METHOD OF OIL PRODUCING
FIELD: petroleum chemistry. SUBSTANCE: method involves hydrotreatment of petroleum oil fractions at the first stage in the presence of catalyst and at the second stage - products obtained at the first stage in the presence of high-silicon catalyst of paraffinization followed by hydrogenizate stabili...
Saved in:
Main Authors | , , , |
---|---|
Format | Patent |
Language | English Russian |
Published |
10.02.1996
|
Subjects | |
Online Access | Get full text |
Cover
Loading…
Abstract | FIELD: petroleum chemistry. SUBSTANCE: method involves hydrotreatment of petroleum oil fractions at the first stage in the presence of catalyst and at the second stage - products obtained at the first stage in the presence of high-silicon catalyst of paraffinization followed by hydrogenizate stabilization. At the first stage catalyst is used at the following ratio of components, wt.-%: nickel oxide 4-6; molybdenum oxide 15-20; zeolite type Z in nickel-hydrogen form 40-50, and aluminium oxychloride - the rest up to 100%. The yield is 87.1 wt.-%. EFFECT: increased yield of the end products. 2 tbl
Изобретение относится к нефтехимии, в частности к получению масел. Цель - повышение выхода целевых продуктов. Получение ведут путем гидрообработки нефтяных масляных фракций на первой ступени в присутствии катализатора и на второй ступени - продуктов первой ступени в присутствии высококремнистого катализатора депарафинизации с последующей стабилизацией гидрогенизата. На первой ступени используют катализатор при следующем соотношении компонентов, мас. %: оксид никеля 4 - 6, оксид молибдена 15 - 20, цеолит типа Y в никельводородной форме 8 - 10, цеолит пентасил в никельводородной форме 40 - 50, оксихлорид алюминия - остальное до 100%. Выход до 87,1 мас.%. 2 табл. |
---|---|
AbstractList | FIELD: petroleum chemistry. SUBSTANCE: method involves hydrotreatment of petroleum oil fractions at the first stage in the presence of catalyst and at the second stage - products obtained at the first stage in the presence of high-silicon catalyst of paraffinization followed by hydrogenizate stabilization. At the first stage catalyst is used at the following ratio of components, wt.-%: nickel oxide 4-6; molybdenum oxide 15-20; zeolite type Z in nickel-hydrogen form 40-50, and aluminium oxychloride - the rest up to 100%. The yield is 87.1 wt.-%. EFFECT: increased yield of the end products. 2 tbl
Изобретение относится к нефтехимии, в частности к получению масел. Цель - повышение выхода целевых продуктов. Получение ведут путем гидрообработки нефтяных масляных фракций на первой ступени в присутствии катализатора и на второй ступени - продуктов первой ступени в присутствии высококремнистого катализатора депарафинизации с последующей стабилизацией гидрогенизата. На первой ступени используют катализатор при следующем соотношении компонентов, мас. %: оксид никеля 4 - 6, оксид молибдена 15 - 20, цеолит типа Y в никельводородной форме 8 - 10, цеолит пентасил в никельводородной форме 40 - 50, оксихлорид алюминия - остальное до 100%. Выход до 87,1 мас.%. 2 табл. |
Author | Esipko E.A Prokof'ev V.P Boldinov V.A Kamenskij A.A |
Author_xml | – fullname: Prokof'ev V.P – fullname: Boldinov V.A – fullname: Kamenskij A.A – fullname: Esipko E.A |
BookMark | eNrjYmDJy89L5WQQ93UN8fB3UfB3U_D39FEICPJ3CXX29HPnYWBNS8wpTuWF0twMCm6uIc4euqkF-fGpxQWJyal5qSXxwaGGZsbmxobGjobGRCgBAFUcIL8 |
ContentType | Patent |
DBID | EVB |
DatabaseName | esp@cenet |
DatabaseTitleList | |
