http://rdf.ncbi.nlm.nih.gov/pubchem/patent/ES-2545805-R1
Outgoing Links
Predicate | Object |
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assignee | http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_c186e9ae8cafab5df5c8d80cfa7b0fa1 |
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classificationCPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C02F1-441 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01D61-04 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01D71-36 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C02F1-444 |
classificationIPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01D69-02 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C02F1-44 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01D63-00 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01D71-36 |
filingDate | 2011-10-04-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
inventor | http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_70c260ef7be429c65612ca00fb5b3f19 http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_cafbdd20d3a401774198b154727dbf3c http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_ef29f7d64d41c0d8b677c85b818e287f |
publicationDate | 2015-10-08-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
publicationNumber | ES-2545805-R1 |
titleOfInvention | Separation Membrane for Seawater Desalination Pretreatment and Seawater Desalination Pretreatment Device |
abstract | A separation membrane is provided for seawater desalination pretreatment capable of supplying an adequate amount of natural water to an RO membrane constantly with a flow that remains high and without increasing the pressure, while withdrawing PET with a high withdrawal rate. A seawater desalination pretreatment device and a seawater desalination method are also provided. The separation membrane for seawater desalination pretreatment is a separation membrane for seawater desalination pretreatment used in the pretreatment for seawater desalination with a reverse osmosis membrane, where # a standard flow A is 2 m / c or more, which is defined as the maximum value of a flow that can meet P2 <= 1.5x1, where P1 represents an average intermembrane differential pressure for the initial 30 minutes and P2 represents an average differential pressure of intermembrane for the 30 minutes after a period of 120 minutes, when filtration is carried out at a fixed flow, and # a saccharide removal rate B or granular carbon removal rate C expressed by the following equations is 0.3, and desirably 0.5 or more; # Saccharide removal rate B = (1 - amount of saccharide in filtered water / amount of saccharide in natural water) # Carbon removal rate C granular = (1 - COP in filtered water / COP in natural water) # where COP refers to an amount of particulate organic carbon (a difference between a total organic carbon amount and a dissolved organic carbon amount). |
priorityDate | 2011-10-04-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
type | http://data.epo.org/linked-data/def/patent/Publication |
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