EP3147572B1 - Gas-saving device - Google Patents
Gas-saving device Download PDFInfo
- Publication number
- EP3147572B1 EP3147572B1 EP15777344.1A EP15777344A EP3147572B1 EP 3147572 B1 EP3147572 B1 EP 3147572B1 EP 15777344 A EP15777344 A EP 15777344A EP 3147572 B1 EP3147572 B1 EP 3147572B1
- Authority
- EP
- European Patent Office
- Prior art keywords
- gas
- fitting
- passages
- inlet
- flow rate
- 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.)
- Active
Links
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 10
- 239000012535 impurity Substances 0.000 claims description 9
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 claims description 5
- 238000005119 centrifugation Methods 0.000 claims description 5
- 229910052802 copper Inorganic materials 0.000 claims description 5
- 239000010949 copper Substances 0.000 claims description 5
- 230000008707 rearrangement Effects 0.000 claims description 4
- 238000011144 upstream manufacturing Methods 0.000 claims description 3
- 238000010438 heat treatment Methods 0.000 claims description 2
- 239000007789 gas Substances 0.000 description 35
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 18
- 239000003915 liquefied petroleum gas Substances 0.000 description 8
- 239000003345 natural gas Substances 0.000 description 6
- 238000002485 combustion reaction Methods 0.000 description 4
- 239000000446 fuel Substances 0.000 description 4
- 238000001914 filtration Methods 0.000 description 3
- 239000012530 fluid Substances 0.000 description 3
- 239000002245 particle Substances 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- ATUOYWHBWRKTHZ-UHFFFAOYSA-N Propane Chemical compound CCC ATUOYWHBWRKTHZ-UHFFFAOYSA-N 0.000 description 2
- 238000011049 filling Methods 0.000 description 2
- 239000003949 liquefied natural gas Substances 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 230000006641 stabilisation Effects 0.000 description 2
- 238000011105 stabilization Methods 0.000 description 2
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 1
- 239000005864 Sulphur Substances 0.000 description 1
- -1 among others Chemical compound 0.000 description 1
- 239000001273 butane Substances 0.000 description 1
- 238000005520 cutting process Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000004880 explosion Methods 0.000 description 1
- 230000008014 freezing Effects 0.000 description 1
- 238000007710 freezing Methods 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- IJDNQMDRQITEOD-UHFFFAOYSA-N n-butane Chemical compound CCCC IJDNQMDRQITEOD-UHFFFAOYSA-N 0.000 description 1
- OFBQJSOFQDEBGM-UHFFFAOYSA-N n-pentane Natural products CCCCC OFBQJSOFQDEBGM-UHFFFAOYSA-N 0.000 description 1
- 239000001294 propane Substances 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000009834 vaporization Methods 0.000 description 1
- 230000008016 vaporization Effects 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
- 238000003466 welding Methods 0.000 description 1
Images
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23K—FEEDING FUEL TO COMBUSTION APPARATUS
- F23K5/00—Feeding or distributing other fuel to combustion apparatus
- F23K5/02—Liquid fuel
- F23K5/14—Details thereof
- F23K5/18—Cleaning or purging devices, e.g. filters
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23K—FEEDING FUEL TO COMBUSTION APPARATUS
- F23K5/00—Feeding or distributing other fuel to combustion apparatus
- F23K5/002—Gaseous fuel
- F23K5/007—Details
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23D—BURNERS
- F23D14/00—Burners for combustion of a gas, e.g. of a gas stored under pressure as a liquid
- F23D14/46—Details, e.g. noise reduction means
- F23D14/68—Treating the combustion air or gas, e.g. by filtering, or moistening
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24C—DOMESTIC STOVES OR RANGESĀ ; DETAILS OF DOMESTIC STOVES OR RANGES, OF GENERAL APPLICATION
- F24C3/00—Stoves or ranges for gaseous fuels
- F24C3/12—Arrangement or mounting of control or safety devices
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23K—FEEDING FUEL TO COMBUSTION APPARATUS
- F23K2400/00—Pretreatment and supply of gaseous fuel
- F23K2400/10—Pretreatment
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23K—FEEDING FUEL TO COMBUSTION APPARATUS
- F23K2400/00—Pretreatment and supply of gaseous fuel
- F23K2400/20—Supply line arrangements
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23K—FEEDING FUEL TO COMBUSTION APPARATUS
- F23K5/00—Feeding or distributing other fuel to combustion apparatus
- F23K5/02—Liquid fuel
Definitions
- the object of the present invention is a device which, being placed downstream of the pressure regulator in a facility for the supply of liquefied petroleum gases or natural gas, improves fuel consumption efficiency in the facility, through loss recovery and impurities removal, by means of a filtering process, and stabilization of the gas flow by rearranging the molecules thereof.
