CN109945214A - A kind of storage tank volatilization gas processing system - Google Patents
A kind of storage tank volatilization gas processing system Download PDFInfo
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- CN109945214A CN109945214A CN201910271479.5A CN201910271479A CN109945214A CN 109945214 A CN109945214 A CN 109945214A CN 201910271479 A CN201910271479 A CN 201910271479A CN 109945214 A CN109945214 A CN 109945214A
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- storage tank
- blower
- combustion apparatus
- processing system
- volatile gas
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- 238000002485 combustion reaction Methods 0.000 claims abstract description 60
- 238000002844 melting Methods 0.000 claims description 11
- 230000008018 melting Effects 0.000 claims description 11
- 239000000463 material Substances 0.000 abstract description 14
- 238000004064 recycling Methods 0.000 abstract description 3
- 239000007789 gas Substances 0.000 description 90
- 239000003921 oil Substances 0.000 description 9
- 238000000034 method Methods 0.000 description 6
- 239000011521 glass Substances 0.000 description 5
- 239000007788 liquid Substances 0.000 description 5
- 238000010521 absorption reaction Methods 0.000 description 4
- 230000008901 benefit Effects 0.000 description 3
- 238000001514 detection method Methods 0.000 description 3
- 238000010586 diagram Methods 0.000 description 3
- 239000012530 fluid Substances 0.000 description 3
- 238000010438 heat treatment Methods 0.000 description 3
- 230000004048 modification Effects 0.000 description 3
- 238000012986 modification Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 239000000446 fuel Substances 0.000 description 2
- 239000000295 fuel oil Substances 0.000 description 2
- 231100000331 toxic Toxicity 0.000 description 2
- 230000002588 toxic effect Effects 0.000 description 2
- 206010008190 Cerebrovascular accident Diseases 0.000 description 1
- 208000006011 Stroke Diseases 0.000 description 1
- 238000009825 accumulation Methods 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 239000004568 cement Substances 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000004880 explosion Methods 0.000 description 1
- 230000003116 impacting effect Effects 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 230000000505 pernicious effect Effects 0.000 description 1
- 238000012797 qualification Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
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Abstract
The present invention provides a kind of storage tank volatilization gas processing system, including the storage tank with Volatile Gas discharge outlet, the storage tank volatilization gas processing system further includes the combustion apparatus being connected with Volatile Gas discharge outlet, the air intake being arranged on the storage tank and the blower that the Volatile Gas in storage tank can be driven to flow to combustion apparatus.The working principle of storage tank volatilization gas processing system in the present invention are as follows: blower generates positive pressure at air intake or generates negative pressure at Volatile Gas discharge outlet, to drive the Volatile Gas in storage tank to flow to combustion apparatus, meanwhile outside air is flowed into storage tank by air intake；Volatile Gas flows into combustion apparatus；Combustible material burns in combustion apparatus in Volatile Gas, to realize the removing and recycling to combustible material in Volatile Gas, avoids the combustible material in Volatile Gas from being directly discharged to atmosphere, and pollute to the environment on storage tank periphery.
Description
Technical field
The present invention relates to a kind of volatilization gas processing systems, more particularly to a kind of storage tank volatilization gas processing system.
Background technique
The storage needs of heavy oil are heated in oil tank, and the temperature of heating easily makes the moisture in oil product boil, thus
It causes vapor to carry various toxic, harmful and inflammable substances in oil product to spill into atmosphere, to the air ring on oil tank periphery
Border pollutes.
In this regard, the treatment process that the prior art uses is mostly to adsorb, decompose and recycle.Wherein, absorption method is for absorption
The problems such as dosage of agent is larger, difficult there are the processing of higher cost and absorption waste material；And there are biggish safety for decomposition method
Hidden danger easily causes oil-gas accumulation, can even set off an explosion when dangerous；In addition, absorption method need complex process, while invest at
This is also larger.
It would therefore be desirable to which a kind of completely new processing system, can be effectively treated the Volatile Gas of tank discharge, to keep away
Combustible material in non-volatile gas is directly discharged to atmosphere, to impact to the environment on storage tank periphery.
