JP6327993B2 - Subcritical water treatment method and apparatus - Google Patents

Subcritical water treatment method and apparatus Download PDF

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JP6327993B2
JP6327993B2 JP2014151244A JP2014151244A JP6327993B2 JP 6327993 B2 JP6327993 B2 JP 6327993B2 JP 2014151244 A JP2014151244 A JP 2014151244A JP 2014151244 A JP2014151244 A JP 2014151244A JP 6327993 B2 JP6327993 B2 JP 6327993B2
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JP2016022468A5 (en
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敏勝 鈴木
敏勝 鈴木
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PCS CO., LTD.
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J3/00Processes of utilising sub-atmospheric or super-atmospheric pressure to effect chemical or physical change of matter; Apparatus therefor
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J3/00Processes of utilising sub-atmospheric or super-atmospheric pressure to effect chemical or physical change of matter; Apparatus therefor
    • B01J3/02Feed or outlet devices therefor
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J3/00Processes of utilising sub-atmospheric or super-atmospheric pressure to effect chemical or physical change of matter; Apparatus therefor
    • B01J3/04Pressure vessels, e.g. autoclaves
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B09DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
    • B09BDISPOSAL OF SOLID WASTE NOT OTHERWISE PROVIDED FOR
    • B09B3/00Destroying solid waste or transforming solid waste into something useful or harmless
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F11/00Treatment of sludge; Devices therefor
    • C02F11/06Treatment of sludge; Devices therefor by oxidation
    • C02F11/08Wet air oxidation
    • GPHYSICS
    • G21NUCLEAR PHYSICS; NUCLEAR ENGINEERING
    • G21FPROTECTION AGAINST X-RADIATION, GAMMA RADIATION, CORPUSCULAR RADIATION OR PARTICLE BOMBARDMENT; TREATING RADIOACTIVELY CONTAMINATED MATERIAL; DECONTAMINATION ARRANGEMENTS THEREFOR
    • G21F9/00Treating radioactively contaminated material; Decontamination arrangements therefor
    • G21F9/28Treating solids
    • G21F9/30Processing

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Description

本発明は、有機系廃棄物、汚泥等を高温、高圧の飽和水蒸気を用いて分解する亜臨界水処理方法及び装置に関する。   The present invention relates to a subcritical water treatment method and apparatus for decomposing organic waste, sludge and the like using high temperature and high pressure saturated steam.

従来の亜臨界水処理装置としては、例えば特許文献1に開示されるように、耐圧容器(圧力容器)内において有機系廃棄物を攪拌しながら、高温、高圧の飽和水蒸気を用いて水分解するとともに熱分解する処理装置がある。   As a conventional subcritical water treatment device, as disclosed in, for example, Patent Document 1, water is decomposed using high-temperature and high-pressure saturated steam while stirring organic waste in a pressure-resistant vessel (pressure vessel). In addition, there is a processing apparatus that thermally decomposes.

このような亜臨界水処理装置を利用して、上記のような有機系廃棄物や汚泥を処理する場合、全部を分解するまでには長時間、高温、高圧状態を維持しなければならず、水蒸気のための熱エネルギー及び攪拌のための回転エネルギーの消費量が非常に大きくなってしまうという問題点がある。   When processing such organic waste and sludge as described above using such a subcritical water treatment device, it must maintain a high temperature and high pressure for a long time before it is completely decomposed. There is a problem that the consumption of heat energy for water vapor and rotational energy for stirring becomes very large.

また、耐圧容器内で長時間、高温、高圧状態を維持した結果、例えば植物の場合、低分子量に分解され、肥料として有用な状態から更に分解されて、炭化状態となって単なるゴミとなってしまうという無駄があった。即ち、エネルギーを大量に消費して過剰な分解をしていた。   In addition, as a result of maintaining a high temperature and high pressure state for a long time in the pressure vessel, for example, in the case of plants, it is decomposed to a low molecular weight, further decomposed from a state useful as a fertilizer, becomes a carbonized state and becomes mere garbage. There was a waste. In other words, a large amount of energy was consumed, resulting in excessive decomposition.

更に、高温、高圧に耐えるために耐圧容器の強度を大きくする必要があり、結果として耐圧容器の容量が制限され、時間当たりの処理量を大きくできないという問題点がある。   Furthermore, it is necessary to increase the strength of the pressure vessel in order to withstand high temperatures and high pressures. As a result, there is a problem that the capacity of the pressure vessel is limited and the amount of processing per hour cannot be increased.

特許第4751977号公報Japanese Patent No. 4751977

本発明は、上記問題点を解決するためになされたものであって、過剰に高温、高圧とする必要がなく、有用物を残すことができ、且つ、大型化を有機系廃棄物や汚泥の時間当たりの処理量を増大させ、また、処理のためのエネルギー消費量を大幅に低減することができる亜臨界水処理方法及び亜臨界水処理装置を提供することを課題とする。   The present invention has been made in order to solve the above-described problems, and it is not necessary to excessively increase the temperature and pressure, can leave useful materials, and increase the size of organic waste and sludge. It is an object of the present invention to provide a subcritical water treatment method and a subcritical water treatment apparatus that can increase the throughput per hour and can significantly reduce the energy consumption for the treatment.

本発明者は、鋭意研究の結果、有機系廃棄物や汚泥からなる処理対象物を、亜臨界水処理する過程において、処理対象物の一部の分解が始まるタイミングを検出し、この分解開始のタイミングで、高温、高圧の飽和水蒸気の供給制御により、分解開始のタイミングにおける温度を短時間維持すれば、処理対象物の他の部分も、順次分解できることを見出した。   As a result of diligent research, the present inventor has detected the timing at which the decomposition of a part of the treatment object starts in the process of subcritical water treatment of the treatment object made of organic waste or sludge, and It has been found that if the temperature at the decomposition start timing is maintained for a short period of time by controlling the supply of high-temperature and high-pressure saturated steam at the timing, the other parts of the object to be processed can also be decomposed sequentially.

本発明者の実験によれば、分解開始の温度は、概ね、稲わら、下水汚泥等は150℃、肉・魚は180℃、プラスチック(Si樹脂を除く)は220℃前後であり、圧力は18〜20気圧であったが、分解開始温度が150℃の材料でも、その分解熱の最高値はプラスチックの分解開始温度を超えていることを見出したAccording to the inventor's experiment, the decomposition start temperature is generally 150 ° C. for rice straw, sewage sludge, etc., 180 ° C. for meat and fish, and 220 ° C. for plastic (excluding Si resin), and the pressure is Although it was 18 to 20 atmospheres, it was found that the maximum value of the decomposition heat exceeded the decomposition start temperature of the plastic even when the decomposition start temperature was 150 ° C.

即ち、本発明は以下のような実施例により上記課題を解決するものである。   That is, this invention solves the said subject with the following Examples.

