SU186607A1 - BURNER OF DIRECT MIX FOR PYROLYSIS AND CONVERSION OF HYDROCARBONS - Google Patents
BURNER OF DIRECT MIX FOR PYROLYSIS AND CONVERSION OF HYDROCARBONSInfo
- Publication number
- SU186607A1 SU186607A1 SU797821A SU797821A SU186607A1 SU 186607 A1 SU186607 A1 SU 186607A1 SU 797821 A SU797821 A SU 797821A SU 797821 A SU797821 A SU 797821A SU 186607 A1 SU186607 A1 SU 186607A1
- Authority
- SU
- USSR - Soviet Union
- Prior art keywords
- burner
- pyrolysis
- hydrocarbons
- conversion
- direct mix
- Prior art date
Links
- 238000006243 chemical reaction Methods 0.000 title description 3
- 150000002430 hydrocarbons Chemical class 0.000 title description 2
- 238000000197 pyrolysis Methods 0.000 title description 2
- 239000000203 mixture Substances 0.000 description 5
- 230000015572 biosynthetic process Effects 0.000 description 3
- 239000003345 natural gas Substances 0.000 description 3
- 239000007800 oxidant agent Substances 0.000 description 3
- 239000001301 oxygen Substances 0.000 description 3
- MYMOFIZGZYHOMD-UHFFFAOYSA-N oxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 description 3
- 229910052760 oxygen Inorganic materials 0.000 description 3
- 238000005755 formation reaction Methods 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 238000002485 combustion reaction Methods 0.000 description 1
- 125000002534 ethynyl group Chemical group [H]C#C* 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- VUZPPFZMUPKLLV-UHFFFAOYSA-N methane;hydrate Chemical compound C.O VUZPPFZMUPKLLV-UHFFFAOYSA-N 0.000 description 1
- 230000001590 oxidative Effects 0.000 description 1
- 238000003786 synthesis reaction Methods 0.000 description 1
- 230000002194 synthesizing Effects 0.000 description 1
Description
Известно несколько конструкций реакторов, дл переработки природного газа на ацетилен и синтез-газ.Several reactor designs are known for processing natural gas to acetylene and synthesis gas.
Предложенна горелка - высокотурбулентное горелочное устройство, основанное на принципе непосредственного смешени . Она состоит из кольцевой камеры, патрубков, по которым подвод тс сырье и окислитель, и фланца дл креплени . Дл завершени смесеобразовани в момент воспламенени смеси и исключени проскока пламени в смесительную зону в кольцевой камере установлены сопла Лавал (например, 20 штук).The proposed burner is a high-turbulent burner based on the principle of direct mixing. It consists of an annular chamber, nozzles, through which raw materials and oxidant are supplied, and a flange for fastening. To complete the mixture formation at the moment of ignition of the mixture and to prevent the leakage of flame into the mixing zone, Laval nozzles (for example, 20 pieces) are installed in the annular chamber.
На чертеже показано устройство горелки.The drawing shows the device burner.
По патрубку 1 в кольцевую камеру 2 с сонлами Лавал 3 подводитс природный газ, по патрубку 4 в кольцевую камеру 5 - техниче-, ский кислород, но кольцевому зазору 6 природный газ и кислород подаютс в реакционную зону 7. Реакционна зона имеет рубашку 8. Запальником 9 метано-кислородна смесь воспламен етс .Natural gas is supplied through nozzle 1 to the annular chamber 2 with Laval's sonla 3, technical oxygen is supplied to the annular chamber 5 through nozzle 4, but natural gas and oxygen are supplied to the reaction zone 7 in the annular gap 6. 9, the methane-oxygen mixture is ignited.
Фланцем 10 горелка крепитс к цельнометаллическому реактору либо к реактору с металлической вставкой.The flange 10 burner is attached to the metal reactor or to the reactor with a metal insert.
Она может работать как при повышенном давлении, так и без давлени .It can work both with increased pressure and without pressure.
Предмет изобретени Subject invention
Горелка непосредственного смешени дл пиролиза и конверсии углеводородов полным или частичным горением без предварительного смешени с окислителем (кислородом), состо ща из кольцевой камеры, подвод ш,ихA direct burner for the pyrolysis and conversion of hydrocarbons by complete or partial combustion without mixing with an oxidizing agent (oxygen), consisting of an annular chamber;
патрубков дл сырь и окислител и фланца дл креплени , отличающа с тем, что, с целью завершени смесеобразовани в момент воспламенени смеси и исключени возможности проскока пламени в смесительнуюnozzles for raw materials and an oxidizer and a flange for fastening, characterized in that, in order to complete the mixture formation at the time of ignition of the mixture and to exclude the possibility of leakage of the flame into the mixing
зону, в кольцевой камере шарнирно закреплено несколько сопел Лавал , например 20.zone, in the annular chamber several Lawal nozzles are hinged, for example, 20.
снsn
Publications (1)
| Publication Number | Publication Date |
|---|---|
| SU186607A1 true SU186607A1 (en) |
Family
ID=
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US4113445A (en) | Process for the partial oxidation of liquid hydrocarbonaceous fuels | |
| US4427362A (en) | Combustion method | |
| US5486269A (en) | Gasification of carbonaceous material in a reactor having a gasification zone and a combustion zone | |
| EP0107225B1 (en) | Process and burner for the partial combustion of solid fuel | |
| AU721782B2 (en) | Dimethyl ether fuel and method of generating power in a dry low NOx combustion system | |
| CA2786642C (en) | Process and burner for producing synthesis gas | |
| Susanto et al. | A moving-bed gasifier with internal recycle of pyrolysis gas | |
| FR2360042A1 (en) | COMBUSTION PROCESS AND APPARATUS | |
| EP0158863A3 (en) | Method of controlling pyrolysis temperature | |
| JPS62402B2 (en) | ||
| US4386941A (en) | Process for the partial oxidation of slurries of solid carbonaceous fuel | |
| US4042344A (en) | Process for the production of gaseous mixtures | |
| US3644555A (en) | Process for the production of acetylene or acetylene and ethylene by pyrolysis of hydrocarbons | |
| CN106854127A (en) | The method and device of hydrocarbon acetylene and/or synthesis gas | |
| US20020064741A1 (en) | Premixing burner block for partial oxidation processes | |
| US4198384A (en) | Multistage incineration of halogenated hydrocarbon containing waste streams | |
| SU186607A1 (en) | BURNER OF DIRECT MIX FOR PYROLYSIS AND CONVERSION OF HYDROCARBONS | |
| DK2410276T4 (en) | Process for chemical reaction of a fuel with oxygen-containing gas by means of a pre-mix burner | |
| JP2003532535A (en) | Supply nozzle for gasification reactor of halogenated substances | |
| US20080033066A1 (en) | System and method for enhancing co production in a gas to liquid system | |
| JP2757966B2 (en) | gas turbine | |
| US5216968A (en) | Method of stabilizing a combustion process | |
| US2702744A (en) | Gasification of powdered fuel and use of a protective gas | |
| US2870231A (en) | Production of unsaturated hydrocarbons | |
| US2905544A (en) | Suspension process for the production of co and h2 from a solid carbonaceous fuel, oxygen and steam |