CA1055420A - Photooxidative destruction of organic wastes - Google Patents
Photooxidative destruction of organic wastesInfo
- Publication number
- CA1055420A CA1055420A CA243,846A CA243846A CA1055420A CA 1055420 A CA1055420 A CA 1055420A CA 243846 A CA243846 A CA 243846A CA 1055420 A CA1055420 A CA 1055420A
- Authority
- CA
- Canada
- Prior art keywords
- alginate
- dye
- beads
- particles
- 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
- 239000010815 organic waste Substances 0.000 title claims abstract description 21
- 230000006378 damage Effects 0.000 title claims abstract description 10
- 235000010443 alginic acid Nutrition 0.000 claims abstract description 71
- 229920000615 alginic acid Polymers 0.000 claims abstract description 71
- 229940072056 alginate Drugs 0.000 claims abstract description 69
- FHVDTGUDJYJELY-UHFFFAOYSA-N 6-{[2-carboxy-4,5-dihydroxy-6-(phosphanyloxy)oxan-3-yl]oxy}-4,5-dihydroxy-3-phosphanyloxane-2-carboxylic acid Chemical compound O1C(C(O)=O)C(P)C(O)C(O)C1OC1C(C(O)=O)OC(OP)C(O)C1O FHVDTGUDJYJELY-UHFFFAOYSA-N 0.000 claims abstract description 68
- 239000002245 particle Substances 0.000 claims abstract description 52
- 238000000034 method Methods 0.000 claims abstract description 25
- 150000002989 phenols Chemical class 0.000 claims abstract description 24
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims abstract description 16
- 229910052751 metal Inorganic materials 0.000 claims abstract description 15
- 239000002184 metal Substances 0.000 claims abstract description 15
- 229910052760 oxygen Inorganic materials 0.000 claims abstract description 15
- 239000001301 oxygen Substances 0.000 claims abstract description 15
- 238000007539 photo-oxidation reaction Methods 0.000 claims abstract description 14
- 239000000975 dye Substances 0.000 claims description 78
- 239000011324 bead Substances 0.000 claims description 43
- 238000007254 oxidation reaction Methods 0.000 claims description 30
- 230000003647 oxidation Effects 0.000 claims description 29
- DSAJWYNOEDNPEQ-UHFFFAOYSA-N barium atom Chemical compound [Ba] DSAJWYNOEDNPEQ-UHFFFAOYSA-N 0.000 claims description 13
- 229910052788 barium Inorganic materials 0.000 claims description 12
- 239000000463 material Substances 0.000 claims description 10
- 235000010413 sodium alginate Nutrition 0.000 claims description 10
- 239000000661 sodium alginate Substances 0.000 claims description 10
- IXPNQXFRVYWDDI-UHFFFAOYSA-N 1-methyl-2,4-dioxo-1,3-diazinane-5-carboximidamide Chemical compound CN1CC(C(N)=N)C(=O)NC1=O IXPNQXFRVYWDDI-UHFFFAOYSA-N 0.000 claims description 9
- 229940005550 sodium alginate Drugs 0.000 claims description 9
- DZBUGLKDJFMEHC-UHFFFAOYSA-N acridine Chemical compound C1=CC=CC2=CC3=CC=CC=C3N=C21 DZBUGLKDJFMEHC-UHFFFAOYSA-N 0.000 claims description 8
- 239000000945 filler Substances 0.000 claims description 8
- ZLNQQNXFFQJAID-UHFFFAOYSA-L magnesium carbonate Chemical compound [Mg+2].[O-]C([O-])=O ZLNQQNXFFQJAID-UHFFFAOYSA-L 0.000 claims description 7
- 239000001095 magnesium carbonate Substances 0.000 claims description 7
- 229910000021 magnesium carbonate Inorganic materials 0.000 claims description 7
- 230000001235 sensitizing effect Effects 0.000 claims description 7
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 claims description 6
- 229910052782 aluminium Inorganic materials 0.000 claims description 6
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 claims description 6
- 235000010410 calcium alginate Nutrition 0.000 claims description 6
- 239000000648 calcium alginate Substances 0.000 claims description 6
- 229960002681 calcium alginate Drugs 0.000 claims description 6
- OKHHGHGGPDJQHR-YMOPUZKJSA-L calcium;(2s,3s,4s,5s,6r)-6-[(2r,3s,4r,5s,6r)-2-carboxy-6-[(2r,3s,4r,5s,6r)-2-carboxylato-4,5,6-trihydroxyoxan-3-yl]oxy-4,5-dihydroxyoxan-3-yl]oxy-3,4,5-trihydroxyoxane-2-carboxylate Chemical compound [Ca+2].O[C@@H]1[C@H](O)[C@H](O)O[C@@H](C([O-])=O)[C@H]1O[C@H]1[C@@H](O)[C@@H](O)[C@H](O[C@H]2[C@H]([C@@H](O)[C@H](O)[C@H](O2)C([O-])=O)O)[C@H](C(O)=O)O1 OKHHGHGGPDJQHR-YMOPUZKJSA-L 0.000 claims description 6
- AYJRCSIUFZENHW-UHFFFAOYSA-L barium carbonate Chemical compound [Ba+2].[O-]C([O-])=O AYJRCSIUFZENHW-UHFFFAOYSA-L 0.000 claims description 5
- 229910052712 strontium Inorganic materials 0.000 claims description 5
- CIOAGBVUUVVLOB-UHFFFAOYSA-N strontium atom Chemical compound [Sr] CIOAGBVUUVVLOB-UHFFFAOYSA-N 0.000 claims description 5
- VEPOHXYIFQMVHW-XOZOLZJESA-N 2,3-dihydroxybutanedioic acid (2S,3S)-3,4-dimethyl-2-phenylmorpholine Chemical compound OC(C(O)C(O)=O)C(O)=O.C[C@H]1[C@@H](OCCN1C)c1ccccc1 VEPOHXYIFQMVHW-XOZOLZJESA-N 0.000 claims description 4
- PCNDJXKNXGMECE-UHFFFAOYSA-N Phenazine Natural products C1=CC=CC2=NC3=CC=CC=C3N=C21 PCNDJXKNXGMECE-UHFFFAOYSA-N 0.000 claims description 4
- 229940037003 alum Drugs 0.000 claims description 4
- CPLXHLVBOLITMK-UHFFFAOYSA-N magnesium oxide Inorganic materials [Mg]=O CPLXHLVBOLITMK-UHFFFAOYSA-N 0.000 claims description 4
- 230000008569 process Effects 0.000 claims description 4
- 150000003839 salts Chemical class 0.000 claims description 4
- 229910000018 strontium carbonate Inorganic materials 0.000 claims description 4
- 239000001016 thiazine dye Substances 0.000 claims description 4
- AGIJRRREJXSQJR-UHFFFAOYSA-N 2h-thiazine Chemical compound N1SC=CC=C1 AGIJRRREJXSQJR-UHFFFAOYSA-N 0.000 claims description 3
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 claims description 3
- 229910052791 calcium Inorganic materials 0.000 claims description 3
- 239000011575 calcium Substances 0.000 claims description 3
- 229910000019 calcium carbonate Inorganic materials 0.000 claims description 3
- 230000000694 effects Effects 0.000 claims description 3
- BDAGIHXWWSANSR-NJFSPNSNSA-N hydroxyformaldehyde Chemical compound O[14CH]=O BDAGIHXWWSANSR-NJFSPNSNSA-N 0.000 claims description 3
- 239000000395 magnesium oxide Substances 0.000 claims description 3
- 239000000203 mixture Substances 0.000 claims description 3
- AAAQKTZKLRYKHR-UHFFFAOYSA-N triphenylmethane Chemical compound C1=CC=CC=C1C(C=1C=CC=CC=1)C1=CC=CC=C1 AAAQKTZKLRYKHR-UHFFFAOYSA-N 0.000 claims description 3
- 230000006872 improvement Effects 0.000 claims description 2
- AXZKOIWUVFPNLO-UHFFFAOYSA-N magnesium;oxygen(2-) Chemical group [O-2].[Mg+2] AXZKOIWUVFPNLO-UHFFFAOYSA-N 0.000 claims description 2
- 159000000008 strontium salts Chemical class 0.000 claims description 2
- 159000000011 group IA salts Chemical class 0.000 claims 1
- 230000001737 promoting effect Effects 0.000 abstract description 11
- 239000003344 environmental pollutant Substances 0.000 abstract description 5
- 231100000719 pollutant Toxicity 0.000 abstract description 5
- 231100000331 toxic Toxicity 0.000 abstract description 4
- 230000002588 toxic effect Effects 0.000 abstract description 4
- 239000000243 solution Substances 0.000 description 47
- 238000006243 chemical reaction Methods 0.000 description 23
- ISWSIDIOOBJBQZ-UHFFFAOYSA-N Phenol Chemical compound OC1=CC=CC=C1 ISWSIDIOOBJBQZ-UHFFFAOYSA-N 0.000 description 22
- 239000000047 product Substances 0.000 description 20
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 20
- 238000010521 absorption reaction Methods 0.000 description 8
- 206010034972 Photosensitivity reaction Diseases 0.000 description 7
- 239000000126 substance Substances 0.000 description 7
- 229950003937 tolonium Drugs 0.000 description 7
- HNONEKILPDHFOL-UHFFFAOYSA-M tolonium chloride Chemical compound [Cl-].C1=C(C)C(N)=CC2=[S+]C3=CC(N(C)C)=CC=C3N=C21 HNONEKILPDHFOL-UHFFFAOYSA-M 0.000 description 7
- QTWJRLJHJPIABL-UHFFFAOYSA-N 2-methylphenol;3-methylphenol;4-methylphenol Chemical compound CC1=CC=C(O)C=C1.CC1=CC=CC(O)=C1.CC1=CC=CC=C1O QTWJRLJHJPIABL-UHFFFAOYSA-N 0.000 description 6
- WXNZTHHGJRFXKQ-UHFFFAOYSA-N 4-chlorophenol Chemical compound OC1=CC=C(Cl)C=C1 WXNZTHHGJRFXKQ-UHFFFAOYSA-N 0.000 description 6
- 229930003836 cresol Natural products 0.000 description 6
- 235000014380 magnesium carbonate Nutrition 0.000 description 6
- IZUPBVBPLAPZRR-UHFFFAOYSA-N pentachlorophenol Chemical compound OC1=C(Cl)C(Cl)=C(Cl)C(Cl)=C1Cl IZUPBVBPLAPZRR-UHFFFAOYSA-N 0.000 description 6
- -1 triphenylmethan`e Chemical compound 0.000 description 6
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 5
- 239000002253 acid Substances 0.000 description 5
- 239000003513 alkali Substances 0.000 description 5
- IWOUKMZUPDVPGQ-UHFFFAOYSA-N barium nitrate Inorganic materials [Ba+2].[O-][N+]([O-])=O.[O-][N+]([O-])=O IWOUKMZUPDVPGQ-UHFFFAOYSA-N 0.000 description 5
- 239000002585 base Substances 0.000 description 5
- 239000000460 chlorine Substances 0.000 description 5
- 229910052801 chlorine Inorganic materials 0.000 description 5
- 150000002500 ions Chemical class 0.000 description 5
- 230000007246 mechanism Effects 0.000 description 5
- 231100000419 toxicity Toxicity 0.000 description 5
- 230000001988 toxicity Effects 0.000 description 5
- 238000011282 treatment Methods 0.000 description 5
- 239000002699 waste material Substances 0.000 description 5
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 4
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 description 4
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 4
- LHGVFZTZFXWLCP-UHFFFAOYSA-N guaiacol Chemical compound COC1=CC=CC=C1O LHGVFZTZFXWLCP-UHFFFAOYSA-N 0.000 description 4
- 238000005342 ion exchange Methods 0.000 description 4
- 229910021645 metal ion Inorganic materials 0.000 description 4
- IWDCLRJOBJJRNH-UHFFFAOYSA-N p-cresol Chemical compound CC1=CC=C(O)C=C1 IWDCLRJOBJJRNH-UHFFFAOYSA-N 0.000 description 4
- 238000011084 recovery Methods 0.000 description 4
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 3
- 238000004458 analytical method Methods 0.000 description 3
- AYJRCSIUFZENHW-DEQYMQKBSA-L barium(2+);oxomethanediolate Chemical compound [Ba+2].[O-][14C]([O-])=O AYJRCSIUFZENHW-DEQYMQKBSA-L 0.000 description 3
- 230000007062 hydrolysis Effects 0.000 description 3
- 238000006460 hydrolysis reaction Methods 0.000 description 3
- 229920000642 polymer Polymers 0.000 description 3
- 235000013824 polyphenols Nutrition 0.000 description 3
- 238000001228 spectrum Methods 0.000 description 3
- KUUVQVSHGLHAKZ-UHFFFAOYSA-N thionine Chemical compound C=1C=CC=CSC=CC=1 KUUVQVSHGLHAKZ-UHFFFAOYSA-N 0.000 description 3
- 238000002211 ultraviolet spectrum Methods 0.000 description 3
- 239000003643 water by type Substances 0.000 description 3
- ISPYQTSUDJAMAB-UHFFFAOYSA-N 2-chlorophenol Chemical compound OC1=CC=CC=C1Cl ISPYQTSUDJAMAB-UHFFFAOYSA-N 0.000 description 2
- 241000251468 Actinopterygii Species 0.000 description 2
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 2
- 206010070834 Sensitisation Diseases 0.000 description 2
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 description 2
- XLOMVQKBTHCTTD-UHFFFAOYSA-N Zinc monoxide Chemical compound [Zn]=O XLOMVQKBTHCTTD-UHFFFAOYSA-N 0.000 description 2
