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HAMASAKI TATSUHIDE

  (濱崎 竜英)

Profile Information

Affiliation
Professor, Faculty of Design Technology, Department of Environmental Science and Technology, Osaka Sangyo University
Degree
Master of Engineering(Mar, 1996, Osaka Sangyo University)
Doctor of Human Environment(Mar, 2016, Osaka Sangyo University)
Contact information
hamasakiest.osaka-sandai.ac.jp
Researcher number
50340617
J-GLOBAL ID
200901044796513069
researchmap Member ID
5000092821
External link

Research Areas

 2

Research History

 4

Education

 1

Committee Memberships

 33
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Awards

 1

Papers

 22
  • Tatsuhide Hamasaki, Yunqi Chen, Tadao Mizuno, Hiroshi Tsuno
    Journal of Japan Sewage Works Association, 57(687) 116-124, Jan 1, 2020  Peer-reviewed
    下水生物学的処理水を対象として、オゾン/過酸化水素処理による有機物の分解実験を、半回分式実験装置を用いて行った。通気したオゾン濃度は50 mg/Lで、過酸化水素は初期に0、7.5、30、75または150 mg/Lを添加した。生物学的処理水の場合、初期過酸化水素濃度は30 mg/Lが最も速いTOC除去速度が得られ、反応器当たり0.08〜0.11 mg C/L/minであるのに対し、生物学的処理水の後段の急速砂ろ過塔でろ過した処理水の場合、初期に添加する過酸化水素濃度は7.5 mg/Lが最も速いTOC除去速度が得られ、0.19〜0.21 mg C/L/minであった。各々で単位TOC除去当たりの消費オゾン量は、26〜36 mg O3/mg Cおよび14〜15 mg O3/mg Cであった。また、生物学的処理水と生物学的処理水をガラス繊維ろ紙でSSを除去した処理水を用いた実験でも、SSを除去した処理水が速い除去速度が得られた。このことから、TOC除去速度はSSの存在が影響することがわかった。ろ過水では、1 mg/L程度までTOCが除去された。
  • Duong Van Nam, Nguyen Hoai Chau, Hamasaki Tatsuhide, Dinh Van Vien, Phan Do Hung
    Vietnam Journal of Science and Technology, 56(2) 236-245, Mar 9, 2018  Peer-reviewed
    Two modified SBRs, specially configured to consist of both oxic and anoxic zones, and be operated with only a single simultaneous oxic/anoxic phase in each treatment batch, were tested to evaluate their applicability in the treatment of RLP wastewater. The effects of COD to TN ratio and their loading rates on the performance of the modified SBRs in the simultaneous removal of organic matter and nitrogen from RLP wastewater were investigated. It was observed that the performance of the two reactors in removal of COD and ammonium-N was similar, and did not remarkably change when varying the COD/TN ratio, as well as COD and TN loading rates in the ranges of 3.4-6.0 gCOD/gN, 0.8-1.7 kgCOD⋅m-3⋅d-1 and 0.15-0.34 kgN⋅m-3⋅d-1, respectively.
  • Tatsuhide Hamasaki
    5th International Conference on Sustainable Development, Sep 6, 2017  Peer-reviewed
  • Tatsuhide HAMASAKI, Xu JIE, Yunqi CHEN, Tadao MIZUNO, Hiroshi TSUNO
    Journal of Environmental Concervation Engineering, 46(48) 430-440, Aug 20, 2017  Peer-reviewed
    An O3/H2O2 advanced oxidation process was experimentally examined for leaching radioactive cesium from contaminated sewage sludge since the excessive oxalic acid from the conventional method of coprecipitation with ferrocyanide complex salts disturbs the process of radioactive cesium removal. The most suitable condition for leaching radioactive cesium was a pH of 3, which subsequently mineralized the oxalic acid effectively. According to this study, 30 mg/L of hydrogen peroxide was an appropriate concentration. TOC was reduced from 100 mg/L to 40 mg/L within 40 minutes. The ozone requirement per TOC removal was 1.9 mgO3/mgC. Therefore, it proved that one molecule of ozone was needed to mineralize one molecule of oxalic acid. Oxalic acid was effectively decomposed at a pH of 3. Therefore, an O3/H2O2 dvanced oxidation process using a multistage reactor with 30 mg/L of hydrogen peroxide was recommended.
  • Tatsuhide Hamasaki, Phan Do Hung, Hiroshi Tsuno
    International Journal of GEOMATE, 12(32) 37-42, Apr 1, 2017  Peer-reviewed
    Pilot tests of a cubic-lattice-based rotating biological contactor were implemented to remove organic matter from wastewater from a milk factory and a hospital in Vietnam. In the milk factory wastewater, the biochemical oxygen demand (BOD) removal ratio was stable between 60% and 90% (average 75%) using this method, with a BOD surface load of 0.002-0.020 kg•m-2•day-1. The average nutrient ratio of the raw wastewater was 0.13 of total nitrogen and 0.015 of total phosphorus compared with 1.0 of BOD. The BOD of treated water was less than 50 mg•L-1, achieving category B of the industrial wastewater standard of Vietnam (QCVN 40:2011). For the hospital wastewater, the BOD removal ratio was stable between 60% and 90% (average 78%), with a BOD surface load of 0.005-0.022 kg•m-2•day-1. The average nutrient ratio of the raw wastewater was 0.25 of total nitrogen and 0.018 of total phosphorus compared with 1.0 of BOD. The BOD of treated water was less than 50 mg•L-1, satisfying category B of the medical wastewater standard of Vietnam (QCVN 28:2010/BTNMT). The electric power consumption was 0.73 KWh•m-3 of wastewater. The sludge conversion ratio from BOD was 0.51 kg TSS•kg BOD-1 based on the excess sludge and suspended solids in raw wastewater and treated water.
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Misc.

