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JPS6317772B2 - - Google Patents
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JPS6317772B2 - - Google Patents

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Publication number
JPS6317772B2
JPS6317772B2 JP10309480A JP10309480A JPS6317772B2 JP S6317772 B2 JPS6317772 B2 JP S6317772B2 JP 10309480 A JP10309480 A JP 10309480A JP 10309480 A JP10309480 A JP 10309480A JP S6317772 B2 JPS6317772 B2 JP S6317772B2
Authority
JP
Japan
Prior art keywords
calcium chloride
aqueous solution
concentration
chloride aqueous
salt
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.)
Expired
Application number
JP10309480A
Other languages
Japanese (ja)
Other versions
JPS5734023A (en
Inventor
Toyozo Iwamoto
Yoshito Kawamura
Eiji Yamatoki
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Tokuyama Corp
Original Assignee
Tokuyama Corp
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Tokuyama Corp filed Critical Tokuyama Corp
Priority to JP10309480A priority Critical patent/JPS5734023A/en
Publication of JPS5734023A publication Critical patent/JPS5734023A/en
Publication of JPS6317772B2 publication Critical patent/JPS6317772B2/ja
Granted legal-status Critical Current

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  • Compounds Of Alkaline-Earth Elements, Aluminum Or Rare-Earth Metals (AREA)

Description

【発明の詳細な説明】 本発明は塩化カルシウム水溶液の濃縮方法に関
する。詳しくは、粒状、フレーク状等の固形塩化
カルシウム製品の製造に適した濃厚塩化カルシウ
ム水溶液を得ることを目的とした塩化カルシウム
水溶液の濃縮方法である。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for concentrating an aqueous calcium chloride solution. Specifically, it is a method for concentrating a calcium chloride aqueous solution for the purpose of obtaining a concentrated calcium chloride aqueous solution suitable for manufacturing solid calcium chloride products such as granules and flakes.

従来、アンモニア・ソーダ法におけるアンモニ
ア蒸留排液或いは塩化アンモニウム水溶液に水酸
化カルシウムを添加してアンモニアの蒸留を行な
つた後の排液は塩化カルシウムを主成分とする水
溶液であり塩化カルシウム製品の原料として一般
に使用される。該製品の1つとして粒状、フレー
ク状等の固形塩化カルシウム製品がある。該固形
塩化カルシウム製品は通常前記蒸留排液を蒸発濃
縮して濃厚な塩化カルシウム水溶液とし、該濃厚
塩化カルシウム水溶液をノズルから滴下すると共
に冷風と接触させて固化し粒状体としたり、ロー
タリードラム式フレーカーでフレーク状体として
製造されている。
Conventionally, the ammonia distillation effluent in the ammonia-soda method or the effluent after distilling ammonia by adding calcium hydroxide to an ammonium chloride aqueous solution is an aqueous solution whose main component is calcium chloride, and is used as a raw material for calcium chloride products. commonly used as One such product is a solid calcium chloride product in the form of granules, flakes, etc. The solid calcium chloride product is usually produced by evaporating and concentrating the distillation waste liquid to form a concentrated calcium chloride aqueous solution, and then dripping the concentrated calcium chloride aqueous solution from a nozzle and solidifying it into granules by contacting with cold air, or by using a rotary drum flaker. It is manufactured in flake form.