(1)圧力容器内に、処理対象物を該圧力容器上部の投入口から投入する投入過程と、該圧力容器内に高温、高圧の水蒸気を供給して、該圧力容器内の処理対象物を攪拌しつつ加温、加圧して分解する亜臨界水処理過程と、前記圧力容器を開けて、前記亜臨界水処理過程を経た前記処理対象物を取出す過程と、を有してなり、前記亜臨界水処理過程は、それまでほぼ時間に比例して穏やかな傾きの直線状に上昇していた、前記圧力容器内の温度又は圧力が、前記傾きに対して20%以上大きい傾きの曲線又は直線に沿って上昇する場合を、急上昇と定義したとき、前記処理対象物の一部の結合の分解が開始するタイミングを、前記圧力容器内の温度が150℃以上の範囲で、前記圧力容器内の1以上の個所の温度及び1以上の個所の圧力のうち、1個所の温度又は圧力の急上昇から検出する過程と、前記の検出の後、前記圧力容器内の温度を、水蒸気の供給量を調整することにより、前記分解の開始のタイミングにおける温度に5〜10分間維持して、前記処理対象物の一部の分解熱により、他の部分の結合の分解を促す過程と、前記5〜10分間の経過後に水蒸気の供給を停止し、且つ、前記処理対象物の他の部分が分解してから、前記圧力容器内の水蒸気を排出する過程と、を有することを特徴とする亜臨界水処理方法。
(2)圧力容器内に、処理対象物を該圧力容器上部の投入口から投入する投入過程と、該 圧力容器内に高温、高圧の水蒸気を供給して、該圧力容器内の処理対象物を攪拌しつつ加 温、加圧して分解する亜臨界水処理過程と、前記圧力容器を開けて、前記亜臨界水処理過 程を経た前記処理対象物を取出す過程と、を有してなる亜臨界水処理方法であって、圧力 容器内に高温、高圧の水蒸気を供給して、該圧力容器内の処理対象物を攪拌しつつ加温、 加圧したとき、それまでほぼ時間に比例して穏やかな傾きの直線状に上昇していた、前記 圧力容器内の温度又は圧力が、前記傾きに対して20%以上大きい傾きの曲線又は直線に 沿って上昇する場合を、急上昇と定義したとき、前記圧力容器内における前記急上昇の開 始時の温度を前記処理対象物における含有物の種類毎に予め測定しておく過程を設け、前 記亜臨界水処理過程は、前記圧力容器内の温度が150℃以上の範囲で、前記圧力容器内 の1以上の個所の温度のうち、1個所の温度が、前記予め測定された急上昇開始時の温度 に到達したときを検出する過程と、前記の検出の後、前記圧力容器内の温度を、水蒸気の 供給量を調整することにより、前記処理対象物の一部の分解の開始のタイミングにおける 前記予め測定された急上昇開始時の温度に5〜10分間維持して、前記処理対象物の一部 の分解熱により、他の部分の結合の分解を促す過程と、前記5〜10分間の経過後に水蒸 気の供給を停止し、且つ、前記処理対象物の他の部分が分解してから、前記圧力容器内の 水蒸気を排出する過程と、を有することを特徴とする亜臨界水処理方法。
(1) A charging process in which an object to be treated is introduced into the pressure vessel from an inlet at the top of the pressure vessel, and high-temperature and high-pressure steam is supplied into the pressure vessel, and the object to be treated in the pressure vessel is A subcritical water treatment process that decomposes by heating and pressurizing while stirring, and a process of opening the pressure vessel and taking out the object to be treated through the subcritical water treatment process. In the critical water treatment process, the temperature or pressure in the pressure vessel has risen in a straight line with a gentle slope almost proportional to the time, and the curved line or straight line has a slope of 20% or more larger than the slope. Is defined as a sudden rise, the timing at which the decomposition of a part of the object to be processed starts, and the temperature in the pressure vessel is within a range of 150 ° C. or higher. Temperature at one or more locations and pressure at one or more locations , 5 a step of detecting the rapid increase in temperature or pressure of one position, after the detection, the temperature of the pressure vessel, by adjusting the amount of water vapor supply, the temperature at the start of timing of the decomposition Maintained for 10 minutes, the process of promoting decomposition of the bonds of other parts by the heat of decomposition of part of the object to be treated , and the supply of water vapor after the lapse of 5 to 10 minutes, and the object to be treated A process of discharging water vapor in the pressure vessel after the other part of the product is decomposed , and a subcritical water treatment method.
(2) in a pressure vessel, and put the process of turning on the processing target from the pressure vessel upper part of the inlet, the hot into the pressure vessel, by supplying high-pressure steam, a processing object of the pressure vessel stirring heated, and pressurized subcritical water treatment processes decompose, open the pressure vessel, subcritical comprising a, a step of taking out the processing object passed through the excessive degree the subcritical water treatment This is a water treatment method, in which high-temperature and high-pressure steam is supplied into a pressure vessel, and when the object to be treated in the pressure vessel is heated and pressurized while stirring , it is gentle until almost until then. When the temperature or pressure in the pressure vessel, which has risen in a straight line with a large slope, rises along a curve or straight line having a slope that is 20% or more larger than the slope , temperature said processing object inception of the surge in pressure vessel The process is measured in advance for each type of inclusions definitive provided, before Kia critical water process is a temperature of between more than 0.99 ° C. in the pressure vessel, the temperature of one or more locations in said pressure vessel Among these, the process of detecting when the temperature at one point has reached the temperature at the start of the pre-measured rapid rise , and after the detection, the temperature in the pressure vessel is adjusted with the supply amount of water vapor By maintaining for 5 to 10 minutes at the temperature at the start of the sudden rise measured in advance at the timing of starting the decomposition of a part of the processing object, the heat of decomposition of a part of the processing object a step of prompting the degradation of connective portions, to stop the supply of Mizu蒸care after the 5-10 minutes, and, after decomposing other parts of the processing object, the steam in the pressure vessel And a discharge process characterized by having a discharge process Water treatment process.