- Liquefied petroleum gases are a mixture of butane and propane, the main component of natural gas being methane which represents between 70% and 90% of the composition thereof. Both can be supplied for consumption in tanks either fixed or portable; in the case of fixed tanks the filling thereof is carried out by means of tankers, and in the case of portable tanks the filling thereof is carried out in industrial plants and its supply to the final user is carried out by replacing the empty tank for a full one.
- the facility is similar both for natural gas and for liquefied petroleum gases, and it comprises a storage tank, a pressure regulator which reduces the fuel pressure inside the tank and controls the outgoing flow, the conveying pipeline which conveys the gas up to the devices consuming said fuel and among which there can be mentioned heating or household hot water boilers, cookers having gas burners or even fridges which use gas as an energy source.
- the efficiency of these facilities depends on the flow rate and the supply pressure and on the impurities percentage the natural gas or liquefied petroleum gases contain.
- the supply pressure and flow rate are reduced by the pressure drop produced by the facility pipes and connections, such as shut-off cocks.
- the supplied gas has certain impurities, such as other hydrocarbons, sulphur, water and other type of substances which, in its combustion process, produce highly polluting emissions or reduce the efficiency thereof.
- ES 1 079 980 U discloses a gas saving device according to the preamble of claim 1.
- DE1132876B refers to a security device for autogenous welding, which includes a system for cutting off gas supply, when water and waste/dirt accumulates inside the filter.
- US3394533A refers to a device for separating liquid and gaseous components of a fluid by means of a non-humid cone-shaped screen disposed in the flow path of the fluid.
- the capacity of separating fluid components with the device allows its use in controllable humidity systems.
- the invention disclosed solves the aforementioned drawbacks by means of a device according to the appended claim 1, which features easy mounting and maintenance, cheap manufacturing costs, which improves combustion efficiency and which reduces polluting emissions.
- the gas saving device for liquefied petroleum gases or natural gas object of the present invention is of the type which are mounted downstream of the pressure regulator and upstream of the devices consuming the liquefied petroleum gases or the natural gas, such as, among others, boilers, cookers, fridges, etc...
- the gas saving device comprises the following elements:
- Figure 1 Plan view of an outline of the saving gas device.
- Figure 1 shows a preferred embodiment of the gas saving device.
- the gas saving device shown in figure 1 is connected downstream to the natural gas or liquefied petroleum gases inlet pipe.
- the gas enters through a central inlet passage (2) into the first three-way T-fitting (1), and the flow thereof splits going out through the two side outlet passages (3) towards the side inlet passages (6) of the second three-way T-fitting (5), through the flexible or rigid pipes (4).
- Both flows coming from the first three-way T-fitting (1) are joined in the central outlet passage of the second fitting (7), increasing the gas speed.
- the gas flows into the steam trap (8) where the impurities contained therein are deposited; furthermore, the gas flows into said steam trap through an activated carbon filter (9), improving the particle and impurities capture, thus achieving the gas to come out substantially pure.
- the gas flows through a copper centrifugation coil (10), wherein the gas molecules rearrangement is achieved, obtaining flow stabilization in the facility and improving the circulation thereof. And after said step, the gas flows towards the consuming devices, through the flow rate regulator (11) which regularizes the gas flow to the consumption requirements.
- connections among the different elements of the invention and the supply facility are hermetically connected by means of the corresponding fittings and connections, such as gaskets, sealing elements, to guarantee the tightness of the facility and therefore to avoid gas leaks which can cause dangerous explosions.
- the gas saving device disclosed in the present invention increases the gas speed and supply flow rate so as to fulfil the requirements of the devices consuming said gas, eliminates the impurities it contains and prevents the problem of freezing by insufficient gas vaporization, thereby causing the combustion to produce a less amount of polluting emissions and particles, and making said combustion be more efficient.
- Another one of the multiple advantages of the invention is that the mounting thereof does not require modifications in the general facility already installed, but only the connection thereof to the inlet pipe for the gas supply.
