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Scale-up Batch Chemical Reactors

06/30/2014 10:01 AM

Hi All,

We have a chemical reactor, a batch reactor. We add ingredients, then put steam in the reactor's jacket to promote the chemical reaction, and once the reaction gets going, since it is exothermic, we put cooling water in the jacket.

They work pretty well. Good enough that we'd like to install more reactors... but 50% larger; or 100% larger. Here's the question: If you know the size and reaction cycle time (start of the process until completion and dumping of reactor) all else being equal, what is the reaction time of a 50% larger reactor? Of a 100% larger reactor?

The existing reactors are 48" Dia x 14' Long. Reaction takes 2.5 hours. Also have reactors that are abit shorter at 12'. I can find their reactor cycle time. Not yet sure of the new reactor dimensions.

Any thoughts on scaling up the reactor cycle time?

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#1

Re: Scale-up Batch Chemical Reactors

06/30/2014 10:55 AM

There is a problem with scaling-up an exothermic process: the heat relased goes up with length cubed, however the cooling surface goes up with length squared. So unless the exotherm can be "caught" by the cooling system on a larger vessel, it makes more sense to install multiples of a vessel size that works rather than larger ones, lest a thermal runaway should reduce the plant to a pile of stinking, smouldering scrap.

Increasing the size of inventory in the plant runs contrary to the principle of Inherent Safety championed by the late Dr. Trevor Kletz, a world-renowned safety guru. If there is a way of converting the process into a continuous one, rather than a batch one, then this will reduce the inventory in the plant. "What you don't have cannot leak" - DrTK.

So this is a project for a qualified and experienced Process Engineer. If one is not on the books, then hire a Consultant; it will be money well-spent.

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#2
In reply to #1

Re: Scale-up Batch Chemical Reactors

06/30/2014 11:40 AM

PW,

Thanks for the reply. Fortunately, the reactants are innocuous, mainly food-grade. But you point is still well-taken.

If we hold the diameter constant, the heat released would be a linear function of the length; that is, double the length, double the volume, double the reactants, double the heat released.

But I think you are putting me on the right track. I will try to get my volume increase by longer length more than larger diameter.

RM

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#3
In reply to #2

Re: Scale-up Batch Chemical Reactors

06/30/2014 12:41 PM

No. Stop. Hire someone.

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#9
In reply to #3

Re: Scale-up Batch Chemical Reactors

07/01/2014 6:38 PM

"No Stop Hire Someone"

Wow, you attended the Lyn charm school. Nice thanks very helpful

Couldn't have done it without you.. wow I am so glad I posted the question.\|

Cant ask a Q without "No Stop Hire Someone" from you or Lynn it seems.

I AM ASKING the Q, just asking. And who thinks that volume is a cubed function of length? Plse raise your hands. Yes, you guys get to go back to algebra class.

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#13
In reply to #3

Re: Scale-up Batch Chemical Reactors

07/01/2014 7:07 PM

PW,

I am re-reading my original post. Where do you get the idea "stop holly cow before something blows up"? Wow, over-reacting (pardon the pun).

It was an innocent basis information gathering question. Nothing to blow up quite yet, no smoldering ruins burning to the core of the earth, limbs flying everywhere. Like a Godzilla movie, perhaps worse. Oh, the humanity.

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#4
In reply to #2

Re: Scale-up Batch Chemical Reactors

06/30/2014 8:01 PM

"all else being equal"

If you increase the size of the reactor all isn't equal any more. you may get away with increasing the length and keeping all else equal.

I agree with PWSlack, you need the help of a chemist or process person.

The reaction rate is a critical unknown here.

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#5
In reply to #2

Re: Scale-up Batch Chemical Reactors

07/01/2014 8:06 AM

longer still means that the heat generated will exceed the interior surface area to transfer the heat to the cooling jacket. you need to go smaller diameter and longer, or insert some kind of cooling loop inside the reactor vessel. listen to these guys and hire someone who knows what he is doing. Even food grade reactants in an exothermic reaction can cause a fire or explosion due to overheating.

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#10
In reply to #5

Re: Scale-up Batch Chemical Reactors

07/01/2014 6:42 PM

"listen to these guys and hire someone who knows what he is doing. "

I could use some choice words here. It is a simple Question I asked.. does anyone have experience with the particular problem. You think I am going to design a reactor based on the snide comments of strangers? Wow, nice forum. Very helpful and extremely friendly. Oh, wait that could be mis-understood. I am being sarcastic.

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#6

Re: Scale-up Batch Chemical Reactors

07/01/2014 8:59 AM

There are some important questions that you need to answer, that will answer your own question. They'll also give you an idea of the safety factor:

  1. what is the reaction kickoff temperature, what is the specific heat output of the reaction, is there a desired mean reaction temperature and what is the desired maximum temperature?
  2. is the current equipment easily capable of maintaining these process conditions or is it strained (eg. cooling system barely able to keep up, is temperature control adequate, etc.)? Is the reaction being run at ideal conditions or is it at a lower temperature/ pressure because it can't control the exotherm of a reaction at full capacity and ideal conditions?
  3. Are you looking at similar reactor designs (eg. glass lined) or is there another option that may have better heat transfer, or could a side arm heat exchanger be installed (potentially for safety reasons as well as speeding up initial heating). Exchange surface area can be obtained in more ways than just reactor walls.
  4. What cooling water/steam temperature levels and flow rates are available and how controllable are they?
  5. a big consideration is always pressure/ vacuum levels that may be required in these processes.
  6. ADEQUATE AGITATION RULES!! Shear sensitivity of your product has to be considered in determining the type of agitation, but the important thing is to be able to transfer product to and away from the heat exchange surfaces and blend it consistently throughout the reaction mass, in order to maintain a consistent overall temperature and reduce both hot spots and the overall temperature gradient away from the cooling areas (usually the centre of the reaction mass is the hottest. VERY important when scaling up.), as well as being capable of doing this throughout all possible viscosities that may occur during the reaction.
  7. Since you have 2 different size reactors have you compared the reaction times and determined if they are the same or different? You should be able to extrapolate from there for a baseline idea.

