Dispersity

(Redirected from Polydispersity index)
A uniform (monodisperse) collection
A non-uniform (polydisperse) collection

In physical and organic chemistry, the dispersity is a measure of the heterogeneity of sizes of molecules or particles in a mixture. A collection of objects is called uniform if the objects have the same size, shape, or mass. A sample of objects that have an inconsistent size, shape and mass distribution is called non-uniform. The objects can be in any form of chemical dispersion, such as particles in a colloid, droplets in a cloud,[1] crystals in a rock,[2] or polymer molecules in a solvent.[3] Polymers can possess a distribution of molecular mass; particles often possess a wide distribution of size, surface area and mass; and thin films can possess a varied distribution of film thickness.[citation needed]

IUPAC has deprecated the use of the term polydispersity index having replaced it with the term dispersity, represented by the symbol Đ (pronounced D-stroke[4]) which can refer to either molecular mass or degree of polymerization. It can be calculated using the equation ĐM = Mw/Mn, where Mw is the weight-average molar mass and Mn is the number-average molar mass. It can also be calculated according to degree of polymerization, where ĐX = Xw/Xn, where Xw is the weight-average degree of polymerization and Xn is the number-average degree of polymerization. In certain limiting cases where ĐM = ĐX, it is simply referred to as Đ. IUPAC has also deprecated the terms monodisperse, which is considered to be self-contradictory, and polydisperse, which is considered redundant, preferring the terms uniform and non-uniform instead.

Overview

IUPAC definition

ĐM = Mw/Mn
where Mw is the mass-average molar mass (or molecular weight) and
Mn is the number-average molar mass (or molecular weight).

Pure Appl. Chem., 2009, 81(2), 351-353

A monodisperse, or uniform, polymer is composed of molecules of the same mass.[5] Natural polymers are typically monodisperse.[6] Synthetic monodisperse polymer chains can be made by processes such as anionic polymerization, a method using an anionic catalyst to produce chains that are similar in length. This technique is also known as living polymerization. It is used commercially for the production of block copolymers. Monodisperse collections can be easily created through the use of template-based synthesis, a common method of synthesis in nanotechnology.[citation needed]

A polymer material is denoted by the term polydisperse, or non-uniform, if its chain lengths vary over a wide range of molecular masses. This is characteristic of man-made polymers.[1]. Natural organic matter produced by the decomposition of plants and wood debris in soils (humic substances) also has a pronounced polydispersed character. It is the case of humic acids and fulvic acids, natural polyelectrolyte substances having respectively higher and lower molecular weights. Another interpretation of polydispersity index is explained in the article Dynamic light scattering (cumulant method subheading). In this sense, the PDI values are in the range from 0 to 1.

The polydispersity index (PDI) or heterogeneity index, or simply dispersity (Đ), is a measure of the distribution of molecular mass in a given polymer sample. Đ calculated is the weight average molecular weight (${\displaystyle M_{w}}$) divided by the number average molecular weight (${\displaystyle M_{n}}$). It indicates the distribution of individual molecular masses in a batch of polymers. Đ has a value equal to or greater than 1, but as the polymer chains approach uniform chain length, Đ approaches unity (1).[7] For some natural polymers Đ is almost taken as unity. Đ (PDI) from polymerization is often denoted as:

${\displaystyle \ PDI=M_{w}/M_{n}}$,

where ${\displaystyle M_{w}}$ is the weight average molecular weight and ${\displaystyle M_{n}}$ is the number average molecular weight. ${\displaystyle M_{n}}$ is more sensitive to molecules of low molecular mass, while ${\displaystyle M_{w}}$ is more sensitive to molecules of high molecular mass.

Effect of polymerization mechanism

Typical dispersities vary based on the mechanism of polymerization and can be affected by a variety of reaction conditions. In synthetic polymers, it can vary greatly due to reactant ratio, how close the polymerization went to completion, etc. For typical addition polymerization, Đ can range around 10 to 20. For typical step polymerization, most probable values of Đ are around 2 —Carothers' equation limits Đ to values of 2 and below.

Living polymerization, a special case of addition polymerization, leads to values very close to 1. Such is the case also in biological polymers, where the dispersity can be very close or equal to 1, indicating only one length of polymer is present.

Effect of reactor type

The reactor polymerization reactions take place in can also affect the dispersity of the resulting polymer. For bulk free radical polymerization with low (<10%) conversion, anionic polymerization, and step growth polymerization to high conversion (>99%), typical dispersities are in the table below.[8]

Polymerization Method Batch Reactor Plug Flow Reactor (PFR) Homogeneous CSTR Segregated CSTR
Free Radical Polymerization (FRP) 1.5-2.0 1.5-2.0 1.5-2.0 1.5-2.0
Anionic Polymerization 1.0 + ε 1.0 + ε 2.0 1.0-2.0
Step-Growth 2.0 2.0 Unbounded (~50) Unbounded (~20-25)

With respect to batch and plug flow reactors (PFRs), the dispersities for the different polymerization methods are the same. This is largely because while batch reactors depend entirely on time of reaction, plug flow reactors depend on distance traveled in the reactor and its length. Since time and distance are related by velocity, plug flow reactors can be designed to mirror batch reactors by controlling the velocity and length of the reactor. Continuously stirred-tank reactors (CSTRs) however have a residence time distribution and cannot mirror batch or plug flow reactors, which can cause a difference in the dispersity of final polymer.