)圧力容器内に高温、高圧の水蒸気を注入して、該圧力容器内の処理対象物を、亜臨界状態として分解する亜臨界水処理装置であって、前記圧力容器内に高温、高圧の水蒸気を供給する水蒸気供給装置と、前記圧力容器内で、前記処理対象物を攪拌する複数の攪拌翼、及び、この攪拌翼を駆動する回転シャフトを含む攪拌装置と、この回転シャフトを、減速機を介して駆動するモーターと、前記水蒸気供給装置を制御して、前記圧力容器への水蒸気供給量を制御する水蒸気制御装置と、前記圧力容器の上部に設けられた、前記処理対象物の投入口、前記圧力容器の下部に設けられた、処理済の前記処理対象物を取出すための取出口、及び、前記圧力容器に設けられた、前記高温、高圧の水蒸気を注入するための水蒸気注入口と、を有してなり、前記水蒸気制御装置は、圧力容器内の1以上の個所の温度を測定する温度センサーと、圧力容器内の1以上の個所の圧力を測定する圧力センサーと、これらのセンサー出力信号が入力される制御装置本体と、この制御装置本体からの指令信号に基づいて、前記水蒸気供給装置による水蒸気供給量を調節する蒸気開閉弁を駆動する開閉弁駆動装置と、を有し、それまでほぼ時間に比例して穏やかな傾きの直線状に上昇していた、前記圧力容器内の温度又は圧力が、前記傾きに対して20%以上大きい傾きの曲線又は直線に沿って上昇する場合を、急上昇と定義したとき、前記制御装置本体は、前記圧力容器内の温度が150℃を越えた範囲で、前記温度センサーによる検出温度及び前記圧力センサーにおける検出圧力の少なくとも一方が、急上昇したとき、前記開閉弁駆動装置に対して、水蒸気の供給量を調整することにより、前記圧力容器内における前記急上昇開始時の温度を5〜10分間維持して、前記処理対象物の一部の分解熱により、他の部分の結合の分解を促すように、前記蒸気開閉弁を制御する指令信号を出力し、且つ、前記5〜10分間の経過後に、前記蒸気開閉弁を閉じる指令信号を出力し、且つ、前記処 理対象物の他の部分が分解してから、前記圧力容器内の水蒸気を排出する信号を出力するように構成されたことを特徴とする亜臨界水処理装置。
(4)圧力容器内に高温、高圧の水蒸気を注入して、該圧力容器内の処理対象物を、亜臨 界状態として分解する亜臨界水処理装置であって、前記圧力容器内に高温、高圧の水蒸気 を供給する水蒸気供給装置と、前記圧力容器内で、前記処理対象物を攪拌する複数の攪拌 翼、及び、この攪拌翼を駆動する回転シャフトを含む攪拌装置と、この回転シャフトを、 減速機を介して駆動するモーターと、前記水蒸気供給装置を制御して、前記圧力容器への 水蒸気供給量を制御する水蒸気制御装置と、前記圧力容器の上部に設けられた、前記処理 対象物の投入口、前記圧力容器の下部に設けられた、処理済の前記処理対象物を取出すた めの取出口、及び、前記圧力容器に設けられた、前記高温、高圧の水蒸気を注入するため の水蒸気注入口と、を有してなり、前記水蒸気制御装置は、圧力容器内の1以上の個所の 温度を測定する温度センサーと、圧力容器内の1以上の個所の圧力を測定する圧力センサ ーと、これらのセンサー出力信号が入力される制御装置本体と、この制御装置本体からの 指令信号に基づいて、前記水蒸気供給装置による水蒸気供給量を調節する蒸気開閉弁を駆 動する開閉弁駆動装置と、を有し、圧力容器内に高温、高圧の水蒸気を供給して、該圧力 容器内の処理対象物を攪拌しつつ加温、加圧したとき、それまでほぼ時間に比例して穏や かな傾きの直線状に上昇していた、前記圧力容器内の温度又は圧力が、前記傾きに対して 20%以上大きい傾きの曲線又は直線に沿って上昇する場合を、急上昇と定義したとき、 前記制御装置本体は、前記処理対象物における含有物の種類毎に予め測定された前記急上 昇開始時の温度が記憶されている記憶部を有し、且つ、前記圧力容器内の温度が、前記処 理対象物における含有物の種類に対応する前記記憶された温度に到達したときの前記温度 センサーの出力信号に基づき、前記開閉弁駆動装置に対して、水蒸気の供給量を調整する ことにより、前記圧力容器内における前記急上昇開始時の温度を5〜10分間維持して、 前記処理対象物の一部の分解熱により、他の部分の結合の分解を促すように、前記蒸気開 閉弁を制御する指令信号を出力し、且つ、前記5〜10分間の経過後に、前記蒸気開閉弁 を閉じる指令信号を出力し、且つ、前記処理対象物の他の部分が分解してから、前記圧力 容器内の水蒸気を排出する信号を出力するように構成されたことを特徴とする亜臨界水処 理装置。
( 3 ) A subcritical water treatment apparatus for injecting high-temperature and high-pressure steam into a pressure vessel and decomposing the object to be treated in the pressure vessel as a subcritical state. A steam supply device for supplying the steam, a plurality of stirring blades for stirring the processing object in the pressure vessel, a stirring device including a rotating shaft for driving the stirring blade, and a speed reduction of the rotating shaft. A motor driven through a machine, a water vapor control device that controls the water vapor supply device to control the amount of water vapor supplied to the pressure vessel, and an input of the processing object provided at the top of the pressure vessel An outlet for removing the processed object to be processed, and a steam inlet for injecting the high-temperature and high-pressure steam provided in the pressure container. And having The water vapor control apparatus receives a temperature sensor that measures the temperature of one or more locations in the pressure vessel, a pressure sensor that measures the pressure of one or more locations in the pressure vessel, and inputs of these sensor output signals. A control device main body and an on-off valve driving device for driving a steam on-off valve that adjusts the amount of water vapor supplied by the water vapor supply device based on a command signal from the control device main body. When the temperature or pressure in the pressure vessel, which has risen in a straight line with a gentle slope in proportion, rises along a curve or straight line with a slope of 20% or more larger than the slope, it is defined as a sudden rise. When the temperature of the inside of the pressure vessel exceeds 150 ° C., at least one of the temperature detected by the temperature sensor and the pressure detected by the pressure sensor is When the temperature rises rapidly, the temperature at the start of the sudden rise in the pressure vessel is maintained for 5 to 10 minutes by adjusting the supply amount of water vapor to the on- off valve driving device, A command signal for controlling the steam on-off valve so as to promote decomposition of the coupling of other parts by the heat of decomposition of the part, and a command signal for closing the steam on-off valve after the elapse of 5 to 10 minutes outputs, and the processing from the other parts is the decomposition of physical objects, wherein the sub-critical water treatment apparatus characterized by being configured to output a signal for discharging the steam in the pressure vessel.
(4) high temperature within the pressure vessel, by injecting high-pressure steam, a processing object of the pressure vessel, a sub-critical water treatment apparatus for decomposing a A臨 field state, a high temperature in the pressure vessel, A steam supply device that supplies high-pressure steam , a plurality of stirring blades that stir the processing object in the pressure vessel, a stirring device that includes a rotating shaft that drives the stirring blade, and the rotating shaft. A motor driven via a speed reducer; a water vapor control device that controls the water vapor supply device to control the amount of water vapor supplied to the pressure vessel; and the processing object provided at the top of the pressure vessel . inlet, provided in a lower portion of said pressure vessel, outlet of order to take out the processing object processed, and, the provided pressure vessel, the hot, steam for injecting high-pressure steam An inlet, and Ri, the steam control unit comprises a temperature sensor for measuring one or more temperatures of locations in the pressure vessel, and pressure Sensor for measuring the pressure in one or more locations in the pressure vessel, these sensor output signals are input a control device main body which is, in accordance with a command signal from the controller body has a opening and closing valve driving apparatus for drive the steam on-off valve for adjusting the steam supply amount of the steam supply device, pressure vessel high temperature, by supplying high-pressure steam, the processing object with stirring warming of the pressure vessel, when pressurized, on the rise in proportion to approximately the time until it gently and kana slope of a straight line In addition, when the temperature or pressure in the pressure vessel rises along a curve or straight line having an inclination of 20% or more larger than the inclination, it is defined as a sudden increase . Species of inclusions in A storage unit that previously measured temperature of the abrupt upper temperature at the start is stored for each, and the storage temperature of the pressure vessel, corresponding to the type of inclusions in the processed object The temperature at the start of the sudden rise in the pressure vessel is adjusted to 5 to 5 by adjusting the supply amount of water vapor to the on-off valve driving device based on the output signal of the temperature sensor when the measured temperature is reached. and maintained for 10 minutes, the part of the heat of decomposition of the processing object, to urge the degradation of the binding of the other part, and outputs a command signal for controlling the vapor opening closed, and, the 5-10 After a lapse of minutes, a command signal for closing the steam on-off valve is output, and a signal for discharging the water vapor in the pressure vessel is output after the other part of the processing object is decomposed. Subcritical water treatment characterized by Science device.

本発明によれば、亜臨界水による処理対象物の分解開始を検知し、分解開始の温度を維持するように高温、高圧蒸気の供給量を最小とすることにより、従来比で約50%のエネルギー消費量で、亜臨界水処理により処理対象物を分解できる。   According to the present invention, the start of decomposition of the object to be treated by subcritical water is detected, and the supply amount of high-temperature and high-pressure steam is minimized so as to maintain the decomposition start temperature. With the energy consumption, the processing object can be decomposed by subcritical water treatment.

これにより、最高温度、最高圧力を低くでき、亜臨界水処理装置を大型化できる。また、処理対象物を過剰に分解することなく有用物とすることも可能となった。   Thereby, the maximum temperature and the maximum pressure can be lowered, and the subcritical water treatment apparatus can be enlarged. In addition, it has become possible to make the object to be treated useful without being excessively decomposed.

本発明の実施例に係る亜臨界水処理装置を示すブロック図The block diagram which shows the subcritical water treatment apparatus which concerns on the Example of this invention. 同亜臨界水処理装置の詳細を示す正面図Front view showing details of the same subcritical water treatment system 同側面図Side view 同平面図Plan view 亜臨界水処理装置の制御系統を示す回路図Circuit diagram showing control system of subcritical water treatment equipment 同実施例に係る亜臨界水処理装置による、処理対象物の分解過程を示すフローチャートThe flowchart which shows the decomposition | disassembly process of the process target object by the subcritical water treatment apparatus which concerns on the same Example.

以下本発明を実施するための形態について図面を参照して説明する。   Embodiments for carrying out the present invention will be described below with reference to the drawings.

図1に示されるように、実施例1に係る亜臨界水処理装置20は、圧力容器22内に高温、高圧の水蒸気を注入して、該圧力容器22内の、放射能汚染された土壌及び汚泥の少なくとも一方を含む処理対象物を分解するものである。   As shown in FIG. 1, the subcritical water treatment apparatus 20 according to the first embodiment injects high-temperature and high-pressure steam into a pressure vessel 22, and radioactively contaminated soil and A processing object containing at least one of sludge is decomposed.

図1〜図3、図5に示されるように、亜臨界水処理装置20は、圧力容器22と、水蒸気供給装置24と、攪拌装置26と、水蒸気制御装置30と、回転シャフト制御装置50とを備えて構成されている。   As shown in FIGS. 1 to 3 and 5, the subcritical water treatment device 20 includes a pressure vessel 22, a steam supply device 24, a stirring device 26, a steam control device 30, and a rotary shaft control device 50. It is configured with.

