JPH0525559B2 - - Google Patents
Info
- Publication number
- JPH0525559B2 JPH0525559B2 JP24986589A JP24986589A JPH0525559B2 JP H0525559 B2 JPH0525559 B2 JP H0525559B2 JP 24986589 A JP24986589 A JP 24986589A JP 24986589 A JP24986589 A JP 24986589A JP H0525559 B2 JPH0525559 B2 JP H0525559B2
- Authority
- JP
- Japan
- Prior art keywords
- fluorine
- iron
- monocarboxylic acid
- present
- wastewater
- 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 - Lifetime
Links
- YCKRFDGAMUMZLT-UHFFFAOYSA-N Fluorine atom Chemical compound [F] YCKRFDGAMUMZLT-UHFFFAOYSA-N 0.000 claims description 36
- 239000011737 fluorine Substances 0.000 claims description 36
- 229910052731 fluorine Inorganic materials 0.000 claims description 36
- 239000007788 liquid Substances 0.000 claims description 23
- -1 monocarboxylic acid iron salt Chemical class 0.000 claims description 22
- 238000000034 method Methods 0.000 claims description 20
- 239000000920 calcium hydroxide Substances 0.000 claims description 8
- AXCZMVOFGPJBDE-UHFFFAOYSA-L calcium dihydroxide Chemical compound [OH-].[OH-].[Ca+2] AXCZMVOFGPJBDE-UHFFFAOYSA-L 0.000 claims description 7
- 230000007935 neutral effect Effects 0.000 claims description 7
- 229910001861 calcium hydroxide Inorganic materials 0.000 claims description 6
- 239000002244 precipitate Substances 0.000 claims description 5
- 239000007787 solid Substances 0.000 claims description 2
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 26
- 229910052742 iron Inorganic materials 0.000 description 13
- 239000007864 aqueous solution Substances 0.000 description 11
- 239000002351 wastewater Substances 0.000 description 11
- 150000003839 salts Chemical class 0.000 description 8
- 235000011116 calcium hydroxide Nutrition 0.000 description 7
- 238000001914 filtration Methods 0.000 description 7
- DHMQDGOQFOQNFH-UHFFFAOYSA-N Glycine Chemical compound NCC(O)=O DHMQDGOQFOQNFH-UHFFFAOYSA-N 0.000 description 6
- 150000002500 ions Chemical class 0.000 description 6
- 150000002762 monocarboxylic acid derivatives Chemical class 0.000 description 6
- 239000002253 acid Substances 0.000 description 5
- 230000000694 effects Effects 0.000 description 5
- RUTXIHLAWFEWGM-UHFFFAOYSA-H iron(3+) sulfate Chemical compound [Fe+3].[Fe+3].[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O RUTXIHLAWFEWGM-UHFFFAOYSA-H 0.000 description 5
- 229910000360 iron(III) sulfate Inorganic materials 0.000 description 5
- 238000002156 mixing Methods 0.000 description 5
- 238000000926 separation method Methods 0.000 description 5
- 238000003756 stirring Methods 0.000 description 5
- GOKIPOOTKLLKDI-UHFFFAOYSA-N acetic acid;iron Chemical compound [Fe].CC(O)=O.CC(O)=O.CC(O)=O GOKIPOOTKLLKDI-UHFFFAOYSA-N 0.000 description 4
- 229920002401 polyacrylamide Polymers 0.000 description 4
- 238000004062 sedimentation Methods 0.000 description 4
- 239000000243 solution Substances 0.000 description 4
- 239000000126 substance Substances 0.000 description 4
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 3
- 235000008733 Citrus aurantifolia Nutrition 0.000 description 3
- 239000004471 Glycine Substances 0.000 description 3
- 235000011941 Tilia x europaea Nutrition 0.000 description 3
- 239000003513 alkali Substances 0.000 description 3
