gas reactor 中文意思是什麼

gas reactor 解釋
氣體反應堆
  • gas : n （pl gases ）1 氣，氣體，氣態 〈cf fluid; solid〉 2 可燃氣，煤氣，沼氣；【礦物】瓦斯。3 【軍事...
  • reactor : n. 1. 反應者，被試驗者；【醫學】有（陽性）反應的人[動物]。2. 【電學】礙圈，扼流圈；電抗器；【化學】反應器；【物理學】反應堆。
  1. Power transformers and reactor fittings - gas and oil actuated relay for liquid immersed transformers and reactors with conservator

    電力變壓器和反應堆配件.液浸變壓器和有存油器的反應堆用氣體和油驅動的繼電器
  2. Power transformer and reactor fittings - part 2 : gas and oil actuated relay for liquid immersed transformers and reactors with conservator

    功率變壓器和電抗器配件.第2部分:帶存油箱的液浸式變壓器和電抗器用氣動和油動繼電器
  3. Power transformer and reactor fittings - part 2 : gas and oil actuated relay for liquid immersed transformers and reactors with conservator ; german version en 50216 - 2 : 2002

    電力變壓器和電抗器配件.第2部分:帶油枕的液體浸沒式
  4. Gas - liquid mass transfer of oxygen - decane - sodium sulfite system in a stirred autoclave reactor

    硝酸反萃體系中表面活性劑對傳質的影響
  5. Gas plasma etcher plasma reactor

    氣體等離子清洗機
  6. During those hours radioactive xenon gas built up in the reactor.

    在這幾個小時中，放射性氣體氙在反應堆中聚集增多。
  7. A differential fixed - bed reactor was employed to study the reaction between iron blast furnace slag ( bfs ) / hydrated lime ( hl ) sorbent and so2 under conditions similar to those in the bag filters of a spray - drying flue gas desulfurization system

    摘要本研究以微分固定床反應器，在模擬噴霧乾燥除硫系統中的袋式過濾器的條件下，探討爐石/氫氧化鈣吸收劑與二氧化硫于低溫下之反應動力學模式。
  8. Influences of structure and operational parameters on gas hold - up in an external - loop reactor

    外環流反應器結構與操作參數對氣含率的影響
  9. Volume : 10 - 4000l gas liquid reactor

    氣液反應設備loop reactor
  10. In this paper, high heat penetration into a moving particulate bed is described mathematically with a comprehensive heat and mass transfer model. the distribution of gas velocity and pressure, the temperature field of gas and solid in the moving particulate bed are examined for different conditions. the results show that thermal penetration into the moving packed - bed particles by fluid flow in porous media is high only in the position near the gas entrance. the thermal penetration thickness tends to increase with the fluid flow velocity and decrease with the particle moving velocity. in the region of thermal penetration, the porosity of solid bed has significant effect on gas field and pressure loss. it is feasible to reduce the gas pressure loss by a larger width / height packed bed in design and operation. the correspondence between thermal infection depth and particle bed height would be helpful to keep high oapacity of reactor and reduce the cost of operation

    針對移動顆粒床中物料層內的高溫氣體滲流傳熱現象，考慮滲流與傳熱的相互作用，採用局部非熱平衡假設建立了多孔介質滲流傳熱物理數學模型並進行了數值計算.研究了不同情況下床內填充多孔介質中的流速、氣固溫度和床層壓力損失.計算結果表明，高溫熱氣對移動床顆粒料層的熱滲透主要發生在滲流入口端區域，增大入口滲流速度以及減小床層物料下移速度將導致物料溫度沿床高慢速下降，熱滲透深度擴大，熱滲透作用區域內的物料溫度水平提高.在熱滲透作用區域，孔隙率對流場和壓力損失有很大的影響.研究結果對于移動顆粒床反應器的設計與運行具有一定的參考作用
  11. Agr advanced gas - cooled reactor

    改進型氣冷反應堆
  12. Criteria for nuclear reactor reactor instrumentation part three. high temperature gas - cooled reactor

    核反應堆儀表準則第3部分:高溫氣冷反應堆
  13. The three - phase slurry - bed technology for the liquid - phase methanol synthesis is a new productive technology which converts synthesis - gas into methanol by taking three - phase slurry reactor

    液相法三相淤漿床甲醇合成技術是一種使用三相淤漿床反應器將合成氣轉化為甲醇的生產新技術。
  14. Comparing to the traditional production technology, the new methanol synthesis process has many advantages which are as follows, high conversion of synthesis - gas per pass, high methanol concentration at reactor exit, isothermal temperature in slurry bed, easy temperature control, simple heat exchanging, excellent technology economy characters and so on. so it becomes a new technology for methanol production that has great industry application

    與傳統生產工藝相比，三相淤漿床甲醇合成工藝具有單程轉化率高，出口甲醇質量分數高；床層等溫，反應條件優良；溫度易於控制，換熱簡單；生產的技術經濟指標優良等特點，因此成為一種應用前景非常廣闊的新興甲醇生產新技術1 。
  15. A two - dimensional model is proposed for simulation of gas phase cracking of 1, 2 - dichloroethane ( edc ) to produce vinyl chloride monomer ( vcm ) in tubular reactor furnace, in which side reaction of coke precursor formation is taken into consideration

    摘要建立了二氯乙烷在管式反應器中進行氣相熱裂解的二維模型，模型考慮了二氯乙烷熱解生成氯乙烯的主反應和生成焦前體的副反應以及氣體密度變化對裂解反應的影響。
  16. Mechanisim of absorption with gas - liquid reaction has been analyzed founded on theory of double film. the two calculation formulas for the absorption rate with gas - liquid reaction were put forward as follows. ( 1 ) the formula for interface wasand it was suitable for calculating any rate. ( 2 ) the general formula was. though the calculating process of this formula was complicated, it was suitable for reactor design, pariticularly for the calculation of absorption with gas - liguid reaction

    根據雙膜理論，分析了氣液反應的吸收機理.提出氣液反應的吸收速率的兩種計算形式: （ 1 ）界面式，該式適用於任意速率的計算; （ 2 ）一般式，該式計算過程較繁瑣，但對反應器設計，尤其是對帶有反應的氣液吸收過程的計算較為適用。
  17. Emission is inducted evenly into the reactor, and effectively interact with recovery solvent sprayed down from top in the filler layer, then passes through the gas and liquid separation system to eliminate moisture for releasing clean air

    廢氣由塔槽底部均勻進入洗滌塔，並在填充層與由上端噴流而下的洗滌液作有效的交換洗滌，再經由氣液分離系統去除水氣，清潔的空氣由出口排出。
  18. 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。
  19. China is poised to develop the world ' s first commercially operated " pebble bed " nuclear reactor after a chinese energy consortium chose a site in the eastern province of shandong to build a 195mw gas - cooled power plant

    一個中國能源企業集團已在山東省選定一座195兆瓦氣冷式核電站的建造地點，標志著中國將建設世界上首個投入商業運營的球床核反應堆。
  20. Considering the water spraying can effectively increase the contact area between gas and water and promote the hydrate production rate, a batch reactor with water spraying was built in order to experimentally investigate the forming performance of natural gas hydrate, the system ' s state parameters ' variation and its effect on induced time of initial pressure and water temperature

    摘要考慮到水的霧化可以有效提高氣水接觸面積，有助於提高水合物生產速率，設計和建造了一個半間歇式霧流強化水合物實驗裝置，用於探索和揭示噴霧強化天然氣水合物制備過程的基本特性，包括制備水合物的形態特徵，形成過程中參數的變化規律，以及系統初始壓力和初始水溫度對形成過程誘導時間的影響。
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