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JP6624451B2 - Waste treatment furnace equipment - Google Patents
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JP6624451B2 - Waste treatment furnace equipment - Google Patents

Waste treatment furnace equipment Download PDF

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JP6624451B2
JP6624451B2 JP2016069067A JP2016069067A JP6624451B2 JP 6624451 B2 JP6624451 B2 JP 6624451B2 JP 2016069067 A JP2016069067 A JP 2016069067A JP 2016069067 A JP2016069067 A JP 2016069067A JP 6624451 B2 JP6624451 B2 JP 6624451B2
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moisture content
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太一 薄木
太一 薄木
知広 傳田
知広 傳田
中山 剛
剛 中山
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JFE Engineering Corp
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Description

本発明は廃棄物の性状としての水分率を計測しその計測値に応じて廃棄物を焼却又はガス化する廃棄物処理炉装置に関する。   The present invention relates to a waste treatment furnace apparatus that measures the moisture content as the property of waste and incinerates or gasifies the waste according to the measured value.

近年、廃棄物焼却炉やガス化炉等の処理炉における廃棄物の焼却又はガス化処理によって発生する熱エネルギーの回収への関心が高まってきており、この熱エネルギーで駆動するボイラ発電設備が設置された廃棄物の処理炉が増加し、高い効率での熱回収を実現できる焼却又はガス化運転が要求されている。一方、廃棄物処理炉から大気中に放出される環境汚染物質の規制が厳しくなるに従い、ダイオキシン類や窒素酸化物など燃焼由来の有害物質の排出を低減する焼却又はガス化運転も必要とされている。   In recent years, there has been increasing interest in the recovery of thermal energy generated by incineration or gasification of waste in treatment furnaces such as waste incinerators and gasification furnaces, and boiler power generation equipment driven by this thermal energy has been installed. The number of waste treatment furnaces has increased, and there is a demand for incineration or gasification operation capable of realizing high-efficiency heat recovery. On the other hand, as regulations on environmental pollutants released into the atmosphere from waste treatment furnaces become more stringent, incineration or gasification operations that reduce emissions of combustion-derived harmful substances such as dioxins and nitrogen oxides are also required. I have.

このように、廃棄物処理炉に高度な燃焼運転制御が望まれているため、自動燃焼制御装置によって上記の要求を満たす運転制御が行われている。自動燃焼制御装置では、処理炉が例えばストーカ式焼却炉の場合、操作量である給塵速度、燃焼火格子送り速度、燃焼空気量、及び冷却空気量などを制御することにより、蒸気発生量を安定化し、かつ排ガス中のダイオキシン類や窒素酸化物濃度を低く抑え、灰中の未燃成分を少なくする目的で、廃棄物を安定して燃焼するように運転されている。しかしながら、このような燃焼制御は、廃棄物の投入の時点で該廃棄物の性状を監視せずに、いずれも燃焼の結果発生する燃焼ガス温度、燃焼ガス中酸素濃度、燃焼ガス中一酸化炭素濃度等を監視する因子として検出して、各操作量の制御値へフィードバックする方法であり、そのため後追い型の制御となり、処理炉に投入する廃棄物の性状が変動した場合に必ずしも安定した運転制御が達成できないことがある。   As described above, since advanced combustion operation control is desired for the waste treatment furnace, operation control that satisfies the above requirements is performed by an automatic combustion control device. In the automatic combustion control device, when the processing furnace is, for example, a stoker-type incinerator, the amount of generated steam is controlled by controlling the manipulated variables such as dust supply speed, combustion grate feed speed, combustion air amount, and cooling air amount. For the purpose of stabilizing, reducing the concentration of dioxins and nitrogen oxides in exhaust gas, and reducing unburned components in ash, it is operated to stably burn waste. However, such combustion control does not monitor the properties of the waste at the time of the input of the waste, and in each case, the combustion gas temperature, the oxygen concentration in the combustion gas, and the carbon monoxide in the combustion gas generated as a result of combustion. This method detects concentration as a monitoring factor and feeds it back to the control value of each manipulated variable.Therefore, it is a follow-up type control, and stable operation control is always necessary when the properties of waste to be fed into the processing furnace fluctuate. May not be achieved.

