JPS5817819A - Method for gas-liquid contact - Google Patents
Method for gas-liquid contactInfo
- Publication number
- JPS5817819A JPS5817819A JP56117469A JP11746981A JPS5817819A JP S5817819 A JPS5817819 A JP S5817819A JP 56117469 A JP56117469 A JP 56117469A JP 11746981 A JP11746981 A JP 11746981A JP S5817819 A JPS5817819 A JP S5817819A
- Authority
- JP
- Japan
- Prior art keywords
- gas
- layer
- electric field
- react
- treated
- 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.)
- Pending
Links
Landscapes
- Gas Separation By Absorption (AREA)
- Physical Or Chemical Processes And Apparatus (AREA)
Abstract
Description
【発明の詳細な説明】
気体と液体とを接触させる方法、例えば、気体中の有効
成分を液体に吸収させるとか、気体中の有害ガスを液体
と反応させて除去する等の方法が広く採用されている。[Detailed Description of the Invention] Methods of bringing gas and liquid into contact, for example, methods in which active ingredients in the gas are absorbed into the liquid, or harmful gases in the gas are removed by reacting with the liquid, are widely adopted. ing.
本発明は気体を電場処理して気液接触効率を向1−させ
る方法にかかる。The present invention relates to a method for improving gas-liquid contact efficiency by treating gas with an electric field.
本発明の研究結果を図により説明する。The research results of the present invention will be explained using figures.
300〜直径の脱硫装置Hの一端からSO2を1200
ppm含む原ガスを100%直径の送入管(2)よりl
m / s e cの速度にて送入し排出管(3)よ
り排出させる。SO2 from one end of the desulfurization equipment H with a diameter of 300 to 1200
100% of the raw gas containing ppm from the inlet pipe (2) of 100% diameter.
It is fed at a speed of m/sec and discharged from the discharge pipe (3).
送水管(4)より水を3枚の金網層(5)を流下させ、
金網群を通過するSO□と反応させる。Water flows down three wire mesh layers (5) from the water pipe (4),
React with SO□ passing through the wire mesh group.
変圧器への第二次線輪からの導線(6)を金網層(5)
の50%前方のガス通路の全面積に亘って設けられた電
極(7)の集合体に連絡する。+8) +9)は接地を
示す。電極(7)に60サイクル15Kvの電圧を与え
て脱硫試験を行ったところ、下記の脱硫成績を得た。The conductor (6) from the secondary wire ring to the transformer is wired to the wire mesh layer (5).
50% in front of the gas passageway over the entire area of the gas passage. +8) +9) indicates grounding. When a desulfurization test was conducted by applying a voltage of 15 Kv to the electrode (7) for 60 cycles, the following desulfurization results were obtained.
15KV電場 電場無し
第1段 73% 28%
第2段 88% 43%
従来広く工業化されているボイラー排ガスの脱硫装置は
層高1〜2mの厚層のラシヒリング層の上方から例えば
PH9等のNaOH液を噴霧し下方からSO2ガスを含
む原ガスを例えば2m/seeの速度で上昇させ気液接
触させる方法であり、その脱硫率は平均95%である。15KV electric field No electric field 1st stage 73% 28% 2nd stage 88% 43% Conventionally, widely industrialized boiler exhaust gas desulfurization equipment pumps NaOH liquid such as pH 9 from above a thick Raschig ring layer with a layer height of 1 to 2 m. This is a method in which the raw gas containing SO2 gas is sprayed from below at a speed of, for example, 2 m/see and brought into gas-liquid contact, and the desulfurization rate is 95% on average.
これに比較して5%の薄層で2回即ち10%の層でN
aOH液より脱硫力の弱い水に接触させて88%の脱硫
率を得たことは15KVの電場の影響である。Compared to this, N
The fact that a desulfurization rate of 88% was obtained by contacting with water, which has a weaker desulfurization power than the aOH liquid, is due to the influence of the 15 KV electric field.
