초록 ▼

A process for the thermo-hydraulic control of gas hydrates in subsea production and injection wells as well as pipelines which transport liquid or gaseous hydrocarbons is described, the process making use of a Nitrogen Generating System foamed or in solution. The control may signify the prevention o

A process for the thermo-hydraulic control of gas hydrates in subsea production and injection wells as well as pipelines which transport liquid or gaseous hydrocarbons is described, the process making use of a Nitrogen Generating System foamed or in solution. The control may signify the prevention of the formation of the gas hydrates or the dissolution of the gas hydrate plug already formed. Under conditions of use designed for the prevention of the formation of gas hydrates the SGN fluid prevents the thermal conditions leading to the gas hydrate plugs. Under conditions of use designed to dissolve the already formed gas hydrate plugs, the SGN fluid alters the thermo-hydraulic conditions which favor the gas hydrate plugs, so that they are dissolved and return to the water+gas phase.

대표청구항 ▼

[ We claim:] [1.] A process for the thermo-hydraulic control of gas hydrates under conditions of gas hydrate formation within a petroleum well, which comprises the following steps:a) preparing in one single mixing vessel an aqueous, equimolar solution of ammonium chloride and sodium nitrite of conce

[ We claim:] [1.] A process for the thermo-hydraulic control of gas hydrates under conditions of gas hydrate formation within a petroleum well, which comprises the following steps:a) preparing in one single mixing vessel an aqueous, equimolar solution of ammonium chloride and sodium nitrite of concentration between 2.0 and 4.5 molar;b) viscosifying the aqueous solution of step a) with hydroxyethyl cellulose of a concentration between 0.3 to 1.2 weight/volume keeping pH at values between 8.0 and 8.3;c) in a separate vessel, preparing a solution of acetic acid activator of 40% volume;d) adding between 1 and 2% volume of activator taken from said separate vessel to aqueous, viscosified solution taken from said one single mixing vessel so as to obtain a foamed and viscosified nitrogen gas fluid;e) pumping the nitrogen gas- and heat-generating foamed and viscosified fluid of step d) through a flexitube positioned in the interior of the production string so as to contact said fluid with the gas hydrate and thus cause the gas hydrate to dissolve as a consequence of the increase in temperature and reduction of pressure;f) recovering the spent fluids and separating the aqueous phase in an adequate separator.