Corrosion inhibitor efficiency

Acylated derivatives of amino acids are generally converted by microbes in rivers and lakes into acids and natural amino acids. Effectiveness data on mild and stainless steels proved the importance of the acyl moiety. The longer alkyl moiety in the acyl substituent (Cg io) greatly improves the corrosion inhibitor efficiency. These detergent-like compounds inhibit the deposition of both organic and inorganic particles, and... 

In another preliminary evaluation of the use of the 6-dimensional eigenvalues from the LDM as universal descriptors we looked at building a model of the inhibitive properties of heterocyclic diazoles for acidic iron corrosion [96]. Table 3.5 shows the computed eigenvalues and corrosion inhibitor efficiencies (CIE %) for a set of diazoles reported by Babic-Samardzija et al. [96]. 

From the main form (Figure 2.25) it is clear that the required corrosion allowance without corrosion inhibitor is 16.3 mm, which means that corrosion inhibitor is a must. The calculated corrosion allowance with 90% corrosion inhibitor efficiency is 1.6 mm, and the calculated corrosion allowance for a dry surface is 0.65 mm. Hence, the design conclusion will be as follows ... 

Wettabihty is defined as the tendency of one fluid to spread on or adhere to a soHd surface (rock) in the presence of other immiscible fluids (5). As many as 50% of all sandstone reservoirs and 80% of all carbonate reservoirs are oil-wet (10). Strongly water-wet reservoirs are quite rare (11). Rock wettabihty can affect fluid injection rates, flow patterns of fluids within the reservoir, and oil displacement efficiency (11). Rock wettabihty can strongly affect its relative permeabihty to water and oil (5,12). When rock is water-wet, water occupies most of the small flow channels and is in contact with most of the rock surfaces as a film. Cmde oil does the same in oil-wet rock. Alteration of rock wettabihty by adsorption of polar materials, such as surfactants and corrosion inhibitors, or by the deposition of polar cmde oil components (13), can strongly alter the behavior of the rock (12). 

Three commercial processes that use these various hot carbonate flow arrangements are the promoted Benfield process, the Catacarb process, and the Giammarco-Vetrocoke process (26—29). Each uses an additive described as a promoter, activator, or catalyst, which increases the rates of absorption and desorption, improves removal efficiency, and reduces the energy requirement. The processes also use corrosion inhibitors, which aHow use of carbon—steel equipment. The Benfield and Catacarb processes do not specify additives. Vetrocoke uses boric acid, glycine, or arsenic trioxide, which is the most effective. 

To reduce the amount of dust produced, water can be added to the abrasive from a circular water sprayer around the no22le. Chemical corrosion inhibitors must be dissolved in the water to prevent flash msting of the steel. Newer methods to reduce dust include the use of ice, soHd carbon dioxide (dry ice), or plastic beads as abrasives. Blasting with dry ice is inexpensive and effective, but the accumulation of carbon dioxide must be avoided in enclosures. Plastic beads are inexpensive, but the cutting efficiency is low and paint removal is slow the beads can be cleaned of paint particles and reused. 

To meet sales specifications, gas produced at the wellheads must be free of water and hydrocarbon liquids. Twin turboexpanders are a key component in this process, providing dewpoint control with optimal efficiency. Initial processing takes place at the wellhead platforms, where methanol is injected to inhibit hydrate formation. A corrosion inhibitor is also added to prevent gas from damaging downstream equipment. 

Inhibitor Efficiency. The value of corrosion inhibitors can be compared on the basis of inhibitor efficiency. Inhibitor efficiency indicates the percentage that corrosion is lowered in the presence of the inhibitor as compared to that in its absence. Inhibitor efficiency can be calculated by using the formula... 

Dissolved solid and gaseous impurities can also affect the pH of the system and this may often lead to decreased inhibitor efficiency. In industrial plant, cooling waters can take up SOj, HjS or ammonia and pH control of inhibited waters will be necessary. The leakage of exhaust gases into engine coolants is an example in which corrosion can occur despite the presence of inhibitors. 

Reaction of adsorbed inhibitors In some cases, the adsorbed corrosion inhibitor may react, usually by electro-chemical reduction, to form a product which may also be inhibitive. Inhibition due to the added substance has been termed primary inhibition and that due to the reaction product secondary inhibition " . In such cases, the inhibitive efficiency may increase or decrease with time according to whether the secondary inhibition is more or less effective than the primary inhibition. Some examples of inhibitors which react to give secondary inhibition are the following. Sulphoxides can be reduced to sulphides, which are more efficient inhibitorsQuaternary phosphonium and arsonium compounds can be reduced to the corresponding phosphine or arsine compounds, with little change in inhibitive efficiency . Acetylene compounds can undergo reduction followed by polymerisation to form a multimolecular protective film . Thioureas can be reduced to produce HS ions, which may act as stimulators of... 

In stimulation fluids containing concentrated HCl, the partial substitution of water by alcohols such as methanol, ethanol, and glycerol increases the corrosivity of the acid fluids and reduces the efficiency of the corrosion inhibitors [1148]. This effect is especially important for fatty amine-based inhibitors. For products containing acetylenic-type inhibitors the detrimental effect is less important and a weight loss may be maintained within acceptable limits using slightly higher, but still reasonable, levels of inhibitor. 