Summary of the invention
In view of the foregoing deficiencies of prior art, the technical problem to be solved in the present invention is that providing a kind of storage tank volatilization
Gas processing system can be effectively treated the Volatile Gas of tank discharge, to avoid the combustible material direct emission in Volatile Gas
To atmosphere.
To achieve the above object, the present invention provides a kind of storage tank volatilization gas processing system, including with Volatile Gas discharge outlet
Storage tank, storage tank volatilization gas processing system further includes the combustion apparatus being connected with Volatile Gas discharge outlet, is arranged described
Air intake on storage tank and the blower that the Volatile Gas in storage tank can be driven to flow to combustion apparatus.
Further, the air outlet of the blower is connected with air intake.
Further, the air inlet of the blower is connected with Volatile Gas discharge outlet, the air outlet of the blower and burning
Equipment is connected.
Further, the air outlet of the blower is connected by check valve with combustion apparatus.
Further, the blower includes the first blower that air outlet is connected with air intake and air inlet and wave
The second blower that discharge outlet of getting angry is connected and air outlet is connected with combustion apparatus.
Further, the combustion apparatus is melting furnaces.
Further, the Volatile Gas discharge outlet is connected by check valve with combustion apparatus.
Further, pressure gauge is installed on the storage tank.
Further, oil plant is stored in the storage tank.
Further, the blower is centrifugal blower.
The gas processing system as described above, storage tank of the present invention volatilizees, has the advantages that
In the present invention storage tank volatilization gas processing system working principle are as follows: blower generated at air intake positive pressure or
Negative pressure is generated at Volatile Gas discharge outlet, to drive the Volatile Gas in storage tank to flow to combustion apparatus, meanwhile, outside air is by air
Entrance flows into storage tank；Volatile Gas flows into combustion apparatus；Combustible material burns in combustion apparatus in Volatile Gas, thus real
Now to the removing and recycling of combustible material in Volatile Gas, the combustible material in Volatile Gas is avoided to be directly discharged to atmosphere, and right
The environment on storage tank periphery pollutes.And the present invention generates positive pressure or in Volatile Gas discharge outlet using blower at air intake
Place generates negative pressure, to drive the Volatile Gas in storage tank smoothly to flow to combustion apparatus, not only realizes the directed flow of Volatile Gas,
And flowing velocity of the Volatile Gas to combustion apparatus is accelerated, it improves this storage tank volatilization gas processing system and the processing of Volatile Gas is imitated
Rate.
Detailed description of the invention
Fig. 1 is the structural schematic diagram of storage tank volatilization gas processing system in the first embodiment of the invention.
Fig. 2 is the structural schematic diagram of storage tank volatilization gas processing system in second of embodiment of the invention.
Fig. 3 is the structural schematic diagram of storage tank volatilization gas processing system in the third embodiment of the invention.
Component label instructions
1 storage tank
2 exhaust pipes
3 combustion apparatus
31 melting furnaces
4 blowers
41 first blowers
42 second blowers
5 check valves
6 pressure gauges
7 air inlet pipe
Specific embodiment
Embodiments of the present invention are illustrated by particular specific embodiment below, those skilled in the art can be by this explanation
Content disclosed by book is understood other advantages and efficacy of the present invention easily.
It should be clear that structure depicted in this specification attached drawing, ratio, size etc., only to cooperate specification revealed
Content is not intended to limit the invention enforceable qualifications, therefore does not have so that those skilled in the art understands and reads
Technical essential meaning, the modification of any structure, the change of proportionate relationship or the adjustment of size are not influencing institute's energy of the present invention
Under the effect of generation and the purpose that can reach, the range that disclosed technology contents can be covered should all be still fallen in
It is interior.Meanwhile cited such as "upper", "lower", "left", "right", " centre " and " one " term in this specification, it is merely convenient to
Narration is illustrated, rather than to limit the scope of the invention, relativeness is altered or modified, and is changing skill without essence
It is held in art, when being also considered as the enforceable scope of the present invention.