廃棄物処理炉の焼却又はガス化運転の安定性を乱す大きな要因として、投入される廃棄物の性状が一定しないため廃棄物の発熱量が変動するという点がある。処理炉へ投入される廃棄物の性状は、廃棄物が収集される地域や、収集される時刻、または天候や、季節によって大きく異なることから、廃棄物の発熱量は大きく変動する。そこで、投入される廃棄物の性状を投入前に求めて、求めた廃棄物の性状により運転制御を行う廃棄物処理炉の制御方法が特許文献1で提案されている。廃棄物の性状のうち、上記発熱量を大きく左右する因子は廃棄物の水分率であり、特許文献1の技術では、廃棄物焼却炉へ廃棄物を供給するコンベアに、コンベア上の廃棄物の重量を計測する重量計測装置と、コンベア上の廃棄物の厚みを計測するレベル計測装置と、コンベア上の廃棄物の水分含有率を計測する赤外線水分計を備え、これらの計測値から廃棄物の性状としての水分率を推定し、その性状に応じた運転制御を行うことが記載されている。また、特許文献2では、廃棄物処理炉の投入口から燃焼室へ向け垂下するシュートに水分率計として静電容量計を配置し、一対の電極間での廃棄物の静電容量を計測することで廃棄物の水分率を得ることとしている。   A major factor that disturbs the stability of the incineration or gasification operation of the waste treatment furnace is that the amount of heat generated by the waste varies because the properties of the waste input are not constant. The properties of the waste fed into the processing furnace vary greatly depending on the area where the waste is collected, the time at which the waste is collected, the weather, and the season, so that the calorific value of the waste greatly varies. Therefore, Patent Document 1 proposes a method of controlling a waste treatment furnace in which the properties of the waste to be input are obtained before the input and the operation control is performed based on the obtained properties of the waste. Among the properties of the waste, a factor that largely affects the calorific value is the moisture content of the waste. According to the technology of Patent Document 1, the conveyor that supplies the waste to the waste incinerator has A weight measuring device that measures the weight, a level measuring device that measures the thickness of the waste on the conveyor, and an infrared moisture meter that measures the moisture content of the waste on the conveyor are provided. It describes that a moisture content as a property is estimated and operation control is performed according to the property. Further, in Patent Document 2, a capacitance meter is arranged as a moisture content meter on a chute hanging from an inlet of a waste treatment furnace toward a combustion chamber, and the capacitance of the waste between a pair of electrodes is measured. In this way, the moisture content of the waste is obtained.

赤外線水分計は、赤外線を測定対象物に照射しその対象物からの赤外線の反射を検出して水分率を求めている。水分は近赤外線の特定波長を吸収する性質があり、測定対象物に含まれる水分量が多くなれば、吸収される赤外線エネルギーも大きくなり、反射する赤外線エネルギー量が減少する。赤外線水分計はこのような現象を応用して、測定対象物の水分含有率を測定するものである。   The infrared moisture meter irradiates an infrared ray to an object to be measured and detects reflection of the infrared ray from the object to obtain a moisture content. Moisture has the property of absorbing a specific wavelength of near-infrared light. If the amount of water contained in the measurement object increases, the absorbed infrared energy increases and the reflected infrared energy decreases. The infrared moisture meter measures the moisture content of the measurement object by applying such a phenomenon.

静電容量計は、静電容量の値と水分率との値の対応関係を保有している水分率算定器に接続されており、静電容量計で計測された計測値から上記対応関係に基づいて水分率を算定できるようになっている。   The capacitance meter is connected to a moisture content calculator that has a correspondence relationship between the value of the capacitance and the value of the moisture content, and the above-described correspondence relationship is obtained from the measurement value measured by the capacitance meter. Moisture percentage can be calculated based on this.

特開2000−283444JP-A-2000-283444 特開2010−216990JP 2010-216990 A

特許文献1に記載の技術では、コンベア上の廃棄物の重量とレベル(高さ)と水分率を計測し、廃棄物の性状を推定している。しかしながら、この技術では、廃棄物の水分率測定に赤外線水分計を用いて廃棄物表層部からの赤外線の反射を計測するため、廃棄物表層部の水分率しか計測できないという問題がある。したがって、表層部よりも下層の廃棄物の水分率が表層部と異なる場合には、不具合が生じることとなってしまう。   In the technique described in Patent Document 1, the weight, level (height), and moisture content of waste on a conveyor are measured to estimate the properties of the waste. However, this technique has a problem that only the moisture content of the surface layer of the waste can be measured because the infrared moisture meter is used to measure the reflection of infrared rays from the surface layer of the waste. Therefore, if the moisture content of the waste below the surface layer is different from that of the surface layer, a problem occurs.

