SU545661A1 - The method of obtaining raw materials for the production of carbon black - Google Patents
The method of obtaining raw materials for the production of carbon blackInfo
- Publication number
- SU545661A1 SU545661A1 SU2135405A SU2135405A SU545661A1 SU 545661 A1 SU545661 A1 SU 545661A1 SU 2135405 A SU2135405 A SU 2135405A SU 2135405 A SU2135405 A SU 2135405A SU 545661 A1 SU545661 A1 SU 545661A1
- Authority
- SU
- USSR - Soviet Union
- Prior art keywords
- raw materials
- production
- carbon black
- obtaining raw
- dealkylation
- Prior art date
Links
Landscapes
- Pigments, Carbon Blacks, Or Wood Stains (AREA)
Description
бестоимость на 2-4 руб. за 1 т и ниже в зкость (см. таблицу). Пример. Газойлевую фракцию, вылипающую в пределах 250-5ОО°С, полученнуюThe cost of 2-4 rubles. 1 t and below viscosity (see table). Example. Gas oil fraction, discharging within 250-5OO ° C, obtained
при термическом крекинге смеси экстракта селективной очистки масел и газойл коксовани , подвергают деалкилированию на пилотной установке. Процесс деалкилировани ведут при температуре 565°С, давлении 30 кг/см и времени реакции 1,5 мин. Из продуктов используют в качестве сырь дл активных и высокоструктурных саж фракцию 20О-500°С. Выход ее составл ет 78%, а в пеоесчете на сырье термокрекинга - 4О%.during thermal cracking of a mixture of an extract of selective purification of oils and gas oil coking, is subjected to dealkylation on a pilot plant. The dealkylation process is carried out at a temperature of 565 ° C, a pressure of 30 kg / cm and a reaction time of 1.5 minutes. Of the products used in the raw material for active and highly structural carbon blacks is a fraction of 20–500 ° C. Its yield is 78%, and in terms of thermal cracking feedstock it is 4%.
кию в присутстви:и водорода на пилотной установке . Процесс ведут при емпературе 550°С, давлении 30 кг/см , времени реакции 2 мин и при мол рном соотношении водорода и сырь деалкилировани 3:1.cue present: and hydrogen on a pilot plant. The process is carried out at a temperature of 550 ° C, a pressure of 30 kg / cm, a reaction time of 2 minutes, and a molar ratio of hydrogen and raw material of dealkylation of 3: 1.
Из продуктов реакции вьщел ют фракцию, кип щую выше , которую используют в качестве сырь дл активных и высокоструктурных саж. Выход ее составл ет 82%,From the reaction products, the fraction boiling above is used, which is used as a raw material for active and highly structural carbon blacks. Its yield is 82%,
а в пересчете на сырье термокрекинга - 41%. П р и м е р 2, Газойлевую фракцию, кип тую в пределах 25О-50О°С полученную при термическом крекинге ароматизирован- ных дистилл тов, подвергают деалкилироваand in terms of raw materials of thermal cracking - 41%. PRI me R 2, the gas oil fraction boiled within 25 ° -50 ° C obtained during the thermal cracking of aromatized distillates is subjected to dealkylation
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| SU2135405A SU545661A1 (en) | 1975-05-16 | 1975-05-16 | The method of obtaining raw materials for the production of carbon black |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| SU2135405A SU545661A1 (en) | 1975-05-16 | 1975-05-16 | The method of obtaining raw materials for the production of carbon black |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| SU545661A1 true SU545661A1 (en) | 1977-02-05 |
Family
ID=20619801
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| SU2135405A SU545661A1 (en) | 1975-05-16 | 1975-05-16 | The method of obtaining raw materials for the production of carbon black |
Country Status (1)
| Country | Link |
|---|---|
| SU (1) | SU545661A1 (en) |
-
1975
- 1975-05-16 SU SU2135405A patent/SU545661A1/en active
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US2423674A (en) | Process of catalytic cracking of petroleum hydrocarbons | |
| GB1386270A (en) | Treatment of by-productoils | |
| GB1481800A (en) | Production of coke | |
| SU545661A1 (en) | The method of obtaining raw materials for the production of carbon black | |
| CH508565A (en) | Prepn of vinyl chloride from acetylene ethylene formed | |
| GB1442691A (en) | Process for producing low sulphur content fuel oils | |
| GB1178528A (en) | Combined Preparation of Electrode Binder Pitch and Carbon Black Feedstock | |
| GB872075A (en) | Nuclear reactor for the generation of energy from fissile elements | |
| US3255270A (en) | Production of acetylene | |
| SU59096A1 (en) | The method of obtaining acetone, acetaldehyde and acetic acid | |
| SU1320221A1 (en) | Method of producing aromatic hydrocarbons | |
| SU557089A1 (en) | The method of processing hydrocarbon raw materials | |
| SU732359A1 (en) | Method of producing fillers and plastifiers for rubber and caoutchou | |
| SU1379304A1 (en) | Method of producing raw material for producing commercial carbon | |
| SU1560543A1 (en) | Method of obtaining needle coke | |
| GB874440A (en) | Improvements in or relating to the preparation of petroleum coke | |
| SU431205A1 (en) | METHOD FOR PREPARATION OF HYDROCARBON RAW FOR COXING: »hPT ^^ 5. ;.; g isijy | |
| JPS5448810A (en) | Liquefaction of coal | |
| SU857227A1 (en) | Method of producing material for carbon black and coke | |
| SU682130A3 (en) | Process for preparation of furfural | |
| SU910727A1 (en) | Process for producing olefins | |
| SU443018A1 (en) | Method for isolating concentrated pyrene fraction | |
| SU1213062A1 (en) | Method of producing highlyaromatized pitch-like product | |
| JPS57212294A (en) | Pyrolysis of heavy hydrocarbon oil | |
| SU148037A1 (en) | Method for producing naphthalene |