公开(公告)号：KR101759066B1

公开(公告)日：2017-07-19

申请号：KR1020150085081

申请日：2015-06-16

Applicant: 한국건설기술연구원

Inventor： 황태문 ,  강준원 ,  권민환

IPC: C02F1/72 ,  C02F1/32 ,  C02F1/50

Abstract: 이취미(맛냄새) 유발물질, 조류독성물질, 의약물질등의유해물질을제거하기위하여기존의재래식공정에 2단자외선산화반응장치를유입원수관로상에추가로설치함으로써, 자외선-과산화수소공정및 자외선-염소공정을순차적으로조합한 2단자외선산화공정에의해유입원수내의유해물질의종류와농도에따라 OH 라디칼을극대화시켜유해물질을제거하고, 이와동시에잔류하는산화제를완벽히처리할수 있고, 이에따라기존의활성탄공정과같은후속흡착공정이필요없게되는, 과산화수소-자외선공정및 염소-자외선공정을조합한 2단자외선고도산화공정을이용하는복합수처리시스템및 그방법이제공된다.

Abstract translation: 通过在业余爱好（味道气味）提供致癌物质，藻类毒素，以去除有害物质，例如在输入的原水导管，紫外线过氧化氢水溶液处理药物物质的两阶段UV氧化装置添加到现有的常规方法，和 UV-由UV依次两级组合在氯处理中，氧化工艺最大化OH按照在生水入口的类型和有害物质的浓度的自由基，并且可以完全处理氧化剂用于除去有害物质，并将残余物在同一时间，yiettara UV处理和氯存在的随后的吸附，过氧化氢不是必需过程，如活性炭处理是提供了使用两阶段的氧化紫外线高度结合紫外线步骤过程和方法复杂的水处理系统。

公开(公告)号：KR101640416B1

公开(公告)日：2016-08-01

申请号：KR1020140048809

申请日：2014-04-23

Applicant: 한국건설기술연구원

Inventor： 황태문 ,  강준원 ,  윤여준 ,  권민환

IPC: C02F1/72 ,  C02F1/32 ,  C02F1/50 ,  G01N33/18 ,  G05D11/08

Abstract: 하천녹조발생으로유발되는조류-기인이취미유발물질, 조류독성물질, 의약물질등의유해물질을제거하기위하여일정한 pH 조건에서관로형자외선반응기전단에염소를투입함으로써, 기존의오존이나과산화수소등의산화제를사용하지않고, 활성탄과같은후속흡착공정이필요없고, 또한, 유입원수의수질특성에따라선택적으로염소주입위치및 주입량을제어하고, 조류-기인유해물질이유입될경우, 염소와자외선을결합한복합산화반응장치에서조류-기인유해물질의종류와농도에따라수치해석을통해결정된자외선강도와염소주입량에따라피드백제어함으로써운전편의성을제공하고, 전력소모량및 약품사용량을절감시키고, 약품오주입을사전에방지할수 있는, 조류-기인유해물질을제거하기위한염소-자외선복합산화수처리장치, 및이를이용한염소주입량과자외선강도가변제어방법이제공된다.

公开(公告)号：KR100271563B1

公开(公告)日：2000-11-15

申请号：KR1019980041176

申请日：1998-09-30

Applicant: 한국건설기술연구원 ,  삼성물산 주식회사 ,  지에스건설 주식회사 ,  (주)대우

Inventor： 강준원 ,  이상은 ,  오현제 ,  이주윤 ,  김광녕 ,  이재천 ,  송기섭 ,  김두일 ,  허형수 ,  이영호 ,  오성민

