JP4340190B2 - Unburned carbon separator and separation method - Google Patents

Unburned carbon separator and separation method Download PDF

Info

Publication number
JP4340190B2
JP4340190B2 JP2004152631A JP2004152631A JP4340190B2 JP 4340190 B2 JP4340190 B2 JP 4340190B2 JP 2004152631 A JP2004152631 A JP 2004152631A JP 2004152631 A JP2004152631 A JP 2004152631A JP 4340190 B2 JP4340190 B2 JP 4340190B2
Authority
JP
Japan
Prior art keywords
unburned carbon
electrode
sieve
coal ash
carbon
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 - Fee Related
Application number
JP2004152631A
Other languages
Japanese (ja)
Other versions
JP2005066591A (en
Inventor
康弘 真弓
淳之 齊田
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.)
Nippon Steel Corp
Original Assignee
Nippon Steel 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 Nippon Steel Corp filed Critical Nippon Steel Corp
Priority to JP2004152631A priority Critical patent/JP4340190B2/en
Publication of JP2005066591A publication Critical patent/JP2005066591A/en
Application granted granted Critical
Publication of JP4340190B2 publication Critical patent/JP4340190B2/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Description

本発明は、石炭灰に含まれる未燃炭素を分離する装置および分離方法に関する。
具体的には、例えば石炭焚火力発電所のボイラーなどで発生する石炭灰に含まれる未燃炭素を分離する装置および分離方法に関する。
The present invention relates to an apparatus and a separation method for separating unburned carbon contained in coal ash.
Specifically, the present invention relates to an apparatus and a separation method for separating unburned carbon contained in coal ash generated in, for example, a boiler of a coal-fired thermal power plant.

例えば石炭焚火力発電所のボイラーなどで発生する石炭灰には約20%以上の未燃炭素が含まれており、この未燃炭素を分離・回収してエネルギー源として用いることが検討されており、従来から種々の提案がなされている。
例えば、特開2003−126832号公報の第0013欄には、静電向流ベルト式の分離装置が開示されている。
この分離装置は、隙間を隔てて上下対方向に配置された電極の中を、有孔の無端ベルトを循環移動させながら、電極の隙間に投入した石炭灰の粒子を表面接触により研磨帯電させ静電気力で未燃炭素を分離するものである。
しかし、特開2003−126832号公報に開示された装置は、無端ベルトを循環移動させながら石炭灰の粒子と表面接触させているためにベルトの磨耗が激しく1回/月の頻度で取り替える必要がありメンテナンスコストが高くなるという問題点があった。
For example, coal ash generated in boilers of coal-fired thermal power plants contains about 20% or more of unburned carbon, and it has been studied to separate and recover this unburned carbon and use it as an energy source. Conventionally, various proposals have been made.
For example, the electrostatic countercurrent belt type separation device is disclosed in column 0013 of JP-A-2003-126732.
This separation device uses a surfaceless contact to electrostatically charge coal ash particles introduced into the gap between the electrodes while circulating and moving a perforated endless belt through the electrodes arranged in a vertical direction with a gap. The unburned carbon is separated by force.
However, since the apparatus disclosed in Japanese Patent Application Laid-Open No. 2003-126732 is in contact with the coal ash particles while circulating the endless belt, the belt is worn out and needs to be replaced once a month. There was a problem that the maintenance cost was high.

また、同じく、特開2003−126832号公報の第0104欄〜第105欄には、サイクロン式の分離装置が開示されている。
この分離装置は、円筒円錐形のケーシングとその内部に設けられ高速回転する分級羽根とから構成されており、上部投入口から投入された石炭灰は遠心力と分級羽根の内部へ向かう空気流の抗力との釣り合い粒径の違いにより未燃炭素を分級するものである。
しかし、この方式についても駆動部があり磨耗の問題が発生する。更には、粒径の違いを利用した分級方式であるので積極的に未燃炭素を分離するものではなく、本発明者らの実験によると、炭素濃度が34%以上の分離効率を達成することは原理的に困難だった。
特開2003−126832号公報
Similarly, columns 0104 to 105 of JP-A-2003-126732 disclose cyclone-type separation devices.
This separation device is composed of a cylindrical conical casing and a classification blade that rotates at a high speed inside the casing, and the coal ash charged from the upper charging port has a centrifugal force and an air flow toward the inside of the classification blade. The unburned carbon is classified by the difference in the particle size in balance with the drag.
However, this method also has a drive part and causes a problem of wear. Furthermore, since it is a classification method using the difference in particle size, it does not actively separate unburned carbon, and according to the experiments by the present inventors, it achieves a separation efficiency with a carbon concentration of 34% or more. Was difficult in principle.
JP 2003-126732 A

本発明は、前述のような従来技術の問題点を解決し、未燃炭素を効率よく回収することでエネルギーコスト削減を行うことができるうえ、未燃炭素を分離・除去した石炭灰を例えばコンクリートの副原料として再利用することができる未燃炭素分離装置および分離方法を提供することを課題とする。   The present invention solves the problems of the prior art as described above, and can reduce the energy cost by efficiently recovering the unburned carbon, and further, coal ash from which unburned carbon is separated and removed, for example, concrete It is an object of the present invention to provide an unburned carbon separation device and a separation method that can be reused as a secondary raw material.

