JPS6144806B2 - - Google Patents
Info
- Publication number
- JPS6144806B2 JPS6144806B2 JP57228982A JP22898282A JPS6144806B2 JP S6144806 B2 JPS6144806 B2 JP S6144806B2 JP 57228982 A JP57228982 A JP 57228982A JP 22898282 A JP22898282 A JP 22898282A JP S6144806 B2 JPS6144806 B2 JP S6144806B2
- Authority
- JP
- Japan
- Prior art keywords
- salt
- caustic soda
- slaked lime
- exhaust gas
- solution
- 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
Links
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 claims description 51
- 235000002639 sodium chloride Nutrition 0.000 claims description 33
- 239000002699 waste material Substances 0.000 claims description 25
- 150000003839 salts Chemical class 0.000 claims description 22
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 claims description 17
- 235000011121 sodium hydroxide Nutrition 0.000 claims description 17
- 239000007789 gas Substances 0.000 claims description 13
- 239000000243 solution Substances 0.000 claims description 13
- 238000005406 washing Methods 0.000 claims description 13
- 239000007788 liquid Substances 0.000 claims description 12
- 238000000034 method Methods 0.000 claims description 12
- 239000011780 sodium chloride Substances 0.000 claims description 11
- AXCZMVOFGPJBDE-UHFFFAOYSA-L calcium dihydroxide Chemical compound [OH-].[OH-].[Ca+2] AXCZMVOFGPJBDE-UHFFFAOYSA-L 0.000 claims description 10
- 239000000920 calcium hydroxide Substances 0.000 claims description 10
- 235000011116 calcium hydroxide Nutrition 0.000 claims description 10
- 229910001861 calcium hydroxide Inorganic materials 0.000 claims description 10
- 229910001385 heavy metal Inorganic materials 0.000 claims description 10
- 239000000779 smoke Substances 0.000 claims description 10
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 claims description 8
- IXCSERBJSXMMFS-UHFFFAOYSA-N hydrogen chloride Substances Cl.Cl IXCSERBJSXMMFS-UHFFFAOYSA-N 0.000 claims description 8
- 229910000041 hydrogen chloride Inorganic materials 0.000 claims description 8
- 239000012535 impurity Substances 0.000 claims description 7
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 claims description 6
- 238000002485 combustion reaction Methods 0.000 claims description 5
- 239000013078 crystal Substances 0.000 claims description 5
- 239000011575 calcium Substances 0.000 claims description 4
- FBAFATDZDUQKNH-UHFFFAOYSA-M iron chloride Chemical compound [Cl-].[Fe] FBAFATDZDUQKNH-UHFFFAOYSA-M 0.000 claims description 4
- 238000004519 manufacturing process Methods 0.000 claims description 4
- BVKZGUZCCUSVTD-UHFFFAOYSA-L Carbonate Chemical compound [O-]C([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-L 0.000 claims description 3
- 229910052791 calcium Inorganic materials 0.000 claims description 3
- 239000011259 mixed solution Substances 0.000 claims description 3
- 229910052979 sodium sulfide Inorganic materials 0.000 claims description 3
- GRVFOGOEDUUMBP-UHFFFAOYSA-N sodium sulfide (anhydrous) Chemical compound [Na+].[Na+].[S-2] GRVFOGOEDUUMBP-UHFFFAOYSA-N 0.000 claims description 3
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 claims description 2
- 239000012452 mother liquor Substances 0.000 description 9
- 235000008733 Citrus aurantifolia Nutrition 0.000 description 5
- 235000011941 Tilia x europaea Nutrition 0.000 description 5
- 239000004571 lime Substances 0.000 description 5
- 239000002244 precipitate Substances 0.000 description 5
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 4