- DIZPMCHEQGEION-UHFFFAOYSA-H aluminium sulfate (anhydrous) Chemical compound [Al+3].[Al+3].[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O DIZPMCHEQGEION-UHFFFAOYSA-H 0.000 description 3
- 150000001768 cations Chemical class 0.000 description 3
- 238000005345 coagulation Methods 0.000 description 3
- 230000015271 coagulation Effects 0.000 description 3
- 239000008394 flocculating agent Substances 0.000 description 3
- 239000004571 lime Substances 0.000 description 3
- 238000001179 sorption measurement Methods 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- 239000004475 Arginine Substances 0.000 description 2
- KRHYYFGTRYWZRS-UHFFFAOYSA-M Fluoride anion Chemical compound [F-] KRHYYFGTRYWZRS-UHFFFAOYSA-M 0.000 description 2
- QNAYBMKLOCPYGJ-REOHCLBHSA-N L-alanine Chemical compound C[C@H](N)C(O)=O QNAYBMKLOCPYGJ-REOHCLBHSA-N 0.000 description 2
- ROHFNLRQFUQHCH-YFKPBYRVSA-N L-leucine Chemical compound CC(C)C[C@H](N)C(O)=O ROHFNLRQFUQHCH-YFKPBYRVSA-N 0.000 description 2
- KZSNJWFQEVHDMF-BYPYZUCNSA-N L-valine Chemical compound CC(C)[C@H](N)C(O)=O KZSNJWFQEVHDMF-BYPYZUCNSA-N 0.000 description 2
- ROHFNLRQFUQHCH-UHFFFAOYSA-N Leucine Natural products CC(C)CC(N)C(O)=O ROHFNLRQFUQHCH-UHFFFAOYSA-N 0.000 description 2
- KDXKERNSBIXSRK-UHFFFAOYSA-N Lysine Natural products NCCCCC(N)C(O)=O KDXKERNSBIXSRK-UHFFFAOYSA-N 0.000 description 2
- 239000004472 Lysine Substances 0.000 description 2
- MTCFGRXMJLQNBG-UHFFFAOYSA-N Serine Natural products OCC(N)C(O)=O MTCFGRXMJLQNBG-UHFFFAOYSA-N 0.000 description 2
- AYFVYJQAPQTCCC-UHFFFAOYSA-N Threonine Natural products CC(O)C(N)C(O)=O AYFVYJQAPQTCCC-UHFFFAOYSA-N 0.000 description 2
- 239000004473 Threonine Substances 0.000 description 2
- KZSNJWFQEVHDMF-UHFFFAOYSA-N Valine Natural products CC(C)C(N)C(O)=O KZSNJWFQEVHDMF-UHFFFAOYSA-N 0.000 description 2
- 235000004279 alanine Nutrition 0.000 description 2
- 229940024606 amino acid Drugs 0.000 description 2
- 235000001014 amino acid Nutrition 0.000 description 2
- 150000001413 amino acids Chemical class 0.000 description 2
- 125000003277 amino group Chemical group 0.000 description 2
- 150000001450 anions Chemical class 0.000 description 2
- ODKSFYDXXFIFQN-UHFFFAOYSA-N arginine Natural products OC(=O)C(N)CCCNC(N)=N ODKSFYDXXFIFQN-UHFFFAOYSA-N 0.000 description 2
- 238000005352 clarification Methods 0.000 description 2
- 230000000052 comparative effect Effects 0.000 description 2
- 239000013078 crystal Substances 0.000 description 2
- XBDQKXXYIPTUBI-UHFFFAOYSA-N dimethylselenoniopropionate Natural products CCC(O)=O XBDQKXXYIPTUBI-UHFFFAOYSA-N 0.000 description 2
- 238000005188 flotation Methods 0.000 description 2
- 239000012530 fluid Substances 0.000 description 2
- 230000005484 gravity Effects 0.000 description 2
- 235000014413 iron hydroxide Nutrition 0.000 description 2
- 159000000014 iron salts Chemical class 0.000 description 2
- PQQAOTNUALRVTE-UHFFFAOYSA-L iron(2+);diformate Chemical compound [Fe+2].[O-]C=O.[O-]C=O PQQAOTNUALRVTE-UHFFFAOYSA-L 0.000 description 2
- NCNCGGDMXMBVIA-UHFFFAOYSA-L iron(ii) hydroxide Chemical compound [OH-].[OH-].[Fe+2] NCNCGGDMXMBVIA-UHFFFAOYSA-L 0.000 description 2
- 229910052751 metal Inorganic materials 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- BDAGIHXWWSANSR-UHFFFAOYSA-N methanoic acid Natural products OC=O BDAGIHXWWSANSR-UHFFFAOYSA-N 0.000 description 2