- 150000007513 acids Chemical class 0.000 description 2
- 230000004931 aggregating effect Effects 0.000 description 2
- 125000003118 aryl group Chemical group 0.000 description 2
- 238000006065 biodegradation reaction Methods 0.000 description 2
- 235000010216 calcium carbonate Nutrition 0.000 description 2
- 230000015556 catabolic process Effects 0.000 description 2
- 125000002091 cationic group Chemical group 0.000 description 2
- 150000001875 compounds Chemical class 0.000 description 2
- 229910052802 copper Inorganic materials 0.000 description 2
- 239000010949 copper Substances 0.000 description 2
- 238000006731 degradation reaction Methods 0.000 description 2
- 229910000514 dolomite Inorganic materials 0.000 description 2
- 239000010459 dolomite Substances 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 2
- 235000013305 food Nutrition 0.000 description 2
- 229960001867 guaiacol Drugs 0.000 description 2
- 239000003295 industrial effluent Substances 0.000 description 2
- 239000003456 ion exchange resin Substances 0.000 description 2
- 229920003303 ion-exchange polymer Polymers 0.000 description 2
- 229910052742 iron Inorganic materials 0.000 description 2
- 239000011133 lead Substances 0.000 description 2
- 235000012245 magnesium oxide Nutrition 0.000 description 2
- 230000003458 metachromatic effect Effects 0.000 description 2
- 238000003801 milling Methods 0.000 description 2
- 231100000252 nontoxic Toxicity 0.000 description 2
- 230000003000 nontoxic effect Effects 0.000 description 2
- 150000002894 organic compounds Chemical class 0.000 description 2
- 239000007800 oxidant agent Substances 0.000 description 2
- 238000006552 photochemical reaction Methods 0.000 description 2
- 230000002165 photosensitisation Effects 0.000 description 2
- 239000003504 photosensitizing agent Substances 0.000 description 2
- IEQIEDJGQAUEQZ-UHFFFAOYSA-N phthalocyanine Chemical compound N1C(N=C2C3=CC=CC=C3C(N=C3C4=CC=CC=C4C(=N4)N3)=N2)=C(C=CC=C2)C2=C1N=C1C2=CC=CC=C2C4=N1 IEQIEDJGQAUEQZ-UHFFFAOYSA-N 0.000 description 2
- 239000011347 resin Substances 0.000 description 2
- 229920005989 resin Polymers 0.000 description 2
- 229920006395 saturated elastomer Polymers 0.000 description 2
- 230000008313 sensitization Effects 0.000 description 2
- 238000001179 sorption measurement Methods 0.000 description 2
- UUCCCPNEFXQJEL-UHFFFAOYSA-L strontium dihydroxide Chemical class [OH-].[OH-].[Sr+2] UUCCCPNEFXQJEL-UHFFFAOYSA-L 0.000 description 2
- RXSHXLOMRZJCLB-UHFFFAOYSA-L strontium;diacetate Chemical compound [Sr+2].CC([O-])=O.CC([O-])=O RXSHXLOMRZJCLB-UHFFFAOYSA-L 0.000 description 2
- 239000006228 supernatant Substances 0.000 description 2
- 239000011269 tar Substances 0.000 description 2
- 238000012546 transfer Methods 0.000 description 2
- 238000003911 water pollution Methods 0.000 description 2
- PHOLIFLKGONSGY-CSKARUKUSA-N (e)-(3-methyl-1,3-benzothiazol-2-ylidene)hydrazine Chemical compound C1=CC=C2S\C(=N\N)N(C)C2=C1 PHOLIFLKGONSGY-CSKARUKUSA-N 0.000 description 1
- NWUYHJFMYQTDRP-UHFFFAOYSA-N 1,2-bis(ethenyl)benzene;1-ethenyl-2-ethylbenzene;styrene Chemical compound C=CC1=CC=CC=C1.CCC1=CC=CC=C1C=C.C=CC1=CC=CC=C1C=C NWUYHJFMYQTDRP-UHFFFAOYSA-N 0.000 description 1
- 150000004345 1,2-dihydroxyanthraquinones Chemical class 0.000 description 1
- VGVRPFIJEJYOFN-UHFFFAOYSA-N 2,3,4,6-tetrachlorophenol Chemical compound OC1=C(Cl)C=C(Cl)C(Cl)=C1Cl VGVRPFIJEJYOFN-UHFFFAOYSA-N 0.000 description 1
- HSQFVBWFPBKHEB-UHFFFAOYSA-N 2,3,4-trichlorophenol Chemical compound OC1=CC=C(Cl)C(Cl)=C1Cl HSQFVBWFPBKHEB-UHFFFAOYSA-N 0.000 description 1
- LINPIYWFGCPVIE-UHFFFAOYSA-N 2,4,6-trichlorophenol Chemical compound OC1=C(Cl)C=C(Cl)C=C1Cl LINPIYWFGCPVIE-UHFFFAOYSA-N 0.000 description 1
- HFZWRUODUSTPEG-UHFFFAOYSA-N 2,4-dichlorophenol Chemical compound OC1=CC=C(Cl)C=C1Cl HFZWRUODUSTPEG-UHFFFAOYSA-N 0.000 description 1
- UXVMQQNJUSDDNG-UHFFFAOYSA-L Calcium chloride Chemical compound [Cl-].[Cl-].[Ca+2] UXVMQQNJUSDDNG-UHFFFAOYSA-L 0.000 description 1
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 1
- XFXPMWWXUTWYJX-UHFFFAOYSA-N Cyanide Chemical compound N#[C-] XFXPMWWXUTWYJX-UHFFFAOYSA-N 0.000 description 1
- RWSOTUBLDIXVET-UHFFFAOYSA-N Dihydrogen sulfide Chemical class S RWSOTUBLDIXVET-UHFFFAOYSA-N 0.000 description 1
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 1
- KFZMGEQAYNKOFK-UHFFFAOYSA-N Isopropanol Chemical compound CC(C)O KFZMGEQAYNKOFK-UHFFFAOYSA-N 0.000 description 1
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 description 1
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 description 1
- 241000220317 Rosa Species 0.000 description 1
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 description 1
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 description 1
- 230000032900 absorption of visible light Effects 0.000 description 1
- 230000002378 acidificating effect Effects 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 230000000996 additive effect Effects 0.000 description 1
- 239000012670 alkaline solution Substances 0.000 description 1
- 150000001336 alkenes Chemical class 0.000 description 1
- 235000010407 ammonium alginate Nutrition 0.000 description 1
- 239000000728 ammonium alginate Substances 0.000 description 1
- KPGABFJTMYCRHJ-YZOKENDUSA-N ammonium alginate Chemical compound [NH4+].[NH4+].O1[C@@H](C([O-])=O)[C@@H](OC)[C@H](O)[C@H](O)[C@@H]1O[C@@H]1[C@@H](C([O-])=O)O[C@@H](O)[C@@H](O)[C@H]1O KPGABFJTMYCRHJ-YZOKENDUSA-N 0.000 description 1
- 238000013459 approach Methods 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 239000012298 atmosphere Substances 0.000 description 1
- WDIHJSXYQDMJHN-UHFFFAOYSA-L barium chloride Chemical compound [Cl-].[Cl-].[Ba+2] WDIHJSXYQDMJHN-UHFFFAOYSA-L 0.000 description 1
- 229910001626 barium chloride Inorganic materials 0.000 description 1
- 230000006399 behavior Effects 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 239000011230 binding agent Substances 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- AXCZMVOFGPJBDE-UHFFFAOYSA-L calcium dihydroxide Chemical compound [OH-].[OH-].[Ca+2] AXCZMVOFGPJBDE-UHFFFAOYSA-L 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 230000003197 catalytic effect Effects 0.000 description 1
- 239000002738 chelating agent Substances 0.000 description 1
- 238000007385 chemical modification Methods 0.000 description 1
- 239000003153 chemical reaction reagent Substances 0.000 description 1
- IZMHKHHRLNWLMK-UHFFFAOYSA-M chloridoaluminium Chemical compound Cl[Al] IZMHKHHRLNWLMK-UHFFFAOYSA-M 0.000 description 1
- 239000000571 coke Substances 0.000 description 1
- 230000000536 complexating effect Effects 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 238000010924 continuous production Methods 0.000 description 1
- 229920001577 copolymer Polymers 0.000 description 1
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- 238000010908 decantation Methods 0.000 description 1
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- 238000009792 diffusion process Methods 0.000 description 1
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- 238000010494 dissociation reaction Methods 0.000 description 1
- 230000005593 dissociations Effects 0.000 description 1
- 238000004090 dissolution Methods 0.000 description 1
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- 239000012153 distilled water Substances 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 239000003651 drinking water Substances 0.000 description 1
- 235000020188 drinking water Nutrition 0.000 description 1
- 230000002349 favourable effect Effects 0.000 description 1
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- 239000007863 gel particle Substances 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 230000005283 ground state Effects 0.000 description 1
- 150000002391 heterocyclic compounds Chemical class 0.000 description 1
- BTXNYTINYBABQR-UHFFFAOYSA-N hypericin Chemical compound C12=C(O)C=C(O)C(C(C=3C(O)=CC(C)=C4C=33)=O)=C2C3=C2C3=C4C(C)=CC(O)=C3C(=O)C3=C(O)C=C(O)C1=C32 BTXNYTINYBABQR-UHFFFAOYSA-N 0.000 description 1
- 229940005608 hypericin Drugs 0.000 description 1
- PHOKTTKFQUYZPI-UHFFFAOYSA-N hypericin Natural products Cc1cc(O)c2c3C(=O)C(=Cc4c(O)c5c(O)cc(O)c6c7C(=O)C(=Cc8c(C)c1c2c(c78)c(c34)c56)O)O PHOKTTKFQUYZPI-UHFFFAOYSA-N 0.000 description 1
- 238000007654 immersion Methods 0.000 description 1
- 238000011065 in-situ storage Methods 0.000 description 1
- 239000003317 industrial substance Substances 0.000 description 1
- 239000002440 industrial waste Substances 0.000 description 1
- 150000002484 inorganic compounds Chemical class 0.000 description 1
- 229910010272 inorganic material Inorganic materials 0.000 description 1
- 239000003446 ligand Substances 0.000 description 1
- 230000031700 light absorption Effects 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- VUZPPFZMUPKLLV-UHFFFAOYSA-N methane;hydrate Chemical compound C.O VUZPPFZMUPKLLV-UHFFFAOYSA-N 0.000 description 1
- CXKWCBBOMKCUKX-UHFFFAOYSA-M methylene blue Chemical compound [Cl-].C1=CC(N(C)C)=CC2=[S+]C3=CC(N(C)C)=CC=C3N=C21 CXKWCBBOMKCUKX-UHFFFAOYSA-M 0.000 description 1
- 229960000907 methylthioninium chloride Drugs 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 230000007935 neutral effect Effects 0.000 description 1
- 239000003960 organic solvent Substances 0.000 description 1
- 230000008520 organization Effects 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- 238000006213 oxygenation reaction Methods 0.000 description 1
- 239000011236 particulate material Substances 0.000 description 1
- 239000012466 permeate Substances 0.000 description 1
- 229940031826 phenolate Drugs 0.000 description 1
- 230000001699 photocatalysis Effects 0.000 description 1
- 238000006303 photolysis reaction Methods 0.000 description 1
- 230000015843 photosynthesis, light reaction Effects 0.000 description 1
- 239000004033 plastic Substances 0.000 description 1
- 229920003023 plastic Polymers 0.000 description 1
- 150000008442 polyphenolic compounds Chemical class 0.000 description 1
- 229910052700 potassium Inorganic materials 0.000 description 1
- 235000010408 potassium alginate Nutrition 0.000 description 1
- 239000000737 potassium alginate Substances 0.000 description 1
- 239000012286 potassium permanganate Substances 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- SSKVDVBQSWQEGJ-UHFFFAOYSA-N pseudohypericin Natural products C12=C(O)C=C(O)C(C(C=3C(O)=CC(O)=C4C=33)=O)=C2C3=C2C3=C4C(C)=CC(O)=C3C(=O)C3=C(O)C=C(O)C1=C32 SSKVDVBQSWQEGJ-UHFFFAOYSA-N 0.000 description 1
- 230000005180 public health Effects 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 230000008929 regeneration Effects 0.000 description 1
- 238000011069 regeneration method Methods 0.000 description 1
- 230000000717 retained effect Effects 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- 239000012266 salt solution Substances 0.000 description 1
