The Effect of Ethanol, Methanol, and Water on the Hydrolytic Degradation of Polyamide-11

The Effect of Ethanol, Methanol, and Water on the Hydrolytic Degradation of Polyamide-11

W&M ScholarWorks Undergraduate Honors Theses Theses, Dissertations, & Master Projects 5-2016 The Effect of Ethanol, Methanol, and Water on the Hydrolytic Degradation of Polyamide-11 Patrick Smith College of William and Mary Follow this and additional works at: https://scholarworks.wm.edu/honorstheses Part of the Polymer Chemistry Commons Recommended Citation Smith, Patrick, "The Effect of Ethanol, Methanol, and Water on the Hydrolytic Degradation of Polyamide-11" (2016). Undergraduate Honors Theses. Paper 965. https://scholarworks.wm.edu/honorstheses/965 This Honors Thesis is brought to you for free and open access by the Theses, Dissertations, & Master Projects at W&M ScholarWorks. It has been accepted for inclusion in Undergraduate Honors Theses by an authorized administrator of W&M ScholarWorks. For more information, please contact [email protected]. THE EFFECT OF ETHANOL, METHANOL, AND WATER ON THE HYDROLYTIC DEGRADATION OF POLYAMIDE 11 Patrick Smith Bachelor of Science, the College of William and Mary 2016 A Senior Honors Thesis Presented for a Bachelor of Science Degree in Chemistry from The College of William and Mary Department of Chemistry The College of William and Mary 2016 Abstract Polyamide 11 (PA11) is commonly used in offshore oil pipelines due to its excellent mechanical properties and chemical resistance. However, PA11 is prone to hydrolysis which is known to significantly reduce the lifetime of these pipelines. This paper explores the effect of ethanol and methanol, two alcohols that are commonly used to prevent the formation of ice-like blockages in the pipeline, on the hydrolytic degradation of PA11. No significant differences in crystallinity were observed between the different test environments. However, PA11 aged in EtOH showed the lowest amount of hydrolytic degradation when compared to PA11 aged in MeOH or pure DI water. iii Acknowledgements Professor David Kranbuehl John-Andrew Samuel Hocker Professor Christopher Abelt Professor Kristin Wustholz Professor Hannes Schniepp Chemistry Department at the College of William and Mary Roy Charles Center Friends, Family, and Colleagues in Lab iv Table of Contents Chapter Page Number 1. Introduction……………………………………………………………………………………………………..….....1 2. Materials and Methods…………………………………………………………………………………………...5 2.1. Synthesis and Preparation of PA-11: neat…………………………………………………………5 2.2. Preparation of Commercial PA-11: NKT…………………………………………………………….5 2.3. Accelerated Aging Study…………………………………………………………………………………….6 2.4. Characterizing Aged Coupons…………………………………………………………………………….7 2.4.1. Molecular Weight Measurements and Hydrolysis Model…………………………7 2.4.2. Crystallinity Measurements…………………………………………………………………….12 2.4.3. Absorbed Liquid Content…………………………………………………………………………13 3. Results……………………………………………………………………………………………………………………..15 3.1. Molecular Weight Data and Rate Constants……………………………………………………….15 3.2. Crystallinity Data………………………………………………………………………………………………..27 3.3. Absorbed Liquid Data…………………………………………………………………………………………30 4. Discussion…………………………………………………………………………………………………………………34 4.1. Molecular Weight and Rate Constants……………………………………………………………….34 4.2. Crystallinity………………………………………………………………………………………………………..37 4.3. Absorbed Liquid…………………………………………………………………………………………………37 5. Conclusion………………………………………………………………………………………………………………..38 v References………………………………………………………………………………………………………………………39 vi Chapter 1: Introduction Polyamide 11 is one of the most widely used polymers for the liner in flexible offshore oil pipelines throughout the world. This thermoplastic is utilized because of its excellent mechanical strength, elasticity, and chemical resistance.1 PA11 is made of many 11- aminoundecnoic acid monomer units, each having an amine end and a carboxylic acid end. The carboxylic acid end (-CO2H) of one monomer unit attaches to the amine end (-NH2) of another monomer unit forming long chains via amide bonds. Although ten of the eleven carbons in each monomer unit are essentially the same as polyethylene (-CH2 repeat unit), the amide groups give rise to PA11’s excellent physical and mechanical properties by allowing molecular interactions such as hydrogen bonding.2 Furthermore, amides are the least reactive of the neutral carboxylic acid derivatives with the only possible interconversion reaction being hydrolysis back to the parent carboxylic acid and amine.3 Since PA11 does not readily react with hydrocarbons, it is the optimal choice for the transport layer in an offshore oil pipeline. Figure 1.1: Top: 11-aminoundecanoic acid monomer Bottom: PA11 repeat unit 1 In offshore oil and natural gas pipelines, about 70% of flow assurance problems come from the formation of gas hydrates.4 Gas hydrates are ice-like solids