Section 3 Flashcards

1
Q

Angled baffles are preferred in the agitation tank to control the swirling action; if the viscosity of the liquid to be mixed is about 200 poise. However, the baffle may be completely eliminated for mixing liquids having viscoisty above __________ poise.

A

600

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1
Q

Tube wall thickness depends on the cor-rosiveness of the fluids and their operating pressure & temperature and is specified by Birmingham wire gauge (B.W.G)-a number which varies from 8 to 18 with the numbers 14 and 16 being more commonly used. Outside diameter of tubes varies from about 15 to 50 mm; however a tube of less than __________ mm outside diameter is generally not recommended for fouling fluids.

A

19

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2
Q

Ratio of tube length to shell diameter for a shell and tube heat exchanger is

A. 8 : 1 to 12 : 1 for both liquid-liquid and gas-gas heat exchangers.
B. 4 : 1 to 8 : 1 for liquid-liquid exchanger.
C. < 4 : 1 for gas-gas exchangers.
D. both(b) & (c).

A

D

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3
Q

The dust collection efficiency of a cyclone separator
A decreases with increase in gas flow rate.
B is inversely proportional to the mass of the dust particle.
C is directly proportional to the radius of the dust particle path.
D none of these.

A

D

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4
Q

In a shell and tube heat exchanger, the overall heat transfer co-efficient is proportional to the tube side (volumetric flow rate)0.8. This is valid, only when the ratio of the tube side film resistance to the total resistance is almost equal to

A

1

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5
Q

Which of the following types of reactors is the safest from operation point of view ?

A

A vapor phase reactor.

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6
Q

In a bag filter, the pressure drop increases directly as the

A

density of the gas and inversely as viscosity of the gas.

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7
Q

The LMTD correction factor (FT) is applied in __________ heat exchangers.

A

all multipass

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8
Q

Movement of pipeline caused by thermal expansion is taken care by providing
A. expansion joint.
B. changes in its direction.
C. change in the shape of pipeline.
D. all (a), (b) and (c).

A

all (a), (b) and (c).

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9
Q

For a cylindrical shell, (subject to the thickness of uppermost course being more than the minimum for diaofthe tank in question), the thickness of the courses of shell

A

decreases upwards.

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10
Q

In the design of a paddle agitator, the ratio (paddle diameter)/(tank diameter) is normally taken as

A

0.80

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11
Q

The design stress, which is more than the damaging stress, is the least unit stress that will render a member unfit for service before the end of its normal life. The design stress factor or factor of safety indicates the margin between design stress and the __________ stress.

A

damaging

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12
Q

Hole diameter of the seive trays in the distillation column ranges from __________ mm.

A

3 to 12.5

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13
Q

Factor of safety (i.e., overdesign factor) in heat transfer equipments is about __________ percent more than the actual/theoretical design factor.

A

15-20

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14
Q

For annular flow of a fluid, the ratio of the equivalent diameter for pressure drop calculation to the equivalent diameter for heat transfer calculation is

A

(d1)/(d1+d2)

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15
Q

In actual operation of distillation column, the vapour is not distributed uniformly among the bubble caps, primarily because of the

A

liquid gradient on the tray.

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16
Q

The minimum shell thickness for tank ≤ 15 metres diameter is limited to __________ mm, for reasons of elastic stability.

A

5

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17
Q

If ‘D’ is the inside diameter of the shell of a shell and tube heat exchanger, then the baffle spacing is usually in the range of

A

D/5 or minimum 2” to 5D.

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18
Q

Brass valves are usually made for pipe sizes __________ inches.

A

≤2

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19
Q

At the following point for a given packing and set of fluids, the pressure drop per metre of packed height, with variation in fluid rates and operating pressure

A

remains same

20
Q

In a shell and tube heat exchanger, triangular pitch arrangement as compared to square pitch arrangement

A

results in higher shell side pressure drop.

21
Q

Pick out the wrong statement about routing of fluids in a shell and tube heat exchanger.

A

Higher pressure fluid stream should be routed through the shell side.

22
Q

The necessary wall thickness for a metallic storage vessel is a function of the
A ultimate tensile strength (or yield point) of the material and operating temperature.
B operating pressure and welding/joint efficiency.
C diameter of the vessel.
D all (a); (b) and (c).

