JP2003305328A5 - - Google Patents

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JP2003305328A5
JP2003305328A5 JP2002319388A JP2002319388A JP2003305328A5 JP 2003305328 A5 JP2003305328 A5 JP 2003305328A5 JP 2002319388 A JP2002319388 A JP 2002319388A JP 2002319388 A JP2002319388 A JP 2002319388A JP 2003305328 A5 JP2003305328 A5 JP 2003305328A5
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digestion gas
reaction tower
gas
water
digestion
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JP2002319388A
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JP2003305328A (en
JP3750648B2 (en
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有機性廃棄物をメタン発酵させて発生した消化ガスが導入され、微生物が付着する充填材を充填した反応塔と、該反応塔へ導入前の消化ガスに空気を供給する空気供給手段と、導入後の消化ガスに水を散布するスプレーノズルとを備えた消化ガスの脱硫装置において、
前記充填材が反応塔内に設けた多孔板状支持部材の上に固定せずに充填されてなり、かつ、前記消化ガスの導入口が前記反応塔の頂部に下向きに設けられていることを特徴とする消化ガスの脱硫装置。
A digestion gas generated by methane fermentation of organic waste is introduced, a reaction tower filled with a filler to which microorganisms adhere, an air supply means for supplying air to the digestion gas before introduction into the reaction tower, and introduction In the digestion gas desulfurization apparatus equipped with a spray nozzle for spraying water to the later digestion gas,
The filler is packed without being fixed on a porous plate-like support member provided in the reaction tower, and the digestion gas inlet is provided downward at the top of the reaction tower. A digester gas desulfurization unit.
前記充填材は、比重が0.9〜1.05で、且つ容積率で80〜95%の空隙を有する合成樹脂体であることを特徴とする請求項1記載の消化ガスの脱硫装置。The digester gas desulfurization apparatus according to claim 1 , wherein the filler is a synthetic resin body having a specific gravity of 0.9 to 1.05 and a void of 80 to 95% by volume ratio . 前記反応塔内を流通する消化ガスの圧力損失を測定するセンサと、その測定値が入力され、予め記憶させてある圧力損失の閾値を超えたら、前記消化ガスの反応塔への導入停止を指令する信号及び/又は警報を出力する演算器とを備えたことを特徴とする請求項1又は2記載の消化ガスの脱硫装置。  A sensor for measuring the pressure loss of the digestion gas flowing through the reaction tower, and when the measured value is input and exceeds a prestored pressure loss threshold value, commands to stop introducing the digestion gas into the reaction tower The digester gas desulfurization apparatus according to claim 1, further comprising: an arithmetic unit that outputs a signal and / or an alarm. 前記反応塔の塔壁、循環水配管又は底部の循環水溜まりに、加熱装置を設けたことを特徴とする請求項1〜3のいずれかに記載の消化ガスの脱硫装置。  The digester gas desulfurization apparatus according to any one of claims 1 to 3, wherein a heating device is provided in a tower wall, a circulating water pipe, or a circulating water pool at the bottom of the reaction tower. 微生物が付着する充填材を充填した反応塔内へ、有機性廃棄物をメタン発酵させて発生した消化ガスを、空気を添加してから導入し、水を散布して消化ガスが含有する硫化水素を洗浄、除去する消化ガスの脱硫方法において、散布する水の一部を反応塔内で循環させると共に、その循環水のpHを測定し、そのpHが1〜6になるように、新水の補給で調整することを特徴とする消化ガスの脱硫方法。  Hydrogen sulfide contained in the digestion gas by introducing the digestion gas generated by methane fermentation of organic waste into the reaction tower packed with the packing material to which microorganisms adhere, after adding air, and spraying water In the desulfurization method for digestion gas, which is washed and removed, a part of the sprayed water is circulated in the reaction tower, the pH of the circulating water is measured, and the fresh water is adjusted so that the pH becomes 1-6. Digestion gas desulfurization method characterized by adjusting by replenishment. 前記新水及び/又は前記散布する水に、前記メタン発酵した消化ガスの冷却で発生する凝縮水及び/又は発酵後の残液を脱水して得た処理水を用いることを特徴とする請求項5記載の消化ガスの脱硫方法。  