JP2013517199A5 - - Google Patents

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JP2013517199A5
JP2013517199A5 JP2012548445A JP2012548445A JP2013517199A5 JP 2013517199 A5 JP2013517199 A5 JP 2013517199A5 JP 2012548445 A JP2012548445 A JP 2012548445A JP 2012548445 A JP2012548445 A JP 2012548445A JP 2013517199 A5 JP2013517199 A5 JP 2013517199A5
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JP
Japan
Prior art keywords
chlorine dioxide
aqueous solution
solution containing
storage tank
containing chlorine
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JP2012548445A
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English (en)
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JP2013517199A (ja
JP5735985B2 (ja
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Priority claimed from PCT/EP2011/050430 external-priority patent/WO2011086147A1/en
Publication of JP2013517199A publication Critical patent/JP2013517199A/ja
Publication of JP2013517199A5 publication Critical patent/JP2013517199A5/ja
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Publication of JP5735985B2 publication Critical patent/JP5735985B2/ja
Expired - Fee Related legal-status Critical Current
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Description

Figure 2013517199

Claims (12)

  1. メタノールを還元剤として用いて塩素酸イオンから二酸化塩素を製造する方法であって、二酸化塩素を含有する水溶液を形成すること、前記二酸化塩素を含有する水溶液の少なくとも一部を60分未満の平均滞留時間内にその最終用途へ送ること、得られた二酸化塩素を含有する水溶液の一部を少なくとも1つの貯蔵タンクに保持することを含む、二酸化塩素を製造する方法。
  2. 前記平均滞留時間が30分未満である、請求項1に記載の方法。
  3. 前記少なくとも1つの貯蔵タンクでの平均滞留時間が1日〜8週である、請求項1又は2に記載の方法。
  4. 前記二酸化塩素を含有する水溶液をポンプタンクに送り、前記水溶液の少なくとも一部をポンプタンクから最終用途に送ることをさらに含む、請求項1から3のいずれか一項に記載の方法。
  5. 前記ポンプタンクでの平均滞留時間が、前記少なくとも1つの貯蔵タンクでの平均滞留時間よりも短い、請求項4に記載の方法。
  6. 前記ポンプタンクでの平均滞留時間が1〜40分である、請求項5に記載の方法。
  7. 二酸化塩素を含有するガスを水性反応媒体から抜き出すこと、前記ガスからの二酸化塩素を水に吸収させることをさらに含む、請求項1から6のいずれか一項に記載の方法。
  8. 二酸化塩素を吸収させるのに使用する水の温度が0〜16℃である、請求項7に記載の方法。
  9. 前記少なくとも1つの貯蔵タンク内の前記二酸化塩素を含有する水溶液を、そこへ送られる前記二酸化塩素を含有する水溶液の温度よりも低い温度で保持する、請求項1から8のいずれか一項に記載の方法。
  10. 前記少なくとも1つの貯蔵タンク内の前記二酸化塩素を含有する水溶液の温度が0〜12℃である、請求項1から9のいずれか一項に記載の方法。
  11. 前記少なくとも1つの貯蔵タンクに送られる前記二酸化塩素を含有する水溶液を、前記タンクに入れる前に精製することをさらに含む、請求項1から10のいずれか一項に記載の方法。
  12. 前記精製が、前記水溶液から二酸化塩素ガスをストリッピングすること、次いで二酸化塩素を水に吸収させて前記少なくとも1つの貯蔵タンクに送られる精製水溶液を得ることを含む、請求項11に記載の方法。
JP2012548445A 2010-01-18 2011-01-14 二酸化塩素の製造方法 Expired - Fee Related JP5735985B2 (ja)

Applications Claiming Priority (5)

Application Number Priority Date Filing Date Title
US29588110P 2010-01-18 2010-01-18
US61/295,881 2010-01-18
EP10150944 2010-01-18
EP10150944.6 2010-01-18
PCT/EP2011/050430 WO2011086147A1 (en) 2010-01-18 2011-01-14 Process for the production of chlorine dioxide

Publications (3)

Publication Number Publication Date
JP2013517199A JP2013517199A (ja) 2013-05-16
JP2013517199A5 true JP2013517199A5 (ja) 2014-07-31
JP5735985B2 JP5735985B2 (ja) 2015-06-17

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ID=42224034

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2012548445A Expired - Fee Related JP5735985B2 (ja) 2010-01-18 2011-01-14 二酸化塩素の製造方法

Country Status (15)

Country Link
US (1) US20120294794A1 (ja)
EP (1) EP2526047B1 (ja)
JP (1) JP5735985B2 (ja)
KR (1) KR101765735B1 (ja)
CN (1) CN102712471B (ja)
AR (1) AR080358A1 (ja)
AU (1) AU2011206595B2 (ja)
BR (1) BR112012016978B1 (ja)
CA (1) CA2785438C (ja)
CL (1) CL2012001982A1 (ja)
MX (1) MX340592B (ja)
MY (1) MY161887A (ja)
PT (1) PT2526047T (ja)
RU (1) RU2562858C2 (ja)
WO (1) WO2011086147A1 (ja)

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CN103101883B (zh) * 2013-03-01 2015-04-15 唐洪权 食品添加剂稳定态二氧化氯溶液生产及活化方法
CN105036083A (zh) * 2015-07-08 2015-11-11 优尼克生技股份有限公司 一种二氧化氯水溶液的保存方法
CN106865501B (zh) * 2015-12-11 2019-03-22 深圳市罗奇环保科技有限公司 二氧化氯的吸收方法
TWI750330B (zh) 2017-02-27 2021-12-21 美商藝康美國公司 用於現場產生二氧化氯之方法
WO2018175732A1 (en) 2017-03-24 2018-09-27 Ecolab USA, Inc. Low risk chlorine dioxide onsite generation system
MX2020001822A (es) 2017-08-17 2020-03-20 Ecolab Usa Inc Sistema de generacion de dioxido de cloro en el sitio de bajo riesgo.
US11970393B2 (en) 2018-07-05 2024-04-30 Ecolab Usa Inc. Decomposition mediation in chlorine dioxide generation systems through sound detection and control
KR102117101B1 (ko) 2018-08-16 2020-05-29 이준식 이산화염소수 희석 장치

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