On the Current Correlators at Low Temperature

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Heat Transfer in Flow Boiling Over a Bundle of Horizontal Tubes

Heat Transfer in Flow Boiling Over a Bundle of Horizontal Tubes

HEAT TRANSFER IN FLOW BOILING OVER A BUNDLEOF HORIZONTAL TUBESB.M.BURNSIDEÃand N.F.SHIRE†School of Engineering and Physical Sciences,Heriot-Watt University,Edinburgh,UKT he paper describes tests boiling R113at atmospheric pressure in upwardflow over a 17row column of square pitched electrically heated tubes.Uniform heatfluxes of10–65kW mÀ2and maximum Reynolds numbers,Re max,between7800and27000 were used.The data at the lower heatfluxes of10and20kW mÀ2consistently exhibited alinear increase of heat transfer coefficient,h,with quality,the slope lower at20kW mÀ2,so that h at10kW mÀ2exceeded that at20kW mÀ2and both reached h at40kW mÀ2forthe maximum quality tested.At the higher heatfluxes a nucleate boiling controlled regionwas observed at low quality,with h equal to the value at the same heatflux as observedwith an isolated tube in a pool,followed by a rise in h at higher quality.The results were com-pared with the work of other researchers.Heat transfer coefficients for q!40kW mÀ2werepredicted to an average r.m.s.deviation of7%,using the asymptoticflow boiling model.How-ever,the sensitivity of h to change of quality andflowrate predicted was much lower thanmeasured and in some cases exhibited opposite trends.Keywords:cross-flow heat transfer;2-phaseflow;boiling models.INTRODUCTIONDesign of cross-flow boiling heat exchangers(Brisbane et al.,1980;Palen and Yang,1981;Burnside,1999) depends on the availability of reliableflow boiling corre-lations.Supporting these,2-phaseflow void fraction and friction multiplier correlations are required.The accuracy of these correlations must be checked by experiment. Two types of correlations forflow boiling heat transfer coefficient,h,(Webb and Gupte,1992)are used in design. They are the superimposition type,equation(1), h¼Sh npbþFh l(1) and the asymptotic type,equation(2),h¼{Sh^nnpbþ(Fh l)^n}1=^n(2)S(,1)is a suppression factor allowing for the effect of 2-phaseflow in reducing the isolated tube boiling heat transfer coefficient,h npb,and F is aflow factor accounting for the enhancement effect of2-phaseflow on the heat transfer coefficient in convection of the liquid phase flowing alone,h l.These boiling and convective com-ponents are combined additively in equation(1).Equation (2)is used usually with S¼1.A variable degree of smooth transition,from the near pool boiling conditions at low velocity and void fraction to dominant convection at high velocities and void fraction,is afforded by varying the index^n.The void fraction and2-phase friction multi-plier are linked to theflow velocity,quality and properties by experimentally based correlations(Schrage et al.,1988; Hsu and Jensen,1988;Dowlati et al.,1992).The object of this work is to provide heat transfer coefficient data over a range of quality,heatflux andflow velocity to help to vali-date current methods of prediction used in heat exchanger design.APPARATUSA full description of the apparatus can be found in Shire (1995)and Shire and Burnside(1999).The boiler is shown in Figure1.It was adapted from a732mm internal dia-meter thin slice kettle reboiler by introducing two brass walls.These sealed off a passage of rectangular cross-section,102mm wide and52mm deep,between the reboi-ler backplate and its toughened glass viewing window.The original shell space outside the brass walls was packed with polypropylene insulation.Mounted in the backplate of the reboiler shell,the17row25.4mm square pitched bundle of19mm diameter,51mm long90Cu:10Ni tubes com-prisedfive columns offive tubes with boiling surfaces inÃCorrespondence to:Dr B.M.Burnside,School of Engineering and Physical Sciences,Heriot-Watt University,Riccarton,Edinburgh,EH144AS,UK.E-mail:b.m.burnside@†Currently at British Energy.5270263–8762/05/$30.00+0.00 #2005Institution of Chemical Engineers/journals Trans IChemE,Part A,May2005 doi:10.1205/cherd.04313Chemical Engineering Research and Design,83(A5):527–538the ‘as machined’condition.The outside tubes of each row were fitted into horizontal semi-cylindrical grooves in the two brass side walls.Thus the rising test fluid washed three columns of tubes in the centre and two columns of half tubes at the outside.The tubes were separated from the window at the front by a 1.5mm viton washer and from the tubeplate at the back by a 3mm gasket.A locknut and washer secured the assembly.The wall thickness of the tube section (Figure 2),was 1.3mm along the length located in the tubeplate.This,together with the insulating effect of the seals and a thick layer of cotton covered fibre-glass insulation over the back of the shell,ensured minimal heat loss from the tube section to the backplate and the surroundings.A 9.5mm diameter,250W cartridge heater fitted closely into a pocket machined in each tube section.The leads protruded through the back of the boiler.Wall thermocouples were mounted on a 15mm pitch circle diameter in a 2mm diameter hole drilled all the way from the window end to emerge in the interior as shown in the figure.The Ni /Cr,Ni /Al thermocouple was soldered into a hole drilled in the end of a 2mm diameter copper slug.These,in turn were soldered into the holes in the tube section forming a seal at the window end.Thethermocouple leads were fed through the open end of the tube section and connected to compensating cable in an isothermal zone behind the boiler.The three full tubes in each row were fitted with wall thermocouples in this way.In the bottom 12rows and the 14th row,one thermo-couple was fitted at the top of the tube,halfway along the heated section,as shown in Figure 2.In the other rows,the central three tubes were fitted with four thermocouples spaced at 908around the circumference.In seven of these tubes the thermocouples were in the centre of the heated length.In four others the top and bottom thermocouples were positioned one-quarter and three-quarters of the heated length from the window end,respectively.Eight mineral insulated metal clad (mimc)thermo-couples,mounted on the tubeplate,were located in the centre of the space between the four adjacent tubes in the posi-tions shown in Figure 1.A further mimc thermocouple (not shown)was positioned at the feed entry.R113was pumped from a reservoir through a metric series rotameter.It flowed through an electrically heated preheater before entering the boiler through three 28mm copper pipes and a wire mesh flow distributor (Figure 1).The two phase mix-ture left the shell through a 102mm diameter opening in the backplate (Burnside et al.,2001).It passed into a 150mm Â150mm Â100mm pyrex tee where disengage-ment occurred.The liquid fraction flowed by gravity back to the reservoir.The vapour flowed up a 100mm riser into a vented,water cooled condenser whence it returned to the reservoir.The boiler,preheater and feed lines and the vapour riser were covered with a thick layer of insulation.The 85tube heaters were connected to seven voltage regulators.Power to these banks was measured by elec-tronic wattmeter.In addition the voltage drop was measured across standard 0:47V resistances in series with each heater.This enabled individual power to each heater to be determined.All the thermocouple emfs were monitored by a computer controlled data logging system sensitive to +3m V.The thermocouples were calibrated using the identical measuring system to +0:15K.A further uncertainty in surface temperature arises due to the effect of uncertainty in the radial position of the thermocouple on the correction for conduction in the tube wall.This is estimated to be 0.5mm on either side of the nominal 15mm diameter.The accuracy of measurements of heat flux varies from +1%at q ¼65kW m À2to +16%at 2kW m À2.Based on these figures,the overall estimated uncertainty in the heat transfer coefficient h is +0:1kW m À2K at q ¼65kW m À2K rising to +0:25kW m À2K at q ¼2kW m À2K,where no evaporation occurs.In some cases these uncertainties may be higher due to doubt about the precise position of some of the thermocouples in the tube wall due to ‘wander’of the drill in the tough tube material when drilling the thermocouple pocket (Shire 1995;Burnside et al.,2001).This will be referred to again below.EXPERIMENTAL PROCEDURE AND DATA REDUCTION Initially,10runs were carried out with a uniform q of 2.5kW m À2K.No vapour formation was observed.The inlet liquid temperature was kept to within 1K of the normal boiling point.Mass fluxes,G max ,between 200and 710kg m À2s À1,referred to the minimum flow area,were used.In these tests the guard heater tubes at the outsidesofFigure 1.Experimentalboiler.Figure 2.Heater tube section assembly.Trans IChemE,Part A,Chemical Engineering Research and Design ,2005,83(A5):527–538528BURNSIDE and SHIREeach row were set to0.5q.The results are shown in Figure3in the form h versus Re max,defined by equation(3).D is the tube diameter and m l is the liquid phase viscosity.Re max¼G max Dm l(3)The values presented are the arithmetic means for the17rows measured.For comparison the predictions of ESDU73031 (1973)are shown.Although the data are somewhat above the prediction at the lower Reynolds numbers,the agreement is within the predicted experimental error indicating the validity of the estimate of error.Fifty-two boiling tests were conducted at massfluxes from200to710kg mÀ2sÀ1over the heatflux range10 to65kW mÀ2.In the majority of the tests the guard heaters were set at the same heatflux,q,as the central tubes in the bundle.In the remainder it was set at0.5q with no effect on the variation of h with x,provided the correct row average heatflux was used in calculating the local quality x.To avoid hysteresis,before commencing the tests the heat flux was set high before being reduced to the nominal value.The rig was allowed to settle to steady conditions for about two hours before data were taken.Then tubewall and liquid temperatures,heater power and the massflow-rate of R113entering the column and R113condensate leaving the condenser were monitored.It was not possible to carry out a meaningful heat balance for the column.The high massflowrates used resulted in entrainment of an unknown amount of liquid with the vapour rising to the condenser.This led to an overestimate of the enthalpyflux to thefluid based on the assumption that theflow into the condenser was all vapour.As a result the calculated difference between power input and the enthalpyflux to thefluid was consistently negative. However,due to the design of the tube sectionfixing, any heatflux direct from the heaters to the backplate or to the surroundings was very small.This was confirmed by tests on the full boiler(Shire,1995)where the overall heat loss from the shell and vapour riser fell from about 7%at q¼5kW mÀ2K to much lower values at higher q. The quality,x,at each row level was calculated from the massflux and the heatflux in the rows below,including the guard heaters,plus half the heatflux in the current row. The error in x at thefirst row level was estimated(Shire, 1995)to vary from14%at5kW mÀ2to8%at65kW mÀ2. At row17,the correspondingfigures are4%at all heat fluxes.Average tubewall temperatures of each row,T wm, were taken to be the arithmetic mean of the measured values for each of the three central tubes,corrected for heat conduc-tion.T w was taken to be the single value available for the tubes with one thermocouple and the arithmetic mean of the four available on the other tubes.The local liquid temp-eratures were calculated as the mean values of the two near-est measurements,T lm(Figure1).Mean heat transfer coefficients for each row were calculated using equation (4).q m is the average heatflux and T wm the arithmetic mean wall temperature for the three central tubes in the row.h m¼q m(T wmÀT lm)(4)It was noticeable that the resulting values of h m,for the rows including tubes with four thermocouples,were not altered significantly by different methods of averaging T w.RESULTSFigure4(a)shows the variation of measured heat transfer coefficient with quality for the lowest Reynolds number used in the tests,Re max¼7800.In this and subsequent figures,data from the bottom three rows of the column have been omitted to avoid the distorting effect of subcool-ing at entry.The values shown in thefigure are calculated from the data for all combinations of row position in the bundle and for all heatfluxes used.On the right hand ordi-nate the isolated tube pool boiling heat transfer coefficients, h npb,predicted by the Mostinski(1963)correlation,are marked for comparison.1These have been verified by Tarrad(1991)in tests on the tube sections used in this inves-tigation.Also plotted is h l,the convective heat transfer coefficient for the liquid phaseflowing alone based on the ESDU(1973)correlations.The data have beenfitted by least squares and thefitted lines are plotted in thefigure. Root mean square deviations,1h,of h from thefits,defined by equation(5),are shown in Table1.1h¼ffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiS(hÀh fit)2NÀ1s(5)They vary from+0:09kW mÀ2K at q¼10kW mÀ2to +0:13kW mÀ2K at q¼40kW mÀ2.This compares well with the estimated error of the experiment.However,the data for rows13and14exhibit more scatter at all heat fluxes than is observed for the other rows,reaching +0:25kW mÀ2K at40kW mÀ2.Moreover,values of h at row13are consistently much higher than at row14which itself