蒸汽加熱的 的英文怎麼說

中文拼音 [zhēngqìjiārède]
蒸汽加熱的 英文
steam heated
  • 蒸 : Ⅰ動詞1. （蒸發） evaporate2. （利用水蒸氣的熱力使食物熟或熱） steam Ⅱ名詞[中醫] （將藥物隔水蒸熟） steaming
  • 汽 : 名詞1. （由液體或某些固體變成的氣體） vapour2. （水蒸氣） steam
  • 的 : 4次方是 The fourth power of 2 is direction
  • 蒸汽 : vapour; reek; breath; steam蒸汽採暖 steam heating; 蒸汽錘 [機械工程] steam hammer; 蒸汽打樁鍾 ste...
  1. Supply & install of 12 ", 18 " steam heaters including pipline modification works in crc tsing yi terminal in 2005

    2005年于華潤青衣油庫改裝油喉並供應及加裝12 "及18 "的油喉蒸汽加熱裝置。
  2. It is widely in sectors of petroleum, chemical engineering, power, printing and dyeing textile for heating and steaming system, condensation water recycling and over heating steam projects

    該閥廣泛用於石油、化工、電力、紡織印染、等行業的各種蒸汽加熱設備，蒸汽管網、凝汽管網、凝結水回收工程和低過熱蒸汽工程。
  3. Purpose : heat with steam to filled carbon dioxide drinks or cool down hot filled drinks

    用途：對灌裝好的含氣清涼飲料進行蒸汽加溫或對灌裝好的熱灌裝飲料進行降溫。
  4. Combined with the actual condition of the plant simulator, this paper analyzes the native and abroad development of the simulation device. the main content is followed : introducing the characteristics and managing specialties of the simulator project in detail ; introducing the simulation object, describing the hardware, software structure and functions of the simulation object ; describing the exploitation process and mathematic model of the main steam, reheater, by - pass system, regenerative heater extraction, deareator, pipes, network system and pumps

    本文分析了國內外模擬培訓裝置的發展狀態，並結合本廠模擬機開發的實際情況，其主要工作如下：詳細介紹了模擬機開發項目的特占和管理特殊性；介紹了模擬對象和所開發模擬機的硬體結構、軟體結構，以及它的功能；詳細介紹了作者參加開發的汽機系統的主蒸汽、再熱蒸汽和旁路系統，回熱抽氣和除氧系統，以及管道、管網和泵等模型的開發過程和數學模型。
  5. The stainless steel reaction vessel is composed of vessel cover, drum body, jacket, mixer, shaft seal actuating device and support, and the part of equipment which directly contacts with material all adopts

    我廠生產的電蒸汽導熱油加熱不銹鋼反應鍋由鍋蓋筒身夾套攪拌器軸封傳動裝置及支承等組成，與鍋內物料接觸處的鍋體和零部件均採用0cr18ni9或1cr18ni9ti不銹耐酸鋼板製成。
  6. Electric - heated warming washing is especially suitable for small sized washing factories and laundries which without steam source

    電/汽加熱方式加溫洗滌，更加適合無蒸汽的洗衣店和小型洗衣廠所使用。
  7. Through analyzing the effect of temperature and nitrogen on crude oil viscosity the influences of different nitrogen injection volume and injection modes on steam displacement are contrasted, the mechanism of nitrogen - assisted steam stimulation is clarified, which includes : heat carrying capacity is raised, the saturation of remaining oil is reduced after nitrogen - assisted injection is made ; crude oil flow is enhanced because of nitrogen compression and dispersion and the change of oil flow shape ; water back - production rate is improved by expanding the steam sweep volume and compensating in - situ energy ; steam distillation effect is enhanced