 28
  • 藤川 陽子, 菅原 正孝, 濱崎 竜英
    環境技術 = Environmental conservation engineering, 41(2) 115-119, Feb 20, 2012  
  • FUJIKAWA Yoko, SUGAHARA Masataka, HAMASAKI Tatsuhide, YONEDA Daisuke, MINAMI Atushi, SUGIMOTO Yusuke, IWASAKI Hajime
    Osaka Sangyo University journal of human environmental studies, 9 261-276, Mar, 2010  
    We have worked on the development of a biological filtration system utilizing indigenous bacteria to remove arsenite, arsenate, iron, manganese and ammonia from groundwater. Among various bacteria, iron bacteria (bacterial species that biologically oxidize dissolved Fe and/or Mn, and deposit them as oxides) together with nitrifiers play the most important role in our system. This report is a brief summary of our pilot study (started in 2004), treating groundwater by the biological filtration. The purpose is to determine the optimal operating conditions to achieve the most efficient removal of arsenic.
  • SUGAHARA Masataka, FUJIKAWA Yoko, HAMASAKI Tatsuhide, ARAI Takenori
    Osaka Sangyo University journal of human environmental studies, 9 243-260, Mar, 2010  
  • Osaka Sangyo University journal of human environmental studies, 9 53-62, Mar, 2010  
    The purpose of this study is to remove pollution matter such as organic matter and nutrients from sewage using a bio film method with string media and then to recover the phosphorus from the used string media. The activated sludge method is the most popular method for sewage treatment. However this method produces a lot of excess sludge and increases the costs of the sewage treatment facility. The results of our experiments on removal of organic matter show that a bio film method using string bio film media can remove organic matters in sewage. Sewage also contains high concentrations of phosphorus, which should be removed to improve the treated water quality but is an important nutrient in agriculture. Since phosphorous becomes depleted in soil by agricultural activity, it must be added regularly to maintain soil fertility. This makes recovered phosphorous a valuable by-product of sewage treatment. This study therefore also evaluated phosphorus recovery from the used string media with hot water and confirmed the possibility of phosphorous recovery by that method.
  • Journal of water and waste, 51(7) 571-580, Jul, 2009  
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Books and Other Publications

