GB790166A - Improvements in or relating to processes and apparatus for effecting a rapid change in temperature of gaseous fluid or for rapidly vaporising liquid fluid - Google Patents
Improvements in or relating to processes and apparatus for effecting a rapid change in temperature of gaseous fluid or for rapidly vaporising liquid fluidInfo
- Publication number
- GB790166A GB790166A GB2914/56A GB291456A GB790166A GB 790166 A GB790166 A GB 790166A GB 2914/56 A GB2914/56 A GB 2914/56A GB 291456 A GB291456 A GB 291456A GB 790166 A GB790166 A GB 790166A
- Authority
- GB
- United Kingdom
- Prior art keywords
- fluid
- screen
- vessel
- temperature
- solid
- 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
- 239000012530 fluid Substances 0.000 title abstract 11
- 238000000034 method Methods 0.000 title abstract 4
- 239000007788 liquid Substances 0.000 title abstract 3
- 239000007787 solid Substances 0.000 abstract 9
- 238000006243 chemical reaction Methods 0.000 abstract 8
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 abstract 6
- MWUXSHHQAYIFBG-UHFFFAOYSA-N nitrogen oxide Inorganic materials O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 abstract 6
- 239000002245 particle Substances 0.000 abstract 6
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 abstract 4
- QQONPFPTGQHPMA-UHFFFAOYSA-N Propene Chemical compound CC=C QQONPFPTGQHPMA-UHFFFAOYSA-N 0.000 abstract 4
- LELOWRISYMNNSU-UHFFFAOYSA-N hydrogen cyanide Chemical compound N#C LELOWRISYMNNSU-UHFFFAOYSA-N 0.000 abstract 4
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 abstract 3
- 238000010438 heat treatment Methods 0.000 abstract 3
- 239000001301 oxygen Substances 0.000 abstract 3
- 229910052760 oxygen Inorganic materials 0.000 abstract 3
- 239000000376 reactant Substances 0.000 abstract 3
- HSFWRNGVRCDJHI-UHFFFAOYSA-N Acetylene Chemical compound C#C HSFWRNGVRCDJHI-UHFFFAOYSA-N 0.000 abstract 2
- OSDWBNJEKMUWAV-UHFFFAOYSA-N Allyl chloride Chemical compound ClCC=C OSDWBNJEKMUWAV-UHFFFAOYSA-N 0.000 abstract 2
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 abstract 2
- 150000001335 aliphatic alkanes Chemical class 0.000 abstract 2
- 150000001336 alkenes Chemical class 0.000 abstract 2
- 229910021529 ammonia Inorganic materials 0.000 abstract 2
- 239000007795 chemical reaction product Substances 0.000 abstract 2
- 239000000460 chlorine Substances 0.000 abstract 2
- 229910052801 chlorine Inorganic materials 0.000 abstract 2
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 abstract 2
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 abstract 1
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 abstract 1
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 abstract 1
- 238000005899 aromatization reaction Methods 0.000 abstract 1
- 230000015572 biosynthetic process Effects 0.000 abstract 1
- 229910002091 carbon monoxide Inorganic materials 0.000 abstract 1
- 239000003054 catalyst Substances 0.000 abstract 1
- 230000003197 catalytic effect Effects 0.000 abstract 1
- 238000002485 combustion reaction Methods 0.000 abstract 1
- 238000001816 cooling Methods 0.000 abstract 1
- 239000000446 fuel Substances 0.000 abstract 1
- 229930195733 hydrocarbon Natural products 0.000 abstract 1
- 150000002430 hydrocarbons Chemical class 0.000 abstract 1
- 239000001257 hydrogen Substances 0.000 abstract 1
- 229910052739 hydrogen Inorganic materials 0.000 abstract 1
- 125000001434 methanylylidene group Chemical group [H]C#[*] 0.000 abstract 1
- 239000000203 mixture Substances 0.000 abstract 1
- 230000003647 oxidation Effects 0.000 abstract 1
- 238000007254 oxidation reaction Methods 0.000 abstract 1
- 239000012188 paraffin wax Substances 0.000 abstract 1
- 229910052697 platinum Inorganic materials 0.000 abstract 1
- 239000000047 product Substances 0.000 abstract 1
- 238000010791 quenching Methods 0.000 abstract 1
- 230000000171 quenching effect Effects 0.000 abstract 1
- 230000001172 regenerating effect Effects 0.000 abstract 1
- 230000008929 regeneration Effects 0.000 abstract 1
- 238000011069 regeneration method Methods 0.000 abstract 1
- 239000004576 sand Substances 0.000 abstract 1
- 239000000126 substance Substances 0.000 abstract 1
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28C—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA COME INTO DIRECT CONTACT WITHOUT CHEMICAL INTERACTION
- F28C3/00—Other direct-contact heat-exchange apparatus
- F28C3/10—Other direct-contact heat-exchange apparatus one heat-exchange medium at least being a fluent solid, e.g. a particulate material
- F28C3/12—Other direct-contact heat-exchange apparatus one heat-exchange medium at least being a fluent solid, e.g. a particulate material the heat-exchange medium being a particulate material and a gas, vapour, or liquid
- F28C3/16—Other direct-contact heat-exchange apparatus one heat-exchange medium at least being a fluent solid, e.g. a particulate material the heat-exchange medium being a particulate material and a gas, vapour, or liquid the particulate material forming a bed, e.g. fluidised, on vibratory sieves
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
