| 序号 | 专利名 | 申请号 | 申请日 | 公开（公告）号 | 公开（公告）日 | 发明人 |
|---|---|---|---|---|---|---|
| 141 | PROCESS FOR PRODUCING AMMONIA | EP14188350.4 | 2014-10-09 | EP3006400B1 | 2017-12-13 | Asensio, Salvador; Diaz, Antonio; Alonso, Rebeca; Hurtado, Ines; Vandervorst, Eric |
| The present invention relates to a process for producing ammonia from an aqueous solution containing ammonium chloride using an electrodialyzer cellstack. | ||||||
| 142 | PROCESS FOR PRODUCING SODIUM CARBONATE/BICARBONATE | EP15820148.3 | 2015-12-22 | EP3244986A1 | 2017-11-22 | VANDERVORST, Eric; SAVARY, David Jean Lucien; DUPONT, Gérard; WALRAVENS, Hugo; DUBOIS, Eric; COQUEREL, Jean-Paul; DAVOINE, Perrine; CAVALIER, Karine; HURTADO DOMINGEZ, Ines; ASENSIO, Salvador |
| Process for producing sodium carbonate with ammonia and/or for producing refined sodium bicarbonate, wherein: a low CO2 content gas generated by a unit for producing sodium carbonate with ammonia and/or generated by a unit for producing refined sodium bicarbonate is enriched into a CO2-enriched gas by using a CO2 concentration module, such as an amine-type or ammonia or PSA or TSA or cryogenic distillation or membrane-type CO2 concentration module, and said CO2-enriched gas has an increased CO2 content of: +10% (at least) to +90% (at most), by volume on a dry gas basis relative to the CO2 concentration of the low content gas, and the CO2-enriched gas is subsequently recycled to the unit for producing sodium carbonate with ammonia and/or to the unit for producing refined sodium bicarbonate, to produce sodium carbonate, or sodium bicarbonate, or to carbonate at least one part of effluent from the unit for producing sodium carbonate and/or from the unit for producing sodium bicarbonate. | ||||||
| 143 | ARRANGEMENT AND PROCESS FOR INTEGRATED FLUE GAS TREATMENT AND SODA ASH PRODUCTION | EP14156466.6 | 2014-02-25 | EP2910295B1 | 2016-08-31 | Stallmann, Olaf; Weingaertner, Christoph; Balfe, Michael Charles |
| 144 | Arrangement and process for integrated flue gas treatment and soda ash production | EP14156466.6 | 2014-02-25 | EP2910295A1 | 2015-08-26 | Stallmann, Olaf; Weingaertner, Christoph; Balfe, Michael Charles |
The arrangement (1) of a flue gas treatment system (2) by carbonation-calcination loop and soda ash production system (3) by Solvay process has CaO and heat for use in the soda ash production system (3) extracted from the flue gas treatment system (2).
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| 145 | Integrated carbon dioxide removal and ammonia-soda process | EP13151691.6 | 2013-01-17 | EP2757071A1 | 2014-07-23 | Kniesburges, Peter |
The present invention relates to an method for producing sodium carbonate by integration of a carbon dioxide capture process with an ammonia-soda process. The present invention moreover relates to a plant for producing sodium carbonate comprising a carbon dioxide capture system and an ammonia-soda system. Uses of fluid streams generated in a carbon dioxide capture process in an ammonia-soda process is moreover disclosed.
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| 146 | Verfahren zur Herstellung von Kalkmilch für die Sodaherstellung | EP13004687.3 | 2013-09-26 | EP2712845A8 | 2014-05-07 | Eichhorn, Ulrich; Hosenthien, Peer; Witte, Torsten; Zutz, Holger |
Das Verfahren zur Herstellung von Soda kann angewendet werden in Sodawerken, die nach dem Solvay-Prozess arbeiten. Das Verfahren zur Herstellung von Kalkmilch für die Sodaherstellung ist gekennzeichnet durch einen Vorwärmerkalk 1 aus dem Herstellungsprozess von Zement und einen Feinkalk 2 aus dem Herstellungsprozess von Kalk, welche in einem Mischvorgang 3 zu einem Vorwärmerkalkgemisch 4 gemischt, das Vorwärmerkalkgemisch 4 mit einem Branntkalk 5 in zwei nachfolgenden Prozessstufen, einem Mischvorgang 6 gemischt und in einem Löschvorgang 7 zu Kalkmilch 8 gelöscht werden und die so hergestellte Kalkmilch 8 dem nachfolgenden Solvay-Prozess zur Herstellung von Soda zugeführt wird.