従来の濃縮方法で得られる濃厚塩化カルシウム
水溶液の濃度は71〜72重量%程度と低く、該水溶
液から得られる固形塩化カルシウム製品は固結し
易く、特に梅雨期は不良品の発生を招くことが多
くある。また、上記固形塩化カルシウム製品はも
ろく、ダストが発生し易いため、作業環境に悪影
響を与えるばかりでなく、製品の損失を招くとい
う問題があつた。上記問題を解決するためには塩
化カルシウム水溶液の濃縮を更に行ないより濃厚
な塩化カルシウム水溶液を用いて造粒すればよい
が、従来の濃縮法では濃度72重量%程度を越えて
濃縮すると蒸発缶内に塩化カルシウムの一水塩の
結晶が析出し溶液の固化が起こるため通常は不可
能であつた。従つて、現在ではやむなく72%まで
濃縮しこれを造粒した後更に乾燥工程に導き乾燥
し、それを冷却設備で冷却して最終製品とする方
法が採用されている。このため設備の複雑化と、
製造コストの増大を招いている。
The concentration of concentrated calcium chloride aqueous solutions obtained by conventional concentration methods is as low as 71 to 72% by weight, and solid calcium chloride products obtained from the aqueous solutions tend to solidify, which can lead to the occurrence of defective products, especially during the rainy season. There are many. Furthermore, the solid calcium chloride product is brittle and easily generates dust, which not only adversely affects the working environment but also causes product loss. In order to solve the above problem, it is possible to further concentrate the calcium chloride aqueous solution and granulate it using a more concentrated calcium chloride aqueous solution, but in the conventional concentration method, if the concentration exceeds about 72% by weight, Normally, this would not be possible because crystals of calcium chloride monohydrate would precipitate and the solution would solidify. Therefore, the current method of concentrating it to 72%, granulating it, leading it to a drying process and drying it, and then cooling it with a cooling equipment to make the final product is adopted. This makes the equipment more complex and
This results in an increase in manufacturing costs.

本発明者等は上述した問題を解消すべく鋭意研
究を重ねた結果、塩化カルシウム水溶液中に食塩
を特定の割合で存在させて、蒸発濃縮を行なうこ
とにより、蒸発缶内で該水溶液が固化することな
く高濃度の濃厚塩化カルシウム水溶液が得られる
ことを見い出した。また、上記濃縮を塩化カルシ
ウム濃度で72.5重量%以上まで行なうと該濃厚塩
化カルシウム水溶液より得られる固形塩化カルシ
ウム製品の固結がなくなり、また強度も向上する
ことを見い出し本発明を完成するに至つた。
As a result of extensive research in order to solve the above-mentioned problems, the present inventors have found that by making common salt exist in a specific ratio in a calcium chloride aqueous solution and performing evaporation concentration, the aqueous solution solidifies in the evaporator. It has been found that a highly concentrated calcium chloride aqueous solution can be obtained without any problems. Furthermore, the inventors have discovered that when the above-mentioned concentration is carried out to a calcium chloride concentration of 72.5% by weight or more, the solid calcium chloride product obtained from the concentrated calcium chloride aqueous solution is free from caking, and its strength is also improved, leading to the completion of the present invention. .

即ち、本発明は塩化カルシウム水溶液を蒸発濃
縮するに際し、塩化カルシウム水溶液中に
NaCl/CaCl2重量比が0.025〜0.041の範囲で食塩
を存在させ、該食塩が析出しない温度で塩化カル
シウム濃度72.5重量%以上に濃縮することを特徴
とする塩化カルシウム水溶液の濃縮方法である。
That is, in the present invention, when evaporating and concentrating a calcium chloride aqueous solution,
This is a method for concentrating a calcium chloride aqueous solution, which is characterized in that common salt is present at a NaCl/CaCl 2 weight ratio in the range of 0.025 to 0.041, and concentration is carried out to a calcium chloride concentration of 72.5% by weight or more at a temperature at which the salt does not precipitate.

本発明において、塩化カルシウム水溶液は塩化
カルシウムを主成分として溶解する水溶液が特に
制限なく使用される。例えば、アンモニア・ソー
ダ法におけるアンモニアの蒸留排液、塩化アンモ
ニウム水溶液に水酸化カルシウムを添加してアン
モニアの蒸留を行なつた後の排液等が代表的であ
る。
In the present invention, as the calcium chloride aqueous solution, an aqueous solution in which calcium chloride is dissolved as a main component can be used without particular limitation. For example, typical examples include ammonia distillation effluent in the ammonia-soda method, and ammonia distillation effluent after adding calcium hydroxide to an aqueous ammonium chloride solution to distill ammonia.

