濾出氮 的英文怎麼說

中文拼音 [chūdàn]
濾出氮 英文
filtrate nitrogen
  • : 動詞(除去液體雜質) filter; strain
  • : 名詞[化學] nitrogen (7號元素, 符號n)
  1. Flesh anhydride and urea nitrogen are the child of protein metabolization, by nephritic eduction body outside, the chroma in its blood can regard reason as the index of function of kidney spherule filtration

    肌酐及尿素為蛋白質代謝的產物,由腎臟排體外,故其血中濃度可作為腎小球過功能的指標。
  2. Pvc pipe, which is connected to filter tank for discharge. feed water passes the catalyst, through 7 loops around the tank to eliminate ammonia and nitrogen and kill bacteria

    管內,連接過水,流入水經過二氧化鈦紫外線光觸媒裝置,藉以氧化?除氨及殺菌後排
  3. ( 3 ) the treatment result of no2 - n is good. when the influent concentration of no2 - n is 0. 01 ~ 2. 23mg / l, the effluent is less than o. lomg / l and the influence of temperature, hydraulic loading the total ratio of gas and water is small

    ( 3 )生物池對亞硝酸鹽的去除效果比較好,試驗期間,水源水中亞硝酸鹽濃度范圍為0 . 01 2 . 23mg / l ,水濃度一般低於0 . 10mg / l ,水溫、速、氣水比對亞硝酸鹽的去除無明顯影響。
  4. The height of media 、 the ratio of gas to liquid 、 hydraulic loading 、 the organic and ammonia loading of influent are the key factors influence the performance of one - stage aerobic baf. the conclusions of the experiment are as following : the best height to remove the organic matter and ammonia is at 60cm 、 120cm from the influent side respectively. the best ratio of gas to liquid is 3 : 1 4 : 1 ; the organic and ammonia loading of influent have litlle influence on the performance of one - stage aerobic baf when the concentration are low ; whe the ratio of gas to liquid is 3 : 1, the ammonia loading is blow 0. 87kgnh _ 4 ~ + - n / m ~ 3. d, the enfluent concentration of ammonia is blow 5mg / l which satisfies the water reuse standard ; at different organic loadings, the removal of organic matter keeps 35 % 45 %. hypothermia is unfavourable to nitrification for one - stage aerobic baf to removel ammonia, the influent concentration of ammonia can ’ t satisfy the water reuse standard

    試驗表明:對有機物的去除主要發生在進水端60cm內,對氨的去除主要發生在進水端120cm內;曝氣生物池運行的最佳氣水比為3 : 1 4 : 1 ;在進水有機物和氨濃度比較小時,水力負荷對其去除率影響不大;在氣水比為3 : 1 ,進水氨負荷小於0 . 87kgnh4 + - n / m3 (料) ? d時,水氨小於5mg / l ,滿足回用水的要求;在不同有機負荷下,有機物去除率保持在35 % 45 % 。
  5. Putting the potassium permanganate into the filter can improve its effect, the removal of organics and ammonia is increased, the influent concentration can satisfy the water reuse standard. but the turbidity of influent is unsatisfactory. the c / n ratio is the key factor to influence the nitrogen - removal of the anoxic / aerobic two - stage baf when the reflux ratio 、 hydraulic loading and the ratio of gas to liquid in aerobic filter are fixed. the anoxic / aerobic two - stage baf has a good removal of organics at different c / n ratio when the reflux ratio is 2, hydraulic loading is 2. 55m ~ 3 / m ~ 2 ? h and the ratio of gas to liquid in aerobic filter is 3 : 1. the influent concentration of organics is blow 7mg / l. from the beginning to 30cm of the anoxic filter, the removal of the organics is significant ; as the c / n ratio increasing, the influent concentration of ammonia is decreasing. when the c / n ratio is 3. 60, the enfluent concentration of ammonia is 3. 05mg / l which satisfies the water reuse standard. when the c / n ration is less than 3. 60, because of the imperfection

    迴流比為2 : 1 ,水力負荷為2 . 55m3 / m2 ? h ,好氧柱氣水比為3 : 1時試驗表明:不同的c / n ( 1 . 05 7 . 45 )下,兩級曝氣生物池對有機物有很好的去除作用,水有機物濃度小於7mg / l ,其中在缺氧柱進水端30cm內對有機物的去除最為明顯;隨著c / n的增加,系統水氨濃度降低,當c / n為3 . 60時,水氨濃度降到3 . 05mg / l ,已經滿足回用水的氨標準; c / n < 3 . 60時,因為缺氧柱的不完全反硝化,體系中硝酸鹽和亞硝酸鹽發生積累影響了好氧柱的硝化反應使氨降解效果較差;系統對總的去除隨著c / n的增加而增加,當c / n為3 . 60時,水總已經降到11 . 18mg / l ,滿足回用水的要求。
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