PL4232B1 - Method for cleaning gases from coke ovens and similar gases. - Google Patents
Method for cleaning gases from coke ovens and similar gases. Download PDFInfo
- Publication number
- PL4232B1 PL4232B1 PL4232A PL423224A PL4232B1 PL 4232 B1 PL4232 B1 PL 4232B1 PL 4232 A PL4232 A PL 4232A PL 423224 A PL423224 A PL 423224A PL 4232 B1 PL4232 B1 PL 4232B1
- Authority
- PL
- Poland
- Prior art keywords
- gases
- soda
- coke ovens
- hydrocarbons
- fact
- Prior art date
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- 239000007789 gas Substances 0.000 title claims description 12
- 238000000034 method Methods 0.000 title claims description 8
- 239000000571 coke Substances 0.000 title claims description 3
- 238000004140 cleaning Methods 0.000 title 1
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 claims description 12
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 claims description 6
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 claims description 6
- 229910021529 ammonia Inorganic materials 0.000 claims description 6
- 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 claims description 4
- PEDCQBHIVMGVHV-UHFFFAOYSA-N Glycerine Chemical compound OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 claims description 4
- 229930003836 cresol Natural products 0.000 claims description 4
- 229930195733 hydrocarbon Natural products 0.000 claims description 4
- 150000002430 hydrocarbons Chemical class 0.000 claims description 4
- 239000007788 liquid Substances 0.000 claims description 3
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 claims description 2
- 239000005977 Ethylene Substances 0.000 claims description 2
- 238000010521 absorption reaction Methods 0.000 claims description 2
- 239000003054 catalyst Substances 0.000 claims description 2
- 239000000295 fuel oil Substances 0.000 claims description 2
- 235000011187 glycerol Nutrition 0.000 claims description 2
- 229910052751 metal Inorganic materials 0.000 claims description 2
- 239000002184 metal Substances 0.000 claims description 2
- 239000007787 solid Substances 0.000 claims description 2
- 239000002904 solvent Substances 0.000 claims description 2
- 150000001720 carbohydrates Chemical class 0.000 claims 1
- DXHPZXWIPWDXHJ-UHFFFAOYSA-N carbon monosulfide Chemical compound [S+]#[C-] DXHPZXWIPWDXHJ-UHFFFAOYSA-N 0.000 claims 1
- 230000005494 condensation Effects 0.000 claims 1
- 238000009833 condensation Methods 0.000 claims 1
- 238000000926 separation method Methods 0.000 claims 1
- 239000002253 acid Substances 0.000 description 4
- BVKZGUZCCUSVTD-UHFFFAOYSA-N carbonic acid Chemical compound OC(O)=O BVKZGUZCCUSVTD-UHFFFAOYSA-N 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- QAOWNCQODCNURD-UHFFFAOYSA-L Sulfate Chemical compound [O-]S([O-])(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-L 0.000 description 2
- NLXLAEXVIDQMFP-UHFFFAOYSA-N Ammonium chloride Substances [NH4+].[Cl-] NLXLAEXVIDQMFP-UHFFFAOYSA-N 0.000 description 1
- VHUUQVKOLVNVRT-UHFFFAOYSA-N Ammonium hydroxide Chemical compound [NH4+].[OH-] VHUUQVKOLVNVRT-UHFFFAOYSA-N 0.000 description 1
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 1
- RWSOTUBLDIXVET-UHFFFAOYSA-N Dihydrogen sulfide Chemical compound S RWSOTUBLDIXVET-UHFFFAOYSA-N 0.000 description 1
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-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
- 235000011114 ammonium hydroxide Nutrition 0.000 description 1
- 230000001627 detrimental effect Effects 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 229910000037 hydrogen sulfide Inorganic materials 0.000 description 1
- 239000003921 oil Substances 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 230000000717 retained effect Effects 0.000 description 1
- 229910052708 sodium Inorganic materials 0.000 description 1
- 239000011734 sodium Substances 0.000 description 1
- 229910021653 sulphate ion Inorganic materials 0.000 description 1
Description
PierwMftiBtwec 17 listopad* 1925 jv C£a»ci&,).Jak wiadomo, kwes*ja wstepnego oczy¬ szczenia wychodzacych z piecówkoksowyeh gazów, które podlegaja oddzieleniu zapo- naoca ekrapiania, ie*t nader wazna.Przedstawimy wynalazek wskazuje kil¬ ka sposobów do zastosowania w zupelnosci lub czesciowo.Gazy pozbawione smoly sa poddawane sile odsrodkowej w celu oddzielenia me¬ chanicznie czesci plynnych i stalych. Spre¬ zone weglowodory dostaja sie przewaznie do wiezy zaopatrzonej pierscieniami Ra- schig'a, przez które przeplywa prad ciez¬ kich olei wtlaczanych pompa, Z olei, u- suwanych z wiezy, otrzymuje sie benzol,, ^ Reszte weglowodorów zabiera do dru¬ giej wiety z pierscieniami Rasehig'a krezol lub inny odpowiedni rozpuszczalnik, Kre¬ zol poddaje sie odpowiedniej temperaturze w celu usuniecia drobnych ilosci pochlon nietych cial i wprpwadza