CN202440010U - Storage tank for volatile liquid materials - Google Patents
Storage tank for volatile liquid materials Download PDFInfo
- Publication number
- CN202440010U CN202440010U CN201220028111XU CN201220028111U CN202440010U CN 202440010 U CN202440010 U CN 202440010U CN 201220028111X U CN201220028111X U CN 201220028111XU CN 201220028111 U CN201220028111 U CN 201220028111U CN 202440010 U CN202440010 U CN 202440010U
- Authority
- CN
- China
- Prior art keywords
- condenser
- waste gas
- storage tank
- volatile liquid
- liquid material
- Prior art date
- 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 - Fee Related
Links
- 239000011344 liquid material Substances 0.000 title claims abstract description 35
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 31
- 239000000463 material Substances 0.000 claims abstract description 11
- 239000000498 cooling water Substances 0.000 claims abstract description 7
- 239000012530 fluid Substances 0.000 claims abstract description 6
- 239000002912 waste gas Substances 0.000 claims description 42
- 239000007789 gas Substances 0.000 claims description 18
- 230000029058 respiratory gaseous exchange Effects 0.000 claims description 12
- 230000005494 condensation Effects 0.000 claims description 10
- 238000009833 condensation Methods 0.000 claims description 10
- 239000010865 sewage Substances 0.000 claims description 4
- 238000004891 communication Methods 0.000 claims description 3
- 230000008676 import Effects 0.000 claims description 3
- 238000007599 discharging Methods 0.000 description 5
- 238000001704 evaporation Methods 0.000 description 4
- 230000008020 evaporation Effects 0.000 description 4
- 230000009286 beneficial effect Effects 0.000 description 2
- 239000013064 chemical raw material Substances 0.000 description 2
- 238000013461 design Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000012545 processing Methods 0.000 description 2
- 230000007306 turnover Effects 0.000 description 2
- 238000010521 absorption reaction Methods 0.000 description 1
- -1 for example Substances 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 230000004630 mental health Effects 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- 231100000004 severe toxicity Toxicity 0.000 description 1
- 230000003068 static effect Effects 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Images
Landscapes
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The utility model relates to a storage tank for volatile liquid materials, comprising a tank body and a condenser, wherein the tank body contains volatile liquid materials, and comprises a lower cylindrical part and an upper dome part; a circular opening is formed in the vicinity of the central position of the dome part; the condenser is in a cylindrical shape and parallel condenser pipes communicated with fluid are arranged in the condenser; cooling water enters the condenser pipe from a condensate water inlet of the condenser pipe, flows through the parallel condenser pipes and then flows out of the condenser pipe from a condensate water outlet of the condenser pipe; and the condenser further comprises a gas flow cavity through which gas passes from bottom to top; the condenser is arranged on the circular opening at the dome part of the tank body; the lower port of the gas flow cavity of the condenser corresponds to the circular opening of the tank body; and the condensate water of the condenser pipes is used for condensing gas materials volatilized into the condenser so that the gas materials are liquefied and then drip to return to the liquid materials.
Description
Technical field
The utility model relates to storage tank, particularly, relates to the storage tank of volatile liquid material.
Background technology
The storage tank of volatile liquid material, for example, oil tank, fluid chemical raw material storage tank etc. mostly adopt the pressure of maintenance jars such as breathing method, deadweight safety valve to be in reasonable levels, and adopt in addition safety guard-safeguard such as static ground wire and discharging rod.In higher season, material temperature also can raise along with the rising of ambient temperature in ambient temperature.Therefore, the volatile liquid material has quickened evaporation rate when temperature build-up, and a large amount of volatilization gas is disposed in the environment through breathing valve and safety valve, contaminated environment.For some the material of severe toxicity is arranged, its volatile matter in addition can threaten near living quarters resident's physical and mental health.
Fig. 1 is the scheme drawing of the oil product storage tank of prior art.
As shown in Figure 1, the oil product storage tank of prior art comprises and is used to store the jar body 1 of oil product and is arranged on the breathing valve 2 and safety valve 3 on jar bodies top.When ambient temperature raise, the temperature of the oil product 4 that holds in jar body 1 increased, thereby quickened volatilization.When the pressure in the jar body 1 reached the plus or minus predetermined value, breathing valve 2 was opened, the pressure in the balance tank body 1.When the pressure in the jar body 1 reaches the malleation predetermined value, the volatile matter gas in the jar body 1 is discharged in the atmosphere through breathing valve 2.In case breathing valve 2 is malfunctioning, the pressure in jar body 1 possibly further raise, and when this pressure reached the threshold value of safety valve 3, safety valve 3 was opened, with the volatile matter gaseous emission in the jar body 1 in atmosphere.Although reduced the pressure in jar body 1 through the discharging volatile matter, guaranteed the safety of oil product storage tank, the volatile matter gas that is discharged in the atmosphere pollutes the environment, and causes for example a large amount of wastes of the material of oil product simultaneously.