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| 147 | Verfahren zum Behandeln von Rauchgas bei Kraftwerken und anderen Anlagen | EP07113903.4 | 2007-08-07 | EP1958683A3 | 2010-08-25 | Krass, Florian, Dr. |
Verfahren zum Binden von gasförmigem CO2, wobei eine konzentrierte Salzsole zum Einsatz kommt. Dabei wird Ammoniak (NH3) und das zu bindende CO2 in die konzentrierte Salzsole eingeleitet. Es entsteht dabei Natriumhydrogencarbonat und/oder Natriumcarbonat, das aus der ammoniakhaltigen Sole entnommen werden kann. In weiteren vor- oder nachgeschalteten Teilprozessen können weitere Bestandteile des Rauchgases eliminiert oder deutlich reduziert werden.
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| 148 | PROCESS FOR PREPARING ULTRA-FINE SODIUM BICARBONATE POWDER | EP07719419.9 | 2007-03-26 | EP2007681A1 | 2008-12-31 | TINSON, Art; D'UVA, Salvatore; HU, Jianzhong; LEFAS, John |
| Ultra-fine sodium bicarbonate powder (mean particle size less than 5 microns) is produced by the mixing and reaction under agitation at control temperatures of solutions of ammonium bicarbonate and sodium chloride. Precipitated sodium bicarbonate is separated by filtration as a slurry which is dried to produce ultra-fine sodium bicarbonate. Ultra-fine sodium bicarbonate produced by this method also exhibits a narrow particle size distribution which is advantageous in blowing agents for thermoplastic resins, to produce a foamed resin with small cells of a narrow size distribution. | ||||||
| 149 | METHOD FOR RECOVERING PURIFIED SODIUM BICARBONATE AND AMMONIUM SULFATE | EP04709968.4 | 2004-02-11 | EP1603834B1 | 2006-11-22 | BICHEL, Joe; SCHAAF, Stephen |
| Process for making ammonium sulfate and sodium bicarbonate from a solution of sodium sulfate and other sodium salts such as sodium sulfite, carbonate, chloride, fluoride, nitrate and nitrite, using evaporation and precipitation unit operations. The sodium bicarbonate produced is suitable for use as a scrubbing agent for flue gas purification. | ||||||
| 150 | Composition comprenant au moins du bicarbonate de sodium, son procédé d'obtention et ses utilisations | EP06000985.9 | 1996-10-31 | EP1659097A1 | 2006-05-24 | Fourcot, Fabrice; Pouxviel, Jean-Claude; Zing, Christophe |
La présente invention a pour objet une nouvelle composition comprenant au moins du bicarbonate de sodium, son procédé d'obtention ainsi que ses utilisations notamment dans le traitement de fumées, dans le domaine de la détergence, et en alimentation animale. La nouvelle composition selon l'invention qui comprend au moins du bicarbonate de sodium, au moins du carbonate de sodium, et au moins de l'ammoniac sous forme de sels d'ammonium, est obtenue par un traitement thermique d'un bicarbonate ammoniacal à une température comprise entre 20 et 150°C. |
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| 151 | METHOD FOR RECOVERING PURIFIED SODIUM BICARBONATE AND AMMONIUM SULFATE | EP04709968.4 | 2004-02-11 | EP1603834A1 | 2005-12-14 | BICHEL, Joe; SCHAAF, Stephen |
| Process for making ammonium sulfate and sodium bicarbonate from a solution of sodium sulfate and other sodium salts such as sodium sulfite, carbonate, chloride, fluoride, nitrate and nitrite, using evaporation and precipitation unit operations. The sodium bicarbonate produced is suitable for use as a scrubbing agent for flue gas purification. | ||||||
| 152 | PROCESS FOR DESALINATION OF SEAWATER | EP00975010.0 | 2000-09-27 | EP1335881B1 | 2004-06-02 | Rongved, Paul |