圧力容器22は、処理対象物を投入するための投入口22Aと、亜臨界水処理を終えた処理対象物を排出するための取出口22Bと、圧力容器22内に高温、高圧の水蒸気を注入するための水蒸気注入口22C(2ヶ所)とを備えている。   The pressure vessel 22 is provided with an inlet 22A for introducing the treatment object, an outlet 22B for discharging the treatment object after the subcritical water treatment, and high-temperature and high-pressure steam is injected into the pressure vessel 22. 22C (two places) for injecting water vapor.

投入口22Aは、圧力容器22の上部に筒状に突出して形成され、上端のクラッチドア23Aによって開閉されるようになっている。   The insertion port 22A is formed in a cylindrical shape projecting from the top of the pressure vessel 22, and is opened and closed by a clutch door 23A at the upper end.

図1の符号22Dは蒸気排出口であり、この蒸気排出口22Dは、圧力容器22の上端から上方に立設された筒状に形成されていて、過剰な蒸気を外部に排出するようにされている。筒状体の更に上端にも蒸気排出口22Eがある。   Reference numeral 22D in FIG. 1 denotes a steam discharge port. The steam discharge port 22D is formed in a cylindrical shape standing upward from the upper end of the pressure vessel 22, and discharges excess steam to the outside. ing. There is also a steam outlet 22E at the upper end of the cylindrical body.

取出口22Bは、圧力容器22の、図1において右端に下向きに傾斜して取付けられ、ハンドル22Fにより開口されて、亜臨界水処理の終わった処理対象物を外部に排出できるようにされている。このとき、攪拌装置26の回転シャフト26Aは、内部の処理対象物を取出口22B方向に押出すように回転される。   The outlet 22B is attached to the right end of the pressure vessel 22 so as to be inclined downward in FIG. 1, and is opened by a handle 22F so that the processing object after the subcritical water treatment can be discharged to the outside. . At this time, the rotating shaft 26A of the stirring device 26 is rotated so as to extrude the processing object inside in the direction of the outlet 22B.

水蒸気供給装置24は、ボイラー24Aによって生産された高温、高圧の水蒸気を、圧力調整弁24B及び蒸気開閉弁36(説明後述)を介して、水蒸気注入口22Cから圧力容器22内に供給するようにされている。   The steam supply device 24 supplies the high-temperature and high-pressure steam produced by the boiler 24A into the pressure vessel 22 from the steam inlet 22C via the pressure adjustment valve 24B and the steam on-off valve 36 (described later). Has been.

攪拌装置26は、圧力容器22内の、ほぼ中心を水平に貫通して配置された回転シャフト26A、及び、この回転シャフト26Aの、長手方向複数箇所に半径方向に延在して取付けられた複数の攪拌翼26Bとを備えて構成されている。回転シャフト26Aは、図1において左端下側に設けられたモーター27から減速機28を介して駆動され、圧力容器22内の処理対象物を攪拌するようにされている。   The stirring device 26 includes a rotating shaft 26A disposed in the pressure vessel 22 so as to pass through substantially the center thereof horizontally, and a plurality of the rotating shafts 26A attached to the rotating shaft 26A so as to extend in the radial direction at a plurality of longitudinal positions. And a stirring blade 26B. The rotating shaft 26 </ b> A is driven from a motor 27 provided on the lower left side in FIG. 1 via a speed reducer 28 to stir the object to be processed in the pressure vessel 22.

ここで、回転シャフト26Aは、通常運転時は、一定間隔で時計方向又は反時計方向に回転方向が切替えられて、攪拌翼26Bが処理対象物を取出口22B側からモーター27方向へ、また、その反対方向に送るようにされている。   Here, during normal operation, the rotating shaft 26A is rotated in a clockwise direction or a counterclockwise direction at regular intervals, and the stirring blade 26B removes the object to be processed from the outlet 22B side to the motor 27 direction. It is sent in the opposite direction.

図5に示されるように、水蒸気制御装置30は、圧力容器22の外側の3箇所に取付けられた温度センサー32A、32Bと、同様に、圧力容器22の上部外側に取付けられた圧力センサー34A、34Bと、水蒸気注入口22Cへの水蒸気の供給量を調整する蒸気開閉弁36と、圧力容器22内の蒸気を排出するための蒸気排出弁37と、制御装置本体40と、を備えて構成されている。   As shown in FIG. 5, the water vapor control device 30 includes temperature sensors 32 </ b> A and 32 </ b> B attached to three locations outside the pressure vessel 22, as well as pressure sensors 34 </ b> A attached to the upper outside of the pressure vessel 22. 34B, a steam opening / closing valve 36 for adjusting the amount of steam supplied to the steam inlet 22C, a steam discharge valve 37 for discharging steam in the pressure vessel 22, and a control device main body 40. ing.

温度センサー32A、32Bは、圧力容器22の内側の温度を検出するようにされ、又、圧力センサー34A、34Bは、圧力容器22の内側の圧力を検出するようにされている。   The temperature sensors 32 </ b> A and 32 </ b> B are configured to detect the temperature inside the pressure vessel 22, and the pressure sensors 34 </ b> A and 34 </ b> B are configured to detect the pressure inside the pressure vessel 22.

これら温度センサー32A、32Bと圧力センサー34A、34Bの検出出力信号は、制御装置本体40に出力するようにされている。   Detection output signals from the temperature sensors 32A and 32B and the pressure sensors 34A and 34B are output to the control device main body 40.

制御装置本体40は、CPUからなり、温度センサー32A、32B、圧力センサー34A、34Bからの検出温度信号及び検出圧力信号に基づいて、開閉弁駆動装置38を介して、蒸気開閉弁36を駆動し、圧力容器22内への蒸気供給量を調整できるようにされている。   The control device main body 40 includes a CPU, and drives the steam on / off valve 36 via the on / off valve driving device 38 based on the detected temperature signal and the detected pressure signal from the temperature sensors 32A and 32B and the pressure sensors 34A and 34B. The amount of steam supplied into the pressure vessel 22 can be adjusted.

回転シャフト制御装置50は、回転シャフト26Aに取付けられて、その回転速度を
検出する回転速度センサー52Aと、回転トルクを検出する回転トルクセンサー52Bとからのセンサー出力信号に基づいて、回転シャフト26Aの回転速度を制御するようにされている。
Rotation shaft controller 50, mounted on the rotation shaft 26A, and the rotational speed sensor 52A which detects the rotational speed, based on the sensor output signal from the torque sensor 52B for detecting the rotational torque of the rotation shaft 26A The rotation speed is controlled.

具体的には、回転シャフト制御装置50は、回転速度センサー52Aから出力信号に基づく回転シャフト26Aの回転速度と、回転トルクセンサー52Bからの出力信号に基づく回転シャフト26Aの回転トルクとの積が一定値となるように、減速機28を介して回転シャフト26Aの回転速度を制御するように構成されている。 Specifically, the rotation shaft control device 50 has a constant product of the rotation speed of the rotation shaft 26A based on the output signal from the rotation speed sensor 52A and the rotation torque of the rotation shaft 26A based on the output signal from the rotation torque sensor 52B. The rotational speed of the rotary shaft 26A is controlled via the speed reducer 28 so as to be a value.

次に、本実施例1にかかる亜臨界水処理装置20によって、水産廃棄物を分解する過程について、図6を参照して詳細に説明する。   Next, the process of decomposing marine waste by the subcritical water treatment apparatus 20 according to the first embodiment will be described in detail with reference to FIG.

なお、圧力容器22は、飽和蒸気により加熱、加圧され、飽和蒸気の圧力は温度と一定の関係があるので圧力の数値は示すことを省略する。   The pressure vessel 22 is heated and pressurized with saturated steam, and since the pressure of the saturated steam has a certain relationship with the temperature, the numerical value of the pressure is not shown.

まず、亜臨界水処理装置20における水蒸気制御装置30の、制御装置本体40及び回転シャフト制御装置50を次のように設定しておく。   First, the control device main body 40 and the rotary shaft control device 50 of the water vapor control device 30 in the subcritical water treatment device 20 are set as follows.