また、特許文献2にあっては、シュート内の廃棄物の水分を静電容量計で測定しているが、炉内へ投入される廃棄物の種類や嵩密度が大きく変動する場合、水分率を正確に測定できない懸念がある。そのため、廃棄物の発熱量の正確な把握が行えず、発熱量の変動に対して廃棄物処理炉の運転条件の変更調整が十分に行えず、廃棄物処理炉を安定して運転できない、という問題が生じる。   Further, in Patent Document 2, the moisture of the waste in the chute is measured by a capacitance meter. However, when the type and bulk density of the waste to be introduced into the furnace vary greatly, the moisture content May not be able to measure accurately. As a result, it is not possible to accurately grasp the calorific value of the waste, and it is not possible to sufficiently change and adjust the operating conditions of the waste treatment furnace with respect to the fluctuation of the calorific value, so that the waste treatment furnace cannot be operated stably. Problems arise.

本発明は、かかる事情に鑑み、廃棄物処理炉へ投入供給される廃棄物の種類や嵩密度が変動しても、廃棄物の水分率を正確に測定し発熱量を正確に把握して、廃棄物の水分率そして発熱量に対応した廃棄物処理炉の運転条件の制御を容易とする廃棄物処理炉装置を提供することを課題とする。   In view of such circumstances, the present invention accurately measures the moisture content of the waste and accurately grasps the calorific value, even if the type or bulk density of the waste charged and supplied to the waste treatment furnace fluctuates, An object of the present invention is to provide a waste treatment furnace apparatus that facilitates control of operating conditions of the waste treatment furnace corresponding to the moisture content and the calorific value of the waste.

上述の課題は本発明によれば、次のように構成される第一発明あるいは第二発明のいずれの廃棄物処理炉装置によっても解決される。   According to the present invention, the above-mentioned object is attained by the waste treatment furnace apparatus of the first invention or the second invention configured as follows.

<第一発明>
廃棄物を焼却又はガス化する廃棄物処理炉の廃棄物投入口から下方に延びるシュート内に廃棄物の水分率と相関性を持つ廃棄物の特性値を測定する測定計の検出要素を設けた廃棄物処理炉装置において、
特性値の測定計に加え、該測定計による特性値の測定値に基づき廃棄物の水分率を算定する水分率算定装置を備え、
特性値の測定計は、静電容量測定計、マイクロ波強度測定計、赤外線強度測定計の三つの測定計のうち二つの測定計が選択され配設されており、これらの測定計の特性値の測定値を上記水分率算定装置へ送るようになっている、
ことを特徴とする廃棄物処理炉装置。
<First invention>
A detection element of a measuring instrument that measures the characteristic value of the waste that has a correlation with the moisture content of the waste is provided in a chute that extends downward from the waste input port of the waste treatment furnace that incinerates or gasifies the waste. In waste treatment furnace equipment,
In addition to the characteristic value measurement meter, comprising a moisture content calculation device that calculates the moisture content of the waste based on the measurement value of the characteristic value by the measurement device,
As for the characteristic value measuring instruments, two of the three measuring instruments of the capacitance measuring instrument, the microwave intensity measuring instrument, and the infrared intensity measuring instrument are selected and arranged, and the characteristic values of these measuring instruments are selected. The measured value of is to be sent to the moisture content calculating device,
Waste treatment furnace apparatus characterized by the above-mentioned.

本発明において、静電容量測定計としては、接触型静電容量測定計、透過型静電容量測定水分計、そしてマイクロ波強度測定計としては接触型マイクロ波強度測定計、透過型マイクロ波強度測定計が挙げられる。   In the present invention, as a capacitance meter, a contact capacitance meter, a transmission capacitance moisture meter, and as a microwave intensity meter, a contact microwave intensity meter, a transmission microwave intensity meter Measuring instrument.

本発明では、廃棄物の種類により、好ましい特性値の測定計の測定値(静電容量値、マイクロ波強度、赤外線強度)を選択・採用し水分率算定する。例えば、水分率が比較的高い廃棄物では静電容量、プラスチックごみが多い廃棄物ではマイクロ波強度、そして家庭からの収集ごみが多い廃棄物では静電容量、産業廃棄物と一般廃棄物(家庭からの収集ごみが主)との混合物では静電容量を選択するようにすることが好ましい。   In the present invention, the moisture content is calculated by selecting and adopting the measurement values (capacitance value, microwave intensity, infrared intensity) of the measuring device having preferable characteristic values depending on the type of waste. For example, waste with relatively high moisture regains capacitance, microwave intensities for waste with a lot of plastic garbage, and capacitance for waste with a lot of garbage collected from homes, industrial and municipal wastes (household and household waste). It is preferable to select the capacitance in a mixture with (i) mainly collected garbage from).