| The invention relates to desalination of Seawater and of brackish water and removal of harmful CO2 gas in exhaust from combustion apparatuses. The exhaust, rich in carbon dioxide (CO2) is diverted to a process chamber, where Seawater, after being mixed with ammonia, as a catalyst to weaken the salt molecules, is pumped into the chamber and dispersed at many points near the top as a fine spray, exposing the salt to the CO2 gas there. The internal bonds of the salt molecules (NACl) are weaker by the ammonia in the water attaching and pulling on their Cl atom. The CO2 in the chamber is attaching and pulling on the Na atom of the salt molecules and further reduces the bond, breaking them apart. Two heavy solids are formed and are removed in a clarifier below. Desalinated seawater in large quantities per ton of salt, over flows from the clarifier, for use in communities and for agriculture. Therewith is also harmful CO2 in the exhaust removed, before being discharged from the process chamber to the environment. The solid NH4Cl can be recycled for ammonia and the second solid NH2CO3 is a saleable product, which may more than pay for the process. | ||||||
| 153 | PROCESS FOR DESALINATION OF SEAWATER | EP00975010.0 | 2000-09-27 | EP1335881A1 | 2003-08-20 | Rongved, Paul |
| The invention relates to desalination of Seawater and of brackish water and removal of harmful CO2 gas in exhaust from combustion apparatuses. The exhaust, rich in carbon dioxide (CO2) is diverted to a process chamber, where Seawater, after being mixed with ammonia, as a catalyst to weaken the salt molecules, is pumped into the chamber and dispersed at many points near the top as a fine spray, exposing the salt to the CO2 gas there. The internal bonds of the salt molecules (NACl) are weaker by the ammonia in the water attaching and pulling on their Cl atom. The CO2 in the chamber is attaching and pulling on the Na atom of the salt molecules and further reduces the bond, breaking them apart. Two heavy solids are formed and are removed in a clarifier below. Desalinated seawater in large quantities per ton of salt, over flows from the clarifier, for use in communities and for agriculture. Therewith is also harmful CO2 in the exhaust removed, before being discharged from the process chamber to the environment. The solid NH4Cl can be recycled for ammonia and the second solid NH2CO3 is a saleable product, which may more than pay for the process. | ||||||
| 154 | METHOD FOR PRODUCTION OF SODIUM BICARBONATE, SODIUM CARBONATE AND AMMONIUM SULFATE FROM SODIUM SULFATE | EP96918561.0 | 1996-06-21 | EP0833799B1 | 2001-12-05 | KRESNYAK, Steve Ormiston Mining & Smelting Co.; HALLDORSON, Jake Ormiston Mining & Smelting Co.; HANTKE, Mark Ormiston Mining & Smelting Co. Ltd. |
| 155 | COMPOSITION COMPRENANT AU MOINS DU BICARBONATE DE SODIUM, SON PROCEDE D'OBTENTION ET SES UTILISATIONS | EP96937380.0 | 1996-10-31 | EP0858429A1 | 1998-08-19 | FOURCOT, Fabrice; POUXVIEL, Jean-Claude; ZING, Christophe |
| A novel composition containing at least sodium bicarbonate, a preparation method therefor, and uses thereof, in particular for processing flue gases, in detergents and in animal food, are disclosed. Said novel composition containing at least sodium bicarbonate, at least sodium carbonate and at least ammonia in the form of ammonium salts is produced by heat treating ammonium bicarbonate at 20-150 °C. | ||||||
| 156 | Destillative Abtrennung von Ammoniak aus der Soda-Endlauge | EP86116950.6 | 1986-12-05 | EP0227978B1 | 1990-03-14 | Dust, Hanspeter, Dr.; Eisenhauer, Gerhard, Dr.; Wickenhäuser, Gerhard, Dr. |
| 157 | Destillative Abtrennung von Ammoniak aus der Soda-Endlauge | EP86116950.6 | 1986-12-05 | EP0227978A2 | 1987-07-08 | Dust, Hanspeter, Dr.; Eisenhauer, Gerhard, Dr.; Wickenhäuser, Gerhard, Dr. |