本発明の濃縮方法において、塩化カルシウム水
溶液は食塩を存在させ、且つ該食塩がNaCl/
CaCl2重量比で0.025〜0.041、好ましくは0.028〜
0.038となるように調整することが必要である。
該食塩が上記範囲より少ないと後述する濃縮操作
により所期の濃度に濃縮する途中で塩化カルシウ
ム1水塩の結晶が析出し、溶液の固化が起こる。
また、食塩が前記範囲より多いと上記濃縮途中で
食塩結晶が析出して成長し、配管の閉塞、前記造
粒時におけるノズルの閉塞を招く。即ち、塩化カ
ルシウム水溶液中の食塩濃度を前記範囲内に調整
することによつて、後述する濃縮操作により、溶
液の固化或いは食塩の析出を防止して塩化カルシ
ウム水溶液の濃度を所期の濃度まで濃縮すること
ができる。塩化カルシウム水溶液中の食塩濃度を
前記範囲内に調整する手段は特に制限されない。
例えば、塩化カルシウム水溶液が前記アンモニ
ア・ソーダ法におけるアンモニア蒸留排液であれ
ば、その液組成は通常塩化カルシウム濃度約10〜
11重量%、食塩濃度約4〜5重量%である。この
ようにNaCl/CaCl2重量比が前記範囲を越えて
いる場合は、該塩化カルシウム水溶液をそのま
ま、場合によつては適当な濃度まで濃縮し、食塩
の過剰分が析出する温度下で析出した食塩を分離
する方法が好適である。
In the concentration method of the present invention, the calcium chloride aqueous solution has common salt present, and the common salt is NaCl/
CaCl2 weight ratio 0.025~0.041, preferably 0.028~
It is necessary to adjust it to 0.038.
If the salt content is less than the above range, crystals of calcium chloride monohydrate will precipitate during concentration to a desired concentration by the concentration operation described later, and the solution will solidify.
Furthermore, if the amount of salt exceeds the above range, salt crystals will precipitate and grow during the concentration, resulting in clogging of piping and nozzles during granulation. That is, by adjusting the salt concentration in the calcium chloride aqueous solution within the above range, the concentration of the calcium chloride aqueous solution can be concentrated to the desired concentration by preventing solidification of the solution or precipitation of salt by the concentration operation described later. can do. There are no particular restrictions on the means for adjusting the salt concentration in the calcium chloride aqueous solution within the above range.
For example, if the calcium chloride aqueous solution is the ammonia distillation effluent in the ammonia-soda method, the liquid composition usually has a calcium chloride concentration of about 10 to
11% by weight, and the salt concentration is about 4-5% by weight. If the NaCl/CaCl 2 weight ratio exceeds the above range, the calcium chloride aqueous solution may be concentrated as it is, depending on the case, to an appropriate concentration, and the excess salt may be precipitated at a temperature that allows it to precipitate. A method of separating common salt is preferred.

