序号 专利名 申请号 申请日 公开(公告)号 公开(公告)日 发明人
221 High purity diphenyl sulfone, preparation and use thereof for the preparation of a poly(aryletherketone) EP14151155.0 2009-10-23 EP2722353A1 2014-04-23 Louis, Chantal; Gandy, William; Ryan, Edward; Underwood, Geoffrey Scott; Yi, Kong

The presence of certain impurities in diphenyl sulfone have a deleterious effect on the properties of the poly(aryletherketone)s produced therein, including one or more of color, melt stability, molecular weight, crystallinity, etc. and here identify those impurities and provide processes for the removal of such impurities.

222 UTILISATION OF DESALINATION WASTE EP09827050 2009-11-20 EP2361224A4 2013-03-06 ZOU LINDA YUAN
223 Process for the joint production of sodium carbonate and sodium bicarbonate EP10166931.5 2010-06-22 EP2399866A1 2011-12-28 Breton, Claude; Chau, Thoi-Dai; Piet, Joffrey

Process for the production of sodium carbonate and sodium bicarbonate out of trona by crushing trona ore and dissolving it in a leaching tank containing a solution comprising sodium carbonate and sodium bicarbonate, and an additive selected from the group consisting of: phosphates, phospholipids, carboxylates, carboxilic acids, and combinations thereof, saturated in sodium bicarbonate, in order to produce solid particles suspended in a production solution comprising sodium carbonate, the solid particles containing insoluble impurities and at least 65% by weight of sodium bicarbonate. The solid particles are separated from the production solution containing sodium carbonate. At least part of the production solution containing sodium carbonate is taken out of the leaching tank.

