MCQOPTIONS
Saved Bookmarks
This section includes 1608 Mcqs, each offering curated multiple-choice questions to sharpen your Chemical Engineering knowledge and support exam preparation. Choose a topic below to get started.
| 1151. |
Hydraulic radius is the ratio of |
| A. | wetted perimeter to flow area. |
| B. | flow area to wetted perimeter. |
| C. | flow area to square of wetted perimeter. |
| D. | square root of flow area to wetted perimeter. |
| Answer» C. flow area to square of wetted perimeter. | |
| 1152. |
The pressure co-efficient is the ratio of pressure forces to __________ forces. |
| A. | viscous |
| B. | inertial |
| C. | gravity |
| D. | surface tension |
| Answer» B. inertial | |
| 1153. |
The capacity of a centrifugal pump Can be increased by increasing the |
| A. | impeller diameter or speed. |
| B. | number of pumps and joining them in series, |
| C. | number of pumps and joining them in parallel. |
| D. | all (a), (b) and (c). |
| Answer» E. | |
| 1154. |
The terminal velocity of a particle moving through a fluid varies as dpn. The value of n is equal to __________ in Stoke's law regime. |
| A. | 1 |
| B. | 0.5 |
| C. | 2 |
| D. | 1.5 |
| Answer» D. 1.5 | |
| 1155. |
The maximum head that can be developed by a single impeller is __________ ft. |
| A. | 25 |
| B. | 100 |
| C. | 250-300 |
| D. | 1000 |
| Answer» D. 1000 | |
| 1156. |
Pressure drop (Δp) for a fluid flowing in turbulent flow through a pipe is a function of velocity (V) as$ |
| A. | V1.8 |
| B. | V-0.2 |
| C. | V2.7 |
| D. | V2 |
| Answer» E. | |
| 1157. |
In centrifugal pumps, cavitation occurs, when pressure of the impeller eye or vane becomes |
| A. | less than atmospheric pressure. |
| B. | more than liquid vapor pressure. |
| C. | less than liquid vapor pressure. |
| D. | more than atmospheric pressure. |
| Answer» D. more than atmospheric pressure. | |
| 1158. |
The equivalent diameter for pressure drop calculation for a duct of square cross-section is given by(where, x = each side of the square duct) |
| A. | x |
| B. | πx |
| C. | 2x |
| D. | x/2 |
| Answer» B. œÄx | |
| 1159. |
The vent valve provided in a liquid handling centrifugal pump is |
| A. | generally a needle valve. |
| B. | used to release any gases that might be vapour locking the pump. |
| C. | helpful in easy removal of samples. |
| D. | all (a), and (b) and (c). |
| Answer» E. | |
| 1160. |
Fanning equation is given by. It is applicable to __________ region flow. |
| A. | transition |
| B. | laminar |
| C. | turbulent |
| D. | both (b) and (c) |
| Answer» E. | |
| 1161. |
For an ideal fluid flow, Reynolds number is |
| A. | 2100 |
| B. | 100 |
| C. | 0 |
| D. | ‚àû |
| Answer» E. | |
| 1162. |
Critical velocity in a pipe flow |
| A. | increases as fluid viscosity increases. |
| B. | increases as pipe diameter increases. |
| C. | independent of fluid density. |
| D. | none of these. |
| Answer» C. independent of fluid density. | |
| 1163. |
When the head pumped against is less than the head of the fluid used for pumping, the usual device is a/an |
| A. | ejector |
| B. | blower |
| C. | injector |
| D. | airlift |
| Answer» E. | |
| 1164. |
For the manometer set up shown in the figure, the pressure difference PA - PB is given by |
| A. | (ρH - ρair)gH |
| B. | (ρH - ρL)gH |
| C. | (ρH - ρL) gH + (ρL - ρair) . g(L - H) |
| D. | (ρH - ρL) gL + (ρL - ρair)gH |
| Answer» B. (œÅH - œÅL)gH | |
| 1165. |
For a given fluid flow rate, which of the following incurs maximum head loss ? |
| A. | Orifice meter |
| B. | Venturimeter |
| C. | Flow nozzle |
| D. | All of them incur the same head loss |
| Answer» B. Venturimeter | |
| 1166. |
A weir is used to measure the large water discharge rate from a river or from an open channel. A weir is not of __________ shape. |
| A. | circular |
| B. | rectangular |
| C. | triangular |
| D. | trapezoidal |
| Answer» B. rectangular | |
| 1167. |
