油測定計 的英文怎麼說

中文拼音 [yóudìng]
油測定計 英文
oil meter
  • : Ⅰ名詞1 (脂肪; 油脂) oil; fat; grease 2 (姓氏) a surname Ⅱ動詞1 (用桐油、油漆等塗抹) apply t...
  • : 動詞1. (測量) survey; fathom; measure 2. (測度; 推測) conjecture; infer
  • : Ⅰ形容詞1 (平靜; 穩定) calm; stable 2 (已經確定的; 不改變的) fixed; settled; established Ⅱ動詞...
  • : Ⅰ動詞1 (計算) count; compute; calculate; number 2 (設想; 打算) plan; plot Ⅱ名詞1 (測量或計算...
  • 測定 : determine; determination; setting-out; admeasurement; assignment; assay; finding
  1. Petroleum products - fuels - determination of octane number, cetane number and calculation of cetane index

    產品.燃料.辛烷值十六烷值的和十六烷指系數的
  2. Cleanliness test for oil system of gas turbine measuring solid particle contaminant in oil liquid by microscopic counting method

    燃氣輪機.系統清潔度試.用顯微鏡數法液中固體顆粒污染度
  3. Methods of test for petroleum and its products - petroleum products - determination of bromine number of distillates and aliphatic olefins - electrometric method

    及石產品的試驗方法.石產品.第130部分:蒸餾產品和脂肪族烯烴溴值.靜電
  4. Then pid flow rate control algorithm is introduced. all experiments made in this chapter are about measuring the valve parameters according to spool positions, single actuator flow rate control by the calculated flow rate feedback control method, free flow rate dividing control under the sufficient pump discharge flow rate situation, proportion flow rate dividing and flow rate dividing based on meter - in flow rate feedback control method under insufficient pump discharge flow rate situation. the results of all experiments proved that the method presented in this thesis is an effective way to overcome the unreasonable flow rate dividing when simultaneously operating multi - actuators with different inertia loads

    第四章介紹了多執行器復合控制實驗系統和實驗方法;介紹了實驗採用的流量控制的pid演算法;並了執行器控制閥和閥芯位移相關的系數;做了單個執行器算流量反饋流量控制、流量足夠情況下多執行器流量任意分配、流量不足情況下多執行器按比例調節流量分配和多執行器進側流量反饋分流控制實驗;通過實驗說明了論文提出的分流控制方法能實現大小慣性負載復合操作時的合理分流。
  5. Butter. determination of ph of the serum. potentiometric method

    .乳清ph值的.電位
  6. Essential oils - determination of carbonyl value - potentiometric methods using hydroxylammonium chloride

    香精.羰基值的.氯化羥銨電勢
  7. Standard test methods for water in crude oils by coulometric karl fischer titration

    用電量卡耳費瑟滴中水的標準試驗方法
  8. Measurement of crude oil yield value. rotovisco method

    屈服值.旋轉粘度
  9. Insulating oil - determination of fibre contamination by the counting method using a microscope

    絕緣.用顯微鏡數法纖維污染物
  10. Insulating oil - determination of fibre contamination by the counting method using a microscope ; german version en 50353 : 2001

    絕緣.用顯微鏡數法纖維污染
  11. Through field tricolor ink density measurement and calculation, the actual analysis of aqueous ink tricolor of error

    本文通過三原色墨實地密度的算,分析實際三原色水性墨存在的誤差。
  12. Insulating liquids. oil - impregnated paper and pressboard. determination of water by automatic coulometric karl fischer titration

    絕緣液體.浸紙及浸紙板.用自動庫侖卡爾費歇爾滴水含量
  13. The method of indirectly measuring force exerted on ground by bucket is used to check cantilever bucket - wheel stacker / reclaimer counter - weight, working out the hydraulic cylinder force to determine the force exerted on ground by bucket and thus counterweight value

    摘要針對懸臂斗輪堆取料機配重的校核提出了1種間接接地力的方法,即通過懸臂升降液壓缸上下腔壓力算出液壓缸受力,進一步推算出堆取料機的接地力,從而確配重安裝量。
  14. Test method for density, relative density and api gravity of crude petroleum and liquid petroleum products by thermohydrometer method