Polypeptides have been under consideration as corrosion inhibitors because of environmental concerns [1358]. Polyaspartate is the most efficient corrosion inhibitor known among the polypeptides [1196]. The molecular weight (1000 to 22,000 Dalton) does not affect the efficiency, but both high calcium ion and... 

The Corrosion Inhibitor, Inhibiting Corrosive Efficiency and Its Relationship with Collector Action... 

To increase equipment reliability and plant efficiency, corrosion inhibitors are used in boiler and cooling water programs to control fouling and deposition on critical heat-transfer surfaces. In cooling systems, corrosion inhibition is commonly achieved through the use of passivators, which encourage the formation of a protective metal oxide film on the metal surface ( 1). ... 

The most efficient system devised by Monsanto uses electrodes fabricated from carbon steel plate, electro-coated on one face with cadmium. These are stacked in parallel so that the electrolyte can be pumped through the gap between successive plates. Overall tire system forms a series of electrochemical cells with a cadmium cathode and a carbon steel anode. Each plate of metal forms the cathode of one cell and the anode of the next in the stack. Electric current is passed across the stack. The electrolyte contains phosphate and borate salts as corrosion inhibitors, EDTA to chelate any cadmium and iron ions generated by corrosion together with hex-amethylenebis(ethyldibutylammonium) phosphate to provide the necessary telraal-kylammonium ions. This electrolyte circulates through the cell from a reservoir and there is provision for the introduction of acjylonitrile and water as feedstock. The overall cell reaction is ... 

C Factor ratings between 155 and 160 are typical for pipelines that have been newly constructed effectively treated with a film-forming corrosion inhibitor. A low C Factor indicates that there is higher internal friction within a pipeline system, and thus a reduction in efficiency. 

The cooling tower, which is an efficient air scrubber can easily become a catchall for contaminants resulting from the location of the tower or from the industrial process. In arid areas, ingress of sand contributes to fouling, which reduces efficiency and contributes to biofilm and under-deposit corrosion. In coastal areas, sand laden with chlorides can cause corrosion of stainless steel components and impair chemical corrosion inhibitor performance. Heavy industries, such as steel or aluminum manufacture, produce severely contaminated cooling water resulting from direct contact with metal slags and lubricants. 

Many 1,2-dithiole derivatives have been patented or recommended for use as pickling or corrosion inhibitors or as additives to lubricating oils (B-66MI43100). They are efficient in preventing high-temperature fouling of oil feedstock (78USP4116812). 

A corrosion inhibitor is a chemical substance that, upon addition to a corrosive environment, results in reduction of corrosion rate to an acceptable level. Corrosion inhibitors are generally used in small concentrations. The principles and applications of corrosion inhibitors are discussed at great length in a recent monograph.47 A corrosion inhibitor should not only mitigate the corrosion, but also be compatible with the environment in the sense that it should not cause any complications. Usually the corrosion inhibitor is rated in terms of inhibition efficiency I and is given by the relationship. 

Attack by organisms other than SRB. Ammonia and amines are produced by microbial decomposition of organic matter under both aerobic and anaerobic conditions (ammo-nification). (Stott)5 These compounds are oxidized to nitrite by aerobic bacteria such as Nitrosomonas or Nitrobacter species. Nitrobacter is very efficient at destroying the corrosion-inhibition properties, of nitrate-based corrosion inhibitors by oxidation, unless a biocidal agent is included in the formulation. The release of ammonia at the surfaces of heat-exchanger tubes has a detrimental effect. (Stott)5... 

Add efficient inhibitors for certain systems since it is believed to assist the formation of a stronger, more stable or more readily repaired passive film. (Miller)24 Phosphates and other inorganic or organic corrosion inhibitors, used in fairly corrosive surroundings, decrease the effects of the SCC. A minimal critical concentration of some oxidizing inhibitors such as nitrites is absolutely necessary to avoid pitting. 

As technology advances, the need for improved performance from materials increases. There is also a continuing economic pressure to minimise costs, which will become increasingly difficult as resources become depleted. Thus, research is aiming at more efficient corrosion protection methods such as improved formulations for paints and corrosion inhibitors, improved metal alloys, better design, and the use of novel materials such as ceramics and plastics. 

For cross country lines containing oil or gas, the corrosive constituents such as water, carbon dioxide, and hydrogen sulfide are usually reduced to a very low level before the fluid enters the line. The lost efficiency required to pump the unwanted constituents and the extra wall thickness required for corrosion allowance usually cannot be economically justified. Even with cleanup systems, some water will get into pipelines. In oil lines, oil soluble corrosion inhibitors usually prevent attack by water settling in low spots, etc. Gas lines are usually dehydrated to 60% of saturation to avoid corrosion from condensing water containing dissolved carbon dioxide. Molecular sieves that reduce water to 5 ppm have proved necessary in lines containing 100% carbon dioxide. 

The most significant impurities in the feed streams to a typical alkylation unit are ethylene, dlolefins, sulfur compounds and water. Corrosion Inhibitors and other chemicals used in upstream processing can also be present in some cases, and these can have harmful effects. The amount of each iaqiurlty that reaches the alkylation reactor varies considerably from refinery to refinery. If accurately determined and properly accounted for, these impurities can explain an appreciable percentage of the acid make-up reported by various operating units. The impurity data shown in Table I can be used to evaluate the merit of Improved upstream process control and/or more efficient feed pretreatment methods. 

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