子分类：
- C01D5/002： .{用添加剂防止晶体吸潮或结块}
- C01D5/004： .{制备粒状、片状或其他形状的产品}
- C01D5/006： .{对粘胶纺丝凝固浴中硫酸钠回收}
- C01D5/008： .{从明矾石制备硫酸钾}
- C01D5/02： .从碱金属盐和硫酸或酸式硫酸盐制备硫酸盐; 酸式硫酸盐的制备
- C01D5/04： .借助于亚硫酸或亚硫酸盐制备硫酸盐,如哈格里夫斯法 {(焦亚硫酸盐或 偏亚硫酸氢盐C01D 5/145)}
- C01D5/06： .用复分解法制备硫酸盐
- C01D5/12： .制备钠或钾与镁的复式硫酸盐
- C01D5/14： .亚硫酸盐的制备(C01D 5/04 优先)
- C01D5/16： .提纯{(C01D 5/145优先)}
- C01D5/18： .脱水 {(C01D 5/145优先)}
| 序号 | 专利名 | 申请号 | 申请日 | 公开（公告）号 | 公开（公告）日 | 发明人 |
|---|---|---|---|---|---|---|
| 161 | How to formulate the alkali metal salt | JP2000575800 | 1999-09-30 | JP2002527330A | 2002-08-27 | フィニー、ロビン |
| (57)【要約】 炭酸水素ナトリウム及び硫酸カリウムを調合するための方法。 一実施例において、硫酸ナトリウム及び炭酸水素アンモニウムは、炭酸水素ナトリウムを形成するために、炭酸塩を除去するべく硫酸で処理した残存するリカー或いはかん水と反応し、硫酸カリウムを沈殿させる。 更なる実施例は、炭酸水素ナトリウムを沈殿させるために、炭酸水素アンモニウム、アンモニアガス又は二酸化炭素を使用する。 この方法の結果、高品質肥料用及び食品用炭酸水素ナトリウムが生成する。 | ||||||
| 162 | Recovered from the crystal waste solution of glycine and Glauber's salt | JP9493190 | 1990-04-10 | JP2931621B2 | 1999-08-09 | JON SHII SANBAAGU |
| 163 | Method and device for concentrating salt-containing solution | JP7653698 | 1998-03-10 | JPH10337401A | 1998-12-22 | WOERNER JOERG; THEISEN WOLFGANG; WETTEBORN KLAUS; GUTMANN ARND; LINN HORST; CHRUBASIK ALFRED; BRANDAU EGBERT |
| PROBLEM TO BE SOLVED: To efficiently concentrate and solidify a salt-contg. soln. at the time of concentrating and solidifying the salt-contg. soln., especially a borate or sulfate-contg. soln-, by the microwave irradiation in a closed vessel by providing a bell-shaped body for a microwave tube and radiating a microwave directly to the salt-contg. soln. SOLUTION: The saltlsoln. to be evaporated and solidified in a preparation vessel 10 is supplied to a vessel 12 by a feed pump through a pipeline 14. A microwave tube 28 is connected to the vessel 12 in the zone of a lid 26 formed in the shape of a diffuser 27, and the vessel 12 is irradiated with a microwave generated by a magnetron through the tube 28 and a bell-shaped body 29. In this case, the cross section of the bell-shaped body 29 or the space between the body and the liq. surface in the vessel 12 is changed, hence the microwave is directly radiated to the liq. surface but not to the side wall of the vessel, and the salt soln. is efficiently heated and evaporated. A jack 37 is provided below the vessel 12 to adjust the height of the vessel 12. | ||||||
| 164 | Method for selectively producing the sulfate corresponding aqueous stream containing water-soluble inorganic sulfide | JP13882793 | 1993-05-02 | JP2637898B2 | 1997-08-06 | RICHAADO II MARAINANGERI; TAMU ENU KAARUNESU |
| 165 | Method for electrolyzing aqueous potassium chloride solution | JP18252794 | 1994-08-03 | JPH0776789A | 1995-03-20 | RIYUUDEIGAA HEENIHISHIYUMITSUT; PEETAA SHIYUMITSUTEINGAA; INGO SHIYUTAARU; KAARU RAINAA BUAMUBATSUHAAZONM |
| PURPOSE: To easily obtain an aq. potassium chloride soln. for alkali electrolysis by adding potassium hydroxide or potassium carbonate to an aq. crude potassium chloride soln. to remove the sulfate ions by precipitation. CONSTITUTION: The precipitates (c) of an aq. potassium chloride soln. (a) are settled in a settling vessel 2, the precipitates (c) are removed by a filter 3, and then the soln. is electrolyzed in an electrolytic cell 4. Subsequently, potassium hydroxide (i) is added to the branched stream of the dil. aq. soln. (e) passed through a dechlorination tank 5 to increase the hydroxide ion concn., and precipitated potassium sulfate (k) is separated by a filter 7. The filtrate (1) is added to the main stream of the aq. soln. (e), potassium hydroxide (m) and potassium carbonate (h) are added to the soln. to increase the hydroxide and/or carbonate ion concns., and the soln. is returned to a salt dissolving tank 1 and recycled. COPYRIGHT: (C)1995,JPO | ||||||
| 166 | Treatment of waste from waste water of dye production | JP8546591 | 1991-04-17 | JPH04225893A | 1992-08-14 | HERUMORUTO FUON PURETSUSEN; KARURUUMITSUHIYAERU RAIHIERUTO; EERITSUHI METSUTSU |
| PURPOSE: To prevent the salt pollution of waste water and to reduce a treatment cost by treating the waste water while recovering potassium sulfate in a waste treatment from two-stages production of perylenetetracarboxylic acid dianhydride. CONSTITUTION: Perylenetetracarboxylic acid diimide is obtd. in a first stage and perylenetetracarboxylic acid dianhydride by hydrolysis in a second stage. A K 2SO 4 mother liquor is introduced from a preliminary batch into the waste sulfuric acid from the second stage and the mixture is treated with active carbon and is filtered. The filtrate is added to the waste water from the first stage contg. KOH and is neutralized. The reaction product is heated and after a surfactant is added thereto, the product is subjected cooling crystallization. The product is then filtered and the filtrate is treated while potassium sulfate is recovered. COPYRIGHT: (C)1992,JPO | ||||||
| 167 | Recover of glycine and glauber's salt from waste crystal liquor | JP9493190 | 1990-04-10 | JPH03204844A | 1991-09-06 | JIYON SHII SANBAAGU |
| PURPOSE: To recover the subject two components by forming a slurry by controlling the temperature of the aqueous raw material solution comprising glycine and sodium sulfate and separating solid mixture. A part of the mother solution is recycled. CONSTITUTION: The subject material is recovered by separating the solid mixture from the mother solution by forming slurry by cooling the aqueous raw material solution consisting of glycine and sodium sulfate to a temperature of about 5°C at a rate of 5.8°C/hour. Seed crystals of glycine may be added before cooling the raw material solution, and seed crystals of 10 hydrate of sodium sulfate during the slurry formation. A part of the separate mother solution may be recycled in the crystallizing tank to reduce the density of the slurry. By this method the waste fluid produced in the process of manufacturing glycine can be minimized and valuable materials can be recovered from the waste fluid. COPYRIGHT: (C)1991,JPO | ||||||
| 168 | Manufacture of available material including synthetic nepheline from bayer's process red mud | JP15877387 | 1987-06-25 | JPS638210A | 1988-01-14 | UIRIAMU HENRII ANDORIYUUZU |
| 169 | Novel permanently flame retardant and smoke retardant composition | JP7862085 | 1985-04-15 | JPS60235887A | 1985-11-22 | SUTEFUAN AI SAREI |
| 170 | Treatment of brine sludge containing high content sodium sulfate and potassium chloride | JP23996183 | 1983-12-21 | JPS59116124A | 1984-07-04 | ROOBERUTO BUINKURAA |
| 171 | Process for manufacturing sulfate of alkali metal | JP1317982 | 1982-01-29 | JPS57145025A | 1982-09-07 | JIYOON BII SAADEISUKO; AAHAATO KEE DOREKUSERU |
| 172 | JPS5644014B2 - | JP14021773 | 1973-12-14 | JPS5644014B2 | 1981-10-16 | |
| 173 | Manufacture ofmagnesium chloride | JP3468080 | 1980-03-18 | JPS55126534A | 1980-09-30 | RONARUDO JIEI AREIN; JIYOSEFU PII MANISUKARUKO; DEEBITSUDO JII BUREISUUEITO |
| 174 | Method of refining waste water | JP14998377 | 1977-12-15 | JPS5376553A | 1978-07-07 | ARUUIN TOTSUPU; KURAUSU SHIYUMIIDERU; GEORUKU SHIEEFUERU |
| 175 | Energy transmission | JP7844177 | 1977-06-30 | JPS5325285A | 1978-03-08 | BURANDON HARISU BAATON; JIYON ARUBAATO SEIJIERU |
| 176 | JPS49106990A - | JP1324974 | 1974-01-31 | JPS49106990A | 1974-10-11 | |
| 177 | JPS4996993A - | JP14021773 | 1973-12-14 | JPS4996993A | 1974-09-13 | |
| 178 | JPS4986419A - | JP9911773 | 1973-09-03 | JPS4986419A | 1974-08-19 | |
| 179 | 트리에탄올아민의 착색 방지 및 컬러 개선을 위한 보관 방법 | KR20160113937 | 2016-09-05 | KR20180027674A | 2018-03-15 | 황소라; 유종철; 서영종; 김길만 |
| 트리에탄올아민의저장중 변색문제해결방법이다양하게제시되고있지만, 그중 착색방지제를처방(공정중 또는후처방)하는것이안전하며, 추가비용이크지않아선호되는방법이다. 종래공정후 처방제로일부물질들이사용되고있으나, 여러가지물질들의혼합처방시 보다개선된효과에대하여언급한기술은찾기어렵다. 본발명은트리에탄올아민의저장중 변색문제해결에있어여러가지물질들의혼합처방시 최적처방조성을제공한다. | ||||||
| 180 | 습윤 기체 혼합물을 제습하기 위한 방법 및 흡수제 | KR1020170073668 | 2017-06-13 | KR1020170141126A | 2017-12-22 | 제내커,올리비에; 빌리,벤야민 |
| 본발명은습윤기체혼합물을디알킬이미다졸륨염 및트리알킬포스페이트를포함하는흡수제와접촉시키는, 습윤기체혼합물을제습하기위한방법에관한것이다. 추가로, 본발명은또한, 본발명에따른흡수제를포함하는흡수식열 펌프, 및본 발명에따른흡수제자체에관한것이다. | ||||||
QQ群二维码
意见反馈
意见反馈