As shown in Figure 1 to Figure 3, the present invention provides a kind of storage tank volatilization gas processing system, including with Volatile Gas discharge outlet
Storage tank 1, the storage tank volatilization gas processing system further include the combustion apparatus 3 being connected with Volatile Gas discharge outlet, be arranged in storage tank 1
On air intake and blower 4 that the Volatile Gas in storage tank 1 can be driven to flow to combustion apparatus 3.Storage tank Volatile Gas in the present invention
The working principle of processing system are as follows: blower 4 generates positive pressure at air intake or generates negative pressure at Volatile Gas discharge outlet, with
The Volatile Gas in storage tank 1 is driven to flow to combustion apparatus 3, meanwhile, outside air is flowed into storage tank 1 by air intake；Volatile Gas
Flow into combustion apparatus 3；Combustible material burns in combustion apparatus 3 in Volatile Gas, to realize to combustibles in Volatile Gas
The removing and recycling of matter avoid the combustible material in Volatile Gas from being directly discharged to atmosphere, and cause to the environment on 1 periphery of storage tank
Pollution.And the present invention generates positive pressure using blower 4 at air intake or generates negative pressure at Volatile Gas discharge outlet, to drive
Volatile Gas in storage tank 1 is smoothly flowed to combustion apparatus 3, not only realizes the directed flow of Volatile Gas, and accelerate Volatile Gas
To the flowing velocity of combustion apparatus 3, this storage tank volatilization gas processing system is improved to the treatment effeciency of Volatile Gas.
The first embodiment
As shown in Figure 1, combustion apparatus 3 is connected by exhaust pipe 2 with Volatile Gas discharge outlet in the present embodiment.In this way, waving
Combustion apparatus 3 will be flowed by exhaust pipe 2 by getting angry.
As shown in Figure 1, the air outlet of blower 4 is connected with the air intake of storage tank 1 in the present embodiment.The present embodiment apoplexy
Machine 4 plays the role of air blower, to air pressurized be sent into storage tank 1 in, thus generated at air intake and in storage tank 1 it is micro- just
Pressure, and the Volatile Gas in storage tank 1 is driven to flow into combustion apparatus 3 by exhaust pipe 2.In addition, in the present embodiment blower 4 air outlet
It is connected by air inlet pipe 7 with air intake.
As shown in Figure 1, pressure gauge 6 is equipped in the present embodiment on storage tank 1, using in the pressure gauge 6 detection storage tank 1
Air pressure, and adjust and formed at the air outlet of blower 4 according to the air pressure in storage tank 1 convenient for staff or corresponding control system
Wind pressure.
As shown in Figure 1, exhaust pipe 2 is connected by check valve 5 with combustion apparatus 3 in the present embodiment, which can be protected
The Volatile Gas demonstrate,proved in storage tank 1 is smoothly flowed to combustion apparatus 3, meanwhile, gas in combustion apparatus 3 can be prevented to exhaust pipe 2 and
Storage tank 1 flows back, and then the high-temperature gas for avoiding combustion apparatus 3 from discharging damages exhaust pipe 2 and storage tank 1.In the present embodiment
Check valve 5 is also referred to as check-valves.
Oil plant is stored in storage tank 1 in the present embodiment.Storage tank 1 is a kind of fluid reservoir in the present embodiment.In other embodiments
Middle storage tank 1 can be also used for storing other types liquid volatile after volatile liquid or heating at normal temperature.
