GB817333A - Process of producing volatile products from residual oils - Google Patents
Process of producing volatile products from residual oilsInfo
- Publication number
- GB817333A GB817333A GB1776356A GB1776356A GB817333A GB 817333 A GB817333 A GB 817333A GB 1776356 A GB1776356 A GB 1776356A GB 1776356 A GB1776356 A GB 1776356A GB 817333 A GB817333 A GB 817333A
- Authority
- GB
- United Kingdom
- Prior art keywords
- line
- per cent
- products
- feed
- residium
- 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
- 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
- C10G9/00—Thermal non-catalytic cracking, in the absence of hydrogen, of hydrocarbon oils
- C10G9/28—Thermal non-catalytic cracking, in the absence of hydrogen, of hydrocarbon oils with preheated moving solid material
- C10G9/30—Thermal non-catalytic cracking, in the absence of hydrogen, of hydrocarbon oils with preheated moving solid material according to the "moving bed" method
Landscapes
- Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Abstract
<PICT:0817333/III/1> In a process of producing volatile products and coke from a residual oil the oil is contacted in a line 40 with particulate solids, preferably from a heating zone 27 heated to a temperature of 1300-1600 DEG F., whereby before entry into a separator 42 it is partly converted to volatile products and partly deposited on the particulate solids, solids from separator 42 pass into a coking zone 3 maintained solids from the heating zone 27 at a temperature of 1250-1400 DEG F. and are fluidized therein by gaseous hydrocarbons introduced through line 9 whereby the deposited portion of the oil is converted into coke and further volatile products which are withdrawn together with the volatile products from the separator 42 through line 17; coke is withdrawn through pipes 21 and 23, a portion being returned to the heating zone 27 through line 25. Some of the residual oil feed may be introduced directly into the coking zone and the gaseous hydrocarbons may comprise naphtha vapours, propane, butane, ethane or a mixture thereof in an amount of 1-10 weight per cent of residium feed. In some cases however the amount of gaseous hydrocarbons used may be 2-3 times the amount of the residium feed. The hot products leaving by line 17 are preferably quenched to 850-1100 DEG F. by means of water or an oil fraction introduced through line 19. The products recovered through line 17 amount to 75-82 weight per cent of the residium feed in addition to the products from the gaseous hydrocarbons employed for fluidizing. The products obtained based on residium feed include 8-20 volume per cent gasoline hydrocarbons boiling about 150-400 DEG F.; 2-10 volume per cent of a fraction boiling at about 400-700 DEG F. and 2-10 volume per cent of tar boiling above 700 DEG F. The process may be combined with a visbreaking treatment of a residual oil, the treatment producing a heavy tar which is then treated in the manner previously described. The visbreaking treatment may be effected at temperatures up to 850-1000 DEG F. pressures of at least 500 p.s.i.g. and for times of 1-30 minutes.ALSO:In a process of producing volatile products and coke from a residual oil the oil is contacted in a line 40 with particulate solids, preferably coke, from a heating zone 27 heated to a temperature of 1300-1600 DEG F. whereby before entry into a separator 42 it is partly converted to volatile products and partly deposited on the particulate solids, solids from separator 42 pass into a coking zone 3 maintained by solids from the heating zone 27 at a temperature of 1250-1400 DEG F. and are fluidized therein by gaseous hydrocarbons introduced through line 9 whereby the deposited portion of the oil is converted into coke and further volatile products which are withdrawn together with the volatile products from the separator 42 through line 17; coke is withdrawn through pipes 21 and 23, a portion being returned to the heating zone 27 through line 25. Some of the residual oil feed may be introduced directly into the coking zone and the gaseous hydrocarbons may comprise naphtha vapours, propane, butane, <FORM:0817333/IV (b)/1> ethane or a mixture thereof in an amount of 1-10 weight per cent of residium feed. In some cases, however, the amount of gaseous hydrocarbons used may be 2-3 times the amount of the residium feed. The hot products leaving by line 17 are preferably quenched to 850-1100 DEG F. by means of water or an oil fraction introduced through line 19. The products recovered through line 17 amount to 75-82 weight per cent of the residium feed in addition to hydrogen, methane and C2-C4 olefines and di-olefines from the fluidizing hydrocarbons. The products based on the residium feed include 30-50 weight per cent hydrogen and C1 to C3 hydrocarbons comprising ethylene, ethane, propylene and propane; 5-15 volume per cent C4 hydrocarbons comprising butadiene, butanes and butenes; 2-6 volume per cent C5 hydrocarbons comprising di-olefines isoprene, piperylene and cyclopentadiene and pentenes.
Publications (1)
Publication Number | Publication Date |
---|---|
GB817333A true GB817333A (en) | 1959-07-29 |
Family
ID=1733385
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB1776356A Expired GB817333A (en) | 1956-06-08 | Process of producing volatile products from residual oils |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB817333A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3259565A (en) * | 1963-03-26 | 1966-07-05 | Exxon Research Engineering Co | Fluidized bed coking process |
-
1956
- 1956-06-08 GB GB1776356A patent/GB817333A/en not_active Expired
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3259565A (en) * | 1963-03-26 | 1966-07-05 | Exxon Research Engineering Co | Fluidized bed coking process |
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