Allyl chloride is formed by the reaction of propene with chlorine at about 500 DEG C., using a process in which a rapid change in temperature of a gaseous fluid is effected by passing the fluid through a screen of free-falling solid particles of size less than 2 mm., which screen is formed by flow of particles from a homogeneously fluidized bed, the temperature of which is considerably different from that of the fluid (see Group III).ALSO:<PICT:0790166/III/1> A rapid change in temperature of a gaseous fluid is effected, or a liquid fluid is rapidly vaporized, by passing the fluid through a screen of free-falling solid particles of size less than 2 mm., which screen is formed by flow of particles from a homogeneously fluidized bed, the temperature of which is considerably different from that of the fluid. The solids fall through a straight or circular slot at the top of a vessel to form a flat or cylindrical screen; a collecting device for the solid is provided at the foot of the vessel and an inlet for the fluid leads into one of the spaces into which the vessel is divided by the screen. The process may be used for the rapid heating of reactants, for the cooling of reaction products, or for controlling the temperature of endothermic or exothermic reactions. Liquid or gaseous hydrocarbons may be cracked by contact with solids which are either inert, e.g. sand, or catalytic; the reaction products may be cooled by introducing a quenching medium into the outlet from the vessel or by passing the products through a second screen of cooled solids. When reactants are to be heated separately, two screens of hot particles may be used, one for each reactant. As shown, hot particles flow from fluidized bed in vessel 5 through slot 15 to form screen 16, being collected in a fluidized bed in vessel 6. The fluid to be treated is supplied through nozzle 17 and passes through screen 16 to outlet 13 and cyclone 35. Solid collects in vessel 38 and is withdrawn at 39 for heating, regenerating if necessary, and return to vessel 5. Heating and regeneration may be carried out by a process according to the invention, the solid being treated as a falling screen with fuel and combustion air. Solid paraffin-containing substances may be converted into ethene or a mixture of olefins at 700-800 DEG C. in the presence of steam and in some cases oxygen. Other reactions referred to are the conversion of methane by steam into carbon monoxide and hydrogen; the conversion of methane by oxygen into ethyne or aromatics; the oxidation of ammonia to nitrogen oxides at 700-1000 DEG C.; the conversion of alkanes to alkenes; the formation of allyl chloride from propene and chlorine at 500 DEG C.; the pyrolytic aromatization of alkanes at 750-900 DEG C.; the reaction between methene, ammonia and oxygen in the presence of platinum catalyst to form hydrogen cyanide; and the reaction between methane and nitrogen oxide at 1000 DEG C. to form hydrogen cyanide.
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| NL790166X | 1955-01-31 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| GB790166A true GB790166A (en) | 1958-02-05 |
Family
ID=19832729
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| GB2914/56A Expired GB790166A (en) | 1955-01-31 | 1956-01-30 | Improvements in or relating to processes and apparatus for effecting a rapid change in temperature of gaseous fluid or for rapidly vaporising liquid fluid |
Country Status (1)
| Country | Link |
|---|---|
| GB (1) | GB790166A (en) |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB2117885A (en) * | 1982-03-30 | 1983-10-19 | Chevron Res | Process and device for recovering heat from a particulate solid containing diverse particle sizes |
| GB2145347A (en) * | 1981-11-16 | 1985-03-27 | Foster Wheeler Energy Corp | Fluidized return of particulate material to a fluidized bed combustor |
| GB2242438A (en) * | 1990-03-26 | 1991-10-02 | Amoco Corp | Catalytic cracking with quenching |
| US5087427A (en) * | 1990-03-26 | 1992-02-11 | Amoco Corporation | Catalytic cracking unit with internal gross cut separator and quench injector |
| US5626741A (en) * | 1990-03-26 | 1997-05-06 | Amoco Corporation | Catalytic cracking with quenching |
| WO2014173791A1 (en) * | 2013-04-23 | 2014-10-30 | Bayer Technology Services Gmbh | Process for the preparation of benzene from methane and carbon dioxide with a fluid-tight dividing wall in the reactor |
-
1956
- 1956-01-30 GB GB2914/56A patent/GB790166A/en not_active Expired
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB2145347A (en) * | 1981-11-16 | 1985-03-27 | Foster Wheeler Energy Corp | Fluidized return of particulate material to a fluidized bed combustor |
| GB2117885A (en) * | 1982-03-30 | 1983-10-19 | Chevron Res | Process and device for recovering heat from a particulate solid containing diverse particle sizes |
| GB2242438A (en) * | 1990-03-26 | 1991-10-02 | Amoco Corp | Catalytic cracking with quenching |
| US5087427A (en) * | 1990-03-26 | 1992-02-11 | Amoco Corporation | Catalytic cracking unit with internal gross cut separator and quench injector |
| GB2242438B (en) * | 1990-03-26 | 1994-10-26 | Amoco Corp | Catalytic cracking with quenching |
| US5626741A (en) * | 1990-03-26 | 1997-05-06 | Amoco Corporation | Catalytic cracking with quenching |
| WO2014173791A1 (en) * | 2013-04-23 | 2014-10-30 | Bayer Technology Services Gmbh | Process for the preparation of benzene from methane and carbon dioxide with a fluid-tight dividing wall in the reactor |
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