IPC: C02F1/78

Abstract: 본 발명은 수처리 기술에 관한 것으로, 특히 브로메이트 검출 장치 및 그를 이용한 수처리 시스템에 관한 것이며, 그 구조가 단순하며 미량분석이 가능한 브로메이트 검출 장치와, 그를 이용하여 미량분석이 가능하며 브로메이트의 연속적인 측정, 감시 및 제어가 가능한 수처리 시스템을 제공하고자 한다. 본 발명에서는 브로메이트의 미량검출을 위하여 FIA(flow injection anlysys) 시스템을 이용한 흡광도 분석법을 채용하였다. 이와 더불어 본 발명에서는 브로메이트 검출 장치의 구조를 단순화하였다. 본 발명으로부터 제공되는 특징적인 브로메이트 검출 장치는 클로로프로마진/염산 혼합 시약과, 시료수를 선택적으로 혼합수단에 유입시키기 위한 선택적 유입수단; 상기 혼합 시약과, 상기 증류수 또는 시료수를 혼합하기 위한 상기 혼합수단; 상기 혼합수단을 통해 제공된 혼합용액 내의 브로메이트를 검출하기 위한 흡광도 분석수단; 및 상기 선택적 유입수단을 제어하기 위한 제어수단을 포함한다.

公开(公告)号：KR1020160148284A

公开(公告)日：2016-12-26

申请号：KR1020150085081

申请日：2015-06-16

Applicant: 한국건설기술연구원

Inventor： 황태문 ,  강준원 ,  권민환

IPC: C02F1/72 ,  C02F1/32 ,  C02F1/50

Abstract: 이취미(맛냄새) 유발물질, 조류독성물질, 의약물질등의유해물질을제거하기위하여기존의재래식공정에 2단자외선산화반응장치를유입원수관로상에추가로설치함으로써, 자외선-과산화수소공정및 자외선-염소공정을순차적으로조합한 2단자외선산화공정에의해유입원수내의유해물질의종류와농도에따라 OH 라디칼을극대화시켜유해물질을제거하고, 이와동시에잔류하는산화제를완벽히처리할수 있고, 이에따라기존의활성탄공정과같은후속흡착공정이필요없게되는, 과산화수소-자외선공정및 염소-자외선공정을조합한 2단자외선고도산화공정을이용하는복합수처리시스템및 그방법이제공된다.

公开(公告)号：KR101617822B1

公开(公告)日：2016-05-19

申请号：KR1020140159128

申请日：2014-11-14

Applicant: 한국건설기술연구원

Inventor： 황태문 ,  윤영한 ,  강준원 ,  권민환 ,  김선백

IPC: G01N31/22 ,  G01N33/18 ,  G06F17/10

CPC classification number: G01N31/22 ,  G01N33/18 ,  G01N33/1813 ,  G01N33/182 ,  G06F17/10

Abstract: 수산화라디칼을주요기작으로유해물질을처리하는데적용되는자외선/과산화수소고도산화공정에서단일연속흐름주입관로상에서시료의유속을변경하고자외선강도를일정하게유지하는연속흐름주입방식을적용함으로써, 증류수로희석배율이조정된과산화수소의농도및 지표물질인로다민 B를실시간으로측정할수 있고, 또한, 상수고도처리나하수방류수에서미량유기오염물질을제거하기위하여적용되는고도산화공정에서수산화라디칼소모인자지수를실시간측정함으로써, 자외선/과산화수소고도산화공정을통해서제거되는유해물질의정량적제거능, 자외선조사량및 과산화수소투입량을정확하게산출할수 있으며, 또한, 자외선/과산화수소고도산화공정에대한실시간자가진단및 공정최적화가가능하므로, 수산화라디칼을극대화시키는기술로실용화할수 있는, 고도산화공정의수산화라디칼소모인자지수실시간측정장치및 그방법이제공된다.

