GB780813A - A method of manufacturing acetylene from hydrocarbons - Google Patents
A method of manufacturing acetylene from hydrocarbonsInfo
- Publication number
- GB780813A GB780813A GB36355A GB36355A GB780813A GB 780813 A GB780813 A GB 780813A GB 36355 A GB36355 A GB 36355A GB 36355 A GB36355 A GB 36355A GB 780813 A GB780813 A GB 780813A
- Authority
- GB
- United Kingdom
- Prior art keywords
- stage
- gas
- acetylene
- nickel
- hydrocarbons
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C11/00—Aliphatic unsaturated hydrocarbons
- C07C11/22—Aliphatic unsaturated hydrocarbons containing carbon-to-carbon triple bonds
- C07C11/24—Acetylene
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C4/00—Preparation of hydrocarbons from hydrocarbons containing a larger number of carbon atoms
- C07C4/02—Preparation of hydrocarbons from hydrocarbons containing a larger number of carbon atoms by cracking a single hydrocarbon or a mixture of individually defined hydrocarbons or a normally gaseous hydrocarbon fraction
- C07C4/06—Catalytic processes
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C2523/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00
- C07C2523/16—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00 of arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
- C07C2523/24—Chromium, molybdenum or tungsten
- C07C2523/26—Chromium
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C2523/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00
- C07C2523/16—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00 of arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
- C07C2523/24—Chromium, molybdenum or tungsten
- C07C2523/28—Molybdenum
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C2523/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00
- C07C2523/16—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00 of arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
- C07C2523/24—Chromium, molybdenum or tungsten
- C07C2523/30—Tungsten
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C2523/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00
- C07C2523/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00 of the iron group metals or copper
- C07C2523/72—Copper
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C2523/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00
- C07C2523/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00 of the iron group metals or copper
- C07C2523/74—Iron group metals
- C07C2523/755—Nickel
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C2523/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00
- C07C2523/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00 of the iron group metals or copper
- C07C2523/76—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups C07C2523/02 - C07C2523/36
- C07C2523/84—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups C07C2523/02 - C07C2523/36 with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
- C07C2523/85—Chromium, molybdenum or tungsten
- C07C2523/86—Chromium
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Abstract
A method for the preparation of acetylene comprises, in combination, a first stage for thermally cracking liquid hydrocarbons which consist mainly of saturated hydrocarbons having boiling-points in the range of 175 DEG to 350 DEG C. to produce a gas which is rich in olefine content by passing the hydrocarbons through a reaction chamber filled with a catalyst from the group of copper, nickel, chromium, and nickel-chrome-steel, which is heated to 700-900 DEG C. under a reduced pressure not above 300 mms. mercury, an intermediate stage for diluting the gas produced in the first stage by mixing it with 3-7 times its volume of a diluent gas, and a second stage in which the diluted gas of the first stage is passed through a second reaction chamber filled with a catalyst selected from the group consisting of molybdenum, tungsten, nickel, and nickel-chrome-steel, and heated to a temperature of 1000-1200 DEG C. under a reduced pressure not above 300 mm. of mercury to produce acetylene. The initial hydrocarbon may be petroleum or light oils such as n-hexane, cyclohexane, decomposed petroleum gases, coke oven gases or synthetic hydrocarbons. The diluent gas may be hydrogen, the residual gas after acetylene extraction, or steam. The initial cracking may be carried out in a pebble heater system, and the second cracking is preferably effected in a refractory furnace. The resultant acetylene may be purified by an extraction method employing dimethyl formamide as a solvent.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB36355A GB780813A (en) | 1955-01-05 | 1955-01-05 | A method of manufacturing acetylene from hydrocarbons |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB36355A GB780813A (en) | 1955-01-05 | 1955-01-05 | A method of manufacturing acetylene from hydrocarbons |
Publications (1)
Publication Number | Publication Date |
---|---|
GB780813A true GB780813A (en) | 1957-08-07 |
Family
ID=9703077
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB36355A Expired GB780813A (en) | 1955-01-05 | 1955-01-05 | A method of manufacturing acetylene from hydrocarbons |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB780813A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE2826003A1 (en) * | 1978-06-14 | 1979-12-20 | Grohe Armaturen Friedrich | Screw-type pipe union - has sleeve with flanged end for nut fitting over elastic bush |
-
1955
- 1955-01-05 GB GB36355A patent/GB780813A/en not_active Expired
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE2826003A1 (en) * | 1978-06-14 | 1979-12-20 | Grohe Armaturen Friedrich | Screw-type pipe union - has sleeve with flanged end for nut fitting over elastic bush |
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