EP0229434A1 - Process for the improvement of the conditioning of gasification agents utilized in an underground coal-gasification process - Google Patents
Process for the improvement of the conditioning of gasification agents utilized in an underground coal-gasification process Download PDFInfo
- Publication number
- EP0229434A1 EP0229434A1 EP86202396A EP86202396A EP0229434A1 EP 0229434 A1 EP0229434 A1 EP 0229434A1 EP 86202396 A EP86202396 A EP 86202396A EP 86202396 A EP86202396 A EP 86202396A EP 0229434 A1 EP0229434 A1 EP 0229434A1
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- EP
- European Patent Office
- Prior art keywords
- gasification
- water
- foam
- conditioning
- gasifying
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
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Classifications
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- E—FIXED CONSTRUCTIONS
- E21—EARTH DRILLING; MINING
- E21B—EARTH DRILLING, e.g. DEEP DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
- E21B33/00—Sealing or packing boreholes or wells
- E21B33/10—Sealing or packing boreholes or wells in the borehole
- E21B33/13—Methods or devices for cementing, for plugging holes, crevices, or the like
- E21B33/138—Plastering the borehole wall; Injecting into the formation
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- E—FIXED CONSTRUCTIONS
- E21—EARTH DRILLING; MINING
- E21B—EARTH DRILLING, e.g. DEEP DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
- E21B21/00—Methods or apparatus for flushing boreholes, e.g. by use of exhaust air from motor
- E21B21/14—Methods or apparatus for flushing boreholes, e.g. by use of exhaust air from motor using liquids and gases, e.g. foams
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- E—FIXED CONSTRUCTIONS
- E21—EARTH DRILLING; MINING
- E21B—EARTH DRILLING, e.g. DEEP DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
- E21B43/00—Methods or apparatus for obtaining oil, gas, water, soluble or meltable materials or a slurry of minerals from wells
- E21B43/16—Enhanced recovery methods for obtaining hydrocarbons
- E21B43/24—Enhanced recovery methods for obtaining hydrocarbons using heat, e.g. steam injection
- E21B43/243—Combustion in situ
Definitions
- the choice and packaging of the gasifying agent is an important element in the industrial development of underground gasification processes for coal.
- the oxygen + water vapor mixture was successfully used in the U.S.A. in the first underground gasification trials carried out on a pilot scale, in coal deposits located at shallow depths.
- the use of water vapor, in mixture with an oxygen-containing gas has many drawbacks for the industrial development of underground gasification of coal in large deposits located at medium or great depth.
- gasifying agent preheated to a temperature of the order of 200 ° C to 250 ° C also has the effect of causing the auto-ignition of the coal as soon as the gasifying agent comes into contact with it. , which excludes any possibility of developing an underground gasification process in which the gasification front would move against the flow direction of the gasifying agent.
- Patent AU-A-64329/80 proposes to use, as gasifying agent, air or oxygen at ambient temperature and to inject liquid water, continuously or intermittently, into the wells of injection of the gasifying agent to minimize the auto-ignition reactions of the carbon and control the position of the gasification zone.
- the primary objective of the present invention is to remedy these difficulties, by avoiding the segregation of the water and the gas which make up the gasifying agent.
- the water injected continuously or intermittently is added with a small dose of foaming agent.
- the water and the oxidizing gas are then treated in a foam generator, operating under high pressure, before being jointly injected into the deposit in the form of a foam constituting a stable and homogeneous two-phase mixture.
- the foaming agent can be a proteinaceous substance, of the kind which are used in the fight against fires and which consist of hydrolysed proteins obtained from natural substances such as: horns, hoofs of cattle, feathers, hair, fish scales ... It can also be a synthetic chemical, such as triethanolamine laurysulfate, sodium laury-ether sulfate or any other surfactant product, foam stabilizer, which makes it possible to maintain the homogeneity of the two-phase mixture during the duration of the gasifier's underground route.
- a synthetic chemical such as triethanolamine laurysulfate, sodium laury-ether sulfate or any other surfactant product, foam stabilizer, which makes it possible to maintain the homogeneity of the two-phase mixture during the duration of the gasifier's underground route.