- 239000004576 sand Substances 0.000 description 1
- 238000012216 screening Methods 0.000 description 1
- 238000004062 sedimentation Methods 0.000 description 1
- 229910052708 sodium Inorganic materials 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 238000000638 solvent extraction Methods 0.000 description 1
- 230000003595 spectral effect Effects 0.000 description 1
- 230000000087 stabilizing effect Effects 0.000 description 1
- 238000010186 staining Methods 0.000 description 1
- 239000007858 starting material Substances 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- LEDMRZGFZIAGGB-UHFFFAOYSA-L strontium carbonate Chemical compound [Sr+2].[O-]C([O-])=O LEDMRZGFZIAGGB-UHFFFAOYSA-L 0.000 description 1
- 230000004083 survival effect Effects 0.000 description 1
- 229940073455 tetraethylammonium hydroxide Drugs 0.000 description 1
- LRGJRHZIDJQFCL-UHFFFAOYSA-M tetraethylazanium;hydroxide Chemical compound [OH-].CC[N+](CC)(CC)CC LRGJRHZIDJQFCL-UHFFFAOYSA-M 0.000 description 1
- 150000004897 thiazines Chemical class 0.000 description 1
- 239000004408 titanium dioxide Substances 0.000 description 1
- 238000004448 titration Methods 0.000 description 1
- UDKYUQZDRMRDOR-UHFFFAOYSA-N tungsten Chemical compound [W][W][W][W][W][W][W][W][W][W][W][W][W][W][W][W][W][W][W][W][W][W][W][W][W][W][W][W][W][W][W][W][W][W][W][W][W][W][W][W][W][W][W][W][W][W][W][W] UDKYUQZDRMRDOR-UHFFFAOYSA-N 0.000 description 1
- 229910052721 tungsten Inorganic materials 0.000 description 1
- 239000010937 tungsten Substances 0.000 description 1
- 150000003739 xylenols Chemical class 0.000 description 1
- 229910052725 zinc Inorganic materials 0.000 description 1
- 239000011701 zinc Substances 0.000 description 1
- 239000011787 zinc oxide Substances 0.000 description 1
Classifications
-
- A—HUMAN NECESSITIES
- A62—LIFE-SAVING; FIRE-FIGHTING
- A62D—CHEMICAL MEANS FOR EXTINGUISHING FIRES OR FOR COMBATING OR PROTECTING AGAINST HARMFUL CHEMICAL AGENTS; CHEMICAL MATERIALS FOR USE IN BREATHING APPARATUS
- A62D3/00—Processes for making harmful chemical substances harmless or less harmful, by effecting a chemical change in the substances
- A62D3/10—Processes for making harmful chemical substances harmless or less harmful, by effecting a chemical change in the substances by subjecting to electric or wave energy or particle or ionizing radiation
- A62D3/17—Processes for making harmful chemical substances harmless or less harmful, by effecting a chemical change in the substances by subjecting to electric or wave energy or particle or ionizing radiation to electromagnetic radiation, e.g. emitted by a laser
-
- A—HUMAN NECESSITIES
- A62—LIFE-SAVING; FIRE-FIGHTING
- A62D—CHEMICAL MEANS FOR EXTINGUISHING FIRES OR FOR COMBATING OR PROTECTING AGAINST HARMFUL CHEMICAL AGENTS; CHEMICAL MATERIALS FOR USE IN BREATHING APPARATUS
- A62D3/00—Processes for making harmful chemical substances harmless or less harmful, by effecting a chemical change in the substances
- A62D3/30—Processes for making harmful chemical substances harmless or less harmful, by effecting a chemical change in the substances by reacting with chemical agents
- A62D3/38—Processes for making harmful chemical substances harmless or less harmful, by effecting a chemical change in the substances by reacting with chemical agents by oxidation; by combustion
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/08—Processes employing the direct application of electric or wave energy, or particle radiation; Apparatus therefor
- B01J19/12—Processes employing the direct application of electric or wave energy, or particle radiation; Apparatus therefor employing electromagnetic waves
- B01J19/122—Incoherent waves
- B01J19/127—Sunlight; Visible light
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/30—Treatment of water, waste water, or sewage by irradiation
- C02F1/32—Treatment of water, waste water, or sewage by irradiation with ultraviolet light
-
- A—HUMAN NECESSITIES
- A62—LIFE-SAVING; FIRE-FIGHTING
- A62D—CHEMICAL MEANS FOR EXTINGUISHING FIRES OR FOR COMBATING OR PROTECTING AGAINST HARMFUL CHEMICAL AGENTS; CHEMICAL MATERIALS FOR USE IN BREATHING APPARATUS
- A62D2101/00—Harmful chemical substances made harmless, or less harmful, by effecting chemical change
- A62D2101/20—Organic substances
-
- A—HUMAN NECESSITIES
- A62—LIFE-SAVING; FIRE-FIGHTING
- A62D—CHEMICAL MEANS FOR EXTINGUISHING FIRES OR FOR COMBATING OR PROTECTING AGAINST HARMFUL CHEMICAL AGENTS; CHEMICAL MATERIALS FOR USE IN BREATHING APPARATUS
- A62D2101/00—Harmful chemical substances made harmless, or less harmful, by effecting chemical change
- A62D2101/20—Organic substances
- A62D2101/22—Organic substances containing halogen
-
- A—HUMAN NECESSITIES
- A62—LIFE-SAVING; FIRE-FIGHTING
- A62D—CHEMICAL MEANS FOR EXTINGUISHING FIRES OR FOR COMBATING OR PROTECTING AGAINST HARMFUL CHEMICAL AGENTS; CHEMICAL MATERIALS FOR USE IN BREATHING APPARATUS
- A62D2101/00—Harmful chemical substances made harmless, or less harmful, by effecting chemical change
- A62D2101/20—Organic substances
- A62D2101/28—Organic substances containing oxygen, sulfur, selenium or tellurium, i.e. chalcogen
-
- A—HUMAN NECESSITIES
- A62—LIFE-SAVING; FIRE-FIGHTING
- A62D—CHEMICAL MEANS FOR EXTINGUISHING FIRES OR FOR COMBATING OR PROTECTING AGAINST HARMFUL CHEMICAL AGENTS; CHEMICAL MATERIALS FOR USE IN BREATHING APPARATUS
- A62D2203/00—Aspects of processes for making harmful chemical substances harmless, or less harmful, by effecting chemical change in the substances
- A62D2203/04—Combined processes involving two or more non-distinct steps covered by groups A62D3/10 - A62D3/40
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/30—Wastewater or sewage treatment systems using renewable energies
- Y02W10/37—Wastewater or sewage treatment systems using renewable energies using solar energy
Landscapes
- Chemical & Material Sciences (AREA)
- Toxicology (AREA)
- Health & Medical Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Health & Medical Sciences (AREA)
- Business, Economics & Management (AREA)
- General Chemical & Material Sciences (AREA)
- Emergency Management (AREA)
- Organic Chemistry (AREA)
- Physics & Mathematics (AREA)
- Electromagnetism (AREA)
- Engineering & Computer Science (AREA)
- Water Supply & Treatment (AREA)
- Hydrology & Water Resources (AREA)
- Optics & Photonics (AREA)
- Life Sciences & Earth Sciences (AREA)
- Environmental & Geological Engineering (AREA)
- Removal Of Specific Substances (AREA)
- Treatment Of Water By Oxidation Or Reduction (AREA)
- Water Treatment By Sorption (AREA)
Abstract
Abstract of the Disclosure A method for promoting the photooxidative destruction of organic waste pollutants by use of gelled metal alginate particles which have been stained with a dye sensitizer. The stained particles are both recoverable and biodegradable. They are effective in promoting the photooxidation of organic wastes including toxic phenol compounds in the presence of visible light and atmospheric oxygen.
Description
`~ ~al55~2~
Background of the Invention ~ -This invention relates to a method for promoting the photooxidative destruction of organic wastes and, more parti- -cularly, to a method utilizing particles of a biodegradable gelled metal alginate which have been stained with a sensitizing dye.
In recent years a justifiable concern has arisen over the presence in water supplies of organic waste pollutants.
Among the more toxic constitutents of effluents are phenols, cresols, xylenols, polyphenols, etc~, which are introduced into ~-the environment from chemical, petrochemical and plastics industries, refineries and coke ovens, and even from decaying vegetation. In a recent report to the United Nations Food and Agriculture Organization (Water Res., 7, 929-41 (1973)), the limit on combined phenols was recommended to be 1 ppm to ensure survival of salmonoids and 2 ppm for coarse fish.
The problem is compounded when water is treated with chlorine for municipal use. Chlorine reacts with phenols in the ppm range to produce o- and ~-chlorophenols up to 2,4,6-~20 trichlorophenol. Because of the off-taste and the odor arising from p-chlorophenol in water, the U. S. Public Health Service (1962) suggested a limit of 0.001 ppm of phenol in drinking water. This is lower than that for cyanide and arseni~c. ~`
Toxicity o these phenols to fish is also greater than that of the unchlorinated phenols.
An outline of these problems and some of the current solutions is given in J. E. Zajic, "Water Pollution, Disposal and Reuse", Vol. 2, pp. 418-426 (1971). There, Zajic reports.
that the following treatments for phenolic wastes may be used:
30 ~ 1) solvent extraction, Z) steam stripping, 3) adsorption, 4) ion exchange, 5) chemical degrada*ion and 6) biological degradation.
Background of the Invention ~ -This invention relates to a method for promoting the photooxidative destruction of organic wastes and, more parti- -cularly, to a method utilizing particles of a biodegradable gelled metal alginate which have been stained with a sensitizing dye.
In recent years a justifiable concern has arisen over the presence in water supplies of organic waste pollutants.
Among the more toxic constitutents of effluents are phenols, cresols, xylenols, polyphenols, etc~, which are introduced into ~-the environment from chemical, petrochemical and plastics industries, refineries and coke ovens, and even from decaying vegetation. In a recent report to the United Nations Food and Agriculture Organization (Water Res., 7, 929-41 (1973)), the limit on combined phenols was recommended to be 1 ppm to ensure survival of salmonoids and 2 ppm for coarse fish.
The problem is compounded when water is treated with chlorine for municipal use. Chlorine reacts with phenols in the ppm range to produce o- and ~-chlorophenols up to 2,4,6-~20 trichlorophenol. Because of the off-taste and the odor arising from p-chlorophenol in water, the U. S. Public Health Service (1962) suggested a limit of 0.001 ppm of phenol in drinking water. This is lower than that for cyanide and arseni~c. ~`
Toxicity o these phenols to fish is also greater than that of the unchlorinated phenols.
An outline of these problems and some of the current solutions is given in J. E. Zajic, "Water Pollution, Disposal and Reuse", Vol. 2, pp. 418-426 (1971). There, Zajic reports.
that the following treatments for phenolic wastes may be used:
30 ~ 1) solvent extraction, Z) steam stripping, 3) adsorption, 4) ion exchange, 5) chemical degrada*ion and 6) biological degradation.
- 2 -~L~55421~) If the phenol concentration is high enough, recovery by solvent ex~raction or steam stripping may be economically feasible. However, phenol concentrations in most industrial affluents are not sufficiently high to justify such procedures.
