WO1987005620A1 - Process for liquefying carbonaceous materials - Google Patents
Process for liquefying carbonaceous materials Download PDFInfo
- Publication number
- WO1987005620A1 WO1987005620A1 PCT/AT1986/000023 AT8600023W WO8705620A1 WO 1987005620 A1 WO1987005620 A1 WO 1987005620A1 AT 8600023 W AT8600023 W AT 8600023W WO 8705620 A1 WO8705620 A1 WO 8705620A1
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- WO
- WIPO (PCT)
- Prior art keywords
- hydrogen
- coal
- gaseous
- carbon
- solid carbon
- Prior art date
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Classifications
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G1/00—Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal
- C10G1/06—Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal by destructive hydrogenation
Definitions
- the invention relates to a method for producing liquid hydrocarbon compounds from gaseous substances and carbon present in solid form.
- the invention relates to a process for the production of liquid hydrocarbons from gaseous hydrocarbons such as methane, propane, butane, ethylene and the like, and from carbon which is in solid form such as graphite, wood, charcoal, coal, coke.
- the invention aims to show a new, technically and economically advantageous way of liquefying coal.
- the processes known for liquefying the coal can be divided into three groups.
- One group is formed by the well-known Fischer-Tropsch synthesis and its variants.
- a synthesis gas containing carbon monoxide and hydrogen is first formed from the coal, and the liquid products are produced therefrom by means of contact catalysis.
- the coal is hydrogenated to liquid products (Chem.Ing.Techn. 46, 925 [1974]).
- the third group is formed by those processes in which the liquid products are extracted from the coal with solvents, advantageously with solvents having a high hydrogen content. This extraction process is also used in combination with coal hydrogenation (NIMDOK suinformation der Chemieindustrie, Budapest, 1975/1).
- the majority of the hydrogen required in the known process for the recovery of liquid hydrocarbons is obtained from water gas and the remaining requirement for hydrogen comes from the volatile constituents of the coal, which are obtained in coal gasification.
- coal with a high proportion of volatile constituents is preferred, not least because the production of hydrogen represents the greatest cost factor in all previously known processes.
- the hydrogen is obtained either electrolytically or from water gas.
- reaction according to equation 2 is preferably carried out under the influence of catalysts (e.g. iron, chromium) at around 400 ° C.
- catalysts e.g. iron, chromium
- the aim of the present invention is to provide a process with which liquid hydrocarbon compounds, in particular from coal, can be obtained much more easily than is the case with the known processes.
- the invention proposes, in a process for the synthesis of liquid hydrocarbons, a C / H ratio of 1: 1 (eg C 6 H 6 ) to approximately 1: 2.1 (eg C 12 H 26 ) and above (eg heavy oils and liquid hydrocarbons with multiple bonds) have, from solid carbon and a hydrogen carrier the hydrogen requirement from gaseous hydrocarbons, eg methane, propane, butane and the like.
- gaseous hydrocarbons do not occur as intermediates in the synthesis process, rather they are fed into the process as raw materials together with solid carbon particles.
- the free hydrogen can be obtained from the gaseous hydrocarbons by thermal dissociation with or without a catalyst at normal pressure or else at elevated pressure.
- the reaction Since the reaction is exothermic to the right, cooling is required during the reaction process.
- the dissipated heat can be used to heat or preheat the starting products (gases + solid carbon particles).
- the further process is based on known processes for the fractional condensation of liquid hydrocarbons.
- the process according to the invention not only enables the coal to be made fully usable for the actual coal liquefaction, it also permits the sensible use of amounts of gaseous hydrocarbons, for example natural gas, which are often available in excess or are available, and which often have to be flared due to the lack of further processing options.