<第二発明>
廃棄物を焼却又はガス化する廃棄物処理炉の廃棄物投入口から下方に延びるシュート内に廃棄物の水分率と相関性を持つ廃棄物の特性値を測定する測定計の検出要素を設けた廃棄物処理炉装置において、
特性値の測定計に加え、該測定計による特性値の測定値に基づき廃棄物の水分率を算定する水分率算定装置を備え、
特性値の測定計は、測定計の検出要素と接触している廃棄物の特性値を測定する接触型測定計と、測定計の検出要素の間に存在している廃棄物を透過して特性値を測定する透過型測定計とが配設されており、これらの測定計の特性値の測定値を上記水分率算定装置へ送るようになっている、
ことを特徴とする廃棄物処理炉装置。
<Second invention>
A measuring element for measuring the characteristic value of the waste that correlates with the moisture content of the waste is installed in a chute that extends downward from the waste inlet of the waste treatment furnace that incinerates or gasifies the waste. In waste treatment furnace equipment,
In addition to the characteristic value measurement meter, comprising a moisture content calculation device that calculates the moisture content of the waste based on the measurement value of the characteristic value by the measurement device,
The characteristic value measurement meter is a contact type measurement device that measures the characteristic value of the waste that is in contact with the detection element of the measurement meter, and transmits the waste existing between the detection elements of the measurement meter. A transmission type measuring device for measuring the value is provided, and the measured value of the characteristic value of these measuring devices is to be sent to the moisture content calculating device,
Waste treatment furnace apparatus characterized by the above-mentioned.

本発明において、接触型測定計としては接触型静電容量測定計、接触型マイクロ波強度測定計、そして透過型測定計としては透過型静電容量測定計、透過型マイクロ波強度測定計が挙げられる。   In the present invention, the contact-type measuring instrument includes a contact-type capacitance measuring instrument, a contact-type microwave intensity measuring instrument, and the transmission-type measuring instrument includes a transmission-type capacitance measuring instrument and a transmission-type microwave intensity measuring instrument. Can be

本発明では、廃棄物の嵩密度により接触型測定計と透過型測定計とから、好ましい型式の測定計の特性値の測定値を採用し水分率算定する。例えば、嵩密度の高い廃棄物には、透過型測定計、そして嵩密度の低い廃棄物には、接触型測定計が好適である。嵩密度の低い廃棄物では廃棄物の空隙が多く透過型測定計では正確に水分率に相関する特性値を測定できないからである。   In the present invention, the moisture content is calculated based on the bulk density of the waste by using the measured values of the characteristic values of the preferred type of the meter from the contact type meter and the transmission type meter. For example, a transmission type meter is suitable for waste having a high bulk density, and a contact type meter is suitable for waste having a low bulk density. This is because waste having a low bulk density has many voids in the waste, and a transmission-type measurement device cannot accurately measure a characteristic value correlated with the moisture content.

以上のように、本発明では、第一発明にあっても、第二発明にあっても、複数の方式の測定計の検出要素をシュートに設け、廃棄物の種類や性状によって測定計の選定を行って適切に水分率を測定できるようにしたので、正確に廃棄物の水分率を測定でき、廃棄物の発熱量を正確に把握できるため、廃棄物処理炉の良好な燃焼又はガス化制御が行え、ひいては安定した運転制御が可能となる。   As described above, according to the present invention, in both the first invention and the second invention, the detection elements of the plurality of types of measurement meters are provided on the chute, and the selection of the measurement meters is determined according to the type and properties of the waste. The water content of waste can be measured accurately and the moisture content of waste can be measured accurately, and the calorific value of waste can be accurately grasped. And stable operation control can be achieved.

本発明の一実施形態装置の概要構成図である。FIG. 1 is a schematic configuration diagram of an apparatus according to an embodiment of the present invention.

