PL2385B1 - A method of producing methyl alcohol or other oxygen-containing organic compounds from carbon oxides. - Google Patents
A method of producing methyl alcohol or other oxygen-containing organic compounds from carbon oxides. Download PDFInfo
- Publication number
- PL2385B1 PL2385B1 PL2385A PL238523A PL2385B1 PL 2385 B1 PL2385 B1 PL 2385B1 PL 2385 A PL2385 A PL 2385A PL 238523 A PL238523 A PL 238523A PL 2385 B1 PL2385 B1 PL 2385B1
- Authority
- PL
- Poland
- Prior art keywords
- organic compounds
- oxygen
- methyl alcohol
- containing organic
- carbon oxides
- Prior art date
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- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 title claims description 9
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical class [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 title claims description 8
- 238000000034 method Methods 0.000 title claims description 8
- 229910052760 oxygen Inorganic materials 0.000 title claims description 3
- 239000001301 oxygen Substances 0.000 title claims description 3
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 title claims 2
- 229910002090 carbon oxide Inorganic materials 0.000 title claims 2
- 150000002894 organic compounds Chemical class 0.000 title claims 2
- 239000007789 gas Substances 0.000 claims description 18
- 238000000746 purification Methods 0.000 claims description 8
- 239000001257 hydrogen Substances 0.000 claims description 7
- 229910052739 hydrogen Inorganic materials 0.000 claims description 7
- 239000000203 mixture Substances 0.000 claims description 7
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims description 5
- 229930195733 hydrocarbon Natural products 0.000 claims description 4
- 150000002430 hydrocarbons Chemical class 0.000 claims description 4
- 239000004215 Carbon black (E152) Substances 0.000 claims description 2
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 claims description 2
- 238000006243 chemical reaction Methods 0.000 claims description 2
- 150000002506 iron compounds Chemical class 0.000 claims description 2
- 231100000572 poisoning Toxicity 0.000 claims description 2
- 230000000607 poisoning effect Effects 0.000 claims description 2
- PAYRUJLWNCNPSJ-UHFFFAOYSA-N Aniline Chemical compound NC1=CC=CC=C1 PAYRUJLWNCNPSJ-UHFFFAOYSA-N 0.000 claims 1
- 230000003197 catalytic effect Effects 0.000 claims 1
- 238000004519 manufacturing process Methods 0.000 claims 1
- 239000012495 reaction gas Substances 0.000 claims 1
- 229910002091 carbon monoxide Inorganic materials 0.000 description 6
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 4
- 229910052717 sulfur Inorganic materials 0.000 description 4
- 239000011593 sulfur Substances 0.000 description 4
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 3
- 229940087654 iron carbonyl Drugs 0.000 description 3
- -1 oxygen organic compounds Chemical class 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 2
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 2
- 229910002092 carbon dioxide Inorganic materials 0.000 description 2
- 238000004140 cleaning Methods 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
- 150000002431 hydrogen Chemical class 0.000 description 2
- 239000004615 ingredient Substances 0.000 description 2
- 150000002898 organic sulfur compounds Chemical class 0.000 description 2
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 1
- 235000008733 Citrus aurantifolia Nutrition 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
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 1
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 description 1
- 235000011941 Tilia x europaea Nutrition 0.000 description 1
- IJCVBMSXIPFVLH-UHFFFAOYSA-N [C].S=O Chemical compound [C].S=O IJCVBMSXIPFVLH-UHFFFAOYSA-N 0.000 description 1
- 150000004945 aromatic hydrocarbons Chemical class 0.000 description 1
- 229910052785 arsenic Inorganic materials 0.000 description 1
- RQNWIZPPADIBDY-UHFFFAOYSA-N arsenic atom Chemical compound [As] RQNWIZPPADIBDY-UHFFFAOYSA-N 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 239000003054 catalyst Substances 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 239000000460 chlorine Substances 0.000 description 1
- 229910052801 chlorine Inorganic materials 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 239000000571 coke Substances 0.000 description 1