- 238000010438 heat treatment Methods 0.000 description 4
- 239000000203 mixture Substances 0.000 description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 3
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 3
- UCKMPCXJQFINFW-UHFFFAOYSA-N Sulphide Chemical compound [S-2] UCKMPCXJQFINFW-UHFFFAOYSA-N 0.000 description 3
- BZHJMEDXRYGGRV-UHFFFAOYSA-N Vinyl chloride Chemical compound ClC=C BZHJMEDXRYGGRV-UHFFFAOYSA-N 0.000 description 3
- 238000001914 filtration Methods 0.000 description 3
- 238000011084 recovery Methods 0.000 description 3
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 2
- 229910002651 NO3 Inorganic materials 0.000 description 2
- NHNBFGGVMKEFGY-UHFFFAOYSA-N Nitrate Chemical compound [O-][N+]([O-])=O NHNBFGGVMKEFGY-UHFFFAOYSA-N 0.000 description 2
- 239000013522 chelant Substances 0.000 description 2
- 239000000460 chlorine Substances 0.000 description 2
- 229910052801 chlorine Inorganic materials 0.000 description 2
- 238000004140 cleaning Methods 0.000 description 2
- 230000000052 comparative effect Effects 0.000 description 2
- 238000001035 drying Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000000295 fuel oil Substances 0.000 description 2
- 230000005484 gravity Effects 0.000 description 2
- 239000010440 gypsum Substances 0.000 description 2
- 229910052602 gypsum Inorganic materials 0.000 description 2
- 229910052742 iron Inorganic materials 0.000 description 2
- 238000000746 purification Methods 0.000 description 2
- 229920005989 resin Polymers 0.000 description 2
- 239000011347 resin Substances 0.000 description 2
- 239000002002 slurry Substances 0.000 description 2
- 239000011734 sodium Substances 0.000 description 2
- 229910052708 sodium Inorganic materials 0.000 description 2
- 241001131796 Botaurus stellaris Species 0.000 description 1
- BHPQYMZQTOCNFJ-UHFFFAOYSA-N Calcium cation Chemical compound [Ca+2] BHPQYMZQTOCNFJ-UHFFFAOYSA-N 0.000 description 1
- UXVMQQNJUSDDNG-UHFFFAOYSA-L Calcium chloride Chemical compound [Cl-].[Cl-].[Ca+2] UXVMQQNJUSDDNG-UHFFFAOYSA-L 0.000 description 1
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 1
- PMZURENOXWZQFD-UHFFFAOYSA-L Sodium Sulfate Chemical compound [Na+].[Na+].[O-]S([O-])(=O)=O PMZURENOXWZQFD-UHFFFAOYSA-L 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 239000012267 brine Substances 0.000 description 1
- 229910000019 calcium carbonate Inorganic materials 0.000 description 1
- 239000001110 calcium chloride Substances 0.000 description 1
- 229910001628 calcium chloride Inorganic materials 0.000 description 1
- 229910001424 calcium ion Inorganic materials 0.000 description 1
- PASHVRUKOFIRIK-UHFFFAOYSA-L calcium sulfate dihydrate Chemical compound O.O.[Ca+2].[O-]S([O-])(=O)=O PASHVRUKOFIRIK-UHFFFAOYSA-L 0.000 description 1
- 238000005119 centrifugation Methods 0.000 description 1
- 229920001429 chelating resin Polymers 0.000 description 1
- 238000005868 electrolysis reaction Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 239000000706 filtrate Substances 0.000 description 1
- 239000003546 flue gas Substances 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 230000008676 import Effects 0.000 description 1
- 239000000543 intermediate Substances 0.000 description 1
- 239000003014 ion exchange membrane Substances 0.000 description 1
- 235000014413 iron hydroxide Nutrition 0.000 description 1
- NCNCGGDMXMBVIA-UHFFFAOYSA-L iron(ii) hydroxide Chemical compound [OH-].[OH-].[Fe+2] NCNCGGDMXMBVIA-UHFFFAOYSA-L 0.000 description 1