図1は、廃棄物処理炉等としての火格子式廃棄物焼却炉1の構成を示す。本発明は、火格子式のみならず他の形式の廃棄物焼却炉にも、また廃棄物焼却炉に限定されず廃棄物ガス化溶融炉にも適用可能であり、以下、廃棄物焼却炉と廃棄物ガス化溶融炉の両者をあわせて、廃棄物処理炉と称することとする。   FIG. 1 shows a configuration of a grate-type waste incinerator 1 as a waste treatment furnace or the like. The present invention can be applied not only to the grate type but also to other types of waste incinerators, and not limited to the waste incinerator, but also to a waste gasification and melting furnace. Both of the waste gasification and melting furnaces are collectively referred to as a waste treatment furnace.

廃棄物焼却炉1は、火格子11の下方に接続して設けられた複数の空気供給系12から燃焼用空気を受け、上記火格子11の上方に形成される燃焼室13で火格子11上の廃棄物Pを焼却するようになっている。火格子11は右方に向けた送り速度で上記廃棄物Pを送っている。上記火格子11の左端上方位置には給塵装置14、例えばプッシャーがごみを火格子11上に送り出すように設けられている。該給塵装置14の上方にはシュート15が上方に延びており、その上端に投入口としてのホッパ16が設けられている。   The waste incinerator 1 receives combustion air from a plurality of air supply systems 12 connected below the grate 11, and a combustion chamber 13 formed above the grate 11 forms a combustion chamber 13 on the grate 11. Waste P is incinerated. The grate 11 sends the waste P at a feed speed toward the right. At a position above the left end of the grate 11, a dust supply device 14, for example, a pusher is provided so as to send out dust onto the grate 11. A chute 15 extends upward above the dust supply device 14, and a hopper 16 is provided at an upper end thereof as an input port.

上記空気供給系12での空気吹込み量、火格子11の送り速度、給塵装置14の送り出し速度は可変となっている。   The amount of air blown in the air supply system 12, the feed speed of the grate 11, and the feed speed of the dust supply device 14 are variable.

本実施形態では、上記シュート15内の廃棄物Pの静電容量を計測する静電容量測定計20A、マイクロ波強度を計測するマイクロ波強度測定計20Bが設けられている。静電容量測定計20Aは、検出要素20A1(例えば、静電容量の測定のための電極)を有し、マイクロ波強度測定計20Bは、マイクロ波強度検出要素20B1を有していて、各検出要素20A1,20B1は上記シュート15の側壁の内面に取り付けられている。かくして、静電容量測定計20A、マイクロ波強度測定計20Bは、シュート15内の検出要素20A1,20B1近傍に存在する廃棄物Pの静電容量、マイクロ波強度を測定する。   In the present embodiment, a capacitance measuring instrument 20A for measuring the capacitance of the waste P in the chute 15 and a microwave intensity measuring instrument 20B for measuring the microwave intensity are provided. The capacitance measuring instrument 20A has a detecting element 20A1 (for example, an electrode for measuring the capacitance), and the microwave intensity measuring instrument 20B has a microwave intensity detecting element 20B1, and each of the detecting elements 20A1 has a detecting element 20B1. The elements 20A1 and 20B1 are attached to the inner surface of the side wall of the chute 15. Thus, the capacitance meter 20A and the microwave intensity meter 20B measure the capacitance and the microwave intensity of the waste P present near the detection elements 20A1 and 20B1 in the chute 15.

上記静電容量測定計20A、マイクロ波強度測定計20Bは、水分率算定器21に接続されている。この水分率算定器21では、予め保有している廃棄物の静電容量の値と水分率の値との関係、マイクロ波強度の値と水分率の値との関係から、上記静電容量測定計20A、マイクロ波強度測定計20Bで計測された静電容量、マイクロ波強度の値から対応する水分率の値を算定できるようになっている。具体的には、水分率算定器21には、廃棄物の静電容量の値と水分率の値との関係、マイクロ波強度の値と水分率の値との関係を予め計測して明らかにした関係データベースが保持されており、静電容量測定計20A、マイクロ波強度測定計20Bから送られてきた廃棄物Pの静電容量、マイクロ波強度の測定値を、上記関係データベースにおける静電容量、マイクロ波強度と水分率との関係と照合して廃棄物の水分率を算定する。   The capacitance meter 20A and the microwave intensity meter 20B are connected to a moisture content calculator 21. The moisture content calculator 21 determines the capacitance from the relationship between the value of the capacitance of the waste and the value of the moisture ratio and the relationship between the value of the microwave intensity and the value of the moisture ratio, which are stored in advance. The value of the corresponding moisture percentage can be calculated from the values of the capacitance and the microwave intensity measured by the total 20A and the microwave intensity measuring meter 20B. Specifically, the moisture content calculator 21 preliminarily measures the relationship between the value of the capacitance of waste and the value of the moisture content, and the relationship between the value of the microwave intensity and the value of the moisture content, and clarifies the relationship. Is stored, and the measured values of the capacitance and the microwave intensity of the waste P sent from the capacitance meter 20A and the microwave intensity meter 20B are stored in the capacitance database in the relation database. Then, the moisture content of the waste is calculated by checking the relationship between the microwave intensity and the moisture content.