- 238000004939 coking Methods 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 239000000356 contaminant Substances 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 239000004571 lime Substances 0.000 description 1
- 125000002496 methyl group Chemical group [H]C([H])([H])* 0.000 description 1
- 239000003595 mist Substances 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 229910052698 phosphorus Inorganic materials 0.000 description 1
- 239000011574 phosphorus Substances 0.000 description 1
- 239000011591 potassium Substances 0.000 description 1
- 229910052700 potassium Inorganic materials 0.000 description 1
- 238000007086 side reaction Methods 0.000 description 1
Description
Pierwszenstwo: 5 kwietnia. 1923 r. (Niemej').Pokazalo sie, ze dzialaniem odpowied¬ nich katalizatorów na mieszanine gazów, skladajaca sie z tlenku lub dwutlenku we¬ gla i wodoru lub weglowodoru, pod cisnie¬ niem i w temperaturze wysokiej mozna o- trzymac z dobra wydajnoscia alkohol me¬ tylowy, a niekiedy i inne tlenowe zwiazki organiczne. Przy przeprowadzaniu tego sposobu w praktyce powstaja czestokroc trudnosci, polegajace na tern, ze masa tra¬ ci szybko swa aktywnosc lub tez powstaja niepozadane reakcje uboczne, np. wytwa¬ rzaja sie weglowodory w ilosci przewaza¬ jacej. Jak wykazaly badania, przyczyna tego zjawiska polega na niedostatecznem oczyszczaniu gazów, pomimo ze oczyszcza¬ nie to przeprowadzone w sposób zwykly z wielka starannoscia, a to z tego powodu, ze w tym wypadku koniecznem bywa u- wolnienie nietylko od siarkowych zwiaz¬ ków organicznych, lecz i od lotnych zwiaz¬ ków zelaza: w szczególnosci zas nalezy u- sunac z gazów slady karbonylku zelaza.Dopiero, gdy gazy zostana oczyszczone w tym stopniu, ze nawet -zapomeca najczul¬ szych srodków analitycznych nie mozna wykryc siarkowych zwiazków organicz¬ nych i lotnych zwiazków zelazowych, masa kontaktowa pracuje przez czas dosc dlugi i wytwarza sie alkohol metylowy oraz zwiazki jemu podobne.Sposób niniejszy umozliwia stosowanie rozmaitych gazów przemyslowych. Najko¬ rzystniej sklad tych gazów powinien byctaki, aby ilosc wodoru przekraczala ilosc tlenku wegla. Mozna np. stosowac gaz wodny o zawartosci 40% tlenku wegla, 55% wodoru, 4% azotu i 1% weglowodorów, lub tez gazy otrzymywane przy destylacji we¬ gla, jako to: gaz swietlny, gaz z koksowni, lub gaz, otrzymywany w niskiej tempera¬ turze koksowania lub tez mieszanine tych gazów, dodajac do niej przed lub po oczy¬ szczeniu, w miare potrzeby, brakujace ilo¬ sci poszczególnych skladników, np. wodo¬ ru lub tlenku wegla, lub tez usuwajac nad¬ miar niektórych z nich, dopóki nie zostanie osiagniety zadany sklad gazu, np. na 1 ob¬ jetosc- tlenku wegla 3 do 4 objetosci wo¬ doru. Weglowodory nienasycone i aroma¬ tyczne mozna przed ostatecznem oczy¬ szczaniem usunac.Do oczyszczania ostatecznego po u- przedniem usunieciu glównej ilosci zanie¬ czyszczen w sposób zwykly stosuje sie najbardziej skuteczne sposoby pracy. I tak np. w celu pochloniecia oksysiarczku we¬ gla (COS) i innych organicznych zwiazków siarkowych uzywa sie dostatecznie wiel¬ kiej ilosci wegla aktywowanego lub roz¬ klada zapomoca wapna sodowego lub po¬ tasowego, lub tez stosuje sie kolejno oba te srodki jednoczesnie. Mozna równiez przepuszczac gazy na goraco ponad masa zawierajaca alkalja. Najbardziej skutecz¬ na metoda oczyszczania polega na tern, ze gazy oczyszczane po zmieszaniu z para wodna przepuszcza sie ponad masa kon¬ taktowa, nadajaca sie do czesciowego przeksztalcania tlenku wegla i pary wodnej na dwutlenek wegla i wodór, wskutek cze¬ go siarkowe zwiazki organiczne rozkladaja sie, wytwarzajac siarkowodór, -który juz z latwoscia mozna usunac.Usuniecie z gazów karbonylku zelaza, który podczas zwyklego oczyszczania tych¬ ze od cial zatruwajacych kontakt nie tak latwo daje sie usunac, wymaga szczegól¬ nego oczyszczenia. W tym celu gazy pro¬ wadzi sie przez warstwe wegla aktywo¬ wanego szczególnie chciwie wchlaniajacego karbonylek zelaza lub tez przepuszcza sie na goraco ponad masa, zawierajaca miedz lub tez ponad kontaktem uprzednim i po¬ wstajaca mgle zelazna usuwa sie zapomo¬ ca filtrów.Oczyszczanie mieszaniny gazów mozna uskutecznic pod zwyklem cisnieniem lub po uprzedniem sprezeniu. Masa kontakto¬ wa nie powinna równiez zawierac siarki i innych skladników szkodliwych; w tym ce¬ lu, jak sie okazalo, najkorzystniej jest do¬ dac do masy pewna ilosc mocnych zasad lub skladników, wytwarzajacych te ostat¬ nie, wskutek czego nieznaczne ilosci siarki, chloru, fosforu, arsenu i t. p. skladników nie szkodza zupelnie, lub tez szkodza tyl¬ ko w stopniu nieznacznym, Aby uniknac ponownego zanieczyszczenia gazów oczy¬ szczonych lotnemi zwiazkami zelaza, naj¬ korzystniej jest komore reakcyjna, jak i czesci metalowe wewnatrz jej, pokryc two¬ rzywem lub wykonac z tworzywa odpor¬ nego na dzialanie tlenku wegla: tworzy¬ wem tym moze byc np. miedz. PLPriority: April 5. 