- 230000001590 oxidative effect Effects 0.000 description 2
- 229920000642 polymer Polymers 0.000 description 2
- 238000001556 precipitation Methods 0.000 description 2
- 239000004474 valine Substances 0.000 description 2
- MTCFGRXMJLQNBG-REOHCLBHSA-N (2S)-2-Amino-3-hydroxypropansäure Chemical compound OC[C@H](N)C(O)=O MTCFGRXMJLQNBG-REOHCLBHSA-N 0.000 description 1
- OSWFIVFLDKOXQC-UHFFFAOYSA-N 4-(3-methoxyphenyl)aniline Chemical compound COC1=CC=CC(C=2C=CC(N)=CC=2)=C1 OSWFIVFLDKOXQC-UHFFFAOYSA-N 0.000 description 1
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 1
- UXVMQQNJUSDDNG-UHFFFAOYSA-L Calcium chloride Chemical compound [Cl-].[Cl-].[Ca+2] UXVMQQNJUSDDNG-UHFFFAOYSA-L 0.000 description 1
- BVKZGUZCCUSVTD-UHFFFAOYSA-L Carbonate Chemical compound [O-]C([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-L 0.000 description 1
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 1
- UQSXHKLRYXJYBZ-UHFFFAOYSA-N Iron oxide Chemical class [Fe]=O UQSXHKLRYXJYBZ-UHFFFAOYSA-N 0.000 description 1
- 229910021578 Iron(III) chloride Inorganic materials 0.000 description 1
- ODKSFYDXXFIFQN-BYPYZUCNSA-P L-argininium(2+) Chemical compound NC(=[NH2+])NCCC[C@H]([NH3+])C(O)=O ODKSFYDXXFIFQN-BYPYZUCNSA-P 0.000 description 1
- AGPKZVBTJJNPAG-WHFBIAKZSA-N L-isoleucine Chemical compound CC[C@H](C)[C@H](N)C(O)=O AGPKZVBTJJNPAG-WHFBIAKZSA-N 0.000 description 1
- KDXKERNSBIXSRK-YFKPBYRVSA-N L-lysine Chemical compound NCCCC[C@H](N)C(O)=O KDXKERNSBIXSRK-YFKPBYRVSA-N 0.000 description 1
- AYFVYJQAPQTCCC-GBXIJSLDSA-N L-threonine Chemical compound C[C@@H](O)[C@H](N)C(O)=O AYFVYJQAPQTCCC-GBXIJSLDSA-N 0.000 description 1
- 229910002651 NO3 Inorganic materials 0.000 description 1
- NHNBFGGVMKEFGY-UHFFFAOYSA-N Nitrate Chemical compound [O-][N+]([O-])=O NHNBFGGVMKEFGY-UHFFFAOYSA-N 0.000 description 1
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 1
- 238000003723 Smelting Methods 0.000 description 1
- QAOWNCQODCNURD-UHFFFAOYSA-L Sulfate Chemical compound [O-]S([O-])(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-L 0.000 description 1
- MGQIWUQTCOJGJU-UHFFFAOYSA-N [AlH3].Cl Chemical compound [AlH3].Cl MGQIWUQTCOJGJU-UHFFFAOYSA-N 0.000 description 1
- 235000011054 acetic acid Nutrition 0.000 description 1
- AZDRQVAHHNSJOQ-UHFFFAOYSA-N alumane Chemical class [AlH3] AZDRQVAHHNSJOQ-UHFFFAOYSA-N 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 1
- 125000000129 anionic group Chemical group 0.000 description 1
- 210000000988 bone and bone Anatomy 0.000 description 1
- 229910052791 calcium Inorganic materials 0.000 description 1
- 239000011575 calcium Substances 0.000 description 1
- 239000001110 calcium chloride Substances 0.000 description 1
- 229910001628 calcium chloride Inorganic materials 0.000 description 1
- WUKWITHWXAAZEY-UHFFFAOYSA-L calcium difluoride Chemical compound [F-].[F-].[Ca+2] WUKWITHWXAAZEY-UHFFFAOYSA-L 0.000 description 1
- 229910001634 calcium fluoride Inorganic materials 0.000 description 1
- 125000002843 carboxylic acid group Chemical group 0.000 description 1
- 150000001735 carboxylic acids Chemical class 0.000 description 1
- 229920006317 cationic polymer Polymers 0.000 description 1
- 239000000919 ceramic Substances 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 230000018044 dehydration Effects 0.000 description 1