For this reason, phenols in dilute industrial effluents are usually adsorbed on activated carbon, for which they may be recovered. On the other hand, Zajic lists several limitations to this method, Vi7.: lack of continuity in the process and contamination of the activated carbon by tars and tar acids beyond regeneration. ;
Similarly, because of their toxicity to most micro~
organisms, biodegradation of phenols is slow; however, the products are non-toxic, andthis is a feasible method of treatment if the concentration is not too high. Chemical oxidation by ~ -ozone, chlorine or potassium permanganate is the fastest de-gradative treatment, but the cost in power and chemcials is --high. In addition, as Zajic notes, with elemental chlorine precaution must be taken to ensure complete reaction of the phenol or the partially chlorinated phenol derivatives impart objec-tionable taste and toxicity to the water.
For these reasons, photooxidation has been studied as a possible solution to the problem. It is attractive because instead o~ requiring stoichiometric quantities of eleatrically or electronically produced oxidants, such as chlorine or ozone, the reaction takes place in the presence of sunliyht, air and catalytic quantities of a promoter. Zinc titanate, zinc oxide, titanium dioxide and beach sand have been found to promote photo-catalytic oxidation of dissolved organic matter on irradiation with sunlamps. See Kinney et al~ "Photolysis Mechanisms for ~30 Pollution Abatement", Report No. TWRC-13, U. S. Dept. of Interior, Federal Water Pollution Control Adm., Ohio Basin Region, Cincinnati, Ohio, October 1969.
For this reason, phenols in dilute industrial effluents are usually adsorbed on activated carbon, for which they may be recovered. On the other hand, Zajic lists several limitations to this method, Vi7.: lack of continuity in the process and contamination of the activated carbon by tars and tar acids beyond regeneration. ;
Similarly, because of their toxicity to most micro~
organisms, biodegradation of phenols is slow; however, the products are non-toxic, andthis is a feasible method of treatment if the concentration is not too high. Chemical oxidation by ~ -ozone, chlorine or potassium permanganate is the fastest de-gradative treatment, but the cost in power and chemcials is --high. In addition, as Zajic notes, with elemental chlorine precaution must be taken to ensure complete reaction of the phenol or the partially chlorinated phenol derivatives impart objec-tionable taste and toxicity to the water.
For these reasons, photooxidation has been studied as a possible solution to the problem. It is attractive because instead o~ requiring stoichiometric quantities of eleatrically or electronically produced oxidants, such as chlorine or ozone, the reaction takes place in the presence of sunliyht, air and catalytic quantities of a promoter. Zinc titanate, zinc oxide, titanium dioxide and beach sand have been found to promote photo-catalytic oxidation of dissolved organic matter on irradiation with sunlamps. See Kinney et al~ "Photolysis Mechanisms for ~30 Pollution Abatement", Report No. TWRC-13, U. S. Dept. of Interior, Federal Water Pollution Control Adm., Ohio Basin Region, Cincinnati, Ohio, October 1969.
- 3 -.t ~ ~r Dye sensitizers have also been used. Thus, Sargent and Sanks in a recent presentation at t~e Photochemical Reaction Engineering Symposium of the American Institute of Chemical -Engineers in Washington, D. C., December 1-5, 1974, entitled "Dye Catalyzed Oxidation of Refractory Organic Wastes Using Visible Light Energy" explained that the reaction sequence for dye sensitization involves absorption of light energy by the dye, transfer of dye energy to dissolved oxygen to form energized oxygen, and oxidation of the organic waste by the energized oxygen.
Accordingly, Sargent and Sanks describe the use of dyes in a homogenous solution to promote aerobic photooxidation -of organic wastes. While this system suffers from the instability of the dye in the homogeneous phase and the need to stain large volumes of water effectively, Sargent and Sanks find it pre~
ferable to the resin-bound d~es which they also tested since binding to ion exchange resins was found to reduce the e~ec-tiveness of the dye as a sensitizer and slow down the reaction as compared to dissolved dyes.
Still, it would be desirable for the sensitizing dye to be bound to a particulate material since txeatment with homogeneous phase dyes results in an intermixing of the dye and the water treated which may be objectionable; whereas, with stained solid particles the phases remain separate. Similarly, use of heterogeneous phase dye-stained particles permits easy recovery of the stained particles by sedimentation or screening, allowing for reclaiming, restoring or reusing. It would also be particularly desirable if a biodegradable base material could be used since this would allow for distribution of the stained particles in polluted lakes and ponds in a one-time application without any detximental environmental effect.
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In regard to resin~bound d~e sensitizers, it is noted that Blosse~, Neckers, Thayer and Schaap in an article entitled "Polvmer-Base Sensl`tizers for P~otooxidants" in the Journal of the American Chemical Society, 95:5820 (1973) report on the use of a Rose Bengal polymer-based reagent to sensitize the generation of singlet molecular oxygen for promoting photochemical reactions.
The base used was an insoluble styrene divinylbenzene copolymer bead. This material, however, is not biodegradable and would be difficult to regenerate.
Accordingly, the need still exists for an effective polymer-based dye sensitizer for promoting photooxidative destruction of organic waste, especially a material which would be biodegradable while at the same time stabilizing the dyes to prolong their useful life over that which they evidence in homogeneous phase systems.
Summary of the Invention The present invention fills this need by providing a feasible method of promoting photooxid~tion of organic waste materials, including phenolic compounds. The method involvés the use of gelled metal alginate particles. The particles are stained with an appropriate sensitizing dye which will photo-catalytically generate singlet oxygen in the presence of sun-- - light or artificial light for effective destruction of the oxidizable pollutants contained in the organic was~es.
.:
In one aspect the invention provides a method for photooxidative destruction of organic wastes found in aqueous effluents utilizing a dye sensitizer to promote the oxidation of said organic wastes by air or oxygen in the presence of visible light, at an at least weakly alkaline pH and under other ; process conditions operable to effect the photooxidation wherein .
~ - 5 -: :
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the improvement comprises using as the promoter biodegradable, gelled metal alginate particles selected from the group consisting of barium alginate, calcium alginate, strontium alginate, and aluminum alginate beads which have been stained with a dye sensitizer selected from the group consisting of the `;
acridine, thiazine, triphenylmethane, phenazine, phthalocyanine classes of cationic dyes, the dye to alginate normality ratio being in the range of 1:30 to 1:200. .;
It is known that most organic waste molecules are -~
not destroyed by direct absorption of visible light, but that when oxygen is excited to a singlet state, it becomes a strong : oxidizing agent capable of oxidizing many ordinarily refractory organic compounds. It is also known that various dyes sensitize or catalyze in situ the generation of~singlet oxygen. The present invention utilizes those known principles in providing a means to effectively oxidize polluting orga~ c compounds. -:
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~L~554zo In addition to providing the known sensitizing function of homogeneous dye systems, however, t~e dye-stained alyinate particles present a heterogeneous phase which has a number of advantageous features. Most significantly, there is no need to separate the dye from the water treated as occurs when a homogeneous dye system is used. In addition, the particles do not, as a rule, introduce a new toxic mate~ial into the environ-ment they are intended to treat since alginate is known to be both non-toxic and biodegradablè ~in fact it is a common bulk additive to food products). Likewise, the dyes used are not notably toxic, and are slowly degraded under conditions of use.
Unlike ion exchange resin particles, alginate particles stabilize the dyes in an active state and prolong their useful 1ife over that which they evidence in homogeneous phase systems.
The gelled particles are mechanically and chemically resistant to deterioration under contemplated conditions of use and may, thus, be reclaimed, restained, and reused several times without .
serious loss of efficiency.
These properties make it possible to treat lndustrial ef1uents containing organic wastes, such as phenols at con-centrations below that for economical recovery, in sunlit lagoons, riffle beds, or in batch or continuous column reactors. It is also possible to use the stained alginate particles for broad-cast application of the particles in lake's, rivers or estuaries where a pollution problem exists. In the latter application, the particles would require no further attention or recovery since they are degraded natural1y to harmless derivatives in a reasonable time.
: . :
~; The pàrticulate base consists of a soluble alginate (such as sodium, potassium or ammonium alginate); gelled by treat-ment with divalent or trivalent metal ions. As an alternative means of obtaining a particular metal ion gelled alginate, an ~,, ',. .
:1055~2~
ion-exchange process can be used to replace the ions in already gelled particles ~ith dIfferent metal ~ons of the particular type desired. In either event, a gelled metal alginate is formed having metal ions available to act as binding agents for the dye.
Barium, calcium, strontium and aluminum alginates are preferred, but alginates of lead, iron, copper and other divalent metal ions can be used if desired.
The particles are stained by immersion in a solution containing a suitable sensitizing dye which will bind to the alginate paLticles. Most of the dye may be incorporated into the gelled alginate particle within a few minutes, but it takes about a day for it to be distributed evenly throughout. ~or the most part cationic dyes which have marked aggregating or metachromatic properties are used. Examples of the types of .... ........ ..
dyes possible include the acridine, thiazine, triphenylmethan`e, phenazine and phthalocyanine classes, with the thiazine dyes being preferred. It is believed that much of the dye in the particle is in an aggregated, photochemically inactive form, but is in equilibrium with the monomeric, photochemically active form. In any~case, the stability of the dyes against chemical and photochemical degradation is markedly increased by binding to the gelled alginate particles. The amount of dye bound to the particles can vary all the way to a 1:1 ratio, depending on the economic considerations, but generally the preferred alginate normality ratios are in the range of 1:30 - 1:200.
The dye i9 usually destroyed or much depleted by an exhaustive photosensitized oxidation reac~ion. Also the dye is sometimes removed from the alginate particle by complexing : .. . .
with oxidation products of the organic waste, but this dye is still photoactive and may continue photosensitizing the reaction ; ;
in the homogeneous phase.
' ' ' . ' - 7 - ~
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. . . . . .
-~(~SS~L20 It is known that dye sensitized photooxidation of phenols increases with pH at least ~o pH 10. Thus, with phenols it is necessary to have a medium which is at least weaXly alkaline (pH ~ 9) to get photooxidation because only the phenolate ion is attacked. Since the gelled alginate particles are neutral, it is thus necessary to add alkali to the solution if oxidation is to be favored. Furthermore, if the products of the reaction are acidic, the medium must be neutralized if the reaction is to be maintained.
One approach to this problem is to simply add to the effluent to be treated (if it is not already alkaline) a basic material which will adjust the pH upward and permit the reaction to go forward. H^owever, in the case of lagoons or natural waters, -this may not be feasible. Therefore, another possible approàch is to establish basic conditions within the gelled alginate particle itself. This obviates the need to add alkali to the entire medi~m. It may be done by milling slightly soluble basic substances into the alginate solution before gelling. Any compatible alkaline filler having a proper soluhility and basic ~o reaction on hydrolysis may be used. Examples are magnesium oxide, magnesium carbonate, calcium carbonate, strontium carbonate, barium carbonate, and mixtures thereof. Thus, it is possible to .
oxidize phenols without addition of alkali to the medium, and in some cases, without the medium becoming alkaline at all. In ;
addition, it has been found that the presence of the basic filler ~
inside the particle accelerates the net diffusion of phenol into -the bead, thus further promoting the oxidation.
In this manner, using either a filled or unfilled gelled metal alginate particle which has been stained with a sensitizing dye, it is possible to effectively promote the photooxidation of organic wastes including aromatics like cresol and phenol. This may be done in a batch or a continuous process ' :, - 8 - ;
,:: , ,,, . ,, " ,, ". , , ~:, , 5~;~20 i~ the presence of sunlight or other visible light and in the ~-presence of air or any other oxygen source. '~
Accordingly, it is an o~ject of the present invention to provide an effective method of promoting photooxidative destruction of organic wastes using dye-stained, gelled, metal '~' alginate particles. ' '~' '-It is another object of the present invention to pro- -: -vide dye-stained, gelled, metal alginate particles containing a basic filler which particles may be used to provide an alkalinè
condition favorable to the oxidation.
Other o~jects and advantages of the present invention will be apparent from the following description and the appended claims.
Description of the Preferred Embodimenks The present invention for promoting photooxidative destruction of orgainic wastes was tested primarily for its effectiveness-in oxidation of phenols because of their outstand- ' ing environmental impact.' Photochemical oxidation does not oxidize phenols completely to carbon dioxide and water, but does destroy the aromatic ring system which is primarily res-~ sponsible for toxicity. The products that do form are probably "' ;~ susceptible to further photooxidation, hydrolysis,and biode~
gradation. There~ore, it is possible that photooxidation could be used as a step pre'liminary to biodegradation in the usual manner, whereby the toxicity of phenols to microorganisms is obviated.