- QSHDDOUJBYECFT-UHFFFAOYSA-N mercury Chemical compound [Hg] QSHDDOUJBYECFT-UHFFFAOYSA-N 0.000 description 1
- 229910052753 mercury Inorganic materials 0.000 description 1
- 239000010446 mirabilite Substances 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 239000012629 purifying agent Substances 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 239000012266 salt solution Substances 0.000 description 1
- 239000013535 sea water Substances 0.000 description 1
- 229910000029 sodium carbonate Inorganic materials 0.000 description 1
- HPALAKNZSZLMCH-UHFFFAOYSA-M sodium;chloride;hydrate Chemical compound O.[Na+].[Cl-] HPALAKNZSZLMCH-UHFFFAOYSA-M 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 150000004763 sulfides Chemical class 0.000 description 1
- 239000002918 waste heat Substances 0.000 description 1
- 238000004065 wastewater treatment Methods 0.000 description 1
Description
本発明は都市ゴミ等の焼却炉排ガスに含まれる
塩化水素を利用して精製食塩を製造する方法に関
する。
最近都市ゴミの焼却炉においては、ゴミの中に
含まれる塩化ビニール等に起因してその排ガス中
に多量の塩化水素が含まれ大きな環境問題となつ
ている。この塩化水素ガスは通常数百ppmと言
われているが時として1000ppmを越えることも
ある。このような塩化水素の除去は苛性ソーダ溶
液により洗滌する方法が最も効率良く、また再資
源化の面からみても除去の際、生成する食塩はこ
れを電解して苛性ソーダと塩化ビニール製造用塩
素を再び生産することができるので、きわめて合
理的な手段といえる。都市ゴミは現在人口10万人
に対して1日約100トン生じておりこれより食塩
1トンが得られる計算になる。したがつて日本全
体で発生する食塩の量は年間数十万トンになる
が、わが国では工業用食塩のほとんどを輸入に頼
つていること、および塩素を含有する塩化ビニー
ル中間体も多量に輸入されている現状よりみて貴
重な資源回収方法と云うことができる。しかしな
がら上記排ガスを苛性ソーダで洗滌する際に生成
する粗食塩溶液(以下洗煙廃液という)中には不
純物として種々の重金属類や食塩分に対し約15%
の芒硝分が存在するためこれらをいかに効率よく
除去して高品質の食塩を得ることができるかとい
う問題点がある。また洗煙廃液中の食塩分濃度は
最高15〜20%で濃縮用熱源を必要とするが重油等
の使用は経済上不利である。
本発明は以上のような問題点を解決するための
ものであつて、すなわち塩化水素を含む都市ゴミ
焼却炉排ガスを洗煙するにあたり苛性ソーダ溶液
および消石灰の混合液を使用し、かつ苛性ソーダ
純分に対する消石灰の重量比を0.1〜0.3とし、得
られた洗煙廃液中のカルシウム分、重金属分を主
体とする不純物を塩化鉄、硫化ソーダおよび炭酸
ソーダを加えることにより除去した後、上記都市
ゴミ焼却炉の燃焼熱により加熱濃縮して食塩結晶
を析出せしめることを特徴とする精製食塩の製造
法である。本発明方法を図面(フローシート)に
より説明すると都市ゴミ焼却炉の排ガスを苛性ソ
ーダ溶液のみで洗滌した場合、および本発明法の
ごとく苛性ソーダ溶液と消石灰により洗滌した場
合の洗煙廃液組成はゴミの種類により多少差異は
あるが代表的には次のごとくである。
The present invention relates to a method for producing purified common salt using hydrogen chloride contained in incinerator exhaust gas such as municipal waste. Recently, in incinerators for municipal waste, a large amount of hydrogen chloride is contained in the exhaust gas due to vinyl chloride, etc. contained in the waste, which has become a major environmental problem. This hydrogen chloride gas is usually said to be several hundred ppm, but sometimes it exceeds 1000 ppm. The most efficient way to remove such hydrogen chloride is to wash it with a caustic soda solution, and from the perspective of recycling, the generated common salt is electrolyzed and reused as caustic soda and chlorine for vinyl chloride production. Since it can be produced, it can be said to be an extremely rational method. Currently, approximately 100 tons of municipal waste is generated per day for every 100,000 people, which is equivalent to 1 ton of salt. Therefore, the amount of table salt generated in Japan as a whole amounts to several hundred thousand tons per year, but Japan relies on imports for most of its industrial salt, and a large amount of vinyl chloride intermediates containing chlorine are also imported. Considering the current situation, this can be said to be a valuable resource recovery method. However, the crude salt solution (hereinafter referred to as smoke washing waste liquid) produced when the above exhaust gas is washed with caustic soda contains impurities that account for about 15% of various heavy metals and salt.