    通過分析溫度、氮氣對原油粘度的影響，對比不同注氮量、不同注入方式等對蒸汽驅油效果的影響，弄清了氮氣輔助蒸汽增產的機理主要表現在：氮氣輔助后增加攜熱能力，降低殘余油飽和度，氮氣的壓縮膨脹作用分散和改變了原油流動形態，增強了原油流動性；擴大蒸汽的波及體積，補充地層能量，提高回採水率，強化蒸汽蒸餾效應。
  8. This paper analyses the water - film formation in steam heating roller and its influence on heat conduction performance to roller, and then provides a better settlement scheme for the problem of how to eliminate the water - film and improve the heat conduction performance of the roller

    摘要就蒸汽加熱輥中水膜的形成、對輥筒的導熱性能的影響進行了分析，針對如何消除水膜、提高輥筒導熱性能的問題提出了解決方法。
  9. A correlation was studied out here :, for experiment with sparger 1 # ;, for experiment with sparger 2 #. sparger decreased interfacial heat transfer coefficient, total clotted liquid and steam energy transfer and weakened surface temperature vibration. it also decreased thickness of hot water layer, attenuated steam condensation and shortened the time of balance

    加裝遮流板使實驗初期階段的表面冷凝換熱系數hif降低76 93 ；減少了累計凝結量67以上；降低蒸汽流能量的傳遞，使表面溫度波動顯著降低；減少了熱水層的厚度；減緩了蒸汽凝結的劇烈程度，大大縮短了系統壓力平衡需要的時間。
  10. Baised on tradition technology, the key product procedure were improvd on extractive mine decompose procedure of monazite in alkali, the new technology can resolve the longer tradition craft flow of vapour sequence heating be prone to emit chamfer higher energy consume 、 unstabilize operation low decompose rate, it can lower produce costing 150 yuan / t, decompose rate can be advanced 2 %

    摘要在傳統工藝的基礎上，對獨居石精礦處理的關鍵工序堿分解進行了改進，重點解決了原工藝蒸汽加熱連續分解的工藝流程長、易冒槽、耗能高、不穩定及分解率相對較低的問題，降低噸處理精礦生產成本150元左右，提高分解率2 %左右。
  11. During the research process, it is from the existing liquid sulfur heating technology - steam heating one, and comgines other several kinds of heating methods. fully comsider the relative merits of heating methods, especially do the detail discussing for utilizing the operating principle of organic carrier heating, technology process and application. giving attention to the operating specialty of harbor, at the same time consider the various kinds of requirements from customers in marker competition, to select suitable technology method in harbor transferring

    在研究過程中主要從已有的液體硫磺加熱工藝? ?蒸汽加熱工藝出發，結合其他多種加熱方式，充分考慮各種加熱方式的優缺點，尤其是對利用有機熱載體加熱的工作原理，工藝流程，應用情況進行詳細論述；兼顧港口作業生產特點，同時考慮市場競爭過程中客戶提出的各種要求等以造出適合港口中轉的工藝方式。
  12. The idea that the field bus is introduced into the field of greenhouse climate control in facility agriculture is present in the dissertation, and a node control system of greenhouse field based upon field bus technology is designed

    本文將現場總線技術引入溫室環境監控領域，設計開發了基於現場總線技術的溫室節點控制系統，基於熱交換平衡建立了溫室溫度動態模型，以及利用蒸汽加溫時溫度的動態模型。
  13. This special membrane is a porous hydrophobic membrane, which means that water vapor can pass through it, but drops of water cannot. by passing hot seawater through one side of the membrane, only the water vapor generated from the seawater passes through, the water vapor is then cooled by the cool water on the other side of the membrane, forming water drops, resulting in freshwater

    在膜蒸餾過程中，被加熱的鹹水產生水蒸汽，水蒸汽透過膜，膜的特點是允許蒸汽透過而液態水卻不能通過，透過的水蒸汽遇到溫度較低的表面后冷凝，冷凝的水滴由於膜的特殊性不能透過膜而返回，將其進行收集便得到淡水。
  14. For the type choice to each ited of technical equipment, rebuilding and its difficult points, we also discussed it. to the three kinds of heating methods steam heating, organic carrier heating and electrical heating mentioned in the paper, it deals with the four sides including energy saving, meeting the requirement of shippers, meeting the requirement of environment protection and technical possibility. we respectively compared its strong points and weak points, finally decided to utilize organic carrier heating as the technical plan of liquid sulfur heating in harbor transferring

