PL780B1 - The method of pyrogenation of crude oil or its distillates. - Google Patents

The method of pyrogenation of crude oil or its distillates. Download PDF

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Publication number
PL780B1
PL780B1 PL780A PL78021A PL780B1 PL 780 B1 PL780 B1 PL 780B1 PL 780 A PL780 A PL 780A PL 78021 A PL78021 A PL 78021A PL 780 B1 PL780 B1 PL 780B1
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PL
Poland
Prior art keywords
oil
generators
pyrogenation
generator
distillates
Prior art date
Application number
PL780A
Other languages
Polish (pl)
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Publication date
Application filed filed Critical
Publication of PL780B1 publication Critical patent/PL780B1/en

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Do pirogenacji ropy sluza zwykle retorty (z zelaza lanego, stali lanej, szamotowe), pio¬ nowe lub poiziome, ogrzewane z zewnatrz do odpowiednio wysokiej temperatury. Retorty takie posiadaja powazne braki. Czeste pe¬ kanie retort, sszyibkie 'zuzywanie sie ich po¬ woduje znaczne koszty remontowe. Regulo¬ wanie temperatury poisz/czególinych retort w piecach przy wielkiej produkcji, wymiaga- jacej setek retort, jest trudne do urzeczy¬ wistnienia, co* ujemnie odbija sie na jakosci otrzymywanych produktów, np. na czystosci bemolu i toluollu.Praktyczniejsae w uzycki sa t. zw. „ge¬ neratory" do otrzymywatnia ga:zu z. ropy, w postaci sizybów, wypelnionych ogniotrwa¬ la cegla. Generatory takie pracuja okresowo: przez pewien czais sa ogrzewane, np. zapo- moca smoly z ropy lub gaziu generatorowego, a nastepnie sluza do pirogenowania wkra- planej do nich ropy.Aparaty takie sa w uzyciu tansze, prost¬ sze, posiadaja jednak ten brak, ze wzgled¬ nie sizybko zostaja ochlodzone' przez piroge- nowana rope i ze temperatura pirio»genaicji w kazdym okresie zmienia sie szybko, waha¬ jac sie w znacznych granicach.Sposób wykonania pirogenacji, wedlug niniejszego wynalazku, majacy glównie na celu pirogenowamie wielkich mas ropy, z za¬ stosowaniem generatorów i majacy na celu zapewnienie równomiernego dzialania ich. a glównie mozliwego zmniejisizenia wahan temperatury pirogenacji, polega na tern, ze caly szereg takich* generatorów (np. 5—6) laczy sie ze soba tak, ze pary, wytworzono z ropy, moga przechodzic z kazdego z nich do nastepnego.Prócz tego 'kazdy generator posiada do¬ plyw ropy, doplyw dla gazów, ogrzewaja¬ cych generator, polaczenie z kominem na czias ogrzewamia i polaczenie z, glówna rura, odprowadzajaca gaizy i pary po pirogenacji do chlodnic. Baterja1 generatorów,' nip. z 6 naczyn, pracuje w sposób ciagly i systema¬ tyczny jak nastepuje. W kazdym czasie je¬ den z generatorów, np. Nr. I jest wylaczony z dgólnego obiegu i poddany ogrzewaniu, np. przez spalarnie w nim gazu generatoro¬ wego, wychodzacego po ogrzaniu do» komina, ewentualnie uprzednio do regeneratora czy rekuperatoira, czy do pogrzewacza ropy i t. p.W tym samym czasie ropa idzie do genera¬ tora sasiedniego1, nastepny z kolei, Nr. II, przez otwarty odpowiedni zawór i przecho¬ dzi w. postaci pary przez, dalsze generatory III, IV... VI przy otwartych odpowiednich zasuwach. W kazdym z nastepnych genera¬ torów pary ropy pnzy ustalonym biegu ba- terji poddane zostaja dzialaniu'wciaz wzra¬ stajacych temperatur, az z generatora VI wychodza przegrzane ostatecznie, np. do 700° do chlodnic. W nastepnym okresie zo¬ staje wylaczony i poddany ogrzewaniu ge¬ nerator Nr. II (dó którego przedtem szla ropa), ropa idzie do generatora Nr. III, a produkty pirogenacji wychodza z ogrza¬ nego przedtem Nr. I. Wskazany sposób pi¬ rogenacji pozwala poddawac pary ropy dzia¬ laniu temperatur stopniowo wzrastajacych az do ustalonej przez doswiadczenie tempe¬ ratury najwyzszej. Badania wykazaly, ze ta¬ kie stopniowe podnoszenie temperatury par ropy zapewnia lepszy wydatek weglowodo- rów aromatycznych, szczególniej benzolu i toluolu. Prócz tego, poniewaz na kazdy z generatorów wypada tylko czesc calkowi¬ tej pracy przegrzania par ropy (np. o 50°), sposób taki pozwala, utrzymywac dosyc stala temperature ostatecznego przegrzania, waha¬ jaca sie w granicach 20—40°. Poniewaz wpu¬ szczanie zimnej ropy do ostatniego z gene¬ ratorów zinacznieby go oziebialo, co naruszy¬ loby szybko prawidlowosc pracy baterji, przeto uzupelniamy baterje przez zastosowa¬ nie sposobu wykonania pirogenaicji, bedace¬ go przedmiotem oddzielnego zgloszenia, i po¬ legajacego na tern, ze rope w postaci cieczy przed wprowadzeniem do wlasciwego apa¬ ratu pirogenacyjnego poddajemy przegrzar niu do 400—500° (np. zapomoca gazów spa¬ linowych, uchodzacych z ogrzewanego gene¬ ratora) pod znacznem cisnieiniem, np. 20 do 25 atm. Wtedy ropa, wpuszczona do gene¬ ratora, dostajac sie pod zwykle cisnienie od¬ parowuje przewaznie kosztem wlasnego cie¬ pla, przez co zostaje zaoszczedzone cieplo generatora. Prócz tego takie wprowaidzainie ropy pozwala równomierniej • rozprowadzic ja w postaci pary w generatorze. PL PLOil pyrogenation is usually carried out by retorts (cast iron, cast steel, chamotte), vertical or horizontal, heated externally to a sufficiently high temperature. Such retorts have serious shortcomings. The frequent cracking of the retorts and their quick wear result in considerable repair costs. Controlling the temperature of individual retorts in furnaces in large-scale production, requiring hundreds of retorts, is difficult to implement, which has a negative impact on the quality of the products obtained, for example on the purity of the flat and toluol. . "Generators" for the supply of fuel tanks: crude oil, in the form of shafts, filled with refractory brick. Such generators are operated periodically: they are heated for some time, e.g. by using oil tar or generator gas, and then These devices are cheaper and simpler to use, but they have the shortage of being cooled relatively quickly by the pyrogenated rope and that the pyrogenic temperature changes rapidly in each period The method of pyrogenation according to the present invention, mainly aimed at pyrogenizing large masses of oil, with the use of generators and aimed at ensuring their even operation, and mainly possible reduction of pyrogenation temperature fluctuations, consists in The point is that a number of such generators (e.g., 5-6) are connected with each other so that the steam, made of oil, can pass from each of them to the next. crude oil flow, feed for gases that heat the generator, connection to the chimney, heats it, and connection to the main pipe, draining gases and pyrogenic vapors to coolers. Battery1 of generators, 'nip. with 6 vessels, it works continuously and systematically as follows. At any one time, one of the generators, eg No. And it is disconnected from the general circulation and subjected to heating, e.g. by incinerators of the producer gas in it, leaving after heating the stack, possibly previously to the regenerator or recuperator, or to the oil heater, etc. At the same time, the oil goes to the generator neighboring1, the next one, No. II, through the open corresponding valve and passes in the form of steam through the further generators III, IV ... VI with the respective sliders open. In each of the following oil steam generators, the pipes following a predetermined course are subjected to the action of constantly rising temperatures, and finally superheated, for example up to 700 °, to coolers emerge from the generator VI. In the next period, the generator No. 5 is turned off and heated. II (where the oil was previously poured), the oil goes to the generator No. III, and the pyrogenation products come out of the previously heated No. I. The indicated method of pyrogenation allows the oil vapor to be subjected to the action of gradually increasing temperatures up to the highest temperature determined by experiment. Studies have shown that such a gradual increase in the temperature of the oil vapor provides a better expenditure of aromatic hydrocarbons, especially benzol and toluol. Moreover, since each of the generators only takes a part of the total work of superheating the oil vapor (eg by 50 °), this method allows the final superheat temperature to be kept fairly constant, ranging from 20 to 40 °. Since injection of cold oil into the last of the generators would cool it down, which would quickly compromise the correct operation of the battery, we replenish the batteries by applying a pyrogenetic method, which is the subject of a separate notification, and which lies on the ground if the rope in the form of a liquid is subjected to overheating to 400-500 ° (eg by means of flue gases coming from a heated generator) before being introduced into a proper pyrogen apparatus, under a significant pressure, for example from 20 to 25 atm. Then the oil admitted to the generator, getting under the usual pressure, evaporates mostly at the expense of its own heat, thus saving the generator's heat. In addition, this introduction of oil allows it to be • distributed more evenly in the form of steam in the generator. PL PL

