CORROSION INHIBITOR FOR THREE-PHASE SYSTEM
FIELD: oil and gas production. ^ SUBSTANCE: invention relates to protection of gas and oil-field equipment and pipelines operated in three-phase highly mineralized media (water, organics, gas) against corrosion and, more specifically, to a method for preparing corrosion inhibitors based on the produ...
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creator | DMITRIEV JURIJ KONSTANTINOVICH AKHMADEEVA GUZEL' IMMAMUTDINOVNA MURATOV MARAT MANSAFOVICH ZAGIDULLIN RAIS NURIEVICH |
description | FIELD: oil and gas production. ^ SUBSTANCE: invention relates to protection of gas and oil-field equipment and pipelines operated in three-phase highly mineralized media (water, organics, gas) against corrosion and, more specifically, to a method for preparing corrosion inhibitors based on the product of condensation of polypropylene-polyamines with higher isomeric alpha-ramified monocarboxylic acids or synthetic fatty acids followed by cyanethylation, oxyalkylation, alkylation, and manufacture of preparative form of inhibitor by adding solvent to a certain portion of active base. Polypropylene-polyamines can be a industrial-grade mixture and above-indicated monocarboxylic acids are those with 6-28 carbon atoms while synthetic fatty acids with 10-28 carbon atoms. Condensation is carried out for 4-6 h at 130-160°C while simultaneously distilling off water, after which reaction mixture is heated to 230-250°C for 1.0-2.5 h in inert gas flow. Resulting products are subjected to cyanethylation, oxyalkylation, and alkylation at 35-80°C for 2-4 h. Preparative form of inhibitor is obtained by adding solvent at 250°C, said solvent being product obtained via amination of bottom residue from butyl alcohol production or aminated distillate thereof. ^ EFFECT: achieved efficient protection of metals against corrosion in hydrogen sulfide-containing three-phase media. ^ 3 cl, 2 tbl, 15 ex |
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Polypropylene-polyamines can be a industrial-grade mixture and above-indicated monocarboxylic acids are those with 6-28 carbon atoms while synthetic fatty acids with 10-28 carbon atoms. Condensation is carried out for 4-6 h at 130-160°C while simultaneously distilling off water, after which reaction mixture is heated to 230-250°C for 1.0-2.5 h in inert gas flow. Resulting products are subjected to cyanethylation, oxyalkylation, and alkylation at 35-80°C for 2-4 h. 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subjects | CHEMICAL SURFACE TREATMENT CHEMISTRY COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATIONOR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL COATING MATERIAL WITH METALLIC MATERIAL COATING METALLIC MATERIAL DIFFUSION TREATMENT OF METALLIC MATERIAL INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION INGENERAL METALLURGY MULTI-STEP PROCESSES FOR SURFACE TREATMENT OF METALLICMATERIAL INVOLVING AT LEAST ONE PROCESS PROVIDED FOR IN CLASSC23 AND AT LEAST ONEPROCESS COVERED BY SUBCLASS C21D OR C22F OR CLASS C25 NON-MECHANICAL REMOVAL OF METALLIC MATERIAL FROM SURFACE |
title | CORROSION INHIBITOR FOR THREE-PHASE SYSTEM |
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