| Predicate |
Object |
| assignee |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_81ad53b64eb74859acdc01278829b080 |
| classificationCPCAdditional |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/F28D2021-0042
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/Y02P60-85 |
| classificationCPCInventive |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/F28F9-0273
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/F28D7-1669
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/F28D7-106
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/A23P30-00
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/A23L3-225
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/F28F9-02
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/A23L3-001
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/F28F9-0275
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/A23L3-22
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/A23L13-60 |
| classificationIPCInventive |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/A23L13-60
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/F28F9-02
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/F28D7-10
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/A23L3-22 |
| filingDate |
2014-11-18-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| inventor |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_60d6773f6b79e81464165d96ada351b5
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_45234e077d0efbe122a3f7d84a140ab8
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_6e318b834c035e88ac1f3958a5e50d54 |
| publicationDate |
2015-05-28-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| publicationNumber |
WO-2015075633-A1 |
| titleOfInvention |
Concentric symmetrical branched heat exchanger system |
| abstract |
A concentric symmetrical branched heat exchanger system (10) includes an inlet manifold (11) that divides the product flow evenly in the first section of the system and also includes an array (13) of tubular concentric heat exchangers (14) arranged in parallel and in series. Flow through each leg of the system can be divided further with secondary manifolds (12). Division of the product flow enables efficient heat exchange at higher and controllable product flow rates and at lower heat exchanger inlet pressures. Having lower inlet pressures reduces the heat exchanger construction cost and allows attachment of cutting or shaping devices at the exchanger exits to create uniquely shaped pieces. The cutting or shaping devices can be installed at the end of the branched heat exchanger to provide cooling and cutting in one process step while eliminating the material handling step of conveying product to and from a blast freezer or similar cooling device. |
| isCitedBy |
http://rdf.ncbi.nlm.nih.gov/pubchem/patent/NO-20190802-A1 |
| priorityDate |
2013-11-19-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| type |
http://data.epo.org/linked-data/def/patent/Publication |