, promote internal-response, the bottom of described tank body 7 is provided with discharging opening 12,
The top of described tank body 7 is connected with charge door 6 and steam discharge pipe 5, added materials by charge door 6, steam discharge pipe 5 discharges the gas of inner volatilization, prevent pressure excessive, the phenomenon of fried tank, described steam discharge pipe 5 is connected to one end of U-shaped pipe 3, the other end of U-shaped pipe 3 connects the input port of adsorbent bed 2 by pipeline, the minimum point of described U-shaped pipe 3 connects waste collection bottle 13, by arranging condenser 4 in steam discharge pipe 5 periphery, by the gas fraction condensation volatilized in reactant, then flow in waste collection bottle 13 and focus on;
The output of described adsorbent bed 2 connects sterilizing chamber 1 by pipeline, active carbon is filled in described adsorbent bed 2, actinolyte 14 and ozone generator 15 are set in described sterilizing chamber 1, waste gas makes macromolecular substances in gas be absorbed by the process of adsorbent bed 2, processing cost reduces greatly, also have a small amount of remaining organic compound to adopt ultraviolet beam to irradiate after adsorption treatment and carry out cracking, adopt ozone simultaneously, ozone is polymerized with in free state polluter atom, generate new, harmless or low harmful substances, as CO2, H2O etc., Pre-Ozonation on Organic Matter has extremely strong oxidation simultaneously, the elimination effect got instant result is had to foul gas and other excitant peculiar smell, finally reach the object of thoroughly purification.
Operation principle of the present utility model is: in tank body 7, arrange lifting device 9, the circulation stirring daring to carry interior thick liquid is realized by lifting device 9 and inner helical blade 10, add fast response, and steam discharge pipe 5 is set at tank body 7 prevents the excessive device damage caused of internal pressure, steam discharge pipe 5 is outer simultaneously connects U-shaped pipe 3 successively, adsorbent bed 2 and sterilizing chamber 1, the organic compounds produced in petrochemical industry being produced thoroughly processes, avoid exhaust emission air and cause air peculiar smell, at the leading portion of U-shaped pipe 3, condenser 4 is set, effectively devil liquor recovery is entered waste collection bottle 13, prevent waste reflux from causing reactant contaminated, avoid waste liquid equally and flow into adsorbent bed 2 with steam, pollute inner active carbon, make the life of equipment of this use more lasting, and improve follow-up exhaust treatment efficiency.
To those skilled in the art, obvious the utility model is not limited to the details of above-mentioned one exemplary embodiment, and when not deviating from spirit of the present utility model or essential characteristic, can realize the utility model in other specific forms.Therefore, no matter from which point, all should embodiment be regarded as exemplary, and be nonrestrictive, scope of the present utility model is limited by claims instead of above-mentioned explanation, and all changes be therefore intended in the implication of the equivalency by dropping on claim and scope are included in the utility model.Any Reference numeral in claim should be considered as the claim involved by limiting.
In addition, be to be understood that, although this description is described according to embodiment, but not each embodiment only comprises an independently technical scheme, this narrating mode of description is only for clarity sake, those skilled in the art should by description integrally, and the technical scheme in each embodiment also through appropriately combined, can form other embodiments that it will be appreciated by those skilled in the art that.
Claims (3)
1. a petrochemical industry reactor, comprise sterilizing chamber, adsorbent bed, U-shaped pipe, condenser, steam discharge pipe, charge door, tank body, heater, lifting device, helical blade, motor, discharging opening, waste collection bottle, actinolyte and ozone generator, it is characterized in that, described tank interior is provided with lifting device, lifting device is made up of enhancing tube and helical blade, helical blade connects on the rotary shaft, and helical blade is arranged in enhancing tube, motor (11) is in transmission connection rotating shaft, and the outside of described tank body is provided with heater; The top of described tank body is connected with charge door and steam discharge pipe, described steam discharge pipe is connected to one end of U-shaped pipe, the other end of U-shaped pipe connects the input port of adsorbent bed by pipeline, the minimum point of described U-shaped pipe connects waste collection bottle, and steam discharge pipe periphery arranges condenser; The output of described adsorbent bed connects sterilizing chamber by pipeline, arranges actinolyte and ozone generator in described sterilizing chamber.