本発明は、前述の課題を解決するために、鋭意検討の結果なされたものであり、電圧を印加してプラスに帯電させた篩網と該篩網を振動させる振動枠とを備えた超音波篩と、電圧を印加してプラスに帯電させた板電極とマイナスに帯電させた棒電極または板電極を備えた電気集塵機とを設けることにより、未燃炭素を効率よく回収することでエネルギーコスト削減を行うことができるうえ、未燃炭素を分離・除去した石炭灰を例えばコンクリートの副原料として再利用することができる未燃炭素分離装置および分離方法を提供するものであり、その要旨とするところは、特許請求の範囲に記載した通りの下記内容である。
(1)石炭灰に含まれる未燃炭素を分離する装置であって、電圧を印加してプラスに帯電させた篩網と該篩網を振動させる振動枠とを備えた超音波篩と、電圧を印加してプラスに帯電させた電極を備えた電気集塵機とを有することを特徴とする未燃炭素分離装置。
(2)前記電極が屈曲路または湾曲路を形成していることを特徴とする(1)に記載の未燃炭素分離装置。
(3)さらに、電圧を印加してプラスに帯電させた網電極フィルターを有することを特徴とする(1)または(2)に記載の未燃炭素分離装置。
(4)前記振動枠を振動させる振動子に絶縁体を装入することを特徴とする請(1)乃至(3)に記載の未燃炭素分離装置。
(5)(1)または(2)に記載の未燃炭素分離装置を用いる未燃炭素分離方法であって、前記石炭灰を前記篩網に通過させることにより、該石炭灰に含まれる未燃炭素をプラスに帯電させ、炭素以外の鉱物の表面に分極を発生させることにより、該鉱物のみを前記電極に捕捉することを特徴とする未燃炭素分離方法。
(6)(3)または(4)に記載の未燃炭素分離装置を用いる未燃炭素分離方法であって、前記石炭灰を前記網電極フィルターに通過させることにより、前記未燃炭素と炭素以外の鉱物とを引き離して該鉱物のみを前記網電極フィルターに捕捉することを特徴とする未燃炭素分離方法。
The present invention has been made as a result of intensive studies in order to solve the above-mentioned problems, and an ultrasonic wave comprising a sieve mesh that is positively charged by applying a voltage and a vibration frame that vibrates the sieve mesh. Energy costs are reduced by efficiently collecting unburned carbon by providing a sieve and a positively charged plate electrode and an electrostatic precipitator equipped with a negatively charged rod or plate electrode. In addition, coal ash from which unburned carbon has been separated and removed can be reused as, for example, a secondary material for concrete, and an unburned carbon separation device and a separation method are provided. Is the following content as described in the claims.
(1) An apparatus for separating unburned carbon contained in coal ash, an ultrasonic sieve having a sieve mesh that is positively charged by applying a voltage and a vibration frame that vibrates the sieve mesh, and a voltage And an electrostatic precipitator equipped with an electrode charged positively by applying an unburned carbon separator.
(2) The unburned carbon separator according to (1), wherein the electrode forms a curved path or a curved path.
(3) The unburned carbon separator according to (1) or (2), further comprising a mesh electrode filter that is positively charged by applying a voltage.
(4) The unburned carbon separator according to any one of (1) to (3), wherein an insulator is inserted into a vibrator that vibrates the vibration frame.
(5) An unburned carbon separation method using the unburned carbon separation device according to (1) or (2), wherein unburned carbon contained in the coal ash by passing the coal ash through the sieve mesh. A method for separating unburned carbon, wherein carbon is charged positively and polarization is generated on the surface of a mineral other than carbon, whereby only the mineral is captured by the electrode.
(6) An unburned carbon separation method using the unburned carbon separator according to (3) or (4), wherein the coal ash is passed through the mesh electrode filter, so that the non-burned carbon and carbon other than carbon A method for separating unburned carbon, wherein the mineral is separated from the mineral and only the mineral is captured by the mesh electrode filter.

