Application of Proprietary Kinetic Hydrate Inhibitors in Gas Flowlines

Abstract

This paper presents the first offshore commercial application of a proprietary kinetic hydrate inhibitor (KHI) developed by Exxon. KHIs are water-soluble, non-toxic1 polymers that inhibit hydrate formation in pipelines at much lower dose rates than methanol or glycol by greatly slowing the rate of hydrate crystal formation. The KHI first underwent laboratory testing in Exxon's 4-in diameter, 275-foot-long hydrate flowloop at pressures up to 1800 psi. It was then field-tested in a 2-in diameter, 1.5-mi-long buried gas flowline in Alberta, Canada in 1996-1997.2 Tests were conducted over a range of salinities and in the presence of methanol and glycol. The offshore KHI application took place in 1998 in an Exxon-operated gas pipeline in the Gulf of Mexico. Before KHI was introduced, the 8-in diameter, 28-mi pipeline required 300 L/day methanol injection to avoid hydrates. KHI injected at 5 L/day inhibited hydrate formation for over six months at approximately 6°F subcooling. Results will be presented for subcooling performance, start-up procedures, operability data, shut-in performance achieved, and cost omparisons to methanol inhibition. The major conclusion of this work is that kinetic hydrate inhibitors are more cost-effective than methanol in many applications. Successful shut-ins and restarts are achievable with kinetic inhibitors. Operability of kinetic inhibitors is similar to methanol. Introduction This paper describes the first offshore demonstration of a kinetic hydrate inhibitor (KHI) developed by Exxon. The KHI is comprised of a water-soluble polymer with the chemical name N-vinyl, N-methyl acetamide-co-vinyl caprolactam (VIMA-VCap). VIMA-VCap successfully inhibited hydrates in an 8-in, 28 mi long gas pipeline between Exxon Company USA's South Pass 89A (SP89A) and West Delta 73A/D (WD73) platforms. This pipeline, which experiences 5-10 °F subcooling year round, operated for over 6 months with as little as 1.3 gallons/day of dilute KHI solution. Prior to the demonstration, 79.3 gallons/day of methanol were injected into this pipeline for hydrate prevention. Hydrates and their impact on oil and gas production are widely discussed in the literature.3,4,5,6 Natural gas hydrates are ice-like solids which form when free water and natural gas combine at high pressure and low temperature. At these conditions, water molecules form polyhedral cages stabilized by light hydrocarbons or other natural gases (e.g., CO2 or H2S) inside the cage. Gas molecules in water cages combine with each other to form a macroscopic hydrate crystal. In a pipeline, hydrate crystals may flow as a slurry or adhere to the pipe wall and form a blockage depending on the contents and geometry of the line. Motivation for KHI Development. Hydrate inhibitor research is motivated by the cost to prevent the plugging tendency of hydrates. A flowline hydrate plug can cause significant downtime, especially offshore where access is difficult and hydrostatic pressures are high.7 Avoiding hydrate formation is preferable to removing a hydrate plug. The most common hydrate prevention methods include: Chemical hydrate inhibition. Traditional chemical inhibition has been to use large doses of methanol or glycols, to shift the hydrate equilibrium to lower temperatures and higher pressures. Methanol is also highly effective at melting hydrates that have already formed. However, large doses of these inhibitors increases operating costs and poses logistical difficulties in remote or offshore applications. Methanol can also cause the total hydrocarbon content of produced water to exceed the allowable limit for water disc

Rheological and Flow Properties of Gas Hydrate Suspensions

“…This limitation is caused by the rheological properties of suspensions with high solid fraction and may depend on flow regime conditions. Potentiality of LDHI has been highlighted under field conditions [13,14]. Three fields of the Eastern Trough Area Project (ETAP) in the United Kingdom Central North Sea are currently operating using KI [15].…”

“…For high Re, f is given by the Nikuradse correlation (see for example Govier and Aziz [38]): (13) Between Reynolds number Re = 3000 and 10 000, f exhibits a small dependence with velocity. This dependence of f can be estimated from the Wood-Colebrook law for pipe with intermediate roughness: (14) In the following, we will focus on flow at large Reynolds number, which is the most encounter flow regime for light oil or condensate.…”

Synthesis and application of a novel combined kinetic hydrate inhibitor

“…as hydrate inhibitors provide a guideline for the development of new green KHIs recently. There are varieties of KHIs utilized in the Gulf of Mexico, the Middle East for nearly a decade [17][18][19][20]. However, due to high cost for importing KHIs, there is few application in China, and the current technique to inhibit hydrate formation is still to inject alcohols such as methanol and ethylene glycol into pipelines.…”

Problems in Gas Hydrates: Practical Guidelines for Field Remediation

“…Expert computer systems are being developed in order to detect hydrate formation on time and apply the corresponding treatment 15 . In some deployments, LDI dosage has been controlled by a computer acquisition system 4 .…”