Wet pipeline treatment for gas transport

Abstract: A wet pipeline through which a hydrate-forming gaseous fluid is to be passed, is first treated by contacting the water therein with a liquid which forms an azeotropic mixture with water. In this way, evaporation of the azeotropic mixture, when the gas is passed through the pipeline, does not result in a water concentration which will form hydrates with the hydrate-forming gaseous fluid.

Description: The present invention relates to a method of treating a pipeline containing water to reduce or prevent the formation of hydrates when hydrate-forming gaseous fluids are subsequently passed therethrough. After a pipeline for the transportation of light hydrocarbons, such as natural gas, has been repaired or constructed and hydro-tested or otherwise exposed to water, it is important that any water remaining in the pipeline be dealt with since light hydrocarbon gases can form hydrates with water and the hydrates can, and often do, reduce or block the flow of gases through pipelines. Additionally, acid gases in the stream of light hydrocarbons such as carbon dioxide and hydrogen sulfide will dissolve in the water thereby producing corrosive acids in the pipelines. Gas hydrates are similar to ice crystals and form by the combination of light hydrocarbon gases and water under certain temperature and pressure conditions. The pipelines have heretofore been dried by passing a waterabsorbing gas such as dry air or nitrogen through the pipeline, by pulling a vacuum on the pipeline, by passing methanol through the pipeline or by a combination of the foregoing techniques. A successful procedure for drying a pipeline which has been used heretofore is to pass methanol through the pipeline. The methanol is usually separated in stages by pipeline pigs which allows the water in the pipeline to be exposed to successive methanol contact which brings about successive dilutions of the methanol-water mixture remaining in the pipeline. Such methanol treatments have resulted in films of methanol-water mixtures remaining in pipelines containing very small amounts of water. However, even very small amounts of water may be sufficient to cause hydrate formation in very long, cold pipelines. For example, a 60cm (24 inch) pipeline which is about 1130 km (700 miles) long will be left with a film of methanol and water mixture on its inside surfaces after a methanol pigging treatment of the type described above. Assuming the film to be about 0.1 millimetre thick, the total volume of the methanol-water mixture left in the pipeline is about 218 cubic metres (7,700 cubic feet) of liquid, most of which is methanol. However, a property of methanol-water mixtures is that the methanol evaporates faster than the water. Thus, as evaporation of the methanol-water mixture left in the pipeline takes place over time, the mixture constantly increases in water concentration. Accordingly, there is a possibility that the methanol will be stripped from the mixture remaining in the pipeline leaving the mixture containing a high concentration of water which can cause the formation of hydrates in the pipeline. FR-A-2691503 discloses a process for the treatment or processing and transport of a natural gas from a gas well, in which the produced gas is contacted with a liquid phase containing water and at least one anti-hydrateadditive. The additive is at least partly miscible with water and vaporizes in the pure state or as an azeotrope. The contact zone is at least part of the production well. We have now devised an improved method of treating pipelines containing water to reduce the formation of gas hydrates. In one aspect, the invention provides a method of treating the wet inside of a pipeline to reduce the formation of a hydrate when a hydrate-forming gaseous fluid is passed therethrough, which method comprises, before passing the gaseous fluid therethrough, first contacting the wet inside of the pipeline with a liquid which forms an azeotropic mixture with water, the amount of said liquid being sufficient to form an azeotropic mixture with the water in the pipeline. According to the invention, a liquid which forms an azeotropic mixture with water is brought into contact with the water in the pipeline. The amount of azeotropic mixture-forming liquid utilized is sufficient to form an azeotropic mixture with the water whereby, as the mixture is evaporated in the pipeline, the water concentration in the remaining mixture does not approach that concentration which will form hydrates with hydrate-forming gaseous fluid. Thereafter, the hydrate-forming gaseous fluid can be flowed through the pipeline. Azeotropic mixtures containing water behave like a single substance in that when the mixture is evaporated the vapour produced has the same composition as the liquid. Thus, by forming an azeotrope mixture with water in a pipeline and ensuring that there is enough of the azeotropic liquid present in the mixture as the mixture evaporates to prevent the formation of hydrates with a hydrate-forming gas stream, at the most favourable conditions for hydrate formation that can exist in the pipeline, the