JPS6010069B2 - Method for separating fine powder from gas cleaning liquid - Google Patents
Method for separating fine powder from gas cleaning liquidInfo
- Publication number
- JPS6010069B2 JPS6010069B2 JP56165821A JP16582181A JPS6010069B2 JP S6010069 B2 JPS6010069 B2 JP S6010069B2 JP 56165821 A JP56165821 A JP 56165821A JP 16582181 A JP16582181 A JP 16582181A JP S6010069 B2 JPS6010069 B2 JP S6010069B2
- Authority
- JP
- Japan
- Prior art keywords
- cleaning liquid
- fine powder
- gas
- cleaning
- powder
- 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
Links
Landscapes
- Industrial Gases (AREA)
Description
【発明の詳細な説明】
本発明は石炭や石炭・重質油スラリ−をガス化した場合
に生成ガスに混合している徴粉の除去方法に係り、特に
徴粉の除去に好適なガス洗浄液からの徴粉分離方法に関
するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for removing powder particles mixed in gas produced when coal or coal/heavy oil slurry is gasified, and a gas cleaning liquid particularly suitable for removing powder particles. The present invention relates to a method for separating powder from powder.
石炭や石炭・車質油スラリーをガス化した時の生成ガス
中には夕−ルや微粒子が多量に混合している。The gas produced when coal or coal/vehicle oil slurry is gasified contains a large amount of coal and fine particles.
これらのタールや微粒子を除去するため、ガス化炉から
排出される生成ガスは流動層クェンチャーに導きタール
分を除去し、微粒子はサイクロンで瓶集している。しか
し、非常に粒径の小さな徴粉やタールは捕集できずにガ
スに同伴されるためスクラバーに導き水で洗浄し、除去
する方法がとられている。洗浄方法としては水を洗浄液
槽からスクラバ−に送り込み、徴粉タールを洗い落し、
水と一緒に洗浄液槽に戻す循環方式が採用されている。In order to remove these tars and fine particles, the generated gas discharged from the gasifier is guided to a fluidized bed quencher to remove the tar, and the fine particles are collected in a cyclone. However, very small particles of powder and tar cannot be collected and are entrained in the gas, so they are removed by introducing them into a scrubber and washing them with water. The cleaning method is to send water from the cleaning liquid tank to the scrubber to wash away the powdery tar.
A circulation system is adopted in which the water is returned to the cleaning liquid tank together with the water.
このためスクラバ−からは徴粉の表面にタールが凝縮し
た物が洗浄液と同時に排出される。したがって長時間に
わたりガス化炉を運転する場合には洗浄液中の徴粉の量
は次第に増加するためスクラバー内や洗浄液循環パイプ
に堆積し、洗浄液の流路を閉塞してしまう。このためス
クラバ−から排出した洗浄液から徴粉を除去する必要が
ありフィルターで炉過することが考えられている。しか
し、洗浄液に混入している徴粉は非常に小さいためフィ
ルターが目語りし、徴粉の分離が困難である。これらの
欠点を改善するものとして水に界面活性剤を添加して洗
浄液とし、この洗浄液で生成ガスから徴粉を洗い落し、
これら徴粉を含有した洗浄液に空気を吹込んで起泡させ
、この起泡により液中に懸濁した微粉を泡表面に吸着し
、これによって泡とともに徴粉を分離し、徴粉を分離し
た洗浄液を再循環使用する技術が特公昭30−1062
号公報に示されている。しかし、この技術のように洗浄
液に空気を吹込むようにすると、空気ポンプなどの空気
源を必要とする欠点がある。本発明はこの欠点を改善し
ようとしてなされたもので、その目的とするところは、
何等設備を用いることなく使用済洗浄液を泡立せること
にある。Therefore, tar condensed on the surface of the powder is discharged from the scrubber at the same time as the cleaning solution. Therefore, when the gasifier is operated for a long period of time, the amount of powder particles in the cleaning liquid gradually increases and accumulates in the scrubber and in the cleaning liquid circulation pipe, thereby clogging the cleaning liquid flow path. For this reason, it is necessary to remove the powdery particles from the cleaning liquid discharged from the scrubber, and it has been considered to pass it through a filter. However, the powder mixed in the cleaning solution is so small that it is visible to the filter, making it difficult to separate the powder. In order to improve these drawbacks, a surfactant is added to water to create a cleaning solution, and this cleaning solution is used to wash away the particles from the generated gas.