The treated water obtained by dehydrating the condensed water generated by cooling the digested gas subjected to methane fermentation and / or the residual liquid after fermentation is used for the fresh water and / or the sprayed water. 6. The method for desulfurizing digestion gas according to 5. 前記新水及び/又は前記散布する水に、前記微生物の付着を促進する薬剤を添加することを特徴とする請求項5又は6記載の消化ガスの脱硫方法。  The digestion gas desulfurization method according to claim 5 or 6, wherein a chemical that promotes adhesion of the microorganism is added to the fresh water and / or the sprayed water. 前記反応塔から排出された消化ガスの酸素濃度を測定し、その測定値が所定の目標値になるように、反応塔への導入前に添加する前記空気の量を自動調整すると共に、同時に該消化ガスの硫化水素濃度も測定し、その測定値に応じて前記酸素濃度の目標値を自動的に変更することを特徴とする請求項5〜7のいずれかに記載の消化ガスの脱硫方法。  The oxygen concentration of the digestion gas discharged from the reaction tower is measured, and the amount of the air added before introduction into the reaction tower is automatically adjusted so that the measured value becomes a predetermined target value. The method for desulfurization of digestion gas according to any one of claims 5 to 7, wherein the hydrogen sulfide concentration of the digestion gas is also measured, and the target value of the oxygen concentration is automatically changed according to the measured value. 前記反応塔へ導入前の有機性廃棄物をメタン発酵させて発生した消化ガスの流量を予め測定し、その測定値に対して一定割合となる空気を該消化ガスに添加してから、前記反応塔内へ導入することを特徴とする請求項5〜7のいずれかに記載の消化ガスの脱硫方法。  The flow rate of the digestion gas generated by methane fermentation of the organic waste before introduction into the reaction tower is measured in advance, and the reaction gas is added to the digestion gas with a constant ratio of the measured value. It introduce | transduces in a tower | column, The desulfurization method of the digestion gas in any one of Claims 5-7 characterized by the above-mentioned. 請求項5〜9のいずれか記載の消化ガスの脱硫方法を実施して、前記微生物及び/又は硫化水素が酸化されてできた単体硫黄の成長で充填材の空隙が閉塞してきたら、前記反応塔内に充填材の充填高さ以上の高さまで水を張り、下部から空気を吹き込んで該充填材を水中で浮動させ、空気の上昇流で微生物や単体硫黄を剥離させて洗浄し、ドレンとして反応塔より流出させることを特徴とする請求項5〜9のいずれかに記載の消化ガスの脱硫方法。  When the digestion gas desulfurization method according to any one of claims 5 to 9 is carried out and the voids of the filler are blocked by the growth of elemental sulfur formed by oxidizing the microorganisms and / or hydrogen sulfide, the reaction tower Fill the inside with water up to the filling height of the filling material, blow air from the lower part to float the filling material in the water, remove the microorganisms and elemental sulfur with the rising air flow, wash and react as drain The desulfurization method for digestion gas according to any one of claims 5 to 9, wherein the desulfurization gas is caused to flow out of the tower. 前記充填材の洗浄を行うタイミングを、反応塔の圧力損失の値で判断することを特徴とする請求項10記載の消化ガスの脱硫方法。  The digestion gas desulfurization method according to claim 10, wherein the timing of cleaning the packing material is determined by a pressure loss value of the reaction tower.
JP2002319388A 2001-11-02 2002-11-01 Digestion gas desulfurization apparatus and desulfurization method Expired - Lifetime JP3750648B2 (en)

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JP2001337290 2001-11-02
JP2001-337290 2001-11-02
JP2002-33548 2002-02-12
JP2002033548 2002-02-12
JP2002319388A JP3750648B2 (en) 2001-11-02 2002-11-01 Digestion gas desulfurization apparatus and desulfurization method

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JP2003305328A JP2003305328A (en) 2003-10-28
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