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asked Feb 24, 2019 in General Aptitude Arjun 1.4k points
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asked Feb 24, 2019 in General Aptitude Arjun 1.4k points
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asked Feb 24, 2019 in General Aptitude Arjun 1.4k points
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asked Feb 24, 2019 in General Aptitude Arjun 1.4k points
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asked Feb 24, 2019 in General Aptitude Arjun 1.4k points
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asked Feb 24, 2019 in General Aptitude Arjun 1.4k points
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asked Feb 24, 2019 in General Aptitude Arjun 1.4k points
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asked Feb 24, 2019 in General Aptitude Arjun 1.4k points
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asked Feb 24, 2019 in General Aptitude Arjun 1.4k points
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asked Feb 24, 2019 in General Aptitude Arjun 1.4k points
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A system of $n$ homogeneous linear equations containing $n$ unknowns will have non-trivial solutions if and only if the determinant of the coefficient matrix is $1$ $-1$ $0$ $\infty$
asked Feb 24, 2019 in Others Arjun 1.4k points
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The value of the expression $\underset{x\rightarrow \frac{\pi }{2}}{lim}\:\left | \frac{tan\:x}{x} \right |$ is $\infty$ $0$ $1$ $-1$
asked Feb 24, 2019 in Others Arjun 1.4k points
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Consider a rigid, perfectly insulated, container partitioned into two unequal parts by a thin membrane (see figure). One part contains one mole of an ideal gas at pressure $P_{i}$ and temperature $T_{i}$ while the other part is evacuated. The membrane ruptures, the gas fills the entire volume and the equilibrium pressure is ... $C_{p}$In$2$ +$R$In$4$ $-C_{v}$In$2$ +$R$In$4$ $R$In$4$ $C_{p}$In$2$
asked Feb 24, 2019 in Others Arjun 1.4k points
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For a single component system, vapor (subscript $g$) and liquid (subscript $f$) coexist in mechanical, thermal and phase equilibrium when $u_{g}=u_{f}$ (equality of specific internal energy) $h_{g}=h_{f}$ (equality of specific enthalpy) $s_{g}=s_{f}$ (equality of specific entropy) $g_{g}=g_{f}$ (equality of specific Gibbs free energy)
asked Feb 24, 2019 in Others Arjun 1.4k points
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For a binary nonideal $A-B$ mixture exhibiting a minimum boiling azeotrope, the activity coefficients, $\gamma_{i} \left ( i=A, B \right )$, must satisfy $\gamma _{A}> 1,\gamma _{B}> 1$ $\gamma _{A}< 1,\gamma _{B}> 1$ $\gamma _{A}= 1,\gamma _{B}= 1$ $\gamma _{A}< 1,\gamma _{B}< 1$
asked Feb 24, 2019 in Others Arjun 1.4k points
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For a fully-developed turbulent hydrodynamic boundary layer for flow past a flat plate, the thickness of the boundary layer increases with distance $x$ from the leading edge of the plate, along the free-stream flow direction, as $x^{0.5}$ $x^{1.5}$ $x^{0.4}$ $x^{0.8}$
asked Feb 24, 2019 in Others Arjun 1.4k points
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Consider a cylinder (diameter $D$ and length $D$), a sphere (diameter $D$) and a cube (side length $D$). Which of the following statements concerning the sphericity $\left ( \Phi \right )$ of the above objects is true: $\Phi _{sphere}> \Phi _{cylinder}> \Phi _{cube}$ ... $\Phi _{sphere}< \Phi _{cylinder}< \Phi _{cube}$ $\Phi _{cylinder}> \Phi _{sphere}= \Phi _{cube}$
asked Feb 24, 2019 in Others Arjun 1.4k points
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Prandtl number signifies the ratio of $\frac{Momentum \: Diffusivity}{Thermal \: Diffusivity}$ $\frac{Mass \: Diffusivity}{Thermal \: Diffusivity}$ $\frac{Thermal \: Diffusivity}{Momentum \: Diffusivity}$ $\frac{Thermal \: Diffusivity}{Mass \: Diffusivity}$
asked Feb 24, 2019 in Others Arjun 1.4k points
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Pool boiling equipment operating above ambient temperature is usually designed to operate far above the critical heat flux near the critical heat flux far above the Leidenfrost point near the Leidenfrost point
asked Feb 24, 2019 in Others Arjun 1.4k points