Air is blown into the cleaning liquid containing these fine powders to foam them, and the fine powders suspended in the liquid are adsorbed to the surface of the foam, thereby separating the fine powders along with the foam, and the cleaning liquid from which the fine powders have been separated. The technology to recycle and use
It is shown in the publication No. However, blowing air into the cleaning liquid as in this technique has the disadvantage of requiring an air source such as an air pump. The present invention was made to improve this drawback, and its purpose is to:
The purpose is to foam a used cleaning liquid without using any equipment.
このため水に界面活性剤を添加した液体を洗浄液とした
ものおいて、洗浄液をスクラバーに供給し、洗浄後徴粉
の混入した洗浄液をスクラバ−よりも圧力の低い洗浄液
槽に排出し、洗浄液が吸収しているガスを放出させ、発
泡するようにしたものである。For this reason, a cleaning liquid made by adding a surfactant to water is supplied to the scrubber, and after cleaning, the cleaning liquid containing the powder is discharged to a cleaning liquid tank whose pressure is lower than that of the scrubber. It releases the absorbed gas and causes foaming.
すなわち、スクラバ−から排出された徴粉を混入する洗
浄液は界面活性剤の添加により水を洗浄液とした場合よ
りも表面張力が小さくなり発泡しやすい状態となってお
り、しかも洗浄液はスクラバ−内で生成ガスの一部であ
る炭酸ガス等を吸収している。このためスクラバーより
も圧力の低い状態にしている洗浄液槽で徴粉を捕集して
発泡し、泡は洗浄液槽表面に移動して浮遊するので泡を
電動の羽根車等で連続的に除去することにより、徴粉は
除去され常に徴粉の少ない洗浄液を循環供給できるよう
にしたものである。本発明は洗浄液として水に界面活性
剤を添加したものを用い、洗浄液槽をスクラバーよりも
低い圧力に保ち吸収ガスを放出させることで効果を発漣
するので、水に界面活性剤の一種である中性洗剤を0.
5wt%添加したものを洗浄液とし、スクラバー圧力3
.0k9/係、石炭・車質油スラリ−供給量17k9/
h、スチーム供給量34k9/h、酸素供給量10kg
′h、洗浄液槽は常圧とし「 6餌時間ガス化炉を運転
し、その効果を調べた。In other words, the surface tension of the cleaning liquid that is mixed with the powder discharged from the scrubber is lower than that when the cleaning liquid is water due to the addition of a surfactant, and the cleaning liquid is more likely to foam inside the scrubber. It absorbs carbon dioxide gas, which is part of the generated gas. For this reason, the powder is collected and foamed in the cleaning liquid tank, which has a lower pressure than the scrubber, and the foam moves to the surface of the cleaning liquid tank and floats, so the foam is continuously removed using an electric impeller, etc. As a result, powdery particles are removed, and a cleaning solution with a small amount of powdery particles can be constantly circulated and supplied. The present invention uses water with a surfactant added as the cleaning liquid, and maintains the cleaning liquid tank at a lower pressure than the scrubber and releases the absorbed gas to produce an effect. 0.0% neutral detergent.
The cleaning liquid containing 5 wt% was used, and the scrubber pressure was 3.
.. 0k9/person in charge, coal/vehicle oil slurry supply amount 17k9/
h, steam supply amount 34k9/h, oxygen supply amount 10kg
The cleaning liquid tank was kept at normal pressure and the gasifier was operated for 6 hours to examine its effectiveness.
