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a response of a cys p2 modified spr gold chip to 10μm of thiacloprid solid and 10μm of imidacloprid dashed and b binding curve of cys p2 modified spr gold chip to hbs ep buffer containing imidacloprid with concentration of 2 10 2

Efficient progressive collapse analysis for robustness evaluation and enhancement of steel concrete composite buildings

Efficient progressive collapse analysis for robustness evaluation and enhancement of steel concrete composite buildings

Cao đẳng - Đại học

... that the falling beam is assumed as point mass, and < /b> impacted beam is initially at stationary state, and < /b> full plastic impact where both beams move together after the impact and < /b> local deformation ... respective advantages and < /b> disadvantages of < /b> each method and < /b> suggests that each analysis should be checked and < /b> selected for a < /b> target in a < /b> progressive way from linear static to < /b> nonlinear dynamic analysis ... element analysis (FEA) of < /b> large numerical model using commercial software such as ABAQUS (ABAQUS, 20 05) and < /b> LS-DYNA (Hallquist, 20 06) Some notable studies adopting detailed FEA include the work by Alashker...
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Tài liệu Design of Feedback Control Systems for Stable Plants with Saturating Actuators ppt

Tài liệu Design of Feedback Control Systems for Stable Plants with Saturating Actuators ppt

Cao đẳng - Đại học

... IIy(t)lloo > and < /b> thus for any X (to)< /b> the basic problem does not have a < /b> solution /// The solution to < /b> the basic problem which was given above assumed that X(t) is a < /b> scalar A < /b> similar solution can be obtained ... Every stable system G(s) with bounded inputs is BIBO stable because the outputs are always bounded The system in figure 4 .2 is finite gain stable because in addition to < /b> being BIBO stable it is ... compensator K(s) is neutrally stable and < /b> finite gain stability is guaranteed because in addition the plant G(s) is stable The result is a < /b> multivariable control system with integrators in the forward...
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Báo cáo khoa học: Insights into the design of a hybrid system between Anabaena ferredoxin-NADP+ reductase and bovine adrenodoxin pot

Báo cáo khoa học: Insights into the design of a hybrid system between Anabaena ferredoxin-NADP+ reductase and bovine adrenodoxin pot

Báo cáo khoa học

... that shows a < /b> typical absorbance band at 450 nm [33] Time-sequential spectra recorded after addition of < /b> CYP1 1A1< /b> to < /b> an anaerobic CO-saturated sample containing the reaction mixture FNRrd/Adxox gave ... typical absorption spectrum of < /b> the CO-ferrous CYP1 1A1< /b> complexed form, characterized by absorbance decreases at 390, 430 and < /b> 480 nm and < /b> by the appearance of < /b> a < /b> peak at 450 nm which exhibits a < /b> large ... FNRrd and < /b> Adxox Data calculated from steady-state spectra recorded in Fig 2A < /b> at 414 nm Adx concentration dependence of < /b> (A)< /b> kobs1, kobs2 and < /b> V0 (lines are drawn in for clarity only, they not represent...
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Báo cáo khoa học:

Báo cáo khoa học: "User studies and the design of Natural Language Systems" doc

Báo cáo khoa học

... interface to < /b> a < /b> database was run3.1 Preliminary analysis and < /b> filtering ning on the machine and < /b> that the database contained information about paintings by Van Gogh and < /b> other artists In fact this was ... information to < /b> answer questions about the database, and < /b> so in principle, the system was capable of < /b> handling all inputs The subjects were asked to < /b> access information from the "database" about a < /b> set ... HPL-BRC-TR-88- 022 , Hewlett-Packard Laboratories, Bristol, U.K., 1988 [sw83] Duane W Small and < /b> Linda J Weldon An experimental comparison of < /b> natural and < /b> structured query languages Human Factors, 25 (3) :25 3 -26 3,...
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surface production operations - design of oil handling systems and facilities

surface production operations - design of oil handling systems and facilities

Hóa học - Dầu khí

... Horizontal Separators 155 Vertical Separators 156 Spherical Separators 157 Centrifugal Separators 159 Venturi Separators 160 Double-Barrel Horizontal Separators 161 Horizontal Separator with a < /b> “Boot” ... Constraint 21 5 Vertical Separators’ Sizing 21 9 Gas Capacity Constraint 21 9 Liquid Capacity Constraint 22 2 Seam -to-< /b> Seam Length 22 4 Slenderness Ratio 22 6 Procedure for Sizing Vertical Separators 22 6 Examples ... Laboratory Analysis 107 Volatile Oil Reservoir 107 Phase Diagram Characteristics 107 Field Characteristics 108 Laboratory Analysis 109 Retrograde Gas Reservoir 109 Phase Diagram Characteristics 109 ...
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Báo cáo hóa học:

