JP2017514689A - アスベスト含有材料の生化学的変性のための方法 - Google Patents
アスベスト含有材料の生化学的変性のための方法 Download PDFInfo
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Abstract
Description
(1)食品産業の廃棄材料に対し、細菌および真菌の成長および/または発酵の組み合わせを行うことによって、好ましくは、Acetobacter aceti種の細菌と、Saccharomyces cerevisiae種の酵母を用いることによって、酸性溶液/懸濁物を調製する工程と、
(2)アスベスト含有材料を、前記発酵の組み合わせから得られた酸性溶液/懸濁物で、120〜170℃の温度、加圧下で1〜24時間処理する工程と、
を含む、方法に関する。
酢製造から得られる液体/固体廃棄物、ワイン製造から得られる液体/固体廃棄物、油製造から得られる廃棄物(例えば、ミルの廃水)、果実の処理もしくは保護または野菜の処理もしくは保護から得られる液体/固体廃棄物(例えば、トマトの皮を漂白するための水、柑橘類の皮を漂白するための水)、ビールの製造から得られる液体/固体廃棄物、飲料の製造から得られる液体/固体廃棄物、果実系ジュースの製造から得られる液体/固体廃棄物、油の精製産業から得られる液体廃棄物、植物性の脂肪の精製産業から得られる液体廃棄物、動物性の脂肪の精製産業から得られる液体廃棄物、使用済の茶葉から得られる液体/固体廃棄物、製菓産業から得られる液体/固体廃棄物、米の処理から得られる液体/固体廃棄物、タバコ製造から得られる液体/固体廃棄物
から選択される。
ワインビネガー製造に使用するつるの剪定から得られる木材存在下、水中の廃棄材料を培養することによって、ビネガー製造から得られた廃棄物から誘導された残留微生物を成長させ、発酵させる。微生物の成長および発酵のための温度は、15〜25℃であり、24〜48時間の範囲である。酸(特に、酢酸および酒石酸)の生成がこの工程中に起こる。このようにして、極端な好酸性微生物および好酸性微生物の代謝活性を上げるために溶液に加えてもよい、または溶液に加えなければならない糖栄養分の量および品質にも依存して、pHが0〜6、好ましくは約2の酸性溶液/懸濁物が得られる。
水中で、液体/固体廃棄材料(絞りかす)を、好ましくは15〜25℃の温度で24〜48時間培養することによって、細菌および真菌の発酵の組み合わせを行う。酸(特に、酢酸および酒石酸)の生成がこの工程中に起こる。このようにして、極端な好酸性微生物および好酸性微生物の代謝活性を上げるために溶液に加えてもよい、または溶液に加えなければならない糖栄養分の量および品質にも依存して、pHが0〜6、好ましくは約2の酸性溶液/懸濁物が得られる。
缶詰工場の廃棄物の処理から誘導される残留微生物を、水中で液体/固体廃棄材料を培養することによって成長させ、発酵させる。微生物の成長および発酵のための温度は、15〜25℃であり、24〜48時間の範囲である。酸(特に、酢酸)の生成がこの工程中に起こる。このようにして、極端な好酸性微生物および好酸性微生物の代謝活性を上げるために溶液に加えてもよい、または溶液に加えなければならない糖栄養分の量および品質にも依存して、pHが0〜6、好ましくは約2の酸性溶液/懸濁物が得られる。
Claims (10)
- アスベスト含有材料を処理するための方法であって、
食品産業の廃棄材料に対し、細菌および真菌の成長および/または発酵の組み合わせを行うことによって、酸性溶液/懸濁物を調製すること、および
アスベスト含有材料を、前記発酵の組み合わせから得られた酸性溶液/懸濁物で、120〜170℃の温度、2〜10barの圧力で処理すること、
を含む、方法。 - 前記成長および/または発酵の組み合わせが、Acetobacter aceti種の細菌と、Saccharomyces cerevisiae種の酵母を用いることによって行われる、
請求項1に記載の方法。 - 前記成長および/または発酵の組み合わせが、
cerevisiae Micrococcaceae、Propionibacteria、Bifidobacteria、Pseudomonas spp.、Aeromonas spp.、Photobacterium spp.、Achromobacter spp.、Shewanella spp.、Xanthomonas spp.、Vibrio spp.、Flavobacterium spp.、Enterobacteriaceae、Bacillus spp.、Clostridium spp.、Brochothrix thermosphacta、Micrococcus spp.、食品産業の廃棄物中に存在する極端な好酸性微生物または好酸性微生物に分類される乳酸菌または微生物、
の1つ以上を単独で、または組み合わせて、また、Acetobacter aceti種と共に用いることによって行われる、
請求項1または2に記載の方法。 - 前記食品産業の廃棄材料が、
酢製造から得られる液体/固体廃棄物、ワイン製造から得られる液体/固体廃棄物、油製造から得られる廃棄物(好ましくは、ミルの廃水)、果実の処理もしくは保護または野菜の処理もしくは保護から得られる液体/固体廃棄物(好ましくは、トマトの皮を漂白するための水、柑橘類の皮を漂白するための水)、ビールの製造から得られる液体/固体廃棄物、飲料の製造から得られる液体/固体廃棄物、果実系ジュースの製造から得られる液体/固体廃棄物、油の精製産業から得られる液体廃棄物、植物性の脂肪の精製産業から得られる液体廃棄物、動物性の脂肪の精製産業から得られる液体廃棄物、使用済の茶葉から得られる液体/固体廃棄物、製菓産業から得られる液体/固体廃棄物、米の処理から得られる液体/固体廃棄物、タバコ製造から得られる液体/固体廃棄物
から選択される、
請求項1〜3のいずれか一項に記載の方法。 - 前記アスベスト含有材料が、脆いマトリックスまたはセメントマトリックス、または圧縮ポリマー型マトリックスに分散したフィブリル形態のアスベストを含む、
請求項1〜4のいずれか一項に記載の方法。 - 前記アスベスト含有材料が、アスベストセメントである、
請求項1〜5のいずれか一項に記載の方法。 - 前記細菌および真菌の発酵の組み合わせは、使用する食品廃棄物の種類に依存して、食品産業の廃棄材料を15〜25℃の温度で、数分から数時間および数日間、培養することによって行われる、
請求項1〜6のいずれか一項に記載の方法。 - 発酵の組み合わせから誘導される酸性溶液/懸濁物で処理する前に、繊維が空気中に放出されるのを防ぐために、前記アスベスト含有材料は、水の霧および減圧条件で粉砕し、好ましくは、いくつかの工程で、アスベスト含有材料をまず大きな粒径に砕き、次いで、1ミリメートル未満の寸法になるまで粉砕する、
請求項1〜7のいずれか一項に記載の方法。 - 酸性溶液/懸濁物を用いたアスベスト含有材料の処理は、アスベスト含有材料を、酸性溶液/懸濁物と共に12〜24時間かけて均質化することによって行われる、
請求項1〜8のいずれか一項に記載の方法。 - 120〜170℃の温度は、好ましくは、1回の処理サイクルで、20℃から170℃までの温度勾配を適用することによって到達する、
請求項1〜9のいずれか一項に記載の方法。
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