The utility model content
The technical matters that the utility model will solve provides the material storage tank that can reduce the volatile matter discharging and volatile matter is reclaimed and handles.
In order to solve the problems of the technologies described above, the utility model provides volatile liquid material storage tank.This volatile liquid material storage tank comprises: tank body, and the highly volatile liquid material of its stored comprises the cylindrical portions may of bottom and the dome portion on top, is provided with circular open near the center of said dome portion; Condenser is drum, comprises the cold finger arranged side by side of fluid communication in it; Cooling water expansion tank gets into from the condensed water import of cold finger; The cold finger arranged side by side of flowing through flows out from the condensation-water drain of condenser, and comprises the supplied gas air flow chamber through therebetween from bottom to top.Said condenser is arranged on the circular open of dome portion of said tank body; The lower port of the air flow chamber of said condenser is corresponding to the circular open of said tank body; Condensed water condensation through cold finger evaporate into the gas material in the said condenser, make its liquefaction after drip to turn back in the liquid material.
In a technical scheme of the utility model; The air flow chamber of said condenser also comprises port; This port connects in the earthing through pipeline gas with the waste gas tourie mutually, will not have the waste gas of condensation to be transported in the water that puts in the said waste gas tourie through this pipeline.
In a technical scheme of the utility model, said waste gas tourie also comprises and the terminal bonded assembly waste gas of said pipeline sparger, waste gas is evenly distributed in the water that puts in the said waste gas tourie.
In a technical scheme of the utility model, said waste gas tourie also comprises introduces the pipeline that sewage plant is handled with the water that wherein puts after absorbing waste gas.
In a technical scheme of the utility model, said waste gas tourie also comprises setting prerotator and connected pipeline at an upper portion thereof, introduces incinerator with the waste gas that will do not absorbed by water and burns.
In a technical scheme of the utility model, be provided with valve between the port of said condenser and the pipeline and switch with switch in working order and between the halted state.
In a technical scheme of the utility model, the dome portion of said tank body is provided with breathing valve, with the pressure in the balancing tank.
In a technical scheme of the utility model, the dome portion of said tank body is provided with safety valve, reduces the pressure in the storage tank under set pressure, to open.
The beneficial effect that the volatile liquid material storage tank of the utility model can be realized reducing the volatile matter discharging and volatile matter is reclaimed and handles.
Description of drawings
Fig. 1 is the scheme drawing of the oil product storage tank of prior art.
Fig. 2 is the scheme drawing of the volatile liquid material storage tank of the utility model.
The specific embodiment
Fig. 2 is the scheme drawing of the volatile liquid material storage tank of the utility model.
As shown in Figure 2, the volatile liquid material storage tank 100 of the utility model comprises tank body 10 and condenser 20.
The amount of capacity of condenser 20 can suitably be selected according to the kind of the volume of tank body 10 and the volatile liquid material that is held etc.Condenser 20 also can be the condenser of any other type, as long as the gas that evaporate in it is had condensation effect preferably.Condenser 20 preferably is located near the center of dome portion 12, because be the vertex of tank body 10 here, the gas material of volatilization rises to here with comparalive ease.Certainly, according to the architectural feature of tank body 10 or the needs of other device are set, also can be with condenser 20 Position Design other position in the tank top is set.
The evaporation rate and the ambient temperature of volatile liquid material 30 are closely related, and when ambient temperature raise, evaporation rate raise; When ambient temperature descended, evaporation rate also descended.Therefore, the condenser 20 of the volatile liquid material storage tank 100 of the utility model can be opened in ambient temperature higher season, and closes lower season in ambient temperature.For example, open at the high temperature season in spring, summer and autumn, and the low temperature season in winter is closed.
In an embodiment of the utility model; The air flow chamber of condenser 20 also can comprise port 24; This port 24 connects in the earthing through pipeline 50 gases with waste gas tourie 40 mutually, will not have the waste gas of condensation to be transported in the water 41 that puts in the waste gas tourie 40 through this pipeline 50.Feeding waste gas in the water 41 will be partly water-soluble 41 and absorbed by water 41.The waste gas that is not absorbed by water 41 will rise to more than the water surface.Therefore, the liquids and gases in the waste gas tourie 40 all will regularly be done further processing.
In an embodiment of the utility model, waste gas tourie 40 also can comprise and pipeline 50 terminal bonded assembly waste gas spargers 52, waste gas is evenly distributed in the water that waste gas tourie 40 puts.Because waste gas is evenly distributed in the water that waste gas tourie 40 puts, so increase the assimilation effect that waste gas sparger 52 can improve 41 pairs of waste gas of water.