© Die destillative Abtrennung von Ammoniak aus alkalisch gestellten Flüssigkeiten, insbesondere mit Kalkmilch versetzten Mutterlaugen des Ammoniak-Soda-Verfahrens in Destillationskolonnen mit Böden erfolgt mit Hilfe von ebenen Lochböden ohne Ablaufschächten, deren Lochböden einen Abstand von 20 bis 150cm, einen Öffnungsquerschnitt von 5 bis 25% und Lochdurchmesser zwischen 0,5 und 7 cm aufweisen. |
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| 158 | Verfahren zum Entfernen von Schwefeloxiden aus chloridhaltigen Verbrennungsabgasen | EP79200210.7 | 1979-05-04 | EP0005301A1 | 1979-11-14 | Voeste, Theodor, Dipl.-Chem. |
Verfahren zum Entfernen von Schwefeloxiden aus Verbrennungsabgas, insbesondere Kraftwerksabgas, wobei das Abgas durch eine Reaktionszone strömt, die nach der Art eines Sprühtrockners arbeitet. In die Reaktionszone wird eine Reinigungsflüssigkeit eingesprüht, die aus einer wässrigen Lösung von Soda und/oder Natriumbicarbonat besteht. In der Reaktionszone wird der Wassergehalt der Reinigungsflüssigkeit durch den Wärmeinhalt des Abgases praktisch vollständig verdampft und das Abgas anschliessend durch ein Filter geleitet. Aus der Reaktionszone und dem Filter werden wasserfreie Feststoffprodukte abgezogen, die zu mindestens 75 Gew.% aus Natriumsulfit, Natriumsulfat und Natriumchlorid bestehen. Diese Feststoffprodukte werden wieder zu Soda aufgearbeitet. Zu diesem Zweck werden die Feststoffprodukte gelöst, Sulfit zu Sulfat oxidiert, so dass eine Natriumsulfat und Natriumchlorid enthaltende Lösung entsteht. Aus dieser Lösung wird das Sulfat abgetrennt und die verbleibende Lösung durch das Solvay-Verfahren zu Soda aufgearbeitet. |
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| 159 | PROCESS FOR MANUFACTURING AN AQUEOUS SODIUM CHLORIDE SOLUTION | US15554381 | 2016-03-02 | US20180050919A1 | 2018-02-22 | Thierry DELPLANCHE; Marc THIJSSEN; Dirk BREUGELMANS |
| A process for manufacturing an aqueous sodium chloride solution and the use of such solution for the manufacturing of crude sodium bicarbonate from SOLVAY ammonia process or for the manufacturing of soda ash, comprising the steps of: a) dispersing a first solid material comprising sodium chloride, sodium carbonate, and sodium sulfate, and a second solid material comprising calcium chloride in an aqueous liquid to produce an aqueous medium; b) subjecting the aqueous medium to clarification to produce a clarified aqueous medium; and c) recovering the clarified aqueous medium as aqueous sodium chloride solution; wherein a weight L/S ratio between the weight of the aqueous liquid used to produce the aqueous medium and the total weight of the first solid material and the second solid material is in the range of from 0.7 to 3.5. | ||||||
| 160 | Method and apparatus on halting global warming | US15618031 | 2017-06-08 | US20170275173A1 | 2017-09-28 | Hsiao-Yuan Li |
| We have described herein a method and associated apparatus that can halt global warming with significant economic benefits. They include (1), re-scrub half the carbon dioxide emitted from calcining baking soda into soda ash to produce twice as much soda ash and twice as much ammonium chloride as comparing with the standard Solvay ammonia soda ash process; Use the ammonium chloride as sugarcane fertilizer producing fuel ethanol, and bagasse, a photosynthesized bio-fuel from carbon dioxide already presented in the earth atmosphere for power generation, and (2), expand the sugarcane plantation areas into desert oasis using desert heat to produce distilled water for irrigation, pumped by solar heated hydraulic press pumps to supplement insufficient rain forest resources on earth's continents to accelerate reaching “carbon neutral” on capture annually twenty five billion tons of anthropogenic carbon dioxide from earth atmosphere economically. | ||||||
