SU193531A1 - - Google Patents
Info
- Publication number
- SU193531A1 SU193531A1 SU1010543A SU1010543A SU193531A1 SU 193531 A1 SU193531 A1 SU 193531A1 SU 1010543 A SU1010543 A SU 1010543A SU 1010543 A SU1010543 A SU 1010543A SU 193531 A1 SU193531 A1 SU 193531A1
- Authority
- SU
- USSR - Soviet Union
- Prior art keywords
- pyrolysate
- resin
- producing
- ammonia
- carried out
- Prior art date
Links
- CVSVTCORWBXHQV-UHFFFAOYSA-N creatine zwitterion Chemical compound NC(=[NH2+])N(C)CC([O-])=O CVSVTCORWBXHQV-UHFFFAOYSA-N 0.000 description 5
- QGZKDVFQNNGYKY-UHFFFAOYSA-N ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 3
- 150000002989 phenols Chemical class 0.000 description 3
- 238000000197 pyrolysis Methods 0.000 description 3
- 239000011347 resin Substances 0.000 description 3
- 229920005989 resin Polymers 0.000 description 3
- ISWSIDIOOBJBQZ-UHFFFAOYSA-N Phenol Natural products OC1=CC=CC=C1 ISWSIDIOOBJBQZ-UHFFFAOYSA-N 0.000 description 2
- 239000003054 catalyst Substances 0.000 description 2
- 238000004508 fractional distillation Methods 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 239000002023 wood Substances 0.000 description 2
- 239000000969 carrier Substances 0.000 description 1
- 238000005039 chemical industry Methods 0.000 description 1
- 230000017858 demethylation Effects 0.000 description 1
- 238000010520 demethylation reaction Methods 0.000 description 1
- 238000004821 distillation Methods 0.000 description 1
- 150000002148 esters Chemical class 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000005011 phenolic resin Substances 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
Description
СПОСОБ ПОЛУЧЕНИЯ МНОГОАТОМНЫХ ФЕНОЛОВMETHOD OF OBTAINING MULTIHEADABLE PHENOLS
Изобретение относитс к области получени многоатомных фенолов, вл ющихс ценным сырьем дл химической промышленности. This invention relates to the field of producing polyatomic phenols, which are valuable raw materials for the chemical industry.
Известен способ получени многоатомных фбноло в, состо щий в том, что древесную смолу подвергают парофазному пиролизу при 450-600°С С последующей фракционной разгонкой лолученного пиролизата.A known method for producing polyatomic fbnolo in consists in that the wood resin is subjected to vapor phase pyrolysis at 450-600 ° C With the subsequent fractional distillation of the obtained pyrolysate.
Выход пиролизата 57%.The output of pyrolysate 57%.
Дл уокорепи процесса и увеличени выхода целевого продукта предлагаетс процесс вести в присутствии катализатора - аммиака.In order to increase the yield of the target product, the process is proposed to be carried out in the presence of an ammonia catalyst.
Пример. Пиролиз газогенераторной смолы .провод т в терМОконтактном аппарате с твердым теплоносителем при 350-550°С. Одповременно со смолой в аппарат ввод тExample. The pyrolysis of the gas-generating resin is carried out in a thermal-contact apparatus with a solid heat carrier at 350-550 ° C. Along with the resin is introduced into the apparatus
аммиак 10%-ной концентрации. Деметилирование эфиров фенолов смолы протекает в паровой фазе. Полученный пиролизат подвергают фракционной нерегонке.ammonia 10% concentration. Demethylation of phenol resin esters occurs in the vapor phase. The resulting pyrolysate is subjected to fractional non-distillation.
Предмет изобретени Subject invention
Способ получени многоатомных фенолов путем парофазного пиролиза древесной смоjibi при повышенной температуре.с носледуюи;ей фракционной разгонкой полученного пиролизата , отличающийс тем, что, с целью увеличени выхода пиролизата и сокращени продолжительности процесса, последний ведут в присутствии аммиака в качестве катализатора .The method of producing polyatomic phenols by vapor-phase pyrolysis of wood smibi at elevated temperature is followed by fractional distillation of the resulting pyrolysate, characterized in that, in order to increase the yield of pyrolysate and reduce the duration of the process, the latter is carried out in the presence of ammonia as a catalyst.
Publications (1)
Publication Number | Publication Date |
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SU193531A1 true SU193531A1 (en) |
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