Understanding Crude Oil Demulsifiers A Technical Guide to Dehydration and Desalting
What Is a Demulsifier
A demulsifier is a surface-active chemical additive specifically designed to break the stable emulsions that form when crude oil and water are intimately mixed during production, and its fundamental mission is to accelerate the separation of the dispersed aqueous phase from the continuous hydrocarbon phase so that the recovered oil can be transported and refined economically and safely. When crude oil is produced from a reservoir it rarely arrives at the surface as a single clean liquid, because the natural surfactants present in the oil, the fine solid particles suspended in the brine, and the intense mechanical shear imparted by pumps, chokes, valves and pipelines all conspire to create remarkably stable water-in-oil emulsions in which tiny droplets of water are wrapped in tough, viscoelastic interfacial films that resist coalescence for long periods of time. These protective films are the heart of the problem, and a demulsifier works precisely by migrating to the oil-water interface, displacing the naturally occurring emulsifiers such as asphaltenes, resins and naphthenic acids, and weakening the interfacial film to the point where adjacent water droplets can merge into progressively larger drops that eventually settle out of the oil under gravity or with the assistance of heat and electrical fields. Beyond simply removing water, a well-designed demulsifier also assists in the removal of dissolved salts, suspended solids and other contaminants that travel with the brine phase, thereby clarifying the interface, reducing the bottom sediment and water content of the crude, and ensuring that the product meets the strict pipeline and refinery specifications that govern commercial crude oil sales. The practical consequences of effective demulsification are considerable, because crude oil that is properly dehydrated is less corrosive to pipelines and storage tanks, more valuable per barrel because it contains less non-hydrocarbon material, cheaper to transport because its viscosity and density are closer to specification, and far less troublesome to process in the refinery, where residual water and salt can poison catalysts, foul heat exchangers and destabilize distillation columns.
Why Crude Oil Emulsions Form and Why They Matter
To appreciate why demulsifiers have become indispensable chemicals in the oil and gas industry it is necessary first to understand the conditions under which crude oil emulsions are born and the serious operational problems they create when they are left untreated. Emulsions form whenever two immiscible liquids, in this case crude oil and formation water or injection water, are vigorously agitated in the presence of surface-active material, and in the upstream oilfield such agitation is essentially unavoidable, because the fluid mixture is throttled through wellhead chokes, propelled by sucker rod pumps and electric submersible pumps, sheared in gathering manifolds and transport pipelines, and repeatedly recycled through separators and treaters before it ever reaches a refinery. Each of these mechanical disturbances breaks the water phase into progressively smaller droplets, and as the droplets become smaller their combined interfacial area expands enormously, which in turn provides more surface for the natural emulsifiers naturally present in the crude, particularly the heavy asphaltene and resin fractions, the acidic naphthenic compounds, and the fine clay and scale particles that are always found in produced water, to adsorb and build a rigid protective skin around every individual droplet. The strength of this interfacial skin depends on a complex balance of crude composition, water chemistry, temperature and shear history, and it is this variability that makes emulsion treatment so site-specific, because an emulsion that breaks within minutes in one field may remain stubbornly stable for weeks in another even though the two crudes appear superficially similar. The consequences of failing to break these emulsions are severe and costly, because water carried in the crude raises its density and viscosity and therefore increases pumping energy and pipeline pressure losses, promotes internal corrosion of steel infrastructure through the activity of chlorides, organic acids and sulfate-reducing bacteria that thrive at the oil-water interface, inflates transportation tariffs because operators are paying to move water rather than oil, and in the worst cases produces rag layers and interface sludge that can plug separators, contaminate saleable crude and force the entire production train to be shut down for cleaning. At the refinery the damage is amplified further, because residual emulsified water brings with it dissolved salts that deposit on heat exchanger surfaces, deactivate the catalysts used in desalting, cracking and hydrotreating units, and release corrosive hydrogen chloride when the salts are hydrolyzed at high temperature, which is why refiners impose strict limits on the water and salt content of the crude they will accept and why effective demulsification upstream is really an investment in the integrity and reliability of the entire downstream value chain.
