http://rdf.ncbi.nlm.nih.gov/pubchem/patent/ES-2756323-T3
Outgoing Links
| Predicate | Object |
|---|---|
| assignee | http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_94e91bcfb95d6bf93d4686e071458ccc |
| classificationCPCAdditional | http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C02F2201-4612 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C02F2001-46142 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C02F2209-29 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C02F2103-08 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C02F2209-05 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C02F2201-4613 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C02F1-36 |
| classificationCPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C02F1-4672 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C02F1-46104 |
| classificationIPCAdditional | http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C02F1-00 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C02F1-30 |
| classificationIPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C02F1-461 |
| filingDate | 2008-04-23-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| grantDate | 2020-04-27-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| inventor | http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_37b97d829c695d78afc2e6126ecd854d http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_5c31859d49243ab28056438c944f5a12 http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_5d2d44ea84cc5d2e7081ee18600825de http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_d23b9fdb2e99334f6e4c1bafb615eb4e http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_08378d6c621fa0e12d06164e6661e935 |
| publicationDate | 2020-04-27-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| publicationNumber | ES-2756323-T3 |
| titleOfInvention | Microcurrent Electrolysis Sterilization Device and Algaecide Method |
| abstract | Microcurrent electrolysis sterilization algicidal device intended to be actuated for electrolysis of seawater or freshwater bodies, comprising: - a tank (5) with an inlet tube (1) and an outlet tube (6 ); - a solution conductivity detector (2) arranged in the inlet tube; - an ultrasonically enhanced microcurrent generator comprising: o a DC electrolysis power supply; or a group of electrolysis electrodes (4), said group of electrolysis electrodes (4) comprising electrodes arranged equidistant in the tank (5) with the order of an auxiliary electrode (14.37) between an anode (12 , 39) and a cathode (13,38), the electrodes in the electrode group (4) are tubular electrodes or sheet electrodes, in the event that the electrodes in the electrode group (4) are tubular electrodes, the tubular electrodes are furthermore arranged coaxially along the radial direction; - a plurality of electrode cable connectors; - an ultrasonic generator (33); and - an ultrasonic reflector (9,41), said ultrasonic generator (33) and said ultrasonic reflector (9) being arranged at both ends of the tank, said ultrasonic generator (33) comprising at least one ultrasonic energy converter (17); the group of electrodes (4) is positioned between the ultrasonic generator and the ultrasonic reflector (9), - a controller comprising: - an evaluation unit; - an electrolysis model unit that is available in three types: - a seawater electrolysis model unit, configured to control the auxiliary electrode (14.37) in an inactive state, through electrolysis between the anode ( 12.39) and the cathode (13.38) after receiving activation signals; - a freshwater electrolysis model unit, configured to, after receiving activation signals, control the auxiliary electrode (14.37) being taken as the cathode, the cathode (13.38), called the original cathode (13.38 ), taken as the anode and the attribute of the anode (12.39), called the original anode (12.39), remains unchanged and the corresponding spaced electrode is shortened to 1/2 of the so-called original spacing used in the seawater mode ; and - a pole inversion electrolysis model unit, said evaluation unit is configured to activate, on the basis of the conductivity value detected by the conductivity detector, the corresponding seawater electrolysis model unit, the unit of freshwater electrolysis model and pole inversion electrolysis model unit, according to a conductivity value of above or below 1500 nS / cm; 40 when the conductivity value is above 1500 nS / cm, activate the seawater electrolysis model unit or when the conductivity value is below 1500 nS / cm, activate the water electrolysis model unit fresh, and when the freshwater electrolysis model is used and the electrolysis potential increases by 20% under the same current conditions, indicate that cathode fouling occurs during the electrolysis process; and when the electrolysis potential (U1 + U2 + U3) increases by 20% under the same electrolysis current and in the same body of fresh water, the pole reversal electrolysis model unit with the current density no greater that 20mA / cm2 and a pole inversion electrolysis time of no more than 1h, where U1 comprises the potential of the electrode and the anode oxidation polarization overpotential; U2 is defined by the following formula: U2 = IR = I x (d / S x μ); where I is the electrolysis current, R is the solution resistance, d is the electrode spacing, S is the electrolysis area and μ is the conductivity of water masses; and U3 comprises the potential of the electrode and the cathode oxidation polarization overpotential, the pole inversion electrolysis consists of: - changing the polarity of the so-called original cathode (13,38), functioning as an anode in the model unit of fresh water electrolysis, at the cathode; - change the polarity of the auxiliary electrode (14,37) at the anode; and - deactivate the so-called original anode (12,39). |
| priorityDate | 2008-04-23-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| type | http://data.epo.org/linked-data/def/patent/Publication |
Incoming Links
Total number of triples: 41.