上記方法は塩化カルシウムと食塩との各温度に
おける相互溶解度曲線を予め作成しておき、該相
互溶解度曲線に基づき前記塩化カルシウム水溶液
の塩化カルシウム濃度において食塩の飽和溶解度
量が前記範囲内となる温度を求め、該温度下で食
塩の分離を行なうことにより当業者が容易に実施
することができる。具体的に例示すれば、前記ア
ンモニア・ソーダ法におけるアンモニア蒸留排液
を38重量%まで濃縮し、45℃の温度で析出する食
塩を過すればNaCl/CaCl2重量比が約0.04の塩
化カルシウム水溶液を得ることができる。また、
他の方法として食塩含有量の少ない塩化カルシウ
ム或いは塩化カルシウム水溶液を前記塩化カルシ
ウム水溶液に添加してNaCl/CaCl2重量比を調
整することも可能である。一方、NaCl/CaCl2
重量比が前記範囲より低い場合、例えば、塩化カ
ルシウム水溶液が、ほぼ純粋な塩化アンモニウム
水溶液に水酸化カルシウムを添加してアンモニア
の蒸留を行なつた後の排液である場合は、該塩化
カルシウム水溶液中に食塩成分を添加して
NaCl/CaCl2重量比が該範囲内となるようにす
ればよい。上記塩化カルシウム水溶液中への食塩
成分の添加方法は特に制限されない。例えば、該
塩化カルシウム水溶液に直接必要量の食塩を投入
する方法、該塩化カルシウム水溶液をそのまま或
いは適当な濃度に濃縮した後該水溶液における食
塩の飽和溶解度量が前記範囲内に入る温度下で食
塩層を通過させる方法、或いは該塩化カルシウム
水溶液に前記食塩濃度が高い塩化カルシウム水溶
液を添加する方法が代表的である。
In the above method, a mutual solubility curve of calcium chloride and common salt at each temperature is created in advance, and based on the mutual solubility curve, the temperature at which the saturated solubility of common salt is within the above range at the calcium chloride concentration of the calcium chloride aqueous solution is determined. Those skilled in the art can easily carry out the separation of common salt at the desired temperature. To give a specific example, if the ammonia distillation effluent in the ammonia-soda method is concentrated to 38% by weight and the salt precipitated at a temperature of 45°C is filtered, an aqueous calcium chloride solution with a NaCl/CaCl 2 weight ratio of about 0.04 is obtained. can be obtained. Also,
As another method, it is also possible to adjust the NaCl/CaCl 2 weight ratio by adding calcium chloride or a calcium chloride aqueous solution with a low salt content to the calcium chloride aqueous solution. On the other hand, NaCl/CaCl 2
When the weight ratio is lower than the above range, for example, when the calcium chloride aqueous solution is a waste liquid obtained by adding calcium hydroxide to an almost pure ammonium chloride aqueous solution and distilling ammonia, the calcium chloride aqueous solution Add salt ingredients inside
The NaCl/CaCl 2 weight ratio may be within this range. The method of adding the salt component to the calcium chloride aqueous solution is not particularly limited. For example, a method of adding the necessary amount of salt directly to the calcium chloride aqueous solution, or a method of directly adding the required amount of salt to the calcium chloride aqueous solution, or a method of adding the calcium chloride aqueous solution as it is or after concentrating it to an appropriate concentration and forming a salt layer at a temperature such that the saturated solubility of salt in the aqueous solution falls within the above range. Typical methods include a method in which a calcium chloride aqueous solution having a high salt concentration is added to the calcium chloride aqueous solution.

本発明において、NaCl/CaCl2重量比を前記
範囲内に調整された塩化カルシウム水溶液は食塩
が析出しない温度で蒸発濃縮される。該温度は一
概に限定することはできないが、通常常圧での塩
化カルシウム水溶液の沸点に設定するのが一般的
である。
In the present invention, an aqueous calcium chloride solution whose NaCl/CaCl 2 weight ratio is adjusted within the above range is evaporated and concentrated at a temperature at which common salt does not precipitate. Although the temperature cannot be absolutely limited, it is generally set to the boiling point of an aqueous calcium chloride solution at normal pressure.

上記塩化カルシウム水溶液の濃縮は塩化カルシ
ウム濃度72.5重量%以上、好ましくは73.0重量%
以上とすることが必要である。該塩化カルシウム
濃度が上記範囲より低いと、該塩化カルシウム水
溶液を用いて得られる固形塩化カルシウム製品の
固結が起こり易くなつたり、強度が低下しダスト
が発生し易くなる。該塩化カルシウム濃度は高い
程上記現象の防止に効果的であるがあまり高過ぎ
ると塩化カルシウムの1水塩の析出が起こる。該
濃度の上限は含まれる食塩の割合によつて多少異
なるが一般に74.5重量%、好ましくは74.0重量%
とすればよい。
Concentrating the calcium chloride aqueous solution has a calcium chloride concentration of 72.5% by weight or more, preferably 73.0% by weight.
It is necessary to do the above. If the calcium chloride concentration is lower than the above range, the solid calcium chloride product obtained using the calcium chloride aqueous solution is likely to caking, its strength is reduced, and dust is likely to be generated. The higher the calcium chloride concentration, the more effective it is in preventing the above phenomenon, but if it is too high, calcium chloride monohydrate will precipitate. The upper limit of the concentration varies somewhat depending on the proportion of salt contained, but is generally 74.5% by weight, preferably 74.0% by weight.
And it is sufficient.