The Three Major Chemical Classes of Demulsifiers
The chemistry of demulsification has evolved over many decades into a sophisticated field, yet the enormous variety of commercial products that fill the market can be traced back to a surprisingly small number of fundamental molecular families, and as a practical matter the majority of demulsifiers used in the industry today belong to three major chemical classes, namely the nonionic ethylene oxide and propylene oxide block polymers which are commonly referred to as polyglycols, the alkylphenol-formaldehyde resin alkoxylates, and the epoxy resin based alkoxylates which are also known as diepoxide based products. The first of these classes, the nonionic EO/PO block copolymers, is built by sequentially adding ethylene oxide and propylene oxide to a suitable initiator such as a glycol, glycerol or an amine, and the resulting molecule consists of hydrophobic polypropylene oxide segments and hydrophilic polyethylene oxide segments arranged in blocks whose relative sizes can be tuned to control the hydrophilic-lipophilic balance of the polymer, so that the product can be tailored to attack emulsions of very different characters, with the longer polyethylene oxide blocks imparting better water solubility and the longer polypropylene oxide blocks providing stronger affinity for the oil phase. Because these block copolymers are nonionic they are remarkably tolerant of high salinity and wide pH ranges, which makes them the workhorse chemistry for many production and desalting applications, although their performance can be limited when the crude is heavily laden with asphaltenes that form exceptionally rigid interfacial films requiring stronger, more highly branched molecules to destabilize. The second major class, the alkylphenol-formaldehyde resin alkoxylates, is produced by condensing alkylphenols with formaldehyde to create a multi-branched phenolic resin backbone and then alkoxylating that backbone with ethylene oxide and propylene oxide to add hydrophilicity and adjust molecular weight, and the resulting structure is characterized by a compact, highly branched core that gives the molecule a much larger effective cross-section at the interface than a simple linear polymer, enabling it to penetrate and disrupt the closely packed asphaltene and resin layers that stabilize the most difficult emulsions. These resin alkoxylates are widely regarded as among the most powerful demulsifier families available, and they are frequently the chemistry of choice for heavy, viscous, asphaltenic and high total acid number crudes where linear polyglycols simply do not have the interfacial strength to achieve clean separation, and their ability to neutralize the charge carried by interfacial material is one of the reasons they perform so well in electrostatic desalters. The third major class, the epoxy resin based alkoxylates, is derived from diepoxide building blocks that are reacted to form a crosslinked or star-shaped backbone before being alkoxylated with ethylene oxide and propylene oxide, and this architecture combines the robustness of a rigid, crosslinked core with the flexibility and water compatibility imparted by the polyether arms, producing molecules that are exceptionally resistant to high temperatures and that maintain their activity even in the presence of heavy solids, high water cuts and the harsh chemical environments found in many refineries and upgraders. Together these three families, sometimes used alone and more often blended together in synergistic combinations, account for the great majority of the demulsifier formulations applied across the industry, and understanding their differences is the first step toward selecting the right product for a given crude, as summarized in Table 1 below.
Table 1. The three major chemical classes of demulsifiers
Chemical class | Structural features | Primary mechanism | Typical applications |
Nonionic EO/PO block polymers (polyglycols) | Linear or branched chains of ethylene oxide and propylene oxide blocks grown from a glycol, glycerol or amine initiator | Interface adsorption, controlled hydrophilicity and film weakening by surface activity | Production separators, general dehydration, high-salinity and broad-pH systems |
Alkylphenol-formaldehyde resin alkoxylates | Highly branched phenolic resin core formed by condensation, alkoxylated with EO and PO | Strong interfacial penetration, charge neutralization, disruption of asphaltene films | Heavy, viscous, high-asphaltene and high-TAN crudes, electrostatic desalters |
Epoxy resin based alkoxylates (diepoxide based) | Crosslinked or star-shaped core from diepoxide building blocks, alkoxylated with EO and PO | Rigid robust backbone, thermal stability, tolerance of solids | Refineries, upgraders, harsh high-temperature and high-solids service |
Complementary Chemistries and Auxiliary Agents