化学便覧の「電磁気と電気化学」の項に[1個の電子に
電圧をかけて加速し、これを気体分子、原子、遊離基、
またはイオン(陽性)などに衝突せしめると、この電子
の持つ運動エネルギーによってその衝撃を受けた分子、
原子・、遊離基、イオンなどは、みずからの有する電子
を1個放出し、陽イオンとなることがある」と定義して
いる。In the "Electromagnetism and Electrochemistry" section of the Chemistry Handbook, there is a ``electromagnetism and electrochemistry'' section that states, ``A voltage is applied to an electron to accelerate it, and it is then transformed into a gas molecule, an atom, a free radical,
Or, when collided with ions (positive), molecules that are bombarded by the kinetic energy of these electrons,
Atoms, free radicals, ions, etc. can release one of their own electrons and become cations.
l−記試験で薄層の金網層でかつ脱硫速度の遅い水で脱
硫効率88%の好成績を得たのは電場の効果によるもの
である。The reason why the desulfurization efficiency of 88% was obtained using a thin wire mesh layer and water having a slow desulfurization rate in the test described in Section 1 is due to the effect of the electric field.
さらに同じ方法で水をPH9のNaOH液に替えて試験
したところ、第1段で8396、第2段で9806の成
績を得た。When the same method was used to replace water with a NaOH solution with a pH of 9, results of 8396 in the first stage and 9806 in the second stage were obtained.
本発明方法はSO□除去に限定されずNOx除去、14
H3、H2S、メルカプタン等の悪臭除去はもちろんの
こと、生産工場における気体成分の吸収等に広く適用出
来る。The method of the present invention is not limited to SO□ removal, but also NOx removal, 14
It can be widely applied not only to the removal of bad odors such as H3, H2S, and mercaptan, but also to the absorption of gaseous components in production plants.
また気液接触装置は性能試験した図示装置に限定されず
、他の機種にも広く適用出来る。Further, the gas-liquid contact device is not limited to the illustrated device whose performance was tested, but can be widely applied to other models.
上述の如く本発明は簡単な安価な設備で効率よい気液接
触効果をあげる特長がある。As described above, the present invention has the advantage of achieving efficient gas-liquid contact effects with simple and inexpensive equipment.
第1図は本発明方法をテストした試験用脱硫装置、第2
図は電極群の側面図を示す。
(tl−−−−−−−一説硫装置 (61−−−−
−−−一導 線12+−−−−−−−−送入管 +
7)−電 極+31−−−−−−排出管 +8+−接
地+41−−−−−−−−送水管 +9+ −接
地(51−−−−−一−−金網層
出顕人 ミウラエンジーャリングインターナショカル株
式会社取締役社長 三 浦 貢Figure 1 shows the test desulfurization equipment in which the method of the present invention was tested;
The figure shows a side view of the electrode group. (tl--------One theory sulfur equipment (61----
−−−1 conductor wire 12+−−−−−−−Feed pipe +
7) -Electrode +31--Discharge pipe +8+-Ground +41--Water pipe +9+-Connection
Earth (51------1--Akihito from the wire mesh layer Mitsugu Miura, President and Director of Miura Engaging International Co., Ltd.)
Claims (1)
を特長とする気液接触方法。A gas-liquid contact method characterized by applying an electric field to the gas to be treated and then causing it to react with the treatment liquid.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP56117469A JPS5817819A (en) | 1981-07-27 | 1981-07-27 | Method for gas-liquid contact |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP56117469A JPS5817819A (en) | 1981-07-27 | 1981-07-27 | Method for gas-liquid contact |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS5817819A true JPS5817819A (en) | 1983-02-02 |
Family
ID=14712448
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP56117469A Pending JPS5817819A (en) | 1981-07-27 | 1981-07-27 | Method for gas-liquid contact |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS5817819A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS62196351A (en) * | 1986-02-25 | 1987-08-29 | Toshiba Tungaloy Co Ltd | Solid lubricative composite material and its production |
CN1059416C (en) * | 1995-12-28 | 2000-12-13 | 中国科学院兰州化学物理研究所 | Composite self-lubricating zircite-graphite material |
JP2014129892A (en) * | 2012-12-28 | 2014-07-10 | Mitsubishi Electric Corp | Humidification apparatus |
-
1981
- 1981-07-27 JP JP56117469A patent/JPS5817819A/en active Pending
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS62196351A (en) * | 1986-02-25 | 1987-08-29 | Toshiba Tungaloy Co Ltd | Solid lubricative composite material and its production |
CN1059416C (en) * | 1995-12-28 | 2000-12-13 | 中国科学院兰州化学物理研究所 | Composite self-lubricating zircite-graphite material |
JP2014129892A (en) * | 2012-12-28 | 2014-07-10 | Mitsubishi Electric Corp | Humidification apparatus |
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