本実施形態では、静電容量測定計20Aにより測定した廃棄物の静電容量測定値から算定した廃棄物の水分率と、マイクロ波強度測定計20Bにより測定した廃棄物のマイクロ波強度測定値から算定した廃棄物の水分率の二つの水分率のうち一つの水分率を選択し、発熱量の算定そして焼却炉の運転制御を行うが、いずれを選択するかは、廃棄物の種類や性状より適宜定められる。例えば、水分率が比較的高い廃棄物には静電容量式、プラスチックごみが多い廃棄物にはマイクロ波式、そして家庭からの収集ごみが多い廃棄物には静電容量式、産業廃棄物と一般廃棄物(家庭からの収集ごみが主)との混合物には静電容量式を選択すること等としてもよい。   In the present embodiment, the water content of the waste calculated from the capacitance measurement value of the waste measured by the capacitance measurement device 20A and the microwave intensity measurement value of the waste measured by the microwave intensity measurement device 20B One of the two moisture rates of the calculated waste moisture rate is selected, the calorific value is calculated, and the operation control of the incinerator is performed.The choice depends on the type and properties of the waste. It is determined as appropriate. For example, wastes with relatively high moisture content are of the capacitive type, wastes with a lot of plastic garbage are of the microwave type, and wastes with a large amount of garbage collected from the home are of the capacitive type, industrial waste and so on. For a mixture with general waste (mainly garbage collected from households), a capacitance type may be selected.

また、本実施形態では、静電容量測定計とマイクロ強度測定計を設けることとしたが、静電容量測定計、マイクロ波強度測定計、赤外線強度測定計の三つの測定計のうち二つの測定計を選択して設けるようにしてもよい。   Further, in the present embodiment, the capacitance meter and the micro-intensity meter are provided, but two of the three meters of the capacitance meter, the microwave intensity meter, and the infrared intensity meter are measured. A total may be selected and provided.

また、上述した静電容量測定計とマイクロ強度測定計を設けるという形態に代え、接触型測定計、透過式測定計を用いて、廃棄物の性状により、いずれかの測定値を用いて水分率を算定するという形態とすることもできる。その場合、接触型測定計としては接触型静電容量測定計、接触型マイクロ波強度測定計、そして透過型測定計としては透過型静電容量測定計、透過型マイクロ波強度測定計が挙げられる。かつ、廃棄物の嵩密度により好ましい型式の測定計の測定値(接触型又は透過型)を採用し水分率算定するのがよい。例えば、嵩密度の高い廃棄物には、透過型測定計、そして嵩密度の低い廃棄物には、接触型測定計が好適である。嵩密度の低い廃棄物では廃棄物の空隙が多く透過型測定計では正確に特性値を測定できないからである。   In addition, instead of providing the above-described capacitance measuring instrument and micro-strength measuring instrument, using a contact-type measuring instrument or a permeation-type measuring instrument, depending on the property of the waste, the moisture content can be determined using one of the measured values. Can be calculated. In that case, the contact-type measuring instrument includes a contact-type capacitance measuring instrument and a contact-type microwave intensity measuring instrument, and the transmission-type measuring instrument includes a transmission-type capacitance measuring instrument and a transmission-type microwave intensity measuring instrument. . In addition, it is preferable that the moisture content is calculated by adopting a measurement value (contact type or transmission type) of a preferred type of measuring instrument depending on the bulk density of the waste. For example, a transmission type meter is suitable for waste having a high bulk density, and a contact type meter is suitable for waste having a low bulk density. This is because waste having a low bulk density has many voids in the waste, and the transmission type measurement device cannot accurately measure the characteristic value.

