氣液平衡 的英文怎麼說
中文拼音 [qìyèpínghéng]
氣液平衡
英文
gas-liquid equilibrium-
Hiding essence of life is the main physiology function of kidney, the essence in kidney is angry, be airframe life activity this, to airframe the physiology activity of each respect all is having all in all effect ; kidney advocate water fluid, basically be the aerification function that the essence in pointing to kidney enrages, to the body fluid inside body be defeated cloth and excrete, maintain the balance that the body fluid inside body metabolizes, the adjustment with rising very important action ; kidney advocate bone gives birth to pith, it is spirit of the energy in kidney has stimulative airframe to grow actually a of growth function main component, the rise and fall that the essence in kidney enrages, affect the growth of bone and growth not only, and the plentiful that also affects spinal cord and encephalon and development ; " tine is bone ", tine and bone give one cause together, the tooth also is filled by institute of gas of the energy in kidney raise, spirit of the energy in kidney is abundant, fall off the tooth is solid and not easily, if kidney is medium air of essence of life is inadequate, criterion the tooth becomes loose easily, inchoate even fall off ; kidney have one ' s ideas straightened out at 2 shade ( external genital organs and anal ), accordingly, frequent micturition, enuresis, urinary incontinence, make water little or anuria, all the aerification function with kidney is wrong about
藏精是腎的主要生理功能,腎中精氣,是機體生命活動之本,對機體各方面的生理活動均起著極其重要的作用;腎主水液,主要是指腎中精氣的氣化功能,對于體內津液的輸布和排泄,維持體內津液代謝的平衡,起著極為重要的調節作用;腎主骨生髓,實際上是腎中精氣具有促進機體生長發育功能的一個重要組成部分,腎中精氣的盛衰,不僅影響骨的生長和發育,而且也影響脊髓和腦髓的充盈和發育; 「齒為骨之餘」 ,齒與骨同出一源,牙齒也由腎中精氣所充養,腎中精氣充沛,則牙齒堅固而不易脫落,若腎中精氣不足,則牙齒易於松動,甚至早期脫落;腎開竅於二陰(外生殖器和肛門) ,因此,尿頻、遺尿、尿失禁、尿少或尿閉,均與腎的氣化功能失常有關。Liquid and vapor phases cannot coexist in equilibrium.
液相和氣相不能在平衡中共存。The paper mainly consider the followings : the performance parameter determination of cryopump, heat load determination and heat transfer of large cryopanel, reasonable distribution of heat load, the condition for construct steady flow in small vertical circle pipeline, balance condition for gas and liquid two - phase flow in the connection pipe between cryopanel and dewar, the safety of cryopump
文中探討了低溫泵性能參數的確定;大抽速低溫抽氣面的熱負載的確定及合理分配;冷凝面上豎直圓管內受熱建立穩定流動的條件;冷凝面與杜瓦間的連接管道內氣液「雙相流動」的平衡條件;低溫泵系統運行的安全問題。Calculating of equilibrium with eos
方程的氣液相平衡計算The anion surfactant nals was the most efficient in the process and was selected as collector by orthogonal method. the interfacial tension and cmc of nals ( cmc 6. 5 10 - 3m ) in the solution was measured by hanging ring test, the function relationship between interfacial tensions and nals concentration was : = - 0. 9523 in 2c - 24. 534 in c - 81. 411. the relation of interfacial adsorption equilibrium in the solution system was respectively tested and calculated with gibbs equation and dynamic method. the conclusion showed that ( 1 ) the experiment result of dynamic method with was highly in coordination with the value which from theoretical calculation. ( 2 ) the surfactant molecule was in arrangement of monomolecular layer at the gas - liquid interface
用吊環法測定了十二烷基硫酸鈉水溶液不同濃度與其界面張力的關系,擬合得到的回歸方程為= - 0 . 9523ln ~ 2c - 24 . 534lnc - 81 . 411 ,同時還測得其臨界膠束濃度值( cmc為6 . 5 10 ~ ( - 3 ) m ) ,運用吉布斯等溫方程和動態法分別計算和測定了該溶液系統的界面吸附平衡關系,結論表明: ( 1 )動態法測定結果基本吻合吉布斯方程的理論計算; ( 2 )表面活性劑分子在氣?液兩相界面是以單分子層形式定向有序排列的。An increase in background gas, as the mud weight overbalance gradually decreases
由於鉆井液密度逐漸下降失去平衡,鉆井液的含氣量上升。This paper proposes the use of steam condensate to wash the acidulation tail gas, then to be used as wash water for washing phosphogypsum, to be returned to the crystallizer, and a calculation is made of water balance in the system, so that the discharge of wastewater and waste gas is up to standard
本文提出用蒸汽冷凝液洗滌酸解尾氣,然後用於洗滌磷石膏的洗水,返回結晶槽,並對系統的水平衡進行計算,可以實現硝酸磷肥生產的廢水和廢氣的達標排放。It is studied that the formation mechanism of taylor bubble and its control method in gas - liquid two - phase flow, which affects the pressure balance and mechanical driving efficiency in the flow of petroleum engineering. experiments show that the formation of taylor bubble in gas - liquid two - phase flow is due to the intensive congregation and amalgamation of small bubbles driven by void fraction waves and that the highly turbulent flow is able to restrain this formation. thus, the flow regime transition may be checked by increasing the flow turbulence and controlling the disturbed frequency