- gaseous hydrocarbons for example natural gas
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- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Life Sciences & Earth Sciences (AREA)
- Wood Science & Technology (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Abstract
Process for producing liquid hydrocarbons by the reaction of solid carbon-containing materials with a gaseous hydrogen-containing substance. The solid carbon-containing material used may be in the form of graphite, wood, charcoal, carbon, coke, etc. in particle form which is applied in combination with a gaseous hydrocarbon providing free hydrogen, such as methane, propane, butane, ethylene, etc. In this way it is not necessary to produce hydrogen by synthesis, which required the use of a substantial part of the carbon used for the carbonaceous material production of water gas.
Description
KohleverflüssigungCoal liquefaction
Die Erfindung betrifft ein Verfahren zur Herstellung flüssiger Kohlenwasserstoffverbindungen aus gasförmigen Stoffen und in fester Form vorliegendem Kohlenstoff. Im speziellen bezieht sich die Erfindung auf ein Verfahren zur Herstellung von flüssigen Kohlenwasserstoffen aus gasförmigen Kohlenwasserstoffen wie Methan, Propan, Butan, Ethylen und dgl. und aus Kohlenstoff, der in fester Form vorliegt, wie Graphit, Holz, Holzkohle, Kohle, Koks. Im besonderen zielt die Erfindung darauf ab, einen neuen, technisch und wirtschaftlich vorteilhaften Weg zur Verflüssigung von Kohle aufzuzeigen.The invention relates to a method for producing liquid hydrocarbon compounds from gaseous substances and carbon present in solid form. In particular, the invention relates to a process for the production of liquid hydrocarbons from gaseous hydrocarbons such as methane, propane, butane, ethylene and the like, and from carbon which is in solid form such as graphite, wood, charcoal, coal, coke. In particular, the invention aims to show a new, technically and economically advantageous way of liquefying coal.
Die zur Verflüssigung der Kohle bekannten Verfahren können in drei Gruppen eingeteilt werden. Die eine Gruppe wird von der bekannten Fischer-Tropsch-Synthese und ihren Varianten gebildet. Bei diesen Verfahren wird aus der Kohle zuerst ein Kohlenmonoxid und Wasserstoff enthaltendes Synthesegas gebildet, und aus diesem werden mittels Kontaktkatalyse die flüssigen Produkte erzeugt.The processes known for liquefying the coal can be divided into three groups. One group is formed by the well-known Fischer-Tropsch synthesis and its variants. In these processes, a synthesis gas containing carbon monoxide and hydrogen is first formed from the coal, and the liquid products are produced therefrom by means of contact catalysis.
Bei der zweiten Gruppe der Verfahren wird die Kohle zu flüssigen Produkten hydriert (Chem.Ing.Techn. 46, 925 [1974]). Die dritte Gruppe wird von denjenigen Verfahren gebildet, bei denen die flüssigen Produkte mit Lösungsmitteln, zweckmäßig mit Lösungsmitteln hohen Wasserstoffgehaltes, aus der Kohle extrahiert werden. Dieses Extraktionsverfahren wird auch in Kombination mit der Kohlehydrierung angewendet (NIMDOK Fachinformationen der Chemieindustrie, Budapest, 1975/1).In the second group of processes, the coal is hydrogenated to liquid products (Chem.Ing.Techn. 46, 925 [1974]). The third group is formed by those processes in which the liquid products are extracted from the coal with solvents, advantageously with solvents having a high hydrogen content. This extraction process is also used in combination with coal hydrogenation (NIMDOK Fachinformation der Chemieindustrie, Budapest, 1975/1).