制御装置本体40は、上昇しつつある圧力容器22内の温度及び圧力を測定して、温度センサー32A、32Bのいずれかのセンサー出力信号による温度が150℃以上で、温度及び圧力の急上昇の検出が可能なように設定され、また、前記の急上昇の急上昇を検知した後、圧力容器22内の温度を、前記検出した急上昇の開始時の温度以上に、5〜10分間維持するように、水蒸気の圧力容器22内への供給量を調整し、且つ、その時間経過後に水蒸気の供給を停止するように設定されている。   The control device main body 40 measures the temperature and pressure in the pressure vessel 22 that is rising, and detects a sudden rise in temperature and pressure when the temperature of the sensor output signal of either of the temperature sensors 32A and 32B is 150 ° C. or higher. In order to maintain the temperature in the pressure vessel 22 at a temperature higher than the detected temperature at the start of the rapid increase for 5 to 10 minutes after detecting the rapid increase. The supply amount of the water vapor into the pressure vessel 22 is adjusted, and the supply of water vapor is stopped after the lapse of time.

回転シャフト制御装置50は、除染処理対象物を攪拌する攪拌装置26における、回転シャフト26Aの回転トルクと回転速度との積が一定となるように、回転シャフト26Aの回転速度を制御するように設定しておく。具体的には、回転速度センサー52Aにより検出される回転速度と、回転トルクセンサー52Bにより検出される回転トルクの積が一定値となるように減速機28を介して制御するThe rotation shaft control device 50 controls the rotation speed of the rotation shaft 26A so that the product of the rotation torque and the rotation speed of the rotation shaft 26A is constant in the stirring device 26 that stirs the object to be decontaminated. Set it. Specifically, control is performed via the speed reducer 28 so that the product of the rotational speed detected by the rotational speed sensor 52A and the rotational torque detected by the rotational torque sensor 52B becomes a constant value.

次に、図7のステップ101に示されるように、投入口22Aを開いて水産廃棄物である処理対象物を圧力容器22内に投入する。   Next, as shown in step 101 of FIG. 7, the input port 22 </ b> A is opened, and a processing object that is a marine waste is input into the pressure vessel 22.

次のステップ102においては、水蒸気供給装置24のボイラー24Aで製造された高温、高圧蒸気を、水蒸気注入口22Cから圧力容器22内に注入する。   In the next step 102, the high-temperature and high-pressure steam produced by the boiler 24A of the steam supply device 24 is injected into the pressure vessel 22 from the steam inlet 22C.

ステップ103に進み、モーター27により攪拌装置26の回転シャフト26Aを回転させて、圧力容器22内で処理対象物の攪拌を開始する。このとき、処理対象物は、例えば、帆立貝のウロ(中腸線)の場合は、粘性が高く、魚の頭部や内臓の場合は大きな塊であるため、攪拌翼26Bには比較的大きな抵抗がかかる。従って、回転シャフト26Aの回転トルクの抵抗は大きくなり、それに対応して回転速度は遅くなる。   Proceeding to step 103, the rotating shaft 26 </ b> A of the stirring device 26 is rotated by the motor 27, and stirring of the processing object is started in the pressure vessel 22. At this time, for example, in the case of a scallop uro (midgut line), the object to be treated is highly viscous, and in the case of a fish head or internal organs, it is a large lump. Therefore, a relatively large resistance is applied to the stirring blade 26B. . Accordingly, the resistance of the rotational torque of the rotating shaft 26A is increased, and the rotational speed is correspondingly decreased.

次のステップ104では、圧力容器22内の温度が150℃に到達したことを、温度センサー32A、32Bの少なくとも1つによって検出する。   In the next step 104, it is detected by at least one of the temperature sensors 32A and 32B that the temperature in the pressure vessel 22 has reached 150 ° C.

このとき、圧力容器22内の処理対象物は、水蒸気が入り込むことにより攪拌抵抗がより小さくなるので、すなわち、回転シャフト26Aの回転トルクが小さくなるので、回転速度は自動的に増大する(ステップ105)。従って、処理対象物は、更に頻繁に攪拌翼26Bにより衝撃を受けて多くの水蒸気が混入し、均一に、且つ、効率よく加熱される。   At this time, the processing object in the pressure vessel 22 has a lower agitation resistance due to the entry of water vapor, that is, the rotational torque of the rotary shaft 26A is reduced, so that the rotational speed automatically increases (step 105). ). Therefore, the object to be treated is more frequently impacted by the agitating blade 26B and a lot of water vapor is mixed therein, and the object to be treated is heated uniformly and efficiently.

上記のように、処理対象物が150℃以上になると、例えば帆立貝のウロに含まれる有機カドミウムや魚の内臓に含まれる有機水銀は蛋白質から分離し、無毒となる。   As described above, when the object to be treated reaches 150 ° C. or higher, for example, organic cadmium contained in scallop shells and organic mercury contained in fish internal organs are separated from proteins and become non-toxic.

蛋白質が亜臨界水処理されると、アミノ酸になるが、この段階で水蒸気の供給を停止又は減少させると分解の進行が止まり、アミノ酸は例えば肥料、家畜の飼料として利用可能となる。   When the protein is treated with subcritical water, it becomes an amino acid, but if the supply of water vapor is stopped or reduced at this stage, the progress of decomposition stops, and the amino acid can be used, for example, as a fertilizer or livestock feed.

更に、高温、高圧の水蒸気を圧力容器22内に注入していくと、ステップ106において、温度センサー32A、32B、又は、圧力センサー34A、34Bの少なくとも1つが、圧力容器22内の温度及び/又は圧力の急上昇を検知する。   Further, when high-temperature and high-pressure steam is injected into the pressure vessel 22, in step 106, at least one of the temperature sensors 32A and 32B or the pressure sensors 34A and 34B Detects a sudden rise in pressure.

ここで、急上昇とは、それまでほぼ時間に比例して温度及び圧力が穏やかな傾きの直線状に上昇していたのが、前記傾きに対して20%以上の傾きの曲線又は直線に沿って上昇する場合を、急上昇と定義する。   Here, the sudden rise means that the temperature and pressure have risen in a straight line with a gentle slope in proportion to the time, but along a curve or straight line with a slope of 20% or more with respect to the slope. A rise is defined as a sudden rise.

本発明者は、実験の結果、上記のように、圧力容器22内の温度及び/又は圧力の急上昇は、圧力容器22内で処理対象物の一部が分解開始すると、高温、高圧の水蒸気による温度及び/又は圧力の上昇の上に、処理対象物の一部の結合の分解による分解熱が加わるためと考えている。   As a result of experiments, the present inventor has found that, as described above, the rapid increase in temperature and / or pressure in the pressure vessel 22 is caused by high-temperature and high-pressure steam when a part of the processing object starts to decompose in the pressure vessel 22. It is considered that heat of decomposition due to decomposition of some bonds of the object to be processed is added to the increase in temperature and / or pressure.

又、本発明者は、上記分解開始温度は、処理対物に含まれる材料の種類によって相違し、更に、一部でも分解が始まると、その分解熱によって、更に異なる種類の材料も順次分解が開始し、追加の高温、高圧の水蒸気による加熱、加圧が不要となることを見出した。 The present inventor has the decomposition initiation temperature, the phases differences depending on the type of material contained in the processing Target product, further the degradation even partially begins, by the heat of decomposition, sequentially even further different types of materials It was found that decomposition started and heating and pressurization with additional high-temperature and high-pressure steam became unnecessary.

更に、このときの条件として、圧力容器22内の温度を、急上昇の開始時点の温度以上に5〜10分間維持すれば、分解が順次自動的に進行していくことを確実にできることがわかった。   Furthermore, as a condition at this time, it has been found that if the temperature in the pressure vessel 22 is maintained for 5 to 10 minutes above the temperature at the start of the sudden rise, it is possible to ensure that the decomposition proceeds automatically in sequence. .