is lower than the trend of the other rows.This points to a systematic error and is attributed to greater than assumed uncertainty in the radial positioning of the thermocouples in these rows.Raising this to between+1and+1:5mm results in estimated errors of the magnitude of the scatterin parison of liquid only convection test data and prediction.1The scale of h on this ordinate is the same as on the left hand ordinate inthis and subsequentfigures.Trans IChemE,Part A,Chemical Engineering Research and Design,2005,83(A5):527–538HEAT TRANSFER IN FLOW BOILING OVER HORIZONTAL TUBES529h observed around these rows at all tested values of q and Re max .No marked difference in flow boiling conditions could be seen around these rows.It was decided to ignore the data taken at rows 13and 14rather than attempt to correct it to account for notional uncertainty in D t =c .Figure 4(b)shows the remaining data for Re max ¼7800.As expected,1h is reduced (Table 1).Data for Re max ¼14000,19500,23000,24000and 27000are shown in Figures 4(c)–(f)respectively,and 1h ,omitting rows 13and 14,in Table 1.Below 50kW m À21h is less than +0:10kW m À2K and rises to a maximum of +0:12kW m À2K at 65kW m À2.Using the fits h ;h (x ,q )at constant Re max ,shown in Figures 4(b)–(f),cross-plots in the form h versus Re max and h versus q ,both at constant quality,were obtained over the whole range of qualities tested.The latter isTable 1.Standard deviation of data from least square fits,kW m 22K (Ãall rows 4–17).Re max q (kW m 22)10204050657800Ã0.090.100.13––78000.060.050.08––140000.060.070.090.11–15400––––0.12195000.090.080.090.100.12230000.07–0.090.100.1224000–0.08–––270000.080.090.090.110.12Figure 4.Data h versus x ,with h npb and h l ,(a)Re max ¼7800,all rows 4–17;(b)Re max ¼7800,rows 4–12,15–17;(c)Re max ¼14000;(d)Re max ¼19500;(e)Re max ¼23000;(f)Re max ¼27000(A ,q ¼10kW m 22;4,q ¼20;Â,q ¼40;W ,q ¼50;O ,q ¼65).Trans IChemE,Part A,Chemical Engineering Research and Design ,2005,83(A5):527–538530BURNSIDE and SHIREshown in Figure 5.The range of the plots was limited,at low qualities because high heat flux data were not available at the lower values of Re max and,at the higher qualities,because low heat flux data were not available at the higher Re max .To show the sensitivity of heat transfer coef-ficient to quality and flowrate,the slopes of the h versus x measured data,(@h =@x )q,Re ,and h versus Re max cross plots,(@h =@Re )q,x ,were calculated over the range of data avail-able.Figures 6and 7(a)show (@h =@x )q,Re for q ¼10and 20kW m À2and the higher heat fluxes,respectively.(@h =@Re )q,x is shown in Figure 7(b).DISCUSSION Limit of Zero QualityUsing the curvefits,the h versus quality data in Figure 4were extrapolated to the value h x ¼0at each flowrate and heat flux,Table 2.At the higher heat fluxes,q 520kW m À2,h x ¼0¼h npb within experimental error,at all flowrates.This agrees with a summary of early work by Collier (1990).Cornwell and Scoones (1988)investigated the boiling of R113at atmospheric pressure in a tube bundle of slightly different geometry.Their data at Re max ¼5700,as revealed byWebb and Gupte (1992),are plotted together with the Re max ¼7800data of the present work (Figure 4(b)),the closest possible match,in Figure 8.Their test bundle was more tightly packed,s =D ¼1.25,and the tube diameter larger,25.4mm,than the values s =D ¼1.33and D ¼19.1mm used here.Extrapolating to zero quality,this data revealed h x ¼0ranging from 18%to 10%greater than h npb as q rose from 12to 36kW m À2.Hsu and Jensen (1988)plotted h versus quality for 1500,Re max ,6000at q ¼12.6kW m À2in a square pitched bundle of 7.94mm diameter tubes,s =D ¼1.3and 1.7in vertical upflow of R113at 2.06b .For these conditions h npb ¼1.1kW m À2(Mostinski,1963).Although the scatter was high near x ¼0,h x ¼0varied from 40to 60%higher than h npb between the lowest and highest flowrates,respec-tively (Hsu and Jensen,1988).However,Fujita et al.(1984)and other studies of boiling on tubes in a column located in a pool of saturated liquid,have shown that h on the bottom tube is the same as h npb measured with the tube on its own in the pool (Fujita et al.,1988).The cross-flow induced by recirculation had no effect on nucleate boiling.In the present tube bundle study,at q ¼10kW m À2,h x ¼0is greater than both h npb and h l up to Re max ¼19500(Table 2).Thus,the explanation cannot be simply that each mode occurs on an area of tube surface separate from the other.In some way the two must be complementary.At higher flowrates h npb ,h x ¼0,h l .Sufficient nucleate boiling sites are active to stop convection occurring over the whole surface.Hwang and Yao (1986),also in R113at 1atm,measured h x ¼0direct for upward flow of 6K subcooled liquid over a single 19mm diameter horizontal tube in a channel 87mm wide for 220,Re max ,17300.At q ¼10kW m À2,h x ¼0at Re max ¼17300was 30%greater than at Re max ¼220.At q ¼20kW m À2,it was 20%greater.At higher heat fluxes h x ¼0did not vary with flowrate,all the data merging into a ‘fully developed’boiling curve,h x ¼0¼0.224q 0:67which they assumed to merge with h npb (q ).Notably,this ‘fully developed’boiling curve data is higher than the Mostinski (1963)pool boiling values.Thus the measured h x ¼0(Hwang and Yao,1986)was 30%higher than the Mostinski h npb at Re max ¼220,rising to 85%higher at Re max ¼17300.The corresponding figures were 35%and 60%higher respectively,at q ¼20kW m À2.At higher q,Figure 5.Cross-plot h versus q at constant quality with h npb and h l ,(a)x ¼0.022;(b)x ¼0.12.(Re max values:A ,7800;4,14000;Â,19500;W ,23000;†,23800;þ,27000).Figure 6.Data,plot of (@h =@x )q,Re versus Reynolds number,q ¼10and 20kW m 22.Trans IChemE,Part A,Chemical Engineering Research and Design ,2005,83(A5):527–538HEAT TRANSFER IN FLOW BOILING OVER HORIZONTAL TUBES 531where h x ¼0did not depend on flowrate,the directlymeasured h x ¼0was 30%higher than the Mostinski h npb at both q ¼40and 65kW m À2.Contrary to the present data,these results show a large dependence of h x ¼0on flowrate at low q and fully developed nucleate boiling levels of h x ¼0very much higher than h npb predicted by the Mostinski correlation.Two Phase FlowBefore discussing the results for 2-phase crossflow it is important to identify the flow regimes obtaining.For a given flow geometry and tube surface character,flowrate,quality and heat flux have an influence on flow regime.Void fraction for the conditions of the tests was calculated using the Schrage et al.correlation (Schrage et al.,1988),equation (6),which has been shown to fit R1131atm data (Schrage et al.,1988).aa h¼1þ0:123Fr À0:191ln x (6)If a =a h ,0:1then a =a h ¼0:1.Based on this,the co-ordinates of the Grant and Chisholm (1979)flow pattern map,U gs (r g =r l )0:5,and U ls (r l m l )1=3=s were evaluated over a range of values of G max and x covering the data.Extra-polating where necessary,the flowmap placed all the tests in the bubbly flow regime.This was surprising since,atFigure 7.Sensitivity of h to quality and flowrate.(a)Data,plot of (@h =@x )q,Re versus Reynolds number;(b)Data,plot of (@h =@Re )q,x versus quality;(c)Equation (2)^n¼4,(@h =@x )q,Re versus Reynolds number;(d)Equation (2),^n ¼4,(@h =@Re )q,x versus quality.Table 2.Limiting values h x ¼0of h (kW m 22K)as x !0.h npb(Mostinski,1963)Re max780014000195002300027000h x ¼0,q ¼100.760.9 1.0 1.10.90.9h x ¼0,q ¼20 1.23 1.1 1.1 1.2– 1.2h x ¼0,q ¼40 2.00 2.0 2.0 2.0 2.1 2.1h x ¼0,q ¼50 2.33– 2.3 2.3 2.3 2.3h x ¼0,q ¼65 2.80–– 2.6 2.7 2.7h l–0.600.810.961.051.14Figure parison of present data with Cornwell and Scoones (1988).Trans IChemE,Part A,Chemical Engineering Research and Design ,2005,83(A5):527–538532BURNSIDE and SHIREthe higher qualities and lower flowrates,intermittent or annular flow was observed in the column of fluid flowing in the passage formed by the gaps between the in-line con-figuration tubes.Xu et al.(1998)have produced a modified version of this flowmap taking into account their air /water experiments,which used a square pitch configuration,s =D ¼1:25.The data of this investigation are shown on the map in Figure 9.All the tests at q ¼10and 20kW m À2were predicted to be in the bubbly flow regime.At q ¼40kW m À2and Re max ¼7800,the data were in the intermittent region at low quality,extending into annular flow at the higher qualities tested.At higher flowrates bubbly flow was predicted in all the tests.At 50and 65kW m À2,at the highest qualities annular flow was pre-dicted at all flowrates,with bubbly flow at the lower quali-ties.Bearing in mind that the flow pattern maps were based on adiabatic experiments with tubes of lower diameter,this was in reasonable agreement with observation.From a design point of view,the dependence of h on x at constant Re max and q in the experiments (Figure 4),is directly related to the development of the flow up the colu-mns of a kettle reboiler bundle,including any change of flow regime.Each point on the loci of h versus Re max at con-stant x and q is derived from data at constant x obtained from tube rows successively lower down the bundle.Each point represents data from different tests at the same q .Thus the relation h x,q ;h (Re )does not refer to a development of flow in a reboiler but purely the effect of changing the flow-rate on h in the general design correlation,equation (7).h ;h (x ,Re ,q ,Freg,Geom,Scond)(7)and applied as such in design.In equation (7),Freg is the flow regime,Geom is the flow geometry and Scond is the tubewall surface condition.In the tests,all the tubes were manufactured in the same batch.The entry effects were eliminated by ignoring the data from the first four rows.Thus,the effects of surface condition and geometry,in this case the position of the row in the column,were minimized.In addition to the evidence of the cross-plots h q ;h q (Re max ,x ¼c ),it would be useful to get physical evidence of the form which this relationship should take.A hypothetical experiment may be devised to do thisdirectly for a specific tube row.Consider a uniformly heated channel,heat flux q .At entrance to the channel the flowrate and quality (or subcooling),x inch (D T sub )can be varied.Conditions are kept within the range of the data.Heat trans-fer measurements are made on an instrumented tube row at a series of increasing flowrates,simultaneously increasing x inch (decreasing D T sub )so that the approach quality to the instrumented row remains the same.It was shown above that most of the data were in the bubbly flow regime.In fact,all of the points covered by the h ;h (Re ,x ¼c )cross-plots,referred to at the end of the Results section,represent data in bubbly flow,as in our hypotheti-cal experiment.In these cross-plots,points at successively higher values of Re max represent rows increasingly higher up the bundle,whereas the data from the hypothetical experiment is all for the same row.The approximation involved in this assumption lies in ignoring any effect of row level on the correlation,equation (7).This might result,for example,from a difference in the distribution of bubbles at the same void fraction,or even a change in the relation-ship between void fraction,x and Re max ,due to different development of the flow up to the levels from which data points were obtained.The approximation involved in ignor-ing these effects is assumed to be of the same order as that involved in the use of design equations such as equation (6),which is used to predict void fraction at any level in the bundle and at any values of x ,G and q .Similarly,Figure 5and the dependence h ;h x,Re may be given physi-cal significance as the data from experiments on the same experimental set up.This time the flowrate is held constant and x inch increased (D T sub decreased)to maintain quality as the uniform q of the bundle is decreased.These arguments will be developed in the later section on correlation.Results:q 510and 20kW m 22At q ¼10kW m À2,h l ,h npb at Re max ¼7800and,rising with flowrate,h l .h npb above Re max ¼14000,Figures 4(b)–(f).To within experimental error h increased linearly with x ,rising from 2.4to 2:7Âh npb and from 3.4to 1:8Âh l between Re max ¼7800and 27000,for the values of x used in the tests.(@h =@x )q,Re (Figure 6),rises linearly with flowrate to Re max ¼19500and even more rapidly thereafter.At Re max ¼27000the effect of increase in quality on h is over four times that at Re max ¼7800.Extra-polating to zero flowrate,(@h =@x )q,Re !0,inferring that quality ceases to affect the heat transfer coefficient in ‘pool’conditions,at the low values used in this study (x 0:06).This seems reasonable since forced convection is absent and nucleate boiling should be dominant.At this heat flux,the sensitivity,(@h =@Re )q,x ,of h to flowrate is independent of flowrate (Figure 7(b)),and is twice as great at x ¼0.04as at x ¼0.02.Similar results were obtained at q ¼20kW m À2Áh l ,h npb at all flowrates (Figures 4(b)–(f)).At the maximum qualities tested,as Re max was increased from 7800to 27000,h rose to between 1.5Âand 1:7Âh npb and 1.5Âand 1:8Âh l .The effect of increase in quality on h was about half that at q ¼10kW m À2but again quadrupled over the range 7800 Re max 27000(Figure 6).(@h =@Re )q,x was again independent of flowrate,and increased by more than 70%over the range 0:02 x 0:04(Figure7(b)).Figure 9.Data plotted on flow pattern map of Xu et al.(1998).Locus of maximum ordinate at each q shown.Trans IChemE,Part A,Chemical Engineering Research and Design ,2005,83(A5):527–538HEAT TRANSFER IN FLOW BOILING OVER HORIZONTAL TUBES533。

