JPS638366B2 - - Google Patents
Info
- Publication number
- JPS638366B2 JPS638366B2 JP53110709A JP11070978A JPS638366B2 JP S638366 B2 JPS638366 B2 JP S638366B2 JP 53110709 A JP53110709 A JP 53110709A JP 11070978 A JP11070978 A JP 11070978A JP S638366 B2 JPS638366 B2 JP S638366B2
- Authority
- JP
- Japan
- Prior art keywords
- water
- medium
- fluidized bed
- ash
- deposits
- 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
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
- F23G5/30—Incineration of waste; Incinerator constructions; Details, accessories or control therefor having a fluidised bed
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D11/00—Solvent extraction
- B01D11/02—Solvent extraction of solids
- B01D11/0215—Solid material in other stationary receptacles
- B01D11/0223—Moving bed of solid material
- B01D11/0226—Moving bed of solid material with the general transport direction of the solids parallel to the rotation axis of the conveyor, e.g. worm
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/18—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/18—Details relating to the spatial orientation of the reactor
- B01J2219/182—Details relating to the spatial orientation of the reactor horizontal
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Combustion & Propulsion (AREA)
- Organic Chemistry (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Gasification And Melting Of Waste (AREA)
- Crucibles And Fluidized-Bed Furnaces (AREA)
Description
この発明は粘着性物質の付着している流動媒体
の再生の方法、特に発電所のボイラの排ガスから
集じんした灰(以下EP灰と称す)を焼却する流
動層焼却炉に使用する流動媒体例えば媒体として
使用した砂等に付着した粘着物を除去、再生して
流動層焼却炉に再供給し運転する流動媒体再生方
法に関する。
大型の火力発電所など、多量の重油原油を燃焼
するボイラからは、未燃カーボンを含む重油灰
(EP灰)が排出される。この重油灰は、廃棄物と
して処理する場合、その性状の特異性から一般の
埋立には適しない。したがつて、特定の業者によ
つて処理される場合が多い。このため、輸送費が
嵩むこと、粉体であることによる取扱上の支障な
ど、種々の問題がある。このため、その発生源で
ある大型ボイラの付帯設備として、重油灰を焼却
し、減容量、減重量を計り、上記の問題を解決又
は軽減しようとする目的の装置が開発されてい
る。また、この装置による利点は、EP灰中に含
まれるバナジウム化合物が、濃縮されることか
ら、バナジウム鉱石と同等の評価が得られ、その
取扱いが有利になるという付加価値がプラスされ
ることになる。
この焼却炉には、各種の型式が存在するが、一
長一短があり、EP灰の焼却が、容易でないこと
は知られているところである。この中で、流動層
炉を用いて、EP灰を処理する装置は、負荷の変
動、灰成分の変化などに比較的順応することから
重要視されている。しかし、この流動層焼却炉に
おいても次のような欠点がある。すなわち流動媒
体(主として砂が用いられている)が経済的に付
着物によつて肥大し、流動不良を起し、長期連続
運転がむつかしくなるため、炉を停止し、媒体の
取り替えを行なう必要が生じることである。
このため、作業性、運転経費、媒体費などの面
で不利益となり、これらの改善が望まれるわけで
ある。
本発明の目的は、上記した従来技術の欠点をな
くし、炉の停止を行なうことなく、媒体を再生し
て、供給し連続運転を可能にする流動媒体再生方
法を提供するにある。
要するに本発明は、運転中のEP灰焼却用の流
動層炉から、連続あるいは不連続的に、媒体を取
り出し、これに水を添加して、媒体表面に付着し
ている。重油灰の灰分中の水可溶成分を抽出し、
付着力の弱まつた不溶成分を機械的に剥離させ、
再生し媒体たる砂を再度、流動層に戻し運転を継
続することを特徴とするものである。
第1表は流動層焼却炉でEP灰を焼却処理した
とき流動媒体に付着したものの分析値の一例であ
る。
This invention relates to a method for regenerating fluidized media to which sticky substances have adhered, and in particular to fluidized media used in fluidized bed incinerators that incinerate ash collected from the exhaust gas of power plant boilers (hereinafter referred to as EP ash). The present invention relates to a method for regenerating a fluidized bed in which sticky substances adhering to sand or the like used as a medium are removed, regenerated, and re-supplied to a fluidized bed incinerator for operation. Boilers that burn large amounts of heavy oil and crude oil, such as large thermal power plants, emit heavy oil ash (EP ash) that contains unburned carbon. When this heavy oil ash is treated as waste, it is not suitable for general landfilling due to its unique properties. Therefore, it is often processed