 4
  • (Role: Joint author)
    学術研究出版, Apr 1, 2017
    水環境問題の起源と法整備、我が国の水環境問題の歴史、また、水環境問題のうち、生活環境項目である有機物質と栄養塩類を取り上げ、その対策の研究事例を紹介した。
  • 濱崎竜英
    ナツメ社, Jun, 2016 (ISBN: 9784816360428)
    国家試験である公害防止管理者試験（水質）では、公害総論、水質概論、汚水処理特論、水質有害物質特論及び大規模水質特論の５科目があるが、その５科目について、過去１０年間の試験問題を分析して出題傾向を示すとともに、出題傾向が高い内容について解説し、併せて問題を掲載してものである。
  • 稲森悠平, 藤田正憲, 古川憲治, 他多数 (Role: Joint author)
    株式会社エヌ・ティー・エス, May, 2007 (ISBN: 9784860431457)
    土壌浸透法による有機物やりんの除去についてとりまとめたもので、これまで実施した実験事例を紹介し、その可能性について記述している。
  • 名。監修, 菅原正孝 (Role: Joint author)
    シーエムシー出版, Dec, 2004
    環境水浄化技術中、「微生物による環境浄化の研究例・実施例」を担当した。河川や湖沼の水質改善を目的とした水浄化技術を解説している。