224 UTILISATION OF DESALINATION WASTE EP09827050.7 2009-11-20 EP2361224A1 2011-08-31 ZOU, Linda, Yuan
A process for producing soda ash from brine waste, the process including reacting brine waste with carbon dioxide and ammonia to produce soda ash, wherein at least a portion of the ammonia is regenerated from ammonium chloride produced during the reaction, the regeneration ideally be achieved by the use of a weak base anion exchange resin.
225 HIGH PURITY DIPHENYL SULFONE, PREPARATION AND USE THEREOF FOR THE PREPARATION OF A POLY(ARYLETHERKETONE) EP09740326.5 2009-10-23 EP2342260A1 2011-07-13 LOUIS, Chantal; GANDY, William; RYAN, Edward; UNDERWOOD, Geoffrey Scott; YI, Kong
The presence of certain impurities in diphenyl sulfone have a deleterious effect on the properties of the poly(aryletherketone)s produced therein, including one or more of color, melt stability, molecular weight, crystallinity, etc. and here identify those impurities and provide processes for the removal of such impurities.
226 A PROCESS FOR THE PRODUCTION OF HCL GAS FROM CHLORIDE SALTS AND FOR THE PRODUCTION OF CARBOHYDRATES EP09787553.8 2009-09-01 EP2321218A1 2011-05-18 BANIEL, Avram; EYAL, Aharon
A process for the co-production of gaseous HCI and a salt product comprising a cation and an anion, which process comprises the steps of a. providing an aqueous solution comprising protons, chloride anions, and cations and anions of the salt product, b. bringing the solution into contact with a substantially immiscible extractant, the extractant comprising: 1) an oil soluble amine, which amine is substantially water insoluble both in free and in salt form; and 2) a carrier solvent for the amine; whereupon HCI selectively transfers to the extractant to form an HCI- carrying extractant and a chloride depleted aqueous solution containing the salt product; c. separating the HCI-carrying extractant from the chloride-depleted aqueous solution; and d. distilling HCI from the separated HCI-carrying extractant to form gaseous HCI and HCI depleted extractant.
227 PREPARATION AND USE OF CATIONIC HALIDES, SEQUESTRATION OF CARBON DIOXIDE EP06752673 2006-07-05 EP1899043A4 2011-03-23 BLAKE STEPHEN WILLIAM MATTHEW; CUFF CHRISTOPHER
A process is described for sequestering carbon dioxide. In the process, a carbonate, oxide or hydroxide of a divalent cation is reacted with the carbon dioxide and water and/or with a species resulting from the dissolution of the carbon dioxide in water, to form a hydrogen carbonate of the divalent cation. The carbonate, oxide or hydroxide of the divalent cation has a low solubility in water. The divalent cation of the hydrogen carbonate of the divalent cation thus formed is exchanged for a monovalent cation using an ion exchange medium, to produce a solution of a hydrogen carbonate of the monovalent cation.
228 INTEGRATED CHEMICAL PROCESS EP07815592.6 2007-11-21 EP2097164A1 2009-09-09 BRENT, Geoffrey Frederick
A mineral carbonation process, characterised in that the silicate feedstock is thermally activated by using heat generated from the combustion of fuel prior to reacting the activated slurry feedstock with carbon dioxide.
229 PREPARATION AND USE OF CATIONIC HALIDES, SEQUESTRATION OF CARBON DIOXIDE EP06752673.1 2006-07-05 EP1899043A1 2008-03-19 BLAKE, Stephen William Matthew; CUFF, Christopher
A process is described for sequestering carbon dioxide. In the process, a carbonate, oxide or hydroxide of a divalent cation is reacted with the carbon dioxide and water and/or with a species resulting from the dissolution of the carbon dioxide in water, to form a hydrogen carbonate of the divalent cation. The carbonate, oxide or hydroxide of the divalent cation has a low solubility in water. The divalent cation of the hydrogen carbonate of the divalent cation thus formed is exchanged for a monovalent cation using an ion exchange medium, to produce a solution of a hydrogen carbonate of the monovalent cation.
230 PROCESS FOR THE TREATMENT OF WASTE OR GASEOUS STREAMS EP04760109.1 2004-04-21 EP1618067A2 2006-01-25 MANSOUR, Momtaz, N.; CHANDRAN, Ravi
The present invention is directed to a process for treating, reducing, and/or stabilizing various wastes or flue gases. In one embodiment, the process is directed to treatment of alkali bearing wastes that include nitrate and/or nitrite-rich wastes. Optionally, the disclosed method can be utilized for treatment of hazardous wastes, including radioactive hazardous waste compounds. In general, the present invention includes processing a waste or gaseous stream with the addition of suitable carbon-containing additives to treat and reduce nitrogen-containing compounds in the waste. Additives may be gaseous, liquid or solid reduction-promoting agents, catalysts, and the like. The reaction products obtained from the process of the invention include mainly alkali carbonate, nitrogen, hydrogen, carbon monoxide and carbon dioxide.
231 WIRKSTOFF UND VORRICHTUNG ZUR ENTSÄUERUNG VON SCHRIFTGUT EP98958763.9 1998-12-16 EP1084299A1 2001-03-21 HERREN, Christian; MONKEWITZ, Martin
Modern techniques for manufacturing paper using mechanical wood pulp has lead to a persistent over-acidification of printed manner, and threatens to permanently destroy the same. This over-acidification can be neutralized by using an alkaline active substance whose main component is a salt having a relatively low water affinity. An alkaline deposit can be deposited on the paper by also using said alkaline active substance. A device suited for deacidification using this active substance comprises a case (10) which can be closed. Printed matter which can be fanned out in a stand (1) is treated in said case. The printed matter is treated by introducing the powdered active substance via a screw conveyor (32) into an air stream circulated by a fan (19a), whereby the printed matter is leafed through in order to expose it to the active substance.
232 PROCEDE D'EPURATION D'UN GAZ EN COMPOSES ACIDES EP99906167.4 1999-01-21 EP1051353A1 2000-11-15 GHODSI, Mehdi; HAVELANGE, Nicolas; POELLAER, Stéphane; NINANE, Léon; DEMILIE, Paul
The invention concerns a method for purifying a gas consisting of acid compounds which consists in subjecting the gas to a dry or semi-wet treatment with a basic reagent comprising an anhydrous sodium carbonate powder, with specific surface area greater more than 2 m2/g, which while it is being handled, is maintained in an atmosphere with relative humidity less than 20 % and/or to which a desiccant has been added.
233 PRODUIT CARBONE RICHE EN LITHIUM UTILISABLE COMME ELECTRODE NEGATIVE DANS UN ACCUMULATEUR AU LITHIUM EP98954533.0 1998-11-06 EP1028914A1 2000-08-23 WILLMANN, Patrick; BILLAUD, Denis; THEVENOT, Laurent
The invention concerns a carbon product rich in lithium for use as negative electrode in a lithium cell, corresponding to the following formula (I): LiNaxCyOz in which x, y and z are such that: 0.4≤x≤0.6; 2.5≤y≤3.5; 0.2≤z≤1. It can be prepared by intercalation of lithium by electrochemical process in a graphite-sodium-oxygen compound.
234 PROCEDE D'OBTENTION DE SEL, NOTAMMENT DE CHLORURE DE POTASSIUM, PAR LIXIVIATION ET REFROIDISSEMENT DE LA SOLUTION EP96902329.0 1996-02-02 EP0827487B1 2000-04-05 Mahue, Bernard
A method for preparing a salt, particularly potassium chloride, by leaching a salt formation with an injected brine solution, and separating salts from the saturated solution by cooling said solution to the eutectic point temperature, recycling the hydrates and crystal mixtures, separating out the crystals, and reinjecting the remaining brine solution.
235 Zero discharge pulp mill cascading water management EP96250103.7 1993-12-07 EP0728864A3 1999-07-28 Nykanen, Tuomo S., Kamyr, Inc.; Grenwood, Brian F., Kamyr, Inc.; Gullichsen, Johan; Kiiskila, Erkki; Mattelmaki, Eskor; Phillips, Joseph, R.; Richardson, Jan T.; Ryham, Rolf; Soderman, Jarmo; Wiklund, Karl G.