上記水分率算定器21は制御装置22に接続されており、この制御装置22は、上記シュート15内の廃棄物Pについて水分率算定器21より受けた水分率の値から、予め保持している対応関係にもとづき、正確な廃棄物の発熱量を推定し、それに応じて安定的な廃棄物の焼却が行われるように、予め保持している制御フローに基づき、空気供給系12、火格子11、給塵装置14へ指令信号を送り、空気供給系12での空気吹込み量、火格子11の送り速度、給塵装置14の送り出し速度等の各操作量を制御するようになっている。   The moisture content calculator 21 is connected to a control device 22, and the control device 22 previously holds the waste P in the chute 15 from the moisture content value received from the moisture content calculator 21. Based on the control relationship, the air supply system 12 and the grate 11 are estimated based on the control flow held in advance so as to accurately estimate the calorific value of the waste and to stably incinerate the waste accordingly. A command signal is sent to the dust supply device 14 to control each operation amount such as the air blowing amount in the air supply system 12, the feed speed of the grate 11, the delivery speed of the dust supply device 14, and the like.

このように本実施形態では、上記シュート15内の廃棄物P、すなわち燃焼室13へ送入される直前の廃棄物Pについて算定された水分率に基づいて、各操作量を制御するようになっているので、廃棄物焼却炉の運転条件を最適に制御できる。   As described above, in the present embodiment, each manipulated variable is controlled based on the moisture content calculated for the waste P in the chute 15, that is, the waste P immediately before being sent to the combustion chamber 13. Therefore, the operating conditions of the waste incinerator can be optimally controlled.

廃棄物焼却炉1に供給された廃棄物Pは次の要領で処理される。   The waste P supplied to the waste incinerator 1 is processed in the following manner.

廃棄物Pはホッパ16へ投入される。該廃棄物Pは、シュート15の下部に設置された給塵装置14(プッシャー)により火格子11上に押し出される。火格子11上の廃棄物Pは火格子11下の空気供給系12から吹き込まれる燃焼用空気により燃焼される。   The waste P is put into the hopper 16. The waste P is pushed out onto the grate 11 by a dust supply device 14 (pusher) installed below the chute 15. The waste P on the grate 11 is burned by the combustion air blown from the air supply system 12 below the grate 11.

ホッパ16から垂下して設けられたシュート15の側壁の内面に検出要素20A1が設けられ、検出要素20A1近傍の廃棄物Pの静電容量を静電容量測定計20Aにより計測する。水分率算定器21では測定された静電容量測定値に基づき水分率が算定される。また、シュート15の側壁の内面に検出要素20B1が設けられ、検出要素20B1近傍の廃棄物Pのマイクロ波強度をマイクロ波強度測定計20Bにより計測する。水分率算定器21では測定されたマイクロ波強度測定値に基づき水分率が算定される。水分率算定器21では、算定された静電容量測定値に基づく水分率とマイクロ波強度測定値に基づく水分率のいずれかを廃棄物の種類や性状により選択し、適切な水分率の値として、制御装置22に送信する。   A detection element 20A1 is provided on the inner surface of the side wall of the chute 15 that is provided hanging from the hopper 16, and the capacitance of the waste P near the detection element 20A1 is measured by the capacitance measurement meter 20A. The moisture content calculator 21 calculates the moisture content based on the measured capacitance value. A detection element 20B1 is provided on the inner surface of the side wall of the chute 15, and the microwave intensity of the waste P near the detection element 20B1 is measured by the microwave intensity meter 20B. The moisture content calculator 21 calculates the moisture content based on the measured microwave intensity. In the moisture content calculator 21, one of the moisture content based on the calculated capacitance measurement value and the moisture content based on the microwave intensity measurement value is selected according to the type or property of the waste, and the moisture content is calculated as an appropriate moisture content value. , To the control device 22.

制御装置22では、水分率算定器21から送られてきた水分率の値から、予め保持している対応関係に基づき、正確な廃棄物の発熱量を推定し、それに応じて予め保持している制御フローに基づき、安定的な廃棄物の焼却処理が行われるように指令信号を発する。
この指令信号によって給塵装置14の送り速度、火格子11の送り速度、火格子11の下方の空気供給系12から吹き込まれる燃焼用空気の吹込み量等の操作量が調整される結果、廃棄物の燃焼状態が制御される。
The control device 22 estimates an accurate calorific value of the waste from the value of the moisture content sent from the moisture content calculator 21 based on the correspondence relationship held in advance, and holds the heat value in advance accordingly. Based on the control flow, a command signal is issued to perform stable waste incineration.
As a result of this command signal, the manipulated variables such as the feed speed of the dust supply device 14, the feed speed of the grate 11 and the amount of combustion air blown from the air supply system 12 below the grate 11 are adjusted. The combustion state of the object is controlled.

