首页> 外国专利> SYSTEM FOR PHOTODEGRADATION OF HIGH DIISOPROPANOLAMINE (DIPA) CONCENTRATION IN WASTEWATER TREATMENT IN THE PRESENCE OF PHOTODEGRADATION CATALYST AND HYDROGEN PEROXIDE

SYSTEM FOR PHOTODEGRADATION OF HIGH DIISOPROPANOLAMINE (DIPA) CONCENTRATION IN WASTEWATER TREATMENT IN THE PRESENCE OF PHOTODEGRADATION CATALYST AND HYDROGEN PEROXIDE

机译:光分解催化剂和过氧化氢存在下废水处理中高浓度双异丙胺(DIPA)的光解系统

摘要

DISCLOSED IS A SYSTEM FOR WASTEWATER TREATMENT FOR COMPLETE REMOVAL OF DIISOPROPANOLAMINE (DIPA) IN HIGH CONCENTRATION (UP TO 30,000 PPM). THE SYSTEM IS A PROCESS (100) FOR TREATING WASTEWATER (110) TO REMOVE A PLURALITY OF ORGANIC CHEMICALS HAVING HIGH ECOTOXICITY AND LOW BIODEGRADABILITY PRODUCED FROM AN OUTLET OF A REFINERY OR GAS TREATMENT PLANT (102). THE PROCESS (100) ACCORDING TO A PREFERRED EMBODIMENT OF THE PRESENT INVENTION STARTS BY PROVIDING A PHOTOCATALYST REACTOR (112) TO PERFORM THE PHOTODEGRADATION PROCESS. THE PHOTOCATALYST REACTOR (112) DECOMPOSES THE PLURALITY OF ORGANIC CHEMICALS INCLUDING DIPA. H202 (108) IS MADE AVAILABLE TO THE PHOTODEGRADATION PROCESS UNDER VISIBLE LIGHT RADIATION FROM A LIGHT SOURCE (106) FOR ENHANCING THE PROCESS OF REMOVING DIPA. THE SYSTEM SHOWED COMPLETE REMOVAL OF DIPA FOR BOTH SYNTHETIC (30,000 PPM DIPA, 55,050 PPM COD) AND ACTUAL WASTEWATERS (27,000 PPM DIPA AND 61,880 PPM COD) EMPLOYING THE 2-STAGE PROCESS USING MONOMETALLIC FOLLOWED BY BIMETALLIC PHOTOCATALYSTS IN THE FORM OF FE/TIO2 AND CU-FE/TIO2, RESPECTIVELY, WITH ADDITION OF H202 UNDER VISIBLE LIGHT IRRADIATION. TOTAL COD REMOVAL OBSERVED FOR THE SYNTHETIC AND ACTUAL WASTEWATERS WERE 80% AND 70%, RESPECTIVELY. THE TREATED WATER (114) HERE NEEDS TO UNDERGO BIODEGRADATION PRIOR TO DISCHARGE. THE TWO-STAGE PHOTODEGRADATION OF WASTEWATER WITH ADDITION OF H202 UNDER THE IRRADIATION OF SUNLIGHT AND AT AN OPTIMAL TEMPERATURE ABOVE ROOM TEMPERATURE TO BELOW 60°C AND UNDER A REACTION PH BETWEEN PH 8 TO PH 11 RESULTS IN ZERO RESIDUAL SLUDGE, SUSPENDED SOLID AND/OR ZERO RESIDUAL WASTEWATER FOR DISPOSAL. THE PHOTOCATALYSTS ARE SEPARATED FROM THE TREATED WATER BY ANY SIMPLE FILTRATION MEANS. MOST ILLUSTRATIVE DIAGRAM: FIGURE 1
机译:公开了一种用于完全去除高浓度(最高30,000 PPM)的双异丙胺(DIPA)的废水处理系统。该系统是用于处理废水(110)以去除由炼油厂或气体处理厂(102)的出口产生的具有高生态毒性和低生物可降解性的多种有机化学品的过程(100)。根据本发明的优选实施例的过程(100)开始于提供光催化剂反应器(112)以执行光分解过程。光催化剂反应器(112)分解包括DIPA在内的多种有机化学品。 H202(108)适用于在来自光源(106)的可见光辐射下进行的光降解过程,以增强DIPA的去除过程。系统显示完全去除合成的(30,000 PPM DIPA,55,050 PPM COD)和实际废水(27,000 PPM DIPA和61,880 PPM COD)的DIPA均采用了二阶段工艺,并按照双金属/光催化作用进行了两步法和CU-FE / TIO2,分别在可见光照射下添加H202。合成废水和实际废水的总去除COD分别为80%和70%。在排放之前,需要对处理过的水(114)进行生物降解。在阳光照射下和室温以上的最佳温度下,温度低于60°C且在pH 8至PH 11的反应pH下,零残留污泥,悬浮固体的废水中添加H202的两阶段光分解或零残留废水进行处理。光催化剂是通过任何简单的过滤手段从处理过的水中分离出来的。最具说明性的图:图1

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