氣體擴散分離 的英文怎麼說

中文拼音 [kuòsǎnfēn]
氣體擴散分離 英文
gaseous diffusional separation
  • : Ⅰ名詞1 (氣體) gas 2 (空氣) air 3 (氣息) breath 4 (自然界冷熱陰晴等現象) weather 5 (氣味...
  • : 體構詞成分。
  • : 動詞(擴大) expand; enlarge; extend
  • : 散動詞1. (由聚集而分離) break up; disperse 2. (散布) distribute; disseminate; give out 3. (排除) dispel; let out
  • : 分Ⅰ名詞1. (成分) component 2. (職責和權利的限度) what is within one's duty or rights Ⅱ同 「份」Ⅲ動詞[書面語] (料想) judge
  • : Ⅰ動詞1 (離開) leave; part from; be away from; separate 2 (背離) go against 3 (缺少) dispens...
  • 氣體 : gas; gaseous fluid
  1. Finally, some simplification methods to the model were studied and a modified block elimination contraposing the features of the model ' s linear system was developed, which can greatly decrease the model ' s requirement to computer resources. in the second part, numerical methodology of hybrid techniques was developed, which uses dfn models developed in the fist part to build continuum approximations of fractured rock

    第三,本文將一種用的水?界面模擬非飽和滲流的數值模型展到裂隙網路中,為用本文所構建的裂隙網路模型模擬裂隙巖成富擁要柳廳錄非飽和滲流提供了一個初步的框架。
  2. The main studies of this thesis have been focused on the mass transport phenomenon in the hollow fiber membrane contactor, including the development of the model of the gas diffusion through the microporous membrane, the analytical solution of the shell side mass transfer differential equation in an orderly packed parallel flow module, the calculation of the shell side flow distribution in a randomly packed module, the estimation of the influence of the random arrangement of the fibers on the shell side mass transfer, and the experiments of the absorption of co2 into water

    膜接觸器是一種通過膜作為兩相之間的界面而實現相間傳質的雜化膜過程。本論文主要研究中空纖維膜接觸器的傳質行為,研究內容包括通過微孔膜模型的建立、中空纖維膜均勻佈的平行流組件殼程傳質微方程的解析求解、中空纖維膜不均勻佈組件中流佈的數學計算、中空纖維膜不均勻佈對殼程傳質影響的估算以及co _ 2吸收實驗。
  3. Clk - proliferation cyclone applicable to the collection of non - fiber drying of granular dust is the main characteristics of a conical dongshen, thus reducing the dust since the dongshen gas exports to the centre to short - circuit the possibility and install a conical reflector screen to prevent the two air separation will have to roll up the dust down, brought out by the increased flow, thereby enhancing the efficiency of dust

    Clk式旋風除塵器,適用於捕集乾燥的非纖維性的顆粒狀粉塵,主要特點是筒身呈圓錐形,因而減少了含塵自筒身中心短路到出口去的可能性,並裝有圓錐形的反射屏,防止兩次流將已經下來的粉塵重新捲起,被上升流帶出,因而提高了除塵效率。
  4. Standard test method for available cyanide with ligand displacement and flow injection analysis utilizing gas diffusion separation and amperometric detection

    氣體擴散分離和電流計探測法對有效氰化物進行配位位移和流量注入析的標準試驗方法
  5. The condensation heat - exchange characteristic of a separate - type heat - pipe was studied on a 1 : 1 model. the heat pipe is heated by electricity, and working fluid is distilled water, and it is cooled by air. the experimental results show that, ( 1 ) when charging liquid ratio is 45 %, condensation heat - exchange coefficient reaches to maxium ; ( 2 ) when there is not non - condensing gas, the coeffcient decreases a little with the increase of vapour pressure, and it decreases by 9. 5 % when the pressure increases from 0. 16mpa to 0. 36mpa ; ( 3 ) when there is non - condensing gas, the coefficient decreases a little, but when the gas is discharged by an exhaust value, it can be improved, when the volume content of the gas is 2. 5 %, it can increased by 22 % ; ( 4 ) the effect of the non - condensing gas on the coefficient decreases with the increase of the pressure, and when the volume content of the gas is 5 % and the pressure increases from 0. 16mpa to 0. 36mpa, the coefficient increases by 6 %. the relative curves are given between condensation heat - exchange coefficient and air flowrate, charging liquid ratio and vapour pressure

    建立了空冷卻實驗臺,熱管的加熱方式為電加熱,工質為蒸餾水.在1 1模型上對式熱管管內凝結換熱特性、不凝性對凝結換熱的影響及不凝性規律進行了試驗,得出式熱管有一最佳充液率,其值為45 %左右;凝結換熱系數隨著蒸汽壓力的增加略有降低,在實驗的壓力范圍內,降低了9 . 5 % ;不凝性式熱管的凝結換熱僅影響冷凝段下部較小部,通過排閥排出不凝性可有效地改善冷凝段下部的凝結換熱;隨著壓力的增加,不凝性式熱管冷凝段的影響減少.這些結論可用於式熱管換熱器的工程設計和控制
  6. Abstract : the condensation heat - exchange characteristic of a separate - type heat - pipe was studied on a 1 : 1 model. the heat pipe is heated by electricity, and working fluid is distilled water, and it is cooled by air. the experimental results show that, ( 1 ) when charging liquid ratio is 45 %, condensation heat - exchange coefficient reaches to maxium ; ( 2 ) when there is not non - condensing gas, the coeffcient decreases a little with the increase of vapour pressure, and it decreases by 9. 5 % when the pressure increases from 0. 16mpa to 0. 36mpa ; ( 3 ) when there is non - condensing gas, the coefficient decreases a little, but when the gas is discharged by an exhaust value, it can be improved, when the volume content of the gas is 2. 5 %, it can increased by 22 % ; ( 4 ) the effect of the non - condensing gas on the coefficient decreases with the increase of the pressure, and when the volume content of the gas is 5 % and the pressure increases from 0. 16mpa to 0. 36mpa, the coefficient increases by 6 %. the relative curves are given between condensation heat - exchange coefficient and air flowrate, charging liquid ratio and vapour pressure

    文摘:建立了空冷卻實驗臺,熱管的加熱方式為電加熱,工質為蒸餾水.在1 1模型上對式熱管管內凝結換熱特性、不凝性對凝結換熱的影響及不凝性規律進行了試驗,得出式熱管有一最佳充液率,其值為45 %左右;凝結換熱系數隨著蒸汽壓力的增加略有降低,在實驗的壓力范圍內,降低了9 . 5 % ;不凝性式熱管的凝結換熱僅影響冷凝段下部較小部,通過排閥排出不凝性可有效地改善冷凝段下部的凝結換熱;隨著壓力的增加,不凝性式熱管冷凝段的影響減少.這些結論可用於式熱管換熱器的工程設計和控制
  7. The paper enlarges the domain of using the method of variable separation with addition, and beneficially tries to obtain analytical solutions of complicated problem, such as 2 - d steady incompressible viscous gas diffusion flow field

    拓展了加法變量法的適用領域,並對二維定常粘性不可壓縮流場這類復雜問題的解析求解進行了有益的嘗試。
  8. By using the new method of variable separation with addition, semi - analytical solutions of 2 - dimensional ( 2 - d ) steady incompressible viscous gas diffusion flow field are obtained in the paper, and suitable conditions are discussed

    摘要運用加法變量法,解析求解了二維定常粘性不可壓縮流場,得到了幾組空流場有源匯和無源匯情況下流場的半解析解,並析了其適用條件。
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