考研英语-试卷104

考研英语-试卷104

考研英语-试卷104(总分:142.00,做题时间:90分钟)一、 Use of English(总题数:2,分数:80.00)1.Section I Use of EnglishDirections: Read the following text. Choose the best word(s) for each numbered blank and mark A, B, C or D.(分数:40.00)__________________________________________________________________________________________ 解析:The 1990s have been designated the Decade Against Drug Abuse by the United Nations. But, (1)_____ less than three years to go before the end of the decade, governments and health organizations (2)_____ that they have made (3)_____ progress in reducing drug, alcohol and tobacco abuse. Today, consumption of all these substances is increasingly steadily worldwide. (4)_____ every country now has problems with (5)_____ drugs. And the world is producing and consuming more alcohol and tobacco than ever. Between 1970 and 1990 beer production (6)_____ rose by over 80 per cent. And, (7)_____ the number of smokers keeps on (8)_____,by the second or third (9)_____ of the next century there could be 10 million deaths each year (10)_____ smoking related illnesses. Drugs are also a huge burden (11)_____ the world economy. In the United States, for example, it"s estimated that alcohol and illegal drug use costs the country tens of billions of dollars each year, mainly (12)_____ health care. When the cost of tobacco related illnesses is added, (13)_____ total more than doubles. Drugs are also closely (14)_____ crime. Many police forces no longer (15)_____ between illegal and legal drugs when fighting crime. In Australia, for example, experts (16)_____ that police in some parts of the country spend between 70 and 80 percent of their time dealing with alcohol-related incidents. One explanation for the increase in drug (17)_____ is simply that people have more money to spend. Tobacco and alcohol companies are now (18)_____ much more on developing countries to take (19)_____ of greater wealth there. And criminals involved in the illegal drug trade are following (20)_____, introducing drugs into countries where they were previously hardly use.(分数:40.00)A.whenB.with √C.asD.if解析:解析:本题是句型结构题。

1641操作手册

1641操作手册
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Safety information ................................................. 2 Safety rules for operation and maintenance .......... 3
Starting the engine .............................................. 19 Before starting ................................................... 19 Starting method EMS 2 ...................................... 20 Starting in extreme cold ..................................... 21 Never use start spray ......................................... 22 Starting with auxiliary batteries .......................... 22

欧司朗 EUP30T-1HMC-0 恒流调光驱动器(单线)说明书

欧司朗 EUP30T-1HMC-0 恒流调光驱动器(单线)说明书

EUP30T-1HMC-0(Product No.: 104100002101)SummaryProduct FeatureDimension(mm)EUP30T-1HMC-0 is a constant current output mode LED driver. The output current can be easily set via DIP switch.The driver supports leading edge (Triac) and trailing edge (ELV) dimmer, and can be compatible with the systems of various brands (Philips, Panasonic, Lutron, Simon, ABB,Siemens,Dalitek etc.) to achieve a smooth dimming effect.ELV220VAC-240VAC 50/60Hz82%@230VAC, Full load ≥0.9@230VAC, Full load Cold start, 15A(twidth=30us measured at 50% Ipeak@230VAC 0.17Amax@230VAC, Full load<20%@230VAC,full load 185*42.5*28.5mm(L*W*H)IP20-20℃~50℃-40℃~85℃, 20-90%RH 75℃PC 30,000h@tc:75℃50V Max ±5%<3%Triac>15,000 times1550mA/9-42VDC/23.1W 600mA/9-42VDC/25.2W 650mA/9-42VDC/27.3W 700mA/9-42VDC/29.4W750mA/9-40VDC/30W 800mA/9-38VDC/30.4W850mA/9-35VDC/29.75W 900mA/9-33VDC/29.7WEUP30T-1HMC-0TcLifetimeMaterialDimensionPacking Size IP Rating Working Temp.Storage Temp.; Humidity Dimming Mode Switch Cycle 3 years Warranty Condition No Load Output Voltage Turn On Delay Time<1s, at 230Vac Efficiency Current THD Inrush Current Current/Voltage/PowerRipple Current Channel Current Tolerance Voltage FrequencyPower Factor Over temperature Short Circuit Over Load Shut down the output, recovers automatically when temp. back to normal.When the output voltage is exceeded, decreases and, recovers automatically when the load is reduced.Shut down the output automatically recovers after faulty condition is removed.OthersFunction ModelOutputInputProtectionTechnical Parameters· Single channel output, output current level selectable by DIP S.W.· Support Leading edge (Triac) and Trailing edge (ELV) dimmer · Dimming range from 40VAC to 240VAC · Built-in active PFC function· Class 2 power supply. Full protective plastic housing · Dimming effect smooth, no flicker· Protections: Short circuit, over load, over temperature· Suitable for indoor LED lighting application, such as down light, spotlights, panel light, and so onNet weight: 150g±5%/PCS; 50PCS/Carton; 8kg±5%/Carton; Carton Size: 430*306*168mm(L*W*H)ApplicationDownlightPanel LightFlood LightSpotlightCeiling Light Track LightFloor LightDecorative LightWiring DiagramAmbient Temperature(℃)L o a d (%)20406080100120-20-101020304050600Dimming CurveDerating Curve※ The contents of this manual are updated without prior notice. If the function of the product you are using is inconsistent with the instructions, the function of the product shall prevail.Please contact us if you have any questions .PF vs Load0.860.880.900.920.940.960.981.00Load(%)P FCurrent Selection TableRemark: Function default setting is: 550mA (@switch are all OFF state)Cautions1.The product shall be installed and serviced by a qualified person.2.This product is non-waterproof. Please avoid the sun and rain. When installed outdoors please ensure it is mounted in a water proof enclosure.3.Good heat dissipation will prolong the working life of the controller. Please ensure good ventilation.4.Please check if the output voltage and current of any LED power supplies used comply with the requirement of the product.5.Please ensure that adequate sized cable is used from the controller to the LED lights to carry the current. Please also ensure that the cable is secured tightly in the connector.6.For safety consideration, PVC or rubber cord of 0.75-1.5mm2 is recommended for input and output terminal(s) . Flat power cord is not suitable. Ensure all wire connections and polarities are correct before applying power to avoid any damages to the LED lights.7.If a fault occurs please return the product to your supplier. Do not attempt to fix this product by yourself.20406080100120Input(%)O u t p u t (%)。

不同提取方法对井冈蜜柚皮精油组成与性质的影响

不同提取方法对井冈蜜柚皮精油组成与性质的影响

李欣,华建新,罗杰洪,等. 不同提取方法对井冈蜜柚皮精油组成与性质的影响[J]. 食品工业科技,2024,45(3):83−97. doi:10.13386/j.issn1002-0306.2023030289LI Xin, HUA Jianxin, LUO Jiehong, et al. Effects of Different Extraction Methods on the Composition and Properties of Jinggang Pomelo Peel Essential Oil[J]. Science and Technology of Food Industry, 2024, 45(3): 83−97. (in Chinese with English abstract). doi:10.13386/j.issn1002-0306.2023030289· 研究与探讨 ·不同提取方法对井冈蜜柚皮精油组成与性质的影响李 欣1,华建新1,罗杰洪1,王国庆2,陈 赣2,周爱梅1,*(1.华南农业大学食品学院,广东省功能食品活性重点实验室,广东广州 510642;2.吉安井冈农业生物科技有限公司,江西吉安 343016)摘 要:以井冈蜜柚皮精油(Jinggang pomelo peel essential oil ,JPPEO )为研究对象,采用水蒸气蒸馏法、低温连续相变法两种方法进行提取,以精油得率为主要指标,研究了萃取温度、压力、时间等因素对井冈蜜柚皮精油得率的影响,并通过正交法进行低温连续相变法提取工艺优化,同时对精油的理化性质及化学组成进行分析。

研究表明,低温连续相变提取井冈蜜柚皮精油(Low-temperature continuous phase transition extraction essential oil ,L-JPPEO )的最佳工艺为:颗粒度30目,萃取温度55 ℃,萃取压力0.6 MPa ,萃取时间60 min ,解析温度70 ℃,此时精油得率为10.99‰,比水蒸气蒸馏法提取的精油(Hydro distillation essential oil ,H-JPPEO )得率高出了2.88倍;理化性质实验结果表明,低温连续相变萃取的井冈蜜柚皮精油的不饱和脂肪酸含量较高,游离脂肪酸含量较低,酯类成分含量较低;傅里叶衰减全反射中红外光谱法(Fourier transform infrared spectroscopy ,FTIR )鉴定出L-JPPEO 和H-JPPEO 含萜烯类化合物、醇类、酚类、醛类以及含羰基化合物。

贝尔冰箱-冰箱大师 冰箱说明书

贝尔冰箱-冰箱大师 冰箱说明书
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Draka 高压电缆样本