In an embodiment of the utility model, waste gas tourie 40 also can comprise introduces the pipeline 42 that sewage plant is handled with the water that wherein puts 41 after absorbing waste gas.Sewage plant can be done further processing with the water of introducing 41, in order to avoid contaminated environment.
In an embodiment of the utility model, waste gas tourie 40 also can comprise setting prerotator 43 and connected pipeline 44 at an upper portion thereof, introduces incinerator with the waste gas that will do not absorbed by water 41 and burns.Incineration process through to waste gas can further reduce the pollution to environment.
In an embodiment of the utility model, can be provided with valve 51 between the port 24 of condenser 20 and the pipeline 50, switch with switch in working order and between the halted state.The turnover valve of the cooling water expansion tank through closing this valve 51 and condenser 20 can be realized closing of condenser 20.On the contrary, the turnover valve of the cooling water expansion tank through opening this valve 51 and condenser 20 can be realized the unlatching of condenser 20.In addition, even valve 51 is closed, still keep under the on-cycle situation at cooling water expansion tank, condenser 20 also can be through the gas material of its condensation and condensation volatilization, makes it become liquid and drips recovery.
In an embodiment of the utility model, can be provided with breathing valve 14 on the dome portion 12 of tank body 10.When the pressure in the volatile liquid material storage tank 100 raise, breathing valve 14 was discharged gas to the outside; When the pressure decay in the volatile liquid material storage tank 100, breathing valve 14 is make-up gas in volatile liquid material storage tank 100 from the outside.Therefore, but breathing valve 14 balancing tanks in pressure.
In an embodiment of the utility model, can be provided with safety valve 15 on the dome portion 12 of tank body 10, reduce the pressure in the storage tank under set pressure, to open.
The absorption of condensation and the waste gas tourie 40 of the volatile liquid material storage tank 100 of the utility model through condenser 20 can realize the beneficial effect that reduces the volatile matter discharging and volatile matter is reclaimed and handles.
Those skilled in the art should be understood that, according to design demand and other factors, can carry out various modifications, combination, part combination and replacement.Such modification, combination, part combine and replacement falls within the scope of accompanying claims or its equivalent.
Claims (8)
1. the storage tank of a volatile liquid material is characterized in that, comprising:
Tank body, the highly volatile liquid material of its stored comprises the cylindrical portions may of bottom and the dome portion on top, is provided with circular open near the center of said dome portion;
Condenser is drum, comprises the cold finger arranged side by side of fluid communication in it; Cooling water expansion tank gets into from the condensed water import of cold finger; The cold finger arranged side by side of flowing through flows out from the condensation-water drain of condenser, and comprises the supplied gas air flow chamber through therebetween from bottom to top;
Wherein said condenser is arranged on the circular open of dome portion of said tank body; The lower port of the air flow chamber of said condenser is corresponding to the circular open of said tank body; Condensed water condensation through cold finger evaporate into the gas material in the said condenser, make its liquefaction after drip to turn back in the liquid material.
2. the storage tank of volatile liquid material as claimed in claim 1; It is characterized in that; The air flow chamber of said condenser also comprises port; This port connects in the earthing through pipeline gas with the waste gas tourie mutually, will not have the waste gas of condensation to be transported in the water that puts in the said waste gas tourie through this pipeline.
3. the storage tank of volatile liquid material as claimed in claim 2 is characterized in that, said waste gas tourie also comprises and the terminal bonded assembly waste gas of said pipeline sparger, waste gas is evenly distributed in the water that puts in the said waste gas tourie.
4. like the storage tank of claim 2 or 3 described volatile liquid materials, it is characterized in that said waste gas tourie also comprises introduces the pipeline that sewage plant is handled with the water that wherein puts after absorbing waste gas.
5. like the storage tank of claim 2 or 3 described volatile liquid materials, it is characterized in that said waste gas tourie also comprises setting prerotator and connected pipeline at an upper portion thereof, introduce incinerator with the waste gas that will do not absorbed and burn by water.
6. like the storage tank of claim 2 or 3 described volatile liquid materials, it is characterized in that, be provided with valve between the port of said condenser and the pipeline and switch with switch in working order and between the halted state.
7. the storage tank of volatile liquid material as claimed in claim 1 is characterized in that, the dome portion of said tank body is provided with breathing valve, with the pressure in the balancing tank.