本発明は、前述の課題を解決するために、鋭意検討の結果なされたものであり、電圧を印加してプラスに帯電させた篩網と該篩網を振動させる振動枠とを備えた超音波篩と、電圧を印加してプラスに帯電させた板電極とマイナスに帯電させた棒電極を備えた電気集塵機とを設けることにより、未燃炭素を効率よく回収することでエネルギーコスト削減を行うことができるうえ、未燃炭素を分離・除去した石炭灰を例えばコンクリートの副原料として再利用することができる未燃炭素分離装置および分離方法を提供するものであり、その要旨とするところは、特許請求の範囲に記載した通りの下記内容である。
(1)石炭灰に含まれる未燃炭素を分離する装置であって、電圧を印加してプラスに帯電させた篩網と該篩網を振動させる振動枠とを備えた超音波篩と、前記超音波篩の後段に設置され電圧を印加してプラスに帯電させた電極を備えた電気集塵機と、該電気集塵機の後段に設置され電圧を印加してプラスに帯電させた網電極フィルターとを有することを特徴とする未燃炭素分離装置。
(2)前記電極が屈曲路または湾曲路を形成していることを特徴とする(1)に記載の未燃炭素分離装置。
(3)前記振動枠を振動させる振動子に絶縁体を装入することを特徴とする(1)または(2)に記載の未燃炭素分離装置。
(4)(1)または(2)に記載の未燃炭素分離装置を用いる未燃炭素分離方法であって、前記石炭灰を前記篩網に通過させることにより、該石炭灰に含まれる未燃炭素をプラスに帯電させ、炭素以外の鉱物の表面に分極を発生させることにより、該鉱物のみを前記電極に捕捉することを特徴とする未燃炭素分離方法。
(5)(1)〜(3)の何れかに記載の未燃炭素分離装置を用いる未燃炭素分離方法であって、前記石炭灰を前記電極フィルターに通過させることにより、前記未燃炭素と炭素以外の鉱物とを引き離して該鉱物のみを前記網電極フィルターに捕捉することを特徴とする未燃炭素分離方法。
The present invention has been made as a result of intensive studies in order to solve the above-mentioned problems, and an ultrasonic wave comprising a sieve mesh that is positively charged by applying a voltage and a vibration frame that vibrates the sieve mesh. Reduce energy costs by efficiently collecting unburned carbon by providing a sieve and an electrostatic precipitator equipped with a positively charged plate electrode and a negatively charged rod electrode. In addition, coal ash from which unburned carbon is separated and removed can be reused, for example, as a secondary raw material for concrete. It is the following contents as described in the claims.
(1) An apparatus for separating the unburned carbon contained in coal ash, the ultrasonic sieve and a vibration frame for vibrating the sieve screen and sieve network has been positively charged by applying a voltage, the An electrostatic precipitator having an electrode that is installed after the ultrasonic sieve and is positively charged by applying a voltage, and a mesh electrode filter that is installed after the electrostatic precipitator and is positively charged by applying a voltage. An unburned carbon separator.
(2) The unburned carbon separator according to (1), wherein the electrode forms a curved path or a curved path.
(3) The unburned carbon separator according to (1) or (2), wherein an insulator is inserted into a vibrator that vibrates the vibration frame.
(4) An unburned carbon separation method using the unburned carbon separator according to (1) or (2), wherein unburned carbon contained in the coal ash by passing the coal ash through the sieve mesh. A method for separating unburned carbon, wherein carbon is charged positively and polarization is generated on the surface of a mineral other than carbon, whereby only the mineral is captured by the electrode.
(5) An unburned carbon separation method using the unburned carbon separator according to any one of (1) to (3) , wherein the unburned carbon is obtained by passing the coal ash through the mesh electrode filter. And separating minerals other than carbon and capturing only the minerals in the mesh electrode filter.

本発明の実施形態について、図1乃至図8を用いて詳細に説明する。
図1および図2は、本発明の未燃炭素分離装置の実施形態を例示する図であり、図1は上面から見た平面図を示し、図2は側面図を示す。
図1および図2において、1は超音波篩、2は電気集塵機、3は網電極フィルター、4はサイクロン、5は篩網、6は振動枠、7は棒電極、8は板電極、9は振動子を示す。
Embodiments of the present invention will be described in detail with reference to FIGS.
FIG. 1 and FIG. 2 are diagrams illustrating an embodiment of the unburned carbon separation device of the present invention. FIG. 1 shows a plan view seen from above, and FIG. 2 shows a side view.
1 and 2, 1 is an ultrasonic sieve, 2 is an electrostatic precipitator, 3 is a mesh electrode filter, 4 is a cyclone, 5 is a sieve mesh, 6 is a vibrating frame, 7 is a rod electrode, 8 is a plate electrode, 9 is A vibrator is shown.

まず、石炭焚火力発電所のボイラーなどで発生する未燃炭素を約20%以上含む石炭灰を、超音波篩1に通過(接触)させる。
超音波篩1には、電圧を印加してプラスに帯電させた篩網5と該篩網5を振動させる振動枠6とが備えられており、振動子9が振動することによって、振動枠6および篩網5が微小振動して、凝縮している石炭灰を分散させるとともに、未燃炭素をプラスに帯電させることができる。
本発明においては、超音波篩1の目開きおよび振動周波数は問わないが、粒径の小さい石炭灰を効率よく分散させるためには、目開きは200μm以下、振動周波数は20kHz程度が好ましい。
次に、分散された石炭灰は、電圧を印加してプラスに帯電させた板電極8とマイナスに帯電させた棒電極7とを備えた電気集塵機2に導入される。
プラスに帯電した未燃炭素は、プラスに帯電した板電極8と反発して電気集塵機2を通過するが、未燃炭素以外の鉱物の表面には分極が発生するため、鉱物のみがプラスに帯電した板電極8に吸引されて捕捉される。
First, coal ash containing about 20% or more of unburned carbon generated in a boiler of a coal-fired thermal power plant is passed (contacted) through the ultrasonic sieve 1.
The ultrasonic sieve 1 is provided with a sieve mesh 5 that is positively charged by applying a voltage and a vibration frame 6 that vibrates the sieve mesh 5. In addition, the sieve screen 5 vibrates slightly to disperse the condensed coal ash and to positively charge the unburned carbon.
In the present invention, the opening and vibration frequency of the ultrasonic sieve 1 are not limited, but in order to efficiently disperse coal ash having a small particle size, the opening is preferably 200 μm or less and the vibration frequency is preferably about 20 kHz.
Next, the dispersed coal ash is introduced into an electric dust collector 2 having a plate electrode 8 that is positively charged by applying a voltage and a bar electrode 7 that is negatively charged.
The positively charged unburned carbon repels the positively charged plate electrode 8 and passes through the electrostatic precipitator 2. However, since the surface of the mineral other than the unburned carbon is polarized, only the mineral is positively charged. The plate electrode 8 is sucked and captured.