by a specific company. Therefore, there are various problems such as increased transportation costs and handling problems due to the powder. For this reason, equipment has been developed as ancillary equipment to the large boiler that is the source of the ash, in order to solve or alleviate the above-mentioned problems by incinerating the heavy oil ash and measuring the volume and weight loss. In addition, the advantage of this device is that since the vanadium compounds contained in EP ash are concentrated, it can be evaluated on the same level as vanadium ore, and it has the added value of being advantageous in its handling. . There are various types of incinerators, but they have advantages and disadvantages, and it is well known that incineration of EP ash is not easy. Among these, equipment that processes EP ash using a fluidized bed furnace is considered important because it is relatively adaptable to load fluctuations and changes in ash composition. However, this fluidized bed incinerator also has the following drawbacks. In other words, the fluidizing medium (mainly sand is used) becomes economically swollen with deposits, causing poor flow and making long-term continuous operation difficult, so it is necessary to shut down the furnace and replace the medium. It is something that happens. This results in disadvantages in terms of workability, operating costs, media costs, etc., and improvements in these areas are desired. SUMMARY OF THE INVENTION An object of the present invention is to provide a method for regenerating a fluidized medium, which eliminates the drawbacks of the prior art described above and allows continuous operation by regenerating and supplying the medium without stopping the furnace. In short, in the present invention, a medium is taken out continuously or discontinuously from an operating fluidized bed furnace for incinerating EP ash, water is added to the medium, and water is attached to the surface of the medium. Extract the water-soluble components in the ash of heavy oil ash,
Mechanically removes insoluble components whose adhesion has weakened,
This method is characterized by returning the recycled media sand to the fluidized bed and continuing the operation. Table 1 shows an example of the analytical values of what adhered to the fluidized medium when EP ash was incinerated in a fluidized bed incinerator.
【表】
この表に示すごとく、主成分は、Na2O,SO3
で、これらはNa2SO4の形で存在していると考え
られる。この他は、V,Fe,Niなどの化合物か
ら成つている。この組成の付着物を媒体(主とし
て天然砂)から分離させる方法としてもつと簡単
にする手段としては、機械的な方法で破砕して、
両者を分離することが考えられるが、この方法
は、次の理由により、実際には剥離しない。なぜ
ならば、表面の付着物は、媒体の砂が破砕される
最低の力では剥離することが困難であり、付着物
を破砕する力を加えると媒体自身も粉化して、再
生という本来の目的が達成されないことが明らか
となつたことである。これは、媒体より付着物の
方が弾力性が高く、衝撃力に強いためと考える。
これらのことから、剥離方法として、付着物の組
成に着目し、約50%近く占めているNa2SO4は、
水に可溶であることから、これを水抽出すると付
着物が容易に剥離すると予想され、次のことを実
施してみた。
実施例としては、先ず、付着物が24.5%ある流
動層炉からの抜出し砂を、重量比で1:1の水を
加えて、ボールミルに入れて湿式下の破砕を10分
間行なつた。その結果、付着物の剥離率は約90%
となり、先の乾式破砕に比べ高い値を示し、さら
に水存在下では媒体である砂自身の粉化は、ほと
んどないことが、剥離物の分析結果より確認でき
た。
水可溶性物質が溶解除去されると砂粒子等水へ
の不溶性物質の粘着接続がなくなりばらばらにな
り、またこれら粒子が接続していても中空網目状
の硬質の海綿状になり打撃により容易に粒子とな
るものである。
なお、剥離率を高めるためには湿式破砕後の砂
表面を、新鮮な水か、あるいは、飽和に達してい
ない前記処理水の過水を用いて洗滌してやる
と、剥離率は、より高いものが期待できる。
また芒硝(Na2SO4,IOH2O)の水に対する溶
解度、即ち水1000grに対しその溶解する量をグラ
ムで示すと第1図のような曲線を示す。横軸は液
温で縦軸は溶解した芒硝の量である。図面からも
判るごとく約33℃の処にピークがある。
一方第1表に示すごとく流動媒体への付着物の
約50%はNa2SO4であることより、処理水は30℃
以上のものを使用することがその溶解除去に効果
のあることが判る。流動媒体は多面体で凹突のあ
るものであるが、付着物はV2O5,Al2O3,