- 238000006297 dehydration reaction Methods 0.000 description 1
- 235000014113 dietary fatty acids Nutrition 0.000 description 1
- 229930195729 fatty acid Natural products 0.000 description 1
- 239000000194 fatty acid Substances 0.000 description 1
- 150000004665 fatty acids Chemical class 0.000 description 1
- 239000011790 ferrous sulphate Substances 0.000 description 1
- 235000003891 ferrous sulphate Nutrition 0.000 description 1
- 239000000706 filtrate Substances 0.000 description 1
- 235000019253 formic acid Nutrition 0.000 description 1
- 239000010842 industrial wastewater Substances 0.000 description 1
- 238000005342 ion exchange Methods 0.000 description 1
- RBTARNINKXHZNM-UHFFFAOYSA-K iron trichloride Chemical compound Cl[Fe](Cl)Cl RBTARNINKXHZNM-UHFFFAOYSA-K 0.000 description 1
- BAUYGSIQEAFULO-UHFFFAOYSA-L iron(2+) sulfate (anhydrous) Chemical compound [Fe+2].[O-]S([O-])(=O)=O BAUYGSIQEAFULO-UHFFFAOYSA-L 0.000 description 1
- PKBRCANVDCVQJP-UHFFFAOYSA-L iron(2+);propanoate Chemical compound [Fe+2].CCC([O-])=O.CCC([O-])=O PKBRCANVDCVQJP-UHFFFAOYSA-L 0.000 description 1
- 229910000359 iron(II) sulfate Inorganic materials 0.000 description 1
- SHXXPRJOPFJRHA-UHFFFAOYSA-K iron(iii) fluoride Chemical compound F[Fe](F)F SHXXPRJOPFJRHA-UHFFFAOYSA-K 0.000 description 1
- 229960000310 isoleucine Drugs 0.000 description 1
- AGPKZVBTJJNPAG-UHFFFAOYSA-N isoleucine Natural products CCC(C)C(N)C(O)=O AGPKZVBTJJNPAG-UHFFFAOYSA-N 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 150000002763 monocarboxylic acids Chemical class 0.000 description 1
- 239000008239 natural water Substances 0.000 description 1
- 238000006386 neutralization reaction Methods 0.000 description 1
- 230000003472 neutralizing effect Effects 0.000 description 1
- 230000003287 optical effect Effects 0.000 description 1
- 239000011574 phosphorus Substances 0.000 description 1
- 229910052698 phosphorus Inorganic materials 0.000 description 1
- 238000011085 pressure filtration Methods 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 235000019260 propionic acid Nutrition 0.000 description 1
- IUVKMZGDUIUOCP-BTNSXGMBSA-N quinbolone Chemical compound O([C@H]1CC[C@H]2[C@H]3[C@@H]([C@]4(C=CC(=O)C=C4CC3)C)CC[C@@]21C)C1=CCCC1 IUVKMZGDUIUOCP-BTNSXGMBSA-N 0.000 description 1
- 239000006228 supernatant Substances 0.000 description 1
- 239000008399 tap water Substances 0.000 description 1
- 235000020679 tap water Nutrition 0.000 description 1
- 238000010998 test method Methods 0.000 description 1
- 238000003828 vacuum filtration Methods 0.000 description 1
- 235000014393 valine Nutrition 0.000 description 1
Landscapes
- Separation Of Suspended Particles By Flocculating Agents (AREA)
- Removal Of Specific Substances (AREA)
Description
[産業上の利用分野]
フツ素は天然水に含有されており、日本の水道
水水質基準ではフツ素濃度は0.8mg/以下とさ
れている。
産業で、フツ素を含有する水性液に光学材料の
加工液および廃水、電子工業における加工液およ
び廃水、金属精錬業・金属製品製造業の加工液お
よび廃水、アルミニウム工業における加工液およ
び廃水、リン酸工業における加工液および廃水、
窯業における加工液および廃水その他がある。
本発明は、フツ素含有水性液のフツ素の除去法
に係り、例えば、工程液や産業廃水等の水性液が
含有するフツ素の除去(分離・濃縮)に利用され
る。
[従来の技術]
フツ素除去法としては、石灰法、硫酸アルミニ
ウムによる凝集沈殿法・清澄ろ過法、活性アルミ
ナゲルによるイオン交換法、骨炭による吸着法な
どが知られている。
[発明が解決しようとする課題]
凝集沈殿によるフツ素含有水性液よりフツ素の
除去法として、従来、大量の石灰を使用し、PHを
10以上としフツ化カルシウムとして沈殿・凝集沈
殿・清澄ろ過する方法、大量の石灰を使用し、PH
10以上で沈殿させた後、硫酸アルミニウムや硫酸
第二鉄を加え中性ないし弱アルカリ性で凝集沈
殿・清澄ろ過する方法等が応用されているが、そ