Medium Voltage Cable RangeOvermany years Draka has established a deservedreputation in the UK as the most trusted and reliablemanufacturer in the Low Voltage cable sector .Thisreputation was earned through our constantcommitment to our brand values.We are capitalising on this vast experience andexpertise to extend the offering of the world’s mosttrusted cable brand into the UK medium voltagemarket,with products founded on the same coreprinciples –customer focus,safety,performanceand durability.Draka UK is introducing a medium voltage cablerange to provide the UK’s leading contractors anddistributors with the highest quality cables for theindustrial and utilities sectors.Our cable exceedsspecification requirements to ensure a lifeexpectancy in excess of industry standards.Whether it is utilised for power distribution;(from wind farms and nuclear power stationsthrough to substations),or in the industrial sector (in applications such as rail networks,airports and major construction developments),our state-of-the-art manufacturing techniques ensure the highest calibre cables and deliver unrivalled longevity and reliability.Added to the numerous industrial projects currently in progress throughout the UK,the energy network isTHE CABLE RANGE THA T DELIVERS DURABILITY AND TRUSTalso being constantly refurbished,upgraded and maintained to cope with the increased electrical consumption.This has in turn created an increased demand for high quality medium voltage cables that will stand the test of time.Draka has the technical capability to meet this demand.Not only for the excellence of our products but also for the technical guidance and support that we offer.For the utilities sector,the range includes11,22and 33kV rated versions with solid aluminium or stranded copper cores,in both singles and triplex,normally with polyethylene outer sheaths.In addition to these variants,a stranded aluminium version is available in singles.For the industrial sector,there are11,22and33kV versions with PVC or Zero Halogen,Low Smoke(OHLS)sheathing with strandedcopper or stranded aluminium conductors dependent on the application.Draka’s medium voltage product range has been developed with leading edge technology and is backed by the resources of one of the world’s major specialist cable companies.Draka Holding NV is an international cable manufacturer with a turnover of2billion Euros and9,000employees.Draka as an organisation is passionate aboutdeveloping world leading products which deliverexceptional value.Customer focus,quality andinnovation are at the heart of everything we do.Ourtechnical experts,research and development andstate-of-the-art manufacturing facility enables theproduction of the highest quality cabling systems.Potential RisksOne of the biggest threats to the effectiveperformance of medium voltage cables are defects inthe insulation system caused by gas voids orimpurities during the insulation of the cable.Theimpact of these defects is magnified with increasingvoltage as the electrical stresses increase and can leadto degradation of the insulation and in the end abreakdown of the cable.Given the vast volume ofmedium voltage cabling required in UK infrastructure,and the number of people,businesses and services thatare totally reliant on a continued supply of power ,anyfailings requiring replacement can be severe and bringmajor cost implications.Built to lastThrough the sophistication of the manufacturingtechniques involved,Draka medium voltage cablelimits the exposure to impurities during the compoundhandling process in production and as a result,it’sdurability is unrivalled.The range is produced at the Nässjöfactory in Sweden which since Draka acquired the site from ABB in 1999,has seen huge investment as part of a major refurbishment and extension programme.It now has the very latest plant and equipment which means it can be classed amongst the world’s most advanced Medium Voltage manufacturing factories.Already the leading medium voltage supplier to the Scandinavian utilities market,Draka has established a proven pedigree in the development of high quality products which are built to last.It is of course to ISO14001and ISO9001certified.BUIL T TO OUTPERFORM DECADE AFTER DECADE AFTERDECADE1Fundamental to the development of high quality,trusted medium voltage cable at Draka’s facility inSweden has been the introduction of R3technologyincluding clean rooms and closed systems formaterials handling –processes usually reserved forhigh voltage cable manufacture.Here,the crucialareas of the factory are contamination-controlled toeradicate the risk of environmental pollutants such asdust,airborne microbes,aerosol particles andchemical vapours from jeopardising the purity of thecable construction.CLEAN MANUFACTURIN Extruder platformDrum take up2Not only does the closed system ensure that thematerials used are not contaminated,those specifiedare all of the highest quality.The conductive cores areformed from copper or aluminium in a comprehensiverange of cross sections.Another major component is XLPE (cross-linkedpolyethylene)–a thermosetting material which is ableto perform in temperatures of up to 90°C withoutprematurely degrading.This contributes considerablyto the resilience of the product.NG.THE SECRETBEHIND220m in length with aCuring Line3In2007,Draka made a€6million investment to refurbish and extend the Nässjösite.The most significant development was the incorporation of a new peroxide cure CCV-Line for the insulation of our medium voltage cores.The line has doubled the capacity of the factory to meet the growing global demands for10-36kV medium voltage cable.4Fed from an extruder platform,the CCV-Line is 220m long with a vertical drop of20m.It features a 200mm diameter tube through which the cable is cross linked at high temperature and high pressure.5Quality control extends across all aspects of the manufacturing process and includes stringent testingTHE QUALITY ANDLONGE vertical drop of20mprocedures including X-rays during production toconfirm the structural integrity of the cable.Inaccordance with European and country specificstandards,Draka medium voltage cable iscontinuously put through long-term water immersiontests,followed by high voltage electrical breakdowntesting to ensure the cables will be fully reliablethroughout their expected operational life-span.All of the above is to ensure that Draka produces thehighest quality medium voltage cables.ER LIFE OF OURCABLEST aping machinemeasurement gaugeCaterpillarCapstanApplication fields1-core armoured power cable.StandardBS6622/BS7835Rated voltage6.35/11(12)kVImpulse voltage95kVFire propagation classBS EN 50266-2-4.T emperature rangeIn continuous operation max.conductor temp 90ºC.Lowest cable temperature during installation:-10ºC.Below 0ºC special precautions must be taken.Bending radiusAt laying:12x D.When installed:8x DD =Overall diameter of cableDesignConductorStranded,round and compacted copper acc.to IEC 60228class 2Conductor screenExtrudedInsulationXLPE,nominal thickness =3.4mmInsulation screenExtruded,bonded or strippableMetallic screenMetallic layer ,copper tapeInner sheathPVC or PE,blackArmourGalvanized aluminium wiresOuter sheathPVC or halogen free compound,red or black1CU-XLPE 11kV10Current rating*Installation conditionsGround temperature:15°CDepth of laying:0.65mGround resistivity:1.0m x°K/W Air temperature25°CTrefoil with screen grounded at both endsNominal values unless otherwise specified.11Application fields1-core armoured power cable.StandardBS6622/BS7835Rated voltage 12.7/22(24)kV Impulse voltage 144kVFire propagation class BS EN 50266-2-4.T emperature rangeIn continuous operation max.conductor temp 90ºC.Lowest cable temperature during installation:-10ºC.Below 0ºC special precautions must be taken.Bending radiusAt laying:12x D.When installed:8x D D =Overall diameter of cableDesignConductorStranded,round and compacted copper acc.to IEC 60228class 2Conductor screen ExtrudedInsulationXLPE,nominal thickness =5.5mm Insulation screenExtruded,bonded or strippable Metallic screenMetallic layer ,copper tape Inner sheath PVC or PE,blackArmourGalvanized aluminium wiresOuter sheathPVC or halogen free compound,red or blackCU-XLPE 22kVCurrent ratingInstallation conditionsGround temperature:15°CDepth of laying:0.65mGround resistivity:1.0m x°K/W Air temperature25°CTrefoil grounded at both ends.Nominal values unless otherwise specified.13Application fields1-core armoured power cable.StandardBS6622/BS7835Rated voltage 19/33(36)kV Impulse voltage 194kVFire propagation class BS EN 50266-2-4.T emperature rangeIn continuous operation max.conductor temp 90ºC.Lowest cable temperature during installation:-10ºC.Below 0ºC special precautions must be taken.Bending radiusAt laying:12x D.When installed:8x D D =Overall diameter of cableDesignConductorStranded,round and compacted copper acc.to IEC 60228class 2Conductor screen ExtrudedInsulationXLPE,nominal thickness =8.0mm Insulation screenExtruded,bonded or strippable Metallic screenMetallic layer ,copper tape Inner sheath PVC or PE,blackArmourGalvanized aluminium wiresOuter sheathPVC or halogen free compound,red or blackCU-XLPE 33kVCurrent rating*Installation conditionsGround temperature:15°CDepth of laying:0.65mGround resistivity:1.0m x°K/W Air temperature25°CTrefoil with screen grounded at both endsNominal values unless otherwise specified.15Application fields3-core armoured power cable.StandardBS6622/BS7835Rated voltage 6.35/11(12)kV Impulse voltage 95kVFire propagation class BS EN 50266-2-4.T emperature rangeIn continuous operation max.conductor temp 90ºC.Lowest cable temperature during installation:-10ºC.Below 0ºC special precautions must be taken.Bending radiusAt laying:12x D.When installed:8x D D =Overall diameter of cableDesignConductorStranded,round and compacted copper acc.to IEC 60228class 2Conductor screen ExtrudedInsulationXLPE,nominal thickness =3.4mm Insulation screenExtruded,bonded or strippable Core identificationcoloured phasetape under screenMetallic screenMetallic layer ,copper tape,over each individual core Filler PP yarn Inner sheath PVC or PE,black ArmourGalvanized steel wiresOuter sheathPVC or halogen free compound,red or blackCU-XLPE 11kVCurrent rating*Installation conditionsGround temperature:15°CDepth of laying:0.65mGround resistivity:1.0m x°K/W Air temperature25°CScreen grounded at both ends.Nominal values unless otherwise specified.17Application fields3-core armoured power cable.StandardBS6622/BS7835Rated voltage 12.7/22(24)kV Impulse voltage 144kVFire propagation class BS EN 50266-2-4.T emperature rangeIn continuous operation max.conductor temp 90ºC.Lowest cable temperature during installation:-10ºC.Below 0ºC special precautions must be taken.Bending radiusAt laying:12x D.When installed:8x D D =Overall diameter of cableDesignConductorStranded,round and compacted copper acc.to IEC 60228class 2Conductor screen ExtrudedInsulationXLPE,nominal thickness =5.5mm Insulation screenExtruded,bonded or strippableCore identificationcoloured phasetape under the copper tapeMetallic screenMetallic layer ,copper tape,over each individual core Filler PP yarn Inner sheath PVC or PE,black ArmourGalvanized steel wiresOuter sheathPVC or halogen free compound,red or blackCU-XLPE 22kVCurrent ratingInstallation conditionsGround temperature:15°CDepth of laying:0.65mGround resistivity:1.0m x°K/W Air temperature25°CScreen grounded at both ends.Nominal values unless otherwise specified.19Application fields3-core armoured power cable.StandardBS6622/BS7835Rated voltage 19/33(36)kV Impulse voltage 194kVFire propagation class BS EN 50266-2-4.T emperature rangeIn continuous operation max.conductor temp 90ºC.Lowest cable temperature during installation:-10ºC.Below 0ºC special precautions must be taken.Bending radiusAt laying:12x D.When installed:8x D D =Overall diameter of cableDesignConductorStranded,round and compacted copper acc.to IEC 60228class 2Conductor screen ExtrudedInsulationXLPE,nominal thickness =8.0mm Insulation screenExtruded,bonded or strippable Core identificationcoloured phasetape under screenMetallic screenMetallic layer ,copper tape,over each individual core Filler PP yarn Inner sheath PVC or PE,black ArmourGalvanized steel wiresOuter sheathPVC or halogen free compound,red or blackCU-XLPE 33kVCurrent rating*Installation conditionsGround temperature:15°CDepth of laying:0.65mGround resistivity:1.0m x°K/W Air temperature25°CScreen grounded at both ends.Nominal values unless otherwise specified.21Application