JPH11169655A - Absorbing method of organic material vapor by easily electrified solvent - Google Patents

Absorbing method of organic material vapor by easily electrified solvent

Info

Publication number
JPH11169655A
JPH11169655A JP9346143A JP34614397A JPH11169655A JP H11169655 A JPH11169655 A JP H11169655A JP 9346143 A JP9346143 A JP 9346143A JP 34614397 A JP34614397 A JP 34614397A JP H11169655 A JPH11169655 A JP H11169655A
Authority
JP
Japan
Prior art keywords
solvent
packed bed
bed
drop
space under
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.)
Granted
Application number
JP9346143A
Other languages
Japanese (ja)
Other versions
JP3570186B2 (en
Inventor
Kazuki Mihara
一気 三原
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Mitsubishi Chemical Corp
Original Assignee
Mitsubishi Chemical Corp
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Mitsubishi Chemical Corp filed Critical Mitsubishi Chemical Corp
Priority to JP34614397A priority Critical patent/JP3570186B2/en
Publication of JPH11169655A publication Critical patent/JPH11169655A/en
Application granted granted Critical
Publication of JP3570186B2 publication Critical patent/JP3570186B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Landscapes

  • Treating Waste Gases (AREA)
  • Gas Separation By Absorption (AREA)

Abstract

PROBLEM TO BE SOLVED: To avoid the danger of ignition due to the electrification of a solvent by collecting and pulling out the solvent in a packed bed lower part so that the solvent flowing down in the bed does not drop drown in a space under the packed bed. SOLUTION: The generation of static electricity in a gas absorbing device 1 is divided into flow electrification generated when the solvent flows down through the packed bed 2 and drop electricity generated when the solvent drops down in the space under the packed bed 2. The former static electricity therein enables to escape by earthing a packing material in the packed bed. But static electricity generated by another drop electrification unenables to escape from the liquid drop because the liquid drop exists in the space. As a result, electrified charge cloud is formed in the space under the packed bed. Then, the formation of electrified charge cloud is avoided by eliminating the liquid drop in the space under the packed bed 2. Therefor the solvent flowing down through the packed bed 2 is controlled to be collected at the lower end of the packed bed 2 and to send to a liquid trap 5 thereunder through a flow-down pipe 7.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は炭化水素系溶剤のよ
うな帯電し易い溶剤を用いて、空気中の炭化水素などを
安全に吸収する方法に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for safely absorbing hydrocarbons and the like in the air by using an easily charged solvent such as a hydrocarbon solvent.

【0002】[0002]

【従来の技術】常温で液状の有機液体の貯槽としては、
一般には大気と連通するベント管を有する常圧型貯槽が
用いられている。このタイプの貯槽からは、気温の変化
等に伴う呼気作用により、常に少量の有機液体蒸気が排
出されている。また、貯槽への有機液体の送入時には多
量の有機液体蒸気が排出される。
2. Description of the Related Art As a storage tank for an organic liquid which is liquid at room temperature,
Generally, an atmospheric pressure storage tank having a vent pipe communicating with the atmosphere is used. From this type of storage tank, a small amount of organic liquid vapor is constantly discharged due to an exhalation effect accompanying a change in temperature or the like. In addition, a large amount of organic liquid vapor is discharged when the organic liquid is sent into the storage tank.

【0003】従来、これらの有機液体の蒸気は、そのま
ま大気中に放出されるのが一般的であった。しかし大気
中への放出は大気汚染を招くので避けるべきであり、特
に大気汚染防止法の有害大気汚染物質に指定されている
ものは、放出抑制が義務付けられている。しかし、貯槽
から発生する有機液体蒸気の濃度は一般に低濃度なの
で、これを効率よく捕集することは相当に困難である。
特にベンゼン、トルエン、キシレン、エチルベンゼン等
の芳香族炭化水素や、ブタン、オクタン、α−オレフィ
ン、シクロヘキサン等の脂肪族ないしは脂環族炭化水
素、さらにはナフサその他の石油製品の場合には、これ
らのガスが空気と混在すると爆鳴気を形成することがあ
るので、その取扱いには格段の注意が必要である。
Conventionally, these organic liquid vapors have generally been released to the atmosphere as they are. However, release to the atmosphere causes air pollution and should be avoided. In particular, emission control of substances specified as harmful air pollutants under the Air Pollution Control Law is required. However, since the concentration of the organic liquid vapor generated from the storage tank is generally low, it is considerably difficult to efficiently collect it.
In particular, in the case of aromatic hydrocarbons such as benzene, toluene, xylene, and ethylbenzene, and aliphatic or alicyclic hydrocarbons such as butane, octane, α-olefin, and cyclohexane, and naphtha and other petroleum products, these are used. Extreme care must be taken in the handling of gases as they can form detonation when mixed with air.

