leaching 的翻譯結(jié)果
本文關(guān)鍵詞:機(jī)械活化強(qiáng)化含砷金精礦浸出的工藝及機(jī)理研究,由筆耕文化傳播整理發(fā)布。
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leaching
Study on Technology and Mechanism of Mechanical Activation Enhancing Leaching of Gold Concentrate Containing Arsenic
機(jī)械活化強(qiáng)化含砷金精礦浸出的工藝及機(jī)理研究
短句來源
Study on Leaching Behavior and Model of HLW-glass under Repository Conditions
高放固化體處置條件下的浸出和模型研究
短句來源
COPPER LEACHING IN ANCIENT CHINA
我國古代浸出法采銅
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FLUIDIZING LEACHING OF ILMENITE
鈦鐵礦的流態(tài)化浸出
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THE DIRECT LEACHING OF ROASTED MOLYBDENITE BY AMMONIA INSTEAD OF AQUEOUS AMMONIA
用氨代替氨水直接浸出鉬焙砂
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FLUIDIZATION WASHING OF FLOCCULATED PULP FROM CARBANATE LEACHING OF SOME URANIUM ORE
某鈾礦石堿浸-絮凝礦漿的流態(tài)化洗滌
短句來源
GOLD EXTRACTION RESEARCH BY HEAP LEACHING FROM LOW-GRADE ORE
低品位金礦堆浸法提金研究
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Study on gold leaching from sulfide ore by using mixed solution of cyanide and aqua ammonia
硫化礦的浸金研究——氰化物和氨水的混合液體系
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An approach to some problems in heap leaching design
堆浸設(shè)計幾個問題的探討
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STUDY ON LEACHING OF REFRACTORY URANIUM IN CLAY
粘土中難浸鈾的研究
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The nutrient contents of precipitation in kg/ha·a were N 12.972, P 0.289, K 7.249, Ca9.154, Mg 3.676. The nutrient contents of the rain leaching of tree layer in kg/ha·a were N 10.715, P 0.249, K9.420, Ca 8.675, Mg 9.574. The leaching amount of N, P, K and accumulations of crown canopy were in linear correlation.
林外雨的元素含量,以kg/ha·a表示,N是12.972,P 0.289,K 7.249,Ca 9.154,Mg 3.676。 喬木層的元素淋溶量,以kg/ha·a表示,N是10.715,P 0.249,K 9.420,Ca 8.675,Mg 9.574。
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The weathering and leaching sequence of Fangshan granodiorite is determined to be: Pb>Zn>Cr>Be>Cu>Co>Cd>Ni.
房山花崗閃長巖的風(fēng)化淋溶序列為:Pb>Zn>Cr>Be>Cu>Co>Cd>Ni;
短句來源
Total ammonia volatilization of six controlled-release fertilizers decreased by 16.62%,23.78%,32.15%,0.11%,16.59% and 37.78% than common urea respectively,and N leaching amount of the fertilizers decreased by 15.84%,38.27%,68.87%,46.17%,52.51% and 62.01% than common urea respectively.
與尿素比較,6種控/緩釋肥料氨揮發(fā)量分別較普通尿素減少16.62%,23.78%,32.15%,0.11%,16.59%和37.78%,氮淋溶量分別較普通尿素減少15.84%,38.27%,68.87%,46.17%,52.51%和62.01%。
短句來源
Ionic leaching order in Shaoshan forest based on the average ionic concentration of 18 months monitoring was K+ >Ca2+ >Cl- >Mg2+ >SO42- >NO3- >NH4+ >Na+.
根據(jù)18個月離子濃度平均值來計算,韶山地區(qū)森林冠層離子的淋溶序列為:K+>Ca2+>Cl->Mg2+>SO42->NO3->NH4+>Na+。
短句來源
The annual NH_3 volatilization was 60 kg N ha~(-1) and NO_3-N leaching loss was 6~84 kg N ha~(-1), according for 15% and 1.4%~20.3% of the applied N fertilizer, respectively.
每年因氨揮發(fā)而造成的肥料氮損失量為60 kg N ha~(-1),占施入肥料氮的15%。 NO_3-N淋溶損失量為6~84 kg N ha~(-1),占肥料施用量的1.4%~20.3%。
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The rate of leaching of Ca(VO_3)_2 is controlled by the parallel reactions between Ca(VO_3)_2 with Na_2CO_3 and NaHCO_3 respectively.
Ca(VO_3)_2的浸取速率受與Na_2CO_3和NaHCO_3的平行反應(yīng)控制;
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The leaching behaviour of Ag in NH_3-O_2 and NH_3-H_2O_2 aqueous solutions was investigated.
研究了Ag在NH_3-O_2和NH_3-H_2O_2水溶液體系中的浸取行為.
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The leaching rate of P2O5 is more than 92%, while those of Fe2O3 and Al2O3 are not more than 17%.
P2O5浸取率大于92%,Fe2O3浸取率及Al2O3浸取率均小于17%。
短句來源
The kinetics of V leaching from Ca(VO_3)_2 and NaCaVO_4 in Na_2CO_3-NaHCO_3 buffer solution has been investigated.
配合從高Ca含釩鋼渣中提釩工作,進(jìn)行了Ca(VO_3)_2和NaCaVO_4在Na_2CO_3-NaHCO_3緩沖溶液中釩浸取動力學(xué)研究。
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After the leaching solution was treated, the concentrations of Cd2+ and Ni2+ can be reduced from: 1086mg/L and 15.4mg/L to: 0.56mg/L and 0.54mg/L respectively. The loss of Zn2+ in the solution is about 1%.
浸取液經(jīng)處理后,Cd2+、Ni2+ 的濃度分別從1086mg/L和15.4mg/L降至0.56mg/L和0.54mg/L,浸出液中鋅的損失大約1%。
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leaching
They are functionally interconnected processes in the soil nitrogen cycle that are involved in the control of long-term nitrogen losses in ecosystems through nitrate leaching and gaseous N losses.
In the circulating fluidized-bed combustion of coal, the content of selenium in ash from the chimney was reduced to one-fourth of its original value and that in leaching water from the chimney decreased by two orders of magnitude using lime.
The Mn/Ce serial catalysts were characterized by Brunauer-Emmett-Teller (BET) analysis and the metal cation leaching was measured by inductively coupled plasma torch-atomic emission spectrometry (ICP-AES).
The metallic ion leaching is comparatively low (Mn>amp;lt;6.577 mg/L and Ce>amp;lt;0.6910 mg/L, respectively) in the CWAO process.
A two-step continuous flow leaching system consisting of an acidifying reactor and a leaching reactor was introduced to achieve the bioleaching of spent nickel-cadmium (Ni-Cd) batteries.
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本文關(guān)鍵詞:機(jī)械活化強(qiáng)化含砷金精礦浸出的工藝及機(jī)理研究,由筆耕文化傳播整理發(fā)布。
本文編號:148361
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