Although the three families described above form the backbone of modern demulsification, the picture is completed by a range of complementary chemistries that either serve as demulsifiers in their own right or act as auxiliary agents that support the performance of the primary product, and among these the glycol esters deserve particular mention because they constitute another common and highly versatile chemical type that is frequently encountered in both production and refining applications. Glycol esters are formed by esterifying polyglycols or glycol derivatives with organic acids, and the resulting products combine the surface activity of the polyether chain with the oil affinity of the ester group, giving them an intermediate character that makes them excellent components for fine-tuning the overall performance of a formulation, for improving the solubility of the blend in the solvent carrier, and for modifying the behavior of the interface in ways that a single polymer family cannot achieve on its own. Beyond the esters, the formulator also has access to a variety of specialized auxiliary products such as the sulfonates, which are anionic surface-active compounds that are used in many demulsifier formulations as wetting agents, meaning that they assist in spreading the chemical across the interface, penetrating the protective films around the water droplets, and improving the contact between the demulsifier and the emulsified water so that the active polymer molecules can do their work more quickly and thoroughly. The practical consequence of this chemistry is that industrial demulsifiers are very often complex reaction products rather than single pure compounds, because the formulator deliberately combines multiple active polymers, auxiliary wetting agents, solvents, and occasionally minor additives into a single package so that each component contributes to a different part of the demulsification process, and the synergistic interplay among these components is frequently the difference between a product that merely performs and a product that performs exceptionally well on a difficult crude. This complexity also explains why the same demulsifier chemistry can behave so differently on different crudes, because each crude presents a unique interfacial environment, and the correct balance of polymers, wetting agents and solvents that breaks one emulsion efficiently may be completely ineffective on another, which is precisely why demulsifier requirements are unique to each location and why careful product selection and testing are indispensable parts of any successful treatment program.
How Demulsifiers Work
The mechanism by which a demulsifier actually breaks an emulsion can be understood as a sequence of coordinated molecular events, and while the precise details vary with the chemistry of the product and the nature of the crude, the general picture is consistent enough to be described with confidence, beginning with the transport of the demulsifier molecules to the oil-water interface. Because demulsifiers are surface-active they naturally concentrate at the interface between the oil and the water droplets, and once there they compete with the naturally occurring emulsifiers such as asphaltenes and resins for space on the film, gradually displacing these rigid, high-molecular-weight components and replacing them with the smaller, more mobile polymer molecules that cannot hold the film together nearly as effectively. As this exchange proceeds, the interfacial film becomes thinner, weaker and more permeable, its viscoelastic strength collapses, and the droplets that were previously protected from one another by their tough skins begin to approach each other more closely when they collide during settling or under the influence of an applied electrical field. The critical step is then coalescence, in which the thin liquid film trapped between two approaching droplets drains away and finally ruptures so that the two droplets merge into a single larger drop, and because the rate of settling of a droplet in a liquid is proportional to the square of its diameter, each successive coalescence event dramatically accelerates the rate at which the water phase separates from the oil, so that a population of micron-sized droplets that would take months to settle is converted within hours into a few large drops that fall rapidly to the bottom of the vessel. In many production facilities this natural coalescence is assisted by heat, which lowers the viscosity of the oil and weakens the interfacial film, by the addition of wash water, which dilutes the emulsion, and by gravity settling or centrifugation, and in refinery desalters it is assisted above all by an electrostatic field that polarizes the water droplets, causes them to align and collide with one another in chains, and dramatically increases the frequency and effectiveness of coalescence, which is why the demulsifier and the electrostatic desalter work together as a single integrated treatment system. The net effect of all these mechanisms is that the water phase separates cleanly from the oil, the interface between the two becomes sharp and free of the troublesome rag layer that characterizes poorly treated emulsions, and the treated crude emerges with a water content low enough to satisfy pipeline and refinery specifications, while the separated water, now largely free of entrained oil, can be handled by downstream water treatment facilities.
