JPS5826027A - Washing method for anhydrous sodium carbonate crystal - Google Patents
Washing method for anhydrous sodium carbonate crystalInfo
- Publication number
- JPS5826027A JPS5826027A JP11923281A JP11923281A JPS5826027A JP S5826027 A JPS5826027 A JP S5826027A JP 11923281 A JP11923281 A JP 11923281A JP 11923281 A JP11923281 A JP 11923281A JP S5826027 A JPS5826027 A JP S5826027A
- Authority
- JP
- Japan
- Prior art keywords
- crystals
- washing
- sodium carbonate
- anhydrous sodium
- soln
- 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.)
- Granted
Links
Landscapes
- Inorganic Compounds Of Heavy Metals (AREA)
- Compounds Of Alkaline-Earth Elements, Aluminum Or Rare-Earth Metals (AREA)
Abstract
Description
【発明の詳細な説明】 本発明は、無水炭酸ソーダ結晶の洗浄方法に関する。[Detailed description of the invention] The present invention relates to a method for cleaning anhydrous soda crystals.
無水炭酸ソーダ結晶は各種の方法で製造されるが、結晶
表面に付着した各河・不純物あるいは溶液を除去したい
場合が多い。Anhydrous sodium carbonate crystals are produced by various methods, but in many cases it is desired to remove impurities or solutions attached to the crystal surface.
通常は水で洗浄し、乾燥することが考えられるが、この
方法では次のような欠点がある。Normally, washing with water and drying is considered, but this method has the following drawbacks.
その1つは、水で洗浄することにより、無水炭酸ソーダ
の表面が炭酸ソーダ含水塩(普通は1水塩)に転移する
ことである。One is that by washing with water, the surface of anhydrous soda carbonate transforms into a hydrated salt of sodium carbonate (usually monohydrate).
他の1つは、無水炭酸ソーダ結晶の表面が溶解流失し、
無水炭酸ソータ結晶の歩留が低下することである。The other is that the surface of the anhydrous soda crystals dissolves and is washed away.
This results in a decrease in the yield of anhydrous carbonate sorter crystals.
本発明者等は、上記欠点を克服する努力を重ね、特定の
条件下で苛性ソーダ水溶液で洗浄することにより、この
問題ケ解決することにk(功したものである。即ち、無
水炭Nソーダ結晶を第1図の領域Xを維持するように苛
性ソーダ水溶液で洗浄することにより本発明の目的が充
分に達せられることを見出しだものである。The present inventors have made repeated efforts to overcome the above-mentioned drawbacks, and have succeeded in solving this problem by washing with a caustic soda aqueous solution under specific conditions. It has been discovered that the object of the present invention can be fully achieved by cleaning the wafer with a caustic soda aqueous solution so as to maintain the area X in FIG.
無水炭酸ソーダは、従来性なわれているし灰を1水塩化
し、これを加熱分解して製造する方法、あるいは特開昭
55−7530号、特願昭55−10025号、特願昭
55−11475号等で開示される水溶液反応による方
法等が考えられる。前者の方法による場合、通常5TD
(、Steam−Tubed Dryer )と称せら
れる乾燥器で炭Uンーダ1水塩を熱分解して無水炭酸ソ
ーダ結晶を得ているが、この方法による場合は炭し・ソ
−ダ1水塩を母液から分けするに際し、母液中不純物濃
度を調節したり、あるいは水にて洗浄することで、製品
中不純物濃度を調節することが可能であるが、後者の場
合は、炭酸ソーダ無水塩を析出させる条件から母液中の
nac1濃度が限定されていたシ、また、水にて洗浄し
た場合は瞬時に分離機内にて水利反応により固結し、無
水のケーキを得ることができない。Anhydrous soda carbonate is conventionally produced by converting ash into monohydrate and thermally decomposing it, or by methods such as JP-A-55-7530, JP-A-55-10025, JP-A-55. A method using an aqueous solution reaction disclosed in No.-11475 etc. can be considered. In the case of the former method, usually 5TD
Anhydrous sodium carbonate crystals are obtained by thermally decomposing carbon dioxide monohydrate in a dryer called a Steam-Tubed Dryer (Steam-Tubed Dryer). When separating from the product, it is possible to adjust the impurity concentration in the product by adjusting the impurity concentration in the mother liquor or washing with water, but in the latter case, the conditions for precipitating the anhydrous sodium carbonate salt Because of this, the concentration of nac1 in the mother liquor was limited, and when washed with water, it instantly solidified in the separator due to a water utilization reaction, making it impossible to obtain an anhydrous cake.