Database_xml | – sequence: 1 dbid: EVB name: esp@cenet url: http://worldwide.espacenet.com/singleLineSearch?locale=en_EP sourceTypes: Open Access Repository |
DeliveryMethod | fulltext_linktorsrc |
Discipline | Medicine Chemistry Sciences |
DocumentTitleAlternate | СПОСОБ ПОЛУЧЕНИЯ МАСЕЛ |
ExternalDocumentID | SU1637313A1 |
GroupedDBID | EVB |
ID | FETCH-epo_espacenet_SU1637313A13 |
IEDL.DBID | EVB |
IngestDate | Fri Jul 19 12:28:14 EDT 2024 |
IsOpenAccess | true |
IsPeerReviewed | false |
IsScholarly | false |
Language | English Russian |
LinkModel | DirectLink |
MergedId | FETCHMERGED-epo_espacenet_SU1637313A13 |
Notes | Application Number: SU19884637531 |
OpenAccessLink | https://worldwide.espacenet.com/publicationDetails/biblio?FT=D&date=19960210&DB=EPODOC&CC=SU&NR=1637313A1 |
ParticipantIDs | epo_espacenet_SU1637313A1 |
PublicationCentury | 1900 |
PublicationDate | 19960210 |
PublicationDateYYYYMMDD | 1996-02-10 |
PublicationDate_xml | – month: 02 year: 1996 text: 19960210 day: 10 |
PublicationDecade | 1990 |
PublicationYear | 1996 |
RelatedCompanies | Kamenskij A.A |
RelatedCompanies_xml | – name: Kamenskij A.A |
Score | 2.4547439 |
Snippet | FIELD: petroleum chemistry. SUBSTANCE: method involves hydrotreatment of petroleum oil fractions at the first stage in the presence of catalyst and at the... |
SourceID | epo |
SourceType | Open Access Repository |
SubjectTerms | CHEMISTRY CRACKING HYDROCARBON OILS FUELS LUBRICANTS METALLURGY MINERAL WAXES PEAT PETROLEUM, GAS OR COKE INDUSTRIES PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVEHYDROGENATION, OLIGOMERISATION, POLYMERISATION RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, ORGASES REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS REFORMING OF NAPHTHA TECHNICAL GASES CONTAINING CARBON MONOXIDE |
Title | METHOD OF OIL PRODUCING |
URI | https://worldwide.espacenet.com/publicationDetails/biblio?FT=D&date=19960210&DB=EPODOC&locale=&CC=SU&NR=1637313A1 |
hasFullText | 1 |
inHoldings | 1 |
isFullTextHit | |
isPrint | |
link | http://utb.summon.serialssolutions.com/2.0.0/link/0/eLvHCXMwfV07T8MwED5VBQEblFd5KQPKFtFg5zVEiNoJKSIPtQnqVtlOInWBqk3F38eJksICm2VLZ_ukz3dn33cGuLcRF7jAWDNFWWq4sE2NCWOkYeZwZtncRLxmI4eRGWT4dW7Me7DsuDBNndCvpjiiRJSQeK-a83r1c4lFm9zKzQNfyq7PJz91qZq3dDGzDmFUOna9JKYxUQlxZ5kaTV3pdlhIR88yUNqTXrRVg8F7H9eklNVvi-Ifw34ihX1UJ9BbbwdwSLqP1wZwELbv3bLZQm9zChehlwYxVWJfiSdvSjKNaUYm0csZKL6XkkCTMyx2u1nMst1a0Dn0ZZBfXIJilNxCj6VgpYOkxnLHFgxxpuc1uVk4bAjDP8Vc_TN2DUddnrE-uoF-td4Wt9KMVvyuUcA3cON0zQ |
link.rule.ids | 230,309,783,888,25576,76876 |
linkProvider | European Patent Office |
linkToHtml | http://utb.summon.serialssolutions.com/2.0.0/link/0/eLvHCXMwfV07T8MwED5VBVE2KK_yzICyRTQ4zyFCNE5IIC-1CepW2U4idYGqTcXfx4mSwgKbZUtn-6TPd2ffdwa4NxBlSqEoksbKUlIKQ5MIU8eSQkxKdINqiNZs5DDSvEx5navzHiw7LkxTJ_SrKY7IEcU43qvmvF79XGLhJrdy80CXvOvzyU0tLOYtXUyrQxgRTywniXFsi7ZtzTIxmlrc7dCRjJ55oLTHPWy9BoPzPqlJKavfFsU9gv2EC_uojqG33g5hYHcfrw3hIGzfu3mzhd7mBM5DJ_ViLMSuEPuBkExjnNl-9HIKguuktifxGRa73Sxm2W4t6Az6PMgvLkBQS6qjx5KR0kRcY7lpMIIokfOa3MxMMoLRn2Iu_xm7g4GXhsEi8KO3Kzjsco7l8TX0q_W2uOEmtaK3jTK-ARTgd8A |
openUrl | ctx_ver=Z39.88-2004&ctx_enc=info%3Aofi%2Fenc%3AUTF-8&rfr_id=info%3Asid%2Fsummon.serialssolutions.com&rft_val_fmt=info%3Aofi%2Ffmt%3Akev%3Amtx%3Apatent&rft.title=METHOD+OF+OIL+PRODUCING&rft.inventor=Prokof%27ev+V.P&rft.inventor=Boldinov+V.A&rft.inventor=Kamenskij+A.A&rft.inventor=Esipko+E.A&rft.date=1996-02-10&rft.externalDBID=A1&rft.externalDocID=SU1637313A1 |