Die bekannten Verfahren haben unter dem Aspekt der industriellen Durchführbarkeit zahlreiche Nachteile. Die auf der Extraktion der Kohle beruhenden Verfahren arbeiten mit geringer Ausbeute, ihr spezifischer (auf eine Einheit flüssiges Verfahrensprodukt bezogener) Energiebedarf ist äußerst hoch, und die Regeneration des Extraktionsmittels verteuert das Verfahren noch mehr. Zur Fischer-Tropsch-Synthese und zur Kohlehydrierung werden außerordentlich
teure Vorrichtungen und viel Energie verbraucht, und der thermische Wirkungsgrad der Verfahren ist nicht zufriedenstellend. Nachteilig ist ferner, daß die genannten Verfahren unter hohem Druck arbeiten, was weitere teuere Vorrichtungen und außerdem die Einhaltung gewisser Sicherheitsmaßnahmen erfordert.The known methods have numerous disadvantages in terms of industrial feasibility. The processes based on the extraction of the coal operate with low yield, their specific energy requirement (based on a unit of liquid process product) is extremely high, and the regeneration of the extractant makes the process even more expensive. For Fischer-Tropsch synthesis and for carbohydrate hydrogenation are extraordinary expensive devices and a lot of energy are consumed, and the thermal efficiency of the processes is unsatisfactory. Another disadvantage is that the methods mentioned work under high pressure, which requires more expensive devices and also the compliance with certain safety measures.
Hinzu kommt, daß der Großteil des Wasserstoffes, der in dem bekannten Verfahren zur Gewinnung flüssiger Kohlenwasserstoffe benötigt wird, aus Wassergas gewonnen wird und der Restbedarf an Wasserstoff aus den flüchtigen Bestandteilen der Kohle stammt, die bei der Kohlevergasung anfallen. Um den Wasserstoffbedarf im herkömmlichen Verfahrensgang zu vermindern, werden Kohlen mit hohem Anteil an flüchtigen Bestandteilen bevorzugt, nicht zuletzt deshalb, weil die Gewinnung von Wasserstoff in allen bisher bekannten Verfahren den größten Kostenfaktor darstellt. Die Gewinnung des Wasserstoffes erfolgt bei allen bisher bekannten Verfahren entweder elektrolytisch oder aus Wassergas.In addition, the majority of the hydrogen required in the known process for the recovery of liquid hydrocarbons is obtained from water gas and the remaining requirement for hydrogen comes from the volatile constituents of the coal, which are obtained in coal gasification. In order to reduce the hydrogen requirement in the conventional process, coal with a high proportion of volatile constituents is preferred, not least because the production of hydrogen represents the greatest cost factor in all previously known processes. In all the processes known to date, the hydrogen is obtained either electrolytically or from water gas.
Wassergas wird erhalten, wenn Dampf über glühende Kohle geleitet wird, entsprechen den folgenden Reaktionen:Water gas is obtained when steam is passed over red-hot coal, corresponding to the following reactions:
Die Reaktion gemäß Gleichung 2 erfolgt vorzugsweise unter Einfluß von Katalysatoren (z.B. Eisen, Chrom) bei rund 400°C.The reaction according to equation 2 is preferably carried out under the influence of catalysts (e.g. iron, chromium) at around 400 ° C.
Gemeinsames Merkmal aller bisher bekannten Verfahren,gleichgültig, ob sie auf den Grundverfahren von BERGIUS, HABER-BOSCH bzw. FISCHER-TROPSCH aufbauen, ist die Gewinnung von Wasserstoff aus Synthesegas, wobei bereits ein wesentlicher Teil der Kohle zur Herstellung von Wassergas verbraucht wird.A common feature of all previously known processes, regardless of whether they are based on the basic processes from BERGIUS, HABER-BOSCH or FISCHER-TROPSCH, is the production of hydrogen from synthesis gas, whereby a substantial part of the coal is already used to produce water gas.
Ziel der vorliegenden Erfindung ist die Schaffung eines Verfahrens, mit dem flüssige Kohlenwasserstoffverbindungen insbesondere aus Kohle wesentlich einfacher gewonnen werden können, als dies mit den bekannten Verfahren der Fall ist.