従って、上記現象の生じない方法として、本発明省は鋭
意検討を加えた結果、本発明をなしえたもので、特定条
件下で苛性ソーダ水溶液で洗浄することを要旨とするも
のである。Therefore, as a result of extensive research, the Ministry of the Invention has developed the present invention as a method that does not cause the above-mentioned phenomenon, and the gist thereof is to wash with a caustic soda aqueous solution under specific conditions.
無水炭酸ソーダ結晶を乾燥する場合、無水炭酸ンーダ結
晶を第1図の震域Xに維持しながら苛性ソーダ水溶液で
洗浄することが必要である。When drying anhydrous sodium carbonate crystals, it is necessary to wash them with an aqueous caustic soda solution while maintaining the anhydrous carbonate crystals in the seismic region X in FIG.
第1図は、本発明方法を実施するための条件を示す図で
あって、横軸は洗浄液である苛性ソーダの濃度を示し、
縦軸は洗浄温度を示す。ここで洗浄温度とは、厳密には
無水炭酸ソーダ結晶の光面温度をいうが、無水炭酸ソー
ダ結晶が上述の後者の方法で製造された製造直後のもの
の場合には、との洗浄温度は、はぼ近似的に洗浄液であ
る苛性ソーダ水溶液の温度と為えてよい。FIG. 1 is a diagram showing the conditions for carrying out the method of the present invention, in which the horizontal axis shows the concentration of caustic soda, which is a cleaning liquid;
The vertical axis indicates the cleaning temperature. Strictly speaking, the washing temperature here refers to the optical surface temperature of the anhydrous sodium carbonate crystal, but in the case where the anhydrous soda crystal has just been produced by the latter method mentioned above, the washing temperature is This can be approximately considered to be the temperature of the caustic soda aqueous solution, which is the cleaning liquid.
洗浄条件が第1図の領域Yに維持されると、無水炭酸ソ
ーダ結晶の表面に炭酸ソーダ1水塩の生成することがあ
るため、洗浄条件としては第1図の領域Xに維持するこ
とが必要である。If the cleaning conditions are maintained in the region Y in FIG. 1, sodium carbonate monohydrate may be generated on the surface of the anhydrous sodium carbonate crystals. Therefore, the cleaning conditions should be maintained in the region X in FIG. is necessary.
本発明は上述の洗浄条件の維持を必須条件とするが、洗
浄後の無水炭酸ソーダ結晶の表面には洗浄液である苛性
ソーダ水溶液の薄い被゛膜が形成されており、苛性ソー
ダが不純物として残る可能性がある。かような苛性ソー
ダも不純物として許容しえない時は、上記苛性ソーダ水
溶液の被膜が付着した無水炭酸ソーダ結晶を炭酸ガス又
は炭酸ガスを含むガスで乾燥するとよい。Although the present invention requires maintenance of the above-mentioned cleaning conditions, a thin film of aqueous caustic soda solution, which is the cleaning liquid, is formed on the surface of the anhydrous soda crystal after cleaning, and there is a possibility that caustic soda may remain as an impurity. There is. When such caustic soda cannot be tolerated as an impurity, it is preferable to dry the anhydrous soda crystals coated with the above caustic soda aqueous solution with carbon dioxide gas or a gas containing carbon dioxide gas.
この乾燥の場合にも、無水炭酸ソーダ結晶表面に付着す
る苛性ソーダの温度に関して第1図の領域Xを維持する
ことが必要である。In the case of this drying as well, it is necessary to maintain the temperature of the caustic soda adhering to the anhydrous soda crystal surface within the range X in FIG. 1.
即ち、付着母液が領域Xにある場合は、炭酸ガス又は炭
酸ガスを含むガスで乾燥するにつれて、表面の苛性ソー
ダ水滓1液は水分が蒸発すると同時に、苛性ソーダが炭
瞑ガスと反応して炭酸ソーダに変り、無水炭酸ソーダ結
晶として表面に析出固着する。That is, when the adhering mother liquor is in region , and precipitates and adheres to the surface as anhydrous sodium carbonate crystals.
乾燥及び反応の進行につれて、無水炭酸ソーダ結晶の表
面にある苛性ソーダζ幾度は急激に減少するため、乾燥
温度はそれに伴い領域Xを維持するように上昇せしめね
ばならない。しかしながら、乾燥の進行につれて乾燥温
度を変えることは実際的ではなく、実際に工業的に実施
する場合には炭酸ガス又は炭酩・ガスを含むガスの温度
を103℃(領域又と領域Yを区画するりの縦軸との交
点)以上とするのがよい。As the drying and reaction proceed, the amount of caustic soda ζ on the surface of the anhydrous sodium carbonate crystals rapidly decreases, so the drying temperature must be increased accordingly to maintain region X. However, it is not practical to change the drying temperature as the drying progresses, and in actual industrial implementation, the temperature of the gas containing carbon dioxide gas or charcoal alcohol/gas is set at 103°C (areas and areas Y are separated). (intersection with the vertical axis of the slide) or more.
以上、説明した本発明方法によれば、洗浄液である苛性
ソーダ水溶液は循環使用が可能であることから、無水炭
酸ソーダ結晶の歩留に悪影響は与えないし、また、乾燥
に使用する炭酸ガス又は炭酸ガスを含むガスとして亜硫
酸ガスを除去した工業燃焼ガスが(必要に応じて若干加
熱することにより)使用可能であることから貞に工業的
に効果の犬なる方法であることが分る。According to the method of the present invention described above, since the caustic soda aqueous solution that is the cleaning liquid can be reused, it does not have an adverse effect on the yield of anhydrous sodium carbonate crystals, and the carbon dioxide or carbon dioxide gas used for drying Since industrial combustion gas from which sulfur dioxide gas has been removed can be used as the gas containing sulfur dioxide (slightly heated if necessary), it is clear that this is a very industrially effective method.
また、使用する苛性ソーダ水溶液は、求める製品純度に
応じて多少の不純物か含まれていてもよいことは勿論で
ある。It goes without saying that the caustic soda aqueous solution used may contain some impurities depending on the desired product purity.
以下、実施例により本発明を更に詳しく説明する。Hereinafter, the present invention will be explained in more detail with reference to Examples.
実施例
塩安ソーダ法で得られる重曹、49%苛性ソーダ水溶液
及び食塩を反応容器にて、105℃、1気圧で反応させ
無水炭酸ソーダ結晶とNaC115wt%、NazOO
s 14.6 %の母液からなるスラリーを得た。この
結晶を濾過により分離した無水炭酸ソーダ結晶の表面に
は食塩が0.6%付着していた。Example: Baking soda obtained by the ammonium chloride soda method, 49% aqueous caustic soda solution, and salt were reacted in a reaction vessel at 105°C and 1 atm to form anhydrous sodium carbonate crystals, 115 wt% NaC, and NazOO.
A slurry consisting of 14.6% mother liquor was obtained. The crystals were separated by filtration, and 0.6% of common salt was found to be attached to the surface of the anhydrous soda crystals.
次にこの結晶を98℃に保持しつつ、90℃、30%の
苛性ソーダ水溶液で洗浄し、ついでこれを109℃の炭
酸ガスで乾燥した。Next, the crystals were washed with a 30% caustic soda aqueous solution at 90°C while being maintained at 98°C, and then dried with carbon dioxide gas at 109°C.
表面に付着した苛性ソーダの部分は完全に無水炭酸ソー
ダに変化しく炭酸ソーダ1水塩は存在せず)、これは強
固にもとの無水炭酸ソーダと1体化しておシ、この部分
が剥離、粉化することはなかった。また、表面の不純物
の食塩は実質的に存在しなかった。The part of the caustic soda that adhered to the surface completely changes to anhydrous sodium carbonate, and there is no carbonate monohydrate), and this solidly integrates with the original anhydrous carbonate soda, and this part peels off. It did not turn into powder. In addition, there was substantially no common salt impurity on the surface.
比較例
実施例と同様にして得られた食塩を含む無水炭酸ソーダ
結晶ケ90℃、11%の苛性ソーダ水溶液にて洗浄した
ところ、結晶表面の1部は炭酸ソーダ1水塩に変シ、た
ちまち、粒子同志が固結し、ブロック状となった。Comparative Example When an anhydrous sodium carbonate crystal containing salt obtained in the same manner as in the example was washed with an 11% aqueous sodium hydroxide solution at 90°C, a portion of the crystal surface converted to sodium carbonate monohydrate and immediately. The particles solidified together and became block-shaped.