Design of the casing of centrifugal pump should be such as to minimise the |
| A. | back flow through impeller |
| B. | loss of kinetic head |
| C. | loss of static head |
| D. | none of these |
| Answer» C. loss of static head | |
| 1168. |
Sewage sludge is an example of the __________ fluid. |
| A. | Bingham plastic |
| B. | Newtonion |
| C. | pseudoplastic |
| D. | dilatent |
| Answer» B. Newtonion | |
| 1169. |
For the production of very high vacuum, a __________ pump is normally used. |
| A. | diffusion |
| B. | centrifugal |
| C. | jet ejector |
| D. | piston |
| Answer» B. centrifugal | |
| 1170. |
Gear pump |
| A. | is a positive displacement pump. |
| B. | is a centrifugal pump. |
| C. | is a non-positive displacement pump. |
| D. | can be started with delivery valve closed. |
| Answer» B. is a centrifugal pump. | |
| 1171. |
Cd for the orifice plate varies from |
| A. | 0.58 to 0.8 |
| B. | 0.93 to 0.98 |
| C. | 0.2 to 0.3 |
| D. | 0.02 to 0.03 |
| Answer» B. 0.93 to 0.98 | |
| 1172. |
The valve used for very remote and accurate control of fluid is a __________ valve. |
| A. | needle |
| B. | globe |
| C. | gate |
| D. | butterfly |
| Answer» B. globe | |
| 1173. |
Fluid flow through a packed bed is represented by the __________ equation. |
| A. | Fanning's |
| B. | Ergun's |
| C. | Hagen-Poiseuille's |
| D. | none of these |
| Answer» C. Hagen-Poiseuille's | |
| 1174. |
The Navier-Stokes equation deals with the law of conservation of |
| A. | mass |
| B. | energy |
| C. | both (a) & (b) |
| D. | momentum |
| Answer» E. | |
| 1175. |
Unit of mass velocity is |
| A. | kg/hr |
| B. | kg/m2. hr |
| C. | kg/m2 |
| D. | kg/m3. hr |
| Answer» C. kg/m2 | |
| 1176. |
While starting an axial flow pump, its delivery valve should be kept |
| A. | open |
| B. | closed |
| C. | either open or closed |
| D. | none of these |
| Answer» B. closed | |
| 1177. |
The discharge through a rectangular weir varies as |
| A. | H1/2 |
| B. | H5/2 |
| C. | H2/5 |
| D. | H3/2 |
| Answer» E. | |
| 1178. |
Which of the following equations applies to the fluid flow through a packed bed for very large Reynolds number ? |
| A. | Fanning equation |
| B. | Blake-Pllummer equation |
| C. | Hagen-Poiseulle equation |
| D. | Kozney-Karman equation |
| Answer» C. Hagen-Poiseulle equation | |
| 1179. |
Specific speed of a centrifugal pump relates it with another pump having the |
| A. | dynamic similarity |
| B. | same efficiency |
| C. | same speed |
| D. | geometrical similarity |
| Answer» B. same efficiency | |
| 1180. |
Boundary layer exists in flow |
| A. | of real fluids. |
| B. | over flat surfaces only. |
| C. | in pipes only. |
| D. | of ideal fluids only. |
| Answer» B. over flat surfaces only. | |
| 1181. |
Select the correct practical example of steady non-uniform flow. |
| A. | Motion of water around a ship in a lake. |
| B. | Motion of river around bridge piers. |
| C. | Steadily decreasing flow through a reducing section. |
| D. | Steadily increasing flow through a pipe. |
| Answer» D. Steadily increasing flow through a pipe. | |
| 1182. |
Momentum transfer in laminar flow of fluids results due to the |
| A. | viscosity |
| B. | density |
| C. | velocity gradient |
| D. | none of these |
| Answer» D. none of these | |
| 1183. |
The maximum depth from which a centrifugal pump can draw water is |
| A. | dependent on the speed of the pump. |
| B. | dependent on the power of the pump. |
| C. | 34 feet. |
| D. | 150 feet. |
| Answer» D. 150 feet. | |
| 1184. |
Cp/Cv is termed as |
| A. | adiabatic constant |
| B. | Mach number |
| C. | Weber number |
| D. | Prandtl number |
| Answer» B. Mach number | |
| 1185. |
The effect of solid boundary on the fluid flow is confined to the boundary layer, except for fluids |
| A. | having high viscosities. |
| B. | moving at low velocities. |
| C. | both (a) & (b). |
| D. | neither (a) nor (b). |
| Answer» D. neither (a) nor (b). | |