possibility of hydrate formation in the pipeline is reduced or eliminated. Thus, in accordance with the drying treatment method of the present invention, the amount of the azeotropic liquid flowed into contact with water in a pipeline is an amount sufficient to form an azeotrope mixture with the water whereby as the azeotrope mixture remaining in the pipeline after the treatment is evaporated, the concentration of water in the mixture does not approach that concentration which will form hydrates. Various azeotropic liquids can be utilized in accordance with the present invention including, but not limited to, ethanol, n-propanol, isopropanol, tert-butyl alcohol, isopropyl ether, ethyl acetate, methyl ethyl ketone and other similar azeotropic liquids. Azeotropic liquid alcohols are preferred in that the presence of an alcohol in admixture with water depresses the temperature at which the water will combine with hydrate forming gases to form hydrates. Suitable azeotrope mixture-forming alcohols for use in accordance with the present invention include, but are not limited to ethanol, n-propanol, isopropanol and tert-butyl alcohol. Of these, ethanol, isopropanol and tert-butyl alcohol are preferred with ethanol being the most preferred. In carrying out the methods of the present invention, it is generally preferred that the azeotropic liquid utilized is combined with the water in a pipeline to be dried in an amount such that water is present in the azeotrope mixture remaining in the pipeline in a low amount, e.g., below about 5% by weight when the azeotropic liquid is ethanol, n-propanol or isopropyl ether; below about 12% by weight when the azeotropic liquid is isopropyl alcohol; and below about 6% by weight when the azeotropic liquid is ethyl acetate. As mentioned, after the pipeline drying operation is complete and the hydrate forming gas stream is flowing therethrough, the azeotrope mixture which remains in the pipeline evaporates in a manner whereby the water in the azeotropic mixture stays at the same concentration. The maximum amount of water that can be tolerated in a specific residual azeotrope mixture is that amount whereby the mixture does not form gas hydrates at the most favorable conditions that will exist in the pipeline for the formation of hydrates. As mentioned above, azeotropic liquid alcohols are preferred because they depress the temperature at which hydrates form. Also, it has been found that azeotrope mixtures of alcohol and water dry faster than the non-azeotrope mixture of methanol and water. A preferred technique for flowing the azeotropic liquid used into contact with water in a pipeline is to flow the liquid through the pipeline in stages separated by a one or more pipeline pigs. The pigs are propelled through the pipeline by a high pressure stream of non-hydrate forming gas such as air, nitrogen or an available process gas. Preferably, the stream of non-hydrate forming gas is air, nitrogen or a process gas which has been dried or otherwise has capacity for absorbing water as the gas flows through the pipeline. A particularly preferred method of the present invention for drying a pipeline containing water which is to transport a hydrate forming gaseous fluid is comprised of the following steps. Ethanol is flowed into contact with water in the pipeline in stages separated by a plurality of pipeline pigs, the amount of the ethanol being such that the resulting residual azeotrope mixture remaining in the pipeline after the drying treatment has been completed contains water in an amount in the range of from about 1% or less to about 5% water by weight of the mixture. As a result, when the hydrate forming gaseous fluid, e.g., natural gas, is flowed through the pipeline, the presence of the ethanol with the water in the remaining azeotrope mixture depresses the temperature at which hydrates can be formed to a very low level, far below the lowest temperature at which the pipeline will be operated. In order to further illustrate the methods of the present invention the following examples are given. EXAMPLE 1 Tests were performed by placing quantities of a mixture of alcohol and water containing 99% methanol and 1% water by weight or an azeotropic mixture of alcohol and water containing 99% ethanol and 1% water by weight in a test apparatus. Dry nitrogen was passed through the apparatus and the dew points of the exiting nitrogen were recorded. During each test, samples of the test alcohol-water mixtures remaining in the apparatus were periodically withdrawn and analyzed for water content. The nitrogen utilized in the test was evaporated liquid nitrogen at ambient temperature, i.e., approximately 23°C, having a dew point of about -90°C. The nitrogen flow rate through the test apparatus was five standard liters per minute at atmospheric pressure. The volume of each test mixture placed in the apparatus was 200 milliliters. The results of these tests are set forth in Table I below. WATER CONTENTS OF EVAPORATING 99% ALCOHOL-1% WATER MIXTURES Elapsed Time, hr:min Ethanol-Water Mixture Methanol-Water Mixture Dew Point, °C Water In Remaining Mixture, % by Wt. Dew Point, °C