The invention relates to a method and apparatus for managing liquid streams in a cellulose pulp mill having a digester (210), a bleach plant (212) and at least first, second and third loops (94-97) of liquid streams in the pulp mill, the loops having liquid streams therein of significantly different contamination levels, the contamination level gradually increasing from the first loop to the third loop. The method comprises the steps of:

  • (a) sensing (in 309, 98) the contamination level in at least the first and second loops;
  • (b) when the contamination level in the first loop exceeds a predetermined level, discharging some of the contaminated liquid from the first loop to the second loop, and replacing it with less contaminated liquid;
  • (c) when the contamination level in the second loop exceeds a predetermined level, discharging some of the contaminated liquid from the second loop to the third loop, and replacing it with less contaminated liquid; and
  • (d) purifying (e.g. in 229 230, 231) the most contaminated liquid from the loops to produce the less contaminated liquid for addition to at least step (b).

236 ZERO DISCHARGE MILL DISTILLATION, SALT RECOVERY, AND WATER MANAGEMENT EP94909414.0 1993-12-07 EP0687323A1 1995-12-20 NYKANEN, Tuomo, S.; GRENWOOD, Brian, F.; GULLICHSEN, Johan; KIISKILA, Erkki; MATTELMAKI, Esko; PHILLIPS, Joseph, R.; RICHARDSON, Jan, T.; RYHAM, Rolf; SODERMAN, Jarmo; WIKLUND, Karl, G.
In minimizing effluents from a cellulose pulp mill, liquid effluents from a bleach plant are concentrated, and then incinerated to produce a residue including sodium, sulfate, and sodium chloride. This residue is distilled with sulfuric acid to produce gaseous hydrogen chloride and remaining residue, the HC1 being used in chloride dioxide production for the bleach plant, while the remaining residue is passed to the recovery loop (e.g. recovery boiler). Sulfur containing gases from the non-condensible gas system may be combusted to produce gaseous sulfur dioxide, which is then converted to sulfuric acid, to distill the residue. Where a non-chlorine bleach plant is provided, the liquid effluents may be concentrated in evaporators and then passed directly to the recovery boiler. The liquid streams in the mill are managed by a cascade principle to reserve the cleanest water for only those processes where it is needed while minimizing its use where it is not necessary.
237 LIQUID CARBON DIOXIDE INJECTION IN EXOTHERMIC CHEMICAL REACTIONS EP91907756.0 1991-03-27 EP0522068B1 1995-11-22 WALLACE, David, Eric; MERRITELLO, Ronald, John; ZYZDA, Leonard, Emil; EISENWASSER, Jacob, David; LAMBESIS, Gary, James
The present invention is directed to an improved method for carrying out a exothermic chemical reaction with carbon dioxide in an aqueous environment. In the method, a fluid solution containing at least one chemical reactant which is exothermically reactive with carbon dioxide is provided. Liquid carbon dioxide is then injected into the solution of the chemical reactant at a pressure above the triple point of at least about 60 psig. The injection of the liquid carbon dioxide takes place under turbulent conditions wherein the liquid carbon dioxide expands to provide carbon dioxide vapor. The carbon dioxide vapor superheats to approach the exothermic reaction temperature which occurs between the carbon dioxide vapor and the chemical reactant. The chemical reactant and the carbon dioxide react in the dispersion exothermically to produce a chemical reaction product. The flow rate of liquid carbon dioxide can be controlled to control the reaction temperature without the encessity for providing any reactor cooling or heat exchange apparatus.
238 Umsetzung eines im flüssigen Zustand vorliegenden Alkalimetalls in ein Alkalicarbonat EP93116999.9 1993-10-20 EP0596331A1 1994-05-11 Tusche, Rudolf, Dr.; Hanebeck, Norbert, Dr.