図3は、本発明によって未燃炭素が分離されるメカニズムを説明する模式図である。
石炭灰に含まれる未燃炭素(C)は導電率の高い物質(良導体)なので、篩網5と接触した際に接地した篩網5を通じて良導体中の動電子(マイナスの電荷)が漏洩するため、図3に示すように、プラスの電荷が表面を支配することになる。
プラスに帯電した未燃炭素(C)は、プラスに帯電した板電極8と反発することによって、電気集塵機2を通過する。
一方、未燃炭素(C)以外の鉱物は、非常に電気を通しにくい物質(絶縁体)なので、マイナスの電荷の漏洩が瞬時に行われず、その結果、絶縁体表面にプラスとマイナスの電荷が存在する分極が発生し、図3に示すように、板電極8に吸引されて捕捉される。
また、鉱物の一部は、篩網5を通過後すでにプラスに帯電した未燃炭素(C)に吸引されて結合するため、板電極8に捕捉されないで電気集塵機2を通過してしまう。
そこで、未燃炭素(C)の分離効率をさらに高めるためには、さらに、電圧を印加してプラスに帯電させた網電極フィルター3を設けることが好ましい。
FIG. 3 is a schematic diagram illustrating the mechanism by which unburned carbon is separated according to the present invention.
Since unburned carbon (C) contained in coal ash is a highly conductive substance (good conductor), moving electrons (negative charges) in the good conductor leak through the grounded mesh screen 5 when in contact with the screen mesh 5. As shown in FIG. 3, positive charges dominate the surface.
The positively charged unburned carbon (C) passes through the electrostatic precipitator 2 by repelling the positively charged plate electrode 8.
On the other hand, minerals other than unburned carbon (C) are substances (insulators) that are extremely difficult to conduct electricity, so negative charges do not leak instantaneously, resulting in positive and negative charges on the insulator surface. The existing polarization occurs and is attracted and captured by the plate electrode 8 as shown in FIG.
In addition, some of the minerals are attracted to and bonded to the unburned carbon (C) that has already been positively charged after passing through the sieve mesh 5, and thus pass through the electrostatic precipitator 2 without being captured by the plate electrode 8.
Therefore, in order to further increase the separation efficiency of unburned carbon (C), it is preferable to further provide a mesh electrode filter 3 that is positively charged by applying a voltage.

図4は、網電極フィルター3によって、未燃炭素(C)が分離されるメカニズムを説明する模式図である。
電気集塵機2を通過した未燃炭素(C)と結合した鉱物は、プラスに帯電した網電極フィルター3に接触しながら通過する際に、未燃炭素(C)から切り離されて、網電極フィルター3に吸引されて捕捉され、分離された未燃炭素(C)は、プラスに帯電しているため、プラスに帯電した網電極フィルター3と反発して通過する。
本発明においては、この網電極フィルター3の目開きは問わないが、石炭灰が通過する際の圧損を小さくするため、この目開きは2〜3mmが好ましい。
分離された未燃炭素(C)は、サイクロン4によって、さらに空気と分離されて炭素粉として回収することができ、エネルギー源として利用することができる。
また、未燃炭素が除去された鉱物は、例えばコンクリートの副原料として再利用することができる。
なお、本発明に用いる超音波篩、電気集塵機、網電極フィルターの印加電圧は問わないが、未燃炭素(C)の分離効率を高めるためには、1KV〜50KVが好ましい。
FIG. 4 is a schematic diagram for explaining a mechanism by which unburned carbon (C) is separated by the mesh electrode filter 3.
The mineral combined with the unburned carbon (C) that has passed through the electrostatic precipitator 2 is separated from the unburned carbon (C) when passing through the positively charged mesh electrode filter 3 in contact with the mesh electrode filter 3. The unburned carbon (C) that has been sucked in, captured, and separated is positively charged and repels and passes through the positively charged mesh electrode filter 3.
In this invention, although the mesh opening of this mesh electrode filter 3 is not ask | required, in order to make the pressure loss at the time of coal ash pass, this mesh opening has preferable 2-3 mm.
The unburned carbon (C) thus separated can be further separated from the air by the cyclone 4 and recovered as carbon powder, and can be used as an energy source.
The mineral from which unburned carbon has been removed can be reused as, for example, a secondary material for concrete.
In addition, although the applied voltage of the ultrasonic sieve, electrostatic precipitator, and mesh electrode filter used for this invention is not ask | required, in order to improve the separation efficiency of unburned carbon (C), 1 KV-50 KV are preferable.

