流化反應器 的英文怎麼說

中文拼音 [liúhuàfǎnyīngqì]
流化反應器 英文
fluidized reactor
  • 流 : Ⅰ動1 （液體移動; 流動） flow 2 （移動不定） drift; move; wander 3 （流傳; 傳播） spread 4 （向壞...
  • 反 : Ⅰ名詞1 （方向相背） reverse side 2 （造反） rebellion 3 （指反革命、反動派） counterrevolutionari...
  • 應 : 應動詞1 （回答） answer; respond to; echo 2 （滿足要求） comply with; grant 3 （順應; 適應） suit...
  • 器 : 名詞1. （器具） implement; utensil; ware 2. （器官） organ 3. （度量; 才能） capacity; talent 4. （姓氏） a surname
  1. Preparation of nanometer titanium dioxide by submerged circulative impinging stream reactor

    撞擊流反應器制備納米二氧化鈦的實驗研究
  2. Study on nitrate - nitrogen removal and community analysis of denitrifying bacteria in downflow fixed - bed bioreactor

    下流式固定床反應器中反硝化細菌類群及其脫氮效率分析
  3. Nitrogen loss in internal - loop granular sludge bed nitrifying reactor

    內環流顆粒污泥床硝化反應器的氮損失
  4. Each reactor is taken off stream in turn for regeneration.

    輪流切斷各個反應器的蒸氣進行催化劑再生。
  5. Research on biomass air gasification in a fluidized - bed reactor

    流化床反應器中生物質空氣氣化試驗研究
  6. 30 % ~ 45. 3 % of extracellular mc and 30 % ~ 51. 7 % of total mc were removed by chl orination. cascade biological contact oxidation reactor was more effective and stable for the treatment of eutrophic water than one - step reactor

    接近於推流反應器的三階生物接觸氧化反應器對富營養化原水的預處理效果與穩定性優于單階生物接觸氧化反應器。
  7. Modeling of an industrial turbulent fluidized bed reactor for manufacture of cyano - ethylene by ammoxidation of propylene

    丙烯氨氧化生產丙烯腈工業流化床反應器的模型化
  8. From the viewpoint of safety technology of chemical reaction with heat release. the technical causes of getting out of control of these reactors are analyzed. hazardous effects of the leakage of chemical reactants both on human and environment, and the existing problems in current safety technological measures are also discussed. the cooling method of jet vaporization based on the jet principle and the direct cooling by non - vaporized liquid are introduced. the development trends of the safety technology for chemical reactors are analyzed

    從放熱化學反應的安全技術觀點出發，分析了放熱化學反應器失控的技術原因、化學反應物泄漏對人員和環境造成的危害、現有安全技術措施存在的問題；介紹了基於射流原理的噴射汽化和非汽化冷卻液體的直接冷卻方法；還展望了化學反應器安全技術的發展方向。
  9. Abstract : from the viewpoint of safety technology of chemical reaction with heat release. the technical causes of getting out of control of these reactors are analyzed. hazardous effects of the leakage of chemical reactants both on human and environment, and the existing problems in current safety technological measures are also discussed. the cooling method of jet vaporization based on the jet principle and the direct cooling by non - vaporized liquid are introduced. the development trends of the safety technology for chemical reactors are analyzed

    文摘:從放熱化學反應的安全技術觀點出發，分析了放熱化學反應器失控的技術原因、化學反應物泄漏對人員和環境造成的危害、現有安全技術措施存在的問題；介紹了基於射流原理的噴射汽化和非汽化冷卻液體的直接冷卻方法；還展望了化學反應器安全技術的發展方向。
  10. A novel model for residual fluid catalytic cracking process ( rfcc ) is proposed. it divides the whole reactor into two part : the riser as ideal pipe flow reactor and the sett - ler as ideal cstr. the model contains six lumps reaction kinetics with serial and parallel network

    通過將實際裝置中發生裂化反應的提升管和沉降段反應器分別考慮為理想的活塞流反應器和連續攪拌式反應器，建立了簡化的渣油催化裂化反應6集總組分的串列和并行反應動力學網路模型。
  11. The proposed method has been successfully applied to the determination of glucose in human serum. the linear range of the glucose concentration was 1. 1 to 110 mm and the detection limit was 0

