Solid Mixing Flashcards

1
Q

Occurs when the granular bed undergoes solid body rotation and then slides, usually intermittently, against the rotating tumbler walls.

A

The Slipping Regime

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2
Q

In this regime, flow consists of discrete avalanches that occur as a grouping of grains travel down the free surface and come to rest before a new grouping is released from above.

A

Avalanching flow, also referred to as slumping

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3
Q

At higher tumbling speeds, discrete avalanches give way to continuous flow at the surface of a blend (Shinbrot et al., 1999a). Grains beneath this surface flowing layer rotate nearly as a solid body with the blender until they reach the surface.

A

Rolling

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4
Q

As the rotation
speed of the tumbler is increased, the surface becomes increasingly sigmoidal until grains become airborne, and at higher speeds yet, the grains centrifuge against the tumbler wall.

A

Cascading, Cataracting, and Centrifuging

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5
Q

Exhibit stick-slip motion so that flow becomes intermittent rather than continuous. This is a situation of practical importance since most industrial applications use particles across a broad range of sizes and materials.

A

Weakly Cohesive Material

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6
Q

Processing blends of dissimilar grains almost invariably promotes ________, characterized by the spontaneous emergence of regions of nonuniform
composition.

A

de-mixing, also referred to
as segregation

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7
Q

Large grains rapidly segregate radially, producing a central core of fine grains surrounded by larger grains.

A

Radial De-mixing

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8
Q

A second stage of segregation occurs in drum tumblers as grains in the core migrate along the tumbling axis. Numerical and experimental investigations have attributed this migration to conflicting causes.

A

Axial De-mixing

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9
Q

These patterns are believed to arise from a competition between surface segregation of coarse grains flowing over a radially segregated core of fine grains and interactions with the boundaries of the tumbler.

A

Competitive Patterned De-mixing

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10
Q

Three of the most common geometries
used in pharmaceutical operations are the:

A

Double cone
V-blender
Bin blender

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11
Q

In these simulations, particles are treated as individual entities with physical properties
appropriate to the problem of interest, and Newton’s laws of motion are integrated for each particle.

A

Particle-dynamic simulations

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12
Q

Two of the most common classes of particle-dynamic simulations are termed:

A

Hard-particle and Soft-particle methods

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13
Q

calculate particle
trajectories in response to instantaneous, binary collisions between particles, and allow particles to follow ballistic trajectories between collisions.

A

Hard-particle methods

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14
Q

allow each particle
to deform elastoplastically and compute responses using standard models from elasticity and tribology theory. This approach permits enduring particle contacts and is therefore the method of choice for tumbler applications.

A

Soft-particle methods,

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15
Q

The faster and more efficient mixing mechanism, yet at the same time it suffers from the same mixing limitations known for
fluids

A

Convection in grains (as in fluids)

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16
Q

Transport associated with flow driven by gravity (in
tumbling blenders) or impellers (in intensified, ribbon, or
other blenders).

A

Convection in the context of granular blenders

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17
Q

The random
relocation of individual grains due to collisions
between adjacent particles and can take hundreds to thousands of revolutions to act.

A

Dispersion, or diffusion

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18
Q

The second class of blenders commonly used in industrial applications_______. It
primarily mix by transporting materials throughout a mixing
vessel by the motion of a stirring device.

A

Convective Blenders

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19
Q

It is one of the most common general-purpose mixers, as it can effectively perform a wide range of mixing processes including
liquid, solid, and liquid-solid blending.

A

Ribbon Blender

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20
Q

Scope of Solid–Solid Mixing (5):

A
  1. Mixing of product for homogenization of quality or reduction of variance
  2. Mixing of active ingredient onto a carrier material
  3. Mixing of multicomponent mixtures as a formulation
  4. Coating of a cohesive component onto a carrier particle
  5. Mixing of fine powders to create a homogeneous mixture at the particulate level
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21
Q

Any sample randomly taken from the mixture will contain the same proportion of each particle as the proportions present in the mixture taken as a whole.

A

Perfect Mixture or Perfect mixture of two types of particles

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22
Q

When two non-interacting components (e.g., free-flowing pellets) with similar properties (size,
shape, elasticity,etc.) are mixed in an ideal mixer, the quality of mixing reaches an asymptotic
limit of random mixing.

A

Random or Stochastic Mixture

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23
Q

When two interacting components are mixed together, a structure or order can build up into the mixture. The units ordered could be a result of agglomeration or cohesion of one component to the other or a mixture of the two.

A

Ordered Mixture

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24
Q

Once the cohesive fraction or minor component saturates available sites on the carrier particles, the remaining fraction will agglomerate.

A

Partially Ordered Random Mixture

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25
Q

When the ordered units contain different numbers of adherent particles and the carrier particles are randomly mixed.

A

Pseudorandom Mixture

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26
Q

Mixing ingredients in any amount in individual batches in an individual mixer or a vessel. All ingredients are loaded into a mixer and agitated for a certain period until
they are homogeneously distributed or mixed.

A

Batch Mixing

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27
Q

Used to mix ingredients continuously in a mixer in a single pass. The
ingredient quantity to be mixed may vary in any range.

A

Continuous Mixing

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28
Q

Occurs due to small scale random motion of particles when they roll over a free surface.