Báo cáo hóa học: " Optimal Design of Noisy Transmultiplexer Systems Huan Zhou1 and Lihua Xie2" docx

Báo cáo khoa học

... 4.1931 32. 0317 5.83 82 48.9783 5.5448 Band 30.8980 11.6430 33. 8104 12. 223 8 76. 1100 6.6835 SNRc = 20 dB Band 26 .1188 9.4181 35. 629 9 10. 522 3 54.5 022 10. 1444 Band 23 .27 97 8.8873 34. 626 9 9.8985 48. 627 ... currently an Associate Editor of < /b> the IEEE Transactions on Automatic Control, International Journal of < /b> Control, Automation and < /b> Systems, and < /b> Journal of < /b> Control Theory and < /b> Applications He is also a < /b> Member ... guard bands (thereby permitting crosstalk), we can eliminate the crosstalk in a < /b> manner analogous to < /b> aliasing cancellation in maximally decimated filter banks by a < /b> careful choice of < /b> transmitters and...
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Part 4: Code of practice for design of composite slabs with profiled steel sheeting ppt

Part 4: Code of practice for design of composite slabs with profiled steel sheeting ppt

Kiến trúc - Xây dựng

... concrete in accordance with BS 8 110 -2: 1985) taking As as Ap, d as ds and < /b> b as Bs) 6.5 .2 Punching shear capacity The punching shear capacity Vp of < /b> a < /b> composite slab at a < /b> concentrated load should be determined ... ensures that subscribers automatically receive the latest editions of < /b> standards Buying standards Orders for all BSI, international and < /b> foreign standards publications should be addressed to < /b> Customer ... is to < /b> obtain data to < /b> enable the values of < /b> the empirical parameters kr and < /b> mr to < /b> be established, which are then used to < /b> determine the shear-bond capacity Vs (see 6.4.1) All testing should be carried...
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ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 1 Part 1 pps

ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 1 Part 1 pps

Kĩ thuật Viễn thông

... Galey, Lonnie W Shelton, Mary E Thro, Benjamin T Banken, Jorge Zafra, Santiago Pacheco, and < /b> Dinesh P Patel We also wish to < /b> acknowledge Lukman Mahfoedz, Fiaz Shahab, Holland Simanjuntak, Richard ... Simanjuntak, Richard Sugeng, Abdul Wahab, Adolf Pangaribuan of < /b> VICO, and < /b> Allen Logue and < /b> Rocky Buras of < /b> Glytech for providing source material, suggestions, and < /b> criticism of < /b> the chapters on heat ... Texas Maurice I Stewart, Ph.D., RE Metairie, Louisiana xiv CHAPTER Overview of < /b> Gas-Handling Facilities * The objective of < /b> a < /b> gas-handling facility is to < /b> separate natural gas, condensate, or oil and...
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ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 1 Part 2 doc

ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 1 Part 2 doc

Kĩ thuật Viễn thông

... 1.1 92 1 .29 1 398 1.474 2. 433 2. 494 2. 573 2. 6 42 ,26 18 26 18 327 2 327 2 327 2 327 2 327 2 327 2 327 2 327 2 327 2 327 2 3 927 3 927 3 927 3 927 523 6 523 6 523 6 523 6 Ft2 Internal Surface Per Ft Length 23 61 24 35 ,23 30 ... as for finned tubes or insulation, then additional terms must be added to < /b> the right side of < /b> Equation 2- 5 Tables 2- 1 and < /b> 2- 2 have basic tube and < /b> coil properties for use in Equation 2- 5 and < /b> Table ... heat, or both Sensible Heat The amount of < /b> heat absorbed or lost by a < /b> substance that causes a < /b> change in the temperature of < /b> the substance is sensible heat It is called sensible heat because it can...
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ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 1 Part 3 pps

ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 1 Part 3 pps

Kĩ thuật Viễn thông

... was MMBtu/hr and < /b> water was being heated, a < /b> heat flux of < /b> 10, 000 Btu/hr-ft2 would be used and < /b> 100 ft2 of < /b> fire tube area would be required Table 2- 12 Standard Burner Sizes and < /b> Minimum Diameter Btu/hr ... Internal gaskets can leak s Head and < /b> tubes can be mechanically cleaned • Individual tubes are replaceable * Tube cannot be cleaned mechanically « Fairly low cost may be lower • Fewer tubes can be ... water heat duty, Btu/hr Table 2- 9 Latent Heat of < /b> Vaporization Compound Methane Ethane Propane n-Butane Isobutane n-Pentane Isopentane Hexane Heptane Octane Nonane Decane Heat of < /b> Vaporization,...
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ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 1 Part 4 pdf

ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 1 Part 4 pdf

Kĩ thuật Viễn thông

... external area of < /b> fin tubes per square foot of < /b> bundle surface area From this data the area of < /b> bundle surface area can be calculated from: where A < /b> = required area of < /b> bundle face, ft2 q = heat duty, Btu/hr ... "U"-Tube No of < /b> Passes 40 56 12 18 25 10 16 22 10. 02 12. 00 13 .25 29 42 52 26 38 48 20 34 44 22 37 44 20 36 44 16 28 36 11 16 10 14 82 1 12 138 76 104 128 35 48 62 32 44 60 15 .25 17 .25 19 .25 69 92 121 68 ... low maintenance, easy accessibility, and < /b> easy expansion by adding more plates Metal plate -and-< /b> frame exchangers are particularly attractive for seawater and < /b> brackish water services However, because...
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ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 1 Part 5 pps

ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 1 Part 5 pps

Kĩ thuật Viễn thông

... 4-7, Typical Gas Association, ICHh Hydrates 103 Natural gas is not a < /b> single component and < /b> a < /b> Mollier diagram will probably not be available Figure 4-8 can be used to < /b> get a < /b> quick approximate solution ... determination of < /b> susceptibility of < /b> a < /b> gas to < /b> form hydrates At concentrations of < /b> 30% or greater, hydrates will form in hydrocarbon gases at about the same temperature as in pure H2S Table 4-1 is an example ... limit scale Heat exchanger type and < /b> number of < /b> tubes Choose TEMA R because of < /b> large size Select type AFL because of < /b> low temperature change and < /b> LMTD correction factor Heat Exchangers 89 The water...
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ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 1 Part 6 potx

ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 1 Part 6 potx

Kĩ thuật Viễn thông

... material It is perfectly acceptable for a < /b> line heater to < /b> have an L} equal to < /b> In this ease all the heat is added downstream of < /b> the choke It is also possible to < /b> have L2 equal to < /b> and < /b> all the heating ... be an even integer, actual Tj and < /b> T2 may differ slightly from that assumed in the calculation The actual values of < /b> Tj and < /b> T2 can be calculated from actual coil lengths LI and < /b> L2 Once the total ... recognized are American National Standard Institute (ANSI) B3 1.3 and < /b> B3 1.8, or American Petroleum Institute (API) Specification 12 K Volume has the tables for ANSI B3 1.3 and < /b> ANSI B3 1.8 Table 5-1...
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ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 1 Part 7 ppsx

ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 1 Part 7 ppsx

Kĩ thuật Viễn thông

... version of < /b> these trays, and < /b> the designs are proprietary Bubble Cap Trays vs Valve Trays At low vapor rates, valve trays will weep Bubble cap trays cannot weep (unless they are damaged) For this reason, ... valve tray this point may be reached after the loss in efficiency of < /b> a < /b> comparable bubble cap tray So, in distillation applications, valve trays can have a < /b> greater vapor turndown ratio than bubble ... cost and < /b> operating complexity associated with an LTX unit CHAPTER Acid Gas Treating * In addition to < /b> heavy hydrocarbons and < /b> water vapor, natural gas often contains other contaminants that may have...
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ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 1 Part 8 doc

ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 1 Part 8 doc

Kĩ thuật Viễn thông

... and < /b> carbon disulfide (CS2) to < /b> form heat-stable salts that cannot be regenerated At temperateres above 24 5 °F a < /b> side reaction with CO2 exists that produces oxazolidone -2, a < /b> heat-stable salt, and < /b> ... Alkanolamine activators Catacarb; Alkanolamine and/< /b> or borate activators Giammarco-Vetrocoke: Arsenic and < /b> other activators Physical Solvent Processes These processes are based on the solubility of < /b> the H2S ... carbonate as a < /b> physical solvent to < /b> remove CO2 and < /b> H2S Propylene carbonate also removes C2+ hydrocarbons, COS, SO2, CS2, and < /b> H2O from the natural gas stream Thus, in one step the natural gas can...
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ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 1 Part 9 pdf

ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 1 Part 9 pdf

Kĩ thuật Viễn thông

... separator is sometimes referred to < /b> as a < /b> gas/glycol separator or "pump gits" separator The wel glycol from the separator flows through a < /b> sock filter to < /b> remove solids and < /b> a < /b> charcoal filter to < /b> absorb ... tc and < /b> e are arbitrary, a < /b> 10- ft bed seems appropriate Calculate volume of < /b> iron sponge to < /b> purchase: Example No 7 -2: Specify Major Parameters for DEA Required: Show that a < /b> DEA unit is an acceptable ... the ambient temperature The reflux accumulator is a < /b> separator used to < /b> separate the acid gases from the condensed water The water is accumulated and < /b> pumped back to < /b> the top of < /b> the stripper as reflux...
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ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 1 Part 10 pdf

ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 1 Part 10 pdf

Kĩ thuật Viễn thông

... flow rates than bubble cap trays in the same diameter contactor (See Table 8-1.) Conventional and < /b> random packing will require approximately the same diameter as bubble caps Structured packing can ... desiccant bed reaches a < /b> temperature of < /b> approximately 21 5°F Additional cooling may cause water to < /b> be adsorbed from the wet gas stream and < /b> presaturate or preload the desiccant bed before the next adsorption ... tower to < /b> return it to < /b> normal operating temperatures (about 100 °F to < /b> 120 °F) before placing it back in service to < /b> dehydrate gas The cooling gas could either be wet gas or gas that has already been...
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ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 2 Part 1 docx

ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 2 Part 1 docx

Kĩ thuật Viễn thông

... Percentage Evaporated at 140°F 25 Reid Vapor Pressure ! 34 30 26 22 18 14 10 Grade 34 -25 Grade 30 -25 Grade 26 -25 Grade 22 -25 Grade 18 -25 Grade 14 -25 40 i Grade 34-40 Grade 30-40 Grade 26 -40 Grade 22 -40 ... cold separator, which is a < /b> threephase separator Water and < /b> glycol come off the bottom, hydrocarbon liquids are routed to < /b> the distillation tower and < /b> gas flows out the top If it is desirable to < /b> recover ... temperature by injecting glycol in the gas after separation of < /b> free water The glycol and < /b> water separate in the cold separator where they are routed to < /b> a < /b> regenerator, the water is boiled off and...
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ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 2 Part 2 pps

ARNOLD, K. (1999). Design of Gas-Handling Systems and Facilities (2nd ed.) Episode 2 Part 2 pps

Kĩ thuật Viễn thông

... two-stage in tandern on same shaft Advantages «Available as non-lubricated especially for air service • Can handle dirty gas • Can handle moderate amounts of < /b> liquids, but no slugs • No pulsating ... earlier In addition, local foundation conditions, type of < /b> drivers available, cost of < /b> fuel, availability of < /b> spare 27 2 Design of < /b> GAS-HANDLING Systems and < /b> Facilities Figure 10- 11 Curve for estimating ... choice of < /b> type of < /b> compressor, and < /b> the type of < /b> compressor depends in part upon horsepower and < /b> number of < /b> stages A < /b> first approximation of < /b> the number of < /b> stages can be made by assuming a < /b> maximum compressor...
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