図5は、本発明に用いる振動枠を振動させる振動子の取り付け状況を示す詳細図である。
図5において、6は振動枠、9は振動子、10は絶縁体を示す。
振動枠6を振動させる振動子9に高電圧を印加すると、超音波篩用直流電源と振動子用の直流電源との間に電流路が発生し電源を破損する場合がある。
そこで図5に示すように、振動子9の中央部に絶縁体10を装入することによって、超音波篩用直流電源と振動子用の直流電源との間の電流路を遮断することができ、電源の破損を防止することができる。
絶縁体の種類は問わないが、強度および耐電圧の観点からセラミックスを用いることが好ましい。
FIG. 5 is a detailed view showing an attachment state of a vibrator that vibrates a vibration frame used in the present invention.
In FIG. 5, 6 is a vibration frame, 9 is a vibrator, and 10 is an insulator.
When a high voltage is applied to the vibrator 9 that vibrates the vibration frame 6, a current path may be generated between the ultrasonic sieve DC power supply and the vibrator DC power supply, and the power supply may be damaged.
Therefore, as shown in FIG. 5, by inserting an insulator 10 in the center of the vibrator 9, the current path between the ultrasonic sieve DC power supply and the vibrator DC power supply can be interrupted. Can prevent damage to the power supply.
The type of insulator is not limited, but it is preferable to use ceramics from the viewpoint of strength and withstand voltage.

図6乃至図8は、本発明に用いる電気集塵機の電極を、くの字にして屈曲路を形成した実施形態を示す図であり、図6は平面図、図7は側面図、図8は電極の模式図である。
図6乃至図8において、1は超音波篩、2は電気集塵機、4はサイクロン、5は篩網、6は振動枠、9は振動子、11はくの字電極を示す。
図6および図7に示すように、電気集塵機2に設置する電極に曲げ加工を加えた複数のくの字電極11にして屈曲路を形成し、プラス電極(+)とマイナス電極(−)を交互に配置する。
図8は、くの字電極の内部の石炭灰および炭素の動きを示す模式図である。
図8に示すように、炭素はくの字電極と反発するため、電極を通り抜けて回収されるが、石炭灰はくの字に曲がった電極の間を通る際に電極面に衝突して捕捉されるため、炭素の分離回収率を向上させることができる。
本実施形態では、図6に示すように電極をくの字にして屈曲路を形成しているが、炭素灰および炭素が電極に衝突すればよいので、例えばS字状にして湾曲路を形成させても同等の効果が得られる。
6 to 8 are diagrams showing an embodiment in which the electrode of the electrostatic precipitator used in the present invention is formed in a U-shape, and a curved path is formed. FIG. 6 is a plan view, FIG. 7 is a side view, and FIG. It is a schematic diagram of an electrode.
6 to 8, 1 is an ultrasonic sieve, 2 is an electrostatic precipitator, 4 is a cyclone, 5 is a sieve mesh, 6 is a vibrating frame, 9 is a vibrator, and 11 is a square electrode.
As shown in FIG. 6 and FIG. 7, a bent path is formed by forming a plurality of dog-shaped electrodes 11 obtained by bending the electrodes installed in the electrostatic precipitator 2, and positive electrodes (+) and negative electrodes (−) are formed. Place them alternately.
FIG. 8 is a schematic diagram showing the movement of coal ash and carbon inside the cross-shaped electrode.
As shown in FIG. 8, the carbon foil repels the electrode and is collected through the electrode, but the coal ash collides with the electrode surface when passing between the bent electrodes. Therefore, the carbon separation and recovery rate can be improved.
In this embodiment, as shown in FIG. 6, the electrode is formed in a U shape to form a curved path. However, since carbon ash and carbon only have to collide with the electrode, the curved path is formed in an S shape, for example. Even if it is made, the same effect is obtained.

なお、電極に捕捉された石炭灰が堆積していくと炭素の分離効果が現象するので、図9に示すような振動子9、9´および簡易ノッカー12を設けることにより、くの字電極に超音波振動または単発的振動を加えることによって捕捉された石炭灰を除去することが好ましい。
具体的には、電極が3枚以上の場合には、中間部の電極への振動付与が非常に困難であるため、図10に示すように超音波振動子9と簡易ノッカー12による単発的振動との併用で実施することが好ましい。
更には、電極が2枚の場合には、図11に示すように、くの字電極の側面に超音波振動子9´を設けて両サイドから超音波振動を付与することが好ましい。
但し、図10、図11での超音波振動子を取付ける場合には、振動子に絶縁体を挿入て絶縁対策を行うことが好ましい。
In addition, as the coal ash trapped on the electrode accumulates, the carbon separation effect occurs, so by providing the vibrators 9, 9 'and the simple knocker 12 as shown in FIG. It is preferable to remove the captured coal ash by applying ultrasonic vibrations or single vibrations.
Specifically, when there are three or more electrodes, it is very difficult to apply vibration to the intermediate electrode, so that the single vibration by the ultrasonic vibrator 9 and the simple knocker 12 is shown in FIG. It is preferable to implement in combination with.
Furthermore, when there are two electrodes, as shown in FIG. 11, it is preferable to provide an ultrasonic transducer 9 'on the side surface of the U-shaped electrode and apply ultrasonic vibration from both sides.
However, when the ultrasonic vibrator shown in FIGS. 10 and 11 is attached, it is preferable to take insulation measures by inserting an insulator into the vibrator.

本発明の未燃炭素分離装置および分離方法を、下記条件にて実施した。
<実験条件1>
・石炭灰の粒径:10〜150μm
・超音波篩の目開き:80μm
・超音波篩の周波数:20KHz
・超音波篩の印加電圧:10KV
・くの字電極の電圧:18KV
・くの字電極のキ゛ャッフ゜:35mm
上記の実験条件で電極が3枚の場合について、超音波振動と簡易ノッカーに
よる単発的振動確認実験を行なった結果を表1に示す。
実験方法として、超音波篩部から100gを投入して、篩上、電極付着、電極下、サイクロンでの回収量を測定することで評価を行なった。その結果、超音波振動だけでは電極に28g付着しており、除去効果が不充分であり、簡易ノッカーによる単発的振動を付与することで大幅に除去が可能なことが判明した。
また、同様に上記の実験条件で電極が2枚の場合について、両サイドから超
音波振動を付与する実験を行なってみた。この場合には、超音波振動のみで殆
ど除去できていることが理解できる。

Figure 0004340190
Figure 0004340190
<実験条件2> The unburned carbon separation device and separation method of the present invention were carried out under the following conditions.
<Experimental condition 1>
・ Coal ash particle size: 10-150μm
・ Opening of ultrasonic sieve: 80μm
・ Frequency of ultrasonic sieve: 20KHz
・ Applied voltage of ultrasonic sieve: 10KV
・ Void electrode voltage: 18KV
・ Cuff of electrode: 35mm
Table 1 shows the results of a single vibration confirmation experiment using ultrasonic vibration and a simple knocker for three electrodes under the above experimental conditions.
As an experimental method, 100 g was introduced from the ultrasonic sieving portion, and evaluation was performed by measuring the amount collected on the sieving, electrode adhesion, under the electrode, and cyclone. As a result, it was found that 28 g was attached to the electrode by ultrasonic vibration alone, and the removal effect was insufficient, and that removal was possible by applying a single vibration by a simple knocker.
Similarly, an experiment was conducted in which ultrasonic vibration was applied from both sides in the case of two electrodes under the above experimental conditions. In this case, it can be understood that it can be removed almost only by ultrasonic vibration.
Figure 0004340190
Figure 0004340190
<Experimental condition 2>

・石炭灰の粒径:10〜150μm
・超音波篩の目開き:80μm
・超音波篩の周波数:20kHz
・超音波篩、電気集塵機、網電極フィルターの印加電圧:4.7KV
・電気集塵機のサイズ:L300mm×W300mm×H200mm
・網電極フィルターの目開き:2mm
上記の実施条件で実施した結果を表3に示す。
表3において、石炭灰(原粉)は、本発明を実施する前の石炭灰を示し、未燃炭素を24%含んでいた。
本発明例1は、超音波振動網および電気集塵機を用いて未燃炭素を分離した結果であり、分離後の粉中の炭素(C)が43.2%まで上昇させることができた。
本発明例2は、超音波振動網、電気集塵機、および、網電極フィルターを用いて未燃炭素を分離した結果であり、分離後の粉中の炭素(C)が55.7%まで上昇させることができ、さらに、本発明例3は、電気集塵機中にくの字電極を用いた結果であり、分離後の粉中の炭素(C)が73%に達した。

Figure 0004340190
-Coal ash particle size: 10-150 μm
・ Opening of ultrasonic sieve: 80μm
・ Frequency of ultrasonic sieve: 20 kHz
・ Applied voltage of ultrasonic sieve, electrostatic precipitator, mesh electrode filter: 4.7KV
・ Size of electrostatic precipitator: L300mm × W300mm × H200mm
-Mesh electrode filter opening: 2 mm
Table 3 shows the results obtained under the above implementation conditions.
In Table 3, coal ash (raw powder) represents coal ash before carrying out the present invention, and contained 24% unburned carbon.
Invention Example 1 is a result of separating unburned carbon using an ultrasonic vibration net and an electric dust collector, and carbon (C) in the powder after separation could be increased to 43.2%.
Invention Example 2 is the result of separating unburned carbon using an ultrasonic vibration net, an electrostatic precipitator, and a net electrode filter, and the carbon (C) in the powder after separation is increased to 55.7%. In addition, Example 3 of the present invention is a result of using a square electrode in the electric dust collector, and the carbon (C) in the powder after separation reached 73%.
Figure 0004340190