Because of the presence of mirabilite, there is a problem in how efficiently these can be removed to obtain high-quality common salt. Furthermore, the salt concentration in the smoke washing waste liquid is at most 15-20%, and a heat source for concentration is required, but the use of heavy oil or the like is economically disadvantageous. The present invention is intended to solve the above-mentioned problems. Specifically, the present invention uses a mixed solution of a caustic soda solution and slaked lime to scrub the flue gas from a municipal waste incinerator containing hydrogen chloride, and uses a mixture of a caustic soda solution and slaked lime, and After adjusting the weight ratio of slaked lime to 0.1 to 0.3 and removing impurities mainly consisting of calcium and heavy metals in the obtained smoke washing waste liquid by adding iron chloride, soda sulfide and soda carbonate, the above municipal waste incinerator is heated. This is a method for producing refined common salt, which is characterized by heating and concentrating the salt using the heat of combustion to precipitate salt crystals. The method of the present invention will be explained with reference to drawings (flow sheets).When exhaust gas from a municipal waste incinerator is washed with only a caustic soda solution, and when it is washed with a caustic soda solution and slaked lime as in the method of the present invention, the composition of the smoke washing waste liquid is determined by the type of garbage. Although there are some differences depending on the situation, typical examples are as follows.
【表】
本発明法においては消石灰は苛性ソーダ純分に
対し重量比で0.1〜0.3好ましくは0.15〜0.2の範囲
で使用する。0.1未満では排ガス中の硫酸分の除
去が不完全であり、0.3をこえると塩化カルシウ
ミが生成し食塩分の損失となる。苛性ソーダ溶液
の濃度は約10〜15重量%であり、硝石灰を混合使
用する。この洗煙工程においては消石灰の代りに
塩化石灰の使用も考えられるが、一般に塩化石灰
は硝石灰に比較して可成り高価でありまた吸湿性
が大で取扱も不便である。大量に発生する都市ゴ
ミ焼却炉の排ガス用の洗滌液としては上記の理由
で塩化石灰の使用は適当でない。この洗煙廃液中
には生成石コウを主体とする不溶性物質が存在す
るのでこれを分離し、その母液に塩化鉄、硫化ソ
ーダを加えさらに要すれば苛性ソーダ等のアルカ
リを加えてPH10〜10.5程度に調整すると、母液中
に含まれる不純重金属分は硫化物として析出しこ
れをフイルタープレス等により濾過分離を行う。
塩化鉄の添加はフロツク状の水酸化鉄沈澱を生ぜ
しめ、微細な重金属硫化物沈澱を共沈させて分離
しやすくする作用を有する。さらに母液中に残存
するカルシウムイオンは炭酸ソーダを添加するこ
とにより炭酸カルシウムとして沈澱させフイルタ
ープレス等により濾過分離する。また一般に都市
ゴミ焼却炉の洗煙廃液中には水銀分の含まれるこ
とが多く、これを厳密に精製するためには最終的
にキレート樹脂またはキレート剤担持活性炭に母
液を通液させて除去する。このようにしてきわめ
て不純物の少い食塩水が得られるので加熱濃縮し
て食塩結晶を析出せしめこれを遠心分離して精製
食塩を得ることができる。本発明法においてはこ
の際、焼却炉の燃焼熱を使用することにより加熱
濃縮工程における新たな熱源を必要としない。
このようにして得られた精製塩の分析値は
NaCl 99.8%以上
Ca 0.001%以下
Mg 0.001%以下
SO4 0.03%以下
となり市販の精製塩に比較して劣るところなくま
た重金属類も検出されない。遠心分離の際の分離
母液は飽和食塩水であり、濃縮前の液に比し若干
不純物が濃縮されているので洗煙廃液と合せて精
製工程に戻すことにより食塩分の回収率を向上さ
せることができる。
以上のように本発明方法によれば
都市ゴミ焼却炉の排ガス洗滌液として苛性ソ
ーダ溶液の約2割を消石灰に置換することによ
り、排ガス中の硫酸根を除去するとともに高価
な苛性ソーダ全量を原料食塩分に再生して薬剤
費を節約し、
洗滌廃液(塩水)の精製は廃水処理法として