    我們研究了固定化反應器中酶反應的條件、洗脫液的ph值、空氣載流流速對晶元性能的影響，在最佳條件下，測量葡萄糖濃度的響應線形范圍為1
  12. Using fcc flow - reaction mathematical model and boundary condition developed in paper ( i ) and the operational constants in commercial fcc riser, the hydrodynamics of catalysts and the distribution of concentration of catalytic cracking products, as well as the temperature of two - phase along the riser are simulated and predicted

    運用已經建立的催化裂化反應的數學模型和模型邊界條件及求解方法，結合煉油廠工業提升管的實際操作參數，模擬預測了催化裂化提升管反應器內催化劑顆粒的流場特徵和原料油反應產物的濃度及氣粒兩相平均溫度的沿程分佈特徵。
  13. Simulating results reveal that hydrodynamics of catalysts in riser reactor is very complex due to the effect of injection and catalysts backmix dramatically near the nozzle, reaction products unevenly distributie along the riser height, there exists apparently temperature gap between gas - phase and solid - phase near the nozzle and the temperture of two phase is nearly equal at middle - top part

    模擬結果表明，由於原料油射流的影響，提升管反應器內催化劑顆粒的流動特徵非常復雜，在噴嘴附近的催化劑顆粒存在明顯的滑落返混；裂化產物濃度沿提升管存在非均勻分佈；氣粒兩相間溫差在噴嘴附近顯著，在中上部氣粒兩相溫度幾乎相等。
  14. Agreement between calculation and experimental data justified the model ' s predictability in pyrolysis reaction of biomass carried out in the fluidized bed reactor

    由該模型得到的計算結果能和實驗值很好吻合，表明它能較好地描述流化床反應器內生物質快速裂解的反應過程。
  15. From this work, a new way to improve the fluidization quality of the ultra - fine powders is found, and the studying result can supply as a basis of further investigation and be able to be used in the design of a spouted bed with a draft tube for the ultra - fine powders

    本研究為改善超細粉的流化質量提供了一種新的思路，研究成果為進一步四川大學碩士學位論文開展有關基礎研究和開發超細粉導向管噴動床反應器提供了良好的基礎。
  16. Progress in research and application of biological fluidized bed for nitrogen removal

    生物流化床反應器脫氮技術的研究與應用進展
  17. Abstract : in this paper, the development status quo and tendency of aerobic fluidized - bed bioreactor used in treatment of organic wastewater at home and abroad are presented. some new types of aerobic fluidized - bed bioreactors are described

    文摘:介紹了國內外好氧生物流化床反應器處理有機廢水技術的發展概況，分析了好氧生物流化床反應技術的發展動向，並介紹了幾種新型的好氧生物流化床反應器。
  18. In this paper. flow properties of multistage fluidized - bed bioreactor with external circulation at a pilot scale is studied. according to characteristic analysis, the model of completely mixing reactor in series is introduced to characterize real reactor as a theoretical model. on the basis of analog computing analysis and discussion of theoretical model. by means of pulse tracer method, experiments on residence time distribution ( rtd ) have been done in different conditions including the change of tracer level, feeding flow rate and circulation flow rate. the result shows when the ratio of circulation flow rate and feeding flow rate amounts to at least 4, the flow properties of multistage fluidized - bed bioreactor with external circulation at a pilot scale is very close to the model of completely mixing reactor in series. an amendatory model has been established by the regression method

    作者首先在對反應器進行特徵分析的基礎上，建立了描述中試規模多級外循環流化床生物反應器流動特性的串級全混流模型，並對理論模型進行了模擬計算分析和討論，在此基礎上，作者分別在無循環和有循環（改變示蹤劑用量、流加流量和循環流量）的條件下，利用脈沖示蹤法對一到五級串聯外循環流化床反應器進行了停留時間分佈實驗，結果表明，在循環流量與流加流量的比值達到大於等於4時，中試規模多級外循環流化床反應器的流動特性接近串級全混流模型，通過數據回歸擬合的方法，建立了中試規模一到五級串聯外循環流化床反應器的流動模型。
  19. It was found that loop reactor could narrow the molecular weight distribution, increase the content of carbonate in product molecules and improve catalyst efficiency

    研究發現，環流反應器能夠使產品分子量分佈變窄，提高產品中碳酸酯基團含量及催化劑的催化效率。
  20. The author experimented the vtbr biochemical reactors - hollow super - fiber - filter - film in tapping reused water, and concluded that tapping reused water is an effective and feasible technique

    筆者對垂直折流（ vtbr ）生化反應器?中空纖維超濾膜中水處理技術進行實驗研究，並得出結論本中水處理技術是一項高效可行的處理技術。
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