A

Diffusive mixing

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29
Q

In _________, High-Shear Mixers are used for texture and enduring the stability of condiments such as dressings, mayonnaise and sauces.

A

Emulsions

30
Q

The dust arising from the mixing or processing of combustible solid materials can form explosive mixtures with air. In the design of plants to handle such materials, consideration must be given to the potential for dust explosions and actions to prevent or minimize dust explosions.

A

Process Safety in Solids Mixing

31
Q
A
32
Q

In addition to taking specific explosion prevention and protection steps, the conditions that can result in a secondary explosion and the frequency of ignition must be minimized.

A

General Design Safety

33
Q

Who proposed the variance reduction ratio?

A

Danckwerts

34
Q

They carried out detailed investigations using a continuous mixer.

A

Weinekotter and Gericke

35
Q

The output concentration was monitored using an _____

A

Optical Probe

36
Q

It refers to the volume of solids in the mixer at any instant.

A

Retention Volume

37
Q

There are two types of Ribbon mixers which are vertical and horizontal ribbon mixers. What is the specific percentage for the vertical ribbon mixer to operate?

A

90%

38
Q

Employ a plow-shaped agitator that travels along the bottom of a U-shaped trough, pushing and folding the material during rotation.

A

Plow mixers

39
Q

This type of mixer consists of a _________ and a screw feeder placed along the wall.

A

Hopper shaped vessel

40
Q

Mixing time for Plow mixer

A

Up to 5 min with random mixing.

41
Q

When two orbiting screws are used, one screw is normally shorter and is called________

A

Satellite screw

42
Q

The mixing action of _________ is due to velocity gradients generated during discharge and recirculation of material

A

Silo Blenders

43
Q

Blender Power Consumption of Gravity system, Single Inverted Cone

A

0.25-0.5

44
Q

Blender Power Consumption of Gravity system, Multioutlet

A

0.1-0.13

45
Q

High Intensity Mixers, serves as handy equipment in the mixing of low viscosity miscible liquid to even the dispersion in ________ application.

A

Adhesive and sealant production

46
Q

For dust to explode, certain conditions have to exist:

A
  1. Particles of dust must be of suitable size.
  2. Concentration of dust in the air must fall within explosive limits.
  3. There must be a source of ignition energy.
47
Q

______________ focused on the petrochemical industry to blend plastic granules in large quantities, particularly for obtaining uniform product quality.

A

Pneumatic blender (Krambrock, 1976)

48
Q

Blender Power Consumption of Gravity Air fluidized system.

A

1-1.5

49
Q

The mixing action in the blender can be achieved by fluidizing the contents. the fluidization creates bubbles in the bed, except for__________ .

A

C-type powders

50
Q

These mixers are commonly preceded by a convective tumbler mixer to provide a reasonable quality before the product is conditioned.

A

High-Shear Mixers

51
Q

The Energy consumption for a paddle mixer is_______

A

150 kW/m3

52
Q

Use mechanical means (e.g., paddles, plows, and ribbons) to create mixing action while keeping the shell stationary.

A

Agitating mixers

53
Q

( T OR F)
Unlike immiscible liquid systems, the density differences play a relatively minor role in de-mixing or segregation of particulate mixtures.

UNDERLINED: DENSITY

A

TRUE

54
Q

(T OR F)
The units ordered could be a result of agglomeration or separation of one component to the other or a mixture of the two

UNDERLINED: SEPARATION

A

FALSE Answer: COHESION

55
Q

(T OR F)
Defined by a Variance of the sample composition equal to zero provided that the sample size is greater than one ordered unit

UNDERLINED: VARIANCE

A

FALSE Answer: Standard deviation

56
Q

(T OR F)
It should be noted that an ordered mixture can have a variance higher than that of a random mixture

UNDERLINED: HIGHER THAN

A

FALSE Answer: Less than

57
Q

(T OR F)
Pseudorandom mixtures show the degree of homogeneity but not the fully disordered texture of random mixtures

UNDERLINED: HOMOGENEITY

A

TRUE

58
Q

If powders exhibit expansion characteristics when aerated, they may be a good candidate for ______________.

A

Pneumatic Blenders

59
Q

___________ normally have recirculation systems either within the blender or placed outside it. This is required to allow all the mixed material to flow out of the blender.

A

Mechanical blenders

60
Q

Determining mixture quality depends on

A

Size

61
Q

Baffles and asymmetric designs in blenders are used to improve_____

A

Convection and rapid mixing

62
Q

9.The most important factor for mixing rate in tumbling blenders is:

A

Loading protocol (top/bottom vs left/right)

63
Q

When scaling down a cohesive mixture, the biggest challenge is:

A

Decreased shear forces

64
Q

According to the passage, what is the minimum particle diameter ratio that can cause radial segregation?

A

1.3

65
Q

What design consideration is important for optimal mixing in tumbling mixers?

A

The charging process and reduction of lumps are crucial.

66
Q

Which mechanism of segregation is caused by the size difference of particles?

A

Trajectory segregation

67
Q

Which type of tumbling mixer utilizes a V-shaped vessel for rotation?

A

Double cone blender

68
Q

A measure of the degree of mixing is the Lacey Mixing Index

A

Mixing Indices

69
Q

Hard-particle methods in simulations are suitable for:

A

Slow dispersive mixing

70
Q

When scaling up a free-flowing mixture, the most important consideration is:

A

Loading conditions and vessel size