. .
Although the photosensitized oxidation of phenols by dye sensitizers i5 generally considered to proceed by a ~
mechanism i'nvolving singlet oxygén generation, other mechanisms '' "' are-known for photosensitized oxidation in general~ and these may occur instead of,'or in addition to, the singlet oxygen mechanism. Any oxidation which is promoted by dye sensitization, '~
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~OSS4ZO
whether through production o~ $inglet oxygen or otherwise is a possible react~on to ~e promoted by the stained alginate particles of t~e present invent~on. T~us, dye sensitizers can also be used to promote the photooxidation of aliphatic amines, mercaptans, olefins, and certain heterocyclic compounds, any of -which may be present as pollutants in industrial effluents. The use of these dye sensitizers bound to the particulate alginate material as in the present invention is often desirable in such photosensitized oxidation reaction, and thus, it i5 possible to use the disclosed process;for the treatment of numerous types of waste effluents in addition to phenolic wastes.
A dye which promotes photochemical oxidation without being consumed by the reactlon is considered a sensitizer~. Its activity may be through a mechanism in which the dye adsorbs visible light energy, transfers it to another compound such as dissolved oxygen, thereby returning to ground state to adsorb more light, or one involving the`transfer of electrons. In the present invention, the dyes that stain the gelled alginate -particles deeply and are retained well are those with marked ;
aggregating or metachromatic properties. Cationic dyes without these properties adsorb to the bead by ion exchange but easily wash out. Fortunately most of the strongly photosensitizing dyes happen to fall into the former category. ~
Staining has been carried out with dyes of the acridine, ~ ~ -thiazine, triphenylmethane, phenazine and phthalocyanine classes of dyes, although the thiazine dyes are preferred since they are often the strongest sensitizers. Aluminum alginate particles bind dyes like thlonine normally, but also bind dyes of classes that are known~to be ligands for the Al~3 ion. These classes include the alizarins and hypericin.
Usually the dyes in an aqueous solution form are used to stain the gelled alginate par~icles. Any concentration dye , . .
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may be used, but those in the 10 4 to 10 3M ran~e are pre~erred.
Likewise, the amount of d~e bound to the partl`cles may vary greatly, ~ut generally the dye to alginate normality ratios used ranged from 1:30 to 1:200. Dyes which are not soluble in water may be applied from an organic solvent solution and then the stained particles transferred to water. For example, the dye chloroaluminum chlorophthalocyanine was put on gelled barium alginate beads in methanol solution and the beads then placed in water.
The gelled alginate particles may be prepared by adding a solution of an alginate (such as sodium alginate) drop-wise to a solution of a divalent; or trivalent metal salt (such as 0.03 M Ba(NO3)2, O.lM CaC12 or O.lM Sr (OOCCH3)2) under gentle stirring. The concentration of alginate solution is not critical to the size of the particle for~ed, but does affect somewhat its mechanical strength and capacity ~or stain. Gelled particles have been made with from 7.5 X 10 3 N (1.5 g/l) alginate solution to 4.2 X 10 2 N (8.5 g/l) alginate solution, that is up to a 1% solution. Mechanical consistency o~ the bead sets ~o the lower limit on concentration of alginate solution; viscosity `~ sets the upper.
As each drop of alginate solution contacts the metal salt solution, a pellicle of gel form~. It then becomes i ~-uniformly gelled as the ions permeate it. The drop shrinks `~
to about one-third of its original volume and becomes a weakl~
elastic, so~t, easily cut, transparent particle or bead. Al-.. . .
though the beads are deformable, they do not crumble under normal careful handling.
In addition to the barium, calcium and strontium salt .
gelling solutions mentioned, lead, iron and copper ones have beén used in a like manner to gell sodium alginate drops. At least 10 3 moIar solutions are used, with the saturation point , , " ~ , ,, : , ~ . ;
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being the upper concentration lLmit.
As mentioned, an alternatl~e means of obtaining a particular metal alginate is to use an ion-exchange process on already gelled alginate particles. Thus, aluminum alginate beads have been made successfully by treating calcium alginate beads with alum solutions.
Beads are separated from supernatant by decantation or draining through a Buchner funnel. They shrink through syneresis if left out of water very long, and so must be kept immersed.
Similarly, they are not stable in strongly alkaline solution' because of hydrolysis, or in solutions containing acids, mono- ~ -valent salts at high concentration, or certain chelating agents ~ ' because of displacement of the divalent metal binding the gel. ~ -If such conditions are encountered in application, chemical modification of the beads to withstand these conditions should ' be used. ;
As mentioned, one method of creating a weakly alkaline condition, which favors photooxidation of phenols, is by use of basic fillers within the gelled alginate particles themselves.
This is easily accomplished by milling the basic materials, ~ ~
such as MgO, MgCO3 CaCO3, SrCO3 BaCO3 or mixtures, into the ' - alginate solution before forming'the gelled particles. While , various amounts may be used,'the preferred ràtio of salt addition ' is lg per 25 ml of alginate solution'. ' ~' A number of examples follow which illustrate the use of stained alginate gel particles in the photosensitized '' oxidation of typical pollutant phenols. Most of these reactions -~; ~ were run in the laboratory in a batch-type readtor, with artifical ~tungsten) lighting, and with oxygen introduced into '30 the system. Reactions have also been fol~owed in open vessels, exposed to the atmosphere and sunlight. Because of the greater intensity of sunlight, these reactions appear generally to go more rapidly and thoroughly than the former.
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Some degree of photosensitized oxidation has been observed with most of the d~es used of the classes mentioned, but the most effective dyes readily available were found to be those of the thiazine class, including Methylene Blue, Thionine, and Toluidine Blue. One of the more effective filled bead systems, barium alginate plus barium carbonate, was used routinely with Toluidine Blue to compare the behavior of different phenols.
ExAMæLE I
Sl:rontium alginate gel beads were prepared by adding 25 ml of 8.6 X 10 3 N sodium alginate (Manugel, Alginate -Industries Ltd.) dropwise ko 500 ml of 0.1 M strontium acetate -solution. The beads were drained, treated with 50 ml of ~
2r x 10 4 M strontium acetate, and with distilled water. They ~ -were then stained with 5.5 x 10 6 moles of Toluidine Blue, so that the ratio of alginate uronic acid residues to dye molecules was 39. -~
These beads were added in a round bottom flask to `~
800 ml of a solution containing 1.025 x 10 3 M phenol and 10 ml of saturated strontium hydroxide solution, and irradiated with ~20 a 750 watt-projector lamp 22 cm from the reaction flask. The flask was kept at approximately 23 by a water bath, and a slow stream of oxygen was ~ed into it. The contents were stirred magnetically to keep the beads circulating through the solution.
Irradiation was continued for 23 hours during which , .
~ ~ time 13 ml more saturated strontium hydroxide was added to ;~ maintain the phenol in an ionized state. The light intensity measured in back of the reactor was 1.25 x 105 erg/cm2sec.
The solution soon turned olive-brown, and the absorp-~ ~ tion speckrum correspondingly showed continuously increasing ;~30 intensity throughout the visible and ultraviolet regions, belong-- ing to oxidation products of phenol. The lack of charact-eriskic bands in the spectrum of these products indicated that ' ~, '. ! ',, . i 10554~0 the aromatic ring system of phenol ~as being destroyed. Analysis of the ultraviolet spectrum showed that about 50% of the phenol had been ox.idized in 23 hours.
Chemical oxygen ~emand (COD) measurements were made with a Precision AquaRator. These showed a reduction from 236 ppm at the beginning to 148 ppm at the time the reaction was stopped. -EXAMPLE II
Barium alginate gel beads containing magnesium carbonate were prepared by adding 25 ml of a 1~ solution of sodium alginate (sample obtained from Xelco Co.), combined with 1 g of freshly precipitated magnesium carbonate, dropwise into 500 ml of 0.05 M
barium nitrate solution. On standing in wash water, the beads began to swell because of replacement of barium in the gel cross- -links by magneslum, but this was suppressed by transferring the beads to 10 3 M barium chloride solution.
The beads were washed twice and stained with 5 x 10 6 moles of Toluidine Blue. The ratio of polyuronic acid equivalents to moles of dye was 215. ~
The stained beads were added in a round bottom flask ;~-Zo to 800 ml of 1.15 x 10 M guaiacol, without addition of external ; base, and the reaction conducted for 23 hours as in Example I.
Under irradiation, the solution darkened rapidly, with ~steadily rising absorption in the visible and ultraviolet regions. Analysis of the ultraviolet spectrum showed that the ~ ~ .
~bands of guaiacol wer,e essentially gone after four hours, b~ing replaced by the broader band of a nonaromatic product. This band too was gone after 23 hours, leaving only continuous absorption. Meanwhile, the beads were bleached, though some dye ~- was~detectable in solution.
The COD fell from 310 ppm at the beginning of the reaction to 138 ppm at the end. After the reaction, alum was added to the solution, whereupon a brown precipitate separated ;. .. , ,. .'. . , , ' .. ' , ' . . . , . . . . . ., ~ .:
,, , ~ , , ~ . . . ,. , : .
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and the COD o~ the supernatant fell to 90 ppm.
EXAMPLE III
Calcium alginate gel ~eads containing dolomite were prepared by adding 25 ml of 1% sodium alginate (Kelco sample) solution, mixed with 0.9 g dolomite (ca. 2CaCO3 MgCO3), drop-wise to 150 ml of 0.1 M calcium chloride solution. These beads were used in two reactions, recovered each time, and restained ~- -a third time with 5 x 10 6 moles of Toluidine Blue. The beads ;~
were added in a round bottom flask to 800 ml of solution, ~ ~
1.015 x 10 3 M in p-cresol, and irradiated as before for a -; -total of 47 hours.
The reaction proceeded without marked discoloration of the contents of the flask, but there was a strong increase of absorption in the shorter ultraviolet. Cresol was destroyed at the rate of about 6% of the remaining cresol per hour. After ~ -47 hours, there was estimated to be no more than about 6~ of the original cresol left. On a weight basis, this amounts to a drop from 112 ppm to 6.6 ppm cresol. -Although this reaction went somewhat slower than when barium or magnesium carbonate is used as a basic filler, the pH of the solution did not become alkaline at any time, as evident from the appearance of the spectrum of cresol. The buildup of visible-absorbing oxidation products was markedly less than in other runs.
EXAMPLE IV
Filled and stained barium alginate gel beads were prepared from 25 ml of 1~ sodium alginate solution (Kelco sample), 1/3 g. of barium carbonate, and 5 x 10 6 moles of Toluidine Blue, as in previous examples. These beads were used in a round bottom flask to oxidize 0.0514 g of p-chlorophenol in 800 ml of water (5 x 10 M). Irradiation was continued for 95 hours.
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10554;20 ~ bsorption due to products rose continually through the vîsi~le spectral region and t~e ultra~iolet above 290 nm.
Below that wavelength, backgrolmd a~sorption decreased after three days. Absorption bands of a definite product appeared -around 250 nm, maximized after about seven hours irradiation, and had vanished at the end of the reaction. In contrast, bands in the region characteristic of p-chlorophenol persisted until the end of the reaction, in an amount about 22~ of the original chlorophenol absorption.
Analysis of the ~inal solutions with 3-methyl-2-benzothiazolinone hydrazone indicated the presence of a phenol, but apparently non p-chlorophenol. It is possible that a pro-duct of the reaction is a phenol which is refractory to further oxidation, perhaps because of a high acid dissociation constant.
The COD fell from 112 ppm at the beginning to 42 ppm at the end, and addition of alum did not decrease it further.
Titration of chloride showed that 73% of that originally in chlorophenol had been released in inorganic form by the oxidation.
In oxidation of more dilute p-chlorophenol solutions (10 4M), destruction of 95% of the starting material could be"
obtained. In an oxidation of 2 x 10 4M, 2,4-di-chlorophenol sensitized hy thionine, 94% loss of the phenol was reached after twenty-four hours.
EXAMPLE V
Strontium alginate gel beads, made from 25 ml of sodium alginate solution, 7.5 x 10 3N, and containing 0.73 g of strontium carbonate, were stained with 5 x 10 6 moles of Toluidine Blue. These were added in a round bottom flask to 800 ml of a solution saturated in pentachlorophenol (10 4M), and oxidation sensitized as usual.