【0004】低濃度で存在する有機物蒸気の回収方法の
一つに溶剤で吸収する方法がある。しかし貯槽から排出
される蒸気をこの方法で回収するには、簡単に実施でき
るものでなければならず、装置及び吸収溶剤は自ずと限
定される。例えば装置としては、中間部に充填床を有し
ていてその下方が液溜めとなっており、この空間部に有
機物蒸気を含むガスを導入し、液溜めからポンプで循環
されて充填床の上面に散布される吸収液と向流接触させ
る型式のものが用いられる。また吸収液としては、常温
における蒸気圧が低く、低粘度で、空気に対して安定で
あり、かつ安価なものでなければならず、通常は炭化水
素系溶剤、特に炭素数9以上の炭化水素溶剤が用いられ
る。このような溶剤としては、重質ガソリン、軽油、灯
油などの石油製品や、ベンゼン、トルエン、キシレン等
の芳香族製品の製造工程から高沸点成分として排出され
る芳香族留分などが挙げられる。
[0004] One of the methods of recovering organic vapor present at a low concentration is a method of absorbing it with a solvent. However, in order to recover the vapor discharged from the storage tank by this method, it must be easily implemented, and the equipment and the absorbing solvent are naturally limited. For example, the device has a packed bed in the middle and a liquid reservoir below it. A gas containing organic vapor is introduced into this space, and the gas is circulated by a pump from the liquid reservoir and the upper surface of the packed bed. A type in which the liquid is brought into countercurrent contact with the absorbing liquid to be sprayed is used. In addition, the absorbing liquid must have a low vapor pressure at room temperature, a low viscosity, be stable to air, and be inexpensive. Usually, hydrocarbon solvents, particularly hydrocarbons having 9 or more carbon atoms, are required. A solvent is used. Examples of such a solvent include petroleum products such as heavy gasoline, light oil, and kerosene, and aromatic fractions discharged as high-boiling components from the process of producing aromatic products such as benzene, toluene, and xylene.

【0005】[0005]

【発明が解決しようとする課題】これらの炭化水素系溶
剤は一般的に体積抵抗率が高く、流動すると静電荷を帯
びる性質がある。前述の如く被吸収成分である有機物蒸
気は空気と混在すると爆鳴気を形成するので、溶剤が静
電荷を帯びると放電により着火する可能性があり、極め
て危険である。炭化水素系溶剤が静電荷を帯びるのを防
止する方法として、従来は溶剤に帯電防止剤を添加し
て、溶剤の電気抵抗を低下させる方法が用いられてい
る。しかし、この方法は費用がかかり、かつ帯電防止剤
の濃度管理に注意を要する。本発明は、帯電防止剤を用
いなくても、溶剤の帯電による着火の危険を回避できる
方法を提供しようとするものである。
These hydrocarbon solvents generally have a high volume resistivity, and have the property of being charged with an electrostatic charge when they flow. As described above, the organic vapor, which is a component to be absorbed, forms explosive gas when mixed with air. Therefore, if the solvent has an electrostatic charge, it may be ignited by discharge, which is extremely dangerous. As a method for preventing a hydrocarbon solvent from being charged with an electrostatic charge, a method of adding an antistatic agent to the solvent to reduce the electric resistance of the solvent has conventionally been used. However, this method is expensive and requires care in controlling the concentration of the antistatic agent. An object of the present invention is to provide a method capable of avoiding the danger of ignition due to charging of a solvent without using an antistatic agent.