8. the storage tank of volatile liquid material as claimed in claim 1 is characterized in that, the dome portion of said tank body is provided with safety valve, reduces the pressure in the storage tank under set pressure, to open.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201220028111XU CN202440010U (en) | 2012-01-21 | 2012-01-21 | Storage tank for volatile liquid materials |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201220028111XU CN202440010U (en) | 2012-01-21 | 2012-01-21 | Storage tank for volatile liquid materials |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202440010U true CN202440010U (en) | 2012-09-19 |
Family
ID=46821464
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201220028111XU Expired - Fee Related CN202440010U (en) | 2012-01-21 | 2012-01-21 | Storage tank for volatile liquid materials |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202440010U (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103010618A (en) * | 2012-12-11 | 2013-04-03 | 广西金桂浆纸业有限公司 | Exhaust device of volatile liquid storage tank |
| CN104773412A (en) * | 2015-02-13 | 2015-07-15 | 江苏新美星包装机械股份有限公司 | Method for preventing gas of chemicals in liquid storage container from dissipating |
| CN105059760A (en) * | 2015-08-07 | 2015-11-18 | 无锡市悦丰化工有限公司 | Novel methylacrylic acid formaldehyde solvent furnace |
| CN110564441A (en) * | 2018-06-06 | 2019-12-13 | 中国石油化工股份有限公司 | Safe recovery system and recovery process for VOCs in styrene storage tank |
| CN111792177A (en) * | 2020-07-09 | 2020-10-20 | 重庆医药高等专科学校 | A kind of ethanol dangerous goods storage device |
-
2012
- 2012-01-21 CN CN201220028111XU patent/CN202440010U/en not_active Expired - Fee Related
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103010618A (en) * | 2012-12-11 | 2013-04-03 | 广西金桂浆纸业有限公司 | Exhaust device of volatile liquid storage tank |
| CN104773412A (en) * | 2015-02-13 | 2015-07-15 | 江苏新美星包装机械股份有限公司 | Method for preventing gas of chemicals in liquid storage container from dissipating |
| CN105059760A (en) * | 2015-08-07 | 2015-11-18 | 无锡市悦丰化工有限公司 | Novel methylacrylic acid formaldehyde solvent furnace |
| CN110564441A (en) * | 2018-06-06 | 2019-12-13 | 中国石油化工股份有限公司 | Safe recovery system and recovery process for VOCs in styrene storage tank |
| CN110564441B (en) * | 2018-06-06 | 2022-02-25 | 中国石油化工股份有限公司 | Safe recovery system and recovery process for VOCs in styrene storage tank |
| CN111792177A (en) * | 2020-07-09 | 2020-10-20 | 重庆医药高等专科学校 | A kind of ethanol dangerous goods storage device |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN202440010U (en) | Storage tank for volatile liquid materials | |
| CN204620626U (en) | For the prosthetic device of contaminated soil | |
| CN105032112B (en) | A kind of gas recovery system for oil of absorption-adsorption-condensation integrated technology | |
| CN105215049A (en) | Box-type complete soil underground water pollution two-phase extracting prosthetic device and application | |
| CN105056706A (en) | Methanol waste gas recycling system based on secondary absorption | |
| CN104773898A (en) | Physicochemical-artificial wetland combined process for strengthening treatment of fluorine and arsenic sewage | |
| CN101402001A (en) | Oil gas recycling and processing apparatus, condensation adsorption method thereof | |
| CN207413049U (en) | A kind of Industrial Boiler environment protection energy-saving equipment | |
| CN205435029U (en) | Automatic drain of vacuum system condenser | |
| CN204953521U (en) | Double -phase extraction prosthetic devices of box complete set soil underground water pollution | |
| CN201644098U (en) | Activated carbon deodorization device | |
| CN1468943A (en) | City domestic garbage treating apparatus and method | |
| CN207024997U (en) | Storage Tank gas recovery system for oil | |
| CN202485339U (en) | Energy-saving vacuum flashing type independent dehumidification system | |
| CN202036558U (en) | Steam sterilization device for loose poria engineering bacterium bag | |
| CN206156995U (en) | Good oxygen mummification device of city domestic sewage excess sludge | |
| CN212757643U (en) | Waste gas treatment device used in kitchen waste biochemical treatment equipment | |
| CN206916026U (en) | A kind of fruit/vegetable waste composting device using secondary waste thing energy-saving heat preserving | |
| CN103131492A (en) | Device and method for condensing and separating water in methane | |
| CN208594294U (en) | Biofermentation steam tail gas heat energy recycling system | |
| CN219879490U (en) | Oil gas recovery device of glass oil tank | |
| CN201458084U (en) | Volatile liquid storage tank | |
| CN204026808U (en) | Energy-saving environmental-protection boiler heating static pressure modernization system | |
| CN203763889U (en) | Triethylene glycol furnace exhaust condenser | |
| CN203612982U (en) | Freezing separation device suitable for refuse landfill leachate |
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 |
Granted publication date: 20120919 Termination date: 20190121 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |