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序号	专利名	申请号	申请日	公开（公告）号	公开（公告）日	发明人
81	纯碱－白碳黑联合制造方法	CN01143247.0	2001-12-21	CN1373086A	2002-10-09	叶天润; 叶阳
一种以含钠化合物、含硅石物料和二氧化碳为原料的纯碱－白碳黑联合制备方法。该方法首先使含硅石的物料与除纯碱外的含钠化合物反应生成中间化合物硅酸钠,硅酸钠再与二氧化碳按式（Ⅰ）反应制备纯碱和白碳黑,或与碳酸氢钠按式（Ⅱ）反应制备纯碱和白碳黑。含钠化合物原料为烧碱、芒硝、食盐等;含硅石的物料为高硅含量的石英砂、石英岩、硅藻土、铁矿石、高岭土、粉煤灰、煤矸石等金属、非金属矿物。
82	氧化至少一种碱金属的方法	CN98104148.5	1998-01-13	CN1198406A	1998-11-11	A·H·A·J·拉希尔; V·H·J·冯·阿森诺依
用于将至少一种碱金属氧化的方法,根据该方法,它通过与氧气反应而使该碱金属以熔融状态氧化,其特征在于将该熔融碱金属分散在流化床(6)中并且在该床(6)中与氧气进行氧化反应,并通过与供应到上述床(6)中的含碳气体起反应而使由此形成的氧化物碳化。
83	硫酸盐工艺中能量和化学品回收的方法和设备	CN92100837.6	1992-02-14	CN1064118A	1992-09-02	塞仆尔·鲁涂
本发明涉及回收硫酸盐工艺中的能量和化学品的方法和设备，其中黑液送入气化反应器，黑液在低于化学计量的氧气存在下，在高于常压下气化，因此无机化合物作为可用于现有制浆工艺的液相化合物被回收，黑液中的有机化合物的能量主要限于气相化合物。在气化中生成的含有含钠化合物的气体送入颗粒冷却器，这些化合物变成固态，在颗粒冷却器中冷却的气体用过滤器净化，然后送入燃气透平。
84	污水处理装置	CN89105510.X	1989-08-19	CN1010771B	1990-12-12	龚德明
一种污水处理装置，该装置是将两个截面为圆形或矩形的筒状结构同心地套在一起，形成内室和环绕内室的外室，在内外室中分别安装有溶气释放器，将泵进的污水，从外室到内室，先后两次与释放器喷出的溶气水相混合，进行气浮净化作用，使污水中悬浮物等形成浮渣上浮而被排除，两次净化后之污水再经过位于内室底部之过滤层以清水流出，从而达到设备简单、投资小、占地少，能耗省，效率高的目的。
85	非常に優れた流動性を有するアルカリ金属重炭酸塩粒子	JP2017533425	2015-12-22	JP2018502814A	2018-02-01	サヴァリー, ダヴィドジャンリュシアン
本発明は、アルカリ金属重炭酸塩粒子と、添加剤としてのアミノ酸とを含有する粉末組成物をもたらす。本発明は、1〜10重量%のアルカリ金属重炭酸塩と、添加剤としてのアミノ酸とを含む水溶液を噴霧乾燥することによる、アルカリ金属重炭酸塩粒子の作製方法にも関する。本発明は更に、添加剤としてのアミノ酸の存在下でアルカリ金属重炭酸塩を共粉砕することによる、アルカリ金属重炭酸塩粒子の作製方法にも関する。【選択図】なし
86	増加した溶解時間を有するアルカリ金属炭酸水素塩粒子	JP2017533434	2015-12-22	JP2018502038A	2018-01-25	サヴァリー, ダヴィドジャンリュシアン; セギャン, ジャン−イヴ; カヴァリエール, カリーヌ
本発明は、アルカリ金属炭酸水素塩粒子および添加物としてを含む粉末組成物に関する。本発明はまた、1〜10重量%のアルカリ金属炭酸水素塩、および添加物として樹脂酸または脂肪酸を含む水溶液または懸濁液を噴霧乾燥することにより、アルカリ金属炭酸水素塩粒子を調製するための方法に関する。本発明は、添加物として樹脂酸の存在下でアルカリ金属炭酸水素塩を共粉砕することにより、アルカリ金属炭酸水素塩粒子を調製するための方法にさらに関する。本発明はまた、添加物として樹脂酸、脂肪酸、またはワックスの存在下でアルカリ金属炭酸水素塩を流動床コーティングすることにより、アルカリ金属炭酸水素塩粒子を調製するための方法に関する。【選択図】なし
87	高純度ジフェニルスルホン、調製、およびポリ(アリールエーテルケトン)の調製のためのその使用	JP2011532648	2009-10-23	JP5734858B2	2015-06-17	ルイス, シャンタル; ギャンディー, ウィリアム; ライアン, エドワード; アンダーウッド, ジェフリースコット; イー, コン

88	褐藻類を原料とする凝集剤用原料、該原料を用いた凝集剤、該凝集剤の製造方法及び該凝集剤を用いた浄化方法	JP2009262493	2009-11-18	JP5646159B2	2014-12-24	牧子榎; 佐藤　道祐; 道祐佐藤; 啓一安岡

89	Method and apparatus for producing sodium bicarbonate	JP2012287988	2012-12-28	JP2014129193A	2014-07-10	SHIMIZU KAZUHIKO; TOBA YUICHIRO; IMAMURA EIJI; SHIMURA MITSUNORI; SHINOHARA MASAYO; IMAHAMA TOSHINOBU; KIN KENJI
PROBLEM TO BE SOLVED: To provide a method and apparatus for producing sodium bicarbonate which can recover high-purity NaHCOfrom NaCl-containing water.SOLUTION: A method for producing sodium bicarbonate includes a recovery step of passing NaCl-containing water containing NaCl and carbonic acid substances through a packed tower 58 packed with an anion exchange resin to recover NaHCO. When the NaCl-containing water is passed through the packed tower 58 packed with the anion exchange resin, the pH of the NaCl-containing water is adjusted according to a ratio of the amount of Clions to the amount of total carbonic acid substances other than free carbon dioxide contained in the NaCl-containing water.
90	Manufacturing method for coating sodium percarbonate particles	JP2010538530	2008-11-20	JP2011506256A	2011-03-03	ライニンガーシュテファン; ヤーコプハラルト; シャイベミヒャエル
流動層中で硫酸ナトリウムを含有する水溶液を過炭酸ナトリウム粒子に噴霧し、かつ同時に水を蒸発させることによる被覆過炭酸ナトリウム粒子の製造方法において、硫酸ナトリウムを含有する水溶液を製造するために硫酸ナトリウム及び過炭酸ナトリウムを含有するダストが使用される。
91	Integrated chemical methods	JP2009537449	2007-11-21	JP2010510161A	2010-04-02	フレデリックブレント，ジェフリー
ケイ酸塩原料が、活性化されたスラリー原料を二酸化炭素と反応させる前に、燃料の燃焼により発生した熱を用いることにより、熱的に活性化されることを特徴とする、鉱物炭酸化法。
92	Injection of liquid carbon dioxide to the exothermic chemical reaction	JP50739091	1991-03-27	JP3337213B2	2002-10-21	アイゼンワッサー，ヤコブ・デーヴィッド; ウォレス，デーヴィッド・エリック; ジズダ，レナード・エミル; メリテロ，ロナルド・ジョン; ランベシス，ゲイリー・ジェームズ
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.
93	Molten salt destruction of alkali metal and alkaline earth metal	JP16152994	1994-07-13	JPH07144186A	1995-06-06	RICHIYAADO REZURII GEI; JIERORUDO GUON; JIYON CHIYAARUZU NIYUUKOMU
PURPOSE: To destroy dangerous waste such as Na in a molten salt bath and to prepare a safe alkali metallic or alkaline earth metallic salt by allowing the alkali metal or alkaline earth metal to react with a CO2 -O2 mixture in the molten salt bath such as a molten alkali carbonate. CONSTITUTION: Alkali metal or alkaline earth metal-containing dangerous waste is fed into a molten salt bath 16 containing a molten salt selected from the group consisting of alkali metallic carbonates, alkali metallic halides, alkaline earth metallic halides and mixtures of those. A CO2 -O2 mixture is also fed into the molten salt bath 16. The ratio between CO2 and O2 is made at least sufficient for stoichiometric reaction with the alkali metal or alkaline earth metal in the waste. The alkali metal or alkaline earth metal is allowed to react with the CO2 and O2 in the molten salt bath 16 at a higher temperature than the melting point of the salt in the bath 16 and the alkali metal or alkaline earth metal is converted into safe carbonate in the bath 16.
94	Production of calcined potassium carbonate and/or potassium carbonate hydrate and apparatus therefor	JP4365194	1994-03-15	JPH06345422A	1994-12-20	ROORANTO SHIRUTOHAUAA; KURAUSU DENEKE
PURPOSE: To reduce or inhibit a formation of dusts and agglomerates by mixing dusts from a process for the production of calcined potassium carbonate with a crude salt and supplying it to a process for the production of calcined potassium carbonate or potassium carbonate hydrate. CONSTITUTION: In case of producing calcined potassium carbonate K ₂CO ₃ and/or potassium carbonate hydrate K ₂CO ₃.1.5H ₂O by drying a crude salt K ₂CO ₃.1.5H ₂O containing ≤3.0% water, the dusts from a process for the production of calcined potassium carbonate are mixed with a crude salt and supplied to a process for the production of calcined potassium carbonate and/or potassium carbonate hydrate. The mutual pellet formation of dust particles can be avoided by a partial recycling of the mixture resulting from a pre-reaction of the crude salt with calcined dusts, and in this case, a large quantity of fluctuating or closely packed dusts can be recovered. COPYRIGHT: (C)1994,JPO
95	Process and equipment for recover of energy and chemicals in sulfate process	JP2810892	1992-02-14	JPH0586590A	1993-04-06	SETSUPO RUOTOU
PURPOSE: To increase electric power output and generate a process steam by passing a hot gas from a gasification reactor into a particle cooler and passing the cooled gas into a gas turbine after purification by a filter. CONSTITUTION: Condensed liquor is passed into a gasification reactor 3 after evaporating moisture of black liquor 1a, 1b in an evaporator 1. A molten mixture of Na2 S and Na2 CO3 is recovered by heating the gasification reactor to 800-1,200 deg.C by introducing air heated at a particle cooler 4. A hot gas is passed into the gasification reactor, cooled down to 300-600 deg.C by compressed air from a compressor 8, Na compound is brought into solid state and the gas is purified by a filter 5. The compressor and a generator 9 are driven by gas sent into a gas turbine 7 through a burning chamber 6 and an exhaust gas is sent to boilers 10 and 11.
96	JPH04504824A -	JP51111390	1990-03-14	JPH04504824A	1992-08-27

97	Sodium bicarbonate particle having treated surface and formed formulation containing the same	JP32559889	1989-12-15	JPH02275714A	1990-11-09	YOROZU HIDENORI; ICHII YUJI; MATSUMOTO KIYOSHI; HASHIMOTO MASAYUKI; HOSHI MASATO
PURPOSE: To obtain sodium bicarbonate particles, having treated surfaces and capable of forming tablet or granule, etc., and simultaneously providing formed formulations excellent in stability without using other binders by coating the surfaces of the sodium bicarbonate particles with Na ₂CO ₃ or a double salt thereof. CONSTITUTION: About ≥50% surfaces of sodium bicarbonate particles having ≥30μm average particle diameter are normally coated with Na ₂CO ₃ or a double salt thereof. In this case, the thickness of the Na ₂CO ₃ on the surfaces of the sodium bicarbonate particles is especially preferably 0.1 to 5μm. The surfaces of the sodium bicarbonate particles are coated by, e.g. heating the sodium bicarbonate particles at ≥70°C. For example, the surfaces of the sodium bicarbonate particles having 200μm average particle diameter may be converted into the sodium carbonate having about 1μm thickness by heating the surfaces at about 100°C temperature for 30min. The resultant sodium bicarbonate particles with the treated surfaces have excellent binding force and the resultant formed formulation is simultaneously excellent in preservation stability. COPYRIGHT: (C)1990,JPO&Japio
98	JPS6047201B2 -	JP3743977	1977-04-01	JPS6047201B2	1985-10-21	AASAA ERU KOORU; ROBAATO DEI RENNITSUKU; MAACHIN DABURYU SABINSUKII

99	JPS584268B2 -	JP10987674	1974-09-24	JPS584268B2	1983-01-25	EEGON JUURI

100	JPS5060862A -	JP10987674	1974-09-24	JPS5060862A	1975-05-26

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