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这个翻译我给你满分 5大神译名的游戏
日 15：27&&&&&来源：游民星空&&&&&编辑：小舟&&&&&
一个好的游戏名，往往能给游戏加上不少印象分。
传奇最网页版，多人团战跨服竞技玩法冰火战场，十年最经典游戏，英雄合击，特效绚丽，赶紧注册试玩一下，
许多国外开发的游戏，直译过来就很恰当，像(League of Legends)、(Cross Fire)、(Dungeon
and Fighter)等等，都是英文名直译过来的。
但是也有一些游戏，直译出来的名字要么太俗，要么很累赘。这时候就需要发挥翻译们的智慧了。有许多游戏名都翻译得非常高大上，给游戏加了很多印象分，玩家接受程度也非常高。一起来看看吧！
1、《古墓丽影》
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原作名《Tomb Raider》
tomb：坟墓，墓穴
raider：袭击者，侵入者
比较一下“古墓入侵”和“古墓丽影”就能发现，第一个翻译虽然非常符合原意，但是跟“古墓丽影”比起来就逊色多了。因为这游戏有一位非常漂亮的女主角，单从“丽”字就能让玩家浮想联翩了。而“影”则突出了古墓里神秘、阴暗的环境。
古墓丽影，这游戏名字就和内容一样经典，这种情况在游戏界是很少见的。两个字，就让这游戏多了一层神秘和美感。
古墓丽影是一款由英国EIDOS公司研发的特色类的游戏，这是一款以女性视觉创作的一款冒险游戏！游戏以美式风格的女英雄为背景打造了一款趣味十足的冒险游戏。
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Pressurized gas scrubbing, pressureswing adsorption, chemicalabsorption, andmembrane and cryogenicprocesses aresome examples of well-establishedtechnologies for the removalofCO2 fromgaseous products.3 The aimofthis work isto design and evaluate an alternativeprocess for the conditioningof natural gases with a large CO2content using gashydrates. The basic idea is to takeadvantage of selectiveenclathration of guest moleculesinside a gas hydrate crystalstructure at elevated pressures andslightly sub-ambient temperatures.In the past, several authors havecontributed their ideasconcerning the conditioning of gaseousmixtures using gashydrates. Spencer et al.4-6 publishedseveral papers discussingthe feasibility of CO2 removal frommulti-component gasstreams, such as synthesis gas(syngas) or flue gases. In1996, investigations of CO2-gasmixtures in hydrate-formationconditions were published.4Thereafter, a hydrate-basedselective removal of CO2 from syn gas was proposed.5Syn gasis a mixture ofH2, CO, andCO2. The syngas is contacted in ahydrate-formation reactor with waterfor the purpose ofproducing a CO2-clathrate slurry and aCO2-depleted vaporphase (mainly H2 and CO). To lowerworking pressures, apromoting agent (e.g., H2S, SO2, andCS2) is added to thescrubbing water. It was concludedthat, after this process, theCO2 content in the syngas will be lessthan y=0.01. Recently,Spencer et al.6 also proposed agas-hydrate-based process forcapturing CO2 from flue gas. Theprocess showed the capabilityof removing more than 90% of CO2 fromthe vaporphase. Kremer7 also publishedextensive modeling and adiscussion regarding the purificationof syngas using gashydrates. He concluded that there isno potential for anapplication of a gas-hydrate-basedprocess froman economicalpoint of view for this task.The CO2 scrubbing fromflue gases(CO2,N2,O2, andH2O)by applying gas hydrates was analyzedtheoretically by Lingaet al.8 andKyono and Saito.9 Bothresearch groups concludedthat a separation process using gashydrates together withtetrahydrofuran (THF) as a promotingagent is generallyfeasible and would achieve a highpurity of recovered CO2together with low cost and energyconsumption.Kang and Lee10 and Duc et al.11published experimentalwork on the hydrate formationconditions of flue gases withand without promoters [THF andtetrabutylammonium bromide(TBAB)]. They were able to confirm theresults of thetheoretical studies by Linga et al.8and Kyono and Saito.9To the best of our knowledge, up tonow, no work has beenpublished regarding the conditioningof CO2-rich naturalgases (e.g., biogas and landfill gas), with the term“conditioning”referring to the removal of inertcomponents and,especially, sour gases. The focus ofthis paper is to study thegeneral thermodynamic and economicfeasibility of using agas-hydrate-based technology for thistask.The following sections will providethe theoretical backgroundfor the presentation of the resultsand discussion ofexpected energetic efficiency.FundamentalsGas hydrates are physical inclusioncompounds belongingto the group of clathrates.They areice-like solids consisting ofthe host molecule water and volatileguest molecules. As aresult of hydrogen bonds, watermolecules form a regularcrystal lattice with well-definedcavities (cages). The crystalstructure is stabilized by encagingsmall guest molecules. Anymolecule can act as a guest as long asit is physically able to fitinto the cavity and does not possessthe ability to formhydrogen bonds with the neighboringwater molecules. Thereis no thermodynamic stability for theempty water latticeitself. A broad introduction to thetopic of gas hydrates isgiven, e.g., byMakogon12 and Sloan andKoh.13Three different gas hydrate crystalstructures are known tobe relevant for practical aspects.These are the cubic structuressI and sII14,15 and the hexagonalstructure sH.16 Some basicstructural properties of the threecrystal modifications areshown in Figure 1.At lowtomoderate pressures (&500bar), a crystal cavity isusually occupied by only oneguestmolecule. For the thermodynamicstabilization of the hydrate phase,not all availablecavities have to be filled with guestmolecules. The degree ofcavity filling varies with guestspecies, temperature, andpressure. Hydrates are thus referredto as nonstoichiometriccompounds. Typical hydrate-formingsubstances are hydrocarbonsof methane up to butane, CO2, as wellas nitrogen.They are also typical natural andbiogas constituents.Figure 2 depicts the hydrateequilibrium curves of puremethane and pure carbon dioxide aswell as an equimolarmixture consisting of CO2 (1) and CH4(2) with y1 = 0.5, asapplied in this work as a