以上の説明より理解される如く、本発明の濃縮
方法によれば、塩化カルシウムの1水塩の析出を
伴なうことなく塩化カルシウム水溶液を高濃度に
濃縮することができる。従つて、濃縮して得られ
た濃厚塩化カルシウム水溶液は造粒、フレーク化
するだけで固結せずしかも強度がある固形塩化カ
ルシウム製品とすることができ、従来のように造
粒、フレーク化の後に乾燥工程等を設ける必要が
なく非常に経済的である。
As understood from the above explanation, according to the concentration method of the present invention, an aqueous calcium chloride solution can be concentrated to a high concentration without precipitation of calcium chloride monohydrate. Therefore, the concentrated calcium chloride aqueous solution obtained by concentration can be made into a solid calcium chloride product that does not solidify and is strong simply by granulating and flaking. It is very economical as there is no need to provide a drying process etc. afterwards.

以下、本発明を具体的に説明するため実施例を
示すが本発明はこれらの実施例に限定されるもの
ではない。
Examples are shown below to specifically explain the present invention, but the present invention is not limited to these Examples.

尚、実施例及び比較例において、折れ強度は次
の方法によつて測定した。
In addition, in the Examples and Comparative Examples, the bending strength was measured by the following method.

Γ折れ強度測定法 第2図に示す如く木片1(たて6cm×よこ2cm
×高さ3cm)を4cmの間隔で平行におき、この上
に試験片2をおいた。さらに該試験片2の中心部
に、たて4cm×よこ2cm×高さ8cmの容積を有す
るボール紙製の容器3をおき、該容器に水銀4を
静かに落し込み、該試験片が折れたところですば
やく重量を秤量した。該重量を試験片にかかる荷
重の断面積で除して折れ強度(g/cm2)を求め
た。従つて折れ強度の大きいほど、固い塩化カル
シウムであり、ダストを発生しにくいといえる。
Γ Bending strength measurement method As shown in Figure 2, a piece of wood 1 (6cm long x 2cm wide)
× height 3 cm) were placed in parallel at intervals of 4 cm, and test piece 2 was placed on top of these. Further, a cardboard container 3 having a volume of 4 cm in length x 2 cm in width x 8 cm in height was placed in the center of the test piece 2, and mercury 4 was gently dropped into the container, causing the test piece to break. By the way, I quickly weighed it. The bending strength (g/cm 2 ) was determined by dividing the weight by the cross-sectional area of the load applied to the test piece. Therefore, it can be said that the higher the bending strength, the harder the calcium chloride is, and the less likely it is to generate dust.

実施例 1 塩化カルシウム10.8g/100c.c.、食塩4.5g/
100c.c.を含むアンモニア・ソーダ法の蒸留排液を
常圧で120℃となるまで濃縮した後45℃に冷却し、
該溶液を45℃に保温して析出した食塩を過し
た。得られた塩化カルシウム水溶液の組成は塩化
カルシウム38.5重量%、食塩1.5重量%(NaCl/
CaCl2=0.039)であつた。この塩化カルシウム水
溶液を常圧で178℃となるまで濃縮し、塩化カル
シウム濃度72.9重量%とした。上記濃縮後の塩化
カルシウム水溶液を巾2cm、長さ10cm、深さ0.5
cmのSUS304製の枠に深さ1mmまで流して冷却し
試験片を作成し、折れ強度を測定した。その結果
折れ強度は42g/cm2であつた。また、上記試験片
2枚を重ねて100gの分銅を載せ、湿度80%の室
内に1週間放置し固結状態を観察したところ、固
結は全くなかつた。更に前記塩化カルシウム水溶
液が固化するまで濃縮し、その常圧での温度及び
塩化カルシウム濃度(以下濃縮限界温度及び限界
濃度という)を測定した結果、濃縮限界温度は
182℃、限界濃度は74.2重量%であつた。
Example 1 Calcium chloride 10.8g/100c.c., salt 4.5g/
The ammonia-soda process distillation waste containing 100 c.c. was concentrated at normal pressure to 120°C, then cooled to 45°C.
The solution was kept at 45° C. and the precipitated common salt was filtered off. The composition of the obtained calcium chloride aqueous solution was 38.5% by weight of calcium chloride, 1.5% by weight of common salt (NaCl/
CaCl 2 =0.039). This calcium chloride aqueous solution was concentrated at normal pressure to 178° C. to give a calcium chloride concentration of 72.9% by weight. The calcium chloride aqueous solution after the above concentration is 2cm wide, 10cm long, and 0.5cm deep.
The sample was poured into a 1 mm deep SUS304 frame and cooled to prepare a test piece, and its bending strength was measured. As a result, the bending strength was 42 g/cm 2 . Further, when the above two test pieces were stacked and a weight of 100 g was placed on them, and the test pieces were left in a room with a humidity of 80% for one week and the state of caking was observed, there was no caking at all. Furthermore, the calcium chloride aqueous solution was concentrated until it solidified, and the temperature and calcium chloride concentration (hereinafter referred to as concentration limit temperature and concentration limit concentration) at normal pressure were measured. As a result, the concentration limit temperature was found to be
At 182°C, the critical concentration was 74.2% by weight.