1923 (Mute ') It has been shown that the action of suitable catalysts on a gas mixture consisting of carbon monoxide or dioxide and hydrogen or hydrocarbon under pressure and high temperature can produce alcohol with good yield methyl, and sometimes other oxygen organic compounds. In carrying out this process in practice, difficulties often arise, such as the fact that the mass of the loss becomes active rapidly or that undesirable side reactions arise, for example, hydrocarbons are produced in a predominant amount. As the research has shown, the reason for this phenomenon lies in the insufficient purification of gases, despite the fact that the purification was carried out in an ordinary manner with great care, because in this case it is sometimes necessary to free not only sulfur organic compounds, but also from volatile iron compounds: in particular, traces of iron carbonyl should be removed from the gases, only after the gases have been purified to such an extent that even the most sensitive analytical agents cannot detect organic sulfur compounds and volatile ferric compounds, the contact mass works for quite a long time and produces methyl alcohol and similar compounds. This method allows the use of a variety of industrial gases. Most preferably the composition of these gases should be such that the amount of hydrogen exceeds the amount of carbon monoxide. For example, it is possible to use a water gas containing 40% carbon monoxide, 55% hydrogen, 4% nitrogen and 1% hydrocarbons, or gases obtained by distilling coal, such as: light gas, coke oven gas, or gas obtained in low temperature coking or a mixture of these gases, adding to it before or after purification, as necessary, the missing amounts of individual components, e.g. hydrogen or carbon monoxide, or removing excess of some of them until the desired gas composition is reached, for example, per 1 volume of carbon monoxide, 3 to 4 volumes of hydrogen. Unsaturated and aromatic hydrocarbons may be removed prior to the final purification. For the final purification, the most effective working methods are usually employed for the final purification prior to removing the major amount of contaminants. For example, in order to absorb carbon oxysulphide (COS) and other organic sulfur compounds, a sufficiently large amount of activated carbon is used, or soda or potassium lime is decomposed, or both are used sequentially simultaneously. You can also pass the gasses hot over a mass containing alkaline. The most effective method of purification is that the gases to be treated, when mixed with water vapor, are passed over the contact mass, suitable for the partial conversion of carbon monoxide and water vapor into carbon dioxide and hydrogen, as a result of which sulfur organic compounds decompose The removal of iron carbonyl from gases, which is not so easily removed from contact poisoning bodies during normal cleaning, requires a special cleaning process to produce hydrogen sulphide, which can easily be removed. For this purpose, the gases are led through a layer of activated carbon, which absorbs the iron carbonyl, or passed hot over the mass containing copper or also over the previous contact, and the resulting iron mist is removed without filtering the mixture. gases can be compressed under normal pressure or with prior compression. The contact mass should also not contain sulfur and other harmful components; for this purpose, it has turned out to be most advantageous to add to the mass a certain amount of strong bases or ingredients that produce the latter, so that small amounts of sulfur, chlorine, phosphorus, arsenic, and other ingredients do not completely or damage only insignificantly. this could be, for example, copper. PL
Claims (2)
Publications (1)
| Publication Number | Publication Date |
|---|---|
| PL2385B1 true PL2385B1 (en) | 1925-07-31 |
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