即ち、次のステップ107では、水蒸気制御装置30、温度センサー32A、32B及び圧力センサー34A、34Bによる、温度又は圧力の急上昇を検出する信号の入力により、開閉弁駆動装置38を介して、蒸気開閉弁36が、前記急上昇の開始時点の温度以上に、圧力容器22内の温度を5〜10分間維持するように制御する(ステップ108参照)。   That is, in the next step 107, the steam opening / closing operation is performed via the on-off valve driving device 38 by the input of a signal for detecting a sudden rise in temperature or pressure by the water vapor control device 30, the temperature sensors 32A, 32B and the pressure sensors 34A, 34B. The valve 36 is controlled to maintain the temperature in the pressure vessel 22 for 5 to 10 minutes above the temperature at the start of the sudden rise (see step 108).

次のステップ109では、蒸気供給を停止して、且つ、蒸気排出口22D、22Eから蒸気を排出して圧力容器22内の温度及び圧力を低減させ、処理対象物の亜臨界水処理を終了する。   In the next step 109, the supply of steam is stopped and the steam is discharged from the steam discharge ports 22D and 22E to reduce the temperature and pressure in the pressure vessel 22, and the subcritical water treatment of the object to be treated is completed. .

次に、ステップ110に進み、圧力容器22の取出口22Bを開いて、処理対象物を取出して、これを放熱する。   Next, it progresses to step 110, the outlet 22B of the pressure vessel 22 is opened, a process target object is taken out, and this is thermally radiated.

なお、上記実施例では、圧力容器22内の温度(及び/又は圧力)変化に基づいて水蒸気の供給を制御しているが、本発明はこれに限定させるものではなく、他のファクターに基づくようにしてもよい。   In the above embodiment, the supply of water vapor is controlled based on the temperature (and / or pressure) change in the pressure vessel 22, but the present invention is not limited to this, and is based on other factors. It may be.

例えば、圧力容器22への蒸気の収支の変化に基づくものでもよい。具体的には、蒸気供給量と蒸気排出量の差が、10〜60分間で20%以上減少したときをファクターとして、水蒸気の供給を制御してもよい。圧力容器22内の温度又は圧力が急上昇するとき、蒸気は処理対象物の加熱に消費されないので、排出量が急減する。   For example, it may be based on a change in the balance of steam to the pressure vessel 22. Specifically, the supply of water vapor may be controlled with the difference between the steam supply amount and the steam discharge amount being reduced by 20% or more in 10 to 60 minutes as a factor. When the temperature or pressure in the pressure vessel 22 rises rapidly, the steam is not consumed for heating the object to be processed, and the discharge amount is rapidly reduced.

上記実施例では、処理対象物が水産廃棄物であったが、本発明はこれに限定されることなく、処理対象物は農剤廃棄物、例えば稲わら、野菜くず、枯草、枯葉、木片、枝等、産業廃棄物、例えばビニールシート、廃棄プラスチック、故紙、製紙残渣、食品廃棄物、例えば残飯等であってもよい。ただし、Si樹脂は分解されないで塊として残る。   In the above embodiment, the processing object is a marine waste, but the present invention is not limited to this, and the processing object is an agricultural agent waste such as rice straw, vegetable waste, hay, dead leaves, wood chips, It may be a branch, industrial waste such as vinyl sheet, waste plastic, waste paper, papermaking residue, food waste such as leftover food. However, the Si resin remains as a lump without being decomposed.

なお、稲わら、紙類、枯れ草等は、分解開始の温度が、蛋白質に比較して低いので、水産廃棄物を亜臨界水処理する場合は、稲わら等を加えるとよい。   In addition, rice straw, papers, dead grass and the like have a lower decomposition initiation temperature than protein, so that rice straw or the like may be added when aquatic waste is treated with subcritical water.

農林水産業、食品産業、化学工業等のあらわる分野の廃棄物処理に利用することができる。   It can be used for waste disposal in various fields such as agriculture, forestry and fisheries, food industry and chemical industry.

20…亜臨界水処理装置
22…圧力容器
22A…投入口
22B…取出口
22C…水蒸気注入口
22D、22E…蒸気排出口
23A…クラッチドア
24…水蒸気供給装置
24A…ボイラー
24B…圧力調整弁
26…攪拌装置
26A…回転シャフト
26B…攪拌翼
27…モーター
28…減速機
30…水蒸気制御装置
32A、32B…温度センサー
34A、34B…圧力センサー
36…蒸気開閉弁
37…蒸気排出弁
38…開閉弁駆動装置
40…制御装置本体
50…回転シャフト制御装置
52A…回転速度センサー
52B…回転トルクセンサー
DESCRIPTION OF SYMBOLS 20 ... Subcritical water treatment apparatus 22 ... Pressure vessel 22A ... Inlet 22B ... Outlet 22C ... Steam inlet 22D, 22E ... Steam outlet 23A ... Clutch door 24 ... Steam supply device 24A ... Boiler 24B ... Pressure regulating valve 26 ... Stirring device 26A ... rotating shaft 26B ... stirring blade 27 ... motor 28 ... speed reducer 30 ... water vapor control device 32A, 32B ... temperature sensor 34A, 34B ... pressure sensor 36 ... steam on / off valve 37 ... steam discharge valve 38 ... on / off valve driving device 40 ... Control device body 50 ... Rotating shaft control device 52A ... Rotational speed sensor 52B ... Rotational torque sensor

Claims (10)