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The pentachlorophenol appeared entirel~ gone a~ter four hours, its place ~eing ta~en b~ a product absorbing at somewhat shor~er wavelengths. This product, too, was nearly gone - ~-after six hours, and after twenty~three hours only broad bands of products in the shorter ultraviolet remained. There was thus evidently complete oxidation of pentachlorophenol to non- ;i-aromatic products in that time.
2,4,6-trichlorophenol and 2, 3, 4, 6-tetrachlorophenol were oxidized in a manner similar to this.
EXAMPLE VI
.
Barium alginate gel beads were made by dropping 85 ml of a 1% sodium alginate solution into 500 ml of 0.04 M barium nitrate solution, and allowed to stand until they had shrunk to constant volume which is from 1/4 to 1/3 of the original volume of alginate solution. The beads were then poured into a glass column 48 cm long by 1.2 cm diameter. The column contained 3.6 x 10 3 equivalents of uronate residues.
The column of beads was stained by drawing 10 3 M
thionine solution into it, until 3.6 x 10 5 moles of dye had ~20 ~ been attached to the beads, giving a polymer equivalent-to dye ratio of-100. The dye was taken up very rapidly, and the beads ;~-appeared purplish-black.
~ ~ .
~ The column was held in an enclosure with three 15-watt ~ ~ .
fluorescent lamps parallel to it. Inside walls of the enclosure were painted white ~or better reflection of light.
Water was poured through the column until the con-, ; ~ centration of dye in the effluent fell to 1 x 10 6 M. The color of dye in water in equilibrium with the beads was barely dis-~cernible.
~30~ A solution, 1 x 10 4 M in phenol and 2 x 10 4 M in tetraethylammonium hydroxide (pH 8.9), and saturated with oxygen (ca. 1.25 ~ 10 3 M), was then introduced into the column.
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When the concentration o~ phenol in t~e ef1uent reached its maximum ~alue, tAe l;`ght was turned on. The phenol solutîon was passed through t~e column at different flow rates, and the ultraviolet spectrum of the effluent recorded at frequent in-tervals.
At a flow rate of 60 ml/hour, phenol was not detectable in the spectrum of ~he effluent, the dominant product being one with an absorption band at 245 nm. At faster flow rates, phenol appeared in the effluent, but at slower flow rates to 30 ml/hour, the 245 nm product was itself almost eliminate~, leaving generally ~ -rising absorption through the ultravislet in indistinct bands.
A total of 1 liter of phenol solution was passed through the column. -After this, 1 liter of 10 4 M p-cresol, and 1 liter of ~
10 4 M p-chlorophenol, were passed similarly through the column, ~ -; with similar results overall. During this time, the dye was not leached from the beads to such an exten~ that replenishment was necessary.
' ~; Higher concentrations of phenols were not used because ~20 of the limited solubility of oxygen in water. Under these conditions, formation of products with absorption in the visible ~ , .
region was not evident.
Unfilled gelled alginate particles are better for :::
such column applications as found in Example VI above and in other situations where the volume created is restricted. They keep the dye better and dissolution of the filler would not limit ~ .
their useful life. Therefore alkali material such as lime water s also metered into the column while processing the organic wasteO
Filled particles are generally preferred for broadcast application and situations where ponds, lagoons or natural waters are treat~d since it is not feasible to add alkali materials :
, ~' ' ' . . .. . . .. . .. . . . . . . . .
iO554;20 under those conditions. Of couxse, i~ t~e waters to be treated are naturally alkaline, unfilled gelled alginate particles could be used. In the application to ponds, lagoons, etc., it is contemplated that this can be a one-time application with the stained gelled alginate particles biodegrading rather than being recovered.
From the foregoing examples, it can be seen that the dye-stained, gelled alginate particles of the present invention are useful in promoting the photooxidation of various phenols found in waste effluen~ts. They are also useful in promoting the photoxidative déstruction of other organic wastes found in aqueous effluents. Similarly, it is believed apparent to one of ordinary skil~ in the art that the same particles could be used to prepare a desired oxidation product of an organic or inorganic compound, if that desired product can be prepared by photosensitized oxidation. By this means then, industrial chemicals could be commercially synthesized and produced in the ~; same manner that industrial waste effluents can be photo- -~ ......
~oxidatively destroyed. -20 ~ While the method herein described constitutes a pre-ferred embodiment of the invention, it is to be understood that the invention is not llmited to this precise method, and that changes may be made therein without departing from the scope of the invention.
.
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Accordingly, Sargent and Sanks describe the use of dyes in a homogenous solution to promote aerobic photooxidation -of organic wastes. While this system suffers from the instability of the dye in the homogeneous phase and the need to stain large volumes of water effectively, Sargent and Sanks find it pre~
ferable to the resin-bound d~es which they also tested since binding to ion exchange resins was found to reduce the e~ec-tiveness of the dye as a sensitizer and slow down the reaction as compared to dissolved dyes.
Still, it would be desirable for the sensitizing dye to be bound to a particulate material since txeatment with homogeneous phase dyes results in an intermixing of the dye and the water treated which may be objectionable; whereas, with stained solid particles the phases remain separate. Similarly, use of heterogeneous phase dye-stained particles permits easy recovery of the stained particles by sedimentation or screening, allowing for reclaiming, restoring or reusing. It would also be particularly desirable if a biodegradable base material could be used since this would allow for distribution of the stained particles in polluted lakes and ponds in a one-time application without any detximental environmental effect.
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In regard to resin~bound d~e sensitizers, it is noted that Blosse~, Neckers, Thayer and Schaap in an article entitled "Polvmer-Base Sensl`tizers for P~otooxidants" in the Journal of the American Chemical Society, 95:5820 (1973) report on the use of a Rose Bengal polymer-based reagent to sensitize the generation of singlet molecular oxygen for promoting photochemical reactions.
The base used was an insoluble styrene divinylbenzene copolymer bead. This material, however, is not biodegradable and would be difficult to regenerate.
Accordingly, the need still exists for an effective polymer-based dye sensitizer for promoting photooxidative destruction of organic waste, especially a material which would be biodegradable while at the same time stabilizing the dyes to prolong their useful life over that which they evidence in homogeneous phase systems.
Summary of the Invention The present invention fills this need by providing a feasible method of promoting photooxid~tion of organic waste materials, including phenolic compounds. The method involvés the use of gelled metal alginate particles. The particles are stained with an appropriate sensitizing dye which will photo-catalytically generate singlet oxygen in the presence of sun-- - light or artificial light for effective destruction of the oxidizable pollutants contained in the organic was~es.
.:
In one aspect the invention provides a method for photooxidative destruction of organic wastes found in aqueous effluents utilizing a dye sensitizer to promote the oxidation of said organic wastes by air or oxygen in the presence of visible light, at an at least weakly alkaline pH and under other ; process conditions operable to effect the photooxidation wherein .
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the improvement comprises using as the promoter biodegradable, gelled metal alginate particles selected from the group consisting of barium alginate, calcium alginate, strontium alginate, and aluminum alginate beads which have been stained with a dye sensitizer selected from the group consisting of the `;
acridine, thiazine, triphenylmethane, phenazine, phthalocyanine classes of cationic dyes, the dye to alginate normality ratio being in the range of 1:30 to 1:200. .;
It is known that most organic waste molecules are -~
not destroyed by direct absorption of visible light, but that when oxygen is excited to a singlet state, it becomes a strong : oxidizing agent capable of oxidizing many ordinarily refractory organic compounds. It is also known that various dyes sensitize or catalyze in situ the generation of~singlet oxygen. The present invention utilizes those known principles in providing a means to effectively oxidize polluting orga~ c compounds. -:
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~L~554zo In addition to providing the known sensitizing function of homogeneous dye systems, however, t~e dye-stained alyinate particles present a heterogeneous phase which has a number of advantageous features. Most significantly, there is no need to separate the dye from the water treated as occurs when a homogeneous dye system is used. In addition, the particles do not, as a rule, introduce a new toxic mate~ial into the environ-ment they are intended to treat since alginate is known to be both non-toxic and biodegradablè ~in fact it is a common bulk additive to food products). Likewise, the dyes used are not notably toxic, and are slowly degraded under conditions of use.
Unlike ion exchange resin particles, alginate particles stabilize the dyes in an active state and prolong their useful 1ife over that which they evidence in homogeneous phase systems.
The gelled particles are mechanically and chemically resistant to deterioration under contemplated conditions of use and may, thus, be reclaimed, restained, and reused several times without .
serious loss of efficiency.
These properties make it possible to treat lndustrial ef1uents containing organic wastes, such as phenols at con-centrations below that for economical recovery, in sunlit lagoons, riffle beds, or in batch or continuous column reactors. It is also possible to use the stained alginate particles for broad-cast application of the particles in lake's, rivers or estuaries where a pollution problem exists. In the latter application, the particles would require no further attention or recovery since they are degraded natural1y to harmless derivatives in a reasonable time.
: . :
~; The pàrticulate base consists of a soluble alginate (such as sodium, potassium or ammonium alginate); gelled by treat-ment with divalent or trivalent metal ions. As an alternative means of obtaining a particular metal ion gelled alginate, an ~,, ',. .
:1055~2~
ion-exchange process can be used to replace the ions in already gelled particles ~ith dIfferent metal ~ons of the particular type desired. In either event, a gelled metal alginate is formed having metal ions available to act as binding agents for the dye.
Barium, calcium, strontium and aluminum alginates are preferred, but alginates of lead, iron, copper and other divalent metal ions can be used if desired.
The particles are stained by immersion in a solution containing a suitable sensitizing dye which will bind to the alginate paLticles. Most of the dye may be incorporated into the gelled alginate particle within a few minutes, but it takes about a day for it to be distributed evenly throughout. ~or the most part cationic dyes which have marked aggregating or metachromatic properties are used. Examples of the types of .... ........ ..
dyes possible include the acridine, thiazine, triphenylmethan`e, phenazine and phthalocyanine classes, with the thiazine dyes being preferred. It is believed that much of the dye in the particle is in an aggregated, photochemically inactive form, but is in equilibrium with the monomeric, photochemically active form. In any~case, the stability of the dyes against chemical and photochemical degradation is markedly increased by binding to the gelled alginate particles. The amount of dye bound to the particles can vary all the way to a 1:1 ratio, depending on the economic considerations, but generally the preferred alginate normality ratios are in the range of 1:30 - 1:200.
The dye i9 usually destroyed or much depleted by an exhaustive photosensitized oxidation reac~ion. Also the dye is sometimes removed from the alginate particle by complexing : .. . .
with oxidation products of the organic waste, but this dye is still photoactive and may continue photosensitizing the reaction ; ;
in the homogeneous phase.
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-~(~SS~L20 It is known that dye sensitized photooxidation of phenols increases with pH at least ~o pH 10. Thus, with phenols it is necessary to have a medium which is at least weaXly alkaline (pH ~ 9) to get photooxidation because only the phenolate ion is attacked. Since the gelled alginate particles are neutral, it is thus necessary to add alkali to the solution if oxidation is to be favored. Furthermore, if the products of the reaction are acidic, the medium must be neutralized if the reaction is to be maintained.
One approach to this problem is to simply add to the effluent to be treated (if it is not already alkaline) a basic material which will adjust the pH upward and permit the reaction to go forward. H^owever, in the case of lagoons or natural waters, -this may not be feasible. Therefore, another possible approàch is to establish basic conditions within the gelled alginate particle itself. This obviates the need to add alkali to the entire medi~m. It may be done by milling slightly soluble basic substances into the alginate solution before gelling. Any compatible alkaline filler having a proper soluhility and basic ~o reaction on hydrolysis may be used. Examples are magnesium oxide, magnesium carbonate, calcium carbonate, strontium carbonate, barium carbonate, and mixtures thereof. Thus, it is possible to .
oxidize phenols without addition of alkali to the medium, and in some cases, without the medium becoming alkaline at all. In ;
addition, it has been found that the presence of the basic filler ~
inside the particle accelerates the net diffusion of phenol into -the bead, thus further promoting the oxidation.
In this manner, using either a filled or unfilled gelled metal alginate particle which has been stained with a sensitizing dye, it is possible to effectively promote the photooxidation of organic wastes including aromatics like cresol and phenol. This may be done in a batch or a continuous process ' :, - 8 - ;
,:: , ,,, . ,, " ,, ". , , ~:, , 5~;~20 i~ the presence of sunlight or other visible light and in the ~-presence of air or any other oxygen source. '~
Accordingly, it is an o~ject of the present invention to provide an effective method of promoting photooxidative destruction of organic wastes using dye-stained, gelled, metal '~' alginate particles. ' '~' '-It is another object of the present invention to pro- -: -vide dye-stained, gelled, metal alginate particles containing a basic filler which particles may be used to provide an alkalinè
condition favorable to the oxidation.