The effects of reactor type on dispersity depend largely on the relative timescales associated with the reactor, and with the polymerization type. In conventional bulk free radical polymerization, the dispersity is often controlled by the proportion of chains that terminate via combination or disproportionation.[9] The rate of reaction for free radical polymerization is exceedingly quick, due to the reactivity of the radical intermediates. When these radicals react in any reactor, their lifetimes, and as a result, the time needed for reaction are much shorter than any reactor residence time. For FRPs that have a constant monomer and initiator concentration, such that the DPn is constant, the dispersity of the resulting monomer is between 1.5 and 2.0. As a result, reactor type does not affect dispersity for free radical polymerization reactions in any noticeable amount as long as conversion is low.

For anionic polymerization, a form of living polymerization, the reactive anion intermediates have the ability to remain reactive for a very long time. In batch reactors or PFRs, well-controlled anionic polymerization can result in almost monodisperse polymer. When introduced into a CSTR however, the residence time distribution for reactants in the CSTR affects the dispersity of the anionic polymer due to the anion lifetime. For a homogeneous CSTR, the residence time distribution is the most probable distribution.[10] Since the anionic polymerization dispersity for a batch reactor or PFR is basically monodisperse, the molecular weight distribution takes on the distribution of the CSTR residence times, resulting in a dispersity of 2. Heterogeneous CSTRs are similar to homogeneous CSTRs, but the mixing within the reactor is not as good as in a homogeneous CSTR. As a result, there are small sections within the reactor that act as smaller batch reactors within the CSTR and end up with different concentrations of reactants. As a result, the dispersity of the reactor lies between that of a batch and that of a homogeneous CSTR.[8]

Step growth polymerization is most affected by reactor type. To achieve any high molecular weight polymer, the fractional conversion must exceed 0.99, and the dispersity of this reaction mechanism in a batch or PFR is 2.0. Running a step-growth polymerization in a CSTR will allow some polymer chains out of the reactor before achieving high molecular weight, while others stay in the reactor for a long time and continue to react. The result is a much more broad molecular weight distribution, which leads to much larger dispersities. For a homogeneous CSTR, the dispersity is proportional to the square root of the Damköhler number, but for a heterogeneous CSTR, dispersity is proportional to the natural log of the Damkohler number.[8] Thus, for the similar reasons as anionic polymerization, the dispersity for heterogeneous CSTRs lies between that of a batch and a homogeneous CSTR.

References

1. ^ Martins, J. A.; Silva Dias, M. A. F. (2009). "The impact of smoke from forest fires on the spectral dispersion of cloud droplet size distributions in the Amazonian region". Environmental Research Letters 4: 015002. doi:10.1088/1748-9326/4/1/015002.
2. ^ Higgins, Michael D. (2000). "Measurement of crystal size distributions" (PDF). American Mineralogist 85: 1105–1116.
3. ^ Okita, K.; Teramoto, A.; Kawahara, K.; Fujita, H. (1968). "Light scattering and refractometry of a monodisperse polymer in binary mixed solvents". The Journal of Physical Chemistry 72: 278. doi:10.1021/j100847a053.
4. ^ Stepto, R. F. T.; Gilbert, R. G.; Hess, M.; Jenkins, A. D.; Jones, R. G.; Kratochvíl P. (2009). "Dispersity in Polymer Science" Pure Appl. Chem. 81 (2): 351–353. DOI:10.1351/PAC-REC-08-05-02.
5. ^ "monodisperse polymer (See: uniform polymer)". IUPAC Gold Book. International Union of Pure and Applied Chemistry. Retrieved 25 January 2012.
6. ^ Brown, William H.; Foote, Christopher S.; Iverson, Brent L.; Anslyn, Eric V. (2012). Organic chemistry (6 ed.). Cengage Learning. p. 1161. ISBN 978-0-8400-5498-2.
7. ^ Peter Atkins and Julio De Paula, Atkins' Physical Chemistry, 9th edition (Oxford University Press, 2010, ISBN 978-0-19-954337-3)
8. ^ a b c Dotson, Neil A.; Galván, Rafael; Laurence, Robert L.; Tirrell, Matthew (1996). Polymerization Process Modeling. VCH Publishers, Inc. pp. 260–279. ISBN 1-56081-693-7.
9. ^ Chanda, Manas (2013). Introduction to Polymer Science and Chemistry: A Problem-Solving Approach, Second Edition. CRC Press. ISBN 978-1-4665-5384-2.
10. ^ Levenspiel, Octave (1999). Chemical Reaction Engineering, Third Edition. John Wiley & Sons. ISBN 0-471-25424-X.