Zur Erreichung dieses Zieles schlägt die Erfindung vor, in einem Verfahren zur Synthese von flüssigen Kohlenwasserstoffen, die ein C/H Verhältnis von 1 : 1 (z.B. C6H6) bis zirka 1 : 2,1 (z.B. C 12H26) und darüber (z.B. Schweröle und flüssige Kohlenwasserstoffe mit Mehrfachbindungen) besitzen, aus festem Kohlenstoff und einem Wasserstoffträger den Wasserstoffbedarf aus gasförmigen Kohlenwasserstoffen, z.B. Methan, Propan, Butan u. dgl., zu decken. Die gasförmigen Kohlenwasserstoffe kommen nicht als Zwischenprodukte im Synthesevorgang vor, sie werden vielmehr als Rohstoffe gemeinsam mit festen Kohlenstoffpartikeln dem Verfahren zugeführt.The aim of the present invention is to provide a process with which liquid hydrocarbon compounds, in particular from coal, can be obtained much more easily than is the case with the known processes. To achieve this goal, the invention proposes, in a process for the synthesis of liquid hydrocarbons, a C / H ratio of 1: 1 (eg C 6 H 6 ) to approximately 1: 2.1 (eg C 12 H 26 ) and above (eg heavy oils and liquid hydrocarbons with multiple bonds) have, from solid carbon and a hydrogen carrier the hydrogen requirement from gaseous hydrocarbons, eg methane, propane, butane and the like. Like. To cover. The gaseous hydrocarbons do not occur as intermediates in the synthesis process, rather they are fed into the process as raw materials together with solid carbon particles.
Die Gewinnung des freien Wasserstoffes aus den gasförmigen Kohlenwasserstoffen kann durch thermische Dissoziation mit oder ohne Katalysator bei Normaldruck oder auch bei Überdruck erfolgen.The free hydrogen can be obtained from the gaseous hydrocarbons by thermal dissociation with or without a catalyst at normal pressure or else at elevated pressure.
So ist beispielsweise aus der Literatur bekannt, daß reines CH4 bei 600°C und 1 bar Druck zu zirka 75 % aus H2-Molekülen und C-Molekülen besteht, wogegen nur noch rund 25 % in From von CH4 vorliegen.For example, it is known from the literature that pure CH 4 at 600 ° C. and 1 bar pressure consists of approximately 75% H 2 molecules and C molecules, whereas only around 25% are present in the form of CH 4 .
Da sich durch Zuführen von festen Kohlenstoffpartikeln das ursprüngliche H/C-Verhältnis von 4/1 in beliebiger Weise verschieben läßt, sind jene Verhältnisse gegeben, die mit oder ohne Anwesenheit von Katalysatoren bzw. bei Normaldruck, Überdruck oder Unterdruck für das Entstehen flüssiger Kohlenwasserstoffe charakteristisch sind.Since the original H / C ratio of 4/1 can be shifted in any manner by adding solid carbon particles, there are those ratios which are characteristic of the formation of liquid hydrocarbons with or without the presence of catalysts or at normal pressure, positive pressure or negative pressure are.
Die Reaktionen verlaufen nach der verallgemeinerten Formel
The reactions follow the generalized formula
Da die Reaktion nach rechts exotherm verläuft, ist eine Kühlung während des Reaktionsvorganges erforderlich. Die abgeführte Wärme kann zum Erhitzen bzw. Vorwärmen der Ausgangsprodukte (Gase + feste Kohlepartikel) verwendet werden.
Der weitere Verfahrensgang beruht auf bekannten Verfahren der fraktionierten Kondensation von flüssigen Kohlenwasserstoffen.Since the reaction is exothermic to the right, cooling is required during the reaction process. The dissipated heat can be used to heat or preheat the starting products (gases + solid carbon particles). The further process is based on known processes for the fractional condensation of liquid hydrocarbons.
Das erfindungsgemäße Verfahren ermöglicht nicht nur eine vollständige Nutzbarmachung der Kohle für die eigentliche Kohleverflüssigung, es gestattet darüber hinaus einen sinnvollen Einsatz von häufig im Überschuß zur Verfügung stehenden oder anfallenden Mengen an gasförmigen Kohlenwasserstoffen, beispielsweise Erdgas, das mangels Weiterverarbeitungsmöglichkeiten zur Zeit oft abgefackelt werden muß.