本発明の未燃炭素分離装置の実施形態を例示する平面図である。It is a top view which illustrates an embodiment of an unburned carbon separation device of the present invention. 本発明の未燃炭素分離装置の実施形態を例示する側面図である。It is a side view which illustrates embodiment of the unburned carbon separation apparatus of this invention. 本発明によって未燃炭素が分離されるメカニズムを説明する模式図である。It is a schematic diagram explaining the mechanism by which unburned carbon is isolate | separated by this invention. 網電極フィルター3によって、未燃炭素(C)が分離されるメカニズムを説明する模式図である。It is a schematic diagram explaining the mechanism by which unburned carbon (C) is isolate | separated by the mesh electrode filter 3. FIG. 本発明に用いる振動枠を振動させる振動子の取り付け状況を示す詳細図である。It is detail drawing which shows the attachment condition of the vibrator which vibrates the vibration frame used for this invention. 本発明に用いる電気集塵機の電極を、くの字にした実施形態を示す平面図である。It is a top view which shows embodiment which made the electrode of the electrostatic precipitator used for this invention the character. 本発明に用いる電気集塵機の電極を、くの字にした実施形態を示す側面図である。It is a side view which shows embodiment which made the electrode of the electrostatic precipitator used for this invention the character. くの字電極の内部の石炭灰および炭素の動きを示す模式図である。It is a schematic diagram which shows the movement of the coal ash and carbon inside a square-shaped electrode. くの字電極に設置する超音波振動子および簡易ノッカーの配置図である。FIG. 5 is a layout view of an ultrasonic transducer and a simple knocker installed on a square electrode. くの字電極が3枚の場合の振動装置の模式図である。It is a schematic diagram of a vibration device in the case of three cross-shaped electrodes. くの字電極が2枚の場合の振動装置の模式図である。It is a schematic diagram of a vibration device in the case of two cross-shaped electrodes.

符号の説明Explanation of symbols

1 超音波篩、
2 電気集塵機、
3 網電極フィルター、
4 サイクロン、
5 篩網、
6 振動枠、
7 棒電極、
8 板電極
9 振動子
10 絶縁体
11 くの字電極
12 簡易ノッカー
13 振動子取付け台
1 ultrasonic sieve,
2 Electric dust collector,
3 mesh electrode filter,
4 Cyclone,
5 sieve mesh,
6 Vibration frame,
7 Rod electrode,
8 Plate electrode 9 Oscillator 10 Insulator 11 U-shaped electrode 12 Simple knocker 13 Oscillator mount

Claims (5)

石炭灰に含まれる未燃炭素を分離する装置であって、電圧を印加してプラスに帯電させた篩網と該篩網を振動させる振動枠とを備えた超音波篩と、前記超音波篩の後段に設置され電圧を印加してプラスに帯電させた電極を備えた電気集塵機と、該電気集塵機の後段に設置され電圧を印加してプラスに帯電させた網電極フィルターとを有することを特徴とする未燃炭素分離装置。 An apparatus for separating the unburned carbon contained in coal ash, the ultrasonic sieve and a vibration frame for vibrating the sieve screen and sieve network has been positively charged by applying a voltage, the ultrasonic sieve An electrostatic precipitator having a positively charged electrode installed at a subsequent stage, and a mesh electrode filter installed at a subsequent stage of the electrostatic precipitator and charged positively by applying a voltage. An unburned carbon separator. 前記電極が屈曲路または湾曲路を形成していることを特徴とする請求項1に記載の未燃炭素分離装置。   2. The unburned carbon separation device according to claim 1, wherein the electrode forms a curved path or a curved path. 前記振動枠を振動させる振動子に絶縁体を装入することを特徴とする請求項1または請求項2に記載の未燃炭素分離装置。   The unburned carbon separation device according to claim 1 or 2, wherein an insulator is inserted into a vibrator that vibrates the vibration frame. 請求項1または請求項2に記載の未燃炭素分離装置を用いる未燃炭素分離方法であって、前記石炭灰を前記篩網に通過させることにより、該石炭灰に含まれる未燃炭素をプラスに帯電させ、炭素以外の鉱物の表面に分極を発生させることにより、該鉱物のみを前記電極に捕捉することを特徴とする未燃炭素分離方法。   An unburned carbon separation method using the unburned carbon separation device according to claim 1 or 2, wherein the unburned carbon contained in the coal ash is added by passing the coal ash through the sieve mesh. A method for separating unburned carbon, wherein only the mineral is captured by the electrode by charging the surface of the mineral and generating polarization on the surface of the mineral other than carbon. 請求項1〜3の何れかに記載の未燃炭素分離装置を用いる未燃炭素分離方法であって、前記石炭灰を前記電極フィルターに通過させることにより、前記未燃炭素と炭素以外の鉱物とを引き離して該鉱物のみを前記網電極フィルターに捕捉することを特徴とする未燃炭素分離方法。 It is an unburned carbon separation method using the unburned carbon separation apparatus in any one of Claims 1-3, Comprising: By passing the coal ash through the mesh electrode filter, minerals other than the unburned carbon and carbon And separating only the minerals into the mesh electrode filter to separate the unburned carbon.
JP2004152631A 2003-08-01 2004-05-24 Unburned carbon separator and separation method Expired - Fee Related JP4340190B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2004152631A JP4340190B2 (en) 2003-08-01 2004-05-24 Unburned carbon separator and separation method

