http://rdf.ncbi.nlm.nih.gov/pubchem/patent/CN-205874555-U

Outgoing Links

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assignee http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_7a3a2a5697f08ca194442d98a4e0abb4
classificationIPCInventive http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C25B1-26
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C25B9-00
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C25B15-02
filingDate 2016-03-29-04:00^^<http://www.w3.org/2001/XMLSchema#date>
grantDate 2017-01-11-04:00^^<http://www.w3.org/2001/XMLSchema#date>
inventor http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_ee583e79bb396f87bcbb95776725fc5b
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_d79f6a6b8335086e6e21272faa8a1ed9
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_0458961f2890cdf0da83eeea58848299
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_0b30a398f63ea687626d9d613a29dda3
publicationDate 2017-01-11-04:00^^<http://www.w3.org/2001/XMLSchema#date>
publicationNumber CN-205874555-U
titleOfInvention Subacidity brineelectrolysis generater
abstract The utility model belongs to the technical field of the disinfection, two kinds of subacidity brineelectrolysis generater of concretely relates to, one kind including supplying trunk line for the raw water, the bypass, supply the hydrochloric acid pipeline, the electrolysis trough, electrolysate pipeline and control system, along raw water supplier to being equipped with an in proper order on the trunk line, two nodes of b, a node and trunk line intercommunication are passed through to the one end of bypass, the other end inserts the electrolysis trough, supply the middle section of hydrochloric acid pipeline connected bypass, the electrolysate pipeline is connected to the delivery port of electrolysis trough, electrolysate pipeline through crosses b node and trunk line intercommunication, trunk line a, installation automatic control valve no. 1 on the pipeline section between two nodes of b, installation pH detector no. 1 on the electrolysate pipeline, automatic control valve two, dilution ratio through the control system automatic control electrolysate, another kind of then the dilution ratio of manual control electrolysate. These two kinds of schemes can both the accurate control electrolysate dilution ratio to the subacidity brineelectrolysis of pH value between 5.0~6.5 that is met the requirements.
isCitedBy http://rdf.ncbi.nlm.nih.gov/pubchem/patent/CN-107928886-A
http://rdf.ncbi.nlm.nih.gov/pubchem/patent/CN-115215412-A
http://rdf.ncbi.nlm.nih.gov/pubchem/patent/CN-108265311-A
priorityDate 2016-03-29-04:00^^<http://www.w3.org/2001/XMLSchema#date>
type http://data.epo.org/linked-data/def/patent/Publication

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Total number of triples: 31.