fields1-core armoured power cable.StandardBS6622/BS7835Rated voltage 6.35/11(12)kV Impulse voltage 95kVFire propagation class BS EN 50266-2-4.T emperature rangeIn continuous operation max.conductor temp 90ºC.Lowest cable temperature during installation:-10ºC.Below 0ºC special precautions must be taken.Bending radiusAt laying:12x D.When installed:8x D D =Overall diameter of cableDesignConductorStranded,round and compacted aluminium acc.to IEC 60228class 2Conductor screen ExtrudedInsulationXLPE,nominal thickness =3.4mm Insulation screenExtruded,bonded or strippable Metallic screenMetallic layer ,copper tape Inner sheath PVC or PE,blackArmourGalvanized aluminium wiresOuter sheathPVC or halogen free compound,red or blackAL -XLPE 11kVCurrent rating*Installation conditionsGround temperature:15°CDepth of laying:0.65mGround resistivity:1.0m x°K/W Air temperature25°CTrefoil grounded at both ends.Nominal values unless otherwise specified.23Application fields1-core armoured power cable.StandardBS6622/BS7835Rated voltage 12.7/22(24)kV Impulse voltage 144kVFire propagation class BS EN 50266-2-4.T emperature rangeIn continuous operation max.conductor temp 90ºC.Lowest cable temperature during installation:-10ºC.Below 0ºC special precautions must be taken.Bending radiusAt laying:12x D.When installed:8x D D =Overall diameter of cableDesignConductorStranded,round and compacted aluminium acc.to IEC 60228class 2Conductor screen ExtrudedInsulationXLPE,nominal thickness =5.5mm Insulation screenExtruded,bonded or strippable Metallic screenMetallic layer ,copper tape Inner sheath PVC or PE,blackArmourGalvanized aluminium wiresOuter sheathPVC or halogen free compound,red or blackAL -XLPE 22kVCurrent ratingInstallation conditionsGround temperature:15°CDepth of laying:0.65mGround resistivity:1.0m x°K/W Air temperature25°CTrefoil grounded at both ends.Nominal values unless otherwise specified.25Application fields1-core armoured power cable.StandardBS6622/BS7835Rated voltage 19/33(36)kV Impulse voltage 194kVFire propagation class BS EN 50266-2-4.T emperature rangeIn continuous operation max.conductor temp 90ºC.Lowest cable temperature during installation:-10ºC.Below 0ºC special precautions must be taken.Bending radiusAt laying:12x D.When installed:8x D D =Overall diameter of cableDesignConductorStranded,round and compacted aluminium acc.to IEC 60228class 2Conductor screen ExtrudedInsulationXLPE,nominal thickness =8.0mm Insulation screenExtruded,bonded or strippable Metallic screenMetallic layer ,copper tape Inner sheath PVC or PE,blackArmourGalvanized aluminium wiresOuter sheathPVC or halogen free compound,red or blackAL -XLPE 33kVCurrent rating*Installation conditionsGround temperature:15°CDepth of laying:0.65mGround resistivity:1.0m x°K/W Air temperature25°CTrefoil grounded at both ends.Nominal values unless otherwise specified.27Application fields3-core armoured power cable.StandardBS6622/BS7835Rated voltage 6.35/11(12)kV Impulse voltage 95kVFire propagation class BS EN 50266-2-4.T emperature rangeIn continuous operation max.conductor temp 90ºC.Lowest cable temperature during installation:-10ºC.Below 0ºC special precautions must be taken.Bending radiusAt laying:12x D.When installed:8x D D =Overall diameter of cableDesignConductorStranded,round and compacted aluminium acc.to IEC 60228class 2Conductor screen ExtrudedInsulationXLPE,nominal thickness =3.4mm Insulation screenExtruded,bonded or strippable Core identificationcoloured phasetape under screenMetallic screenMetallic layer ,copper tape,over each individual core Filler PP yarn Inner sheath PVC or PE,black ArmourGalvanized steel wiresOuter sheathPVC or halogen free compound,red or blackAL -XLPE 11kVCurrent rating*Installation conditionsGround temperature:15°CDepth of laying:0.65mGround resistivity:1.0m x°K/W Air temperature25°CScreen grounded at both ends.Nominal values unless otherwise specified.29Application fields3-core armoured power cable.StandardBS6622/BS7835Rated voltage 12.7/22(24)kV Impulse voltage 144kVFire propagation class BS EN 50266-2-4.T emperature rangeIn continuous operation max.conductor temp 90ºC.Lowest cable temperature during installation:-10ºC.Below 0ºC special precautions must be taken.Bending radiusAt laying:12x D.When installed:8x D D =Overall diameter of cableDesignConductorStranded,round and compacted copper acc.to IEC 60228class 2Conductor screen ExtrudedInsulationXLPE,nominal thickness =5.5mm Insulation screenExtruded,bonded or strippableCore identificationcoloured phasetape under the copper tapeMetallic screenMetallic layer ,copper tape,over each individual core Filler PP yarn Inner sheath PVC or PE,black ArmourGalvanized steel wiresOuter sheathPVC or halogen free compound,red or blackAL -XLPE 22kVCurrent ratingInstallation conditionsGround temperature:15°CDepth of laying:0.65mGround resistivity:1.0m x°K/W Air temperature25°CScreen grounded at both ends.Nominal values unless otherwise specified.31Application fields3-core armoured power cable.StandardBS6622/BS7835Rated voltage 19/33(36)kV Impulse voltage 194kVFire propagation class BS EN 50266-2-4.T emperature rangeIn continuous operation max.conductor temp 90ºC.Lowest cable temperature during installation:-10ºC.Below 0ºC special precautions must be taken.Bending radiusAt laying:12x D.When installed:8x D D =Overall diameter of cableDesignConductorStranded,round and compacted aluminium acc.to IEC 60228class 2Conductor screen ExtrudedInsulationXLPE,nominal thickness =8.0mm Insulation screenExtruded,bonded or strippable Core identificationcoloured phasetape under screenMetallic screenMetallic layer ,copper tape,over each individual core Filler PP yarn Inner sheath PVC or PE,black ArmourGalvanized steel wiresOuter sheathPVC or halogen free compound,red or black3AL -XLPE 33kVCurrent rating*Installation conditionsGround temperature:15°CDepth of laying:0.65mGround resistivity:1.0m x°K/W Air temperature25°CScreen grounded at both ends.Nominal values unless otherwise specified.33Application fieldsSingle-core,distribution cable for outdoors use in 3-phase formation.Installation in pipes and ground/water .Standard BS 7870-4.10Rated voltage 6.35/11(12)kVFlame propagation classThe PE sheath is not flame-retardantT emperature rangeIn continuous operation max 90ºC.Lowest cable temperature during installation:-20ºC.Below 0ºC special precautions must be taken.Impulse voltage 95kVBending radiusAt fixed mounting:10x D.At laying:15x DDesignConductorStranded,round and compacted copper acc.to IEC 60228class 2Conductor screen ExtrudedInsulationXLPE,nom.thickness =3.4mm Insulation screen Extruded bonded Concentric conductor Annealed copper wires SheathMDPE,black1CU-XLPE -CWS-PE 11kV35Electrical data at +20°CCurrent rating*Current ratings conditions Ambient temperature air:25ºC Ground temperature:15ºC Depth of burial:0.7mThermal resistance of soil 1.0ºKm/WTrefoil with screen grounded at both ends Nominal values unless otherwise specified.Application fieldsSingle-core,distribution cable for outdoors use in 3-phase formation.Installation in pipes and ground/water .Standard BS 7870-4.10Rated voltage 12.7/22(24)kVFlame propagation classThe PE sheath is not flame-retardantT emperature rangeIn continuous operation max 90ºC.Lowest cable temperature during installation:-20ºC.Below 0ºC special precautions must be taken.Impulse voltage 144kVBending radiusAt fixed mounting:10x D.At laying:15x DDesignConductorStranded,round and compacted copper acc.to IEC 60228class 2Conductor screen ExtrudedInsulationXLPE,nom.thickness =5.5mm Insulation screen Extruded bonded Concentric conductor Annealed copper wires SheathMDPE,black1CU-XLPE -CWS-PE 22kV37Electrical data at +20°CCurrent rating*Current ratings conditions Ambient temperature air:25ºC Ground temperature:15ºC Depth of burial:0.7mThermal resistance of soil:1.0ºKm/W Trefoil with screen grounded at both ends Nominal values unless otherwise specified.Application fieldsSingle-core,distribution cable for outdoors use in 3-phase formation.Installation in pipes and ground/water .Standard BS 7870-1.10Rated voltage 19/33(36)kVFlame propagation classThe PE sheath is not flame-retardantT emperature rangeIn continuous operation max 90ºC.Lowest cable temperature during installation:-10ºC.Below 0ºC special precautions must be taken.Impulse voltage 194kVBending radiusAt fixed mounting:10x D.At laying:15x DDesignConductorStranded,round and compacted copper acc.to IEC 60228class 2Conductor screen ExtrudedInsulationXLPE,nom.thickness =8.0mm Insulation screen Extruded bonded Concentric conductor Annealed copper wires SheathMDPE,black1CU-XLPE -CWS-PE 33kV39Electrical data at +20°CCurrent rating*Current ratings conditions Ambient temperature air:25ºC Ground temperature:15ºC Depth of burial:0.7mThermal resistance of soil:1.0ºKm/W Trefoil with screen grounded at both ends Nominal values unless otherwise specified.Application fields3-core cable.distribution cable for outdoors use.Installation in pipes and ground.Standard BS 7870-4.10Rated voltage 6.35/11(12)kVFire propagation classThe PE sheath is not flame-retardantT emperature rangeIn continuous operation max.conductor temp 90ºC.Lowest cable temperature during laying -20ºC.Below 0ºC special precautions must be taken.Impulse voltage 95kVBending radiusAt fixed mounting:10x D.At laying:15x DDesignConductorStranded,round copper acc.to IEC 60228class 22Conductor screen ExtrudedInsulationXLPE,nom.thickness =3.4mm Insulation screen Extruded bonded Concentric conductor Annealed copper wires SheathMDPE,blackLaying upThree stranded single-core cables in triplex formation3CU-XLPE-CWS-PE TRIPLEX 11kV41Electrical data at +20°CCurrent rating*Current ratings conditionsAmbient temperature air:25ºC Ground temperature:15ºC Depth of burial:0.7mThermal resistance of soil:1.0ºKm/W Screen grounded at both ends.Nominal values unless otherwise specified.Application fields3-core cable.distribution cable for outdoors use.Installation in pipes and ground.Standard BS 7870-4.10Rated voltage 12.7/22(24)kVFire propagation classThe PE sheath is not flame-retardantT emperature rangeIn continuous operation max.conductor temp 90ºC.Lowest cable temperature during laying -20ºC.Below 0ºC special precautions must be taken.Impulse voltage 144kVBending radiusAt fixed mounting:10x D.At laying:15x DDesignConductorStranded,round copper acc.to IEC 60228class 2Conductor screen ExtrudedInsulationXLPE,nom.thickness =5.5mm Insulation screen Extruded bonded Concentric conductor Annealed copper wires SheathMDPE,blackLaying upThree stranded single-core cables in triplex formation3CU-XLPE-CWS-PE TRIPLEX 22kV43Electrical data at +20°CCurrent rating*Current ratings conditionsAmbient temperature air:25ºC Ground temperature:15ºC Depth of burial:0.7mThermal resistance of soil:1.0ºKm/W Screen grounded at both ends.Nominal values unless otherwise specified.Application fields3-core cable.distribution cable for outdoors use.Installation in pipes and ground.Standard BS 7870-4.10Rated voltage 19/33(36)kVFire propagation classThe PE sheath is not flame-retardantT emperature rangeIn continuous operation max.conductor temp 90ºC.Lowest cable temperature during laying -20ºC.Below 0ºC special precautions must be taken.Impulse voltage 194kVBending radiusAt fixed mounting:10x D.At laying:15x DDesignConductorStranded,round copper acc.to IEC 60228class 2Conductor screen ExtrudedInsulationXLPE,nom.thickness =8.0mm Insulation screen Extruded bonded Concentric conductor Annealed copper wires SheathMDPE,blackLaying upThree stranded single-core cables in triplex formation3CU-XLPE-CWS-PE TRIPLEX 33kV45Electrical data at +20°CCurrent rating*Current ratings conditionsAmbient temperature air:25ºC Ground temperature:15ºC Depth of burial:0.7mThermal resistance of soil:1.0ºKm/W Screen grounded at both ends.Nominal values unless otherwise specified.Application fieldsSingle-core,distribution cable for outdoors use in 3-phase formation.Installation in pipes and ground/water .Standard BS 7870-4.10Rated voltage 6.35/11(12)kVFlame propagation classThe PE sheath is not flame-retardantT emperature rangeIn continuous operation max 90ºC.Lowest cable temperature during installation:-20ºC.Below 0ºC special precautions must be taken.Impulse voltage 95kVBending radiusAt fixed mounting:10x D.At laying:15x DDesignConductorStranded,round and compacted aluminium acc.to IEC 60228class 2Conductor screen ExtrudedInsulationXLPE,nom.thickness =3.4mm Insulation screen Extruded bonded Concentric conductor Annealed copper wires SheathMDPE,black1AL -XLPE -CWS-PE 11kV。