Fe2O3,NiOを主成物とする硬質の海綿状体をな
すものと推定され、この骨格内を芒硝が満たして
いるという状態でこの組合せが強力な弾性をもつ
付着物となる原因と思考される。
従つて水に溶解させ芒硝を除くときは硬質海綿
状体は容易に破砕され、流動媒体は付着物のない
ものに復帰することができるものである。
第2図はこの発明にかかる装置の配置フローを
示す図面である。
EP灰を焼却する流動層焼却炉1から溢流又は
抽出された粘着物の付着した要再生の流動媒体
は、管路11により破砕機2に送られる。管路2
1からは水又は再生処理に使用した水で粘着物の
不飽和液が送られ、破砕的粘着物剥離打撃たる機
械的な力が加えられ撹拌が行なわれる。一定時間
破砕機2内に滞留した媒体は分離機3へ管路22
により送られる。分離機3内では、砂等の流動媒
体と、水可溶性物質の溶液と微粒不溶性物質との
混合物たるスラリーとは分離される。処理済みの
流動媒体は管路31により流動層焼却炉1に送ら
れ再使用される。スラリーは管路32より排出さ
れ、流動層焼却炉1の排ガスにより濃縮又は乾燥
されV2O5等は有効利用される。
本発明を実施することにより、流動媒体が流動
層焼却炉内で流動層を形成することの支障となる
粘着物が効率良く除去された媒体を循環供給する
ことができ、安定した焼却処理をすることがで
き、媒体の消費量の低減、V2O5の回収、運転停
止による装置効率の低下の防止、これに関する作
業員の不要等種々の効果を奏するものである。[Table] As shown in this table, the main components are Na 2 O, SO 3
Therefore, these are thought to exist in the form of Na 2 SO 4 . Others are made of compounds such as V, Fe, and Ni. An easy way to separate deposits of this composition from the medium (mainly natural sand) is to crush them mechanically.
Although it is conceivable to separate the two, this method does not actually separate them for the following reason. This is because it is difficult to remove the deposits on the surface with the minimum force required to crush the sand in the medium, and if a force that crushes the deposits is applied, the medium itself will also be pulverized, defeating the original purpose of recycling. It has become clear that this will not be achieved. This is thought to be because the deposits have higher elasticity and are stronger against impact force than the medium.
Based on these facts, we focused on the composition of the deposits as a peeling method, and Na 2 SO 4 , which accounts for about 50%,
Since it is soluble in water, it was expected that the deposits would be easily peeled off when extracted with water, so we tried the following. As an example, first, sand extracted from a fluidized bed furnace containing 24.5% of deposits was mixed with water at a weight ratio of 1:1, placed in a ball mill, and subjected to wet crushing for 10 minutes. As a result, the removal rate of deposits is approximately 90%.
This value was higher than that of the dry crushing method described above, and it was confirmed from the analysis results of the exfoliated materials that there was almost no pulverization of the sand itself in the presence of water. When water-soluble substances are dissolved and removed, sand particles and other insoluble substances lose their adhesive connections to water and become fragmented, and even if these particles are connected, they become hard, spongy, hollow mesh-like particles that easily become particles when struck. This is the result. In addition, in order to increase the peeling rate, if the sand surface after wet crushing is washed with fresh water or with overwater of the treated water that has not reached saturation, the peeling rate will be higher. You can expect it. Furthermore, when the solubility of Glauber's salt (Na 2 SO 4 , IOH 2 O) in water, that is, the amount dissolved in 1000 grams of water, is expressed in grams, the curve shown in Figure 1 is shown. The horizontal axis is the liquid temperature and the vertical axis is the amount of dissolved Glauber's salt. As can be seen from the drawing, there is a peak at approximately 33°C. On the other hand, as shown in Table 1, about 50% of the deposits on the fluid medium are Na 2 SO 4 , so the treated water is kept at 30°C.