As shown in Figure 1, combustion apparatus 3 is melting furnaces 31, specially glass melter in the present embodiment.In this way, in Volatile Gas
Combustible material will burn in melting furnaces 31, and the fuel as melting furnaces 31 uses, and not only avoid the part combustible material and directly arrange
It puts to atmosphere, and atmosphere is polluted, and realize and the part combustible material is made full use of, saved the energy.Meanwhile
Storage tank volatilization gas processing system is blown into Volatile Gas into melting furnaces 31 through the above way in the present embodiment, also increases in melting furnaces 31
Amount of oxygen, so that the burning in melting furnaces 31 is more abundant.In addition, the burning that other types also can be used in other embodiments is set
Standby 3, such as boiler etc..Storage tank volatilization gas processing system is also referred to as at a kind of environmental protection of wet tank Volatile Gas in the present embodiment
Reason system is related to the storage of volatile liquid after effumability liquid under various room temperature or heating, uses, meanwhile, it is related to storing up
It deposits, using the enterprise of heavy oil, ratio glass factory or cement plant etc. need the biggish enterprise of fuel quantity.Storage tank is waved in the present embodiment
Processing system of getting angry is mainly used for glass factory.
Above-mentioned air intake and Volatile Gas discharge outlet are provided with the top of storage tank 1 in the present embodiment；In other embodiments
Middle air intake and Volatile Gas discharge outlet can be also provided on the side wall of storage tank 1, and are connected respectively with the lower end of two extensions
Logical, the upper end of two extensions is extended upwardly to higher than in storage tank 1 at the liquid level of oil plant.
Above-mentioned blower 4 uses centrifugal blower in the present embodiment, and other types also can be used in blower 4 in other embodiments
Blower, such as axial fan, diagonal flow fan or cross-flow fan etc..
Storage tank volatilization gas processing system in the present embodiment, thoroughly solves storage tank 1 by way of burning and discharges Volatile Gas
It is influenced caused by environment.This storage tank volatilizees gas processing system for a kind of completely new processing system.
Second of embodiment
As shown in Fig. 2, combustion apparatus 3 is connected by exhaust pipe 2 with Volatile Gas discharge outlet in the present embodiment.In this way, waving
Combustion apparatus 3 will be flowed by exhaust pipe 2 by getting angry.
As shown in Fig. 2, in the present embodiment there are two blowers 4, respectively the first blower 41 and the second blower 42.First blower
41 air outlet is connected with air intake, which will generate micro-positive pressure at air intake and in storage tank 1, to push away
Volatile Gas in dynamic storage tank 1 is flowed to combustion apparatus 3.Meanwhile second the air inlet of blower 42 be connected with Volatile Gas discharge outlet,
And second the air outlet of blower 42 be connected with combustion apparatus 3, which will generate negative pressure at Volatile Gas discharge outlet,
To attract the Volatile Gas in storage tank 1 to flow to combustion apparatus 3.Above-mentioned first blower 41 plays the role of air blower, the second blower
42 play the role of air-introduced machine.The present embodiment uses above-mentioned two blower 4, i.e. the first blower 41 and the second blower 42, effectively increases
The air pressure of the strong Volatile Gas for flowing into combustion apparatus 3, to guarantee when encountering the larger situation of the air pressure in combustion apparatus 3, storage tank 1
In Volatile Gas can smoothly, flow rapidly into combustion apparatus 3.
The air inlet of the first blower 41 is communicated with atmosphere in the present embodiment, and the air outlet of the first blower 41 passes through air inlet pipe
7 are connected with air intake.As shown in Fig. 2, the air inlet of the second blower 42 is arranged by exhaust pipe 2 and Volatile Gas in the present embodiment
Mouth connection is put, and the air outlet of the second blower 42 is connected by check valve 5 with combustion apparatus 3.The check valve 5 can guarantee volatilization
Gas smoothly flows into combustion apparatus 3 by exhaust pipe 2 and the second blower 42, and prevent gas in combustion apparatus 3 to the second blower 42,
Exhaust pipe 2 and storage tank 1 flow back, and avoid impacting the second blower 42 and storage tank 1.
As shown in Fig. 2, pressure gauge 6 is equipped in the present embodiment on storage tank 1, to utilize gas in the pressure gauge 6 detection storage tank 1
Pressure, and the working condition of blower 4 is adjusted according to the air pressure in storage tank 1 convenient for staff or corresponding control system.