Truma Ignis 2000产品说明书

APPENDIX A – Error CodesIf the appliance malfunctions, LED 2 (refer to “Overview / Designation of parts” on page 2) will flash to indicate the malfunction. There are short and long intervals of flashing. The flashing will repeat every 3 seconds.1. Note the flashing intervals and check the list below.2. Reset the appliance:–Switch off the appliance. / – Wait 5 seconds / –Switch the appliance on again.3. If an error code is still displayed, contact an authorized Truma service center.Error code Flash codes =short = 0l = long = 1Error Description1s,s,s,s,s,s,s,l Flame not detected There is a flame-detection error at the burner because the flame was not de-tected after release of gas and ignition.Important: The system indicates this error only after three attempts at intervalsof approximately 30 seconds.2s,s,s,s,s,s,l,s Error at over temperatureswitches (EOS, BOS)The exhaust over temperature switch (EOS) or burner over temperature switch (BOS) is open/unplugged.3s,s,s,s,s,s,l,l Error at exhaust pressureswitch (EPS)The EPS did not close when the flue fan was actuated because the fan did not push enough air through the exhaust channel. A cause could be, e.g., blocking of the exhaust channel or a faulty switch.ORThe EPS is closed even though the flue fan is not running. Cause is a defective EPS or flue fan.4s,s,s,s,s,l,s,s Error at water over tem-perature switch (WOS)The WOS opened at a water temperature of over 185 °F (85 °C).5s,s,s,s,s,l,s,l Flame detected at incor-rect time There is an error in flame detection of the burner because the flame was detected – before ignition or– before the release of gas or– after the gas was switched off.6s,s,s,s,s,l,l,s Error in the safety circuitfor gas valve There is a heating request but gas cannot be released.One of the switches WOS, EOS, BOS, EPS is open/unplugged.7s,s,s,s,s,l,l,l Error of burner MCUinternal RAM Error detected in the burner MCU’s internal safety monitoring feature (safety variables are no longer correct or RAM/STACK was overwritten by mistake).9s,s,s,s,l,s,s,l Malfunction of wateroutlet temperature sensorWOT Water outlet temperature sensor WOT – has a short circuit or– is open/unplugged.10s,s,s,s,l,s,l,s Error in the safety circuit There is a heating request but gas is not released because a valve-actuationsignal was not activated.11s,s,s,s,l,s,l,l Error of MCU watchdoggas release There is a heating request but the MCU watchdog does not release the gas path.12s,s,s,s,l,l,s,s Internal error13s,s,s,s,l,l,s,l Short circuit shut-off valve Short circuit detection in the gas valve (shut-off part) detected a current> 1000 mA and shut off.16s,s,s,l,s,s,s,s Malfunction of the MCU Internal error of the control unit.20s,s,s,l,s,l,s,s Malfunction of water inlettemperature sensor WIT Water inlet temperature sensor WIT– has a short circuit or– is open/unplugged or– the temperature of the sensor is colder than 14 °F (-10 °C).21s,s,s,l,s,l,s,l Malfunction of circulationline temperature sensorWCT Circulation line temperature sensor WCT– has a short circuit or– is open/unplugged or– the temperature of the sensor is colder than 14 °F (-10 °C).22s,s,s,l,s,l,l,s Malfunction of gas valve,modulation section Error at gas valve, modulation level, because - the modulator has a short circuit or- is open/unplugged.23s,s,s,l,s,l,l,l Voltage is too high The main power supply’s voltage detector measured a voltage level of >16.4 V. 24s,s,s,l,l,s,s,s Voltage is too low The main power supply’s voltage detector measured a voltage level of <10 V.25s,s,s,l,l,s,s,l Flue fan current con-sumption error The current detector for the flue fan has measured a current outside the permit-ted limits.26s,s,s,l,l,s,l,s Circulation pump currentconsumption error The current detector at the circulation pump has measured a current outside the permitted limits.27s,s,s,l,l,s,l,l Water circulation pump isrunning dry.The circulation pump does not generate water flow. The water system may not be filled or not sufficiently vented.The circulation pump tries (20 times) to generate a water flow every 30 s (if successful, the error is reset).28s,s,s,l,l,l,s,s Too low gas pressure.Gas supply (in vehicle) to the appliance insufficient.29s,s,s,l,l,l,s,l Too high heat powerrequired.You are trying to use more hot water than the appliance can supply.30s,s,s,l,l,l,l,s Risk of freezing.Temperature in the appliance below 27 °F (3 °C).31s,s,s,l,l,l,l,l Decalcification finished.–32s,s,l,s,s,s,s Current too low.Current in the antifreeze kit too low (e.g. cable break).33s,s,l,s,s,s,s,l Current too high.Current in the antifreeze kit too high (e.g. short circuit).37。