2. a kind of petrochemical industry reactor according to claim 1, it is characterized in that, the bottom of described tank body is provided with discharging opening.
3. a kind of petrochemical industry reactor according to claim 1, is characterized in that, fills active carbon in described adsorbent bed.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420490588.9U CN204208567U (en) | 2014-08-28 | 2014-08-28 | A kind of petrochemical industry reactor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420490588.9U CN204208567U (en) | 2014-08-28 | 2014-08-28 | A kind of petrochemical industry reactor |
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| Publication Number | Publication Date |
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| CN204208567U true CN204208567U (en) | 2015-03-18 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201420490588.9U Expired - Fee Related CN204208567U (en) | 2014-08-28 | 2014-08-28 | A kind of petrochemical industry reactor |
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| CN (1) | CN204208567U (en) |
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104874203A (en) * | 2015-05-28 | 2015-09-02 | 长春黄金研究院 | Zeolite dynamic adsorption column |
| CN104984677A (en) * | 2015-07-24 | 2015-10-21 | 苏州硅果电子有限公司 | Viscous liquid material mixing and stirring device |
| CN107474889A (en) * | 2017-09-26 | 2017-12-15 | 龚梁涛 | A kind of natural gas extraction equipment selexol process equipment |
| CN107756621A (en) * | 2017-10-26 | 2018-03-06 | 龙影 | A kind of refractory material preparation EGR |
| CN108246218A (en) * | 2018-03-21 | 2018-07-06 | 成都勇进电子科技有限公司 | The mechanized production system and production technology of petrochemicals |
| CN109331746A (en) * | 2018-09-28 | 2019-02-15 | 大连理工大学 | A kind of novel solid particle thermal chemical reaction device and method |
| CN109569372A (en) * | 2018-12-28 | 2019-04-05 | 宁夏红山河食品股份有限公司 | A kind of compound fragrant material mixing and blending machine and stirring means |
| CN112316882A (en) * | 2021-01-05 | 2021-02-05 | 蓬莱禄昊化工机械有限公司 | Medicine reation kettle with sampling detects function |
-
2014
- 2014-08-28 CN CN201420490588.9U patent/CN204208567U/en not_active Expired - Fee Related
Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104874203A (en) * | 2015-05-28 | 2015-09-02 | 长春黄金研究院 | Zeolite dynamic adsorption column |
| CN104984677A (en) * | 2015-07-24 | 2015-10-21 | 苏州硅果电子有限公司 | Viscous liquid material mixing and stirring device |
| CN107474889A (en) * | 2017-09-26 | 2017-12-15 | 龚梁涛 | A kind of natural gas extraction equipment selexol process equipment |
| CN107756621A (en) * | 2017-10-26 | 2018-03-06 | 龙影 | A kind of refractory material preparation EGR |
| CN107756621B (en) * | 2017-10-26 | 2019-06-25 | 唐山市蓝奥耐火材料有限公司 | Circulator is used in a kind of preparation of refractory material |
| CN108246218A (en) * | 2018-03-21 | 2018-07-06 | 成都勇进电子科技有限公司 | The mechanized production system and production technology of petrochemicals |
| CN109331746A (en) * | 2018-09-28 | 2019-02-15 | 大连理工大学 | A kind of novel solid particle thermal chemical reaction device and method |
| CN109331746B (en) * | 2018-09-28 | 2021-11-19 | 大连理工大学 | Novel solid particle thermochemical reaction device and method |
| CN109569372A (en) * | 2018-12-28 | 2019-04-05 | 宁夏红山河食品股份有限公司 | A kind of compound fragrant material mixing and blending machine and stirring means |
| CN112316882A (en) * | 2021-01-05 | 2021-02-05 | 蓬莱禄昊化工机械有限公司 | Medicine reation kettle with sampling detects function |
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Addressee: HANGZHOU XIEHONG TECHNOLOGY CONSULTING CO., LTD. Document name: Notification to Go Through Formalities of Registration |
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| 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: 20150318 Termination date: 20170828 |