1 廃棄物焼却炉
20A 静電容量測定計
20B マイクロ波強度測定計
20A1,20B1 検出要素
21 水分率算定装置
DESCRIPTION OF SYMBOLS 1 Waste incinerator 20A Capacitance meter 20B Microwave intensity meter 20A1, 20B1 Detecting element 21 Moisture calculation device

Claims (2)

廃棄物を焼却又はガス化する廃棄物処理炉の廃棄物投入口から下方に延びるシュート内に廃棄物の水分率と相関性を持つ廃棄物の特性値を測定する測定計の検出要素を設けた廃棄物処理炉装置において、
特性値の測定計に加え、該測定計による特性値の測定値に基づき廃棄物の水分率を算定する水分率算定装置と、
廃棄物処理炉の操作量を廃棄物の水分率にもとづき制御する制御装置とを備え、
特性値の測定計は、静電容量測定計、マイクロ波強度測定計、赤外線強度測定計の異なる形式の三つの測定計のうち二つの測定計が選択され配設されており、これら二つの測定計の特性値の測定値を上記水分率算定装置へ送り、二つの測定値からそれぞれについて水分率を算出し、二つの水分率の一方を制御装置へ送るようになっている、
ことを特徴とする廃棄物処理炉装置。
A measuring element for measuring the characteristic value of the waste that correlates with the moisture content of the waste is installed in a chute that extends downward from the waste inlet of the waste treatment furnace that incinerates or gasifies the waste. In waste treatment furnace equipment,
A moisture content calculating device that calculates the moisture content of the waste based on the measured value of the property value by the measuring device ,
A control device for controlling the operation amount of the waste treatment furnace based on the moisture content of the waste ,
Meter characteristic values, the capacitance meter, a microwave intensity meter, are arranged two meter is selected among the three meter different types of infrared intensity meter, these two The measured value of the characteristic value of the measuring meter is sent to the above-described moisture content calculating device , the moisture content is calculated from each of the two measured values, and one of the two moisture content is sent to the control device .
Waste treatment furnace apparatus characterized by the above-mentioned.
廃棄物を焼却又はガス化する廃棄物処理炉の廃棄物投入口から下方に延びるシュート内に廃棄物の水分率と相関性を持つ廃棄物の特性値を測定する測定計の検出要素を設けた廃棄物処理炉装置において、
特性値の測定計に加え、該測定計による特性値の測定値に基づき廃棄物の水分率を算定する水分率算定装置と、
廃棄物処理炉の操作量を廃棄物の水分率にもとづき制御する制御装置とを備え、
特性値の測定計は、測定計の検出要素と接触している廃棄物の特性値を測定する接触型測定計と、測定計の検出要素の間に存在している廃棄物を透過して特性値を測定する透過型測定計とが配設されており、これらの二つの測定計の特性値の測定値のうち一方の測定計からの測定値を上記水分率算定装置へ送り、二つの測定値からそれぞれについて水分率を算出し、二つの水分率の一方を制御装置へ送るようになっている、
ことを特徴とする廃棄物処理炉装置。
A measuring element for measuring the characteristic value of the waste that correlates with the moisture content of the waste is installed in a chute that extends downward from the waste inlet of the waste treatment furnace that incinerates or gasifies the waste. In waste treatment furnace equipment,
In addition to the meter characteristic value, and water content calculated equipment to calculate the moisture content of the waste based on the measured value of the characteristic value by the meter,
A control device for controlling the operation amount of the waste treatment furnace based on the moisture content of the waste ,
The characteristic value measurement meter is a contact type measurement device that measures the characteristic value of the waste that is in contact with the detection element of the measurement meter, and transmits the waste existing between the detection elements of the measurement meter. A transmission type measuring device for measuring the value is provided, and the measured value from one of the measured values of the characteristic values of these two measured values is sent to the above-mentioned moisture content calculating device , and the two measured values are measured. Calculate the moisture percentage for each from the value, and send one of the two moisture percentages to the control device ,
Waste treatment furnace apparatus characterized by the above-mentioned.
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