Other o~jects and advantages of the present invention will be apparent from the following description and the appended claims.
Description of the Preferred Embodimenks The present invention for promoting photooxidative destruction of orgainic wastes was tested primarily for its effectiveness-in oxidation of phenols because of their outstand- ' ing environmental impact.' Photochemical oxidation does not oxidize phenols completely to carbon dioxide and water, but does destroy the aromatic ring system which is primarily res-~ sponsible for toxicity. The products that do form are probably "' ;~ susceptible to further photooxidation, hydrolysis,and biode~
gradation. There~ore, it is possible that photooxidation could be used as a step pre'liminary to biodegradation in the usual manner, whereby the toxicity of phenols to microorganisms is obviated.
. .
Although the photosensitized oxidation of phenols by dye sensitizers i5 generally considered to proceed by a ~
mechanism i'nvolving singlet oxygén generation, other mechanisms '' "' are-known for photosensitized oxidation in general~ and these may occur instead of,'or in addition to, the singlet oxygen mechanism. Any oxidation which is promoted by dye sensitization, '~
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~OSS4ZO
whether through production o~ $inglet oxygen or otherwise is a possible react~on to ~e promoted by the stained alginate particles of t~e present invent~on. T~us, dye sensitizers can also be used to promote the photooxidation of aliphatic amines, mercaptans, olefins, and certain heterocyclic compounds, any of -which may be present as pollutants in industrial effluents. The use of these dye sensitizers bound to the particulate alginate material as in the present invention is often desirable in such photosensitized oxidation reaction, and thus, it i5 possible to use the disclosed process;for the treatment of numerous types of waste effluents in addition to phenolic wastes.
A dye which promotes photochemical oxidation without being consumed by the reactlon is considered a sensitizer~. Its activity may be through a mechanism in which the dye adsorbs visible light energy, transfers it to another compound such as dissolved oxygen, thereby returning to ground state to adsorb more light, or one involving the`transfer of electrons. In the present invention, the dyes that stain the gelled alginate -particles deeply and are retained well are those with marked ;
aggregating or metachromatic properties. Cationic dyes without these properties adsorb to the bead by ion exchange but easily wash out. Fortunately most of the strongly photosensitizing dyes happen to fall into the former category. ~
Staining has been carried out with dyes of the acridine, ~ ~ -thiazine, triphenylmethane, phenazine and phthalocyanine classes of dyes, although the thiazine dyes are preferred since they are often the strongest sensitizers. Aluminum alginate particles bind dyes like thlonine normally, but also bind dyes of classes that are known~to be ligands for the Al~3 ion. These classes include the alizarins and hypericin.
Usually the dyes in an aqueous solution form are used to stain the gelled alginate par~icles. Any concentration dye , . .
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may be used, but those in the 10 4 to 10 3M ran~e are pre~erred.
Likewise, the amount of d~e bound to the partl`cles may vary greatly, ~ut generally the dye to alginate normality ratios used ranged from 1:30 to 1:200. Dyes which are not soluble in water may be applied from an organic solvent solution and then the stained particles transferred to water. For example, the dye chloroaluminum chlorophthalocyanine was put on gelled barium alginate beads in methanol solution and the beads then placed in water.
The gelled alginate particles may be prepared by adding a solution of an alginate (such as sodium alginate) drop-wise to a solution of a divalent; or trivalent metal salt (such as 0.03 M Ba(NO3)2, O.lM CaC12 or O.lM Sr (OOCCH3)2) under gentle stirring. The concentration of alginate solution is not critical to the size of the particle for~ed, but does affect somewhat its mechanical strength and capacity ~or stain. Gelled particles have been made with from 7.5 X 10 3 N (1.5 g/l) alginate solution to 4.2 X 10 2 N (8.5 g/l) alginate solution, that is up to a 1% solution. Mechanical consistency o~ the bead sets ~o the lower limit on concentration of alginate solution; viscosity `~ sets the upper.
As each drop of alginate solution contacts the metal salt solution, a pellicle of gel form~. It then becomes i ~-uniformly gelled as the ions permeate it. The drop shrinks `~
to about one-third of its original volume and becomes a weakl~
elastic, so~t, easily cut, transparent particle or bead. Al-.. . .
though the beads are deformable, they do not crumble under normal careful handling.
In addition to the barium, calcium and strontium salt .
gelling solutions mentioned, lead, iron and copper ones have beén used in a like manner to gell sodium alginate drops. At least 10 3 moIar solutions are used, with the saturation point , , " ~ , ,, : , ~ . ;
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being the upper concentration lLmit.
As mentioned, an alternatl~e means of obtaining a particular metal alginate is to use an ion-exchange process on already gelled alginate particles. Thus, aluminum alginate beads have been made successfully by treating calcium alginate beads with alum solutions.
Beads are separated from supernatant by decantation or draining through a Buchner funnel. They shrink through syneresis if left out of water very long, and so must be kept immersed.
Similarly, they are not stable in strongly alkaline solution' because of hydrolysis, or in solutions containing acids, mono- ~ -valent salts at high concentration, or certain chelating agents ~ ' because of displacement of the divalent metal binding the gel. ~ -If such conditions are encountered in application, chemical modification of the beads to withstand these conditions should ' be used. ;
As mentioned, one method of creating a weakly alkaline condition, which favors photooxidation of phenols, is by use of basic fillers within the gelled alginate particles themselves.
This is easily accomplished by milling the basic materials, ~ ~
such as MgO, MgCO3 CaCO3, SrCO3 BaCO3 or mixtures, into the ' - alginate solution before forming'the gelled particles. While , various amounts may be used,'the preferred ràtio of salt addition ' is lg per 25 ml of alginate solution'. ' ~' A number of examples follow which illustrate the use of stained alginate gel particles in the photosensitized '' oxidation of typical pollutant phenols. Most of these reactions -~; ~ were run in the laboratory in a batch-type readtor, with artifical ~tungsten) lighting, and with oxygen introduced into '30 the system. Reactions have also been fol~owed in open vessels, exposed to the atmosphere and sunlight. Because of the greater intensity of sunlight, these reactions appear generally to go more rapidly and thoroughly than the former.
~ .
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Some degree of photosensitized oxidation has been observed with most of the d~es used of the classes mentioned, but the most effective dyes readily available were found to be those of the thiazine class, including Methylene Blue, Thionine, and Toluidine Blue. One of the more effective filled bead systems, barium alginate plus barium carbonate, was used routinely with Toluidine Blue to compare the behavior of different phenols.
ExAMæLE I
Sl:rontium alginate gel beads were prepared by adding 25 ml of 8.6 X 10 3 N sodium alginate (Manugel, Alginate -Industries Ltd.) dropwise ko 500 ml of 0.1 M strontium acetate -solution. The beads were drained, treated with 50 ml of ~
2r x 10 4 M strontium acetate, and with distilled water. They ~ -were then stained with 5.5 x 10 6 moles of Toluidine Blue, so that the ratio of alginate uronic acid residues to dye molecules was 39. -~
These beads were added in a round bottom flask to `~
800 ml of a solution containing 1.025 x 10 3 M phenol and 10 ml of saturated strontium hydroxide solution, and irradiated with ~20 a 750 watt-projector lamp 22 cm from the reaction flask. The flask was kept at approximately 23 by a water bath, and a slow stream of oxygen was ~ed into it. The contents were stirred magnetically to keep the beads circulating through the solution.
Irradiation was continued for 23 hours during which , .
~ ~ time 13 ml more saturated strontium hydroxide was added to ;~ maintain the phenol in an ionized state. The light intensity measured in back of the reactor was 1.25 x 105 erg/cm2sec.
The solution soon turned olive-brown, and the absorp-~ ~ tion speckrum correspondingly showed continuously increasing ;~30 intensity throughout the visible and ultraviolet regions, belong-- ing to oxidation products of phenol. The lack of charact-eriskic bands in the spectrum of these products indicated that ' ~, '. ! ',, . i 10554~0 the aromatic ring system of phenol ~as being destroyed. Analysis of the ultraviolet spectrum showed that about 50% of the phenol had been ox.idized in 23 hours.
Chemical oxygen ~emand (COD) measurements were made with a Precision AquaRator. These showed a reduction from 236 ppm at the beginning to 148 ppm at the time the reaction was stopped. -EXAMPLE II
Barium alginate gel beads containing magnesium carbonate were prepared by adding 25 ml of a 1~ solution of sodium alginate (sample obtained from Xelco Co.), combined with 1 g of freshly precipitated magnesium carbonate, dropwise into 500 ml of 0.05 M
barium nitrate solution. On standing in wash water, the beads began to swell because of replacement of barium in the gel cross- -links by magneslum, but this was suppressed by transferring the beads to 10 3 M barium chloride solution.
The beads were washed twice and stained with 5 x 10 6 moles of Toluidine Blue. The ratio of polyuronic acid equivalents to moles of dye was 215. ~
The stained beads were added in a round bottom flask ;~-Zo to 800 ml of 1.15 x 10 M guaiacol, without addition of external ; base, and the reaction conducted for 23 hours as in Example I.
Under irradiation, the solution darkened rapidly, with ~steadily rising absorption in the visible and ultraviolet regions. Analysis of the ultraviolet spectrum showed that the ~ ~ .
~bands of guaiacol wer,e essentially gone after four hours, b~ing replaced by the broader band of a nonaromatic product. This band too was gone after 23 hours, leaving only continuous absorption. Meanwhile, the beads were bleached, though some dye ~- was~detectable in solution.
The COD fell from 310 ppm at the beginning of the reaction to 138 ppm at the end. After the reaction, alum was added to the solution, whereupon a brown precipitate separated ;. .. , ,. .'. . , , ' .. ' , ' . . . , . . . . . ., ~ .:
,, , ~ , , ~ . . . ,. , : .
~L~559~Z~
and the COD o~ the supernatant fell to 90 ppm.
EXAMPLE III
Calcium alginate gel ~eads containing dolomite were prepared by adding 25 ml of 1% sodium alginate (Kelco sample) solution, mixed with 0.9 g dolomite (ca. 2CaCO3 MgCO3), drop-wise to 150 ml of 0.1 M calcium chloride solution. These beads were used in two reactions, recovered each time, and restained ~- -a third time with 5 x 10 6 moles of Toluidine Blue. The beads ;~
were added in a round bottom flask to 800 ml of solution, ~ ~
1.015 x 10 3 M in p-cresol, and irradiated as before for a -; -total of 47 hours.
The reaction proceeded without marked discoloration of the contents of the flask, but there was a strong increase of absorption in the shorter ultraviolet. Cresol was destroyed at the rate of about 6% of the remaining cresol per hour. After ~ -47 hours, there was estimated to be no more than about 6~ of the original cresol left. On a weight basis, this amounts to a drop from 112 ppm to 6.6 ppm cresol. -Although this reaction went somewhat slower than when barium or magnesium carbonate is used as a basic filler, the pH of the solution did not become alkaline at any time, as evident from the appearance of the spectrum of cresol. The buildup of visible-absorbing oxidation products was markedly less than in other runs.
EXAMPLE IV
Filled and stained barium alginate gel beads were prepared from 25 ml of 1~ sodium alginate solution (Kelco sample), 1/3 g. of barium carbonate, and 5 x 10 6 moles of Toluidine Blue, as in previous examples. These beads were used in a round bottom flask to oxidize 0.0514 g of p-chlorophenol in 800 ml of water (5 x 10 M). Irradiation was continued for 95 hours.
.: : .
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.
i .. , ~ . . . .
,, , .
~: .
10554;20 ~ bsorption due to products rose continually through the vîsi~le spectral region and t~e ultra~iolet above 290 nm.
Below that wavelength, backgrolmd a~sorption decreased after three days. Absorption bands of a definite product appeared -around 250 nm, maximized after about seven hours irradiation, and had vanished at the end of the reaction. In contrast, bands in the region characteristic of p-chlorophenol persisted until the end of the reaction, in an amount about 22~ of the original chlorophenol absorption.