referencemixture. Along the threephaseboundary line, there is coexistencebetween the solid gashydrate, the aqueous liquid, and thevapor phase. Hydrateformation is possible on and above therespective equilibriumline. From an isothermal point ofview, the lower equilibriumpressure of CO2 hydrate can beinterpreted by means of apreferential enclathration of CO2molecules with respect tomethane.Gas-cleaning processes for the removalof CO2 from gaseousprocess streams can generally beclassified into fourtypes: absorption, adsorption,cryogenic, and membraneprocesses. In the field of biogasconditioning, the latter twoare in the pilot phase, whereasadsorption and absorption arethe process types most commonly used.3Taking a look attechnologies for small- andmedium-scale conditioning ofgases with high CO2 content (assumingno industrial wasteheat to be available) from an economicpoint of view, thepressurized gas scrubbing (PGS) iscurrently the process ofchoice (e.g., Klinski3). One of themain advantages of usingwater as a scrubbing agent in PGS canbe seen in its highflexibility toward raw gas capacityand composition as well asits capability of a simultaneousremoval of other undesiredfeed gas constituents, such as H2S,SO2, andNH3. The maindrawbacks of this technology are thenecessity of additionalwater removal (drying) after thescrubbing step as well as therelatively high rates of scrubbingwater in circulation. Adetailed description of the PGS isgiven by Sattler.18 Becauseof the wide acceptance of the PGSprocess for purification ofhigh CO2 biogas streams, PGS here waschosen as a referenceprocess to evaluate the relativethermodynamic efficiency ofthe newly proposed gas hydrateprocess. For a better comparisonof the two processes, both the PGS andgas hydrateprocess (GHP) were modeled in thecontext of this work.The solubility of the natural gasconstituents in theaqueous liquid at the respectivepressure and temperaturepk and Tk, were described by a simplified version oftheKrichevsky-Kasarnovsky19 equation bymeans of its molarfraction xi,k公式Therein, fi,k, vi,k, and p0Ws denotethe fugacity of component iin the vapor phase, the partial molarvolume of the component,and the vapor pressure of pure water,respectively.Vapor fugacities were directlycalculated using the Wagnerequation of state in the GERGformulation.20 The partialmolar volumes of the reference gasconstituents CH4 and CO2were taken from the literature.21 Toaccount for the temperaturedependence of theHenry coefficient,the following correlationwas usedHi, 公式e2TConstants Ai-Ci were determined byregression of experimentalgas solubility date taken from theliterature22-29 andare tabulated in Table 1.To predict the three-phase equilibriumline of CH4-CO2mixtures for this work, thedescription of the hydrate phaseaccording to the solid solution theoryby van der Waals andPlatteeuw30 was chosen. This modelprovides a relationbetween the chemical potential of thefilled hydrate and theliquid water with respect to areference state for which thehypothetically empty hydrate latticeis chosen (superscripts H,L, and β). The difference of thechemical potentials betweenwatermolecules in the liquid and solidphases can be expressedas follows:ΔμHW? μLW - μHW? μLW - eμβWt Δμβ-HWT e3TIf the system is in its equilibriumstate (/), eq 3 becomesΔμH-LWeT_, p_T ¼! 0 e4TThe chemical potential of the liquidwater phase can generallybe expressed by means of its activity.This work assumes a thus, the activityof the liquid water is equalto the water molar fraction (aW =xW).ΔμH-LW? μL0WeT, p0T- μβWt RT lneaLWT- Δμβ-HW≈Δμβ-L0Wt RT lnexLWT- Δμβ-HWe5TThe terms Δμ0Wβ-L and ΔμWβ-H describe the difference of thechemical potential between the watermolecules in the hypotheticalempty hydrate lattice and the pureliquid as well asbetween the empty and the filledhydrate lattice. The latter canbe directly calculated fromthefractional filling of the hydratecages θi,j using the followingexpression:Δμβ-HW? -RTXiνi lne1-Xjθi, jT e6TAccording to the van derWaals-Platteeuw model, θi,j can berelated to the fugacity of guestcomponents in the vapor phaseand the temperature-dependent Langmuirconstant Ci,j.θi, j ¼Ci, j f Gj1tPj Ci, j f Gje7TFor this work, the Langmuir constantswere correlated asproposed by Anderson et al.31Ci, jeTT ? C0i, j exp -εi, jRT_ _e8TBecause Anderson’s model31 provides adirectmathematical solutionof the configurational integral, nonumerical solution of thelatter is required and, thus,thismodelomits the typical problems ofextreme model sensitivity andresulting numerical difficulties duringparameter optimization procedures.Additionally, Anderson’smodel31 possesses an excellentcapability of reproducing themacroscopic temperature dependence ofLangmuir constants.Appropriate procedures for thedetermination of the parametersCi,j and εi,j as well as a discussionof the advantage of using themodel of Anderson et al.31 were taken fromWindmeier.32The values for Ci,j were determined byregression to puremethane and pure CO2 hydrateequilibrium and compositionaldata. An extensive summary ofavailable hydrateequilibrium data was recently compiledby Windmeier.32
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求英语大神翻译：反观当下大恩不言谢
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汉语跟英语是不能完全对译的,这里可以用：in the opposite, we can find that xxx(后面就说现在的事就行了..最后带个现在的时间状语）,on the contrary,之类的也行.
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