【0006】[0006]

【課題を解決するための手段】本発明によれば、中間部
に充填床を有しており、充填床の下方が空間となってい
るガス吸収装置に、充填床の下方から被吸収成分を含む
ガスを導入して床内を上昇させ、上方からは帯電し易い
溶剤を導入して床内を流下させ、床内で気液接触させて
被吸収成分を溶剤で吸収するに際し、充填床を流下して
きた溶剤が床下方の空間を滴下しないように床下部で溶
剤を捕集して抜出すことにより、溶剤の帯電による着火
の危険を回避することができる。
According to the present invention, a gas-absorbing device having a packed bed in an intermediate portion and having a space below the packed bed serves to absorb the components to be absorbed from below the packed bed. A gas containing gas is introduced to raise the inside of the bed, and a solvent that is easily charged is introduced from above to flow down the inside of the bed, and gas-liquid contact is made in the bed to absorb the component to be absorbed with the solvent. By collecting and extracting the solvent at the lower part of the floor so that the flowing solvent does not drop into the space below the floor, the danger of ignition due to the charging of the solvent can be avoided.

【0007】[0007]

【発明の実施の形態】本発明についてさらに詳細に説明
すると、炭化水素系溶剤のような帯電し易い溶剤を用い
るガス吸収装置における静電気の発生は、溶剤が充填床
を流下するときの流動帯電と、充填床から下方の空間に
滴下するときの滴下帯電とに分けることができる。この
うち前者の流動帯電により発生した静電気は、充填床の
充填材をアースにしておくことにより、充填材を介して
逃すことができる。しかし後者の滴下帯電により発生し
た静電気は、液滴が空間に存在するため、液滴から静電
気を逃すことは不可能である。その結果、充填床下方の
空間には帯電した液滴からなる帯電電荷雲が形成され
る。労働省産業安全研究所の静電気安全指針によれば、
一般に電荷雲の規模が直径0.7m以上で、電荷雲内の
平均電界が1kV/cm以上になると、ブラシ放電が発
生するとされている。
BEST MODE FOR CARRYING OUT THE INVENTION The present invention will be described in further detail. The generation of static electricity in a gas absorbing device using a solvent which is easily charged such as a hydrocarbon-based solvent is caused by flow electrification when the solvent flows down a packed bed. And drop electrification at the time of dropping from the packed bed to the space below. Of the above, the static electricity generated by the former flow electrification can be released via the filler by grounding the filler in the packed bed. However, the static electricity generated by the latter drop charging cannot escape the static electricity from the droplet because the droplet exists in the space. As a result, a charged cloud of charged droplets is formed in the space below the packed bed. According to the Ministry of Labor's Industrial Safety Research Institute's static electricity safety guidelines,
Generally, when the size of the charge cloud is 0.7 m or more in diameter and the average electric field in the charge cloud is 1 kV / cm or more, brush discharge is generated.

【0008】本発明では、充填床から下方の空間に液滴
を滴下させないことにより、帯電電荷雲の形成を回避す
る。そのため、充填床を流下してきた溶剤は充填床の下
端で捕集し、流下管を経て下方の液溜めに送るようにす
る。充填床の下端で流下してきた溶剤を捕集する装置と
しては、種々のものを用いることができる。図1はこの
ような装置の1例で、充填床下端の充填材の支持板が、
キャップ付きのガス上昇管を備えた構造となっている。
図2は他の例で、充填床の充填材支持板の直下に落下す
る溶剤の捕集器を設けたものである。
In the present invention, the formation of a charged charge cloud is avoided by preventing the droplets from dropping into the space below the packed bed. Therefore, the solvent flowing down the packed bed is collected at the lower end of the packed bed, and sent to the lower reservoir through the downflow pipe. Various devices can be used for collecting the solvent flowing down at the lower end of the packed bed. FIG. 1 shows an example of such an apparatus, in which a support plate for a filler at the lower end of a packed bed is
It has a structure with a gas riser with a cap.
FIG. 2 shows another example in which a collector for a solvent that falls directly below a filler support plate of a packed bed is provided.