對大管徑氣-液兩相流動中嚴重影響壓力平衡與機械驅動效率的段塞流生成機制和控制方法進行了研究,實驗證明段塞流的形成是由於空隙率波的大幅度增長使氣泡高度集中,並形成聚並所致。強湍流運動可以抑制taylor泡的形成。因此,通過強化湍流或控制擾動頻率可以對氣泡聚並起明顯的抑制作用。The results demonstrated that the orientation of fc moiety within fc16ab monolayer changed and the angle between the interface and cyclopentadienyl ring from 70 to the cyclopentadienyl ring parallel to the air / water interface. the compressibility of fc16ab monolayer increased with the concentration of cl - increasing on the subphase containing counterions. the compressibility of fc16ab monolayer and the angle of fc contacting the water surface increased with the concentration of cl " increasing
山70改變至茂環平面和氣液界面幾乎平行;在含抗衡離子的亞相上,我們發現cl ~ -能改善fc _ ( 16 ) ab單分子膜的剛性,且隨著cl ~ -的濃度增加,單分子膜的剛性也有增加的趨勢,但增加的趨勢逐近減弱。The azeotropic distillation of the system acetic acid - water - azeotropic agent ( isopropyl acetate and butyl acetate ) is simulated. due to the non - ideal behavior, nrtl - hoc and uniquac - hoc model is used to depict vapor - liquid phase equilibrium behavior of this system. concerning the liquid in the decanter, the stability is checked by tangent plane stability analysis, and the initialization of phase splitting calculation is produced. a good estimate of the phase fration is gotten by successive substitution with newton ' s method, and every component of two phase is gotten by mass equilibrium equation. finally, the solution of this equation is produced with successive substitution calcultion. the naphtali - sandholm method is used to simulation of azeotropic distillation. by virtue of this combined calculation method, the simulation is begun with operational data as basical data. the results of simulation accord with the operating data, which proved that the combined calculation method is credible
該體系具有高度非理想性,氣液相平衡模型採用nrtl - hoc和uniquac - hoc模型,採用切平面判據法對進入分層器中的液相進行液相穩定性測試,提供液液相分離計算的初值,再結合牛頓拉夫森迭代法運算求得相分割系數,根據物料衡算求出各相組成,循環迭代可求得分層各組分數據,共沸精餾模擬計算採用那夫塔列-山德荷姆全變量迭代演算法。The results are compared with the data offered by asher. 3. the factors of compressibility of humid air are calculated by this new state equation
計算了本文提出的熱力學參數范圍內真實濕空氣的焓和熵; 5 .用eos法和活度系數法對濕空氣的汽液相平衡進行了計算。Abstract : the model parameters for uniquac and nrtl equations are obtained by using the infinite dilute activity coefficients of a component at several temperature and the nonlinear regressive technique. the vaporliquid equilibrium ( vle ) data calculated by using the parameters for uniquac or nrtl equation is agreement with that from vle experiment
文摘:通過一個組分在不同溫度下的無限稀釋活度系數,利用非線性回歸確定了四氫呋喃1 , 4丁二醇、水1 , 4丁二醇二元體系的uniquac 、 nrtl溶液模型參數.用所獲得的兩溶液模型參數對三元氣液平衡數據進行理論推算,並與實測的三元氣液平衡數據進行比較,發現兩結果比較吻合These deviations are not acceptable for typical calculations in hat. similar problems occur for caes plants. in order to meet the demands of engineering design, the humid air must be regarded as a kind of real gas and more accurate thermodynamic properties of the humid air are acquired at high temperature and high pressure
本文針對新型熱力循環中對高溫高壓濕空氣熱力學性質參數的需求,以濕空氣透平和壓縮空氣蓄能系統中的工質為研究對象,在維里狀態方程的框架下,運用對應態原理,提出一個適合計算高溫高壓濕空氣熱力學性質的對應態維里方程,並利用兩種方法對濕空氣的汽液相平衡進行計算。A concise physical picture is furnished by chemical potential curve about the law of phase equilibrium, saturated vapour pressure of curved liquid surface, evaporation and condensation etc
通過曲線描述,提供了關于相平衡、彎曲液面飽和蒸氣壓以及蒸發、凝結等規律比較直觀的物理圖像。Is the professional manufacturer of the country of producing storeage logistics equipment such as hydraulic lift tables, balance crane, jib crane, etc. the products adopt the domestic and international advanced production technology and craft
是國內生產液壓升降臺平衡吊旋臂吊氣墊裝置等倉儲物流設備的專業廠家。產品採用國內外先進的生產技術和工藝。The measurement of vle data by using an improved still
一種高沸點差三元體系氣液平衡數據的測量Predication of atmospheric vle for the ternary system dimethyl carbonate - methanol - n - hexane
正己烷三元體系氣液平衡數據的推算This article takes the chemical physics experiments " binary liquid - vapor equilibrium phase diagram " for the study, using the computer program to draw the liquid - vapor equilibrium phase diagram conveniently, and can extract composes is 0. 75 time gas phase composition and the boiling point respectively is 0. 5772, 64. 9737
文章採用計算機程序方便地繪出氣液平衡相圖,並求出了溶液組成為任意值時(以摩爾分數為0 . 75為例)的氣相組成和沸點分別為0 . 5772 , 64 . 9737 。Vle vapor liquid equilibrium app
Vle氣液平衡裝置P - t - v condition of the saturated hydrogen can be accurately predicted as well as thermodynamic properties and phase equilibrium of hydrogen fluid through this equation
此方程可用於飽和氫溶液氣液兩相p - v - t關系、熱力學性質以及氣液平衡關系的預測。分享友人