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KATALIS

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Academic year: 2023

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NUR ISTIANAH,ST,MT,M.Eng

KATALIS

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Outline

Definisi, Jenis-jenis, Klasifikasi katalis Katalis homogen

Reaksi katalisis Katalis Heterogen Deaktivasi katalis

Katalis dalam Industri, dan bidang lainnya Pengenalan reaktor dan bioreaktor

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Definition

• Catalyst is a foreign material that hinder or accelerate the reaction process by a factor of a million or much more. It need not be pr esent in large amounts.

• The man-made catalysts, mostly solids, usually aim to cause the high-temperature rupture or synthesis of materials. These reactions play an important role in many industrial processes, such as the production of petrochemicals, polymers, and plastics.

• It is estimated that well over 50% of all the chemical products produced today are made with the use of catalysts.

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Definition

Catalyst types:

• Porous(the slolid contains many fine pores, a nd the surface of these pores suppIies the a rea needed for the high rate of reaction)

• Monolithic/honeycomb/supported (continuo us unitary structures containing many narro w, parallel and usually straight passages)

• Molucular sieve(Sometimes pores are so sm all that they will admit small molecules but prevent large ones from entering)

• Coated surface

• Living cell or enzyme(biocatalyst)

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1

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Role of catalyst

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Catalytic reaction

Homogenious Heterogenious

Example

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Catalytic reaction

• Some reaction need to use catalyst such as Ha logenation-dehalogenation, Hydration-dehydrat ion, Hydrogenation-dehydrogenation, Oxidation , Isomerization, Alkylation-dealkylation

(Foggler)

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Catalyst

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Heterogeneous catalyst

• Since more than one phase is present, the mass transfer of material from phase to phase must b e considered in the rate equation

• Example: burning reaction

• C + O2  CO2

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Heterogeneous catalyst

• So do with aerobic fermentation

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Mecanism of catalytic reaction

1. Mass transfer (diffusion) of the reactant(s) from the bulk flu id to the external surface of the catalyst pellet

2. Diffusion of the reactant from the pore mouth through the catalyst pores to the immediate vicinity of the internal cat alytic surface

3. Adsorption of reactant A onto the catalyst surface 4. Reaction on the surface of the catalyst

5. Desorption of the products from the surface

6. Diffusion of the products from the interior of the pellet to the pore mouth at the external surface

7. Mass transfer of the products from the external pellet surfa ce to the bulk fluid

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Mecanism of catalytic reaction

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Catalytic reaction

• However, each type has different reaction control (that are dominant in influencing reaction)

• Surface reaction, mass transfer, and alsotemperat ure may affect the rate of catalytic reaction

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Homogeneous catalyst

A homogeneous reaction is one that involves only on e phase.

Contribution of homogeneous catalytic process in c hemical industry is significantly smaller compared to heterogeneous catalytic process, it is only about 17-20

%.

The significance of homogeneous catalysis is growing rapidly particularly in the area of pharmaceutical and polymer industry.

Some of the important industrial processes include: 1.

Oxidations of alkenes such as production of acetalde hyde, propylene oxide etc. 2. Polymerization such as production of polyethylene, polypropylene or polyest ers

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Homogeneous catalyst

• In homogeneous catalysis, all the reactants and c atalysts are present in a single fluid phase and us ually in the liquid phase.

• Homogeneous catalysts are the simple molecules or ions such as HF, H2SO4, Mn+2 as well as com plex molecules such as organometallic complex es, macrocyclic compounds and large enzyme molecules

• During one catalytic cycle, the catalyst may pass through several intermediate forms and finally pr oduce the products. After end of each catalytic cycle, the catalyst itself should be regenerated wi thout any change

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Catalysis by Organometallic complexes

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HOMOGENEOUS CATALYST

- general acid and base catalysis (ester hydrolysis),

- Lewis acids as catalysts (Diels-Alder reactions). B6,

- organic catalysts (thiazolium ions in

Cannizzarro reactions of polyols(sweetener) - porphyrin complexes (epoxidations,

hydroxylations), acid production,

- enzymatic processes, (polyester condensations).PET

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NUR ISTIANAH,ST,MT,M.Eng

KATALIS(II)

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Catalyst Deactivation

Costs to industry for catalyst replacement and process shutdown total billions of dollars per year.

catalyst deactivation id inavitable(can not be avoided) for most processes

The loss over time of catalytic activity and/or selectivity, is a problem.

Slow down the deactivation please!

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Mechanisms of Deactivation

• Sulfur, arsenic, phosphorous, and selenium

Poisoning

• crystallite growth, support and pore collapse

Thermal degradation

• Atomic or polymeris Carbon, coke

Fouling

• Volatile metal carbonyl

Vapor formation

• Cause sintering and others

Solid reaction

• Mechanical failure

crushing

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Mechanisms of Deactivation

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Poisoning

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Fouling

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Fouling

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Sintering

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Chemical reaction

• (1) reactions of the vapor phase with the catal yst surface to produce (a) inactive bulk and sur face phases (rather than strongly adsorbed spe cies), (b) volatile compounds that exit the catal yst and reactor in the vapor phase, or (c) sinter ing due to adsorbate interactions, that we call chemical-assisted sintering to distinguish it fro m thermal sintering previously discussed;

• (2) catalytic solid-support or catalytic solid-pro moter reactions, and

• (3) solid-state transformations of the catalytic

phases during reaction.

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Vapor formation

volatile

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Vapor formation

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Crushing

• (1) crushing of granular, pellet, or monolit hic catalyst forms due to a load in fixed b eds;

• (2) attrition, the size reduction, and/or br eakup of catalyst granules or pellets to pr oduce fines, especially in fluid or slurry b eds; and

• (3) erosion of catalyst particles or monolit

h coatings at high fluid velocities in any r

eactor design.

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Effects of deactivation

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Prevention

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Regeneration

• Despite our best efforts to prevent it, the loss of catalytic activity in most processes is inevita ble. When the activity has declined to a critical level, a choice must be made among four alter natives:

• (1) restore the activity of the catalyst

(regeneration)

• (2) use it for another application,

• (3) reclaim and recycle the important and/or ex pensive catalytic components, or

• (4) discard the catalyst.

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Regeneration

• The ability to reactivate a catalyst depends upo n the reversibility of the deactivation process.

• carbon and coke formation is relatively easily r eversed through gasification with hydrogen, w ater, or oxygen.

• Sintering is generally irreversible and hard to b e regenerated

• Some poisons or foulants can be selectively re

moved by chemical washing, mechanical treat

ments, heat treatments, or oxidation

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Catalytic reactor

Fixed bed

Fluidized bed Moving

bed

Need more catalyst, efficient contacting

Effective temperature control, good product distribution

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Catalytic reactor

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Catalytic reactor

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Catalytic

reactor

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NUR ISTIANAH,ST,MT,M.Eng

THANK YOU

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