第1図は、本発明方法を実施するための苛性ソーダ水溶
液濃度と洗浄温度の条件を示すグラフであり、領域Xが
、本発明を実施するための条件を示す領域である。
代理人内 1) 明
代理人萩原亮−FIG. 1 is a graph showing the conditions of caustic soda aqueous solution concentration and cleaning temperature for implementing the method of the present invention, and region X is the region showing the conditions for implementing the present invention. Agents 1) Akira Agent Ryo Hagiwara
Claims (1)
の領域Xを維持するように、無水炭酸ソーダ結晶を苛性
ソーダ水浴液で洗浄することを特徴とする無水炭酸ソー
ダ結晶の洗浄方法(2)洗浄ののち、炭酸ガス又は炭酸
ガスを含む雰囲気で乾燥する特許請求の範囲第(1)項
の無水炭酸ソーダ結晶の洗浄方法(A method for cleaning anhydrous soda carbonate crystals, which is characterized in that when cleaning 11% sodium hydroxide crystals, the anhydrous sodium carbonate crystals are washed with a caustic soda water bath solution so as to maintain the area X in the k:1 diagram (2) ) The method for cleaning anhydrous soda crystals according to claim (1), which comprises drying in carbon dioxide gas or an atmosphere containing carbon dioxide gas after cleaning.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP11923281A JPS5826027A (en) | 1981-07-31 | 1981-07-31 | Washing method for anhydrous sodium carbonate crystal |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP11923281A JPS5826027A (en) | 1981-07-31 | 1981-07-31 | Washing method for anhydrous sodium carbonate crystal |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS5826027A true JPS5826027A (en) | 1983-02-16 |
JPS6363485B2 JPS6363485B2 (en) | 1988-12-07 |
Family
ID=14756226
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP11923281A Granted JPS5826027A (en) | 1981-07-31 | 1981-07-31 | Washing method for anhydrous sodium carbonate crystal |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS5826027A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS63286341A (en) * | 1987-05-20 | 1988-11-24 | Teijin Ltd | Film for electronic photograph |
-
1981
- 1981-07-31 JP JP11923281A patent/JPS5826027A/en active Granted
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS63286341A (en) * | 1987-05-20 | 1988-11-24 | Teijin Ltd | Film for electronic photograph |
Also Published As
Publication number | Publication date |
---|---|
JPS6363485B2 (en) | 1988-12-07 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US3899571A (en) | Method for the removal of organic substances from sodium aluminate solution | |
US4303621A (en) | Process for the recovery of methionine and potassium bicarbonate | |
JPS5826027A (en) | Washing method for anhydrous sodium carbonate crystal | |
US3150177A (en) | Process for producing biuret | |
US4610865A (en) | Process for the production of potassium peroxymonosulphate triple salt | |
US2380620A (en) | Production of alkali metal percarbonates | |
SU1279954A1 (en) | Method of producing sodium thiosulfate | |
US4112061A (en) | Production of sodium sulfite utilizing mother liquor from the sodium metabisulfite process | |
US2080528A (en) | Process of manufacturing anhydrous sodium sulphite | |
US2089557A (en) | Process for recovering sodium sulphate and increasing the yield of boric acid | |
US2666686A (en) | Production of sodium bicarbonate and ammonium chloride in modified ammonia-soda type process | |
US1430449A (en) | Method of preparing aluminum-chloride crystals | |
US3259471A (en) | Producing sodium sesquicarbonate using diatomaceous earth as a filter aid | |
US2487480A (en) | Process for producing ammonium sulfamate | |
US1883262A (en) | Process of recovering alkali metal salts from brines | |
US2533114A (en) | Manufacture of glutamic acid | |
JPH05295568A (en) | Method for regenerating alkaline etchant of aluminum | |
GB2224726A (en) | Potassium persulphate | |
US3109705A (en) | Production of a non-caking borax | |
CA1093786A (en) | Production of sodium sulfite | |
US2806881A (en) | Production of acrylamide | |
US2021986A (en) | Production of pure lithium compounds from impure solutions | |
US2816891A (en) | E- jackson | |
JPS6047207B2 (en) | Method for producing cupric hydroxide | |
JPH0368856B2 (en) |