れらの凝集分離法ではフツ素濃度を約10mg/以
下にすることは困難である。
本発明は、フツ素含有水性液に対し、モノカル
ボン酸鉄塩および水酸化カルシウムの新たな組み
合わせを用い、凝集沈殿、浮上、清澄ろ過、脱水
ろ過等の固液分離法で、安い費用でフツ素濃度を
できるだけ小さく、約10mg/以下にしようとす
るものである。
[課題を解決するための手段]
本発明は、フツ素含有水性液に、フツ素1モル
に対し0.1モル以上のモノカルボン酸鉄塩を加え、
水酸化カルシウムを加えてPHを中性附近ないしア
ルカリ性とし、生成した沈殿・フロツクを固液分
離することを特徴とするフツ素含有水性液よりフ
ツ素の除去法である。
本発明に係るモノカルボン酸鉄塩とは、モノカ
ルボン酸と鉄イオン例えば鉄()イオンとの塩
で、モノカルボン酸としては、ギ酸、酢酸、プロ
ピオン酸等の脂肪酸、グリシン、アラニン、バリ
ン、ロイシン、イソロイシン、セリン、スレオニ
ン、リジン、アルギニン等のアミノ酸が用いられ
る。
すなわち、モノカルボン酸鉄塩としては、ギ酸
鉄塩、酢酸鉄塩、プロピオン酸鉄塩、グリシン鉄
塩、アラニン鉄塩、バリン鉄塩、ロイシン鉄塩、
イソロイシン鉄塩、セリン鉄塩、スレオニン鉄
塩、リジン鉄塩、アルギニン鉄塩その他のモノカ
ルボン酸鉄塩を、一般に水溶液として用いる。
本発明に係るモノカルボン酸鉄塩は、鉄の水酸
化物・酸化物とモノカルボン酸、モノカルボン酸
アルカリ、またはそれらの水溶液を混合する方
法、混合前または混合した後、PHを調節する方
法、酸化する方法、鉄塩(塩酸塩、硫酸塩、硝酸
塩、炭酸塩等)の水溶液にモノカルボン酸、モノ
カルボン酸アルカリ、またはそれらの水溶液を混
合する方法、混合前または混合した後、PHを調節
する方法、酸化する方法等により結晶または溶液
としてえられる。
本発明に係るモノカルボン酸鉄塩は多価陽イオ
ンの鉄イオン(Fe2+、Fe3+)がモノカルボン酸
と当量的に中和する場合と部分的に中和する場合
があり、部分的に中和する場合は残存する陽イオ
ンの電荷はモノカルボン酸以外の陰イオンと塩・
錯イオンをつくり、対イオンを有する。
本発明に係るモノカルボン酸鉄塩は当量的に中
和した塩でもよく、部分的に中和した塩でもよ
い。
本発明は、次の要領で実施される。
フツ素含有水性液に、モノカルボン酸鉄塩の水
溶液の適量を加えて攪拌し、次いで石灰乳を加え
て攪拌し、PHを中性附近ないしアルカリ性とす
る。PHは一般に8〜10付近が好ましい。なお、そ
の際必要に応じて無機凝集剤、有機凝集剤をさら
に添加し急速攪拌および緩速攪拌し、沈殿・フロ
ツクを生成させたのち固液分離する。また、薬液
の添加・混合法は、フツ素含有水性液にモノカル
ボン酸鉄塩の水溶液と石灰乳を同時に加えて攪拌
しPHを中性附近ないしアルカリ性としてもよい。
モノカルボン酸鉄塩の添加量はフツ素1モルに
対して0.1モル以上で、約0.3モル以上が効果的で
ある。モノカルボン酸鉄塩の添加量が0.1モル未
満では十分な沈殿・フロツクを生成させることが
難しく好ましくない。
固液分利法としては、重力または遠心力の場に
おける沈降や浮上、重力ろ過、減圧ろ過、加圧ろ
過、およびプレスフイルター等を応用する。
モノカルボン酸鉄塩はアルカリ、酸、モノカル
ボン酸アルミニウム塩、無機凝集剤、有機凝集剤
などと併用することができる。
無機凝集剤として、硫酸第二鉄、硫酸第一鉄、
塩化第二鉄、ポリ鉄その他の鉄塩、硫酸アルミニ
ウム、塩酸アルニウム、PACなどのアルムニウ
ム塩その他が、有機凝集剤として、ポリアクリル
アミド、弱陰イオン変性ポリアクリルアミドその
他の高分子凝集剤が、一般に水溶液として用いら
れる。
本発明に係るモノカルボン酸鉄塩は非イオン
性・陽イオン性の高分子凝集剤、無機塩、モノカ
ルボン酸アルミニウム塩、非イオン性有機物を混
合することができ、それらの結晶または水溶液を
混合して使用することができる。
カルボン酸は非局在化π電子を有する大きな、
弱い酸である。モノカルボン酸鉄塩、水酸化カル
シウムと作用して生成するモノカルボン酸カルシ
ウムは水への溶解性が大で、水中で一部は解離し
水和イオン、錯イオンを生成し、フツ化物イオン
と作用し、他の方法にくらべ少ない使用量で、か
つ低いPH(中性附近ないしアルカリ性)で安定な
難溶性塩を生成し、また生成したフツ化鉄や水酸
化鉄その他の吸着活性が寄与するものと考えられ
る。なお、アミノ酸はカルボン酸基とアミノ基を
有し、アミノ基はフツ素除去に有効に作用すると
考えられる。
実施例 1
フツ素含有工場廃水(フツ素濃度:800〜950
mg/)について、その水性液500mlを、容量500
mlのビーカーに採り、ジヤーテスターを使用して
150rpmで攪拌し、まず酢酸鉄()を1.0mol/
F−mol添加し、5分間攪拌を行う、次に水酸化
カルシウム溶液を加えてPHを10.5とし150rpmで
10分間、100rpmで10分間、30rpmで15分間攪拌
を行つた後、30分静置し沈殿させた後、上澄み液
をろ過し、ろ液のフツ素濃度を測定したところ処
理水のフツ素濃度は9.80mg/であつた。なお、
フツ素濃度の測定は、「JIS、K−0102工場廃水試
験方法(34)−2イオン電極法」により測定した。
本発明によれば、高濃度フツ素含有廃水の処理
に応用して、処理水のフツ素濃度を約10mg/以
下にすることができた。
実施例 2
実施例1と同様の方法により、本発明に係る酢
酸鉄と、硫酸第二鉄を併用したところ表1の結果
をえた。
[Industrial Application Fields] Fluorine is contained in natural water, and the Japanese tap water quality standards set the fluorine concentration at 0.8 mg/or less. In industry, fluorine-containing aqueous liquids include processing liquids and wastewater for optical materials, processing liquids and wastewater in the electronics industry, processing liquids and wastewater in the metal smelting industry and metal product manufacturing industry, processing liquids and wastewater in the aluminum industry, and phosphorus. processing fluids and wastewater in the acid industry;