| 1186. |
Foot valves are provided in the suction line of a centrifugal pump to |
| A. | avoid priming, every time we start the pump. |
| B. | remove the contaminant present in the liquid. |
| C. | minimise the fluctuation in discharge. |
| D. | control the liquid discharge. |
| Answer» B. remove the contaminant present in the liquid. | |
| 1187. |
During ageing of fluid carrying pipes, the |
| A. | pipe becomes smoother with use. |
| B. | friction factor increases linearly with time. |
| C. | absolute roughness decreases with time. |
| D. | absolute roughness increases linearly with time. |
| Answer» E. | |
| 1188. |
A fluid which has a linear relationship between the magnitude of applied shear-stress and the resulting rate of deformation is called a/an __________ fluid. |
| A. | Newtonion |
| B. | Non-Newtonion |
| C. | ideal |
| D. | incompressible |
| Answer» B. Non-Newtonion | |
| 1189. |
Drag is the force component exerted on an immersed object, |
| A. | passing the centroid of the body at 60°to the direction of motion. |
| B. | the component being parallel to theflow direction. |
| C. | the component being normal to the flow direction. |
| D. | none of these. |
| Answer» C. the component being normal to the flow direction. | |
| 1190. |
For the free settling of a spherical particle through a fluid, the slope of, CD-log NRe , plot is |
| A. | 1 |
| B. | -1 |
| C. | 0.5 |
| D. | -0.5 |
| Answer» C. 0.5 | |
| 1191. |
I.D. of 1/4" schedule 40 pipe is 0.364". I.D. of a 1/2" schedule 40 pipe would be __________ inch |
| A. | 4.728 |
| B. | 0.5 |
| C. | 0.622 |
| D. | 0.474 |
| Answer» D. 0.474 | |
| 1192. |
For flow through an orifice from a reservoir, the actual velocity at the vena con-tracta is given by |
| A. | 2gh |
| B. | C.V. 2gh |
| C. | Cd 2gh |
| D. | Cc 2gh |
| Answer» C. Cd 2gh | |
| 1193. |
A compressor that takes suction at a pressure below atmospheric and discharge against atmospheric pressure is called a __________ pump. |
| A. | sump |
| B. | volute |
| C. | vacuum |
| D. | submerged |
| Answer» D. submerged | |
| 1194. |
A 2" gate valve fitted in a pipe is replaced by a similar globe valve. Pressure drop in gate valve was Δp. For the same discharge, the pressure drop across globe valve is$ |
| A. | Δp |
| B. | < Δp |
| C. | > Δp |
| D. | Δp2 |
| Answer» D. Œîp2 | |
| 1195. |
In parallel pipe problems, the |
| A. | head loss is the same through each pipe. |
| B. | discharge is the same through all the pipes. |
| C. | total head loss is equal to the sum of the head losses through each pipe. |
| D. | none of these. |
| Answer» B. discharge is the same through all the pipes. | |
| 1196. |
__________ forces act on a particle moving through a stationary fluid. |
| A. | Gravity |
| B. | Drag |
| C. | Buoyant |
| D. | all (a), (b), & (c) |
| Answer» E. | |
| 1197. |
What is the shear rate at the pipe wall, in case of laminar flow of Newtonion fluids in a pipe of diameter 'D' & length 'L' incurring a pressure drop 'Δp' with average velocity 'Vavg'?$ |
| A. | D Δp/8L |
| B. | D Δp/4L |
| C. | 8 . Vavg/D |
| D. | 4 . Vavg/D |
| Answer» D. 4 . Vavg/D | |
| 1198. |
Multistage centrifugal pumps are generally used for |
| A. | high head. |
| B. | low head but high discharge. |
| C. | highly viscous liquid. |
| D. | slurries of high solid concentration. |
| Answer» B. low head but high discharge. | |
| 1199. |
If 'x' is the depth of flow in an open channel of large width, then the hydraulic radius is equal to |
| A. | x |
| B. | x/2 |
| C. | x/3 |
| D. | 2x/3 |
| Answer» B. x/2 | |
| 1200. |
The variable required to be known in correlations used for estimating the horse power of a centrifugal gas compressor and hence its cost are P. Inlet pressure Q. Compressor rpm R. Delivery pressure S. Volumetric flow rate at inlet. |
| A. | P, Q and R |
| B. | P and R |
| C. | R and S |
| D. | P, Rand S |
| Answer» B. P and R | |