Previous posts have made good points, but the question you asked was not safety related (although this is still always important), and it's actually not what you should be asking as a manufacturer. Chemical reactions generally have a rate that may be controlled by conditions such as pressure/ temperature, and the mass is more likely to affect the controllability rather than the rate. So as an example- if your products are adequately blended and then you require a 30 minute induction period (steam heating), followed by a 2 hour reaction time, and you scale the mixer up by doubling the length (essentially similar exchange areas) with proportionate mixing it should be essentially the same. If you have to go with a different ratio it may be different- a design with a lower surface area/ volume ratio may take longer to heat (eg. a 45 minute induction period) that will slightly increase this time, while additional heat exchangers could potentially reduce it instead (but do require additional pumps, cleaning etc.). The reaction time may actually decrease with a different design that has a lower ratio as this will tend to run hotter, but will the product quality still be acceptable even if it's still within the safety factors?

So the question that should have been asked before ordering the new reactors was: are we satisfied with the existing reaction rate, levels of process control and quality of finished product or do these need to be improved, and if so what design is needed to accomplish this safely and effectively?

(Sorry for the lecture, but this is what the chemical engineer should have done!!)

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#7
In reply to #6

Re: Scale-up Batch Chemical Reactors

07/01/2014 10:41 AM

It's all about heat transfer rates. Hire someone experienced.

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#11
In reply to #6

Re: Scale-up Batch Chemical Reactors

07/01/2014 6:53 PM

THANK you for an informed answer. This addressed my question. It is very helpful.

To the others, "listen to these guys and hire someone who knows what he is doing. " I see that answer and the answer to do an internet search all the time. The assumption in the "listen to these guys and hire someone who knows what he is doing. " answer is that I am going to fire up the old reactor maker and build one for cheap. I am going to build a reactor, never did it before, but hey what could go wrong? That is gotta be in the mind of someone writing "listen to these guys and hire someone who knows what he is doing. "

I suspect a lot of OP's posting questions on topics they don't know about is they are trying to get to the background considerations. They themselves are not building the equipment they are asking about. they want to learn about the considerations behind a design.


So lets try to not use the "you are a dummy, get someone competent" response.

OK, gurus ?

Thanks

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#8

Re: Scale-up Batch Chemical Reactors

07/01/2014 12:37 PM

There are numerous ways that additional heat reduction can be provided for chemical reactors. Some are: additional agitation (although you didn't say if agitation is used); different materials of construction to one with greater heat conduction if acceptable with materials present and produced such as glass lined to Stainless Steel; use of chilled water instead of ambient; use of a coolant with a higher latent heat capacity; constructing with internal "coolant wings" but only if agitated; increasing coolant surfaces; circulation of the materials through an external heat exchanger in addition to jacket cooling (be very cautious with this method); changing the design of the contact points of the reactor to the jacket (stay bolts vs. dimpled for an example); slower addition of materials if possible; and several others.

I have purposely not given any more than brief details since these decisions should and must be made by a chemical engineer qualified in process engineering. Caution, not all ChE's have this knowledge!

War story to make you very cautious--- I once had to do an accident investigation for a run away exothermic reaction. 10,000gal reactor went exo and operators couldn't dump it in time. It exploded, wiped out the control room and other distant structures. One operator was found in several pieces and the wedding ring of the other was all they could find. Caution, caution, caution! Let the qualified make the recommendations and design decisions.

Good Luck, Old Salt

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#12
In reply to #8

Re: Scale-up Batch Chemical Reactors

07/01/2014 7:03 PM

Ha, another helpful response. Thank you indeed Mr Salt, all points are well taken. I will see that these points are addressed by the actual designer/manufacturer.

Absolutely agree to have the qualified make the detailed design. I am simply at the preliminary design stage and only trying to see the effects of scale-up. I am not, repeat not, building a reactor.

I do appreciate your emphasis on the inherent hazards of reactors, without the heavy hand of derision. Perhaps we could learn from your comments in more ways than one.

Rock

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#14
In reply to #12

Re: Scale-up Batch Chemical Reactors

07/02/2014 8:39 PM

RockM....

You are getting some very good advice from those who have posted above, and I agree with those comments.

But I also think it is probably important to discuss a bit the nature of your question and the background of the CH4 discussions.

First, and most importantly, mention an exothermic reaction to most chemical engineers and they get a bit nervous and excited. These types of reactions are responsible for the most deadly, spectacular and career ending accidents in history. So you are treading on sensitive ground.

Secondly, you should know that these for a are littered with newbee technical questions from those who are WAY< WAY over their heads ! ( e.g. I used to weld bicycles, now I want to weld nuclear reactors.... tell me how ?)

Chem-Es feel that the combination of these two things can cause disaster !

Hope that you can understand ???!!

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#15
In reply to #14

Re: Scale-up Batch Chemical Reactors

07/02/2014 11:01 PM

RockM

Agree with you. Also some Chem-E's are not smart enough to realize they have neither of the two points you have listed. A good Chem-E knows the limitations of his/her knowledge and experience, admits it, sticks to it and only does work is qualified for. Additional education/experience is the way to expand his/her pool of knowledge and skills. Fewer exothermal "Oh $hits" that way.

An analogy to this is: In the medical fields, I wouldn't want a proctologist doing cardiac surgery on me!

Good Luck, Old Salt

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