実施例 2 実施例1と同様にして得られたNaCl/CaCl2
=0.039の塩化カルシウム水溶液を加温して塩化
カルシウムを溶解してNaCl/CaCl2=0.034の塩
化カルシウム水溶液を調整し、これを常圧で182
℃となるまで濃縮し、塩化カルシウム濃度74.0重
量%とした。上記濃縮後の塩化カルシウム水溶液
を用いて実施例1と同様にして試験片を作成し、
折れ強度を測定したところ78g/cm2であつた。ま
た、実施例1と同様にして固結状態を観察したと
ころ、固結は全くなかつた。更に、前記調整後の
塩化カルシウム水溶液の濃縮限界温度は183℃、
限界濃度は74.3重量%であつた。
Example 2 NaCl/CaCl 2 obtained in the same manner as Example 1
= 0.039 calcium chloride aqueous solution is heated to dissolve the calcium chloride to prepare a calcium chloride aqueous solution of NaCl/CaCl 2 = 0.034, and this is heated at normal pressure to 182
It was concentrated until the temperature reached ℃, giving a calcium chloride concentration of 74.0% by weight. A test piece was prepared in the same manner as in Example 1 using the above concentrated calcium chloride aqueous solution,
The bending strength was measured and found to be 78 g/cm 2 . Further, when the caking state was observed in the same manner as in Example 1, there was no caking at all. Furthermore, the concentration limit temperature of the calcium chloride aqueous solution after the adjustment is 183°C,
The critical concentration was 74.3% by weight.

実施例 3 実施例1と同様にして得られたNaCl/CaCl2
=0.039の塩化カルシウム水溶液を加温して塩化
カルシウムを溶解しNaCl/CaCl2=0.025の塩化
カルシウム水溶液を調整し、これを常圧で180℃
となるまで濃縮し、塩化カルシウム濃度72.5重量
%とした。上記濃縮後の塩化カルシウム水溶液を
用いて実施例1と同様にして試験片を作成し、折
れ強度を測定したところ、40g/cm2であつた。ま
た、実施例1と同様にして固結状態を観察したと
ころ、固結は全くなかつた。更に、前記調整後の
塩化カルシウム水溶液の濃縮限界温度は180℃、
限界濃度は73.2重量%であつた。
Example 3 NaCl/CaCl 2 obtained in the same manner as Example 1
=0.039 calcium chloride aqueous solution was heated to dissolve the calcium chloride to prepare a calcium chloride aqueous solution of NaCl/CaCl 2 =0.025, and this was heated at 180℃ at normal pressure.
It was concentrated to give a calcium chloride concentration of 72.5% by weight. A test piece was prepared in the same manner as in Example 1 using the concentrated calcium chloride aqueous solution, and the bending strength was measured, and it was found to be 40 g/cm 2 . Further, when the caking state was observed in the same manner as in Example 1, there was no caking at all. Furthermore, the concentration limit temperature of the calcium chloride aqueous solution after the adjustment is 180°C,
The critical concentration was 73.2% by weight.

