用蒸汽加熱的 的英文怎麼說

中文拼音 [yòngzhēngjiāde]
用蒸汽加熱的 英文
steam-heated
  • : Ⅰ動詞1 (使用) use; employ; apply 2 (多用於否定: 需要) need 3 (敬辭: 吃; 喝) eat; drink Ⅱ名...
  • : 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
  • : 名詞1. (由液體或某些固體變成的氣體) vapour2. (水蒸氣) steam
  • : 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. Taking the lest total internal losing exergy for target function, the distribute of difference in temperature among the three - effect is also acquired. an experimental device for three - effect falling - film evaporation was designed and constructed. the experiments of potassium carbonate solution was finished under different temperature of vapor and different input material liquid volume

    建立了三效降膜實驗裝置,以碳酸鉀溶液為原料進行了不同溫度、不同進料量實驗研究,得到了實驗設備(火)損分佈,並研究了各部分損失(火)及有效利(火)值與溫度與進料量關系。
  2. The article gives us a method to improve the quality of steam ; such as reducing and disusing the backwater of sugar producing in producing steam, adoping indirect heating method, and disaffiliating sugar producing

    改善品質提高酒精質量方法:減少或不製糖回水來生產;不與製糖生產同步;採間接
  3. In the third, this paper makes a survey on components of the exhausted flue gas and waste heat resource, and discusses the possibility and methods of steam generation and air preheating with the waste heat. and then, the analysis on the advantages and disadvantages of heat recovery plants with conventional steel - water heat pipes and inorganic heat - transfer heat pipes is carried out. the paper also gives a valuation about the plan and features of the design of heat recovery

    對余源排煙成分和余資源量進行標定,討論余回收產生燃燒空氣可行性和方法,分析常規余回收技術設計、採普通鋼-水管和無機傳管等傳元件設計余回收裝置優缺點,並對余回收設計方案及其特點進行總體評價。
  4. The method of concentrating the decoloration solution of tylosin is usually carried out by thin film vacuum concentration. in this experiment, the concentration process is modified by using the nanofiltration membrane technique which is free from corrosive due to the extractant solvent and in the same time, heating and decomposition of the antibiotic are eliminated, the concentration course ia also distinctly shortened. in this process the small molecule can be filtered by water, and the quality of the product such as, the tyramine content, the solubility of the product, improved significantly. in addition, the membrane filtration process could save consumption of steam and cooling water

    泰樂星提煉過程中原工藝脫色液薄膜真空濃縮,本試驗改進為耐溶媒納濾膜濃縮,料液不需要即可濃縮,防止了料液高溫分解破壞,濃縮收率明顯提高在濃縮同時,部分小分子雜質可以隨水分子一起通過納濾膜而除掉,成品質量明顯提高,解決了原工藝成品酪胺、溶解度不合格質量問題省去了原工藝濃縮中費較高、冰鹽水,經濟效益可觀。
  5. The new developments of htm station technique were introduced from the aspects such as changing the htm pipeline type in pet htm station, increasing the switch forms of steam atomization and compressed air atomization, increasing the steam generator, sending stripping tower off - gas to combination and using new material nd steel in air preheater

    摘要從改變聚酯媒站媒爐媒管線形式、增霧化與壓縮空氣霧化切換形式、增發生器、提塔尾氣送燒、空氣預器採新型材質nd鋼等方面介紹媒站技術新發展。
  6. 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

    該閥廣泛於石油、化工、電力、紡織印染、等行業各種設備,管網、凝管網、凝結水回收工程和低過工程。
  7. Purpose : heat with steam to filled carbon dioxide drinks or cool down hot filled drinks

    途:對灌裝好含氣清涼飲料進行溫或對灌裝好灌裝飲料進行降溫。
  8. Some volatilizable substances such as methanol in steam can come into product directly, and influence product greatly if the factory adopts traditional heating method in alcohol production. there fore, improving steam quality is very important to alcohol production

    摘要當甜菜糖蜜酒精生產企業採傳統直接方式生產酒精時,甲醇等易揮發組分直接進入產品,對酒精質量影響很大,因此改善品質對酒精質量是至關重要
  9. 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,與鍋內物料接觸處鍋體和零部件均採0cr18ni9或1cr18ni9ti不銹耐酸鋼板製成。
  10. Electric - heated warming washing is especially suitable for small sized washing factories and laundries which without steam source

    電/方式溫洗滌,更適合無洗衣店和小型洗衣廠所使
  11. 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、氮氣對原油粘度影響,對比不同注氮量、不同注入方式等對驅油效果影響,弄清了氮氣輔助增產機理主要表現在:氮氣輔助后增能力,降低殘余油飽和度,氮氣壓縮膨脹作分散和改變了原油流動形態,增強了原油流動性;擴大波及體積,補充地層能量,提高回採水率,強化餾效應。
  12. 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液體硫磺工藝? ?工藝出發,結合其他多種方式,充分考慮各種方式優缺點,尤其是對利有機載體工作原理,工藝流程,應情況進行詳細論述;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各種要求等以造出適合港口中轉工藝方式。
  13. 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溫室節點控制系統,基於交換平衡建立了溫室溫度動態模型,以及利溫時溫度動態模型。
  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要求,結合港口特殊作業環境探討了對工藝制約以及對各項技術設備選型、改造等難點也進行了探討,對文中提到三種方式、、有機載體、電從節能滿足貨主要求,滿足環保要求,工藝可靠性四方面著手,分別比較其優劣,最終選定利有機載體作為港口中轉液體硫磺工藝方案。
  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,在常溫高分壓下吸附(工作) ;在較高溫度,低分壓下解析(再生) ,即吸附劑在吸附過程中吸附水分,在再生過程中依靠高品質再生氣(乾燥空氣擴散和低分壓兩種機理共同作而得以徹底清除。
  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

    本系列水櫃適於具有船舶上,水供船員生活之
  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,方式為電,工質為餾水.在1 1模型上對分離式管管內凝結換特性、不凝性氣體對凝結換影響及不凝性氣體擴散規律進行了試驗,得出分離式管有一最佳充液率,其值為45 %左右;凝結換系數隨著壓力略有降低,在實驗壓力范圍內,降低了9 . 5 % ;不凝性氣體對分離式凝結換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凝結換;隨著壓力,不凝性氣體對分離式管冷凝段影響減少.這些結論可於分離式管換工程設計和控制
  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,方式為電,工質為餾水.在1 1模型上對分離式管管內凝結換特性、不凝性氣體對凝結換影響及不凝性氣體擴散規律進行了試驗,得出分離式管有一最佳充液率,其值為45 %左右;凝結換系數隨著壓力略有降低,在實驗壓力范圍內,降低了9 . 5 % ;不凝性氣體對分離式凝結換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凝結換;隨著壓力,不凝性氣體對分離式管冷凝段影響減少.這些結論可於分離式管換工程設計和控制
  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,利變換工序副產低壓分解銨鹽並提氨,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混煉室採夾套結構,可通水冷卻或傳導效果好,混煉室底部裝有測溫電偶,可進行溫度控制,無論低溫混煉還是混煉,均可得到滿意效果。
分享友人