知られる塩化鉄―硫化ソーダ法を適用して不純
重金属類を除去し、要すればキレート樹脂によ
る厳密な精製を行うので析出食塩中に重金属類
は全く含まれない。
精製後塩水の濃縮には上記焼却炉の燃焼熱を
利用することにより別個に加熱用エネルギーを
必要としない。
等種々の効果を挙げることができる。従来このよ
うな高品質の精製食塩は海水よりイオン交換膜電
解およびスチームによる濃縮で精製食塩より純度
の劣る並塩を苦汁から分離した後、さらに水に溶
解し精製剤を加えて不純物を沈澱せしめ、濾過等
の手段によりこれを除去した後、再びスチームに
より濃縮し精製食塩の結晶を析出させる方法を採
用しているが、本発明法によれば排ガス中の塩化
水素および燃焼熱を利用して1回のみの濃縮析出
により同等の純度を有する精製食塩を製造するこ
とができるので重油、電解電力等の高価なエネル
ギーを全く必要とせず産業上利用価値が大であ
る。
以下の実施例、比較例において%はいずれも重
量基準である。
実施例
苛性ソーダ10%、消石灰1.7%の混合溶液210
を使用して都市ゴミ焼却炉排ガス(温度60℃、
HCl1100ppm、SO2100ppm)15000Nm3の洗滌を
行い生成した硫酸カルシウム2水塩を主体とする
沈澱を含む洗煙廃液を得た。その組成は次のごと
くである。
PH 6.5
比重 1.15
NaCl 15%
Na2SO4 0.6%
CaSO4 2H2O 2.5%
CaCO3 6000ppm
Mg 60ppm
Cd 1.1ppm
Cr 1.3ppm
Hg 5ppm
Pb 50ppm
Zn 350ppm
As 0.1ppm
この廃液をフイルタープレスにて濾過し主とし
て石コウ分を分離した後、濾液100に塩化第2
鉄50g、硫化ソーダ3gを加えて溶解し少量の苛性
ソーダ溶液を添加してPH10に調整した後、フイル
タープレスで濾過し、主として重金属を除去し、
さらにこの母液に炭酸ソーダ300gを加えて溶解
した後再びフイルタープレスで濾過する。この母
液をキレート樹脂充填塔に通液後上記都市ゴミ焼
却炉廃熱ボイラーからの蒸気(蒸気回収量110
Kg、蒸気使用量100Kg)を加熱源とする濃縮缶に
入れ115℃にて濃縮し水約75Kgを蒸発させ食塩の
スラリー25を得た。このスラリーを遠心分離し
て母液を分離した後、水1を加えて洗滌しさら
に遠心分離し食塩結晶10.5Kgを得た。これを乾燥
した後、分析すると次の結果が得られた。
NaCl 99.8%
Ca 0.005%
Mg 0.003%
SO4 0.028%
重金属類 検出されず
比較例
実施例と同じ都市ゴミ焼却炉排ガス15000Nm3
を苛性ソーダ12%溶液210で洗滌し次の組成液
を得た。
PH 5.8
比重 1.15
NaCl 15%
Na2SO4 3%
沈澱物 2000ppm
CaCO3 5000ppm
Mg 40ppm
Cd 1.1ppm
Cr 1.3ppm
Hg 5ppm
Pb 40ppm
Zn 360ppm
As 0.1ppm
この液100をフイルタープレスにて濾過後、
蒸気を加熱源とするドライヤーで濃縮固化せしめ
た。この結晶を粉砕乾燥後分析すると
NaCl 82.8%
Na2SO4 16.6%
Ca 250ppm
Mg 280ppm
重金属合量 2800ppm
上記のように不純物きわめて多く工業塩として
も全く使用に耐えない。[Table] In the method of the present invention, slaked lime is used in a weight ratio of 0.1 to 0.3, preferably 0.15 to 0.2, based on the pure caustic soda. If it is less than 0.1, the removal of sulfuric acid content in the exhaust gas is incomplete, and if it exceeds 0.3, calcium chloride is produced and salt is lost. The concentration of caustic soda solution is about 10-15% by weight, and nitrate lime is mixed and used. In this smoke washing process, it is possible to use chloride lime instead of slaked lime, but chloride lime is generally considerably more expensive than nitrate lime, has greater hygroscopicity, and is inconvenient to handle. For the reasons mentioned above, it is not appropriate to use lime chloride as a cleaning solution for exhaust gas from municipal waste incinerators, which generate a large amount of waste. This smoke washing waste liquid contains insoluble substances mainly composed of gypsum, so this is separated, iron chloride and sodium sulfide are added to the mother liquor, and if necessary, an alkali such as caustic soda is added to bring the pH to 10 to 10.5. When adjusted to , the impure heavy metals contained in the mother liquor precipitate as sulfides, which are separated by filtration using a filter press or the like.