Water In Remaining Mixture, % by wt. 0:00 -4.7 1.35 13.2 1.33 0:30 -2.7 10.4 1:00 -3.6 1.48 9.5 1.58 1:30 -4.2 9.3 2:00 -4.4 1.58 9.2 2.35 2:30 -5.3 9.1 3:00 -5.7 1.88 10.0 5.73 3:30 -6.2 ≤-70.0 4:00 -7.1 1.09 4:30 -25.3 4:50 ≤-70.0 From Table I it can be seen that the methanol water mixture increased in water content as the mixture was evaporated by the nitrogen, i.e., the mixture changed from about 1% water to nearly 6% water. This is contrasted with the azeotrope mixture of ethanol and water which remained about the same throughout the test. Example 2 The test procedure described in Example 1 was repeated utilizing three alcohol-water mixtures, namely, a mixture of 95% ethanol and 5% water, a mixture of 95% isopropanol and 5% water and a mixture of 95% methanol and 5% water. The results of the tests are shown in Table II below. WATER CONTENTS OF EVAPORATING 95% ALCOHOL-5% WATER MIXTURES Elapsed Time, hr:min Ethanol Water Isopropanol-Water Methanol-Water Dew Pt. °C Water in Mixture left, % by wt. Dew Pt., °C Water in Mixture left, % by wt. Dew Pt., °C Water in Mixture left, % by wt. 0:00 3 6.07 2.1 6.02 12 6.45 0:30 1.1 -2.9 9.2 1:00 0 5.98 -5.1 5.54 8.3 8.34 1:30 -0.2 -5.9 8.3 2:00 -0.3 6.2 -7.7 4.33 8.7 9.23 2:30 -0.4 -9.6 9.1 3:00 -0.6 5.75 -12.1 3.04 9.6 12.56 3:30 -1.5 -16.1 10.2 4:00 -3.1 5.66 -20.8 2.91 5.4 21.05 4:30 -15.8 -44.6 ≤-70.0 4:50 ≤-70.0 8.46 ≤-70.1 1.96 From Table II it can be seen that the methanol-water mixture increased in water content from a beginning value of about 6.5% by weight to a final value of about 21% by weight. This is very close to hydrate forming conditions for methanol-water mixtures. For example, at natural gas pressures and temperatures of about 2,000 psig and 4°C, hydrates will form with a 75% methanol-25% water by weight mixture. The water content of the ethanol-water azeotrope mixture showed a slight increase from about 6% to about 8.5% by weight. The isopropanol-water azeotrope mixture showed a decreasing water concentration in the residual mixture as the solution was evaporated. Example 3 The test apparatus described in Example 1 was modified to include a chilled section to determine the affect of cooling the gas stream, i.e., to determine if evaporated liquid would condense. The test mixture described in Example 2 were retested to determine the time required to completely dry the mixtures. The results of these tests are set forth in Table III. DRYING TIMES FOR 99% ALCOHOL-1% WATER MIXTURES Elapsed Time, hr:min Methanol-Water Dew Point, °C Ethanol-Water Dew Point, °C Isopropanol-Water Dew Point, °C 0:00 14:3 12.4 10.4 0:30 13.5 -2.2 -6.9 1:00 13.1 -3.2 -6.1 1:30 13.1 -3.2 -6.1 2:00 13.3 -3.2 -7.7 2:30 13.5 -3.4 -10.6 3:00 13.6 -3.7 -12.4 3:30 13.7 -3.9 -14.7 4:00 14.0 -4.4 -17.9 4:30 14.2 -4.9 -22.1 5:00 13.4 -5.3 -30.2 5:30 9.1 -5.9 ≤-70.0 6:00 6.7 -7.0 6:30 1.6 -8.0 7:00 -3.7 -9.6 7:30 -5.9 -13.4 8:00 -7.8 -28.1 8:30 -12.2 ≤-70.0 1 9:00 -17.3 9:30 -23.6 10:00 -33.1 10:30 ≤-70.0 1 From Table III it can be seen that the azeotrope mixtures with ethanol or isopropanol dried faster than the methanol-water mixture. As shown, the isopropanol-water azeotrope mixture dried in about half the time required for the methanol-water mixture to dry.

Claims: A method of treating the wet inside of a pipeline to reduce the formation of a hydrate when a hydrate-forming gaseous fluid is passed therethrough, which method comprises, before said gaseous fluid is passed therethrough, first contacting the wet inside of the pipeline with a liquid which forms an azeotropic mixture with water, the amount of said liquid being sufficient to form an azeotropic mixture with the water in the pipeline. A method according to claim 1, wherein said liquid is an alcohol, preferably ethanol, isopropanol or tert-butyl alcohol. A method according to claim 1, wherein said liquid is ethanol, npropanol or isopropyl ether, and the azeotropic mixture contains up to 5% water by weight. A method according to claim 1, 2 or 3, wherein said azeotropic liquid is contacted with said water in said pipeline by propelling at least one pipeline pig, preferably a plurality of separated pipeline pigs, in the pipeline by a stream of non-hydrate-forming gas. A method according to claim 4, wherein said stream of nonhydrate-forming gas is air, nitrogen or a process gas, preferably a waterabsorbing gas. A method of transporting a hydrate-forming gaseous fluid in a pipeline, wherein the pipeline is first treated by the method of any of claims 1 to 5, and thereafter the gaseous fluid is flowed therethrough, and wherein the amount of said liquid is sufficient to form an azeotropic mixture with said water whereby, as said mixture is evaporated in said pipeline, the water concentration in the remaining mixture does not approach that concentration which will form hydrates with said hydrate-forming gaseous fluid. A method according to claim 6, wherein said hydrate-forming gaseous fluid is natural gas.

Inventors: BRADLEY GARY W, BRADLEY, GARY W.
Applicants: HALLIBURTON ENERGY SERV INC, HALLIBURTON ENERGY SERVICES, INC.
Application year: 1998
Main classification: B08B17
IPC codes: F26B5, F17D1, B08B9, B08B17