The process according to the invention not only enables the coal to be made fully usable for the actual coal liquefaction, it also permits the sensible use of amounts of gaseous hydrocarbons, for example natural gas, which are often available in excess or are available, and which often have to be flared due to the lack of further processing options.
Claims
1. Verfahren zur Herstellung von flüssigen Kohlenwasserstoffen durch Reaktion von festem Kohlenstoff mit einem gasförmigen Wasserstoffträger, dadurch gekennzeichnet, daß man den Wasserstoffbedarf abdeckende gasförmige Kohlenwasserstoffe gemeinsamt mit festen Kohlenstoffpartikeln dem Syntheseverfahren zuführt.1. A process for the production of liquid hydrocarbons by reaction of solid carbon with a gaseous hydrogen carrier, characterized in that gaseous hydrocarbons covering the hydrogen requirement are fed together with solid carbon particles to the synthesis process.
2. Verfahren nach Anspruch 1, dadurch gekennzeichnet, daß man als gasförmige Kohlenwasserstoffe Methan, Propan, Butan, Ethylen oder dgl. Gase einsetzt.2. The method according to claim 1, characterized in that the gaseous hydrocarbons used are methane, propane, butane, ethylene or the like. Gases.
3. Verfahren nach Anspruch 1, dadurch gekennzeichnet, daß man den für die Synthese erforderlichen freien Wasserstoff durch thermische Dissoziation, gegebenenfalls in Anwesenheit von Katalysatoren und/oder unter Anwendung von Überdruck, der eingesetzten gasförmigen Kohlenwasserstoffe gewinnt. 3. The method according to claim 1, characterized in that one obtains the free hydrogen required for the synthesis by thermal dissociation, optionally in the presence of catalysts and / or using excess pressure, of the gaseous hydrocarbons used.
Priority Applications (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EP19860901736 EP0266339A1 (en) | 1986-03-19 | 1986-03-19 | Process for liquefying carbonaceous materials |
PCT/AT1986/000023 WO1987005620A1 (en) | 1986-03-19 | 1986-03-19 | Process for liquefying carbonaceous materials |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
PCT/AT1986/000023 WO1987005620A1 (en) | 1986-03-19 | 1986-03-19 | Process for liquefying carbonaceous materials |
Publications (1)
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WO1987005620A1 true WO1987005620A1 (en) | 1987-09-24 |
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Family Applications (1)
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PCT/AT1986/000023 WO1987005620A1 (en) | 1986-03-19 | 1986-03-19 | Process for liquefying carbonaceous materials |
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WO (1) | WO1987005620A1 (en) |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE712254C (en) * | 1938-03-03 | 1941-10-21 | I G Farbenindustrie Akt Ges | Process for the production of hydrocarbon oils by catalytic pressure hydrogenation of coals, tars, mineral oils and similar substances or by pressure extraction of solid carbonaceous fuels |
US3617467A (en) * | 1968-12-06 | 1971-11-02 | Atlantic Richfield Co | Processes for retorting oil shale |
WO1984003515A1 (en) * | 1983-03-02 | 1984-09-13 | British Petroleum Co Plc | Electric arc conversion process and apparatus |
-
1986
- 1986-03-19 WO PCT/AT1986/000023 patent/WO1987005620A1/en unknown
- 1986-03-19 EP EP19860901736 patent/EP0266339A1/en not_active Withdrawn
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE712254C (en) * | 1938-03-03 | 1941-10-21 | I G Farbenindustrie Akt Ges | Process for the production of hydrocarbon oils by catalytic pressure hydrogenation of coals, tars, mineral oils and similar substances or by pressure extraction of solid carbonaceous fuels |
US3617467A (en) * | 1968-12-06 | 1971-11-02 | Atlantic Richfield Co | Processes for retorting oil shale |
WO1984003515A1 (en) * | 1983-03-02 | 1984-09-13 | British Petroleum Co Plc | Electric arc conversion process and apparatus |
Also Published As
Publication number | Publication date |
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EP0266339A1 (en) | 1988-05-11 |
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