Presentations

 23
  • Yichen Chen, Bingzi Chen, Tatsuhide Hamasaki
    The 13th International Conference on Geotechnique, Construction Materials and Environment, Nov 15, 2023
  • Bingzi Chen, Yichen Chen, Shogo Taniguchi, Tatsuhide Hamasaki
    The 13th International Conference on Geotechnique, Construction Materials and Environment, Nov 15, 2023
  • Tatsuhide Hamasaki
    The 13th International Conference on Geotechnique, Construction Materials and Environment, Nov 15, 2023
  • Tatsuhide Hamasaki, Bingzi Chen, Yichen Chen, Shogo Taniguchi, Tadao Mizuno
    The 32nd Annual Conference on Ozone Science and Technology in Japan, Jun 22, 2023
  • Tatsuhide Hamasaki, Bingzi Chen, Yichen Chen, Shogo Taniguchi, Tadao Mizuno
    The 32nd Annual Conference on Ozone Science and Technology in Japan, Jun 22, 2023
  • Jun 22, 2022
  • 陳冰子, Nanthapong Chantaraprachoom, 濱崎竜英, 谷口省吾, 水野忠雄
    第30回年次研究講演会, Nov 25, 2021, 特定非営利活動法人日本オゾン協会
    本研究は、回分式実験によりオゾンと4種の人工甘味料の反応量論について検討した。初期人工甘味料濃度を0.2 mmol/L、オゾン水濃度を0.0015〜0.0096 mmol/Lとして2分間反応させた。スクラロースについてはほとんど分解せず、オゾンの減少も少なかったことからほとんど反応が起こっていないと考えられた。サッカリン二水和物、アスパルテーム、アセスルファムカリウムは、オゾン1 molに対して、それぞれ0.92 mol、ア0.67 mol、1.1 mol分解することが確認できた。
  • 濱崎竜英, 焦菁, 陳冰子, Nanthapong Chantaraprachoom, 水野忠雄
    第30回年次研究講演会, Nov 25, 2021, 特定非営利活動法人日本オゾン協会
    本研究は、オゾン/過酸化水素促進酸化による蓚酸の分解について、反応器に過酸化水素を連続して添加する場合の最適な添加量を確認するとともに、先行研究で実施してきた実験開始直前に1度に過酸化水素を添加する方法や実験開始前に1度、その後にもう1度添加する方法と比較することを目的とした。蓚酸の分解量から、最適な添加量は1.0 mg/L/minであることがわかった。また、蓚酸の分解量に対するオゾンの消費量や過酸化水素消費量から連続添加が最適であることがわかった。
  • Nanthapong Chantaraprachoom, Bingzi Chen, Tatsuhide Hamasaki, Shogo Taniguchi, Tadao Mizuno
    第30回年次研究講演会, Nov 25, 2021, 特定非営利活動法人日本オゾン協会
    Even though O3/H2O2 based AOP has been proven to be an effective polishing treatment for sewage effluent, some of organic compounds were still found after treatment as the TOC value of treated sample was around 1 mg/L. In pursue of identifying these remaining substances, High Performance HPSEC-OCD was used to determine range of AMW of the remaining substances. In this study, four HPSEC-OCD results were observed and compared: (a) sewage effluent before AOP, (b) after ozone only treatment, (c) after ozonation with hydrogen peroxide addition in the beginning, (d) after ozonation with hydrogen peroxide continuously added. HPSEC-OCD chromatograms show that biopolymer in AMW range of 30,000 Da and LMW neutrals in AMW range of 500 Da were removed in all cases. However, humic substances and building blocks in AMW range of 2,700 and 2,000 Da are only removed in presence of hydrogen peroxide. LMW acids in which has AMW range of 1,100-1,200 Da were found irremovable. Furthermore, concentration in this AMW range increased after all treatment. The increase was hypothesized to be by-products of AOP reactions with larger molecules.
  • 濱崎竜英, 陳冰子, 谷口省吾, 橋口亜由未, 水野忠雄
    日本オゾン協会第29回年次研究講演会, Jan 12, 2021, 特定非営利活動法人日本オゾン協会
    A basic experiment was conducted using a batch type experimental device for confirmation of artificial sweetener decomposition amount with respect to ozone consumption. The artificial sweeteners used in the experiment was saccharin sodium dihydrate. Ozone water with an actual measurement value of 7.8 mg/L was gradually mixed with ultrapure water to make 50 mL, it injected into 100 mL of artificial sweetener 0.1 mmol/L. The experiment time was 2 minutes. As a result of the experiment, saccharin sodium dihydrate was decomposed by 0.5 mol with respect to 1 mol of ozone.
  • Caiting Zhu, Chi Qiu, Tatsuhide Hamasaki
    The 54th Annual Conference of Japan Society on Water Environment 2020 in Iwate, Mar 17, 2020, Japan Society on Water Environment
  • Chi Qiu, Caiting Zhu, Tatsuhide Hamasaki
    The 54th Annual Conference of Japan Society on Water Environment 2020 in Iwate, Mar 17, 2020, Japan Society on Water Environment
  • 焦菁, 陳冰子, 濱崎竜英, 水野忠雄, 津野洋
    特定非営利活動法人日本オゾン協会第28回年次研究講演会, Jun 21, 2019, Japan Ozone Association
    An O3/H2O2 advanced oxidation process was experimentally examined to decompose oxalic acid. The method used was an adaptation of H2O2 decomposition via a continuous adding method to our reactor. As compared with the method of adding H2O2 at one time just before the start of the experiment and at two steps which have been carried out in the previous research, the degradation rate of TOC more continues at 1.0-2.0 mgC/L/min under the condition of pH3 and at 0.5-1.0 mgC/L/min under the condition of pH 7 during the experiment time.
  • 陳冰子, 李程, 谷口省吾, 濱崎竜英, 水野忠雄
    特定非営利活動法人日本オゾン協会第28回年次研究講演会, Jun 21, 2019, Japan Ozone Association
    An O3 oxidation process and an O3/H2O2 advanced oxidation process were experimentally examined to decompose artificial sweeteners, which have the tendency to accumulate in ambient water. The artificial sweeteners examined in this experiment were saccharin sodium dihydrate, sucralose, aspartame, and acesulfame K. Decomposition of these sweeteners was achieved via both an O3 oxidation process and an O3/H2O2 advanced oxidation process. However, our results showed that organic byproducts were formed using both the processes.
  • 李程, 陳允麒, 濱崎竜英, 水野忠雄, 津野洋
    特定非営利活動法人日本オゾン協会第28回年次研究講演会, Jun 21, 2019, Japan Ozone Association
