PL4232B1 - Method for cleaning gases from coke ovens and similar gases. - Google Patents

Method for cleaning gases from coke ovens and similar gases. Download PDF

Info

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
Application number
PL4232A
Other languages
Polish (pl)
Filing date
Publication date
Application filed filed Critical
Publication of PL4232B1 publication Critical patent/PL4232B1/en

Links

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)

Zastrzezenia patentowe. 1. Sposób oczyszczania gazów z pieców koksowych i gazów analogicznych, oddzie¬ lonych skraplaniem, znamienny tern, ze po usunieciu smoly stosuje sie mechaniczne oddzielanie czesci stalych i plynnych, za- pomoca sily odsrodkowej, przyczem spre¬ zone weglowodory podlegaja rozdzieleniu zapomoca ciezkich olei tak, ze reszta we¬ glowodorów moze byc wydzielana krezo¬ lem lub innym analogicznym rozpuszczal¬ nikiem.Patent claims. 1. The method of purifying gases from coke ovens and analogous gases, separated by condensation, characterized by the fact that after removing the tar, mechanical separation of solid and liquid parts by means of centrifugal force is applied, because the compressed hydrocarbons are separated by heavy oils, thus that the remainder of the hydrocarbons may be isolated with cresol or other analogous solvent. 2. Sposób wedlug zastrz. 1, znamien¬ ny tern, ze po pochlonieciu kwasu weglo¬ wego oddzialywuje sie na gaz soda z do¬ datkiem gliceryny, która usuwa siarczek wegla.2. The method according to claim 1, characterized by the fact that after the absorption of the carbohydrate, soda with the addition of glycerin interacts with the gas to remove the carbon sulfide. 3. Sposób wedlug zastrz. 1 i 2, zna¬ mienny tern, ze gaz oczyszcza sie kwasem siarczanym w aparatach metalowych w ce¬ lu wysuszenia i pozbawienia sladów sody oraz amonjaku przyczem stosuje sie kata¬ lizator, pochlaniajacy etylen. ,,L' Air Liauide", S-te anonyme pour PEtude et 1 'Exploitat io n des Procedes Georges Claude, Zastepca: I. Myszczynski, rzecznik patentowy. PL3. The method according to p. 1 and 2, the significant point that the gas is purified with sulfuric acid in metal apparatuses in order to dry it and remove traces of soda and ammonia, using a catalyst that absorbs ethylene. ,, L 'Air Liauide ", S-te anonyme pour PEtude et 1' Exploitat io n des Procedes Georges Claude, Deputy: I. Myszczynski, patent attorney. PL
PL4232A 1924-10-21 Method for cleaning gases from coke ovens and similar gases. PL4232B1 (en)

Publications (1)

Publication Number Publication Date
PL4232B1 true PL4232B1 (en) 1926-04-30

Family

ID=

Similar Documents

Publication Publication Date Title
US1422007A (en) Method of stripping the illuminants from and of purifying coal gas by means of charcoal
US3324627A (en) Process for the purification of gases
US3505784A (en) Scrubbing process for removing carbon dioxide from low-sulfur fuel gases or synthesis gases
CN102181308B (en) Vacuum potassium carbonate coke oven gas desulfurization-sulfuric acid preparation process and processing system thereof
DE2226215C3 (en) Process for the regeneration of a loaded absorbent which is obtained when acidic components are washed out of gases
CN103589462A (en) Technological method for purifying coal oven gas and recovering chemical products
US3492788A (en) Process of separating solvent vapor and water vapor from gases in scrubbing processes using a liquid organic absorbent
CN102824823B (en) Liquid phase load type gas desulfurizing agent
US3120993A (en) Gas purification process
GB1300669A (en) Improvements in or relating to the removal of carbon dioxide and/or hydrogen sulphide from cracked gases
DE2127768C3 (en) Process for the desulphurization of gases
US3787559A (en) Desulfurization of water-containing hot compressed gases
PL4232B1 (en) Method for cleaning gases from coke ovens and similar gases.
CN210057873U (en) Coking plant gas clean system VOCs tail gas processing apparatus
DE2912115B2 (en) Process for the selective desulphurization of gases
CN210751969U (en) Naphthalene-containing waste gas treatment system
US3554690A (en) Apparatus and method for removing carbon dioxide from process gases
US2638405A (en) Amine treating and dehydration of gases
US1717761A (en) Purification of coke-oven gases and the like
GB956179A (en) Acetylene recovery process
US3931389A (en) Process of desulfurizing hot gases
PL237732B1 (en) Device for cleaning of coke oven gas from naphthalene, ammonia and hydrogen sulfide
KR100864426B1 (en) How to Remove Hydrogen Emulsion from Coke Oven Gas
GB605634A (en) Improvements in or relating to the purification of coke oven gas
SU491235A3 (en) The method of extraction of methyl pyrrolidone from gases