実施例 4 塩化アンモニウム水溶液に水酸化カルシウムを
添加してアンモニアを蒸留した後の排液(塩化カ
ルシウム濃度10.8重量%)に食塩を添加して
NaCl/CaCl2=0.038の塩化カルシウム水溶液を
調整した。該塩化カルシウム水溶液を常圧で178
℃まで濃縮し、塩化カルシウム濃度73.1重量%と
した。上記濃縮後の塩化カルシウム水溶液を用い
て実施例1と同様にして試験片を作成し、折れ強
度を測定したところ、45g/cm2であつた。また、
実施例1と同様にして固結状態を観察したところ
固結は全くなかつた。更に、前記調整後の塩化カ
ルシウム水溶液の濃縮限界温度は182℃、限界濃
度は74.3重量%であつた。
Example 4 After adding calcium hydroxide to an aqueous ammonium chloride solution and distilling ammonia, salt was added to the effluent (calcium chloride concentration 10.8% by weight).
A calcium chloride aqueous solution with NaCl/CaCl 2 =0.038 was prepared. The calcium chloride aqueous solution was heated to 178% at normal pressure.
It was concentrated to ℃ to give a calcium chloride concentration of 73.1% by weight. A test piece was prepared in the same manner as in Example 1 using the concentrated calcium chloride aqueous solution, and the bending strength was measured to be 45 g/cm 2 . Also,
When the caking state was observed in the same manner as in Example 1, there was no caking at all. Further, the concentration limit temperature of the calcium chloride aqueous solution after the above adjustment was 182° C., and the limit concentration was 74.3% by weight.

比較例 1 実施例1において食塩の過温度を変えて、食
塩の過を行ない塩化カルシウム38.5重量%、
NaCl/CaCl2=0.055の塩化カルシウム水溶液を
得た。この塩化カルシウム水溶液を常圧で170℃
濃度67.0重量%まで濃縮したところ白濁し始めた
ので直ちに実施例1と同様にして試験片を作成し
て折れ強度を測定した。その結果は35g/cm2であ
つた。また、実施例1と同様にして固結状態を観
察したところ、強固に固結していた。
Comparative Example 1 In Example 1, the overtemperature of the common salt was changed and the overheating of the common salt was carried out to obtain 38.5% by weight of calcium chloride,
A calcium chloride aqueous solution with NaCl/CaCl 2 =0.055 was obtained. This calcium chloride aqueous solution was heated to 170℃ at normal pressure.
When the mixture was concentrated to a concentration of 67.0% by weight, it began to become cloudy, so a test piece was immediately prepared in the same manner as in Example 1 and its bending strength was measured. The result was 35 g/cm 2 . Moreover, when the solidification state was observed in the same manner as in Example 1, it was found that the solidification was firmly solidified.

比較例 2 実施例1において濃縮温度を172℃とし、塩化
カルシウム濃度70.9重量%とした以外は同様にし
て試験片を作成し、折れ強度を測定したところ29
g/cm2であつた。また、実施例1と同様にして固
結状態を観察したところ強固に固結していた。
Comparative Example 2 A test piece was prepared in the same manner as in Example 1 except that the concentration temperature was 172°C and the calcium chloride concentration was 70.9% by weight, and the bending strength was measured.29
g/ cm2 . In addition, when the solidification state was observed in the same manner as in Example 1, it was found to be firmly solidified.