図面は本発明の上記条件で徴粉を浮遊させ、これを連続
除去し、循環している洗浄液に混入している微粉濃度の
経時変化を従来法と比較したものである。The drawing shows a comparison of the changes over time in the concentration of fine powder mixed in the circulating cleaning solution with the conventional method by suspending and continuously removing fine powder under the above-mentioned conditions of the present invention.
洗浄液として水を使用した場合には洗浄液中の徴粉濃度
1はガス化開始後の経過時間と共に増加し6餌時間で約
鼠れ%になっている。When water is used as the cleaning liquid, the powder concentration 1 in the cleaning liquid increases with the elapsed time after the start of gasification, and reaches approximately 1% after 6 feeding hours.
一方本発明すなわち水に中性洗剤0.5M添加した場合
の洗浄液中の徴粉濃度2はガス化開始後約3畑時間まで
はゆるやかに増加し約1.細t%となり、その後はほと
んど変化がなく2.0〜2.がt%を維持し、常に徴粉
の少ない洗浄水を循環供給できる。このように本発明に
よれば洗浄液に混入している徴粉を除去できる状態に浮
遊分離させる効果はきわめて大きいことを示している。
本発明によれば洗浄液に浸入している徴粉を空気ポンプ
等の設備を用いることなく泡に付着させて浮遊させるこ
とができ、徴粉を容易に除去できる。On the other hand, according to the present invention, when 0.5M of a neutral detergent is added to water, the powder concentration 2 in the cleaning solution increases slowly until about 3 field hours after the start of gasification, and increases to about 1. It becomes a fine t%, and there is almost no change after that, at 2.0 to 2. t%, and can constantly circulate and supply cleaning water with little powdery appearance. As described above, the present invention shows that the effect of floating and separating the powder particles mixed in the cleaning liquid in a state where they can be removed is extremely large.
According to the present invention, the powder particles that have entered the cleaning liquid can be made to adhere to the foam and suspended without using equipment such as an air pump, and the powder particles can be easily removed.
図面は本発明の効果を従来法による結果と比較したグラ
フである。The drawing is a graph comparing the effects of the present invention with the results of the conventional method.
Claims (1)
ガス化した生成ガスに含有する微粉を水に界面活性剤を
添加した洗浄液で洗浄除去する方法において、前記洗浄
剤の洗浄液をスクラバーよりも圧力の低い液層に排出し
、圧力差により洗浄液が吸収しているガスを放出により
発泡させ、微粉を洗浄液から浮遊分離することを特徴と
するガス洗浄液からの微粉分離方法。1. A method in which coal and coal/heavy oil slurry are gasified and fine powder contained in the gasified gas is washed and removed with a cleaning solution made by adding a surfactant to water, in which the cleaning solution of the cleaning agent is applied at a pressure higher than that of a scrubber. A method for separating fine powder from a gas cleaning liquid, which is characterized by discharging the gas into a liquid layer with a low temperature, causing the gas absorbed by the cleaning liquid to be released and foaming due to a pressure difference, and floating and separating the fine powder from the cleaning liquid.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP56165821A JPS6010069B2 (en) | 1981-10-19 | 1981-10-19 | Method for separating fine powder from gas cleaning liquid |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP56165821A JPS6010069B2 (en) | 1981-10-19 | 1981-10-19 | Method for separating fine powder from gas cleaning liquid |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5867318A JPS5867318A (en) | 1983-04-21 |
| JPS6010069B2 true JPS6010069B2 (en) | 1985-03-14 |
Family
ID=15819630
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP56165821A Expired JPS6010069B2 (en) | 1981-10-19 | 1981-10-19 | Method for separating fine powder from gas cleaning liquid |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6010069B2 (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP4568573B2 (en) * | 2004-10-15 | 2010-10-27 | 三菱重工業株式会社 | Biomass gasification gas processing system |
-
1981
- 1981-10-19 JP JP56165821A patent/JPS6010069B2/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5867318A (en) | 1983-04-21 |
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