Feeding and blending Flashcards

1
Q

what is the idea continuous feeding and blending units?

A

is to replaced the IBC with the feeding and blending unit (FBU)

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2
Q

what is the advantages of the continuous blender?

A

ensures the homogenity of the powder blend

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3
Q

what are general strenghs of continuous processing?

A

easy to integrate into an existing continuous process
Small footprint (less GMP space)
Less risk of demixing due to small volume, less itermediate tanks
No scale up
cuts off of operating costs
improved product quality (homogeneous shear rate and limite RTD)

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4
Q

which feeder system do we have?

A

Volumetric and gravimetric feeding

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5
Q

what is the main difference volumetric and gravimetric feeding

A

the screw speed is constanst in the volumertic feeding, whereas in the gravimetric feeding the the screw speed is based on the loss of weight

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6
Q

What makes volumetric feeder difficult?

A

it changes the density at a constanst feeding. e..g Amore fedd the feeder is, the higher the bulk density which chould leads to bad zone. Also agglomeration.

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7
Q

what can be done in a case of a agglomeration?

A

inregtration of a cone mill

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8
Q

What

makes proper volumetric feeding challenging

A

Distrurbances resultsing in unequal material flow (feed rate vairation)
-Fill level can have an impact on bulk density
Natrual variation of product bulk density
Formation of dead zones, bridging, agglomeration, which leads to non-uniform filling of feeding too requires more control

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9
Q

What should be used instead of the volumetric feeding?

A

Gravimetric or Loss in Weight Feeding

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10
Q

How

does a Loss In Weight Feeder work

A
  1. Setpoint by the formulation
  2. control unit which set the rpm of the LWF
  3. the Load cell measures the loss of weight of the feeder
  4. the control can calculate how much material is being feeding
  5. Increase of the rmp of te screws, if the setpoint is not reached
  6. Aim is to maintain the constant flow of the material at the outled of the material
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11
Q

What happened if the fill run empty

A
  1. in refill one should be in the steady state as long as possible
  2. Refill of the feeder, we have the increase of weight, weight signal can not be used during the refill process, therefore we switch shortly to the volumetric mood (plus settling time)
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12
Q

what is the NAMUR Na 40 used for?

A

to measure feeder accuracy independently

both refill method and head affect are considered during the test

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13
Q

how is the dosing accuracy in the N 40 defined?

A

as the deviation of the mean value from the nominal value

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14
Q

how is the assessment of the performance of the LWF?

A

it has to be accuracy, by using the NAMUR which meaasures the the consistancy of the feeder flow around the setpoints

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15
Q

whih type of mixing principle do we have?

A

radial and axial mixing

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16
Q

radial mixing?

A

homogeneous bledn particles with each other

17
Q

axial mixing?

A

continuous mixing, detect the variation, bulk density changes

18
Q

How is fluctaution damp out?

A

by the RTD of the blender

19
Q

what happend of the RDT is increased?

A

the bigger the RDT, the better the demp effect of the belnder and still obatin a good quality

20
Q

to obtained the long RDT, the speed has to be lower. what is the conquencey of that?

A

it leads to an increase of the radial mixing , which affects the axial mixing. it’s reduces the variance reduction ratio

21
Q

what is the disavantages of the a higher RDT?

A

the better the blending process will be. But it aslo leads to increase of the blender size,affecting the start up phase (genra out of steck material)

22
Q

what does steady state means?

A

the input through the feeder equal the outcome of the blender. When the input and output is constanst, the mass of the blender is constanst

23
Q

how does a particle behaves inside a continuous blender?

A

each particle moves at a different speed through the blender–> probabality density function

24
Q

on what does the speed of the particle depends?

A

on particle characteristics (shape, size, density, van der waals etc)

25
Q

what happend if the one has difference powder characteristics?

A

if their speed is different through the blender, it can have an impact on startup but also material traceability

26
Q

what is at the SS?

A

the speed of the partciles does differ anymore

27
Q

how can the SS be reached quickly?

A

by using a smaller blender

28
Q

what are some challenges of CM?

A
equipemt complexity
complex formulation (too many ingredients, it's not possible to arrange so many feeders around one blender
29
Q

what are the challenges in low through put rates?

A

limitation of numbers of loss in weight feeders
load cell of loss in weight feeders ( resolution vs accuracy)
Volumetic feed rate of loss in weigh feeder
start up and shut down losses in continuous blender

30
Q

what is better in a low through put rates

A

semi continous or mini batch belnding Approach

31
Q

what are the benefits of CM?

A

higher quality, higher patient safety, faster time to market , reduced cost