Corrosion and gas hydrate inhibitors having improved water solubility and increased biodegradability
AssigneeClariant Produkte (Deutschland) GmbH
InventorsUwe Dahlmann, Michael Feustel
Life of this patent
Estimating the term…
Loading patent…
AssigneeClariant Produkte (Deutschland) GmbH
InventorsUwe Dahlmann, Michael Feustel
Estimating the term…
The invention provides the compounds of the formula (1) where R1 is C1- to C22-alkyl, C2- to C22-alkenyl, C6- to C30-aryl or C7- to C30-alkylaryl, —CHR5—COO− or —O−, R2 is hydrogen —CH3 or —OH, R3, R4 are each independently C1- to C22-alkyl, C2- to C22-alkenyl, C6- to C30-aryl or C7- to C30-alkylaryl, R5 is hydrogen, C1- to C22-alkyl or C2- to C22-alkenyl, A is a C2- to C4-alkylene group, D is a C2- to C5-alkylene group which may contain one or two heteroatoms, m is a number from 0 to 30, n is a number from 1 to 18, and also their use as corrosion and gas hydrate inhibitors.
A compound of the formula (1)
Dependencies are inferred from the claim text.
Drawings are temporarily unavailable. Open the PDF at USPTO
From the US filing history. Foreign family members aren’t listed.
Radicals containing only hydrogen and carbon atoms attached to ring carbon atoms: acyclic radicals containing more than six carbon atoms
Compositions for drilling of boreholes or wells; Compositions for treating boreholes or wells, e.g. for completion or for remedial operations:…
Compositions for drilling of boreholes or wells; Compositions for treating boreholes or wells, e.g. for completion or for remedial operations:…
Inhibiting corrosion or fouling in apparatus for treatment or conversion of hydrocarbon oils, in general: by addition of corrosion inhibitors
Term ended 13 Aug 2025 (estimated)
The present invention relates to an additive and to a process for corrosion inhibition and gas hydrate inhibition on and in equipment for extracting and transporting hydrocarbons in crude oil extraction and processing.
In industrial processes in which metals come into contact with water or else with biphasic oil-water systems, there is the risk of corrosion. This is particularly marked when the aqueous phase, as in the case of crude oil production and processing operations, has a high salt content or, as a result of dissolved acidic gases such as carbon dioxide or hydrogen sulfide, is acidic. It is therefore not possible to exploit a deposit and to process crude oil without special additives to protect the equipment used.
Although suitable corrosion protectors for crude oil extraction and processing have been known for some time, they will become unacceptable for offshore applications in the future for reasons of environmental protection.
a) General Method for the Preparation of the Alkenylsuccinimidoalkylamines
A stirred apparatus equipped with distillation head with condenser was initially charged with 2.5 mol of the appropriate alkenylsuccinic anhydride (based on hydrolysis number) with nitrogen purging and heated to 60° C. 2.5 mol of the appropriate alkylendiamine were then added dropwise over 2 hours, in which time the reaction mixture heated to approx. 100° C. The reaction mixture was stirred at 100° C. for a further 1 h and then the reaction temperature was continuously increased from 100° C. to 160° C. over a period of 8 hours, in which time water of reaction distilled off. Finally, reaction was continued at 160° C. for 4 hours.
671 g of dodecenyl-/tetradecenylsuccinic anhydride (HN=418.1 mg KOH/g) and 255.5 g of dimethylaminopropylamine (DMAPA) were used to obtain 875 g of dodecenyl-/tetradecenylsuccinimido-N,N-dimethylpropylamine having AV=3.2 mg KOH/g and basic N=4.03%.