- the distance between the foam generator and the gasification area will be minimized.
- each injection well is equipped with two concentric tubes: the external casing 1, used for injecting the oxidizing gas, ends at a short distance from the vein to be gasified by one or more filter screens 2 with mesh one to two millimeters in diameter.
- each injection well is fitted with a casing 5.
- a foam generator installed at the head of each of the injection wells is connected to this casing via a shut-off valve 6. Closing this valve allows the foam generator to be isolated, for maintenance operations, without decompressing the underground gasifier.
- the foam generator comprises a metal casing 7, capable of withstanding the gas injection pressure, one or more filter screens 8 with mesh of one to two millimeters in diameter and one or more sprayers, such as 9, located at a few decimetres upstream of the filter screens 8.
- the oxidizing gas under pressure is supplied via line 10 and the mixture of water and foaming agent through line 11.
- the second objective of using a gasifying agent in the form of foam is to avoid self-ignition of the coal in the presence of a gas with a high oxygen content, by ensuring a uniform distribution of water and gas and continuously maintaining a film of water on the surface of the coal which inhibits oxidation reactions.
- the third objective of using a gasifying agent in the form of foam is to promote the circulation of gas along the carbon front during gasification and to prevent a large fraction of the gasifying agent from bypassing the reaction, filtering through the cracks and cavities that remain between the rocky scree of the already carbonated area. This result is the consequence of the different behavior of the foam, depending on the temperature. In the hot zone near the reaction front, the rise in temperature evaporates the foam bubbles and the gasifying agent circulates along the carbon front in the form of a homogeneous gas phase.
- the evaporation of the water contained in the bubbles of foam causes a rapid decline in temperature and, after a relatively short time, the presence of the foam realizes the filling of the cracks and cavities that remain between the scree.
- a gasifying agent in the form of foam prepared from water added with a foaming agent and from a gas containing oxygen can be adapted to all underground coal gasification processes. .
- FIG. 3 shows, in a section passing through a vertical plane, an underground gasification process by filtration without prior connection, at the level of the vein, in which the well 12 is used for the injection of a gasifying agent, under high pressure, and the well 13 for the recovery of the gas produced.
- the gasification begins with the firing of the coal at the bottom of the well 13 and it progresses against the flow direction of the gasifying agent.
- the preconditioning of the gasifying agent in the form of foam ensures a uniform distribution of the water and the oxidizing gas, in the layer of carbon, and maintains on the surface of the carbon a film of water which inhibits the oxidation reactions. , which makes it possible to use a gasifying agent with a high oxygen content, without causing self-ignition of the coal in the vicinity of the injection well.
- FIG. 4 shows, in a section passing through a vertical plane, a gasification process in which the gasifying agent with high oxygen content is injected into a very long borehole 14, drilled in the thickness of the vein and coated with a steel casing, the gas produced being evacuated by the well 15.
- the gasification begins with the ignition of the coal, at a point located at a short distance from the well 15.
- the gasification operation includes alternating periods during which the injection point of the gasifying agent remains fixed and periods during which the injection point is retracted, by controlled combustion of the casing.
- the preconditioning of the gasifying agent in the form of foam prevents backburning of the casing.
- the retraction operations of the injection point of the gasifying agent are controlled by temporary interruptions of the water supply to the foam generator, going hand in hand with an adjustment of the gas flow rate to a value which allows the backburning of the casing. .
- FIG. 5 shows, in a section passing through the thickness of the layer, an underground gasification process in which the gasification operation takes place between an injection borehole 16 and a recovery borehole 17, along a channel 18 , open in the thickness of the layer, and which is limited on one side by the coal being gasified and on the other side by rock scree from the caving of the roof, in the zone 19 already gasified.
- the gasifying agent injected in the form of foam ensures the filling of the cracks and cavities that remain between the rocky scree of the blasted zone, which has the effect of channeling the flow of gases along the coal gasification front, in the area where the rise in temperature evaporates the bubbles that make up the foam.