圧力容器内に、処理対象物を該圧力容器上部の投入口から投入する投入過程と、該圧力容器内に高温、高圧の水蒸気を供給して、該圧力容器内の処理対象物を攪拌しつつ加温、加圧して分解する亜臨界水処理過程と、前記圧力容器を開けて、前記亜臨界水処理過程を経た前記処理対象物を取出す過程と、を有してなり、
前記亜臨界水処理過程は、
それまでほぼ時間に比例して穏やかな傾きの直線状に上昇していた、前記圧力容器内の温度又は圧力が、前記傾きに対して20%以上大きい傾きの曲線又は直線に沿って上昇する場合を、急上昇と定義したとき、前記処理対象物の一部の結合の分解が開始するタイミングを、前記圧力容器内の温度が150℃以上の範囲で、前記圧力容器内の1以上の個所の温度及び1以上の個所の圧力のうち、1個所の温度又は圧力の急上昇から検出する過程と、
前記の検出の後、前記圧力容器内の温度を、水蒸気の供給量を調整することにより、前記分解の開始のタイミングにおける温度に5〜10分間維持して、前記処理対象物の一部の分解熱により、他の部分の結合の分解を促す過程と、
前記5〜10分間の経過後に水蒸気の供給を停止し、且つ、前記処理対象物の他の部分 が分解してから、前記圧力容器内の水蒸気を排出する過程と、
を有することを特徴とする亜臨界水処理方法。
A charging process in which an object to be treated is introduced into the pressure vessel from an inlet at the top of the pressure vessel, and high-temperature and high-pressure steam is supplied into the pressure vessel, and the object to be treated in the pressure vessel is stirred. A subcritical water treatment process that decomposes by heating and pressurization, and a process of opening the pressure vessel and taking out the processing object through the subcritical water treatment process,
The subcritical water treatment process includes:
The temperature or pressure in the pressure vessel, which had risen in a straight line with a gentle slope in proportion to the time until then, rises along a curve or straight line with a slope that is 20% or more larger than the slope. Is defined as a sudden rise, the timing at which decomposition of a part of the object to be processed starts, and the temperature in the pressure vessel is within a range of 150 ° C. or more, and the temperature at one or more locations in the pressure vessel. And a process of detecting from a sudden rise in temperature or pressure at one of the one or more pressures;
After the detection, the temperature in the pressure vessel is maintained at the temperature at the timing of the decomposition for 5 to 10 minutes by adjusting the supply amount of water vapor, and a part of the processing object is decomposed. The process of promoting the decomposition of bonds in other parts by heat,
A process of stopping the supply of water vapor after the lapse of 5 to 10 minutes and discharging the water vapor in the pressure vessel after the other part of the processing object is decomposed ;
A subcritical water treatment method characterized by comprising:
圧力容器内に、処理対象物を該圧力容器上部の投入口から投入する投入過程と、該圧力 容器内に高温、高圧の水蒸気を供給して、該圧力容器内の処理対象物を攪拌しつつ加温、 加圧して分解する亜臨界水処理過程と、前記圧力容器を開けて、前記亜臨界水処理過程を 経た前記処理対象物を取出す過程と、を有してなる亜臨界水処理方法であって、
圧力容器内に高温、高圧の水蒸気を供給して、該圧力容器内の処理対象物を攪拌しつつ 加温、加圧したとき、それまでほぼ時間に比例して穏やかな傾きの直線状に上昇していた 、前記圧力容器内の温度又は圧力が、前記傾きに対して20%以上大きい傾きの曲線又は 直線に沿って上昇する場合を、急上昇と定義したとき、前記圧力容器内における前記急上 昇の開始時の温度を前記処理対象物における含有物の種類毎に予め測定しておく過程を設 け、
前記亜臨界水処理過程は、
前記圧力容器内の温度が150℃以上の範囲で、前記圧力容器内の1以上の個所の温度 のうち、1個所の温度が、前記予め測定された急上昇開始時の温度に到達したときを検出 する過程と、
前記の検出の後、前記圧力容器内の温度を、水蒸気の供給量を調整することにより、前 記処理対象物の一部の分解の開始のタイミングにおける前記予め測定された急上昇開始時 温度に5〜10分間維持して、前記処理対象物の一部の分解熱により、他の部分の結合の分解を促す過程と、
前記5〜10分間の経過後に水蒸気の供給を停止し、且つ、前記処理対象物の他の部分 が分解してから、前記圧力容器内の水蒸気を排出する過程と、
を有することを特徴とする亜臨界水処理方法。
A charging process in which an object to be treated is introduced into the pressure vessel from an inlet at the top of the pressure vessel, Supply high-temperature and high-pressure steam into the container, and heat the processing object in the pressure container while stirring. The subcritical water treatment process that decomposes by pressurization and the subcritical water treatment process by opening the pressure vessel A process of taking out the treated object, and a subcritical water treatment method comprising:
Supply high-temperature and high-pressure steam into the pressure vessel, and stir the object to be processed in the pressure vessel. When heating and pressurizing, it had risen in a straight line with a gentle slope almost proportional to the time. The temperature or pressure in the pressure vessel is a curve having an inclination of 20% or more larger than the inclination or When rising along a straight line is defined as a sudden rise, the sudden rise in the pressure vessel The temperature at the start of the ascentIn advance for each type of inclusion in the object to be treatedSet up a process to measure The
The subcritical water treatment process includes:
In the range where the temperature in the pressure vessel is 150 ° C. or higher,In the pressure vesselOne or more locationstemperature One of themWhen the temperature reaches the pre-measured temperature at the start of the sudden riseDetect The process of
After said detectionThe temperature in the pressure vessel,By adjusting the supply amount of water vapor, Some of the objects to be processedAt the start of decompositionAt the start of the pre-measured spike ofThe process of maintaining the temperature for 5 to 10 minutes and promoting the decomposition of the bonds of other parts by the heat of decomposition of the part of the objectWhen,
Stop the supply of water vapor after the elapse of 5 to 10 minutes, and other part of the processing object A process of discharging water vapor in the pressure vessel after being decomposed;
HaveA subcritical water treatment method characterized by the above.
請求項において、
前記予め測定された温度のうち、前記急上昇開始時の温度が最もい種類の前記含有物についての前記急上昇開始時の温度が測定されたとき、前記圧力容器内の温度を、前記 上昇開始時の温度に5〜10分間維持して、前記処理対象物の一部の分解熱により、他の部分の結合の分解を促す過程を開始することを特徴とする亜臨界水処理方法。
In claim 2 ,
Wherein among the previously measured temperature, when the temperature of the jump start of the jump start temperature lowest had a type of the content of is measured, the temperature of the pressure vessel, the sudden increase start A subcritical water treatment method, comprising maintaining a temperature at the time for 5 to 10 minutes, and starting a process of promoting decomposition of bonds in other parts by heat of decomposition of a part of the object to be treated.
請求項1乃至3のいずれかにおいて、  In any one of Claims 1 thru | or 3,
前記水蒸気の供給量の調整を、前記分解の開始のタイミングからの追加の水蒸気による  The adjustment of the supply amount of the steam is performed by additional steam from the timing of the start of the decomposition. 加熱、加圧をしないことで実行することを特徴とする亜臨界水処理方法。A subcritical water treatment method, which is carried out without heating and pressurization.
請求項1乃至4のいずれかにおいて、
前記処理対象物を攪拌する攪拌装置の回転シャフトを、モーターから減速機を介して駆動するようにし、この回転シャフトの回転トルクと回転速度との積が一定となるように、前記減速機を介して前記回転シャフトの回転速度を制御することを特徴とする亜臨界水処理方法。
In any one of Claims 1 thru | or 4 ,
The rotating shaft of the stirring device that stirs the object to be processed is driven from the motor through the speed reducer, and the product of the rotational torque and the rotational speed of the rotating shaft is made constant through the speed reducer. And controlling the rotational speed of the rotary shaft.
請求項において、
前記圧力容器内の温度が150℃を越えること、及び、前記回転シャフトの回転トルクの変動幅が一定値以下となることの一方の条件が充足されたときから、前記圧力容器内の温度及び圧力の少なくとも一方の急上昇開始時の検知を開始することを特徴とする亜臨界水処理方法。
In claim 5 ,
The temperature and pressure in the pressure vessel are satisfied when one of the conditions that the temperature in the pressure vessel exceeds 150 ° C. and the fluctuation range of the rotational torque of the rotary shaft becomes a certain value or less is satisfied. A subcritical water treatment method characterized by starting detection of at least one of the sudden rises.
圧力容器内に高温、高圧の水蒸気を注入して、該圧力容器内の処理対象物を、亜臨界状態として分解する亜臨界水処理装置であって、
前記圧力容器内に高温、高圧の水蒸気を供給する水蒸気供給装置と、
前記圧力容器内で、前記処理対象物を攪拌する複数の攪拌翼、及び、この攪拌翼を駆動する回転シャフトを含む攪拌装置と、
この回転シャフトを、減速機を介して駆動するモーターと、
前記水蒸気供給装置を制御して、前記圧力容器への水蒸気供給量を制御する水蒸気制御装置と、
前記圧力容器の上部に設けられた、前記処理対象物の投入口、前記圧力容器の下部に設けられた、処理済の前記処理対象物を取出すための取出口、及び、前記圧力容器に設けられた、前記高温、高圧の水蒸気を注入するための水蒸気注入口と、
を有してなり、
前記水蒸気制御装置は、圧力容器内の1以上の個所の温度を測定する温度センサーと、圧力容器内の1以上の個所の圧力を測定する圧力センサーと、これらのセンサー出力信号が入力される制御装置本体と、この制御装置本体からの指令信号に基づいて、前記水蒸気供給装置による水蒸気供給量を調節する蒸気開閉弁を駆動する開閉弁駆動装置と、を有し、
それまでほぼ時間に比例して穏やかな傾きの直線状に上昇していた、前記圧力容器内の温度又は圧力が、前記傾きに対して20%以上大きい傾きの曲線又は直線に沿って上昇する場合を、急上昇と定義したとき、前記制御装置本体は、前記圧力容器内の温度が150℃を越えた範囲で、前記温度センサーによる検出温度及び前記圧力センサーにおける検出圧力の少なくとも一方が、急上昇したとき、前記開閉弁駆動装置に対して、水蒸気の供給 量を調整することにより、前記圧力容器内における前記急上昇開始時の温度を5〜10分間維持して、前記処理対象物の一部の分解熱により、他の部分の結合の分解を促すように、前記蒸気開閉弁を制御する指令信号を出力し、且つ、前記5〜10分間の経過後に、前記蒸気開閉弁を閉じる指令信号を出力し、且つ、前記処理対象物の他の部分が分解してか ら、前記圧力容器内の水蒸気を排出する信号を出力するように構成されたことを特徴とする亜臨界水処理装置。