Description
- The object of the present invention is a device which, being placed downstream of the pressure regulator in a facility for the supply of liquefied petroleum gases or natural gas, improves fuel consumption efficiency in the facility, through loss recovery and impurities removal, by means of a filtering process, and stabilization of the gas flow by rearranging the molecules thereof.
- It is well known in the state of the art the use of liquefied petroleum gases that are present in natural gas, which is used as fuel in domestic, commercial and industrial environments.
- Liquefied petroleum gases are a mixture of butane and propane, the main component of natural gas being methane which represents between 70% and 90% of the composition thereof. Both can be supplied for consumption in tanks either fixed or portable; in the case of fixed tanks the filling thereof is carried out by means of tankers, and in the case of portable tanks the filling thereof is carried out in industrial plants and its supply to the final user is carried out by replacing the empty tank for a full one.
- The facility is similar both for natural gas and for liquefied petroleum gases, and it comprises a storage tank, a pressure regulator which reduces the fuel pressure inside the tank and controls the outgoing flow, the conveying pipeline which conveys the gas up to the devices consuming said fuel and among which there can be mentioned heating or household hot water boilers, cookers having gas burners or even fridges which use gas as an energy source.
- The efficiency of these facilities depends on the flow rate and the supply pressure and on the impurities percentage the natural gas or liquefied petroleum gases contain. The supply pressure and flow rate are reduced by the pressure drop produced by the facility pipes and connections, such as shut-off cocks.
- On the other hand, the supplied gas has certain impurities, such as other hydrocarbons, sulphur, water and other type of substances which, in its combustion process, produce highly polluting emissions or reduce the efficiency thereof.
-
ES 1 079 980 Uclaim 1. -
DE1132876B refers to a security device for autogenous welding, which includes a system for cutting off gas supply, when water and waste/dirt accumulates inside the filter. -
US3394533A refers to a device for separating liquid and gaseous components of a fluid by means of a non-humid cone-shaped screen disposed in the flow path of the fluid. The capacity of separating fluid components with the device allows its use in controllable humidity systems. - The invention disclosed solves the aforementioned drawbacks by means of a device according to the appended
claim 1, which features easy mounting and maintenance, cheap manufacturing costs, which improves combustion efficiency and which reduces polluting emissions. - The gas saving device for liquefied petroleum gases or natural gas object of the present invention, is of the type which are mounted downstream of the pressure regulator and upstream of the devices consuming the liquefied petroleum gases or the natural gas, such as, among others, boilers, cookers, fridges, etc...
- The gas saving device comprises the following elements:
- A first inlet three-way T-fitting, having a central passage as a gas inlet and two side passages as a gas outlet, wherein the inlet central passage is connected to the pipe coming from the pressure regulator;
- A second outlet three-way T-fitting, having two side inlet passages and a central outlet passage, and wherein the central passage is connected to the first end of the steam trap;
- Two flexible or rigid pipes which connect the side outlet passages of the first fitting to the side inlet passages of the second fitting.
- A steam trap having a cylindrical shape and with the inner diameter thereof being longer than the inner diameter of the passages of the first and second fittings.
- A flow rate regulator, the flow rate regulator being connectable to a supply pipe of said consuming devices.
- Inside the steam trap, the gas flow is defined, wherein the gas is is first passed through an activated carbon filter, through which all the impurities carried in the gas are eliminated.
- Next, the gas is passed through a copper coil which causes a centrifugation by means of which the rearrangement of the molecules thereof is achieved.
- Then, through said flow rate regulator, wherein the end thereof situated downstream of said flow rate regulator is connected to the second end of the steam trap, and the end thereof situated upstream of the flow rate regulator is connected to the supply pipe of the consuming devices.
- By means of the gas filtering, using activated carbon, practically all particle and impurities are removed, thus improving the effect of the steam chamber as far as filtering is concerned. Furthermore, by using the copper centrifugation coil the rearrangement of gas molecules is achieved, improving the stability of the flow rate throughout the whole facility and reducing the friction loss.
-
Figure 1 : Plan view of an outline of the saving gas device. -
- 1. First inlet three-way T-fitting
- 2. Central inlet passage of the first fitting
- 3. Side inlet passage of the first fitting
- 4. Flexible or rigid pipes
- 5. Second outlet three-way T-fitting
- 6. Side inlet passage of the second fitting
- 7. Central outlet passage of the second fitting.