As shown in Fig. 2, combustion apparatus 3 is melting furnaces 31, specially glass melter in the present embodiment.And above-mentioned air intake and
Volatile Gas discharge outlet is respectively positioned on the top of storage tank 1.Storage tank 1 is specially a kind of fluid reservoir in this implementation.Storage tank is waved in the present embodiment
The manufacturing enterprise that processing system of getting angry is suitable for having melting furnaces 31.
The third embodiment
As shown in figure 3, combustion apparatus 3 is connected by exhaust pipe 2 with Volatile Gas discharge outlet in the present embodiment.In this way, waving
Combustion apparatus 3 will be flowed by exhaust pipe 2 by getting angry.
As shown in figure 3, the air inlet of blower 4 is connected with Volatile Gas discharge outlet in the present embodiment, the air outlet of blower 4 with
Combustion apparatus 3 is connected.Blower 4 will form negative pressure at Volatile Gas discharge outlet in the present embodiment, to attract the volatilization in storage tank 1
Gas is flowed to combustion apparatus 3.Blower 4 plays the role of air-introduced machine in the present embodiment.
Meanwhile the air inlet of blower 4 is connected by exhaust pipe 2 with Volatile Gas discharge outlet in the present embodiment, blower 4 goes out
Air port is connected by check valve 5 with combustion apparatus 3.The check valve 5 can guarantee that Volatile Gas is smoothly flowed by exhaust pipe 2 and blower 4
Enter combustion apparatus 3, and prevent the gas in combustion apparatus 3 from flowing back to blower 4, exhaust pipe 2 and storage tank 1, avoids to blower 4 and storage
Tank 1 impacts.
As shown in figure 3, pressure gauge 6 is equipped in the present embodiment on storage tank 1, to utilize gas in the pressure gauge 6 detection storage tank 1
Pressure, and the working condition of blower 4 is adjusted according to the air pressure in storage tank 1 convenient for staff or corresponding control system.
As shown in figure 3, air intake is communicated with atmosphere in the present embodiment.And air intake and Volatile Gas discharge outlet are respectively positioned on
The top of storage tank 1.Air intake is communicated with the lower end of air inlet pipe 7 in the present embodiment, and the upper end of the air inlet pipe 7 is communicated with atmosphere.
Combustion apparatus 3 can use glass melter in the present embodiment.For storage enterprise and it is other do not have combustion apparatus
3 enterprise, when using storage tank volatilization gas processing system in the present embodiment, microburner is can be used in combustion apparatus 3, with benefit
The combustible material in the Volatile Gas being introduced into is burnt with microburner, to dispose toxic, pernicious gas.
Oil plant is stored in storage tank 1 in the present embodiment, which is also referred to as fluid reservoir or oil tank.
In conclusion the present invention effectively overcomes various shortcoming in the prior art and has high industrial utilization value.
The above-described embodiments merely illustrate the principles and effects of the present invention, and is not intended to limit the present invention.It is any ripe
The personage for knowing this technology all without departing from the spirit and scope of the present invention, carries out modifications and changes to above-described embodiment.Cause
This, institute is complete without departing from the spirit and technical ideas disclosed in the present invention by those of ordinary skill in the art such as
At all equivalent modifications or change, should be covered by the claims of the present invention.
Claims (10)
- The gas processing system 1. a kind of storage tank volatilizees, including the storage tank (1) with Volatile Gas discharge outlet, which is characterized in that further include The combustion apparatus (3) that is connected with Volatile Gas discharge outlet, the air intake being arranged on the storage tank (1) and storage tank can be driven (1) blower (4) that the Volatile Gas in is flowed to combustion apparatus (3).
- 2. storage tank volatilization gas processing system according to claim 1, which is characterized in that the air outlet and sky of the blower (4) Gas entrance is connected.
- 3. according to claim 1 storage tank volatilize gas processing system, which is characterized in that the air inlet of the blower (4) with wave Discharge outlet of getting angry is connected, and the air outlet of the blower (4) is connected with combustion apparatus (3).
- 4. storage tank volatilization gas processing system according to claim 3, which is characterized in that the air outlet of the blower (4) passes through Check valve (5) is connected with combustion apparatus (3).
