PL48151B1 - - Google Patents
Download PDFInfo
- Publication number
- PL48151B1 PL48151B1 PL98020A PL9802062A PL48151B1 PL 48151 B1 PL48151 B1 PL 48151B1 PL 98020 A PL98020 A PL 98020A PL 9802062 A PL9802062 A PL 9802062A PL 48151 B1 PL48151 B1 PL 48151B1
- Authority
- PL
- Poland
- Prior art keywords
- cleaning compositions
- compounds
- sulfur
- deposits
- gases
- Prior art date
Links
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 claims description 5
- 238000004140 cleaning Methods 0.000 claims description 5
- 229910052717 sulfur Inorganic materials 0.000 claims description 5
- 239000011593 sulfur Substances 0.000 claims description 5
- 239000007789 gas Substances 0.000 claims description 4
- 239000000203 mixture Substances 0.000 claims description 4
- 238000000034 method Methods 0.000 claims description 2
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 claims 3
- QIGBRXMKCJKVMJ-UHFFFAOYSA-N Hydroquinone Chemical compound OC1=CC=C(O)C=C1 QIGBRXMKCJKVMJ-UHFFFAOYSA-N 0.000 claims 2
- UFWIBTONFRDIAS-UHFFFAOYSA-N Naphthalene Chemical compound C1=CC=CC2=CC=CC=C21 UFWIBTONFRDIAS-UHFFFAOYSA-N 0.000 claims 2
- 150000001875 compounds Chemical class 0.000 claims 2
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical class [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 claims 1
- 229930192627 Naphthoquinone Natural products 0.000 claims 1
- 150000001412 amines Chemical class 0.000 claims 1
- 150000001454 anthracenes Chemical class 0.000 claims 1
- PYKYMHQGRFAEBM-UHFFFAOYSA-N anthraquinone Natural products CCC(=O)c1c(O)c2C(=O)C3C(C=CC=C3O)C(=O)c2cc1CC(=O)OC PYKYMHQGRFAEBM-UHFFFAOYSA-N 0.000 claims 1
- 150000004056 anthraquinones Chemical class 0.000 claims 1
- 239000007864 aqueous solution Substances 0.000 claims 1
- 239000000460 chlorine Substances 0.000 claims 1
- 229910052801 chlorine Inorganic materials 0.000 claims 1
- 238000005108 dry cleaning Methods 0.000 claims 1
- 239000002440 industrial waste Substances 0.000 claims 1
- 150000002791 naphthoquinones Chemical class 0.000 claims 1
- 150000003839 salts Chemical class 0.000 claims 1
- 239000011265 semifinished product Substances 0.000 claims 1
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 4
- 239000000654 additive Substances 0.000 description 2
- 230000000996 additive effect Effects 0.000 description 2
- 229910052742 iron Inorganic materials 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- 230000002378 acidificating effect Effects 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 230000001079 digestive effect Effects 0.000 description 1
- 230000007935 neutral effect Effects 0.000 description 1
- 150000002894 organic compounds Chemical class 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 238000005554 pickling Methods 0.000 description 1
- 239000010802 sludge Substances 0.000 description 1
- 150000003464 sulfur compounds Chemical class 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Description
W zuzytej zas masie czyszczacej, której sklad sta¬ nowi przykladowo 40% rudy darniowej + 60% osadów potrawiennych; 50% rudy darniowej + 50% osadów potrawiennych; 60% rudy darniowej + 40% osadów potrawiennych uaktywnionych wo¬ da odpadowa z generatora dwugazu typu „Viag", zawartosc siarki podnosi sie od 55% siarki do 62% w porównaniu z masami bez tego dodatku. 5 Przy zastosowaniu samych osadów potrawiennych uaktywnionych równiez woda odpadowa z gene¬ ratora dwugazu typu „Viag" zawartosc siarki w masie zuzytej wzrasta od 46% do 74% siarki w porównaniu z masami bez tego dodatku.Stwierdzono, ze proces usuwania zwiazków siarki z gazów przy zastosowaniu mas czyszczacych otrzymanych sposobem wedlug wynalazku moze byc prowadzony w srodowisku zasadowym, obo¬ jetnym lub kwasnym.Stwierdzono, ze optymalne stezenie roztworów wodnych przenosników tlenu stosowanych do uaktywnienia mas czyszczacych miesci sie w gra¬ nicach od 0,001 g do 5 g zwiazku organicznego na 100 ml wody. PLIn the cleaning mass used, the composition of which is, for example, 40% of bog iron ore + 60% of post-pickling deposits; 50% bog ore + 50% post-digestion deposits; 60% of bog iron + 40% of digestive sludge activated by the waste water from the Viag type two gas generator, the sulfur content rises from 55% of sulfur to 62% compared to the masses without this additive. The sulfur content in the waste mass waste from the Viag-type two gas generator increases from 46% to 74% of sulfur compared to the masses without this additive. It has been found that the process of removing sulfur compounds from gases using the cleaning masses according to the invention may carried out in an alkaline, neutral or acidic environment. It has been found that the optimal concentration of the aqueous oxygen carrier solutions used to activate the cleaning masses is within the limits of 0.001 g to 5 g of organic compound per 100 ml of water. PL
Claims (1)
Publications (1)
| Publication Number | Publication Date |
|---|---|
| PL48151B1 true PL48151B1 (en) | 1964-04-15 |
Family
ID=
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| GB1420504A (en) | Process for purifying effluents | |
| US7906027B2 (en) | Mercury removal process | |
| CH612159A5 (en) | Process for removing oxygen dissolved in water and solutions usable for this purpose | |
| FR2442820A1 (en) | IMPROVED PROCESS FOR PURIFYING BROMINATED ORGANIC PRODUCTS | |
| PL48151B1 (en) | ||
| FR2528041B1 (en) | ||
| JP2003245678A (en) | Wastewater treatment method using catalyst | |
| JP7341633B2 (en) | How to purify organically contaminated soil | |
| FI854447A0 (en) | FOERFARANDE SOM DELVIS SKER I TORRT TILLSTAOND FOER ATT KVARHAOLLA FOERORENANDE AEMNEN I ROEKGASEN. | |
| CN105177192B (en) | Deliming without ammonium agent and leather deliming without ammonium technique | |
| GB1089136A (en) | Improvements relating to the production of sulphonic acids | |
| GB497708A (en) | Improvements in or relating to the production and use of cation-exchange material | |
| SU1544498A1 (en) | Method of removing harmful admixtures from mineral resources | |
| SU1662939A1 (en) | Method of dechlorination and debromination of water | |
| SU889632A1 (en) | Method of treatment of boller waste water | |
| RU97106876A (en) | METHOD FOR CLEANING GAS CONDENSATE, OIL AND OIL PRODUCTS FROM HYDROGEN HYDROGEN | |
| DE721892C (en) | Process for the production of organic sulfur compounds | |
| US2522140A (en) | Method of breaking emulsions to recover wool fat | |
| SU1239485A1 (en) | Method of drying porous materials | |
| MD613G2 (en) | Process for 2 - mercapto - 1,3,4 - oxadiasols preparation | |
| SU551259A1 (en) | Composition for water dechlorination | |
| SU994772A1 (en) | Dust-suppression composition | |
| SU1194849A1 (en) | Method of water dehalogenation | |
| SU1238883A1 (en) | Method of recovery of waste sand | |
| ES431788A1 (en) | Process for the manufacture of 1,3-bis- beta-ethylhexyl- 5-amino-5-methyl-hexahydropyrimidine and a derivative of the 5-nitro analogue thereof |