Processing fluids and wastewater from the ceramic industry, etc. The present invention relates to a method for removing fluorine from a fluorine-containing aqueous liquid, and is used, for example, to remove (separate and concentrate) fluorine contained in aqueous liquids such as process liquids and industrial wastewater. [Prior Art] Known methods for removing fluorine include a lime method, a coagulation sedimentation method/clarification filtration method using aluminum sulfate, an ion exchange method using activated alumina gel, and an adsorption method using bone char. [Problem to be solved by the invention] Conventionally, as a method for removing fluorine from a fluorine-containing aqueous liquid by coagulation and precipitation, a large amount of lime was used to lower the pH.
Calcium fluoride is precipitated, flocculated, and clarified through filtration, using a large amount of lime, and the PH
After precipitation at a temperature of 10 or higher, aluminum sulfate or ferric sulfate is added to coagulate and precipitate in neutral or weakly alkaline conditions, followed by clarification filtration. It is difficult to reduce the value to less than /. The present invention uses a new combination of iron monocarboxylate and calcium hydroxide to treat fluorine-containing aqueous liquids at low cost by solid-liquid separation methods such as coagulation sedimentation, flotation, clarifying filtration, and dehydration filtration. The aim is to keep the elementary concentration as low as possible, to about 10mg/or less. [Means for Solving the Problems] The present invention includes adding 0.1 mol or more of a monocarboxylic acid iron salt per 1 mol of fluorine to a fluorine-containing aqueous liquid,
This is a method for removing fluorine from a fluorine-containing aqueous solution, which is characterized by adding calcium hydroxide to make the pH near neutral or alkaline, and separating the formed precipitate and floc from solid and liquid. The monocarboxylic acid iron salt according to the present invention is a salt of a monocarboxylic acid and an iron ion, such as an iron () ion, and examples of the monocarboxylic acid include fatty acids such as formic acid, acetic acid, and propionic acid, glycine, alanine, valine, Amino acids such as leucine, isoleucine, serine, threonine, lysine, and arginine are used. That is, the monocarboxylic acid iron salts include iron formate, iron acetate, iron propionate, iron glycine, iron alanine, iron valine, iron leucine,
Isoleucine iron salts, serine iron salts, threonine iron salts, lysine iron salts, arginine iron salts and other monocarboxylic acid iron salts are generally used as aqueous solutions. The iron monocarboxylate salt according to the present invention can be produced by mixing iron hydroxide/oxide with monocarboxylic acid, alkali monocarboxylate, or an aqueous solution thereof, or by adjusting the PH before or after mixing. , a method of oxidizing, a method of mixing a monocarboxylic acid, an alkali monocarboxylic acid, or an aqueous solution thereof with an aqueous solution of iron salts (hydrochloride, sulfate, nitrate, carbonate, etc.), and adjusting the pH before or after mixing. It can be obtained as crystals or solutions by adjusting methods, oxidizing methods, etc. In the monocarboxylic acid iron salt according to the present invention, iron ions (Fe 2+ , Fe 3+ ), which are polyvalent cations, may neutralize the monocarboxylic acid equivalently or partially; When neutralizing the remaining cations, the charge of the remaining cations is reduced by anions other than monocarboxylic acids and salts.