that form when small gases, like ethane or methane, combine with water at low temperature and high pressure. Under these conditions, water molecules are able to hydrogen bond with one another and form crystalline lattices around gas molecules. These gas molecules stabilize the water molecules allowing crystallization above the freezing point of water. Gas hydrates represent a severe operational problem as the hydrate crystals deposited on the pipe walls accumulate as large plugs. This leads to pressure build-up and eventually rupture of the pipe. Since the removal of hydrate plugs is both time consuming and costly, steps are taken to prevent the formation of gas hydrates.5 The most common hydrate prevention technique is the use of chemical inhibitors. Chemical inhibitors - such as methanol and ethanol - displace the hydrate formation point to a temperature and pressure outside of the normal operating conditions of the pipes.5 In general, efficiency of inhibitors is inversely proportional to the molecular weight, making methanol more efficient than ethanol. In addition to its high efficiency, methanol is typically the most available and cost effective, making it the most commonly used hydrate inhibitor in the oil and gas industry. The work in this thesis will investigate the effect that the gas hydrate inhibitors methanol and ethanol have on the degradation of PA11. Degradation of PA11 occurs when the amide linkages breakdown, resulting in shorter polymer chains with lower molecular weights. There are many reactions that can initiate the degradation of PA11. The most common form of degradation of PA11 is oxidation, which can be induced either by high heat or ultraviolet radiation in the presence of atmospheric oxygen. Both 2 thermal and photo-induced oxidation disrupt the reformation of amide bonds by altering the amine or acid end-groups. This typically occurs via formation of free radicals or peroxides. As mentioned before, PA11 is also susceptible to hydrolytic degradation. Hydrolytic degradation occurs when an amide bond is split into an amine and a carboxylic acid upon reaction with water. Offshore oil pipelines are typically not exposed to high heat, oxygen, or ultraviolet radiation, making hydrolytic degradation the predominant form of degradation, and thus the focus of this study. Earlier work by Meyer, suggests that hydrolytic degradation of PA11 approaches an equilibrium between hydrolysis (chain scission) and polymerization (recombination).6 In the forward, recombination, reaction, the amine end attacks the carboxylic acid end resulting in a longer chain polymer. In the reverse, hydrolysis reaction, water attacks the amide bond resulting in two polymer chains of lower molecular weight. The equilibrium reaction of PA11 with the hydrolysis rate constant (kH) and the recombination rate constant (kp) is as follows: Figure 1.2: Overall reaction of polyamides: hydrolysis (to the right) and recombination (to the left). This overall reaction is a result of the reversible elementary steps in the hydrolysis of an amide bond.7 While hydrolysis occurs at the amide bond, polymerization can also occur as the newly exposed acid end group can recombine with a nearby amine end group. Until equilibrium is reached, one of these two competing reactions occurs at a faster rate depending on the 3 concentration of reactants, resulting in a change in molecular weight. At equilibrium, the rate of the forward reaction is equal to the rate of the reverse reaction resulting in no net change in 6 molecular weight; this is called the equilibrium molecular weight (Mwe). By monitoring the molecular weights as a function of time, the degradative effects of ethanol, methanol and deionized water (DI) were studied. 4 Chapter 2: Materials and Methods 2.1 Synthesis and Preparation of PA11: neat Pure PA11 was synthesized in the laboratory. To synthesize the polymer, 11- aminoundecanoic acid powder was evenly spread onto a Teflon-lined 100 x 15 mm soda lime glass petri dish. This dish was then placed into an oven at room temperature which was then flooded with Argon to remove any ambient oxygen from the system. Oxygen at high temperatures changes the chemical structure of PA-11 through oxidation and is therefore removed prior to polymerization. Upon establishment of an anaerobic environment, the oven was ramped to 240oC, held for four hours, then returned back to room temperature. To make the polymer a uniform thickness, the resulting block of PA11 was heat pressed into a 0.50mm film via a Model C Carver Hydraulic Laboratory Press. The process for pressing the PA11 is as follows, the polymer was sandwiched between two Teflon-lined metal plates, which was then placed into a chamber made of PTFE Teflon film. Then the Teflon chamber was flooded with Argon and heated 180oC for 20 minutes, which is well

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