    As a follow up to our previously reported work, an O3/H2O2 advanced oxidation process was experimentally examined for the decomposition of oxalic acid. This process was an adaptation of the step addition process previously reported for H2O2 in our reactor. In this study, not only TOC decomposition rate but also ozone consumption rate and hydrogen peroxide consumption rate are compared. And additionally following experiment was conducted in which under the experiment condition of pH 3, pH is readjusted at 3 when hydrogen peroxide is added at the second step. As a result, it was found that decomposition progressed more than the experiment when not added by two steps.
  • 濱崎竜英, 陳冰子, 谷口省吾, 水野忠雄, 津野洋
    特定非営利活動法人日本オゾン協会第28回年次研究講演会, Jun 21, 2019, Japan Ozone Association
    As a follow up to our previously reported work, an advanced oxidation process involving O3/H2O2 was examined for decomposing organic matter in the effluent obtained from a final sedimentation tank, which was a part of the biological treatment process for sewage. The experiment was conducted using three addition methods of H2O2, which were addition at the beginning once, two-steps addition and continuance addition. The rate of decomposition was evaluated by calculating the rates of TOC decomposition, O3 consumption and H2O2 consumption. In case of this study, the continuance addition method decreased to 3.0 mgC/L, it was the lowest in the other methods.
  • 高浪 龍平, 濱崎 竜英, 谷口 省吾, 尾崎 博明
    第18回環境技術学会年次大会, Jun 30, 2018
  • 陳冰子, 陳允麒, 濱崎竜英, 水野忠雄, 津野洋
    特定非営利活動法人日本オゾン協会第27回年次研究講演会, Jun 22, 2018, 特定非営利活動法人日本オゾン協会
    Three O3/metal advanced oxidation processes were examined to decompose oxalic acid and acetic acid. The metals used were iron, aluminum, and manganese and each process was tested under pH7 and pH3 conditions. Oxalic acid was hardly decomposed with iron and aluminum under pH7 or pH3 conditions, however it was highly decomposed with manganese under pH3 conditions. Acetic acid was not decomposed with any metal under pH7 conditions. Thus, we conclude that oxalic acid is decomposed when permanganate ions react with hydrogenoxalate ions.
  • 陳允麒, 濱崎竜英, 谷口省吾, 水野忠雄, 津野洋
    特定非営利活動法人日本オゾン協会第27回年次研究講演会, Jun 22, 2018, 特定非営利活動法人日本オゾン協会
    An O3/H2O2 advanced oxidation process was experimentally examined to decompose oxalic acid. Organic byproducts and mineralized oxalic acid were measured using a total organic carbon (TOC) analyzer and ion-chromatography under pH7 and pH3 conditions. The resulting data show that the removal rate of TOC was nearly equal to the removal rate of oxalic ions and hence, oxalic acid was almost completely mineralized by the O3/H2O2 advanced oxidation process.
  • 李程, 陳允麒, 濱崎竜英, 水野忠雄, 津野洋
    特定非営利活動法人日本オゾン協会第27回年次研究講演会, Jun 22, 2018, 特定非営利活動法人日本オゾン協会
    We have previously decomposed oxalic acid using an O3/H2O2 advanced oxidation process, where ozone gas feeds continuously, hydrogen peroxide is introduced immediately before the experiment, and sample water is introduced in batches (called a semibatch process). In this study, we use a semibatch approach again, but hydrogen peroxide is introduced twice; once immediately before the experiment and once during the experiment, after the first batch has been used. The resulting data show that this approach has a higher rate of TOC removal, even with the same quantity of hydrogen peroxide.
  • 濱崎竜英, 藤井信輔, 陳允麒, 水野忠雄, 津野洋
    特定非営利活動法人日本オゾン協会第27回年次研究講演会, Jun 22, 2018, 特定非営利活動法人日本オゾン協会
    An O3/H2O2 advanced oxidation process was experimentally examined to remove decomposing organic matter from sedimentation tank effluents of a biological sewage treatment plant. The effluents were obtained from a sewage treatment plant in the Kansai region, Japan, and filtered through a glass fiber filter to remove suspended solids. The resulting data show that suspended solids disturb the decomposition of organic matter in the effluents by forming HO radicals from ozone and hydrogen peroxide.
  • Tatsuhide Hamasaki, Wu Ting, Chen Yunqi, Tadao Mizuno, Tadao Mizuno
    26th Annual Conference on Ozone Science & Technology, Japan Ozone Association, Jun 15, 2017, Japan Ozone Association
    An O3/H2O2 advanced oxidation process was experimentally examined for decomposing organic matter in effluent from a final sedimentation tank of biological treatment process for sewage and filtrated water of the effluent through a rapid sand filter. These samples were taken from two sewage treatment plants in Kansai region. It was presumed the process forming HO radical, and organic decomposing rate became higher by the process.
  • Chen Yunqi, Tatsuhide Hamasaki, Wu Ting, Tadao Mizuno, Hiroshi Tsuno
    26th Annual Conference on Ozone Science & Technology, Japan Ozone Association, Jun 15, 2017, Japan Ozone Association
    An O3/H2O2 advanced oxidation process was experimentally examined for decomposing oxalic acid and acetic acid. Regarding sample water with 7.5 mg/L of hydrogen peroxide under pH3, oxalic acid as TOC was decomposed effectively. Regarding sample water with 150 mg/l of hydrogen peroxide, decomposition rate was reduced compared the water with 7.5 mg/L of hydrogen peroxide. Acetic acid was decomposed well, adding hydrogen peroxide more and taking decomposing time more under pH7. It was not decomposed under pH3.