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The desired liquid-phase reaction $D+E\overset{k_{1}}{\rightarrow}F \:\:\:\:\:\:\:\:\:r_{F}=k_{1}\:C_{D}^{2}\:C_{E}^{0.3}$ ... molar feed rates of $D$ and $E$ are shown in figure. Each scheme is designed for the same conversion. The scheme that gives the most favorable product distribution is:
asked Feb 24, 2019 in Others Arjun 1.4k points
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For a first order reaction in a porous spherical catalyst pellet, diffiusional effects are most likely to lower the observed rate of reaction for slow reaction in a pellet of small diameter slow reaction in a pellet of large diameter fast reaction in a pellet of small diameter fast reaction in a pellet of large diameter
asked Feb 24, 2019 in Others Arjun 1.4k points
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A thermocouple senses temperature based on the Nernst Effect Maxwell Effect Seebeck Effect Peltier Effect
asked Feb 24, 2019 in Others Arjun 1.4k points
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The correct expression for the Colburn $j$-factor for mass transfer that relates Sherwood number ($Sh$), Reynolds number ($Re$) and Schmidt number ($Sc$) is $\frac{Sh}{\left ( Re \right )\left ( Sc \right )^{1/3}}$ $\frac{Sh}{\left ( Re \right )^{1/2}\left ( Sc \right )}$ $\frac{Sh}{\left ( Re \right )^{1/2}\left ( Sc \right )^{1/3}}$ $\frac{Sh}{\left ( Re \right )\left ( Sc \right )}$
asked Feb 24, 2019 in Others Arjun 1.4k points
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In the drying of non-dissolving solids at constant drying conditions, the internal movement of moisture in the solid has a dominant effect on the drying rate during the initial adjustment period only the constant rate period only the falling rate period only both the initial adjustment and constant rate periods
asked Feb 24, 2019 in Others Arjun 1.4k points
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Three distillation schemes for separating an equimolar, constant relative volatility $ABC$ mixture into nearly pure components are shown. The usual simplifying assumptions such as constant molal overflow, negligible heat loss, ideal trays are valid. All the schemes are designed for minimum total reboiler duty. Given ... of total reboiler duty is $I, II, III$ $III, I, II$ $II,I, III$ $III, II, I$
asked Feb 24, 2019 in Others Arjun 1.4k points
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Consider the two countercurrent heat exchanger designs for heating a cold stream from $t_{in}$ to $t_{out}$ as shown in figure. The hot process stream is available at $T_{in}$. The inlet stream conditions and overall heat transfer coefficients are identical in both the designs. The heat transfer area in Design $I$ and ... $A_{HX}^{I}< A_{HX}^{II}\:\:\:\:T_{out}^{I}= T_{out}^{II}$
asked Feb 24, 2019 in Others Arjun 1.4k points
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Producer gas is obtained by passing air through red hot coke thermal cracking of naphtha passing steam through red hot coke passing air and steam through red hot coke
asked Feb 24, 2019 in Others Arjun 1.4k points
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In Kraft process, the essential chemical reagents used in the digester are caustic soda, mercaptans and ethylene oxide caustic soda, sodium sulphide and soda ash quick lime, salt cake and dimethyl sulphide baking soda, sodium sulphide and mercaptans
asked Feb 24, 2019 in Others Arjun 1.4k points
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The most common catalyst used for oxidation of $o$-xylene to phthalic anhydride is $V_{2}O_{5}$ $Pd$ $Pt$ $Ag$
asked Feb 24, 2019 in Others Arjun 1.4k points
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In petroleum refining operations, the process used for converting paraffins and naphthenes to aromatics is alkylation catalytic reforming hydrocracking isomerization
asked Feb 24, 2019 in Others Arjun 1.4k points
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The combination that correctly matches the polymer in Group-$1$ with the polymerization reaction type in Group-$2$ ... $R-III$ $P-I$, $Q-III$, $R-II$ $P-III$, $Q-II$, $R-I$ $P-II$, $Q-III$, $R-I$
asked Feb 24, 2019 in Others Arjun 1.4k points
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The product of the eigenvalues of the matrix $\begin{pmatrix} 2 &3 \\ 0& 7 \end{pmatrix}$ is ______________________ (rounded off to one decimal place).