Claims (1)

1. Zastrzezenie patentów e, Sposób pirogenacji ropy lub jej destyla¬ tów, tern! znamienny, ze do pirogenacji sluzy baterja polaczonych z soba generatorów, przyczem w kazdym czasie jeden z genera¬ torów, wylaczony wtedy z ogólnego obiegu, jest ogrzewany, ropa zas, dostajaca sie do sasiedniego najbardziej wystudzonego gene¬ ratora, przechodzi w postaci pary przez po¬ zostale generatory o stopniowo wzrastajacej temperaturze, a z ostatniego generatora ga¬ zy i pary ostatecznie przegrzane daza do skraplaczy. Kazimierz Smolenski. PL PL1. Claiming for patents. Method of pyrogenating crude oil or its distillates. characterized by the fact that a battery of generators connected with each other is used for pyrogenation, while at any time one of the generators, then excluded from the general circulation, is heated, and the oil, getting to the next coolest generator, passes in the form of steam through the Generators with gradually increasing temperature were left, and from the last generator of gas and steam, ultimately superheated flows to the condensers. Kazimierz Smolenski. PL PL
PL780A 1921-06-03 The method of pyrogenation of crude oil or its distillates. PL780B1 (en)

Publications (1)

Publication Number Publication Date
PL780B1 true PL780B1 (en) 1924-10-31

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