Addition of iron chloride produces a floc-like iron hydroxide precipitate, which has the effect of co-precipitating fine heavy metal sulfide precipitates and making them easier to separate. Further, calcium ions remaining in the mother liquor are precipitated as calcium carbonate by adding sodium carbonate and separated by filtration using a filter press or the like. In addition, smoke washing waste fluid from municipal garbage incinerators often contains mercury, and in order to strictly purify this, the mother liquor must be finally removed by passing the mother liquor through a chelating resin or chelating agent-supported activated carbon. . In this way, a saline solution with very few impurities can be obtained, which can be heated and concentrated to precipitate salt crystals, which can then be centrifuged to obtain purified salt. At this time, in the method of the present invention, by using the combustion heat of the incinerator, no new heat source is required in the heating concentration step. The analytical value of the purified salt obtained in this way is 99.8% NaCl or more, Ca 0.001% or less, Mg 0.001% or less, SO 4 0.03% or less, which is not inferior to commercially available purified salt, and no heavy metals are detected. The mother liquor separated during centrifugation is a saturated saline solution, and the impurities are slightly more concentrated than the liquid before concentration, so the recovery rate of salt can be improved by returning it to the purification process along with the smoke washing waste liquid. I can do it. As described above, according to the method of the present invention, by replacing approximately 20% of the caustic soda solution with slaked lime as an exhaust gas cleaning solution for municipal waste incinerators, sulfuric acid radicals in the exhaust gas are removed, and the entire amount of expensive caustic soda is replaced with raw material salt. The washing waste liquid (salt water) is purified by applying the iron chloride-soda sulfide method, which is known as a wastewater treatment method, to remove impure heavy metals, and if necessary, rigorous purification using chelate resin is performed. Because this process is carried out, the precipitated salt does not contain any heavy metals. By utilizing the combustion heat of the incinerator, no separate heating energy is required for concentrating the purified brine. Various effects can be mentioned. Conventionally, such high-quality purified salt is produced by separating ordinary salt, which is less pure than purified salt, from bittern through ion-exchange membrane electrolysis and steam concentration from seawater, and then dissolving it in water and adding a purifying agent to precipitate impurities. However, the method of the present invention utilizes hydrogen chloride in the exhaust gas and the heat of combustion. Since refined common salt having the same purity can be produced by only one concentrated precipitation, expensive energy such as heavy oil or electrolytic power is not required at all, and it has great industrial utility value. In the following Examples and Comparative Examples, all percentages are based on weight. Example Mixed solution of 10% caustic soda and 1.7% slaked lime 210
Using municipal waste incinerator exhaust gas (temperature 60℃,
A smoke washing waste liquid containing precipitates mainly composed of calcium sulfate dihydrate was obtained by washing with 15,000 Nm 3 (HCl 1100 ppm, SO 2 100 ppm). Its composition is as follows. PH 6.5 Specific gravity 1.15 NaCl 15% Na 2 SO 4 0.6% CaSO 4 2H 2 O 2.5% CaCO 3 6000ppm Mg 60ppm Cd 1.1ppm Cr 1.3ppm Hg 5ppm Pb 50ppm Zn 350ppm As 0.1ppm This waste liquid is filtered with a filter press and mainly After separating the gypsum component, dichloride is added to the filtrate 100%.
Add 50g of iron and 3g of sodium sulfide to dissolve it, add a small amount of caustic soda solution to adjust the pH to 10, and then filter with a filter press to remove mainly heavy metals.