A subcritical water treatment apparatus for injecting high-temperature and high-pressure steam into a pressure vessel and decomposing a treatment object in the pressure vessel as a subcritical state,
A steam supply device for supplying high-temperature, high-pressure steam into the pressure vessel;
In the pressure vessel, a plurality of stirring blades for stirring the object to be processed, and a stirring device including a rotating shaft for driving the stirring blades;
A motor that drives the rotating shaft via a speed reducer;
A water vapor control device that controls the water vapor supply device to control the amount of water vapor supplied to the pressure vessel;
Provided in the pressure vessel, provided in the upper portion of the pressure vessel, provided in the lower portion of the pressure vessel, and provided in the lower portion of the pressure vessel for taking out the processed treatment object. A steam inlet for injecting the high-temperature, high-pressure steam;
Having
The water vapor control device includes a temperature sensor that measures the temperature of one or more locations in the pressure vessel, a pressure sensor that measures the pressure of one or more locations in the pressure vessel, and a control to which these sensor output signals are input. An apparatus main body, and an on-off valve driving device for driving a steam on-off valve that adjusts the amount of water vapor supplied by the water vapor supply device based on a command signal from the control device main body,
The temperature or pressure in the pressure vessel, which had risen in a straight line with a gentle slope in proportion to the time until then, rises along a curve or straight line with a slope that is 20% or more larger than the slope. Is defined as a sudden rise, when the temperature inside the pressure vessel exceeds 150 ° C., at least one of the temperature detected by the temperature sensor and the pressure detected by the pressure sensor suddenly rises. By adjusting the supply amount of water vapor to the on-off valve driving device, the temperature at the start of the sudden rise in the pressure vessel is maintained for 5 to 10 minutes, and the partial decomposition heat of the processing object To output a command signal for controlling the steam on-off valve so as to promote disassembly of other parts, and to close the steam on-off valve after the elapse of 5 to 10 minutes. Outputs, and the processing other portions et al or by decomposition of the object, the sub-critical water treatment apparatus characterized by being configured to output a signal for discharging the steam in the pressure vessel.
圧力容器内に高温、高圧の水蒸気を注入して、該圧力容器内の処理対象物を、亜臨界状 態として分解する亜臨界水処理装置であって、
前記圧力容器内に高温、高圧の水蒸気を供給する水蒸気供給装置と、
前記圧力容器内で、前記処理対象物を攪拌する複数の攪拌翼、及び、この攪拌翼を駆動 する回転シャフトを含む攪拌装置と、
この回転シャフトを、減速機を介して駆動するモーターと、
前記水蒸気供給装置を制御して、前記圧力容器への水蒸気供給量を制御する水蒸気制御 装置と、
前記圧力容器の上部に設けられた、前記処理対象物の投入口、前記圧力容器の下部に設 けられた、処理済の前記処理対象物を取出すための取出口、及び、前記圧力容器に設けら れた、前記高温、高圧の水蒸気を注入するための水蒸気注入口と、
を有してなり、
前記水蒸気制御装置は、圧力容器内の1以上の個所の温度を測定する温度センサーと、 圧力容器内の1以上の個所の圧力を測定する圧力センサーと、これらのセンサー出力信号 が入力される制御装置本体と、この制御装置本体からの指令信号に基づいて、前記水蒸気 供給装置による水蒸気供給量を調節する蒸気開閉弁を駆動する開閉弁駆動装置と、を有し
圧力容器内に高温、高圧の水蒸気を供給して、該圧力容器内の処理対象物を攪拌しつつ 加温、加圧したとき、それまでほぼ時間に比例して穏やかな傾きの直線状に上昇していた 、前記圧力容器内の温度又は圧力が、前記傾きに対して20%以上大きい傾きの曲線又は 直線に沿って上昇する場合を、急上昇と定義したとき、前記制御装置本体は、前記処理対象物における含有物の種類毎に予め測定された前記急上昇開始時の温度が記憶されている記憶部を有し、且つ、前記圧力容器内の温度が、前記処理対象物における含有物の種類に対応する前記記憶された温度に到達したときの前記温度センサーの出力信号に基づき、 記開閉弁駆動装置に対して、水蒸気の供給量を調整することにより、前記圧力容器内にお ける前記急上昇開始時の温度5〜10分間維持して、前記処理対象物の一部の分解熱により、他の部分の結合の分解を促すように、前記蒸気開閉弁を制御する指令信号を出力し 、且つ、前記5〜10分間の経過後に、前記蒸気開閉弁を閉じる指令信号を出力し、且つ 、前記処理対象物の他の部分が分解してから、前記圧力容器内の水蒸気を排出する信号を出力するように構成されたことを特徴とする亜臨界水処理装置。
High temperature pressure vessel, by injecting high-pressure steam, a processing object of the pressure vessel, a sub-critical water treatment apparatus for decomposing a subcritical state,
A steam supply device for supplying high-temperature, high-pressure steam into the pressure vessel;
In the pressure vessel, a plurality of stirring blades for stirring the object to be processed, and a stirring device including a rotating shaft for driving the stirring blades ;
A motor that drives the rotating shaft via a speed reducer;
A water vapor control device that controls the water vapor supply device to control the amount of water vapor supplied to the pressure vessel ;
Wherein provided on the upper portion of the pressure vessel, inlet of the processing object, said kicked set at the bottom of the pressure vessel, outlet for taking out the processing object processed, and, provided in the pressure vessel et a, and the hot, steam injection port for injecting the high pressure steam,
Having
The water vapor control device includes a temperature sensor that measures the temperature of one or more locations in the pressure vessel, a pressure sensor that measures the pressure of one or more locations in the pressure vessel, and a control to which these sensor output signals are input. An apparatus main body, and an on- off valve driving device for driving a steam on-off valve that adjusts the amount of water vapor supplied by the water vapor supply device based on a command signal from the control device main body ,
When high-temperature and high-pressure steam is supplied into the pressure vessel and the object to be treated in the pressure vessel is heated and pressurized while stirring , it rises in a straight line with a gentle slope almost proportional to the time until then. When the temperature or pressure in the pressure vessel that rises along a curve or straight line having a slope that is 20% or more larger than the slope is defined as a sudden rise, the control device main body It has a storage unit that stores the temperature at the start of the sudden rise measured in advance for each type of inclusion in the object, and the temperature in the pressure vessel is the kind of inclusion in the processing object. based on the output signal of the temperature sensor when it reaches the corresponding said stored temperature, for the previous SL-off valve driving apparatus, by adjusting the amount of water vapor supply, our Keru the spike in the pressure vessel the temperature at the start of It was maintained to 10 minutes, by a portion of the heat of decomposition of the processing object, to urge the degradation of the binding of the other part, and outputs a command signal for controlling the vapor-off valve, and the 5-10 After a lapse of minutes, a command signal for closing the steam on-off valve is output, and a signal for discharging the water vapor in the pressure vessel is output after the other part of the processing object is decomposed. A subcritical water treatment apparatus characterized by that.
請求項7又は8において、  In claim 7 or 8,
前記制御装置本体は、前記開閉弁駆動装置に対して、前記急上昇開始のタイミングから  The control device main body starts from the timing of the sudden rise with respect to the on-off valve drive device. の追加の水蒸気による加熱、加圧をしないことで、前記水蒸気の供給量の調整をする信号A signal to adjust the supply amount of water vapor by not heating or pressurizing with additional water vapor を出力するように構成されたことを特徴とする亜臨界水処理装置。The subcritical water treatment apparatus is configured to output
請求項7乃至9のいずれかにおいて、
前記回転シャフトの回転速度センサー及び回転トルクを検出する回転トルクセンサーと、
この回転速度センサー及び回転トルクセンサーの出力信号が入力される回転シャフト制御装置と、を更に有し、
この回転シャフト制御装置は、前記回転シャフトの回転速度と回転トルクとの積が一定値となるように、前記回転シャフトの回転速度を、前記減速機を介して制御するように構成されたことを特徴とする亜臨界水処理装置。
In any one of Claims 7 thru | or 9 ,
A rotational speed sensor for detecting a rotational speed sensor and a rotational torque of the rotational shaft;
A rotation shaft control device to which output signals of the rotation speed sensor and the rotation torque sensor are input, and
The rotation shaft control device is configured to control the rotation speed of the rotation shaft via the speed reducer so that a product of the rotation speed and the rotation torque of the rotation shaft becomes a constant value. A subcritical water treatment device.
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