Abstract translation: 本发明提供了一种用于在高级氧化过程中实时测量羟自由基清除指数的装置和方法。 此外，提供了一种用于在高级氧化过程中实时测量羟基自由基清除指数的装置和方法，其中连续流动注射方案应用于使用紫外线/过氧化氢的高级氧化方法， 用于通过羟基自由基的主要机理处理有害物质，以改变单个连续流动注射管上的测试样品的流速，并均匀地保持紫外线的强度，从而测量浓度 使用蒸馏水调节稀释比的过氧化氢和作为实际指标物质的罗丹明B。 另外，高级氧化工艺中的羟基自由基清除指数，用于去除少量先进处理的水中的有机污染物或废水污水，从而精确测量除去先进的有害物质的功率 使用紫外线/过氧化氢的氧化处理，照射的紫外线的量和引入的过氧化氢的量。 使用紫外线/过氧化氢和工艺优化的高级氧化工艺的实时自检是可能的，从而使羟基自由基最大化的技术可以商业化。

公开(公告)号：KR1020020007469A

公开(公告)日：2002-01-29

申请号：KR1020000040326

申请日：2000-07-13

Applicant: 한국건설기술연구원 ,  (주)우대기술단 ,  주식회사 경호엔지니어링 종합건축사사무소

Inventor： 오현제 ,  김원재 ,  지재성 ,  안병성 ,  강예석 ,  강준원

IPC: C02F1/72

Abstract: PURPOSE: A method for controlling advanced oxidation process by control of CT(C: Concentration of disinfectant, T: Contact time) value based on concentration of residual ozone and flowrate of raw wastewater. CT value indicates the oxidizing power of ozone. According to the method, concentration of residual ozone and flowrate of raw wastewater are measured instantly for calculating CT value. Ozone and hydrogen peroxide are injected into wastewater according to calculated CT value. CONSTITUTION: The system includes: an ozone/AOP contactor(2) for reacting ozone and hydrogen peroxide with wastewater; a means(4) for measuring flowrate of raw wastewater; a means(5) for measuring concentration of residual ozone; an ozone generator(8) supplying ozone to the ozone/AOP contactor.

Abstract translation: 目的：根据残留臭氧浓度和原废水流量，通过控制CT（C：消毒剂浓度，T：接触时间）值控制高级氧化过程的方法。 CT值表示臭氧的氧化能力。 根据该方法，立即测量残留臭氧浓度和废水流量，计算CT值。 根据计算的CT值将臭氧和过氧化氢注入废水中。 规定：该系统包括：臭氧/ AOP接触器（2），用于使臭氧和过氧化氢与废水反应; 用于测量原废水流量的方法（4） 用于测量残留臭氧浓度的方法（5）; 向臭氧/ AOP接触器供应臭氧的臭氧发生器（8）。

公开(公告)号：KR101306155B1

公开(公告)日：2013-09-10

申请号：KR1020120063750

申请日：2012-06-14

Applicant: 한국건설기술연구원

Inventor： 황태문 ,  강준원 ,  윤여준 ,  권민환

IPC: C02F1/72 ,  C02F1/32

CPC classification number: C02F1/72 ,  C02F1/325 ,  C02F2201/002 ,  C02F2201/4612

Abstract: PURPOSE: An automatic control apparatus of an advanced oxidation and a method thereof are provided to be able to provide stable and safe water by variably controlling the system operation in consideration of the total reactivity of chemical components inhibiting the production of OH radical in the inflow water, and treating the trace amount of medical substances existing in the water to be processed, tastes and odor materials, and to be able to save energy in operation. CONSTITUTION: An automatic control method of an advanced oxidation process comprises the following steps: a step of selecting elimination target contaminants by monitoring water quality factors of the source water including the UV254 absorbance; a step of measuring the OH radical production inhibition reaction index in consideration of the reactivity of chemical components inhibiting OH radical production by using rhodamine B as an indicator; a step of calculating the UV irradiation amount and the hydrogen peroxide injection amount required in the water treatment system, and the elimination capacity to the elimination target contaminant of the water treatment system in consideration of the selected elimination target contaminant and the measured OH radical production inhibition reaction index; and a step of calculating the UV irradiation amount and the hydrogen peroxide according to a target elimination capacity to the elimination target contaminant, and adjusting the UV irradiation amount and the hydrogen peroxide injection amount by comparing the calculated UV irradiation amount and hydrogen peroxide injection amount. [Reference numerals] (AA) Start; (BB) Selecting elimination target contaminants; (CC) Monitoring UV absorbance in real time (wavelength 254 nm); (DD) Database; (EE) Measuring OH radical production inhibition and reaction indexes; (FF) Extracting quantum yield, molar extinction coefficient and specific reaction rate; (GG) Selecting the rate of elimination target contaminants; (HH) Calculating UV irradiation amount and hydrogen peroxide injection amount (I_0*t) (using math formula 8); (II) (real I_0*t)> targetI_0*t)?; (JJ) Re-adjusting UV irradiation amount; (KK) Revising and control UV irradiation amount and hydrogen peroxide injection amount; (LL) End