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
JP2003205248 2003-08-01
JP2004152631A JP4340190B2 (en) 2003-08-01 2004-05-24 Unburned carbon separator and separation method

Publications (2)

Publication Number Publication Date
JP2005066591A JP2005066591A (en) 2005-03-17
JP4340190B2 true JP4340190B2 (en) 2009-10-07

Family

ID=34425048

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2004152631A Expired - Fee Related JP4340190B2 (en) 2003-08-01 2004-05-24 Unburned carbon separator and separation method

Country Status (1)

Country Link
JP (1) JP4340190B2 (en)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102844380B (en) * 2010-04-14 2015-08-12 高桥玄策 Electroconductive thermoplastic resin
KR101402937B1 (en) 2012-06-22 2014-06-02 코카스엔텍 주식회사 A Method for floatation bottom ash from unburned coal
CN103706476A (en) * 2013-12-24 2014-04-09 戴若夫 Barrier type ultrasonic vibrator assembly for ultrasonic electrostatic filter
WO2018066079A1 (en) * 2016-10-04 2018-04-12 中国電力株式会社 Coal-fired power generation equipment

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5295183U (en) * 1976-01-14 1977-07-16
JPH0215564Y2 (en) * 1984-09-05 1990-04-26
WO2002076620A1 (en) * 2001-03-27 2002-10-03 Kawasaki Jukogyo Kabushiki Kaisha Method for electrostatically separating particles, apparatus for electrostatically separating particles, and processing system

Also Published As

Publication number Publication date
JP2005066591A (en) 2005-03-17

Similar Documents

Publication Publication Date Title
US5695549A (en) System for removing fine particulates from a gas stream
US8506687B2 (en) Electrostatic precipitator and self cleaning collection belt therefor
FI59030B (en) FOERFARANDE FOER RENING AV STOFTBEMAENGD GAS
JP3981014B2 (en) Method for electrostatic separation of particles
US8653394B2 (en) Electrostatic separation method and electrostatic separation device
CA2496381A1 (en) Grid type electrostatic separator/collector and method of using same
DE69933211D1 (en) METHOD AND DEVICE FOR SEPARATING PARTICLES FROM AN AIRFLOW
JPS6031547B2 (en) Electrostatic separation method and device for particles with different physical properties
JP4340190B2 (en) Unburned carbon separator and separation method
ATE25207T1 (en) METHOD AND DEVICE FOR SEPARATION OF GRAINY MATERIALS.
US3664092A (en) Collecting apparatus for electrostatic precipitators
JP2006043684A (en) Ash separator, ash separation method, and unburned carbon separation method using the same
WO2012139642A1 (en) Apparatus for removal of particulate matter from a gas
JP7425891B2 (en) electrostatic separator
JP3340282B2 (en) Electrostatic sorting device
WO2022085182A1 (en) Electrostatic separation device and method
US20110146486A1 (en) Collecting plate cleaning using resonant frequency wave application
KR19980074238A (en) Electrostatic Filtration Dust Collecting Method by Corona Discharge and Its Apparatus
WO2016125442A1 (en) Dust collector
JP2000140690A (en) Dry type dust collector
JP3413535B2 (en) Electric dust collector
SU1002012A1 (en) Electric cleaner
JPH07265736A (en) Electric precipitator
JPH0631201A (en) Electric precipitator and dust collecting electrode
JPH10235228A (en) Electrostatic sorting device

Legal Events

Date Code Title Description
A621 Written request for application examination

Free format text: JAPANESE INTERMEDIATE CODE: A621

Effective date: 20060907

A977 Report on retrieval

Free format text: JAPANESE INTERMEDIATE CODE: A971007

Effective date: 20080905

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20080916

A521 Written amendment

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20081027

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20090324

A521 Written amendment

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20090430

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: 20090623

A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

A61 First payment of annual fees (during grant procedure)

Free format text: JAPANESE INTERMEDIATE CODE: A61

Effective date: 20090703

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

Free format text: PAYMENT UNTIL: 20120710

Year of fee payment: 3

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

Free format text: PAYMENT UNTIL: 20130710

Year of fee payment: 4

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

Free format text: PAYMENT UNTIL: 20130710

Year of fee payment: 4

S531 Written request for registration of change of domicile

Free format text: JAPANESE INTERMEDIATE CODE: R313531

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

Free format text: PAYMENT UNTIL: 20130710

Year of fee payment: 4

R350 Written notification of registration of transfer

Free format text: JAPANESE INTERMEDIATE CODE: R350

S533 Written request for registration of change of name

Free format text: JAPANESE INTERMEDIATE CODE: R313533

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

Free format text: PAYMENT UNTIL: 20130710

Year of fee payment: 4

R350 Written notification of registration of transfer

Free format text: JAPANESE INTERMEDIATE CODE: R350

LAPS Cancellation because of no payment of annual fees