Abstract
Description
Le choix et le conditionnement de l'agent gazéifiant constituent un élément important du développement industriel des procédés de gazéification souterraine du charbon.The choice and packaging of the gasifying agent is an important element in the industrial development of underground gasification processes for coal.
Le mélange oxygène + vapeur d'eau a été utilisé avec succès aux U.S.A. lors des premiers essais de gazéification souterraine réalisés à l'échelle pilote, dans des gisements de houille situés à faible profondeur. Cependant, l'utilisation de vapeur d'eau, en mélange avec un gaz contenant de l'oxygène, présente de nombreux inconvénients pour le développement industriel de la gazéification souterraine du charbon dans des gisements de grande étendue situés à moyenne ou à grande profondeur.The oxygen + water vapor mixture was successfully used in the U.S.A. in the first underground gasification trials carried out on a pilot scale, in coal deposits located at shallow depths. However, the use of water vapor, in mixture with an oxygen-containing gas, has many drawbacks for the industrial development of underground gasification of coal in large deposits located at medium or great depth.
Contrairement à ce qui se passe dans les installations de gazéification du charbon extrait, la vapeur ne peut pas être produite par récupération des pertes de chaleur des gazogènes. Il en résulte que la production de vapeur ne contribue pas à l'amélioration du bilan énergétique du procédé mais qu'elle entraîne une augmentation du prix de revient du gaz, par les investissements en générateurs de vapeur et par la consommation de combustible qu'elle nécessite.Contrary to what happens in gasification plants for extracted coal, steam cannot be produced by recovering heat losses from gas generators. It follows that the production of steam does not contribute to the improvement of the energy balance of the process but that it leads to an increase in the cost price of the gas, by the investments in steam generators and by the consumption of fuel which it need.
Par ailleurs, le développement de la gazéification souterraine dans les gisements profonds implique un allongement des circuits de distribution des agents gazéifiants et une augmentation de la pression de gazéification. Dans ces conditions, la nécessité de maintenir la température de l'agent gazéifiant au-dessus du point d'ébullition de l'eau entraîne une forte augmentation du coût des conduites de distribution et des puits d'injection, dont le diamètre doit être augmenté et pour lesquels il faut prévoir des compensateurs de dilatation et des revêtements isolants de forte épaisseur.In addition, the development of underground gasification in deep deposits involves an extension of the distribution circuits for gasifying agents and an increase in gasification pressure. Under these conditions, the need to maintain the temperature of the gasifying agent above the boiling point of water leads to a sharp increase in the cost of distribution pipes and injection wells, the diameter of which must be increased. and for which expansion compensators and thick insulating coatings must be provided.
L'utilisation d'un agent gazéifiant préchauffé jusqu'à une température de l'ordre de 200° C à 250° C a également pour effet de provoquer l'auto-inflammation du charbon dès que l'agent gazéifiant entre en contact avec lui, ce qui exclut toute possibilité de développement d'un procédé de gazéification souterraine dans lequel le front de gazéification se déplacerait à contre courant du sens d'écoulement de l'agent gazéifiant.The use of a gasifying agent preheated to a temperature of the order of 200 ° C to 250 ° C also has the effect of causing the auto-ignition of the coal as soon as the gasifying agent comes into contact with it. , which excludes any possibility of developing an underground gasification process in which the gasification front would move against the flow direction of the gasifying agent.
Le brevet AU-A-64329/80 propose d'utiliser, comme agent gazéifiant, de l'air ou de l'oxygène à température ambiante et d'injecter de l'eau liquide, de façon continue ou intermittente,dans les puits d'injection de l'agent gazéifiant pour minimiser les réactions d'auto-inflammation du charbon et contrôler la position de la zone de gazéification.Patent AU-A-64329/80 proposes to use, as gasifying agent, air or oxygen at ambient temperature and to inject liquid water, continuously or intermittently, into the wells of injection of the gasifying agent to minimize the auto-ignition reactions of the carbon and control the position of the gasification zone.