Creates a complex ion and has a counter ion. The monocarboxylic acid iron salt according to the present invention may be an equivalently neutralized salt or a partially neutralized salt. The present invention is carried out as follows. An appropriate amount of an aqueous solution of iron monocarboxylate is added to the fluorine-containing aqueous solution and stirred, and then milk of lime is added and stirred to adjust the pH to near neutral or alkaline. Generally, pH is preferably around 8 to 10. At this time, an inorganic flocculant or an organic flocculant is further added as required, and rapid stirring or slow stirring is performed to form a precipitate or floc, followed by solid-liquid separation. Further, as for the method of adding and mixing the chemical solution, an aqueous solution of an iron monocarboxylate salt and milk of lime may be simultaneously added to a fluorine-containing aqueous solution and stirred to adjust the pH to near neutral or alkaline. The amount of monocarboxylic acid iron salt to be added is 0.1 mol or more per 1 mol of fluorine, and approximately 0.3 mol or more is effective. If the amount of the monocarboxylic acid iron salt added is less than 0.1 mol, it is difficult to generate sufficient precipitates and flocs, which is not preferable. As the solid-liquid separation method, sedimentation or flotation in a field of gravity or centrifugal force, gravity filtration, vacuum filtration, pressure filtration, press filter, etc. are applied. The monocarboxylic acid iron salt can be used in combination with an alkali, an acid, a monocarboxylic acid aluminum salt, an inorganic flocculant, an organic flocculant, and the like. As an inorganic flocculant, ferric sulfate, ferrous sulfate,
Aluminum salts such as ferric chloride, polyiron and other iron salts, aluminum sulfate, aluminum hydrochloride, PAC, etc. are used as organic flocculants, polyacrylamide, weakly anion modified polyacrylamide and other polymer flocculants are generally used in aqueous solutions. used as. The monocarboxylic acid iron salt according to the present invention can be mixed with nonionic/cationic polymer flocculants, inorganic salts, monocarboxylic acid aluminum salts, and nonionic organic substances, and their crystals or aqueous solutions can be mixed. and can be used. Carboxylic acids are large, with delocalized π electrons.
It is a weak acid. Calcium monocarboxylate, which is produced by interacting with iron monocarboxylate and calcium hydroxide, has a high solubility in water, and a portion of it dissociates in water to form hydrated ions and complex ions, and forms fluoride ions. This method produces stable, poorly soluble salts at low pH (nearly neutral or alkaline) with a smaller amount used than other methods, and the adsorption activity of iron fluoride, iron hydroxide, and other substances produced contributes. considered to be a thing. Note that amino acids have a carboxylic acid group and an amino group, and the amino group is thought to effectively act on fluorine removal. Example 1 Fluorine-containing factory wastewater (Fluorine concentration: 800-950
mg/), add 500 ml of the aqueous liquid to a volume of 500
mL beaker and use a jar tester.
Stir at 150 rpm, and first add 1.0 mol of iron acetate ()/
Add F-mol and stir for 5 minutes, then add calcium hydroxide solution to adjust the pH to 10.5 at 150 rpm.
After stirring for 10 minutes, 10 minutes at 100 rpm, and 15 minutes at 30 rpm, the supernatant liquid was filtered after being allowed to settle for 30 minutes, and the fluorine concentration of the filtrate was measured. was 9.80mg/. In addition,
The fluorine concentration was measured by "JIS, K-0102 Factory wastewater test method (34)-2 ion electrode method". According to the present invention, when applied to the treatment of wastewater containing high concentration of fluorine, it was possible to reduce the fluorine concentration of the treated water to about 10 mg/or less. Example 2 In the same manner as in Example 1, the iron acetate according to the present invention and ferric sulfate were used in combination, and the results shown in Table 1 were obtained.
【表】
本発明に係る酢酸鉄と硫酸第二鉄との併用によ
り顕著なフツ素除去効果がえられた
実施例 3
フツ素含有水性液(フツ素濃度:115mg/)
に、本発明にかかるギ酸鉄()溶液(濃度
6.2wt%)を加え、実施例1と同様の方法により
処理したところ表2の結果が得られた。[Table] Example 3 in which a remarkable fluorine removal effect was obtained by the combined use of iron acetate and ferric sulfate according to the present invention 3 Fluorine-containing aqueous liquid (fluorine concentration: 115 mg/)
The iron formate () solution (concentration) according to the present invention is
6.2wt%) was added and treated in the same manner as in Example 1, the results shown in Table 2 were obtained.
【表】
実施例 4
フツ素含有水性液(フツ素濃度:115mg/)
に、本発明にかかるグリシン鉄()溶液(濃度
8.0wt%)を加え、実施例1と同様の方法により
処理したところ表3の結果がえられた。[Table] Example 4 Fluorine-containing aqueous liquid (Fluorine concentration: 115 mg/)
The iron glycine () solution (concentration) according to the present invention is
8.0wt%) was added and treated in the same manner as in Example 1, the results shown in Table 3 were obtained.