Professional Memberships

 7
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Research Projects

 17
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Industrial Property Rights

 2

Social Activities

 4

研究テーマ

 7
  • 研究テーマ（英語）
    土壌浸透式水浄化法の研究
    キーワード（英語）
    土壌浸透法、水浄化、りん除去
    概要（英語）
    土壌を用いて、路面排水や河川水などに含まれる有機物やリンを除去する研究である。
    研究期間（開始）（英語）
    2001/04/01
  • 研究テーマ（英語）
    開発途上国の環境保全に関する研究
    キーワード（英語）
    開発途上国、環境
    概要（英語）
    技術的財政的に対応が困難な途上国における廃水処理技術や浄水技術の研究開発及び事業展開
    研究期間（開始）（英語）
    2001/04/01
  • 研究テーマ（英語）
    鉄バクテリア法による地下水中砒素の除去
    キーワード（英語）
    鉄バクテリア、鉄、マンガン、砒素
    概要（英語）
    地下水中に生息する鉄などを酸化させる鉄バクテリアを用いて、地下水に含まれている砒素をはじめ、鉄、マンガンを除去し、また、併せてアンモニアを硝化させる研究である。
    研究期間（開始）（英語）
    2003/04/01
    研究期間（終了）（英語）
    2011/03/31
  • 研究テーマ（英語）
    ひも状生物接触担体を用いた下水処理
    キーワード（英語）
    生物接触酸化法、下排水処理、汚泥の減量化、リン回収
    概要（英語）
    ひも状の生物接触担体を用いた下水処理法に関する研究で、有機物の除去とともに、余剰汚泥の削減やリンの回収についても取り組んでいる。
    研究期間（開始）（英語）
    2006/04/01
    研究期間（終了）（英語）
    2011/03/31
  • 研究テーマ（英語）
    浄水汚泥を用いた硫黄酸化物の除去
    キーワード（英語）
    鉄、鉄バクテリア法、硫黄酸化物
    概要（英語）
    地下水を水源とした浄水場の内、鉄バクテリア法を採用している浄水場で発生する汚泥を用いた空気中の硫黄酸化物の除去の研究を行っている。
    研究期間（開始）（英語）
    2010/04/01
  • 研究テーマ（英語）
    廃棄物等を用いた地下水中のふっ素除去
    キーワード（英語）
    ふっ素　地下水　吸着
    概要（英語）
    廃棄物など安価で入手しやすい材料による地下水中のふっ素を吸着・除去する
    研究期間（開始）（英語）
    2013/04/01
  • 研究テーマ（英語）
    オゾンを用いた促進酸化法による有機物の分解
    キーワード（英語）
    オゾン、促進酸化法、過酸化水素
    概要（英語）
    オゾンと過酸化水素を併用した促進酸化法をによる有機酸の分解や下水処理水中の有機物分解の研究を行っている。
    研究期間（開始）（英語）
    2016/04/01
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