Cette façon de procéder évite les difficultés résultant de l'utilisation de la vapeur d'eau mais elle entraîne d'autres difficultés. En effet, l'eau et le gaz constituent deux phases de densités très différentes et, si la couche à gazéifier présente d'importantes différences de niveau en raison de son épaisseur ou de son pendage, les deux constituants de l'agent gazéifiant peuvent se séparer par gravité, avant que l'eau ait eu le temps de s'évaporer, cette séparation ayant pour conséquence l'arrêt des réactions dans la partie basse de la couche et la surchauffe des parties hautes.This procedure avoids the difficulties resulting from the use of water vapor but it causes other difficulties. Indeed, water and gas constitute two phases of very different densities and, if the layer to be gasified has significant differences in level due to its thickness or its dip, the two constituents of the gasifying agent can separate by gravity, before the water has had time to evaporate, this separation having the consequence of stopping the reactions in the lower part of the layer and overheating of the upper parts.
La présente invention a pour premier objectif de remédier à ces difficultés, en évitant la ségrégation de l'eau et du gaz qui composent l'agent gazéifiant. A cet effet, préalablement à son introduction dans le circuit souterrain, l'eau injectée de façon continue ou intermittente est additionnée d'une faible dose d'agent moussant. L'eau et le gaz oxydant sont ensuite traités dans un générateur de mousse, fonctionnant sous haute pression, avant d'être injectés conjointement dans le gisement sous la forme d'une mousse constituant un mélange diphasique stable et homogène.The primary objective of the present invention is to remedy these difficulties, by avoiding the segregation of the water and the gas which make up the gasifying agent. To this end, prior to its introduction into the underground circuit, the water injected continuously or intermittently is added with a small dose of foaming agent. The water and the oxidizing gas are then treated in a foam generator, operating under high pressure, before being jointly injected into the deposit in the form of a foam constituting a stable and homogeneous two-phase mixture.
L'agent moussant peut être une substance protéinique, du genre de celles qui sont utilisées dans la lutte contre les incendies et qui sont constituées par des protéines hydrolysées obtenues à partir de substances naturelles telles que : cornes, sabots de bovins, plumes, poils, écailles de poissons... Il peut également être un produit chimique de synthèse, tel que le laurysulfate de triéthanolamine, le laury-éther sulfate de sodium ou tout autre produit tensioactif, stabilisateur de mousse, qui permette de maintenir l'homogénéité du mélange diphasique pendant la durée du parcours souterrain de l'agent gazéifiant.The foaming agent can be a proteinaceous substance, of the kind which are used in the fight against fires and which consist of hydrolysed proteins obtained from natural substances such as: horns, hoofs of cattle, feathers, hair, fish scales ... It can also be a synthetic chemical, such as triethanolamine laurysulfate, sodium laury-ether sulfate or any other surfactant product, foam stabilizer, which makes it possible to maintain the homogeneity of the two-phase mixture during the duration of the gasifier's underground route.
Pour réduire la consommation d'agent moussant, la distance entre le générateur de mousse et la zone de gazéification sera réduite au minimum.To reduce the consumption of foaming agent, the distance between the foam generator and the gasification area will be minimized.
L'invention est décrite maintenant sur la base des dessins annexés, à titre d'exemples uniquement, montrant en :
- Figure 1 une première variante d'application du procédé suivant laquelle la production de mousse est réalisée au fond des puits d'injection des agents gazéifiants ;
- Figure 2 une seconde variante d'application, suivant laquelle la production de mousse est réalisée en surface ;
- Figures 3 à 5 l'application du procédé suivant l'invention respectivement à trois procédés de gazéification, pour lesquels le conditionnement de l'agent gazéifiant sous forme de mousse présente un intérêt particulier.
- Figure 1 a first alternative application of the method according to which the production of foam is carried out at the bottom of the injection wells of the gasifying agents;
- Figure 2 a second application variant, according to which the production of foam is carried out on the surface;
- Figures 3 to 5 the application of the process according to the invention respectively to three gasification processes, for which the packaging of the gasifying agent in the form of foam is of particular interest.
