Predicted protein targets (top 20)
| gene | UniProt | supporting neighbours | confidence | |
|---|---|---|---|---|
| ▸ | TTR | P02766 | 3/20 | 0.44 |
| ▸ | PTPRC | P08575 | 3/20 | 0.42 |
| ▸ | POLB | P06746 | 3/20 | 0.37 |
| ▸ | KMT2A | Q03164 | 2/20 | 0.37 |
| ▸ | MAPT | P10636 | 2/20 | 0.37 |
| ▸ | L3MBTL1 | Q9Y468 | 2/20 | 0.37 |
| ▸ | MEN1 | O00255 | 1/20 | 0.37 |
| ▸ | HPGD | P15428 | 1/20 | 0.37 |
| ▸ | CDC25A | P30304 | 1/20 | 0.37 |
| ▸ | CDC25B | P30305 | 1/20 | 0.37 |
| ▸ | CTDSP1 | Q9GZU7 | 1/20 | 0.37 |
| ▸ | TDP1 | Q9NUW8 | 1/20 | 0.37 |
| ▸ | CHEK1 | O14757 | 1/20 | 0.37 |
| ▸ | CSNK2A2 | P19784 | 4/20 | 0.35 |
| ▸ | CSNK2B | P67870 | 4/20 | 0.35 |
| ▸ | CSNK2A1 | P68400 | 4/20 | 0.35 |
| ▸ | CSNK2A3 | Q8NEV1 | 4/20 | 0.35 |
| ▸ | KDM4E | B2RXH2 | 1/20 | 0.34 |
| ▸ | CA12 | O43570 | 1/20 | 0.34 |
| ▸ | CA1 | P00915 | 1/20 | 0.34 |
Click a target to see other patent compounds predicted against it — the reverse direction, in place.
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 | |
|---|---|---|---|---|
| SCHEMBL599579 | 0.88 | TTR (0.44) | TTRPTPRCPOLBKMT2AMAPT | |
| SCHEMBL10947300 | 0.82 | S100A4 (0.43) | TTRPTPRCKMT2AMAPTHPGD | |
| SCHEMBL604996 | 0.81 | MAOA (0.39) | TTRPTPRCPOLBKMT2AMAPT | |
| SCHEMBL10942357 | 0.79 | KDM4E (0.40) | TTRPTPRCCSNK2A2CSNK2BCSNK2A1 | |
| SCHEMBL5846676 | 0.76 | MAPT (0.44) | POLBKMT2AMAPTMEN1HPGD | |
| SCHEMBL10945370 | 0.74 | — | — | |
| SCHEMBL10947560 | 0.74 | — | — | |
| SCHEMBL10944549 | 0.74 | TTR (0.33) | TTRPTPRCMAPTCSNK2A2CSNK2B | |
| SCHEMBL9680985 | 0.72 | ALDH1A1 (0.46) | POLBKMT2AMAPTL3MBTL1HPGD | |
| SCHEMBL10948633 | 0.72 | — | — |
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 294 patents — showing the first 20. claimed = in the patent's claims; disclosed = body only.