Furthermore, 300 g of soda carbonate is added to this mother liquor and dissolved, and then filtered again using a filter press. After passing this mother liquor through a chelate resin packed tower, steam from the above municipal waste incinerator waste heat boiler (steam recovery amount 110
100 kg) was placed in a concentrator using a heating source and concentrated at 115°C, and about 75 kg of water was evaporated to obtain a salt slurry 25. This slurry was centrifuged to separate the mother liquor, washed with 1 portion of water, and further centrifuged to obtain 10.5 kg of salt crystals. After drying this, it was analyzed and the following results were obtained. NaCl 99.8% Ca 0.005% Mg 0.003% SO 4 0.028% Heavy metals Not detected Comparative example Municipal garbage incinerator exhaust gas 15000Nm 3 same as Example
was washed with 12% caustic soda solution 210 to obtain a solution with the following composition. PH 5.8 Specific gravity 1.15 NaCl 15% Na 2 SO 4 3% Precipitate 2000ppm CaCO 3 5000ppm Mg 40ppm Cd 1.1ppm Cr 1.3ppm Hg 5ppm Pb 40ppm Zn 360ppm As 0.1ppm After filtering 100 of this liquid with a filter press,
It was concentrated and solidified using a dryer that uses steam as a heat source. Analysis of this crystal after crushing and drying revealed that it contained an extremely large amount of impurities, making it completely unsuitable for use as an industrial salt.
図面は本発明法を例示するフローシートであ
る。
The drawing is a flow sheet illustrating the method of the invention.
Claims (1)
するにあたり、苛性ソーダ溶液および消石灰の混
合液を使用し、かつ苛性ソーダ純分に対する消石
灰の重量比を0.1〜0.3とし、得られた洗煙廃液中
のカルシウム分および重金属分を主体とする不純
物を塩化鉄、硫化ソーダおよび炭酸ソーダを加え
ることにより除去した後、上記都市ゴミ焼却炉の
燃焼熱により加熱濃縮して食塩結晶を析出せしめ
ることを特徴とする精製食塩の製造法。1. When washing municipal waste incinerator exhaust gas containing hydrogen chloride, a mixed solution of caustic soda solution and slaked lime is used, and the weight ratio of slaked lime to the pure caustic soda content is 0.1 to 0.3, and the smoke washing waste liquid obtained is The method is characterized in that impurities mainly consisting of calcium and heavy metals are removed by adding iron chloride, sodium sulfide and soda carbonate, and then heated and concentrated using the combustion heat of the municipal waste incinerator to precipitate salt crystals. Manufacturing method of refined table salt.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP57228982A JPS59116123A (en) | 1982-12-23 | 1982-12-23 | Manufacture of purified salt |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP57228982A JPS59116123A (en) | 1982-12-23 | 1982-12-23 | Manufacture of purified salt |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS59116123A JPS59116123A (en) | 1984-07-04 |
JPS6144806B2 true JPS6144806B2 (en) | 1986-10-04 |
Family
ID=16884909
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP57228982A Granted JPS59116123A (en) | 1982-12-23 | 1982-12-23 | Manufacture of purified salt |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS59116123A (en) |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP4540170B2 (en) * | 1999-02-24 | 2010-09-08 | 邦明 ▲高▼松 | Process for producing ionized salt |
CN109970080A (en) * | 2019-04-02 | 2019-07-05 | 江苏杰林环保科技有限公司 | A kind of heavy metals removal method in chemical industry abraum salt |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5043056A (en) * | 1973-08-20 | 1975-04-18 | ||
JPS5240476A (en) * | 1975-09-26 | 1977-03-29 | Daido Kagaku Sochi Kk | Process and equipment for treating exhaust gas from waste incinerator |
JPS571423A (en) * | 1980-06-06 | 1982-01-06 | Chlorine Eng Corp Ltd | Treating method for waste gas containing hydrogen chloride and sulfur oxide |
-
1982
- 1982-12-23 JP JP57228982A patent/JPS59116123A/en active Granted
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5043056A (en) * | 1973-08-20 | 1975-04-18 | ||
JPS5240476A (en) * | 1975-09-26 | 1977-03-29 | Daido Kagaku Sochi Kk | Process and equipment for treating exhaust gas from waste incinerator |
JPS571423A (en) * | 1980-06-06 | 1982-01-06 | Chlorine Eng Corp Ltd | Treating method for waste gas containing hydrogen chloride and sulfur oxide |
Also Published As
Publication number | Publication date |
---|---|
JPS59116123A (en) | 1984-07-04 |
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