Dans la première variante chaque puits d'injection est équipé de deux tubes concentriques : le tubage extérieur 1, utilisé pour l'injection du gaz oxydant, se termine à faible distance de la veine à gazéifier par un ou plusieurs tamis filtrants 2 à mailles de un à deux millimètres de diamètre. Le tubage intérieur 3, utilisé pour l'injection du mélange d'eau et d'agent moussant, se termine à quelques décimètres en amont des tamis filtrants 2, par un ou plusieurs pulvérisateurs tels que 4 ou par un dispositif en tôle perforée, qui assure la dispersion de l'eau en fines gouttelettes.In the first variant, each injection well is equipped with two concentric tubes: the external casing 1, used for injecting the oxidizing gas, ends at a short distance from the vein to be gasified by one or more filter screens 2 with mesh one to two millimeters in diameter. The inner casing 3, used for injecting the mixture of water and foaming agent, ends a few decimeters upstream of the filter screens 2, by one or more sprayers such as 4 or by a perforated sheet device, which ensures the dispersion of water into fine droplets.
Dans la deuxième variante, chaque puits d'injection est équipé d'un tubage 5. Un générateur de mousse, installé en tête de chacun des puits d'injection est relié à ce tubage par l'intermédiaire d'une vanne d'arrêt 6. La fermeture de cette vanne permet d'isoler le générateur de mousse, pour procéder à des opérations d'entretien, sans décomprimer le gazogène souterrain. Le générateur de mousse comporte une enveloppe métallique 7, capable de résister à la pression d'injection du gaz, un ou plusieurs tamis filtrants 8 à mailles d'un à deux millimètres de diamètre et un ou plusieurs pulvérisateurs, tels que 9, situés à quelques décimètres en amont des tamis filtrants 8. Le gaz oxydant sous pression est alimenté par la conduite 10 et le mélange d'eau et d'agent moussant par la conduite 11.In the second variant, each injection well is fitted with a
L'utilisation d'un agent gazéifiant sous forme de mousse a pour deuxième objectif d'éviter l'auto-inflammation du charbon, en présence d'un gaz à haute teneur en oxygène, en assurant une répartition uniforme de l'eau et du gaz et en maintenant continuellement à la surface du charbon un film d'eau qui inhibe les réactions d'oxydation.The second objective of using a gasifying agent in the form of foam is to avoid self-ignition of the coal in the presence of a gas with a high oxygen content, by ensuring a uniform distribution of water and gas and continuously maintaining a film of water on the surface of the coal which inhibits oxidation reactions.
L'utilisation d'un agent gazéifiant sous forme de mousse a pour troisième objectif de favoriser la circulation du gaz le long du front de charbon en cours de gazéification et d'éviter qu'une fraction importante de l'agent gazéifiant contourne la zone de réaction, en filtrant à travers les fissures et les cavités qui subsistent entre les éboulis rocheux de la zone déjà gazéifiée. Ce résultat est la conséquence du comportement différent de la mousse, suivant la température. Dans la zone chaude proche du front de réaction, l'élévation de la température assure l'évaporation des bulles de mousse et l'agent gazéifiant circule, le long du front de charbon, sous la forme d'une phase gazeuse homogène. Dans la zone gazéi fiée, remplie d'éboulis rocheux, l'évaporation de l'eau contenue dans les bulles de mousse provoque un rapide déclin de la température et, au bout d'un temps relativement court, la présence de la mousse réalise le colmatage des fissures et des cavités qui subsistent entre les éboulis.The third objective of using a gasifying agent in the form of foam is to promote the circulation of gas along the carbon front during gasification and to prevent a large fraction of the gasifying agent from bypassing the reaction, filtering through the cracks and cavities that remain between the rocky scree of the already carbonated area. This result is the consequence of the different behavior of the foam, depending on the temperature. In the hot zone near the reaction front, the rise in temperature evaporates the foam bubbles and the gasifying agent circulates along the carbon front in the form of a homogeneous gas phase. In the gas zone folded, filled with rocky scree, the evaporation of the water contained in the bubbles of foam causes a rapid decline in temperature and, after a relatively short time, the presence of the foam realizes the filling of the cracks and cavities that remain between the scree.