- 8. Steam trap
- 9. Activated carbon filter
- 10. Copper centrifugation coil
- 11. Flow rate regulator
-
Figure 1 shows a preferred embodiment of the gas saving device. - The gas saving device shown in
figure 1 is connected downstream to the natural gas or liquefied petroleum gases inlet pipe. The gas enters through a central inlet passage (2) into the first three-way T-fitting (1), and the flow thereof splits going out through the two side outlet passages (3) towards the side inlet passages (6) of the second three-way T-fitting (5), through the flexible or rigid pipes (4). Both flows coming from the first three-way T-fitting (1) are joined in the central outlet passage of the second fitting (7), increasing the gas speed. Then, the gas flows into the steam trap (8) where the impurities contained therein are deposited; furthermore, the gas flows into said steam trap through an activated carbon filter (9), improving the particle and impurities capture, thus achieving the gas to come out substantially pure. Still inside the steam trap (8), the gas flows through a copper centrifugation coil (10), wherein the gas molecules rearrangement is achieved, obtaining flow stabilization in the facility and improving the circulation thereof. And after said step, the gas flows towards the consuming devices, through the flow rate regulator (11) which regularizes the gas flow to the consumption requirements. - It is well known by those skilled in the art that the connections among the different elements of the invention and the supply facility are hermetically connected by means of the corresponding fittings and connections, such as gaskets, sealing elements, to guarantee the tightness of the facility and therefore to avoid gas leaks which can cause dangerous explosions.
- The gas saving device disclosed in the present invention, increases the gas speed and supply flow rate so as to fulfil the requirements of the devices consuming said gas, eliminates the impurities it contains and prevents the problem of freezing by insufficient gas vaporization, thereby causing the combustion to produce a less amount of polluting emissions and particles, and making said combustion be more efficient.
- Another one of the multiple advantages of the invention is that the mounting thereof does not require modifications in the general facility already installed, but only the connection thereof to the inlet pipe for the gas supply.
Claims (1)
- Gas saving device configured for gas consuming devices such as furnaces, stoves and heating boilers, of the type being mounted downstream of a pressure regulator and upstream of said consuming devices, said gas saving device comprising:a first inlet three-way T-fitting (1), having a central passage as a gas inlet and two side passages as a gas outlet, wherein the inlet central passage is connectable to a pipe coming from said pressure regulator;a second outlet three-way T-fitting (5), having two side inlet passages and a central outlet passage, and wherein the central passage is connected to the first end of a steam trap (8); the steam trap (8) having a cylindrical shape and with the inner diameter thereof being longer than the inner diameter of the central passages of said first T-fitting (1) and second T-fittings (5);two flexible or rigid pipes (4) which connect the side outlet passages of the first fitting (1) to the side inlet passages of the second fitting (5);a flow rate regulator (11), the flow rate regulator (11) being connectable to a supply pipe of said consuming devices; and
characterized in that,inside the steam trap (8), a gas flow is defined, wherein the gas is first passed through an activated carbon filter (9) through which al/ the impurities carried in the gas are eliminated;next, through a copper coil (10) which causes a centrifugation by means of which the rearrangement of the molecules thereof is achieved; then, through said flow rate regulator (11).