Demulsifier Requirements Are Unique to Each Location
One of the most important lessons learned in decades of oilfield experience is that demulsifier requirements are unique to each location, and any attempt to treat a new crude with a product that worked beautifully on a different crude from a different field is a gamble that will frequently fail, because the behavior of an emulsion is determined by the entire history and composition of the fluids that form it. The composition of the crude itself is the first and most obvious variable, since a light paraffinic crude, a heavy asphaltenic crude and a high total acid number crude each produce interfacial films of completely different character, with the asphaltenic crude requiring a highly branched, strongly penetrating chemistry while the paraffinic crude may respond better to a linear polymer, and the properties of the water phase matter just as much, because the salinity, hardness, pH and dissolved solids content of the brine all influence the charge and rigidity of the interfacial film and therefore the type of demulsifier that will be effective. The process conditions under which the emulsion is treated constitute the second group of variables, because the operating temperature, the residence time available in the separator or treater, the pressure, the applied voltage in an electrostatic desalter, and the shear history of the fluid all shift the optimum demulsifier selection and dosage, and what works at a warm, low-shear facility may be entirely inadequate at a cold, high-shear installation treating the very same crude. Because of this complexity the industry has developed a disciplined methodology for product selection that revolves around the bottle test, in which representative samples of the actual crude and water are placed in graduated bottles, treated with candidate demulsifiers at various dosages, heated to simulate field temperature, shaken or stirred to reproduce field mixing, and then observed for the rate of water drop, the sharpness of the interface, the clarity of the separated water and the final bottom sediment and water content, and the results of these tests, which should always be repeated on fresh samples because emulsions change over time, provide the evidence needed to choose both the product and the injection rate. Once a product has been selected the work is not finished, because the optimum treatment is then fine-tuned in the field through systematic dosage trials, adjustments to injection points and mixing intensity, and continuous monitoring of the treated crude, and this ongoing optimization is what transforms a good demulsifier into a reliable and economical one, as summarized in Table 2 below.
Table 2. Key considerations in demulsifier selection and optimization
Consideration | Key variables | Impact on treatment | Screening and optimization tool |
Crude composition | Paraffinic, asphaltenic, heavy, high-TAN and sulfur content | Determines the required chemistry class and molecular architecture | Bottle tests on representative field samples |
Water phase chemistry | Salinity, hardness, pH and dissolved solids | Affects film charge, rigidity and product tolerance | Bottle tests and water analysis |
Process conditions | Temperature, residence time, pressure, voltage and shear | Shifts the optimum product and dosage window | Bottle tests at field temperature and field trials |
Contaminants | Fine solids, scale, production chemicals and corrosion products | Can stabilize emulsions or consume the demulsifier | Interface and rag layer inspection, dosage trials |
Economics | Product price, dosage and disposal cost of separated water | Determines the most cost-effective formulation | Treatment cost per barrel comparison |
UNPChemicals Demulsifier Products
Building on this deep understanding of emulsion chemistry and the site-specific nature of demulsification, UNPChemicals has developed the DEMET series of crude oil demulsifiers, a comprehensive product family that covers the full spectrum of dehydration and desalting needs and is divided, according to the dehydration speed required and the final water content of the treated crude, into three main categories known as the dryer type, the fast dehydration or dropper type, and the desalter type, so that operators can match the product to the exact duty of their facility. The DEMET series draws on a synergistic combination of complementary chemistries, including resin oxyalkylates that provide charge neutralization at the interface, block copolymers that control interfacial rheology, and polyacrylates that modify the wettability of solid particles, and this balanced formulation enables the products to handle challenging crudes such as heavy, high-TAN and high-asphaltene oils while maintaining consistent performance across a wide range of operating temperatures from roughly 80 to 150 degrees Celsius and across broad pH and salinity windows.
Representative products in the range include the resin oxyalkylate DEMET A-21, a dark amber liquid oxyalkylate widely used for crude oil desalting in exploration and upstream applications, the high-performance DEMET C-168 which has been demonstrated as an effective equivalent to the well-known Nouryon Witbreak DRC-168 and which achieves clear phase separation and a dehydrated water content of 0.5 percent or less within roughly 30 to 60 minutes under standard conditions, and specialized grades such as the propylene glycol block polyether DEMET G-415, the proprietary electric desalting blend DEMET M-9510 and a range of polymerized polyol, polyoxyalkylene glycol and esterified phenolic polymer products, all of which can be further tailored through the AP-type multi-branched and AR-type resin-initiated polymer platforms to match the specific crude and process of each customer. By combining rigorous molecular design with extensive field experience and a customer-centric approach to formulation and service, UNPChemicals aims to deliver demulsifiers that not only meet stringent dehydration and desalting specifications but also reduce treatment times, lower dosage requirements and minimize the oil content of the separated water, thereby helping producers and refiners around the world protect their assets, cut operating costs and maximize the value of every barrel they handle.