【0009】本発明によれば、充填床で被吸収成分を含
むガスと炭化水素系溶剤のような帯電し易い溶剤とを向
流接触させてガス吸収を行うに際し、充填床下方の空間
における帯電電荷雲の形成を回避することができるの
で、炭化水素蒸気を含む空気など爆鳴気を形成するよう
なガスでも安全に処理することができる。
According to the present invention, when the gas containing the component to be absorbed and the easily-charged solvent such as a hydrocarbon-based solvent are brought into countercurrent contact with each other in the packed bed to absorb the gas, the charging in the space below the packed bed is performed. Since the formation of a charge cloud can be avoided, even a gas that forms a detonation gas such as air containing hydrocarbon vapor can be safely treated.

【図面の簡単な説明】[Brief description of the drawings]

【図1】本発明を実施する装置の1例の部分模式図であ
る。
FIG. 1 is a partial schematic view of an example of an apparatus for implementing the present invention.

【図2】本発明を実施する装置の他の例の部分模式図で
あり、aは正面図、bは捕集器の平面図である。
FIGS. 2A and 2B are partial schematic views of another example of an apparatus for practicing the present invention, wherein a is a front view, and b is a plan view of a collector.

【符号の説明】[Explanation of symbols]

1 ガス吸収装置 2 充填床 3 捕集器 4 ガス導入管 5 液溜め 6 循環ポンプ 7 流下管 DESCRIPTION OF SYMBOLS 1 Gas absorption device 2 Packing bed 3 Collector 4 Gas introduction pipe 5 Liquid reservoir 6 Circulation pump 7 Downflow pipe

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 FI B01D 53/72 ──────────────────────────────────────────────────の Continued on front page (51) Int.Cl. 6 Identification code FI B01D 53/72

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】 中間部に充填床を有しており、充填床の
下方が空間となっているガス吸収装置に、充填床の下方
から被吸収成分を含むガスを導入して床内を上昇させ、
上方から帯電し易い溶剤を導入して床内を流下させ、床
内で気液接触させて被吸収成分を溶剤で吸収するに際
し、充填床を流下してきた溶剤が床下方の空間を滴下し
ないように床下部で溶剤を捕集して抜出すことを特徴と
する方法。
1. A gas containing a component to be absorbed is introduced from below the packed bed into a gas absorbing device having a packed bed at an intermediate portion and having a space below the packed bed, and ascending the inside of the bed. Let
Introduce a solvent that is easily charged from above and let it flow down the floor.When absorbing the component to be absorbed with the solvent by gas-liquid contact in the bed, make sure that the solvent flowing down the packed bed does not drip into the space below the bed. Collecting and extracting the solvent at the bottom of the floor.
【請求項2】 被吸収成分が空気と爆鳴気を形成するも
のであることを特徴とする請求項1記載の方法。
2. The method according to claim 1, wherein the component to be absorbed is one that forms a detonation with air.
【請求項3】 被吸収成分を含むガスが、液体炭化水素
の貯槽から発生した希薄な炭化水素を含む空気であるこ
とを特徴とする請求項1又は2記載の方法。
3. The method according to claim 1, wherein the gas containing the component to be absorbed is air containing a dilute hydrocarbon generated from a liquid hydrocarbon storage tank.
【請求項4】 溶剤が炭化水素系溶剤であることを特徴
とする請求項1ないし3のいずれかに記載の方法。
4. The method according to claim 1, wherein the solvent is a hydrocarbon solvent.
JP34614397A 1997-12-16 1997-12-16 Absorption method of organic vapor by solvent which is easily charged Expired - Fee Related JP3570186B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP34614397A JP3570186B2 (en) 1997-12-16 1997-12-16 Absorption method of organic vapor by solvent which is easily charged

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP34614397A JP3570186B2 (en) 1997-12-16 1997-12-16 Absorption method of organic vapor by solvent which is easily charged

Publications (2)