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
ES201430523A ES2547957B1 (en) | 2014-04-08 | 2014-04-08 | Gas saving device |
PCT/ES2015/070175 WO2015155388A1 (en) | 2014-04-08 | 2015-03-12 | Gas-saving device |
Publications (3)
Publication Number | Publication Date |
---|---|
EP3147572A1 EP3147572A1 (en) | 2017-03-29 |
EP3147572A4 EP3147572A4 (en) | 2018-03-07 |
EP3147572B1 true EP3147572B1 (en) | 2021-01-13 |
Family
ID=54250611
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP15777344.1A Active EP3147572B1 (en) | 2014-04-08 | 2015-03-12 | Gas-saving device |
Country Status (6)
Country | Link |
---|---|
US (1) | US20170184305A1 (en) |
EP (1) | EP3147572B1 (en) |
ES (2) | ES2547957B1 (en) |
MX (1) | MX362395B (en) |
PT (1) | PT3147572T (en) |
WO (1) | WO2015155388A1 (en) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB2535994B (en) * | 2015-02-27 | 2018-08-01 | Eco Device Ltd | Gas saving device |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3394533A (en) * | 1966-06-17 | 1968-07-30 | Lockheed Aircraft Corp | Liquid-gas separator |
Family Cites Families (32)
Publication number | Priority date | Publication date | Assignee | Title |
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GB191317972A (en) * | 1914-02-07 | 1914-12-03 | Charles William Thomas Harmer | A Gas Filter for Blowpipes. |
DE1132876B (en) * | 1959-02-20 | 1962-07-12 | Wittener Kunststoffgesellschaf | Safety template for welding systems of the oxy-fuel welding technology |
US3186150A (en) * | 1962-10-01 | 1965-06-01 | Mc Graw Edison Co | Apparatus for the treatment of gases |
US3347026A (en) * | 1965-01-14 | 1967-10-17 | Mc Graw Edison Co | Fluid separator |
US3977850A (en) * | 1976-02-17 | 1976-08-31 | Combustion Engineering, Inc. | Centrifugal separator |
US4297116A (en) * | 1978-07-10 | 1981-10-27 | Aitken, Inc. | Apparatus for separating foreign matter from a gas stream |
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JP3323781B2 (en) * | 1996-09-05 | 2002-09-09 | ę„ę®ę Ŗå¼ä¼ē¤¾ | Gas transfer piping |
CA2188839C (en) * | 1996-10-25 | 2001-01-02 | David Speed | Recovery of gas from drilling fluid returns in underbalanced drilling |
JP3778388B2 (en) * | 1997-02-17 | 2006-05-24 | ę±äŗ¬ē¦ęÆę Ŗå¼ä¼ē¤¾ | Gas purge combustor, gas purge method and gas replacement method using gas purge combustor |
JPH11182986A (en) * | 1997-12-22 | 1999-07-06 | Matsushita Electric Ind Co Ltd | Drier for air conditioner |
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KR200264661Y1 (en) * | 1999-06-03 | 2002-02-20 | ģ“ģģ° | The equipment absorb and exclude analien of heating boiler's fuel evaporation-burning equipment |
JP2003166700A (en) * | 2001-11-30 | 2003-06-13 | Nippon Sanso Corp | Valve for liquefied petroleum cylinder with decompression function |
US6835236B2 (en) * | 2002-01-25 | 2004-12-28 | Sporlan Valve Company | Molded core filter drier with filter media molded to core |
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US8640468B2 (en) * | 2008-05-21 | 2014-02-04 | Raytheon Company | Isothermal gas supply and method for minimizing the temperature excursion of a gas mixture released therefrom |
CN201715535U (en) * | 2010-05-28 | 2011-01-19 | å±±č„æé³ē ¤äø°åč„äø(éå¢)ęéč“£ä»»å ¬åø | Device for simply removing dust before blowing air entering into combustion furnace |
AU2013203259B2 (en) * | 2012-05-08 | 2016-09-22 | Release Energy Pty Ltd | Inline Non-targeted Component Removal |
US9764268B2 (en) * | 2012-12-14 | 2017-09-19 | Entegris, Inc. | Gas purification filter unit |
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-
2014
- 2014-04-08 ES ES201430523A patent/ES2547957B1/en not_active Revoked
-
2015
- 2015-03-12 WO PCT/ES2015/070175 patent/WO2015155388A1/en active Application Filing
- 2015-03-12 EP EP15777344.1A patent/EP3147572B1/en active Active
- 2015-03-12 US US15/302,026 patent/US20170184305A1/en not_active Abandoned
- 2015-03-12 PT PT157773441T patent/PT3147572T/en unknown
- 2015-03-12 ES ES15777344T patent/ES2879048T3/en active Active
- 2015-03-12 MX MX2016012807A patent/MX362395B/en active IP Right Grant
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3394533A (en) * | 1966-06-17 | 1968-07-30 | Lockheed Aircraft Corp | Liquid-gas separator |
Also Published As
Publication number | Publication date |
---|---|
PT3147572T (en) | 2021-04-19 |
WO2015155388A1 (en) | 2015-10-15 |
MX362395B (en) | 2019-01-15 |
EP3147572A4 (en) | 2018-03-07 |
US20170184305A1 (en) | 2017-06-29 |
EP3147572A1 (en) | 2017-03-29 |
MX2016012807A (en) | 2017-01-05 |
ES2547957B1 (en) | 2016-04-29 |
ES2547957A1 (en) | 2015-10-09 |
ES2879048T3 (en) | 2021-11-19 |
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