谷轮ZW系列(中间补气涡旋)压缩机应用指南

AE4-1381May 2011ZW21 to ZW61KAE and ZW30 to ZW61KSECopeland Scroll® Water Heating CompressorsTABLE OF CONTENTSSection Page Section PageIntroduction (2)ZW**KA Application (2)ZW**KS ApplicationVapour Injection - Theory of Operation (2)Heat Exchanger and Expansion Device Sizing (3)Flash Tank Application (3)Intermediate Pressure and Vapour Injection Superheat (3)Application ConsiderationsHigh Pressure Cut-Out (4)Low Pressure Cut-Out (4)Discharge Temperature Protection (4)Discharge Temperature Control (4)Discharge Mufflers (4)Oil Dilution and Compressor Cooling (4)Electrical Considerations (5)Brazing and Vapour Injection Line (5)Low Ambient Cut-Out (5)Internal Pressure Relief Valve (5)Internal Temperature Protection (5)Quiet Shutdown (5)Discharge Check Valve (5)Motor Protector (5)Accumulators (5)Screens (6)Crankcase Heat-Single Phase (6)Crankcase Heat-Three Phase (6)Pump Down Cycle (6)Minimum Run Time (6)Reversing Valves (6)Oil Type (7)System Noise & Vibration (7)Single Phase Starting Characteristics (7)PTC Start Components (7)Electrical Connections (7)Deep Vacuum Operation (7)Shell Temperature (7)Suction & Discharge Fittings (7)Three Phase Scroll Compressors (8)Brief Power Interruptions ..........................................8Assembly Line ProceduresInstalling the Compressor (8)Assembly Line Brazing Procedure (8)Pressure Testing (8)Assembly Line System Charging Procedure (8)High Potential (AC Hipot) Testing (9)Unbrazing System Components (9)Service ProceduresCopeland Scroll Functional Check (9)Compressor Replacement After Motor Burn (10)Start Up of a New or Replacement Compressor (10)FiguresBrief Product Overview (11)ZW21KAE Envelope (R-134a) (11)ZWKAE Envelope (R-407C, Dew Point) (12)ZWKA Envelope (R-22) (12)ZWKS Envelope (R-22) (13)ZWKSE Envelope (R-407C, Dew Point) (13)Heat Pump with Vapour Injection – EXV Control (14)Heat Exchanger Schematic (14)Heat Pump with Flash Tank (15)Possible Flash Tank Configuration (15)Oil Dilution Chart (16)Crankcase Heater (17)Compressor Electrical Connection (17)Scroll Tube Brazing (17)How a Scroll Works (18)IntroductionThe ZW**KA and ZW**KS Copeland Scroll®compressors are designed for use in vapour compression heat pump water heating applications. Typical model numbers include ZW30KA-PFS and ZW61KSE-TFP. This bulletin addresses the specifics of water heating in the early part and deals with the common characteristics and general application guidelines for Copeland Scroll compressors in the later sections. Operating principles of the scroll compressor are described in Figure 15 at the end of this bulletin.As the drive for energy efficiency intensifies, water heating by fossil-fueled boilers and electric elements is being displaced by vapour compression heat pumps. Emerson Climate Technologies has developed two lines of special water heater compressors to meet the requirements of this demanding application. ZW**KA compressors are designed for lighter duty applications where the ambient temperature does not fall below 0°C and where lower water temperatures can be accepted as the ambient temperature falls. ZW**KS compressors are equipped with a vapour injection cycle which allows reliable operation in cold climates with significantly enhanced heating capacity, higher efficiency, and minimal requirement to reduce water outlet temperatures. Figure 1gives a brief product overview.Water heating is characterized by long operating hours at both high load and high compression ratios. Demand for hot water is at its highest when ambients are low and when conventional heat pump capacity falls off. On the positive side, the system refrigerant charge is usually small, so the risk to the compressor from dilution and flooded starts will usually be lower than in split type air-to-air heat pumps.Water heaters must operate in a wide range of ambient temperatures, and many systems will require some method of defrost. Some systems such as Direct Heating, Top Down Heating or Single Pass Heating operate at a constant water outlet temperature with variable water flow. Others such as Recirculation Heating, Cyclic Heating or Multipass Heating use constant water flow with the water outlet and inlet temperatures both rising slowly as the storage tank heats up. Both system types need to cope with reheating a tank where the hot water has been partially used, and reheating to the setpoint temperature is required. More complex systems deliver water at relatively low temperatures for under-floor heating circuits and are switched over to sanitary water heating a few times per day to provide higher temperature water for sanitary use. In addition, some countries have specific water temperature requirements for legionella control.ZW**KA ApplicationThe application envelopes for ZW**KA compressors are shown in Figures 2 - 4.Appropriate system hardware and control logic must be employed to ensure that the compressor is always operating within the envelope. Small short-term excursions outside the envelope are acceptable at the time of defrost when the load on the compressor is low. Operation with suction superheat of 5 -10K is generally acceptable except at an evaporating tem-perature above 100C when a minimum superheat of 10K is required.ZW**KS ApplicationThe ZW**KS* vapour-injected scroll compressors differ from ZW**KA models in many important details:• Addition of vapour injection• Significantly different application envelopes• Some differences in locked rotor amps (LRA), maximum continuous current (MCC), andmaximum operating current (MOC) – seenameplatesThe application envelopes for ZW**KS compressors are shown in Figures 5 and 6.Vapour Injection – Theory of Operation Operation with vapour injection increases the capacity of the outdoor coil and in turn the capacity and efficiency of the system – especially in low ambient temperatures. A typical schematic is shown in Figure 7. A heat exchanger is added to the liquid line and is used to cool the liquid being delivered to the heating expansion device. Part of the liquid refrigerant flow is flashed through an expansion valve on the evaporator side of the heat exchanger at an intermediate pressure and used to subcool the main flow of liquid to the main expansion device. Vapour from the liquid evaporating at intermediate pressure is fed to the vapour injection port on the ZW**KS compressor. This refrigerant is injected into the mid-compression cycle of the scroll compressor and compressed to discharge pressure. Heating capacity is increased, because low temperature liquid with lower specific enthalpy supplied to the outdoor coil increases the amount of heat that can be absorbed from the ambient air. Increased heat absorbed from the ambient increases the system condensing temperature and in turn the compressor power input. The increase in power inputalso contributes to the improvement in the overall heating capacity.Vapour Injection can be turned on and off by the addition of an optional solenoid valve on the vapour injection line on systems using a thermostatic expansion valve. Alternatively, an electronic expansion valve can be used to turn vapour injection on and off and to control the vapour injection superheat. A capillary tube is not suitable for controlling vapour injection.The major advantage of the electronic expansion valve is that it can be used to optimise the performance of the system and at the same time control the discharge temperature by injecting “wet vapour” at extreme operating conditions.The configurations and schematics shown are for reference only and are not applicable to every system. Please consult with your Emerson Application Engineer.Heat Exchanger and Expansion Device Sizing Various heat exchanger designs have been used successfully as subcoolers. In general they should be sized so that the liquid outlet temperature is less than 5K above the saturated injection temperature at the customer low temperature rating point. At very high ambient temperatures, it will normally be beneficial to turn vapour injection off to limit the load on the compressor motor. Application Engineering Bulletin AE4-1327 and Emerson Climate Technologies Product Selection Software can be used to help size the subcooling heat exchanger and thermal expansion valves, but selection and proper operation must be checked during development testing. Plate type subcoolers must be installed vertically with the injection expansion device connected at the bottom through a straight tube at least 150mm long to ensure good liquid distribution. See the schematic in Figure 8. Flash Tank ApplicationA possible flash tank configuration is shown in Figure9. This particular configuration is arranged to have flow through the flash tank and expansion devices in heating, and it bypasses the tank in defrost mode. The flash tank system works by taking liquid from the condenser and metering it into a vessel through a high-to-medium pressure expansion device. Part of the liquid boils off and is directed to the compressor vapour injection port. This refrigerant is injected into the mid-compression cycle of the scroll compressor and compressed to discharge pressure. The remaining liquid is cooled, exits from the bottom of the tank at intermediate pressure, and flows to the medium-to-low pressure expansion device which feeds the outdoor coil. Low temperature liquid with lower specific enthalpy increases the capacity of the evaporator without increasing mass flow and system pressure drops.Recommended tank sizing for single compressor application in this size range is a minimum of 200 mm high by 75 mm in diameter with 3/8 in. (9.5mm) tubing connections, although it is possible to use a larger tank to combine the liquid/vapour separation and receiver functions in one vessel. A sight tube (liquid level gauge) should be added to the tank for observation of liquid levels during lab testing. See schematic diagram Figure 10 for clarification.It is important to maintain a visible liquid refrigerant level in the tank under all operating conditions. Ideally the liquid level should be maintained in the 1/3 to 2/3 full range.Under no circumstances should the level drop to empty or rise to a full tank. As the tank level rises, liquid droplets tend to be swept into the vapour line leading to “wet” vapour injection. Although this can be useful for cooling a hot compressor, the liquid quantity cannot be easily controlled. Compressor damage is possible if the tank overflows. If liquid injection is required for any reason, it can be arranged as shown in Figures 7 and 9.Since liquid leaves the tank in a saturated state, any pressure drop or temperature rise in the line to the medium-to-low pressure expansion device will lead to bubble formation. Design or selection of the medium-to-low pressure expansion device requires careful attention due to the possible presence of bubbles at the inlet and the low pressure difference available to drive the liquid into the evaporator. An electronic expansion valve is the preferred choice. Intermediate Pressure and Vapour Injection SuperheatPressure in the flash tank cannot be set and is a complex function of the compressor inlet condition and liquid condition at the inlet of the high-to-medium pressure expansion device. However, liquid level can be adjusted, which in turn will vary the amount of liquid subcooling in the condenser (water to refrigerant heat exchanger) and vary the injection pressure. Systems with low condenser subcooling will derive the biggest gains by the addition of vapour injection. Systems operating with high pressure ratios will show the largest gains when vapour injection is applied. Such systems will have higher vapour pressure and higher injectionmass flow. Intermediate pressures in flash tank and heat exchanger systems should be very similar unless the subcooling heat exchanger is undersized and there is a large temperature difference between the evaporator and the liquid sides. Vapour exiting a flash tank will be saturated and may pick up 1 - 2K superheat in the vapour line to the compressor. Vapour injection superheat cannot be adjusted on flash tank systems. Heat exchanger systems will be at their most efficient when the vapour injection superheat is maintained at approximately 5K.APPLICATION CONSIDERATIONSHigh Pressure Cut OutIf a high pressure control is used with these compressors, the recommended maximum cut out settings are listed in Figure 1. The high pressure control should have a manual reset feature for the highest level of system protection. It is not recommended to use the compressor to test the high pressure switch function during the assembly line test.Although R-407C runs with higher discharge pressure than R-22, a common setting can be used. The cutout settings for R-134a are much lower, and the switches must be selected or adjusted accordingly.Low Pressure Cut OutA low pressure cut out is an effective protection against loss of charge or partial blockage in the system. The cut out should not be set more than 3 - 5K equivalent suction pressure below the lowest operating point in the application envelope. Nuisance trips during defrost can be avoided by ignoring the switch until defrost is finished or by locating it in the line between the evaporator outlet and the reversing valve. This line will be at discharge pressure during defrost. Recommended settings are given in Figure 1. Discharge Temperature ProtectionAlthough ZW compressors have an internal bi-metal Therm-O-Disc®(TOD) on the muffler plate, external discharge temperature protection is recommended for a higher level of protection and to enable monitoring and control of vapour injection on ZW**KS* models. The protection system should shut down the compressor when the discharge line temperature reaches 125°C. In low ambient operation, the temperature difference between the scroll center and the discharge line is significantly increased, so protection at a lower discharge temperature, e.g. 120°C when the ambient is below 0°C, will enhance system safety. For the highest level of system protection, the discharge temperature control should have a manual reset feature. The discharge sensor needs to be well insulated to ensure that the line temperature is accurately read. The insulation material must not deteriorate over the expected life of the unit.Discharge Temperature ControlSome systems use an electronic expansion valve to control the vapour injection superheat and a thermistor to monitor the discharge temperature. This combination allows the system designer to inject a small quantity of liquid to keep the discharge temperature within safe limits and avoid an unnecessary trip. Liquid injection should begin at approximately 115°C and should be discontinued when the temperature falls to 105°C. Correct functioning of this system should be verified during system development. It is far preferable to use liquid injection into the vapour injection port to keep the compressor cool rather than inject liquid into the compressor suction which runs the risk of diluting the oil and washing the oil from the moving parts. If some operation mode requires liquid injection but without the added capacity associated with “wet” vapour injection, a liquid injection bypass circuit can be arranged as shown in Figures 7 and 9.Caution: Although the discharge and oil temperature are within acceptable limits, the suction and discharge pressures cannot be ignored and must also fall within the approved application envelope.Discharge MufflersDischarge mufflers are not normally required in water heaters since the refrigerant does not circulate within the occupied space.Oil Dilution and Compressor CoolingThe oil temperature diagram shown in Figure 11is commonly used to make a judgment about acceptable levels of floodback in heat pump operation. Systems operating with oil temperatures near the lower limit line are never at their most efficient. Low ambient heating capacity and efficiency will both be higher if floodback is eliminated and the system runs with 1 - 5K suction superheat. Discharge temperature can be controlled by vapour injection, “wet” vapour injection, or even liquid injection if necessary. In this situation, the oil temperature will rise well into the safe zone, and the compressor will not be at risk of failure from diluted oil. The oil circulation rate will also be reduced as crankcase foaming disappears. Special care needs to be taken at the end of defrost to ensure that the compressor oil is not unacceptably diluted. The system will resume heating very quickly and bearing loads willincrease accordingly, so proper lubrication must be ensured.Electrical ConsiderationsMotor configuration and protection are similar to those of standard Copeland Scroll compressors. In some cases, a larger motor is required in the ZW**KS* models to handle the load imposed by operating with vapour injection. Wiring and fuse sizes should be reviewed accordingly.Brazing the Vapour Injection LineThe vapour injection connection is made from copper coated steel, and the techniques used for brazing the suction and discharge fittings apply to this fitting also. Low Ambient Cut-OutA low ambient cut-out is not required to limit heat pump operation with ZW**KS compressors. Water heaters using ZW**KA compressors must not be allowed to run in low ambients since this configuration would run outside of the approved operating envelope causing overheating or excessive wear. A low ambient cut-out should be set at 0°C for ZW**KA modelsIn common with many Copeland Scroll compressors, ZW models include the features described below: Internal Pressure Relief (IPR) ValveAll ZW compressors contain an internal pressure relief valve that is located between the high side and the low side of the compressor. It is designed to open when the discharge-to-suction differential pressure exceeds 26 - 32 bar. When the valve opens, hot discharge gas is routed back into the area of the motor protector to cause a trip.Internal Temperature ProtectionThe Therm-O-Disc® or TOD is a temperature-sensitive snap disc device located on the muffler plate between the high and low pressure sides of the compressor. It is designed to open and route excessively hot discharge gas back to the motor protector. During a situation such as loss of charge, the compressor will be protected for some time while it trips the protector. However, as refrigerant leaks out, the mass flow and the amperage draw are reduced and the scrolls will start to overheat.A low pressure control is recommended for loss of charge protection in heat pumps for the highest level of system protection. A cut out setting no lower than 2.5 bar for ZW**KA* models and 0.5 bar for ZW**KS* models is recommended. The low pressure cut-out, if installed in the suction line to the compressor, can provide additional protection against an expansion device failed in the closed position, a closed liquid line or suction line service valve, or a blocked liquid line screen, filter, orifice, or TXV. All of these can starve the compressor for refrigerant and result in compressor failure. The low pressure cut-out should have a manual reset feature for the highest level of system protection. If a compressor is allowed to cycle after a fault is detected, there is a high probability that the compressor will be damaged and the system contaminated with debris from the failed compressor and decomposed oil.If current monitoring to the compressor is available, the system controller can take advantage of the compressor TOD and internal protector operation. The controller can lock out the compressor if current draw is not coincident with the contactor energizing, implying that the compressor has shut off on its internal protector. This will prevent unnecessary compressor cycling on a fault condition until corrective action can be taken.Quiet Shut downAll scrolls in this size range have a fast acting valve in the center of the fixed scroll which provides a very quiet shutdown solution. Pressure will equalize internally very rapidly and a time delay is not required for any of the ZW compressors to restart. Also refer to the section on “Brief Power Interruption”. Discharge Check ValveA low mass, disc-type check valve in the discharge fitting of the compressor prevents the high side, high pressure discharge gas from flowing rapidly back through the compressor. This check valve was not designed to be used with recycling pump down because it is not entirely leak-proof.Motor ProtectorConventional internal line break motor protection is provided. The protector opens the common connection of a single-phase motor and the center of the Y connection on three-phase motors. The three-phase protector provides primary single-phase protection. Both types of protectors react to current and motor winding temperature.AccumulatorsThe use of accumulators is very dependent on the application. The scroll’s inherent ability to handle liquid refrigerant during occasional operating flood back situations often makes the use of an accumulator unnecessary in many designs. If flood back is excessive, it can dilute the oil to such an extent thatbearings are inadequately lubricated, and wear will occur. In such a case, an accumulator must be used to reduce flood back to a safe level that the compressor can handle.In water heaters, floodback is likely to occur when the outdoor coil frosts. The defrost test must be done at an outdoor ambient temperature of around 0°C in a high humidity environment. Liquid floodback must be monitored during reversing valve operation, especially when coming out of defrost. Excessive floodback occurs when the sump temperature drops below the safe operation line shown in Figure 11 for more than 10 seconds.If an accumulator is required, the oil return orifice should be 1 - 1.5mm in diameter depending on compressor size and compressor flood back results. Final oil return hole size should be determined through testing. ScreensScreens with a mesh size finer than 30 x 30 (0.6mm openings) should not be used anywhere in the system with these compressors. Field experience has shown that finer mesh screens used to protect thermal expansion valves, capillary tubes, or accumulators can become temporarily or permanently plugged with normal system debris and block the flow of either oil or refrigerant to the compressor. Such blockage can result in compressor failure.Crankcase Heater - Single PhaseCrankcase heaters are not required on single phase compressors when the system charge is not over 120% of the limit shown in Figure 1. A crankcase heater is required for systems containing more than 120% of the compressor refrigerant charge limit listed in Figure 1. This includes long line length systems where the extra charge will increase the standard factory charge above the 120% limit.Experience has shown that compressors may fill with liquid refrigerant under certain circumstances and system configurations, notably after longer off cycles when the compressor has cooled. This may cause excessive start-up clearing noise, or the compressor may lock up and trip on the protector several times before starting. The addition of a crankcase heater will reduce customer noise and light dimming complaints since the compressor will no longer have to clear out liquid during startup. Figure 12lists the crankcase heaters recommended for the various models and voltages.Crankcase Heat – Three-PhaseA crankcase heater is required for three-phase compressors when the system charge exceeds the compressor charge limit listed in Figure 1and an accumulator cannot be piped to provide free liquid drainage during the off cycle.Pump Down CycleA pump down cycle for control of refrigerant migration is not recommended for scroll compressors of this size. If a pump down cycle is used, a separate external check valve must be added.The scroll discharge check valve is designed to stop extended reverse rotation and prevent high-pressure gas from leaking rapidly into the low side after shut off. The check valve will in some cases leak more than reciprocating compressor discharge reeds, normally used with pump down, causing the scroll compressor to cycle more frequently. Repeated short-cycling of this nature can result in a low oil situation and consequent damage to the compressor. The low-pressure control differential has to be reviewed since a relatively large volume of gas will re-expand from the high side of the compressor into the low side on shut down. Minimum Run TimeThere is no set answer to how often scroll compressors can be started and stopped in an hour, since it is highly dependent on system configuration. Other than the considerations in the section on Brief Power Interruptions, there is no minimum off time. This is because scroll compressors start unloaded, even if the system has unbalanced pressures. The most critical consideration is the minimum run time required to return oil to the compressor after startup.Since water heaters are generally of compact construction, oil return and short cycling issues are rare. Oil return should not be a problem unless the accumulator oil hole is blocked.Reversing ValvesSince Copeland Scroll compressors have very high volumetric efficiency, their displacements are lower than those of comparable capacity reciprocating compressors. As a result, Emerson recommends that the capacity rating on reversing valves be no more than 2 times the nominal capacity of the compressor with which it will be used in order to ensure proper operation of the reversing valve under all operating conditions.The reversing valve solenoid should be wired so that the valve does not reverse when the system isshut off by the operating thermostat in the heating or cooling mode. If the valve is allowed to reverse at system shutoff, suction and discharge pressures are reversed to the compressor. This results in pressures equalizing through the compressor which can cause the compressor to slowly rotate until the pressures equalize. This condition does not affect compressor durability but can cause unexpected sound after the compressor is turned off.Oil TypeThe ZW**K* compressors are originally charged with mineral oil. A standard 3GS oil may be used if the addition of oil in the field is required. See the compressor nameplate for original oil charge. A complete recharge should be ~100 ml less than the nameplate value.ZW**K*E are charged with POE oil. Copeland 3MAF or Ultra 22 CC should be used if additional oil is needed in the field. Mobil Arctic EAL22CC, Emkarate RL22, Emkarate 32CF and Emkarate 3MAF are acceptable alternatives. POE oil is highly hygroscopic, and the oil should not be exposed to the atmosphere except for the very short period required to make the brazing connections to the compressor.System Noise and VibrationCopeland Scroll compressors inherently have low sound and vibration characteristics, but the characteristics differ in some respects from those of reciprocating or rotary compressors. The scroll compressor makes both a rocking and a torsional motion, and enough flexibility must be provided to prevent vibration transmission into any lines attached to the unit. This is usually achieved by having tubing runs at least 30cm long parallel to the compressor crankshaft and close to the shell. ZW compressors are delivered with rubber grommets to reduce vibration transmission to the system baseplate.Single Phase Starting CharacteristicsStart assist devices are usually not required, even if a system utilizes non-bleed expansion valves. Due to the inherent design of the Copeland Scroll, the internal compression components always start unloaded even if system pressures are not balanced. In addition, since internal compressor pressures are always balanced at startup, low voltage starting characteristics are excellent for Copeland Scroll compressors. Starting current on any compressor may result in a significant “sag” in voltage where a poor power supply is encountered. The low starting voltage reduces the starting torque of the compressor and subsequently increases the start time. This could cause light dimming or a buzzing noise where wire is pulled through conduit. If required, a start capacitor and potential relay can be added to the electrical circuit. This will substantially reduce start time and consequently the magnitude and duration of both light dimming and conduit buzzing.PTC Start ComponentsFor less severe voltage drops or as a start boost, solid state Positive Temperature Coefficient devices rated from 10 to 25 ohms may be used to facilitate starting for any of these compressors.Electrical ConnectionThe orientation of the electrical connections on the Copeland Scroll compressors is shown in Figure 13 and is also shown on the wiring diagram on the top of the terminal box cover.Deep Vacuum OperationScrolls incorporate internal low vacuum protection and will stop pumping (unload) when the pressure ratio exceeds approximately 10:1. There is an audible increase in sound when the scrolls start unloading. This feature does not prevent overheating and destruction of the scrolls, but it does protect the power terminals from internal arcing.Copeland Scroll compressors(as with any refrigerant compressor) should never be used to evacuate a refrigeration or air conditioning system. The scroll compressor can be used to pump down refrigerant in a unit as long as the pressures remain within the operating envelope. Prolonged operation at low suction pressures will result in overheating of the scrolls and permanent damage to the scroll tips, drive bearings and internal seal. (See AE24-1105 for proper system evacuation procedures.)Shell TemperatureCertain types of system failures, such as condenser or evaporator blockage or loss of charge, may cause the top shell and discharge line to briefly but repeatedly reach temperatures above 175ºC as the compressor cycles on its internal protection devices. Care must be taken to ensure that wiring or other materials, which could be damaged by these temperatures, do not come in contact with these potentially hot areas. Suction and Discharge FittingsCopeland Scroll compressors have copper plated steel suction and discharge fittings. These fittings are far more rugged and less prone to leaks than。