【表】
比較例
なお、比較例(本発明以外)として、塩化カル
シウムと硫酸第二鉄を添加し、消石灰PH調整を行
つた場合のフツ素含有廃水の処理結果を表4−1
に、ポリ鉄またはPACを添加し、消石灰でPH調
整を行つた場合のフツ素含有廃水の処理結果を表
4−2に示す。
ポリ鉄、PACは、安定な錯体を生成していて、
吸着活性ではあるが化学反応によるフツ素除去の
性質は良くなく、それらを使用する方法では本発
明のような効果はえられない。[Table] Comparative Example As a comparative example (other than the present invention), Table 4-1 shows the treatment results of fluorine-containing wastewater when calcium chloride and ferric sulfate were added and slaked lime pH was adjusted.
Table 4-2 shows the treatment results for fluorine-containing wastewater when polyiron or PAC was added to the fluoride and PH was adjusted with slaked lime. Polyiron, PAC forms a stable complex,
Although they have adsorption activity, their ability to remove fluorine through chemical reactions is not good, and methods using them cannot achieve the effects of the present invention.
【表】【table】
【表】
[発明の効果]
本発明の方法によれば、実施例からもわかるよ
うに、著しく少ない薬剤添加量で、かつ従来の方
法にくらべ低いPH(中性附近ないしアルカリ性)
で残留フツ素を約10mg/以下または約5mg/
程度にすることが可能で、排水のための酸による
中和は不要または少量の酸の添加ですみ、なお、
固液分離に高分子凝集剤のポリアクリルアミドま
たは弱陰イオン性ポリアクリルアミド等を使用す
れば凝集沈澱、清澄ろ過等の分離速度をより大に
することができ、フツ素除去技術としての本発明
の工業価値は大きい。[Table] [Effects of the invention] According to the method of the present invention, as can be seen from the examples, the amount of added chemicals is significantly smaller, and the pH is lower than that of the conventional method (nearly neutral to alkaline).
to reduce residual fluoride to about 10mg/or less or about 5mg/
Neutralization with acid for drainage is unnecessary or only a small amount of acid needs to be added.
If a polymer flocculant such as polyacrylamide or weakly anionic polyacrylamide is used for solid-liquid separation, the separation speed of coagulation-sedimentation, clarifying filtration, etc. can be increased, and the present invention as a fluorine removal technology The industrial value is great.
Claims (1)
0.1モル以上のモノカルボン酸鉄塩を加え、水酸
化カルシウムを加えてPHを中性附近ないしアルカ
リ性とし、生成した沈殿・フロツクを固液分離す
ることを特徴とするフツ素含有水性液のフツ素の
除去法。1 per mole of fluorine in a fluorine-containing aqueous liquid
A fluorine-containing aqueous liquid characterized by adding 0.1 mole or more of a monocarboxylic acid iron salt, adding calcium hydroxide to make the pH near neutral or alkaline, and separating the formed precipitate and floc from solid and liquid. removal method.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP24986589A JPH03109993A (en) | 1989-09-26 | 1989-09-26 | Method for removing fluorine from aqueous solution containing fluorine |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP24986589A JPH03109993A (en) | 1989-09-26 | 1989-09-26 | Method for removing fluorine from aqueous solution containing fluorine |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH03109993A JPH03109993A (en) | 1991-05-09 |
| JPH0525559B2 true JPH0525559B2 (en) | 1993-04-13 |
Family
ID=17199343
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP24986589A Granted JPH03109993A (en) | 1989-09-26 | 1989-09-26 | Method for removing fluorine from aqueous solution containing fluorine |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH03109993A (en) |
Families Citing this family (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP4602064B2 (en) * | 2004-12-16 | 2010-12-22 | オルガノ株式会社 | Method for treating fluorine / phosphorus-containing water containing chelating agent |
| JP4726216B2 (en) * | 2005-11-02 | 2011-07-20 | オルガノ株式会社 | Fluorine / phosphorus treatment method and apparatus for water containing chelating agent |
| JP2008018745A (en) * | 2006-07-10 | 2008-01-31 | Mitsui Eng & Shipbuild Co Ltd | Underwater cleaning robot |
| CN103508523A (en) * | 2012-06-19 | 2014-01-15 | 四川环能德美科技股份有限公司 | Water treatment composite flocculating agent and application thereof |
-
1989
- 1989-09-26 JP JP24986589A patent/JPH03109993A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPH03109993A (en) | 1991-05-09 |
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