Abstract translation: 目的：提供一种先进氧化的自动控制装置及其方法，以便能够通过可变地控制系统操作来提供稳定和安全的水，其考虑到抑制流入水中OH自由基产生的化学成分的总反应性 ，并处理存在于待处理水中的微量医药物质，味道和气味物质，并能够节约能源。 构成：先进氧化工艺的自动控制方法包括以下步骤：通过监测源水的水质因子（包括UV254吸光度）来选择消除目标污染物的步骤; 考虑到通过使用罗丹明B作为指示剂来抑制OH自由基生成的化学成分的反应性，测定OH自由基产生抑制反应指数的步骤; 考虑到所选择的消除目标污染物和测量的OH自由基产生抑制，计算水处理系统中所需的UV照射量和过氧化氢注入量以及对水处理系统的消除目标污染物的消除能力的步骤 反应指数; 以及根据目标消除能力将UV照射量和过氧化氢计算到消除目标污染物的步骤，以及通过比较计算的UV照射量和过氧化氢喷射量来调节UV照射量和过氧化氢注射量。 （附图标记）（AA）开始; （BB）选择消除目标污染物; （CC）实时监测UV吸光度（波长254 nm）; （DD）数据库; （EE）测量OH自由基产生抑制和反应指数; （FF）提取量子产率，摩尔消光系数和比反应速率; （GG）选择消除目标污染物的比例; （HH）计算UV照射量和过氧化氢注入量（I_0 * t）（使用数学公式8）; （II）（real I_0 * t）> targetI_0 * t）？ （JJ）重新调整紫外线照射量; （KK）修改和控制紫外线照射量和过氧化氢注射量; （LL）结束

公开(公告)号：KR100373513B1

公开(公告)日：2003-02-25

申请号：KR1020000040567

申请日：2000-07-14

Applicant: 한국건설기술연구원 ,  (주)우대기술단 ,  주식회사 경호엔지니어링 종합건축사사무소

Inventor： 오현제 ,  김원재 ,  지재성 ,  안병성 ,  강예석 ,  강준원

IPC: C02F1/78

Abstract: PURPOSE: Ozone consumption rate constant (kc) is a factor calculating CT(C: concentration of disinfectant, T: Contact time) value indicated oxidizing power of ozone. According to the method, CT value is calculated by kc for controlling concentration of ozone and hydrogen peroxide. CONSTITUTION: The system includes: an ozone/AOP contactor(2) for reacting ozone and hydrogen peroxide with wastewater; a means(3) for measuring flowrate of raw wastewater; a means(4) for calculating kc; a pump(6) for injecting hydrogen peroxide into the ozone/AOP contactor; an ozone generator(7) supplying ozone to the ozone/AOP contactor; a means(8) for monitoring concentration of ozone supplied to the ozone/AOP contactor; and a kc control unit(9) for controlling the amount of ozone and hydrogen peroxide to be supplied.

Abstract translation: 目的：臭氧消耗速率常数（kc）是计算CT的因子（C：消毒剂浓度，T：接触时间）值表示臭氧的氧化能力。 根据该方法，通过用于控制臭氧和过氧化氢浓度的kc来计算CT值。 组成：该系统包括：用于使臭氧和过氧化氢与废水反应的臭氧/ AOP接触器（2）; 用于测量未处理废水流量的装置（3）; 一个用于计算kc的装置（4）; 用于将过氧化氢注入臭氧/ AOP接触器的泵（6） 向臭氧/ AOP接触器供应臭氧的臭氧发生器（7） 一个用于监测提供给臭氧/ AOP接触器的臭氧浓度的装置（8）; 和用于控制臭氧和过氧化氢的供应量的kc控制单元（9）。

