http://rdf.ncbi.nlm.nih.gov/pubchem/patent/CN-204208332-U
Outgoing Links
| Predicate | Object |
|---|---|
| assignee | http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_d6a6f422b091ba12ea61d4adbf1b0e8e |
| classificationIPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07H15-256 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01D9-02 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07H1-06 |
| filingDate | 2014-10-08-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| grantDate | 2015-03-18-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| inventor | http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_75cbf43511db6914732a3154c4a56548 http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_132ab358e9d0d0da9bcc79af673fc1c9 |
| publicationDate | 2015-03-18-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| publicationNumber | CN-204208332-U |
| titleOfInvention | Continuous purification prepares high-purity content rebaudioside-A crystallization apparatus |
| abstract | The utility model relates to the purification preparation technology of RA, be specifically related to a kind of continuous purification and prepare high-purity content rebaudioside-A crystallization apparatus, the utility model comprises primary crystallization district, secondary crystallization district and post processing zone, and described primary crystallization district is left standstill tank, centrifugal filter device, evaporator and drying device connected to form successively by pipeline by the first storage tank, the second agitator tank, one-level; Described secondary crystallization district comprises secondary agitator tank, secondary leaves standstill tank and centrifugal filter device; Described secondary agitator tank leaves standstill tank by pipeline and secondary and is connected, and secondary is left standstill tank and is connected with centrifugal filter device by pipeline; Described post processing zone comprises the second storage tank, the 3rd storage tank, the first agitator tank, centrifugal filter device.The utility model has the advantages that: crystallization process is controlled, by controlling the crystallization time in each district, making between crystallizing cycle and yield, to reach best equalization point, reducing crystallizing cycle, thus reaching best separating effect. |
| isCitedBy | http://rdf.ncbi.nlm.nih.gov/pubchem/patent/CN-104548648-A |
| priorityDate | 2014-10-08-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| type | http://data.epo.org/linked-data/def/patent/Publication |
Incoming Links
Total number of triples: 27.