提升管裂化 的英文怎麼說

中文拼音 [dīshēngguǎnlièhuà]
提升管裂化 英文
riser cracking
  • 提 : 提動詞（垂手拿著） carry （in one's hand with the arm down）
  • 升 : Ⅰ動詞1 （由低往高移動） rise; hoist; go up; ascend 2 （等級提高） promote Ⅱ量詞1 （容量單位） lit...
  • 管 : Ⅰ名詞1 （管子） pipe; tube 2 （吹奏的樂器） wind musical instrument 3 （形狀似管的電器件） valve;...
  • 裂 : 裂動詞[方言] （東西的兩部分向兩旁分開） open
  • 提升 : 1 （提高職級） promote; advance 2 （向高處運） hoist; elevate3 [數學] lifting; 提升器 lifting mec...
  1. The company takes advantage of advanced dcs control system, high efficient float valve tray technology, high efficient energy - saving exchange techniques, fcc catalytic cracking double riser, two - generator regeneration process, polypropylene with loop reactor process and refining and blending process of high - number gasoline, etc. to ensure providing the users with high - tech qualified products

    公司採用先進的dcs控制系統，高效的浮閥塔盤技術，高效節能交換技術， fcc催化裂化雙提升管、兩器再生工藝，環管聚丙烯工藝，高排號汽油精製調和工藝等，確保高科技合格產品送至用戶手中。
  2. Study on conversion of coker gas oil by two - stage riser fluid catalytic cracking

    焦化蠟油兩段提升管催化裂化研究
  3. Application of two - stage riser catalytic cracking technology in petrochemical factory of yumen oilfield

    兩段提升管催化裂化技術在玉門煉油化工總廠的應用
  4. 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。
  5. The kinetic characteristics of two - stage riser fluid catalytic cracking ( tsrfcc ) technology were studied, and experimental data were simulated by using the modified three lumping kinetic model of tsrfcc

    摘要利用修正的兩段提升管催化裂化的三集總動力學模型分析了兩段提升管催化裂化技術的動力學特點，並對中試裝置的試驗數據進行了擬合。
  6. 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。
  7. 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。
  8. Shortcoming of conventional rfcc reactor and advantage of tsrfcc technology

    傳統催化裂化提升管反應器的弊端與兩段提升管催化裂化
  9. Maximizing yield of propylene by two - stage riser catalytic pyrolysis of heavy oil

    兩段提升管催化裂解多產丙烯研究
  10. Kinetic characteristics analysis of two - stage riser fluid catalytic cracking technology

    兩段提升管催化裂化技術動力學特點分析
  11. The results show that this model could explain the principle of tsrfcc technology in view of kinetics, and the calculated data agree well with the experimental data

    結果表明，此模型能很好地對兩段提升管催化裂化技術的原理從動力學方面予以解釋，計算數據與試驗值吻合良好。
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