比較例 3 実施例1と同様にして得られたNaCl/CaCl2
=0.039の塩化カルシウムを加温して塩化カルシ
ウムを溶解し、NaCl/CaCl2=0.018の塩化カル
シウム水溶液を調整し、これを常圧で173℃とな
るまで濃縮し、塩化カルシウム濃度70.7重量%と
した。上記濃縮後の塩化カルシウム水溶液を用い
て実施例1と同様にして試験片を作成し、折れ強
度を測定した。その結果18Kg/cm2であつた。ま
た、実施例1と同様にして固結状態を観察した結
果、強固に固結していた。更に、前記調整後の塩
化カルシウム水溶液の濃縮限界温度は174℃、限
界濃度は71.1重量%であつた。
Comparative Example 3 NaCl/CaCl 2 obtained in the same manner as Example 1
= 0.039 calcium chloride is heated to dissolve the calcium chloride to prepare a calcium chloride aqueous solution of NaCl/CaCl 2 = 0.018, and this is concentrated at normal pressure to 173°C to give a calcium chloride concentration of 70.7% by weight. did. A test piece was prepared in the same manner as in Example 1 using the concentrated calcium chloride aqueous solution, and the bending strength was measured. The result was 18Kg/ cm2 . Moreover, as a result of observing the solidification state in the same manner as in Example 1, it was found that the solidification state was firmly solidified. Further, the concentration limit temperature of the calcium chloride aqueous solution after the above adjustment was 174° C., and the limit concentration was 71.1% by weight.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は折れ強度の測定に用いる装置を示す。
図において、1は木片、2は試験片、3は容器、
4は水銀を夫々示す。
FIG. 1 shows the apparatus used to measure bending strength.
In the figure, 1 is a wooden piece, 2 is a test piece, 3 is a container,
4 represents mercury.

Claims (1)

【特許請求の範囲】 1 塩化カルシウム水溶液を蒸発濃縮するに際
し、塩化カルシウム水溶液中にNaCl/CaCl2
量比が0.025〜0.041の範囲で食塩を存在させ、該
食塩が析出しない温度で塩化カルシウム濃度72.5
重量%以上に濃縮することを特徴とする塩化カル
シウム水溶液の濃縮方法。 2 塩化カルシウム及び食塩を含有した水溶液中
の食塩を析出させ、分離することによりNaCl/
CaCl2重量比を0.025〜0.041の範囲に調整した後
濃縮を行なう特許請求の範囲1記載の方法。 3 塩化カルシウム水溶液に食塩成分を添加して
NaCl/CaCl2重量比を0.025〜0.041の範囲に調整
した後濃縮を行なう特許請求の範囲1記載の方
法。
[Claims] 1. When concentrating a calcium chloride aqueous solution by evaporation, common salt is present in the calcium chloride aqueous solution with a NaCl/CaCl 2 weight ratio in the range of 0.025 to 0.041, and the calcium chloride concentration is 72.5 at a temperature at which the salt does not precipitate.
A method for concentrating an aqueous calcium chloride solution, the method comprising concentrating an aqueous solution of calcium chloride to more than % by weight. 2. By precipitating and separating the salt in the aqueous solution containing calcium chloride and common salt, NaCl/
The method according to claim 1, wherein the concentration is carried out after adjusting the CaCl 2 weight ratio to a range of 0.025 to 0.041. 3 Adding salt components to calcium chloride aqueous solution
The method according to claim 1, wherein the concentration is carried out after adjusting the NaCl/CaCl 2 weight ratio to a range of 0.025 to 0.041.
JP10309480A 1980-07-29 1980-07-29 Concentration of calcium chloride aqueous solution Granted JPS5734023A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP10309480A JPS5734023A (en) 1980-07-29 1980-07-29 Concentration of calcium chloride aqueous solution

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP10309480A JPS5734023A (en) 1980-07-29 1980-07-29 Concentration of calcium chloride aqueous solution

Publications (2)

Publication Number Publication Date
JPS5734023A JPS5734023A (en) 1982-02-24
JPS6317772B2 true JPS6317772B2 (en) 1988-04-15

Family

ID=14345041

Family Applications (1)

Application Number Title Priority Date Filing Date
JP10309480A Granted JPS5734023A (en) 1980-07-29 1980-07-29 Concentration of calcium chloride aqueous solution

Country Status (1)

Country Link
JP (1) JPS5734023A (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104495904B (en) * 2014-12-30 2016-08-31 宁波环洋化工有限公司 A kind of production method of calcium chloride dihydrate

Also Published As

Publication number Publication date
JPS5734023A (en) 1982-02-24

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