sie ponownie do obiegu. Pochloniete przez krezol niewielkie ilosci cial wogóle nie warto wydzielac, lecz moglyby one utrudniac prace aparatów skraplajacych.Kwas weglowy w kolumnie z pierscie¬ niami Raschig'a zabiera sie zapomoca cyr¬ kulujacego roztworu amonjakalnego.. Roz¬ twór odswieza sie nastepnie wedlug sposo¬ bu opatentowanego we Francji, mianowi¬ cie: „Sposobu usuwania kwasu weglowe¬ go, a ewentualnie siarkowodoru z gazów,zawierajacych takowy, przy ciagiem od¬ swiezaniu cieczy pochlaniajacej", albo tez destyluje sie w celu wydzielenia amonjaku i przeslania go do aparatów, w których u- lega przetworzeniu na siarczany lub inne produkty. Reszta amonjaku z gazów w wie¬ zy (lub w przedluzeniu poprzedniej) zosta¬ je pochlonieta cyrkulujaca woda. W wy¬ padku wskazanym w nawiasie, wode spo- zytkówuje sie do roztworu amonjakalnego.W celu dokladniejszego pochloniecia kwasu weglowego, uzupelnia sie dzialanie amo¬ njaku roztworem sody w innej kolumnie.Dodajac do sody w pewnym stosunku gliceryne, ulatwia sie jednoczesnie pochla¬ nianie siarkowodoru.Gazy traktowane tym sposobem, prócz wilgoci, moga jeszcze zawierac slady sody i amonjaku, nalezy zatem najdokladniej je usunac.W tym celu w ostatniej kolumnie mozna je poddac dzialaniu pradu kwasu siarcza- nego, który wywiera potrójny efekt, t. j. wysusza, usuwa slady sody i amonjaku.Sposób suszenia jest wskazany szcze¬ gólnie w razie, gdy trzeba przetworzyc a- monjak w siarczan. Stosuje sie. wówczas bardzo duze ilosci kwasu siarczanego, któ¬ re przechodza przez kolumne, tracac nie¬ wiele wody, tak, ze stezony kwas nie dzia¬ la szkodliwie na metalowe scianki apara¬ tów. Ponadto, dodany do kwasu w bardzo malej ilosci katalizator pozwala kwasowi na szybkie pochlanianie pod cisnieniem znacznej czesci etylenu, który mozna prze¬ tworzyc na alkohol. Kwas siarczany po¬ rywany gazami, zatrzymuje sie w dodatko- wem naczyniu, zawieraj acem w razie po¬ trzeby sode w stanie twardym. PLFirstMftiBtwec November 17, 1925 jv C £ a »ci &,). As is known, the question of the preliminary purification of coke oven gases, which are separated by an anti-scratch method, is very important. We will present the invention in several ways. to be used in whole or in part. Tar-free gases are subjected to centrifugal force to mechanically separate the liquid and solid parts. The compressed hydrocarbons usually get to the tower equipped with Rschig rings, through which the current of heavy oils injected by the pump flows. From the oils, removed from the tower, benzol is obtained, and the rest of the hydrocarbons are taken to the second Fresh with Rasehig's rings cresol or other suitable solvent, the Cresol is subjected to an appropriate temperature to remove small amounts of absorbed non-bodies and recirculated. Small amounts of bodies absorbed by the cresol are not worth separating, but they could hinder the operation of the condensers. The carbonic acid in the Raschig ring column is taken with a circulating ammoniacal solution. The solution is then refreshed according to the method patented in France, namely: "A method of removing carbonic acid, and possibly hydrogen sulfide from gases containing it, while continuously refreshing the absorbing liquid", or it is also distilled to separate the ammonia and send it to apparatus in which The rest of the ammonia from the gases in the tower (or in the extension of the previous one) is absorbed into the circulating water. In the case indicated in the brackets, the water is put into an ammonia solution. a more precise absorption of carbonic acid is supplemented by the action of ammonia with a solution of soda in another column. By adding glycerin to the soda in a certain ratio, it is easier Gases treated in this way, apart from moisture, may still contain traces of soda and ammonia, so they should be removed most thoroughly. For this purpose, in the last column, they can be subjected to the action of a current of sulfuric acid, which has a triple effect, i.e. dries, removes traces of soda and ammonia. The method of drying is particularly advisable when it is necessary to transform the mono into sulphate. Apply. then very large amounts of sulfuric acid which pass through the column, losing little water, so that the concentrated acid is not detrimental to the metal walls of the apparatus. Moreover, a very small amount of the catalyst added to the acid allows the acid to rapidly absorb, under pressure, a significant portion of the ethylene which can be converted into alcohol. The sulfate acid, entrained with gases, is retained in an additional vessel containing, if necessary, hard sodium. PL
Claims (3)
Publications (1)
| Publication Number | Publication Date |
|---|---|
| PL4232B1 true PL4232B1 (en) | 1926-04-30 |
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