    研究了液體硫磺自身對工藝的要求，結合港口特殊作業環境探討了對工藝的制約以及對各項技術設備的選型、改造等難點也進行了探討，對文中提到的三種加熱方式、蒸汽加熱、有機熱載體加熱、電加熱從節能滿足貨主要求，滿足環保要求，工藝的可靠性四方面著手，分別比較其優劣，最終選定利用有機熱載體加熱作為港口加熱中轉液體硫磺的工藝方案。
  15. Dr low - grade hot regeneration absorbing type desiccator, comprehensive varyimg voltage absorb and become the warm advantage that absorb, absorb under the high steam partial pressure of the normal atmospheric temperature ( work ) ; in high temperature, low steam partial pressure is it analyze to lay ( regeneration ), namely moisture that absorbent absorbed in the course of absorbing, rely on high - quality getting angry between thermal diffusion and low partial pressure two mechanism common to act on and can drive out completely in the course of regeneration

    Dr微熱再生吸附式乾燥機，綜合變壓吸附和變溫吸附之優點，在常溫高蒸汽分壓下吸附（工作） ；在較高溫度，低蒸汽分壓下解析（再生） ，即吸附劑在吸附過程中吸附的水分，在再生過程中依靠高品質再生氣（乾燥空氣加熱）的熱擴散和低分壓兩種機理的共同作用而得以徹底清除。
  16. This series of hot water tank can be installed on ship, which have the power source of steam. it can supply the hot water for crewmen

    本系列蒸汽加熱水櫃適用於具有蒸汽熱源的船舶上，加熱后的熱水供船員生活之用。
  17. 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

    建立了空氣冷卻實驗臺，熱管的加熱方式為電加熱，工質為蒸餾水.在1 1模型上對分離式熱管管內凝結換熱特性、不凝性氣體對凝結換熱的影響及不凝性氣體的擴散規律進行了試驗，得出分離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 % ；不凝性氣體對分離式熱管的凝結換熱僅影響冷凝段下部較小部分，通過排氣閥排出不凝性氣體可有效地改善冷凝段下部的凝結換熱；隨著壓力的增加，不凝性氣體對分離式熱管冷凝段的影響減少.這些結論可用於分離式熱管換熱器的工程設計和控制
  18. 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:建立了空氣冷卻實驗臺，熱管的加熱方式為電加熱，工質為蒸餾水.在1 1模型上對分離式熱管管內凝結換熱特性、不凝性氣體對凝結換熱的影響及不凝性氣體的擴散規律進行了試驗，得出分離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 % ；不凝性氣體對分離式熱管的凝結換熱僅影響冷凝段下部較小部分，通過排氣閥排出不凝性氣體可有效地改善冷凝段下部的凝結換熱；隨著壓力的增加，不凝性氣體對分離式熱管冷凝段的影響減少.這些結論可用於分離式熱管換熱器的工程設計和控制
  19. An ammonia separator is added, and the byproduct low - pressure steam from the shift section is used to heat and decompose the ammonium salt and ammonia is stripped, resulting in the effective elimination of crystallization of the ammonium salt

    增設氨分離裝置，利用變換工序副產的低壓蒸汽加熱分解銨鹽並汽提氨，可以有效解決銨鹽結晶問題。
  20. 4, mix room an adoption to clip a set of structure, can water cool off or the steam heat, hot conduct effective, mix room bottom to have to measure thermocouple, can carry on a temperature control, whether the low temperature mix a or a heating to mix or not, all can get satisfied result

    4混煉室採用夾套結構，可通水冷卻或蒸汽加熱，熱傳導效果好，混煉室底部裝有測溫熱電偶，可進行溫度控制，無論低溫混煉還是加熱混煉，均可得到滿意的效果。
分享友人
分享到 Line

分享到臉書