⚠ Novel chemotype — no close known analogue (best Tanimoto < 0.3). Unexplored chemical space relative to ChEMBL.
Similar compounds — the chemically nearest patent molecules
Nearest neighbours by Morgan-fingerprint cosine across the patent-compound collection, with each neighbour's top predicted target and the predicted targets it shares with this molecule.
| Compound | similarity | top predicted | shared targets | |
|---|---|---|---|---|
| SCHEMBL30784603 | 0.87 | — | — | |
| SCHEMBL32689416 | 0.87 | — | — | |
| SCHEMBL5484757 | 0.87 | — | — | |
| SCHEMBL8836529 | 0.87 | — | — | |
| SCHEMBL15465901 | 0.82 | — | — | |
| SCHEMBL60759 | 0.82 | — | — | |
| SCHEMBL336140 | 0.82 | — | — | |
| SCHEMBL1288146 | 0.82 | — | — | |
| SCHEMBL755304 | 0.82 | — | — | |
| SCHEMBL8836511 | 0.78 | — | — |
Similarity is cosine over the 2,048-bit Morgan fingerprint (≈ Tanimoto). Identical fingerprints score 1.00.
Patent provenance — the patents this molecule appears in, and who filed them
Claimed or disclosed in 63 patents — showing the first 20. claimed = in the patent's claims; disclosed = body only.
| Patent | Title | Assignee | Published | Priority | Filing | Country | Status |
|---|---|---|---|---|---|---|---|
| CN-118317832-A | Hydrocracking catalyst comprising Y zeolite and beta zeolite having a lattice parameter strictly greater than 24.50 angstrom at a Y/beta ratio of 5 to 12 for producing naphtha | IFP 新能源公司 | 2024-07-09 | — | — | CN | disclosed |
| CN-118317833-A | Hydrocracking catalyst comprising zeolite Y and zeolite beta in a Y/beta ratio strictly greater than 12 for naphtha production | IFP 新能源公司 | 2024-07-09 | — | — | CN | disclosed |
| WO-2024126013-A1 | HYDROCRACKING CATALYST COMPRISING A SPECIFIC ZEOLITE Y FOR NAPHTHA PRODUCTION | IFP Energies Nouvelles (FR) | 2024-06-20 | — | — | WO | disclosed |
| WO-2024110231-A1 | PROCESS FOR PRODUCING MIDDLE DISTILLATES COMPRISING A SERIES OF CATALYSTS INCLUDING A BETA ZEOLITE CATALYST HAVING A SILICA/ALUMINA RATIO OF LESS THAN 25 | IFP Energies Nouvelles (FR) | 2024-05-30 | — | — | WO | disclosed |
| WO-2024110230-A1 | PROCESS FOR PRODUCING MIDDLE DISTILLATES BY CO-PROCESSING OF MINERAL FEEDSTOCK WITH A RENEWABLE FEEDSTOCK COMPRISING A SERIES OF CATALYSTS, INCLUDING A BETA ZEOLITE-BASED CATALYST | IFP Energies Nouvelles (FR) | 2024-05-30 | — | — | WO | disclosed |
| CN-115747530-B | Method for separating and extracting molybdenum and tungsten from molybdenum-tungsten bulk concentrate | 郑州大学 | 2023-12-01 | — | — | CN | disclosed |
| WO-2023169943-A1 | HYDROCRACKING CATALYST COMPRISING TWO ZEOLITES Y, ONE SPECIFIC ZEOLITE Y OF WHICH BEING FOR NAPHTHA PRODUCTION | IFP Energies Nouvelles (FR) | 2023-09-14 | — | — | WO | disclosed |
| WO-2023117475-A1 | CATALYST COMPRISING A SUPPORT BASED ON SILICO-ALUMINIC MATRIX AND ON ZEOLITE, PREPARATION THEREOF AND PROCESS FOR HYDROCRACKING HYDROCARBON FEEDSTOCKS | IFP Energies Nouvelles (FR) | 2023-06-29 | — | — | WO | disclosed |
| WO-2023110650-A1 | HYDROCRACKING CATALYST COMPRISING A SPECIFIC ZEOLITE Y AND AN MFI-STRUCTURE ZEOLITE FOR PRODUCING A STEAM-CRACKING FEEDSTOCK | IFP Energies Nouvelles (FR) | 2023-06-22 | — | — | WO | disclosed |
| WO-2023094396-A1 | HYDROCRACKING CATALYST COMPRISING A ZEOLITE Y AND A ZEOLITE BETA IN A Y/BETA RATIO STRICTLY GREATER THAN 12 FOR NAPHTHA PRODUCTION | IFP Energies Nouvelles (FR) | 2023-06-01 | — | — | WO | disclosed |
| US-20090118556-A1 | ZEOLITIC CATALYST WITH A CONTROLLED DOPING ELEMENT CONTENT, AND IMPROVED PROCESS FOR PROCESSING HYDROCARBON FEEDS | INSTITUT FRANCAIS DU PETROLE (FR) | 2009-05-07 | — | — | US | disclosed |
| CN-101208411-A | Method for producing middle distillates by the hydroisomerization and hydrocracking of feedstocks obtained from the fischer-tropsch method | INST FRANCAIS DU PETROLE (FR) | 2008-06-25 | — | — | CN | disclosed |
| US-20070118008-A1 | Process for producing middle distillates by hydroisomerizing and hydrocracking feeds from the Fischer-Tropsch process | INSTITUT FRANCAIS DU PETROLE (FR) | 2007-05-24 | — | — | US | disclosed |
| US-20070056879-A1 | Process for producing middle distillates by hydroisomerizing and hydrocracking feeds from the fischer-tropsch process using a doped catalyst based on mesoporous alumina-silica with a controlled macropore content | INSTITUT FRANCAIS DU PETROLE (FR) | 2007-03-15 | — | — | US | disclosed |
| US-20070017850-A1 | Process for producing middle distillates by hydroisomerizing and hydrocracking feeds from the Fischer-Tropsch process using a multifunctional guard bed | INSTITUT FRANCAIS DU PETROLE (FR) | 2007-01-25 | — | — | US | disclosed |
| CN-1290815-C | Glutaraldehyde preparing method by cyclopentene heterogeneous catalytic oxidation | DALIAN CHEMICAL PHYSICS INST (CN) | 2006-12-20 | — | — | CN | disclosed |
| US-20060070915-A1 | Doped catalyst and improved process for treatment of hydrocarbon feedstocks | INSTITUT FRANCAIS DU PETROLE (FR) | 2006-04-06 | — | — | US | disclosed |
| CN-1490294-A | Glutaraldehyde preparing method by cyclopentene heterogeneous catalytic oxidation | 中国科学院大连化学物理研究所 | 2004-04-21 | — | — | CN | disclosed |
| CN-1113841-C | Cyclopentene oxidizing process for synthesizing glutaraldehyde | QILU PETROCHEMICAL CO SINOPEC (CN) | 2003-07-09 | — | — | CN | disclosed |
| CN-1348948-A | Cyclopentene oxidizing process for synthesizing glutaraldehyde | QILU PETROCHEMICAL CO CHINA (CN) | 2002-05-15 | — | — | CN | disclosed |