A

all (a); (b) and (c).

23
Q

In a multiple effect evaporator system having ‘n’ effects, the amount of water evaporated per unit surface area in approximately equal to __________ times that in a single effect.

A

(1/n)th

24
Q

Pick out the wrong statement
A. In a flanged and standard dished head, the crown radius is ≤ shell outside diameter.
B. In a flanged and shallow dished head, the crown radius is > shell outside diameter.
C. Flat head covers are most suitable for larger vessels operating at very high pressure.
D. Flanged only head is a type of flat head in which gradual change in the shape at the centre results in reduced local stresses.

A

C

25
Q

Pick out the wrong statement pertaining to the design of a horizontal tube evaporator.

A

Liquor flows inside the tube, while the steam is outside submerging the tube.

26
Q

Weep holes provided in the plates of a distillation column
A. facilitate draining out liquid from a tray when the unit is not in operation.
B. are normally located near the overflow weir so that any delivery of liquid during operation follows approximately the same path as the overflow fluid.
C. must be large enough (usually 1/4” to 5/8” dia) to prevent plugging but should not deliver excessive amount of fluid during operation.
D. all (a), (b) and (c).

A

D

27
Q

Steam is preferred to be used as a heating medium in heat exchangers, because of its

A

high latent heat.

28
Q

__________ shapedroof is the most commonly used roof for cylinderical storage tanks.

A

Conical

29
Q

Pick out the wrong statement pertaining to ‘Horton sphere’ used for the storage of liquid ammonia.

A

Horton sphere is used for the storage of liquid at sub-zero temperature at very high pressure upto 200 kg/cm2.

30
Q

Value of Peclet number = ∞, is the representative of

A

plug flow.

31
Q

In most of the shell and tube heat exchangers, the tube pitch is generally __________ the tube diameter.

A

1.25-1.50 times

32
Q

Accidents in chemical plants are mostly due to

A

faulty operating procedures.

33
Q

In a distillation column, bubble caps are located on trays with a pitch of __________ times the outside diameter of the caps.

A

1.3 to 2

34
Q

1.2 to 3.8 cms is the value of the
A. downcomer liquid seal in case of a balanced tray design.
B. static submergence in case of a bubble cap tray for column operating under pressure (≥ 1 atm.).
C. skirt clearance for bubble caps.
D. all (a), (b) and (c).

A

D

35
Q

For identical operating conditions, the pressure drop over __________ tray is the highest out of the following.

A

bubble cap

36
Q

A perforated plate has holes of diameter dn arranged in a pitch ph. Each hole has a tube of I.D. dt passing through it. The ligament efficiency is given by

A

(ph - dt)/ph

37
Q

__________ is the determining factor for the number of bubble caps to be used per tray.

A

Permissible slot velocity

38
Q

Pick out the wrong statement about distillation operation

A

Flash distillation, differential distillation & steam distillation are all continuous distillation processes.

39
Q

Low pressure steam (with saturation temperature between 105 to 120°C) is usually used in the vacuum evaporators, which normally employ a vacuum of about __________ mm Hg (referred to a 760 mm mercury barometer).

A

650

40
Q

Which of the following is the best tube material from thermal conductivity point of view alone?

A

Copper

41
Q

Normal screwed fittings are used for pipes upto a diameter of __________ inches.

A

3

42
Q

In a shell and tube heat exchanger, the clearance of the tube is generally

A

not less than one-fourth of the tube diameter or 3/16”.

43
Q

Diameter of the seive tray column is determined by the

A

upper limit of the vapour velocity.

44
Q

For a given fluid, as the pipe diameter increases, the pumping cost

A

decreases.

45
Q

Maximum acceptable total liquid gradient over a tray is about __________ mm.

A

12.5

46
Q

In case of a ‘thin’ pressure vessel, the ratio of its diameter to wall thickness is

A

> 10

47
Q

High pressure fluid in a shell and tube heat exchanger should preferably be routed through the

A

tubes to avoid the expansion of high pressure shell construction.

48
Q

Bubble cap tray is the most commonly used tray in large distillation column, because

A

of its flexibility and nearly constant efficiency under varying conditions of operation.