SU53854A1 - Apparatus for the oxidation of organic compounds - Google Patents
Apparatus for the oxidation of organic compoundsInfo
- Publication number
- SU53854A1 SU53854A1 SU53854A1 SU 53854 A1 SU53854 A1 SU 53854A1 SU 53854 A1 SU53854 A1 SU 53854A1
- Authority
- SU
- USSR - Soviet Union
- Prior art keywords
- organic compounds
- oxidation
- reactor
- air
- reaction
- Prior art date
Links
- 150000002894 organic compounds Chemical class 0.000 title description 2
- 230000003647 oxidation Effects 0.000 title 1
- 238000007254 oxidation reaction Methods 0.000 title 1
- 238000010438 heat treatment Methods 0.000 description 4
- 238000000034 method Methods 0.000 description 2
- PNEYBMLMFCGWSK-UHFFFAOYSA-N AI2O3 Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 1
- 239000007795 chemical reaction product Substances 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 238000009413 insulation Methods 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 229910001120 nichrome Inorganic materials 0.000 description 1
- 239000007800 oxidant agent Substances 0.000 description 1
- 239000012476 oxidizable substance Substances 0.000 description 1
- MYMOFIZGZYHOMD-UHFFFAOYSA-N oxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052904 quartz Inorganic materials 0.000 description 1
- 239000010453 quartz Substances 0.000 description 1
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N silicon dioxide Inorganic materials O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 1
Description
Предлагаемый анпарат предназначаетс дл окислени органических соединений воздухом или кислородом согласно способу, описанному в авторском свидетельстве .N« 51180.The proposed anaparate is intended to oxidize organic compounds with air or oxygen according to the method described in the author's certificate .N "51180.
Аппарат, изображений на фиг. 1 (вертикальный разрез) и на фиг. 2 (горизонтальный разрез), состоит из внутренней металлической трубы /, котора вставлена во внешнюю трубу 2 из огнеупорного шамога, покрытую тепловой изол цией 3. В кольцевом пространстве между трубами помещены электрические нагревательные элементы 4, при помощи которых происходит предварительное разогревание трубы 7, вл ющейс реактором дл проведени процесса. Нагревательные элементы состо т из нихромовых спиралей, укрепленных на алундовых или кварцевых трубках и расположенных позонно (верхн , средн и нижн зоны) таким образом , чтобы представл лась возможность их последовательного и параллельного включени , а также полного выключени отдельных зон обогрева.The apparatus, of the images in FIG. 1 (vertical section) and in FIG. 2 (horizontal section) consists of an inner metal pipe /, which is inserted into the outer pipe 2 of refractory shamog covered with thermal insulation 3. Electrical heating elements 4 are placed in the annular space between the pipes, by means of which the pipe is preheated reactor for the process. The heating elements consist of nichrome spirals mounted on alundum or quartz tubes and arranged in the zone (upper, middle and lower zones) so that they can be switched on in series and in parallel, as well as completely turning off individual heating zones.
Верхн крышка реактора снабжена штуцером 5 дл ввода смеси окисл емых веществ и воздуха, нижн крышка-штуцером 6 дл удалени продуктов реакции.The upper lid of the reactor is equipped with a fitting 5 for introducing a mixture of oxidizable substances and air, and a lower lid fitting 6 for removing the reaction products.
Во внешней трубе устроены штуцер 7 дл подачи и штуцер 8 дл удалени наружного воздуха, омывающего реактор и отвод щего избыточную теплоту реакции, которую можно частично регенерировать, использу нагретый таким образом воздух в качестве окислительного агента.A supply nozzle 7 and nozzle 8 are arranged in the outer tube to remove the outside air that washes the reactor and removes excess heat of reaction, which can be partially regenerated using the air thus heated as an oxidizing agent.
В верхней крышке реактора имеютс отверсти дл ввода термопар в реакционное пространство.There are openings in the upper lid of the reactor for the entry of thermocouples into the reaction space.
Конструкци реактора позвол ет применить автоматическое управление и регулирование процесса путем соединени термопары, помещенной в зоне холодного пламени с электрическим терморегул тором, включающим и выключающим по мере надобности либо обогрев реактора, либо вентил тор, подающий воздух дл охлаждени .The design of the reactor allows the use of automatic control and regulation of the process by connecting a thermocouple placed in the cold flame zone with an electric thermostat that turns on and off as needed either heating the reactor or a fan supplying air for cooling.
В некоторых случа х внутреннюю реакционную трубу целесообразно замен ть пучком параллельно работающих труб - реакторов меньшего диаметра.In some cases, it is advisable to replace the inner reaction tube with a bundle of parallel operating tubes — reactors of smaller diameter.
Family
ID=
Similar Documents
Publication | Publication Date | Title |
---|---|---|
JP2791985B2 (en) | Waste heat treatment equipment and method of operating the equipment | |
US4046085A (en) | Method and apparatus for treating waste material in a counter-current incinerator | |
SU53854A1 (en) | Apparatus for the oxidation of organic compounds | |
US5531169A (en) | Treatment of liquid waste material | |
KR20180125518A (en) | Furnace Furnace and Heat Treatment Method for Heat Treatment of Metal Strips | |
JPH0123173B2 (en) | ||
JPH0221121A (en) | Combustion method by catalyst of organic compound and combustion apparatus by catalyst of organic compound | |
JPS628712B2 (en) | ||
JP3909088B2 (en) | Metal reduction and melting methods | |
US3915655A (en) | Process and apparatus for burning gas and vapor mixture produced in the purification of coke gas ovens | |
JPH03127A (en) | Indirect heating in reaction room for endothermic reaction and apparatus for performing it | |
CN212068677U (en) | Reactor and preheater arrangement | |
FR2621311B1 (en) | METHOD AND DEVICE FOR THE SIMULTANEOUS CONTINUOUS GRAPHITIZATION OF LONG CARBON PRODUCTS AND CARBON GRAINS FLOWING IN COUNTER-CURRENT | |
CN212283564U (en) | Waste gas catalytic oxidation device | |
JP3731684B2 (en) | High temperature heat exchanger for removing dioxins and combustion furnace apparatus using the high temperature heat exchanger | |
ATE60366T1 (en) | RADIAL TUBE BURNER WITH CATALYST BED FOR HEAT TREATMENT FURNACES. | |
KR100438763B1 (en) | Method for supplying and disposing the reducing gas of tempering furnace with a catalytic combustion reaction, and apparatus thereof | |
EP3354328B1 (en) | A system and method for purifying gas | |
SU877242A1 (en) | Apparatus for burning waste gases | |
RU2385869C1 (en) | Method of producing phenyl- or methylphenylchlorosilanes, heat provision scheme and reactor for realising said method | |
RU2740021C2 (en) | Apparatus for purifying gas from hydrogen sulphide | |
JP4509514B2 (en) | Pollutant gas decomposition device and contaminated soil treatment device | |
JPH02217302A (en) | Method for indirectly heating process gas flow in reaction chamber for endothermic reaction and apparatus for practicing said method | |
SU992600A1 (en) | Hood-type furnace | |
JPH0630267Y2 (en) | Endothermic endothermic gas generator |