温度漂移英语

温度漂移英语Temperature Drift。

Temperature drift refers to the phenomenon where the accuracy of a measurement or the stability of a system is affected by changes in temperature. It is a common issue in various fields, including electronics, physics, and engineering. In this article, we will delve into the concept of temperature drift, its causes, and its impact on different systems.Temperature drift occurs due to the dependence of certain physical properties on temperature. As temperature changes, these properties also change, leading to variations in the measurements or performance of a system. One of the most common examples of temperature drift is seen in electronic devices, particularly in resistors and capacitors.In electronic circuits, resistors are used to control the flow of current. However, resistors are not perfectly stable and can exhibit temperature-dependent variations in resistance. This means that the resistance of a resistor can change with temperature, leading to inaccurate measurements or calculations. Similarly, capacitors can also experience temperature drift, affecting the performance of circuits that rely on their capacitance values.The causes of temperature drift can be attributed to various factors. One of the primary factors is the thermal expansion of materials. When a material is subjected to temperature changes, it expands or contracts, altering its dimensions and properties. This expansion or contraction can introduce changes in the accuracy of measurements or the stability of a system.Another factor contributing to temperature drift is the change in electrical conductivity with temperature. Some materials exhibit a decrease in electrical resistance as temperature increases, while others show the opposite behavior. This change in conductivity can affect the performance of electronic components and systems, leading to temperature-dependent variations.Furthermore, temperature drift can also be influenced by the thermal coefficient of materials. The thermal coefficient represents the rate at which a material's properties change with temperature. Materials with high thermal coefficients are more prone to temperature drift, as small temperature changes can result in significant variations in their properties.The impact of temperature drift can be detrimental in many applications. In scientific experiments or industrial processes that require precise measurements, temperature drift can introduce errors and compromise the accuracy of the results. In electronic devices, temperature drift can lead to unstable performance, affecting the reliability and functionality of the system.To mitigate the effects of temperature drift, various techniques are employed. One common approach is temperature compensation, where the system is designed to account for the temperature-dependent variations. This can involve using temperature sensors to monitor the temperature and adjust the system accordingly. Additionally, the use of temperature-stable components and materials can help minimize temperature drift.In conclusion, temperature drift is a significant concern in various fields, affecting the accuracy and stability of measurements and systems. It is caused by the temperature dependence of certain physical properties, such as resistance and conductivity. Understanding the causes and impact of temperature drift is crucial in developing strategies to minimize its effects and ensure reliable and accurate performance in various applications. By implementing temperature compensation techniques and utilizing temperature-stable components, the adverse effects of temperature drift can be mitigated, leading to improved system performance and more accurate measurements.。

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a rXiv:h ep-ph/68336v131Aug26On the Current Correlators at Low Temperature B.L.Ioffe ∗Institute of Theoretical and Experimental Physics,117218,Moscow,B.Cheremushkinskaya 25Abstract It is demonstrated,that the calculations of current correlators at low T ,per-formed in Ref.’s [1],[2],[3]by the methods of current algebra,are correct contrary to the statements of the recent paper by Mallik [4].The correlators of hadronic currents were considered in Ref.[1,2]at finite and small temperature T in order of T 2(see also [3]).The method of consideration was the partial conservation of the axial current (PCAC)and current algebra.The main result obtained was the following.If the correlator is represented as the sum over intermediate hadronic states (resonances),then in order T 2there is no shifts of the resonances masses (poles of the correlators)and the only interesting physical phenomenon which occurs in this order is the parity mixing,i.e.the admixture of states with opposite parity in the given channel and,in some cases,also an isospin mixing.The thermal correlators of vector and axial isovector currents were considered:C J µν(q,T )=i d 4xe iqx n n |T {Ja µ(0),J a ν(x )}exp[(Ω−H )/T ]n (1)(J =V,A ;a is isospin index).Here e −Ω= n n |exp(−H/T )|n and the sum is over the full set of the eigenstates of the Hamiltonian H .It was demonstrated that in the limit of massless pions in order of T 2(−q 2=Q 2≫T 2)C V µν(q,T )=(1−ε)C V µν(q,0)+εC A µν(q,0)(2)C A µν(q,T )=(1−ε)C A µν(q,0)+εC V µν(q,0),(3)where ε=T 2/6F 2π,F π=93MeV is the pion decay constant.The derivation of (2),(3)was based on the fact,that in order T 2it is sufficient to account for contributions of two lowest states in (1)–vacuum and one pion.Then the factor T 2arises simply from the one –pion phase space.The contributions of higher excited states are suppressed as T k ,k =4,6...(in case of pions)or e −m h /T ,where m h are the masses of massive hadronicstates.The mentioned above result arises immediately from(2),(3)after decomposition of C Jµν(q,T)and C Jµν(q,0)into the sum over intermediate states.In the paper by Mallik[4]it was found that the case of degenerate(or nearly degen-erate)intermediate states requires special consideration.(Such case was not considered in[1,2,3]).In[4]the correlator of the vector currents was considered,ρandω-mesons are assumed to be degenerate,mρ=mω,their widths were neglected.It was found that ρandωmass shifts are absent in agreement with[1,2],but the residue at theρmeson pole in order T2changes its universal form1−εto1−(1+g21/3)ε,where g1is theρωπcoupling constant.It is important to mention that this result is valid only at q2=m2ρ.If |q2−m2ρ|is large enough,|q2−m2ρ|≫mρT,then the proportional to g21term in the residue is multiplied by the factor of order T2/(q2−m2ρ),its contribution is of order T4,i.e.of the order of the neglected terms.Therefore,the domain in q2,where the proportional to g21correction is essential,is narrow at small T.For example,if we would like to apply the procedure,common in the vector dominance model,and extrapolate the correlator from q2=m2ρto q2=0,we shall put g21=0.The account of theρ-meson width drasti-cally changes the situation.In this real physical situationρandω-mesons are no more degenerate,ρ→ωπtransition proceeds through the emission of pions in the p-wave,the small numerator which arises from theρ→ωπ→ρtransition is not compensated by the denominator.The effect ofρ→ωπ→ρtransitions results in appearance of the T4terms in C Vµν(q,T)and the formulae(2),(3)are intact.So,the result[Eq.(1.1)]of the Ref.[4]is very limited–only in a model,whereρwidth is neglected and even there in the narrow interval of q2.Turn now to the second problem,discussed in[4]:the T2correction to nucleon coupling λin the correlator of nucleon currents[5]-[7].This correction was calculated in Ref.[8]asλT=λ 1−(g2A+1)F2π ,(4)where g A is the nucleon axial coupling constant.In Ref.[4]it is claimed,that g2A term in(4)would be missed in the calculations performed by the method of Ref.[1,2].This is,however,not true.The correlators of baryon currents were considered in[2],but only the mixing of correlators with different isospin and opposite parity was discussed.No calculation of the residue at nucleon pole was performed.If such calculation would be done by PCAC technique,the proportional to g2A term would arise from1References[1]M.Dey,V.L.Eletsky and B.L.Ioffe,Phys.Lett.B252,620(1990)[2]V.L.Eletsky and B.L.Ioffe,Phys.Rev.D47,3083(1993)[3]V.L.Eletsky and B.L.Ioffe,Phys.Rev.D51,2371(1995).[4]S.Mallik,Eur.Phys.J C45,777(2006).[5]B.L.Ioffe,Nucl.Phys.B188,317(1981).[6]V.M.Belyaev and B.L.Ioffe,Sov.Phys.JETP56,493(1982).[7]B.L.Ioffe,Zs.Phys.C18,67(1983).[8]H.Leutwyler and A.V.Smilga,Nucl.Phys.B342,302(1990)3。

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