- 5. storage tank volatilizees gas processing system according to claim 1, which is characterized in that the blower (4) include air outlet with The first blower (41) and air inlet that air intake is connected are connected with Volatile Gas discharge outlet and air outlet is set with burning The second blower (42) that standby (3) are connected.
- 6. storage tank volatilization gas processing system according to claim 1, which is characterized in that the combustion apparatus (3) is melting furnaces (31)。
- 7. storage tank volatilization gas processing system according to claim 1, which is characterized in that the Volatile Gas discharge outlet passes through unidirectional Valve (5) is connected with combustion apparatus (3).
- 8. storage tank volatilization gas processing system according to claim 1, which is characterized in that be equipped with pressure on the storage tank (1) Table (6).
- 9. storage tank volatilization gas processing system according to claim 1, which is characterized in that store oil plant in the storage tank (1).
- 10. storage tank volatilization gas processing system according to claim 1, which is characterized in that the blower (4) is centrifugal blower.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201910271479.5A CN109945214A (en) | 2019-04-04 | 2019-04-04 | A kind of storage tank volatilization gas processing system |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201910271479.5A CN109945214A (en) | 2019-04-04 | 2019-04-04 | A kind of storage tank volatilization gas processing system |
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| Publication Number | Publication Date |
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| CN109945214A true CN109945214A (en) | 2019-06-28 |
Family
ID=67012585
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| CN201910271479.5A Pending CN109945214A (en) | 2019-04-04 | 2019-04-04 | A kind of storage tank volatilization gas processing system |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110817177A (en) * | 2019-12-18 | 2020-02-21 | 大连福佳·大化石油化工有限公司 | Closed discharge system of mechanical pump sealing white oil tank |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2005177650A (en) * | 2003-12-22 | 2005-07-07 | Yamaha Corp | Inflammable volatile organic compounds gas treatment device, inflammable volatile organic compounds gas treatment system, and inflammable volatile organic compounds gas treatment method |
| CN102913918A (en) * | 2011-08-01 | 2013-02-06 | 中国石油化工股份有限公司 | Catalytic combustion processing method of high-concentration organic exhaust gas |
| CN204056865U (en) * | 2014-07-09 | 2014-12-31 | 南京天膜科技股份有限公司 | A kind of full regenerative apparatus of breathing emission gases of nitrogen-sealed storage tank |
| CN206417438U (en) * | 2016-11-03 | 2017-08-18 | 浙江邦成化工有限公司 | A kind of hydrochloric acid tank for being used to prepare the phenylbutyric acid hydrochloride of 4 amino 3 |
| CN209876951U (en) * | 2019-04-04 | 2019-12-31 | 中国建材国际工程集团有限公司 | Storage tank volatile gas treatment system |
-
2019
- 2019-04-04 CN CN201910271479.5A patent/CN109945214A/en active Pending
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2005177650A (en) * | 2003-12-22 | 2005-07-07 | Yamaha Corp | Inflammable volatile organic compounds gas treatment device, inflammable volatile organic compounds gas treatment system, and inflammable volatile organic compounds gas treatment method |
| CN102913918A (en) * | 2011-08-01 | 2013-02-06 | 中国石油化工股份有限公司 | Catalytic combustion processing method of high-concentration organic exhaust gas |
| CN204056865U (en) * | 2014-07-09 | 2014-12-31 | 南京天膜科技股份有限公司 | A kind of full regenerative apparatus of breathing emission gases of nitrogen-sealed storage tank |
| CN206417438U (en) * | 2016-11-03 | 2017-08-18 | 浙江邦成化工有限公司 | A kind of hydrochloric acid tank for being used to prepare the phenylbutyric acid hydrochloride of 4 amino 3 |
| CN209876951U (en) * | 2019-04-04 | 2019-12-31 | 中国建材国际工程集团有限公司 | Storage tank volatile gas treatment system |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110817177A (en) * | 2019-12-18 | 2020-02-21 | 大连福佳·大化石油化工有限公司 | Closed discharge system of mechanical pump sealing white oil tank |
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