⚠ 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 | |
|---|---|---|---|---|
| SCHEMBL28272237 | 0.80 | — | — | |
| SCHEMBL6525302 | 0.79 | — | — | |
| SCHEMBL6907542 | 0.79 | — | — | |
| SCHEMBL4730261 | 0.79 | — | — | |
| SCHEMBL9842114 | 0.75 | — | — | |
| Methane SCHEMBL28000160 | 0.72 | — | — | |
| Fluoride SCHEMBL27206897 | 0.72 | — | — | |
| SCHEMBL6058221 | 0.69 | — | — | |
| SCHEMBL157338 | 0.69 | — | — | |
| SCHEMBL819657 | 0.69 | — | — |
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 34 patents — showing the first 20. claimed = in the patent's claims; disclosed = body only.
| Patent | Title | Assignee | Published | Priority | Filing | Country | Status |
|---|---|---|---|---|---|---|---|
| US-8835702-B2 | Method for mitigating the formation of by-products during the production of haloalkane compounds | HONEYWELL INTERNATIONAL INC. (US) | 2014-09-16 | — | — | US | claimed |
| EP-1509485-B1 | 1,1,1,3,3-PENTACHLOROPROPANE PROCESS PURGE STREAM CONCENTRATION USING A SECONDARY REFLUXED EVAPORATOR AND SECONDARY PRODUCT RECOVERY | OCCIDENTAL CHEM CO (US) | 2013-03-13 | — | — | EP | claimed |
| EP-1509485-A4 | 1,1,1,3,3-PENTACHLOROPROPANE PROCESS PURGE STREAM CONCENTRATION USING A SECONDARY REFLUXED EVAPORATOR AND SECONDARY PRODUCT RECOVERY | BASIC CHEMICALS COMPANY LLC (US) | 2006-06-14 | — | — | EP | claimed |
| EP-1509485-A1 | 1,1,1,3,3-PENTACHLOROPROPANE PROCESS PURGE STREAM CONCENTRATION USING A SECONDARY REFLUXED EVAPORATOR AND SECONDARY PRODUCT RECOVERY | Vulcan Chemicals (US) | 2005-03-02 | — | — | EP | claimed |
| US-6720466-B2 | A two-stage distillation process for economically producing 1,1,1,3,3-pentachloroprpane by reacting carbon tetrachloride and vinyl chloride under conditions which preserve the activity of the catalyst | Vulcan Chemicals, a division of Vulcan Materials Company | 2004-04-13 | — | — | US | claimed |
| WO-2003089391-A1 | 1,1,1,3,3-PENTACHLOROPROPANE PROCESS PURGE STREAM CONCENTRATION USING A SECONDARY REFLUXED EVAPORATOR AND SECONDARY PRODUCT RECOVERY | VULCAN CHEMICALS (US) | 2003-10-30 | — | — | WO | claimed |
| US-20030199716-A1 | 1,1,1,3,3-pentachloropropane process purge stream concentration using a secondary refluxed evaporator and secondary product recovery | VULCAN CHEMICALS DIVISION OF VULCAN MATERIALS COMPANY | 2003-10-23 | — | — | US | claimed |
| CN-105753633-A | Method For Mitigating The Formation Of By-products During The Production Of Haloalkane Compounds | 霍尼韦尔国际公司 | 2016-07-13 | — | — | CN | disclosed |
| US-8835702-B2 | Method for mitigating the formation of by-products during the production of haloalkane compounds | HONEYWELL INTERNATIONAL INC. (US) | 2014-09-16 | — | — | US | disclosed |
| US-8835702-B2 | Method for mitigating the formation of by-products during the production of haloalkane compounds | HONEYWELL INTERNATIONAL INC. (US) | 2014-09-16 | — | — | US | disclosed |
| EP-2718250-A2 | METHOD FOR MITIGATING THE FORMATION OF BY-PRODUCTS DURING THE PRODUCTION OF HALOALKANE COMPOUNDS | Honeywell International, Inc. (US) | 2014-04-16 | — | — | EP | disclosed |
| EP-2718250-A2 | METHOD FOR MITIGATING THE FORMATION OF BY-PRODUCTS DURING THE PRODUCTION OF HALOALKANE COMPOUNDS | Honeywell International, Inc. (US) | 2014-04-16 | — | — | EP | disclosed |
| CN-103562165-A | Method for slowing down the formation of by-products during the production of haloalkane compounds | HONEYWELL INT INC | 2014-02-05 | — | — | CN | disclosed |
| US-20030149316-A1 | Separation of heavy ends from streams of halogenated alkanes | OCCIDENTAL CHEMICAL CORPORATION | 2003-08-07 | — | — | US | disclosed |
| EP-1328496-A1 | PROCESS FOR THE MANUFACTURE OF 1,1,1,3,3-PENTACHLOROPROPANE | Vulcan Materials Company (US) | 2003-07-23 | — | — | EP | disclosed |
| US-6552238-B1 | Introducing steam into bottom fraction, removing vapors and condensing | VULCAN CHEMICALS | 2003-04-22 | — | — | US | disclosed |
| WO-2003020676-A1 | SEPARATION OF HEAVY ENDS FROM STREAMS OF HALOGENATED ALKANES | VULCAN CHEMICALS (US) | 2003-03-13 | — | — | WO | disclosed |
| WO-2002028806-A1 | PROCESS FOR THE MANUFACTURE OF 1,1,1,3,3-PENTACHLOROPROPANE | VULCAN MATERIALS COMPANY (US) | 2002-04-11 | — | — | WO | disclosed |
| US-6313360-B1 | Process for the manufacture of 1, 1, 1, 3, 3-pentachloropropane | VULCAN MATERIALS COMPANY | 2001-11-06 | — | — | US | disclosed |
| EP-0729932-A1 | Method of producing halopropane | CENTRAL GLASS COMPANY, LIMITED (JP) | 1996-09-04 | — | — | EP | disclosed |