GB1129568A - Method of operating regenerative furnaces and apparatus therefor - Google Patents
Method of operating regenerative furnaces and apparatus thereforInfo
- Publication number
- GB1129568A GB1129568A GB38492/66A GB3849266A GB1129568A GB 1129568 A GB1129568 A GB 1129568A GB 38492/66 A GB38492/66 A GB 38492/66A GB 3849266 A GB3849266 A GB 3849266A GB 1129568 A GB1129568 A GB 1129568A
- Authority
- GB
- United Kingdom
- Prior art keywords
- mass
- plenum
- burn out
- manifold
- passages
- 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
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10S585/00—Chemistry of hydrocarbon compounds
- Y10S585/949—Miscellaneous considerations
- Y10S585/95—Prevention or removal of corrosion or solid deposits
Landscapes
- Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Thermal Sciences (AREA)
- Organic Chemistry (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
- Incineration Of Waste (AREA)
- Physical Or Chemical Processes And Apparatus (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Air Supply (AREA)
- Furnace Details (AREA)
Abstract
1,129,568. Regenerative chemical furnaces. UNION CARBIDE CORP. 26 Aug., 1966 [31 Aug., 1965], No. 38492/66. Heading F4B. [Also in Division C5] In a method, for the production of acetylene and/or ethylene by cracking propane in a regenerative furnace, comprising three regenerative masses 13, 14, 15 each having a plurality of longitudinal passages 19 therethrough, combustion chambers 16 and 17 and plenum chambers 20 and 21, which includes alternating heat and make steps through the furnace, the make step deposits foreign materials on the walls of the passages of the mass through which the gas flows after cracking, and the foreign materials are removed by burn out steps which precede or are combined with the heat step. In a left-hand (L.H.) make step feed stock mixed with steam in a mixer 51, is fed through a manifold 36 to plenum chamber 21 and then through L.H. mass 15, central mass 14 in which most of the cracking takes place, and R.H. mass 13 in which quenching and deposition of tar takes place, the off-gas flowing through plenum chamber 20, manifold 34 and conduit 45 to storage. In a L.H. burn out fuel gas and air are supplied to manifold 34 via conduits 33 and 37 respectively and the mixture is ignited by an electrical impulse from cable 61, and the burning mixture passes through the plenum chamber 20, to the passages 19 of mass 13 from which it burns tar, the exhaust passing through the masses 14 and 15, the plenum 21, manifold 36 and conduit 44 to an exhaust stack. In a L.H. heat step air is supplied via conduit 37, manifold 34, plenum 20 and passages 19 to combustion chamber 17 and fuel is supplied via conduits 23, 25, 28 to burners 29, the combustion re-heating the mass 14 and the combustion products being exhausted as in a L.H. burn out. The burn out step may be combined with the beginning of a heat step by setting three-way valve 26 to supply half the fuel to burner 29 and half to plenum 34. Solenoid-type valves automatically controlled by electric timers are used throughout. It is not always necessary to have a burn out at the beginning of (or before) each heat step. A differential pressure switch which responds to the pressure drop across the furnace to bring the burn out into operation when the drop reaches a preselected value, may be provided.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US48402765A | 1965-08-31 | 1965-08-31 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB1129568A true GB1129568A (en) | 1968-10-09 |
Family
ID=23922437
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB38492/66A Expired GB1129568A (en) | 1965-08-31 | 1966-08-26 | Method of operating regenerative furnaces and apparatus therefor |
Country Status (9)
Country | Link |
---|---|
US (1) | US3472907A (en) |
JP (1) | JPS4920473B1 (en) |
BE (1) | BE686233A (en) |
DK (1) | DK138083B (en) |
ES (2) | ES330647A1 (en) |
GB (1) | GB1129568A (en) |
IL (1) | IL26384A (en) |
NL (1) | NL150505B (en) |
SE (1) | SE331835B (en) |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3888302A (en) * | 1973-10-01 | 1975-06-10 | Kaiser Steel Corp | Method for removing deposits from interior surfaces of regenerative heat exchangers |
US4061544A (en) * | 1976-05-03 | 1977-12-06 | Koppers Company, Inc. | Apparatus for providing waste gas recirculation in coke oven batteries |
Family Cites Families (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CA538572A (en) * | 1957-03-26 | L. Hasche Rudolph | Pyrolytic process for endothermically altering a gaseous material | |
US2785212A (en) * | 1954-11-29 | 1957-03-12 | Phillips Petroleum Co | Regenerative furnace and production of unsaturated hydrocarbons therein |
US3093697A (en) * | 1960-05-27 | 1963-06-11 | Union Carbide Corp | Process for producing acetylene |
-
1965
- 1965-08-31 US US484027A patent/US3472907A/en not_active Expired - Lifetime
-
1966
- 1966-08-24 IL IL26384A patent/IL26384A/en unknown
- 1966-08-26 GB GB38492/66A patent/GB1129568A/en not_active Expired
- 1966-08-27 ES ES0330647A patent/ES330647A1/en not_active Expired
- 1966-08-29 NL NL666612137A patent/NL150505B/en unknown
- 1966-08-29 SE SE11594/66A patent/SE331835B/xx unknown
- 1966-08-30 DK DK444366AA patent/DK138083B/en unknown
- 1966-08-31 BE BE686233D patent/BE686233A/xx unknown
- 1966-08-31 JP JP41057035A patent/JPS4920473B1/ja active Pending
-
1967
- 1967-05-29 ES ES341108A patent/ES341108A1/en not_active Expired
Also Published As
Publication number | Publication date |
---|---|
DE1593654B2 (en) | 1975-07-17 |
US3472907A (en) | 1969-10-14 |
ES341108A1 (en) | 1968-07-16 |
ES330647A1 (en) | 1967-09-16 |
DE1593654A1 (en) | 1972-04-13 |
BE686233A (en) | 1967-02-28 |
IL26384A (en) | 1970-09-17 |
JPS4920473B1 (en) | 1974-05-24 |
DK138083B (en) | 1978-07-10 |
SE331835B (en) | 1971-01-18 |
DK138083C (en) | 1978-11-27 |
NL6612137A (en) | 1967-03-01 |
NL150505B (en) | 1976-08-16 |
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