Publication Number Publication Date
JPH11169655A true JPH11169655A (en) 1999-06-29
JP3570186B2 JP3570186B2 (en) 2004-09-29

Family

ID=18381415

Family Applications (1)

Application Number Title Priority Date Filing Date
JP34614397A Expired - Fee Related JP3570186B2 (en) 1997-12-16 1997-12-16 Absorption method of organic vapor by solvent which is easily charged

Country Status (1)

Country Link
JP (1) JP3570186B2 (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2009067851A (en) * 2007-09-11 2009-04-02 Nippon Oil Corp Hydrocarbon recovery system, deaeration apparatus used therefor and hydrocarbon recovery method
JP2016150338A (en) * 2015-02-16 2016-08-22 現代自動車株式会社Hyundai Motor Company Absorption tower with absorption reaction separator
JP2016150339A (en) * 2015-02-16 2016-08-22 現代自動車株式会社Hyundai Motor Company Gas collecting plant

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2009067851A (en) * 2007-09-11 2009-04-02 Nippon Oil Corp Hydrocarbon recovery system, deaeration apparatus used therefor and hydrocarbon recovery method
JP2016150338A (en) * 2015-02-16 2016-08-22 現代自動車株式会社Hyundai Motor Company Absorption tower with absorption reaction separator
JP2016150339A (en) * 2015-02-16 2016-08-22 現代自動車株式会社Hyundai Motor Company Gas collecting plant

Also Published As

Publication number Publication date
JP3570186B2 (en) 2004-09-29

Similar Documents

Publication Publication Date Title
DE2760187C2 (en)
US3748829A (en) Adsorbing evaporative emission during fueling of automotive vehicles
US5453114A (en) Method of dehydrating natural gas for reducing emissions of hydrocarbon impurities
JP5807233B2 (en) Deodorizing device
US4908047A (en) Soot removal from exhaust gas
US2849150A (en) Vapor recovery system
US5125230A (en) Soot removal from exhaust gas
CN109789343B (en) Method for aerating flammable liquids to extract flammable vapors
JP3570186B2 (en) Absorption method of organic vapor by solvent which is easily charged
CA2125356A1 (en) Vapor recovery system
EP0659167A4 (en) Apparatus for controlling fuel vapor flow.
EP0529401B1 (en) Process for absorption of explosive gases in a mass transfer column
DE3210236C2 (en) Process for cleaning an exhaust gas stream laden with steam and / or gaseous pollutants
CN206404563U (en) Harbour oil gas recovery processing system
CN205379781U (en) Normal atmospheric temperature diesel oil absorption - non -passivation adsorbs organic gas processing apparatus
CN105084289A (en) Novel efficient absorption type oil and gas recovery system for gas station
CN114011208A (en) Gasoline vapor recovery unit
KR102024774B1 (en) Pollutant treating apparatus using electrospray
CN207413080U (en) VOCS recycles filter device
CN207605552U (en) The adsorption/desorption device of petroleum vapor recovery
JP2511576B2 (en) Purification device and purification method for gas containing organic solvent
CN202237588U (en) Liquid separation device
CN102225293A (en) Oil gas recovery reactor for removing hydrogen sulfide gas from crude oil vapor
JPH09141039A (en) Gasoline vapor adsorption, separation and recovery method and device therefor
CN104128052A (en) Siphon washing type asphalt tail gas treatment method

Legal Events

Date Code Title Description
A977 Report on retrieval

Free format text: JAPANESE INTERMEDIATE CODE: A971007

Effective date: 20040428

TRDD Decision of grant or rejection written
A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 20040601

A61 First payment of annual fees (during grant procedure)

Free format text: JAPANESE INTERMEDIATE CODE: A61

Effective date: 20040614

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20080702

Year of fee payment: 4

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20080702

Year of fee payment: 4

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20090702

Year of fee payment: 5

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20090702

Year of fee payment: 5

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20100702

Year of fee payment: 6

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20100702

Year of fee payment: 6

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20110702

Year of fee payment: 7

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20120702

Year of fee payment: 8

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20130702

Year of fee payment: 9

LAPS Cancellation because of no payment of annual fees