Q. For identical situation, condensing film coefficient in case of a horizontal condenser is almost __________ the value expected in case of vertical condenser.

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Q. Diameter of rivet hole (d, mm) and the plate thickness (t, mm) are related by Unwin's formula as

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Q. A binary liquid azeotropic mixture has boiling point lower than either of the components, when it shows __________ deviation from Raoult's Law.

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Q. In which of the following evaporators, steam is fed inside the tube while the liquor is outside the tube ?

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Q. A high vapour velocity is required for high plate efficiency in a seive plate coloumn. The satisfactory value of operating vapor velocity for design purpose in seive plate column is about __________ percent of the flooding velocity.

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Q. The approximate liquid depth in an agitation tank is equal to (where, d = tank diameter)

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Q. Baffle width is normally taken as __________ times the tank diameter.

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Q. A cylinderical pressure vessel of volume 6 πm³ has to be designed to withstand a maximum internal pressure of 10 atm. The allowable design stress of the material is 125N/mm² and corrosion allowance is 2 mm. The thickness of the vessel for a length/diameter ratio of 3 will be close to

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Q. Which of the following packing materials provides for maximum mass transfer ?

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Q. Cylindrical storage tanks used for the storage of volatile liquids (e.g., naphtha) have __________ roofs.

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Q. Larger depth of liquid on the trays of a distillation column

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Q. Pick out the wrong statement.

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Q. Pick out the wrong statement.

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Q. In the downcomer of a distillation column, the minimum recommended residence time is about __________ seconds.

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Q. In a multipass shell and tube heat exchanger, the baffles on shell side is primarily provided for

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Q. For turbine agitator, the impeller diameter is about

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Q. If a single tube pass heat exchanger is converted to two passes; for the same flow rate, the pressure drop per unit length in tube side will __________ times.

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Q. __________ of water makes it a widely used coolant in heat exchangers.

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Q. The equivalent diameter for fluid flow through a channel of constant non-circular cross section of area 'A' is given by (where, P = perimeter of the channel in contact with the fluid)

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Q. Fouling factor must be included in the calculation of over all design heat transfer coefficient, when the liquid

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