asked Feb 24, 2019 in Others Arjun 1.4k points
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For a hydraulic lift with dimensions shown in figure, assuming $g=10\:m/s^{2}$, the maximum diameter $D_{left}$ (in $m$) that lifts a vehicle of mass $1000 \:kg$ using a force of $100 \:N$ is ____________________ (rounded off to two decimal places).
asked Feb 24, 2019 in Others Arjun 1.4k points
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The liquid flow rate through an equal percentage control valve, when fully open, is $150$ gal/min and the corresponding pressure drop is $50$ psi. If the specific gravity of the liquid is $0.8$, then the valve coefficient, $C_{V}$, in gal/(min $psi^{0.5}$) is _________________ (rounded off to two decimal places).
asked Feb 24, 2019 in Others Arjun 1.4k points
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Consider a sealed rigid bottle containing $CO_{2}$ and $H_{2}O$ at $10$ bar and ambient temperature. Assume that the gas phase in the bottle is pure $CO_{2}$ and follows the ideal gas law. The liquid phase in the bottle contains $CO_{2}$ ... $CO_{2}$ dissolved in $H_{2}O$ is __________________ (rounded off to three decimal places).
asked Feb 24, 2019 in Others Arjun 1.4k points
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The solution of the ordinary differential equation $\frac{dy}{dx}+3y=1$, subjects to the initial condition $y=1$ at $x=0$, is $\frac{1}{3}\left ( 1+2e^{-x/3} \right )$ $\frac{1}{3}\left ( 5-2e^{-x/3} \right )$ $\frac{1}{3}\left ( 5-2e^{-3x} \right )$ $\frac{1}{3}\left ( 1+2e^{-3x} \right )$
asked Feb 24, 2019 in Others Arjun 1.4k points
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The value of the complex number $i^{-1/2}$ (where $i=\sqrt{-1}$) is $\frac{1}{\sqrt{2}}\left ( 1-i \right )$ $-\frac{1}{\sqrt{2}}i$ $\frac{1}{\sqrt{2}}i$ $\frac{1}{\sqrt{2}}\left ( 1+i \right )$
asked Feb 24, 2019 in Others Arjun 1.4k points
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An incompressible Newtonian fluid flows in a pipe of diameter $D_{1}$ at volumetric flow rate $Q$. Fluid with same properties flows in another pipe of diameter $D_{2}=D_{1}/2$ at the same flow rate $Q$ . The transition length required for achieving fully-developed flow is $l_{1}$ for the ... $D_{2}$. Assuming steady laminar flow in both cases, the ratio $l_{1}/l_{2}$ is: $1/4$ $1$ $2$ $4$
asked Feb 24, 2019 in Others Arjun 1.4k points
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A disk turbine is used to stir a liquid in a baffled tank. To design the agitator, experiments are performed in a lab-scale model with a turbine diameter of $0.05 \:m$ and a turbine impeller speed of $600$ $rpm$. The liquid viscosity is $0.001$ $Pa$ $s$ while the liquid density is $1000$ ... actual application is $P_{2}$, then the ratio $P_{2}/P_{1}$ is $10^{3}$ $10^{4}$ $10^{5}$ $10^{6}$
asked Feb 24, 2019 in Others Arjun 1.4k points
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Consider two non-interacting tanks-in-series as shown in figure. Water enters $TANK$ $1$ at $q$ $cm^{3}/s$ and drains down to $TANK$ $2$ by gravity at a rate $k\sqrt{h_{1}}\;\left ( cm^{3}/s \right )$. Similarly, water drains from $TANK$ $2$ ... $\frac{2}{\left ( 36s+1 \right )^{2}}$ $\frac{2}{\left ( 49s+1 \right )^{2}}$
asked Feb 24, 2019 in Others Arjun 1.4k points
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