Die Erfindung betrifft ein Verfahren zur Umsetzung eines im flüssigen Zustand vorliegenden Alkalimetalls in ein Alkalicarbonat, wobei zunächst ein Gasstrom aus einem Sauerstoff beinhaltenden ersten Gas bereitgestellt wird, in dem das flüssige Alkalimetall dispergiert wird. In einer ersten Umsetzung zwischen dem Alkalimetall und dem ersten Gas entsteht ein in dem Gasstrom dispergiertes Zwischenprodukt. Dem Gasstrom wird weiterhin eine gasförmige Verbindung des Kohlenstoffs, insbesondere Kohlendioxid, zugemischt, welche in einer zweiten Umsetzung mit dem Zwischenprodukt reagiert zu dem gewünschten Alkalicarbonat, welches in in dem Gasstrom feinverteilter Form erhalten wird. Schließlich wird das Alkalicarbonat aus dem Gasstrom abgeschieden. Das Verfahren ist besonders geeignet zur Umsetzung von Natrium zu Natriumcarbonat, wobei es sich besonders eignet zur Umwandlung von Natrium, welches in einem Kernreaktor als Kühlmittel gedient hat, in ein unmittelbar endlagerfähiges Produkt. Die Erfindung betrifft auch eine Vorrichtung zur Durchführung des Verfahrens.

239 Verfahren zur Spaltung von Natriumsulfat oder Kaliumsulfat enthaltenden Stoffen EP92203031.7 1992-10-02 EP0540072A1 1993-05-05 Bandel, Gebhard, Dr.; Fitting, Arno, Dr.; Samant, Gurudas, Dr.; Tacke, Michael

Natriumsulfat oder Kaliumsulfat enthaltende Stoffe werden durch thermische Behandlung gespalten. Zur Vermeidung von Agglomeration und H₂S-Bildung erfolgt die Spaltung in einer Wirbelschicht, in reduzierender Atmosphäre im Gebiet der NaAlO₂-Bildung in Abhängigkeit vom SO₂-Partialdruck mit einem Sauerstoff-Partialdruck von 10⁻⁴ bis 10⁻¹⁴ bar, unter Zusatz von Al₂O₃ und/oder Al(OH)₃ enthaltenden Stoffen mit einer Korngröße unter 3 mm in einer zur Bildung von NaAlO₂ überstöchiometrischen Menge, bei Temperaturen von 900 - 1300°C, unter Erzeugung mindestens eines Teiles der erforderlichen Reaktionswärme durch Verbrennung von kohlenstoffhaltigen Stoffen in der Wirbelschicht, und unter Entfernung des SO₂-Gehaltes aus dem Abgas.

240 PROCESS FOR REMOVING COATINGS FROM SENSITIVE SUBSTRATES, AND BLASTING MEDIA USEFUL THEREIN EP90911455 1990-03-14 EP0463121A4 1992-10-07 KIRSCHNER, LAWRENCE
Blasting media for removing coatings from sensitive metal and composite surfaces, and a process useful therewith, wherein the blasting media comprise mixtures of water-soluble bicarbonate particles, e.g., sodium bicarbonate particles, with a hydrophobic silica flow/anti-caking agent.
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