    用溫差比重原有和液化石產品的密度相對密度和api重量的試驗方法
  15. This text completely and systematically studies the status and the development of the pyrolysis and the fluidization of biomass, which distill the bio - oil in the domestic and international area, as well as the existing problems. this thesis primarily include following aspects : ( l ), by experimenting and measuring the energy ( heat value ) and the content of c, h, n chemical element of right 20 kinds of common biomass, on the base of the experimental result, and respectively established the biomass energy predict experiment formula with the element of h and c is from change, and passed the ro. os examination, which provides the basis and convenience for flash pyrolysis fluidization device energy to convert the rate to compute with biomass energy utilization calculation ; ( 2 ), proceeded the tg and dtg experimentation equal velocity ( 10 ? / min, 20 ? / min, 40 ? / min, 60 ? / min ) heating and constant temperature heating by studying on eight kinds of biomass samples, according to the experimental data and arrhenius formula, we established the dynamics model of pyrolysis of, then, using the goast - redfern and p function, we also solved the dynamics parameters and analyze out every kind of biomass ' s frequency factor and parameters of activation energy, and established the every kind of dynamics model of pyrolysis of biomass, all of these provide the theories and basis to make sure the reactor ' s flash pyrolysis work temperature scope design and the describing of pyrolysis reactor dynamics ; ( 3 ), in order to study and ascertain the process of heat completely getting to pyrolysis time of varied size biomass particles, we observed and measured the ratio of length and diameter ( l / d ) with the varied biomass through electron microscope, we concluded the l / d ratios usually is from 5. 0 to 6. 0, the average is 5. 3 ; ( 4 ), we studied the process of biomass transiting and the theory of complete pyrolysis time with the theory of complicated heat field, we got the time ( t ) of the varied size biomass particles arriving to complete pyrolysis, and we knew that the complete pyrolysis time and the time which get to the biggest production ratio are identical, all of these studies provide the theory base for design and forecasting the flash pyrolysis reactor solid state resort time ; ( 5 ), according to the above experiment result, synthesize to make use of the engineering the mechanics, engineering the material, machine the design to learn the principle, deduce, establish the theory of rotation cone flash pyrolysis reactor material resort time ( t ) and reasonable rotation velocity ( or frequency ) relation theory ; and ( 6 ), we gave the reactor ' s smallest cone angle certain, reactor cone wall strength design theory, the reactor production ability theory, the power design method and the critical rotation velocity theory

    本文較全面、系統地綜述了國內外生物質熱解液化制取生物燃技術研究發展現狀及存在的問題,主要研究內容有: ( 1 )實驗、了20種常見生物質的能量(發熱量)和c 、 h 、 n元素含量,根據實驗結果分別建立了以h和c為自變量的生物質能量預經驗公式,並通過r _ ( 0 . 05 )檢驗;為閃速熱解液化裝置能量轉化率算和生物質能量利用率算提供了依據和方便; ( 2 )選擇了8種生物質試樣作了等加熱速率( 10 min 、 20 min 、 40 min 、 60 min )和恆溫加熱的tg和dtg實驗,根據實驗數據和阿倫尼烏斯公式建立了生物質熱解反應動力學微分方程,並採用goast - redfem積分法和p函數對其動力學參數進行了求解,解析出各種生物質的頻率因子和活化能參數,進而建立了各種生物質的熱解動力學模型,為科學確反應器的閃速熱解工作溫度范圍及熱解反應動力學描述,提供了理論和依據; ( 3 )為研究和確不同尺度的生物質顆粒中心達到全熱解的時間,在體視顯微鏡下對不同粒度的生物質顆粒的長徑比進行了實驗觀察和,得出生物質的長徑比( l d )一般在5 . 0 6 . 0之間,平均為5 . 3的結果; ( 4 )採用復雜溫度場傳熱學理論對生物質傳熱過程及充分熱解時間理論進行了研究,解析推導出了不同尺寸生物質顆粒中心溫度達到充分熱解溫度的時間( t ) ,得出了理論推導的充分熱解時間與最大產率的熱解時間相一致的結果,為閃速熱解反應器固相滯留時間設和預提供了理論依據; ( 5 )根據上述實驗結果,綜合運用工程力學、工程材料、機械設學原理,推導、建立了轉錐式閃速熱解反應器物料滯留時間( )與轉速(或頻率)合理匹配理論; ( 6 )提出了轉錐式閃速熱解反應器的最小錐角設、錐壁強度設、生產能力設理論和功率算方法及臨界轉速理論等。
  16. Essential oils. determination of the carbonyl value. potentiometric methods using hydroxylammonium chloride

    香精.羰基值的.氯化羥銨電位量法
  17. Diesel fuel and petrol filters for internal combustion engines - filtration efficiency using particle counting and contaminant retention capacity

    內燃機用柴燃料和汽過濾器.用粒子數和污物滯留量過濾效率
  18. Graphic technology - determination of rheological properties of paste inks and vehicles by the falling rod viscometer

    圖形技術.採用墜桿粘度對糊狀墨和載色體流變性的
  19. Oil - water - gas three - phase flow experimental facility is a equipment to calibrate the production well - logging instrument, and is also is a indispensable equipment to make interpretation plate, study interpretation method and verify interpretation data

    摘要、水、氣三相流模擬實驗裝置是為生產井儀器提供標量的場所,也是製作解釋圖版、研究解釋方法和驗證解釋資料不可或缺的設施。
  20. Based on prandtl ' s momentum transportation, this paper calculates in detail the physical quantities such as eddy viscosities, and ratio of eddy viscosity to motion viscosity, total stresses with respect to relative position in three regions of viscous sub - layer, buffer layer, and main turbulent stream for non - newtonian fluid flowing turbulently in ducts, which according to karman ' s three layer models and measurement of fluid parameters in evaluation apparatus, discusses the influence of polymer drag reduction on flowing properties of non - newton fluid, analyzes quantitatively principle of turbulent reduction phenomenon and condition of increasing reduction rate

    摘要以普蘭德動量傳遞理論為基礎,按照卡門的三層模型,通過室內模擬環道用0號柴及加入減阻劑在圓管內的流動參數的算了非牛頓型流體管內湍流邊界層的層流內層、過渡層、湍流中心的渦流粘度,渦流粘度與運動粘度比、總應力隨相對位置的變化等量參數,探討了高分子減阻劑對非牛頓流體流動特性的影響,對湍流減阻現象的機理與增大減阻率的條件進行了量分析。
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