It can be seen that the use of the above substances is effective in dissolving and removing them. The fluid medium is polyhedral and has concavities, but the deposits are V 2 O 5 , Al 2 O 3 ,
It is estimated that it forms a hard spongy body whose main components are Fe 2 O 3 and NiO, and this combination, with the skeleton filled with Glauber's salt, is the reason for the formation of a strongly elastic deposit. being thought about. Therefore, when dissolving in water to remove Glauber's salt, the hard spongy bodies are easily crushed and the fluidized medium can be returned to a state free of deposits. FIG. 2 is a drawing showing the arrangement flow of the apparatus according to the present invention. A fluidized medium that overflows or is extracted from a fluidized bed incinerator 1 that incinerates EP ash and that requires regeneration and has sticky substances attached thereto is sent to a crusher 2 through a pipe 11. Conduit 2
From No. 1, the unsaturated liquid of the sticky material is sent with water or the water used in the recycling treatment, and a mechanical force is applied as a crushing blow to peel off the sticky material, and stirring is performed. The medium that has remained in the crusher 2 for a certain period of time is sent to the separator 3 through a pipe 22.
Sent by. In the separator 3, a fluid medium such as sand and a slurry, which is a mixture of a solution of a water-soluble substance and a particulate insoluble substance, are separated. The treated fluidized medium is sent to the fluidized bed incinerator 1 through a pipe 31 and reused. The slurry is discharged from the pipe 32, concentrated or dried by the exhaust gas from the fluidized bed incinerator 1, and V 2 O 5 and the like are effectively utilized. By carrying out the present invention, it is possible to circulate and supply a fluidized medium in which sticky substances that hinder the formation of a fluidized bed in a fluidized bed incinerator are efficiently removed, thereby achieving stable incineration processing. This has various effects such as reducing the amount of media consumed, recovering V 2 O 5 , preventing a decrease in equipment efficiency due to shutdown, and eliminating the need for workers.
第1図は芒硝の水に対する溶解度と液温の関係
図、第2図はこの発明の実施にかかる装置の配置
と管路を示す図面である。
1……流動層焼却炉、2……破砕機、3……分
離機、11,21,22,31,32……管路。
FIG. 1 is a diagram showing the relationship between the solubility of Glauber's salt in water and the liquid temperature, and FIG. 2 is a diagram showing the arrangement of an apparatus and pipe lines according to the present invention. 1... Fluidized bed incinerator, 2... Crusher, 3... Separator, 11, 21, 22, 31, 32... Pipe line.
Claims (1)
及び水不溶性物質を含む付着物を付着した流動媒
体を、連続的または不連続的に抜き出し、前記媒
体を水で洗浄し、さらに機械的作用を与えること
により前記不着物を剥離除去することを特徴とす
る流動媒体再生方法。1. The fluidized medium used in the operating fluidized bed reactor and which has deposits containing water-soluble and water-insoluble substances is continuously or discontinuously extracted, the medium is washed with water, and further subjected to mechanical action. A method for regenerating a fluid medium, characterized in that the adhering matter is peeled off and removed by applying the following.
Priority Applications (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP11070978A JPS5538415A (en) | 1978-09-11 | 1978-09-11 | Regeneration, supply, and operation of fluidic medium |
| DE19792935687 DE2935687A1 (en) | 1978-09-08 | 1979-09-04 | Regeneration of fluidised bed granulate esp. from combustion furnace - by washing off adhering material in water or dilute soln. of adhering material |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP11070978A JPS5538415A (en) | 1978-09-11 | 1978-09-11 | Regeneration, supply, and operation of fluidic medium |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5538415A JPS5538415A (en) | 1980-03-17 |
| JPS638366B2 true JPS638366B2 (en) | 1988-02-22 |
Family
ID=14542464
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP11070978A Granted JPS5538415A (en) | 1978-09-08 | 1978-09-11 | Regeneration, supply, and operation of fluidic medium |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5538415A (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP5721251B2 (en) * | 2010-06-03 | 2015-05-20 | 株式会社タクマ | How to recycle spent sand in a fluidized bed furnace |
| CN106196029A (en) * | 2016-08-30 | 2016-12-07 | 江苏汇能锅炉有限公司 | A kind of cycle of higher pressure fluidized-bed combustion boiler |
-
1978
- 1978-09-11 JP JP11070978A patent/JPS5538415A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5538415A (en) | 1980-03-17 |
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