公开(公告)号：KR100373511B1

公开(公告)日：2003-02-25

申请号：KR1020000040325

申请日：2000-07-13

Applicant: 한국건설기술연구원 ,  (주)우대기술단 ,  주식회사 경호엔지니어링 종합건축사사무소

Inventor： 오현제 ,  김원재 ,  지재성 ,  안병성 ,  강예석 ,  강준원

IPC: C02F1/72

Abstract: PURPOSE: A consumed amount of ozone is measured instantly for calculating ozone and hydrogen peroxide demands. Then, the amount of ozone and hydrogen peroxide, corresponding to consumed amount, are injected automatically. CONSTITUTION: The system includes: a means(3) installed at one side of an ozone/AOP contactor(2) to measure raw wastewater flowrate; an I.D measurer(4) to measure instant ozone demand; a pump(6) for injecting hydrogen peroxide into the ozone/AOP contactor(2); an ozone generator(7) for supplying ozone to the ozone/AOP contactor; a means(8) for monitoring ozone concentration from the ozone generator(7).

Abstract translation: 目的：立即测量消耗的臭氧量，以计算臭氧和过氧化氢的需求量。 然后，自动注入与消耗量相对应的臭氧和过氧化氢的量。 构成：该系统包括：安装在臭氧/ AOP接触器（2）的一侧以测量原始废水流量的装置（3）; 测量即时臭氧需求的I.D测量器（4）; 一个用于将过氧化氢注入臭氧/ AOP接触器（2）的泵（6）; 臭氧发生器（7），用于向臭氧/ AOP接触器供应臭氧; 一个用于监测来自臭氧发生器（7）的臭氧浓度的装置（8）。

公开(公告)号：KR1020000021897A

公开(公告)日：2000-04-25

申请号：KR1019980041175

申请日：1998-09-30

Applicant: 한국건설기술연구원 ,  삼성물산 주식회사 ,  지에스건설 주식회사 ,  (주)대우

Inventor： 강준원 ,  이상은 ,  오현제 ,  이주윤 ,  김광녕 ,  이재천 ,  송기섭 ,  김두일 ,  허형수 ,  이영호 ,  오성민

IPC: C02F1/78

CPC classification number: C02F1/78 ,  C02F1/722 ,  C02F2201/782 ,  G01N21/00 ,  G01N33/0039

Abstract: PURPOSE: An apparatus for measuring decomposition velocity of ozone and a water processing system using the same are provided to consecutively measure the decomposition velocity of the ozone, to measure the decomposition velocity of the ozone in real time, and to automatically control using the apparatus. CONSTITUTION: An apparatus for measuring decomposition velocity of ozone comprises: a container of reaction of ozone for mixing condensed water of the ozone with sample water, by being supplied with the condensed water of the ozone from a provider of the condensed water of the ozone; a mixer for consecutively mixing a color reagent in a predetermined rate, by consecutively picking up the sample water; an absorbance analyzer for consecutively measure residual density of the ozone, through analyzing the residual density of the color reagent, in the sample water mixed with the color reagent; and a recorder for consecutively recording the residual density of the ozone, measured in the absorbance analyzer.

Abstract translation: 目的：提供一种用于测量臭氧分解速度的装置和使用其的水处理系统，以连续测量臭氧的分解速度，实时测量臭氧的分解速度，并使用该装置自动控制。 构成：用于测量臭氧分解速度的装置包括：通过从臭氧冷凝水提供者供应臭氧的冷凝水，将臭氧与样品水混合的臭氧反应容器; 用于连续地拾取样品水的混合器，用于以预定速率连续混合着色试剂; 通过分析与着色剂混合的样品水中的着色试剂的残留密度，连续测定臭氧的残留密度的吸光度分析仪; 以及用于连续记录在吸光度分析仪中测量的臭氧的残留密度的记录器。