L'utilisation d'un agent gazéifiant sous forme de mousse préparé à partir d'eau additionnée d'un agent moussant et à partir d'un gaz contenant de l'oxygène, peut s'adapter à tous les procédés de gazéification souterraine du charbon.The use of a gasifying agent in the form of foam prepared from water added with a foaming agent and from a gas containing oxygen, can be adapted to all underground coal gasification processes. .
La figure 3 montre suivant une coupe passant par un plan vertical un procédé de gazéification souterraine par filtration sans liaison préalable, au niveau de la veine, dans lequel le puits 12 est utilisé pour l'injection d'un agent gazéifiant, sous haute pression, et le puits 13 pour la récupération du gaz produit. La gazéification débute par la mise à feu du charbon au fond du puits 13 et elle progresse à contre courant du sens d'écoulement de l'agent gazéifiant. Le conditionnement préalable de l'agent gazéifiant sous forme de mousse assure une répartition uniforme de l'eau et du gaz oxydant, dans la couche de charbon, et maintient à la surface du charbon un film d'eau qui inhibe les réactions d'oxydation, ce qui permet d'utiliser un agent gazéifiant à haute teneur en oxygène, sans provoquer l'auto-inflammation du charbon au voisinage du puits d'injection.FIG. 3 shows, in a section passing through a vertical plane, an underground gasification process by filtration without prior connection, at the level of the vein, in which the
La figure 4 montre, suivant une coupe passant par un plan vertical, un procédé de gazéification dans lequel l'agent gazéifiant à haute teneur en oxygène est injecté dans un sondage de grande longueur 14, foré dans l'épaisseur de la veine et revêtu d'un tubage en acier, le gaz produit étant évacué par le puits 15. La gazéification débute par la mise à feu du charbon, en un point situé à une petite distance du puits 15. L'opération de gazéification comporte une alternance de périodes durant lesquelles le point d'injection de l'agent gazéifiant reste fixe et de périodes durant lesquelles le point d'injection est rétracté, par combustion contrôlée du tubage. Le conditionnement préalable de l'agent gazéifiant sous forme de mousse empêche la rétrocombustion du tubage. Les opérations de rétraction du point d'injection de l'agent gazéifiant sont contrôlées par des interruptions temporaires de l'alimentation en eau du générateur de mousse, allant de pair avec un ajustement du débit de gaz à une valeur qui permette la rétrocombustion du tubage.FIG. 4 shows, in a section passing through a vertical plane, a gasification process in which the gasifying agent with high oxygen content is injected into a very
La figure 5 montre suivant une coupe passant dans l'épaisseur de la couche un procédé de gazéification souterraine dans lequel l'opération de gazéification se déroule entre un sondage d'injection 16 et un sondage de récupération 17, le long d'un chenal 18, ouvert dans l'épaisseur de la couche, et qui est limité d'un côté par le charbon en cours de gazéification et de l'autre côté par des éboulis de roche provenant du foudroyage du toit, dans la zone 19 déjà gazéifiée. L'agent gazéifiant injecté sous forme de mousse assure le colmatage des fissures et des cavités qui subsistent entre les éboulis rocheux de la zone foudroyée, ce qui a pour effet de canaliser l'écoulement des gaz le long du front de gazéification du charbon, dans la zone où l'élévation de la température assure l'évaporation des bulles qui constituent la mousse.FIG. 5 shows, in a section passing through the thickness of the layer, an underground gasification process in which the gasification operation takes place between an
Claims (8)
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
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BE6048181 | 1986-01-16 | ||
BE6/48181A BE904055A (en) | 1986-01-16 | 1986-01-16 | PROCESS FOR IMPROVING THE CONDITIONING OF GASIFYING AGENTS USED IN SUBTERRANEAN GASIFICATION PROCESSES. |
Publications (2)