| Patent | Title | Assignee | Published | Priority | Filing | Country | Status |
|---|---|---|---|---|---|---|---|
| CN-107522610-B | Polycarboxylic acid production system with enhanced residence time distribution for oxidative digestion | 奇派特石化有限公司 | 2022-10-14 | — | — | CN | claimed |
| EP-1993989-B1 | POLYCARBOXYLIC ACID PRODUCTION SYSTEM EMPLOYING OXIDATIVE DIGESTION WITH REDUCED OR ELIMINATED UPSTREAM LIQUOR EXCHANGE | GRUPO PETROTEMEX SA DE CV (MX) | 2018-11-07 | — | — | EP | claimed |
| EP-1989164-B1 | POLYCARBOXYLIC ACID PRODUCTION SYSTEM EMPLOYING COOLED MOTHER LIQUOR FROM OXIDATIVE DIGESTION AS FEED TO IMPURITY PURGE SYSTEM | GRUPO PETROTEMEX SA DE CV (MX) | 2018-02-14 | — | — | EP | claimed |
| EP-2574606-B1 | Polycarboxylic acid production system employing cooled mother liquor from oxidative digestion as feed to impurity purge system | GRUPO PETROTEMEX SA DE CV (MX) | 2016-09-28 | — | — | EP | claimed |
| EP-2574606-A1 | Polycarboxylic acid production system employing cooled mother liquor from oxidative digestion as feed to impurity purge system | GRUPO PETROTEMEX, S.A. DE C.V. (MX) | 2013-04-03 | — | — | EP | claimed |
| US-7884232-B2 | For production of crude terephthalic acid by oxidation of p-xylene in bubble column reactor; cost efficiency | EASTMAN CHEMICAL COMPANY (US) | 2011-02-08 | — | — | US | claimed |
| EP-2251315-A1 | Crude therephthalic acid composition and production process thereof | EASTMAN CHEMICAL COMPANY (US) | 2010-11-17 | — | — | EP | claimed |
| US-7772424-B2 | producing purified terephthalic acid from para-xylene; purification; reduce impurities and by-products | EASTMAN CHEMICAL COMPANY (US) | 2010-08-10 | — | — | US | claimed |
| US-7683210-B2 | carried out in a bubble column reactor that provides for a highly efficient reaction at relatively low temperatures; crude terephthalic acid of higher purity than that made via conventional high temperature oxidation | EASTMAN CHEMICAL COMPANY (US) | 2010-03-23 | — | — | US | claimed |
| JP-2009528358-A | — | — | 2009-08-06 | — | — | JP | claimed |
| WO-2007103046-A2 | POLYCARBOXYLIC ACID PRODUCTION SYSTEM EMPLOYING OXIDATIVE DIGESTION WITH REDUCED OR ELIMINATED UPSTREAM LIQUOR EXCHANGE | EASTMAN CHEMICAL COMPANY (US) | 2007-09-13 | — | — | WO | claimed |
| WO-2007103047-A2 | POLYCARBOXYLIC ACID PRODUCTION SYSTEM WITH ENHANCED HEATING FOR OXIDATIVE DIGESTION | EASTMAN CHEMICAL COMPANY (US) | 2007-09-13 | — | — | WO | claimed |
| US-20070208190-A1 | Polycarboxylic acid production system employing oxidative digestion with reduced or eliminated upstream liquor exchange | ALPEK POLYESTER, S.A. DE C.V. (MX) | 2007-09-06 | — | — | US | claimed |
| US-20070208193-A1 | Polycarboxylic acid production system employing cooled mother liquor from oxidative digestion as feed to impurity purge system | ALPEK POLYESTER, S.A. DE C.V. (MX) | 2007-09-06 | — | — | US | claimed |
| US-20070208192-A1 | Polycarboxylic acid production system employing hot liquor removal downstream of oxidative digestion | ALPEK POLYESTER, S.A. DE C.V. (MX) | 2007-09-06 | — | — | US | claimed |
| US-20070208191-A1 | Polycarboxylic acid production system employing enhanced multistage oxidative digestion | ALPEK POLYESTER, S.A. DE C.V. (MX) | 2007-09-06 | — | — | US | claimed |
| EP-1784378-A1 | CRUDE TEREPHTHALIC ACID COMPOSITION AND PRODUCTION PROCESS THEREOF | EASTMAN CHEMICAL COMPANY (US) | 2007-05-16 | — | — | EP | claimed |
| US-20060287552-A1 | Optimized liquid-phase oxidation | GRUPO PETROTEMEX, S.A. DE C.V. (MX) | 2006-12-21 | — | — | US | claimed |
| WO-2006028818-A1 | CRUDE TEREPHTHALIC ACID COMPOSITION AND PRODUCTION PROCESS THEREOF | EASTMAN CHEMICAL COMPANY (US) | 2006-03-16 | — | — | WO | claimed |
| US-20060047148-A1 | Optimized liquid-phase oxidation | ALPEK POLYESTER, S.A. DE C.V. (MX) | 2006-03-02 | — | — | US | claimed |