Analysis of the ~inal solutions with 3-methyl-2-benzothiazolinone hydrazone indicated the presence of a phenol, but apparently non p-chlorophenol. It is possible that a pro-duct of the reaction is a phenol which is refractory to further oxidation, perhaps because of a high acid dissociation constant.
The COD fell from 112 ppm at the beginning to 42 ppm at the end, and addition of alum did not decrease it further.
Titration of chloride showed that 73% of that originally in chlorophenol had been released in inorganic form by the oxidation.
In oxidation of more dilute p-chlorophenol solutions (10 4M), destruction of 95% of the starting material could be"
obtained. In an oxidation of 2 x 10 4M, 2,4-di-chlorophenol sensitized hy thionine, 94% loss of the phenol was reached after twenty-four hours.
EXAMPLE V
Strontium alginate gel beads, made from 25 ml of sodium alginate solution, 7.5 x 10 3N, and containing 0.73 g of strontium carbonate, were stained with 5 x 10 6 moles of Toluidine Blue. These were added in a round bottom flask to 800 ml of a solution saturated in pentachlorophenol (10 4M), and oxidation sensitized as usual.
.. ' .
!
' . , , .
, .. . .
.. . . . .
', '' , ' ' : , . . .
~L055~
The pentachlorophenol appeared entirel~ gone a~ter four hours, its place ~eing ta~en b~ a product absorbing at somewhat shor~er wavelengths. This product, too, was nearly gone - ~-after six hours, and after twenty~three hours only broad bands of products in the shorter ultraviolet remained. There was thus evidently complete oxidation of pentachlorophenol to non- ;i-aromatic products in that time.
2,4,6-trichlorophenol and 2, 3, 4, 6-tetrachlorophenol were oxidized in a manner similar to this.
EXAMPLE VI
.
Barium alginate gel beads were made by dropping 85 ml of a 1% sodium alginate solution into 500 ml of 0.04 M barium nitrate solution, and allowed to stand until they had shrunk to constant volume which is from 1/4 to 1/3 of the original volume of alginate solution. The beads were then poured into a glass column 48 cm long by 1.2 cm diameter. The column contained 3.6 x 10 3 equivalents of uronate residues.
The column of beads was stained by drawing 10 3 M
thionine solution into it, until 3.6 x 10 5 moles of dye had ~20 ~ been attached to the beads, giving a polymer equivalent-to dye ratio of-100. The dye was taken up very rapidly, and the beads ;~-appeared purplish-black.
~ ~ .
~ The column was held in an enclosure with three 15-watt ~ ~ .
fluorescent lamps parallel to it. Inside walls of the enclosure were painted white ~or better reflection of light.
Water was poured through the column until the con-, ; ~ centration of dye in the effluent fell to 1 x 10 6 M. The color of dye in water in equilibrium with the beads was barely dis-~cernible.
~30~ A solution, 1 x 10 4 M in phenol and 2 x 10 4 M in tetraethylammonium hydroxide (pH 8.9), and saturated with oxygen (ca. 1.25 ~ 10 3 M), was then introduced into the column.
.- ..:, . . .
~ - 17 - ~
' -. "
,"' :', . . - ' '. , , ' " '. ' , . . : .
10554Z(~
When the concentration o~ phenol in t~e ef1uent reached its maximum ~alue, tAe l;`ght was turned on. The phenol solutîon was passed through t~e column at different flow rates, and the ultraviolet spectrum of the effluent recorded at frequent in-tervals.
At a flow rate of 60 ml/hour, phenol was not detectable in the spectrum of ~he effluent, the dominant product being one with an absorption band at 245 nm. At faster flow rates, phenol appeared in the effluent, but at slower flow rates to 30 ml/hour, the 245 nm product was itself almost eliminate~, leaving generally ~ -rising absorption through the ultravislet in indistinct bands.
A total of 1 liter of phenol solution was passed through the column. -After this, 1 liter of 10 4 M p-cresol, and 1 liter of ~
10 4 M p-chlorophenol, were passed similarly through the column, ~ -; with similar results overall. During this time, the dye was not leached from the beads to such an exten~ that replenishment was necessary.
' ~; Higher concentrations of phenols were not used because ~20 of the limited solubility of oxygen in water. Under these conditions, formation of products with absorption in the visible ~ , .
region was not evident.
Unfilled gelled alginate particles are better for :::
such column applications as found in Example VI above and in other situations where the volume created is restricted. They keep the dye better and dissolution of the filler would not limit ~ .
their useful life. Therefore alkali material such as lime water s also metered into the column while processing the organic wasteO
Filled particles are generally preferred for broadcast application and situations where ponds, lagoons or natural waters are treat~d since it is not feasible to add alkali materials :
, ~' ' ' . . .. . . .. . .. . . . . . . . .
iO554;20 under those conditions. Of couxse, i~ t~e waters to be treated are naturally alkaline, unfilled gelled alginate particles could be used. In the application to ponds, lagoons, etc., it is contemplated that this can be a one-time application with the stained gelled alginate particles biodegrading rather than being recovered.
From the foregoing examples, it can be seen that the dye-stained, gelled alginate particles of the present invention are useful in promoting the photooxidation of various phenols found in waste effluen~ts. They are also useful in promoting the photoxidative déstruction of other organic wastes found in aqueous effluents. Similarly, it is believed apparent to one of ordinary skil~ in the art that the same particles could be used to prepare a desired oxidation product of an organic or inorganic compound, if that desired product can be prepared by photosensitized oxidation. By this means then, industrial chemicals could be commercially synthesized and produced in the ~; same manner that industrial waste effluents can be photo- -~ ......
~oxidatively destroyed. -20 ~ While the method herein described constitutes a pre-ferred embodiment of the invention, it is to be understood that the invention is not llmited to this precise method, and that changes may be made therein without departing from the scope of the invention.
.
: ~ . . .
. -:
30~
' -:
.:
.
- . .
Claims
A method for photooxidative destruction of organic wastes found in aqueous effluents utilizing a dye sensitizer to promote the oxidation of said organic wastes by air or oxygen in the presence of visible light, at an at least weakly alkaline pH and under other process conditions operable to effect the photooxidation wherein the improvement comprises using as the promoter biodegradable, gelled metal alginate particles selected from the group consisting of barium alginate, calcium alginate, strontium alginate, and aluminum alginate beads which have been stained with a dye sensitizer selected from the group consisting of the acridine, thiazine, triphenylmethane, phenazine, phthalocyanine classes of cationic dyes, the dye to alginate normality ratio being in the range of
1:30 to 1:200.
The method of claim 1 wherein said beads are prepared by adding a solution of sodium alginate to a solution of divalent metal salt selected from the group consisting of barium, calcium and strontium salts to form a gelled bead.
The method of claim 1 wherein said beads are prepared by treating calcium alginate beads with alum solution.
The method of claim 1 wherein thiazine dyes are used.
The method of claim 1 wherein said organic wastes include phenolic compounds and said photooxidation takes place under weakly alkaline conditions.
The method of claim 5 wherein said alginate particles contain an alkaline salt filler material to provide at least a portion of said alkaline conditions.
The method of claim 6 wherein said filler is selected from the group consisting of magnesium oxide, magnesium carbonate, calcium carbonate, strontium carbonate, barium carbonate and mixtures thereof.
.
The method of claims 5 wherein said alginate particles are gelled beads selected from the group con-sisting of barium alginate, calcium alginate, strontium alginate and aluminum alginate beads and said sensitizing dye is a thiazine dye.
The method of claim 1 wherein said beads are prepared by adding a solution of sodium alginate to a solution of divalent metal salt selected from the group consisting of barium, calcium and strontium salts to form a gelled bead.
The method of claim 1 wherein said beads are prepared by treating calcium alginate beads with alum solution.
The method of claim 1 wherein thiazine dyes are used.
The method of claim 1 wherein said organic wastes include phenolic compounds and said photooxidation takes place under weakly alkaline conditions.
The method of claim 5 wherein said alginate particles contain an alkaline salt filler material to provide at least a portion of said alkaline conditions.
The method of claim 6 wherein said filler is selected from the group consisting of magnesium oxide, magnesium carbonate, calcium carbonate, strontium carbonate, barium carbonate and mixtures thereof.
.
The method of claims 5 wherein said alginate particles are gelled beads selected from the group con-sisting of barium alginate, calcium alginate, strontium alginate and aluminum alginate beads and said sensitizing dye is a thiazine dye.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US05/551,532 US3951797A (en) | 1975-02-21 | 1975-02-21 | Photooxidative destruction of organic wastes |
Publications (1)
Publication Number | Publication Date |
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CA1055420A true CA1055420A (en) | 1979-05-29 |
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ID=24201656
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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CA243,846A Expired CA1055420A (en) | 1975-02-21 | 1976-01-20 | Photooxidative destruction of organic wastes |
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US (1) | US3951797A (en) |
CA (1) | CA1055420A (en) |
GB (1) | GB1519736A (en) |
Families Citing this family (19)
Publication number | Priority date | Publication date | Assignee | Title |
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FR2387658A1 (en) * | 1977-03-25 | 1978-11-17 | Ciba Geigy Ag | PROCEDURE FOR FIGHTING MICROORGANISMS |
JPS55115484A (en) * | 1979-02-28 | 1980-09-05 | Asahi Chem Ind Co Ltd | Heterogeneous sensitizer for photosensitized oxidation |
US4432344A (en) * | 1981-07-15 | 1984-02-21 | Focus Environmental Systems | Method and apparatus for solar destruction of toxic and hazardous materials |
FR2588548A1 (en) * | 1985-10-11 | 1987-04-17 | Bernard Michel Louis | Water purification and reoxygenation process |
US5186907A (en) * | 1987-03-30 | 1993-02-16 | Mitsubishi Denki Kabushiki Kaisha | Apparatus for treating organic waste gas |
US4915804A (en) * | 1988-12-20 | 1990-04-10 | Allied-Signal Inc. | Titanate bound photosensitizer for producing singlet oxygen |
US4921589A (en) * | 1988-12-20 | 1990-05-01 | Allied-Signal Inc. | Polysiloxane bound photosensitizer for producing singlet oxygen |
US5559035A (en) * | 1992-08-24 | 1996-09-24 | Umpqua Research Company | Solid phase calibration standards |
DE4336512C2 (en) * | 1993-04-23 | 2002-12-12 | Mitsubishi Electric Corp | Reaction control method and apparatus using carbon black molecules and organometallic complexes in an excited state |
WO1998005594A1 (en) * | 1996-08-05 | 1998-02-12 | Solar Dynamics Limited | A portable water purification system |
US20020096479A1 (en) | 2000-06-02 | 2002-07-25 | Butters Brian E. | System and method for photocatalytic treatment of contaminated media |
US6136203A (en) * | 1997-09-10 | 2000-10-24 | Purifics Enviromental Technologies, Inc. | System and method for photocatalytic treatment of contaminated media |
GB2359560B (en) * | 1999-12-22 | 2002-03-20 | Reckitt Benckiser | Photocatalytic cleaning compositions, atricles and methods |
RU2235688C2 (en) * | 2002-02-14 | 2004-09-10 | Федеральное государственное унитарное предприятие "Государственный научный центр "Научно-исследовательский институт органических полупродуктов и красителей" | Water photodisinfecting method |
US20070020300A1 (en) * | 2002-03-12 | 2007-01-25 | Ecolab Inc. | Recreational water treatment employing singlet oxygen |
NO331569B1 (en) | 2010-01-19 | 2012-01-30 | Sorbwater Technology As | Process for removing contaminants from a continuous hydrocolloid liquid stream. |
RU2483774C1 (en) * | 2012-04-28 | 2013-06-10 | Общество С Ограниченной Ответственностью "Плазма-Про" | Method of processing toxic liquid wastes |
CN104014371B (en) * | 2014-06-16 | 2016-05-18 | 湖州师范学院 | Calcium alginate carrying metal phthalocyanine microballoon catalysis material and preparation method thereof |
CN115010207B (en) * | 2022-02-14 | 2023-07-21 | 昆明理工大学 | Method for repairing toxic, harmful and refractory organic pollutants in wetland by utilizing copper slag photocatalysis reinforcement |
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US3544322A (en) * | 1966-07-21 | 1970-12-01 | Yoshikazu Yamada | Photosensitive dispersion in a hydrophilic binder incorporating a stabilizer |
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- 1975-02-21 US US05/551,532 patent/US3951797A/en not_active Expired - Lifetime
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1976
- 1976-01-20 CA CA243,846A patent/CA1055420A/en not_active Expired
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US3951797A (en) | 1976-04-20 |
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