http://rdf.ncbi.nlm.nih.gov/pubchem/patent/CN-211035766-U

Outgoing Links

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assignee http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_ef330e1c1c52e49c6ab1040b6e038b48
classificationIPCInventive http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07H1-00
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/A61P31-12
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07H19-056
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/A61K31-7056
filingDate 2019-11-26-04:00^^<http://www.w3.org/2001/XMLSchema#date>
grantDate 2020-07-17-04:00^^<http://www.w3.org/2001/XMLSchema#date>
inventor http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_edd28f08715d0cde69fa000eb09cf615
publicationDate 2020-07-17-04:00^^<http://www.w3.org/2001/XMLSchema#date>
publicationNumber CN-211035766-U
titleOfInvention Chemical drug synthesis system
abstract The utility model discloses a chemical drug synthesis system, wherein a liquid ammonia steel cylinder is arranged at the front end of the synthesis system, the liquid ammonia steel cylinder is connected with an ammonolysis reaction kettle through a pipeline, the ammonolysis reaction kettle is connected with a fresh methanol storage tank through a pipeline, and the fresh methanol storage tank is provided with a first magnetic circulating pump on the pipeline between the ammonolysis reaction kettles; the rear end of the ammonolysis reaction kettle is provided with a plate and frame type pressure filter through a pipeline, the ammonolysis reaction kettle is connected with an ammonia adsorption device through a pipeline, and the rear end of the plate and frame type pressure filter is connected with a crystallization kettle through a pipeline; the rear end of the crystallization kettle is connected with a separation tank through a pipeline, the rear end of the separation tank is connected with a double-cone vacuum drier through a pipeline, and the rear end of the separation tank is connected with a recovered ethanol distillation kettle through a pipeline. The synthesis system realizes continuous production, improves the production efficiency, utilizes the recovered methanol and ethanol for production, and saves the production cost.
priorityDate 2019-11-26-04:00^^<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: 24.