Publication Number | Publication Date |
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EP0229434A1 true EP0229434A1 (en) | 1987-07-22 |
EP0229434B1 EP0229434B1 (en) | 1990-04-18 |
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Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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EP19860202396 Expired - Lifetime EP0229434B1 (en) | 1986-01-16 | 1986-12-30 | Process for the improvement of the conditioning of gasification agents utilized in an underground coal-gasification process |
Country Status (3)
Country | Link |
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EP (1) | EP0229434B1 (en) |
BE (1) | BE904055A (en) |
DE (1) | DE3670526D1 (en) |
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US6725933B2 (en) | 2001-09-28 | 2004-04-27 | Halliburton Energy Services, Inc. | Method and apparatus for acidizing a subterranean well formation for improving hydrocarbon production |
WO2006018306A1 (en) * | 2004-08-17 | 2006-02-23 | Dew Pitchmastic Plc | Bioremediation foam and delivery method |
GB2518626A (en) * | 2013-09-25 | 2015-04-01 | Venture Engineering Services Ltd | Well apparatus and method for use in gas production |
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BE906016A (en) * | 1986-12-22 | 1987-04-16 | Ledent Pierre | NOVEL PROCESS FOR THE PRODUCTION OF METHANE BY SUBTERRANEAN GASIFICATION OF COAL. |
BE1012151A3 (en) * | 1995-02-14 | 2000-06-06 | Ledent Pierre | Method to operate a coal deposit by underground coal gasification |
US20100252255A1 (en) * | 2006-05-17 | 2010-10-07 | Karen Budwill | Increased microbial production of methane gas from subsurface hydrocarbon containing formations |
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1986
- 1986-01-16 BE BE6/48181A patent/BE904055A/en not_active IP Right Cessation
- 1986-12-30 EP EP19860202396 patent/EP0229434B1/en not_active Expired - Lifetime
- 1986-12-30 DE DE8686202396T patent/DE3670526D1/en not_active Expired - Lifetime
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EP1298280A1 (en) * | 2001-09-28 | 2003-04-02 | Halliburton Energy Services, Inc. | Fracturing with downhole foam mixing |
EP1298281A1 (en) * | 2001-09-28 | 2003-04-02 | Halliburton Energy Services, Inc. | Acid stimulating with downhole foam mixing |
US6662874B2 (en) | 2001-09-28 | 2003-12-16 | Halliburton Energy Services, Inc. | System and method for fracturing a subterranean well formation for improving hydrocarbon production |
US6719054B2 (en) | 2001-09-28 | 2004-04-13 | Halliburton Energy Services, Inc. | Method for acid stimulating a subterranean well formation for improving hydrocarbon production |
US6725933B2 (en) | 2001-09-28 | 2004-04-27 | Halliburton Energy Services, Inc. | Method and apparatus for acidizing a subterranean well formation for improving hydrocarbon production |
AU2002300782B2 (en) * | 2001-09-28 | 2007-01-18 | Halliburton Energy Services, Inc. | System and method for fracturing a subterranean well formation for improving hydrocarbon production |
WO2006018306A1 (en) * | 2004-08-17 | 2006-02-23 | Dew Pitchmastic Plc | Bioremediation foam and delivery method |
GB2518626A (en) * | 2013-09-25 | 2015-04-01 | Venture Engineering Services Ltd | Well apparatus and method for use in gas production |
US9702224B2 (en) | 2013-09-25 | 2017-07-11 | Venture Engineering Services Limited | Well apparatus and method for use in gas production |
CN107401393A (en) * | 2017-07-31 | 2017-11-28 | 山西晋城无烟煤矿业集团有限责任公司 | Water pumping gas production integration goaf gas extraction well casing programme and its construction method |
CN107401393B (en) * | 2017-07-31 | 2023-07-25 | 山西晋城无烟煤矿业集团有限责任公司 | Drainage and gas production integrated goaf gas extraction well body structure and construction method thereof |
Also Published As
Publication number | Publication date |
---|---|
BE904055A (en) | 1986-05-15 |
DE3670526D1 (en) | 1990-05-23 |
EP0229434B1 (en) | 1990-04-18 |
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