http://rdf.ncbi.nlm.nih.gov/pubchem/patent/CN-113856507-A
Outgoing Links
| Predicate | Object |
|---|---|
| assignee | http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_62f4d8f0c6a29ec21e41a5ccb8acab76 |
| classificationCPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C01F7-02 |
| classificationIPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01F23-70 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C01F7-02 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01F23-00 |
| filingDate | 2021-10-18-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| inventor | http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_5ef0b749c58074ae2a03f0649beb83d6 http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_1354e1f796fbd6e42b8928bfa2c21598 http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_738e009449378376b9b0784ccec82e7a http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_7ec1a2e6ca4a56397cb05631fd360120 http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_618ae391947b0b55c572ae228b9b58eb http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_a3d3fbf1090eae2c83d2badc19706aa1 http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_8719f41a6cc589562840f74b0d17c22d |
| publicationDate | 2021-12-31-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| publicationNumber | CN-113856507-A |
| titleOfInvention | A kind of imported bauxite slurry preparation device and method |
| abstract | The present invention relates to a process method for preparing imported bauxite slurry. The device is connected with a high-concentration mother liquor tank, the outlet of the high-concentration mother liquor tank is connected with the secondary preparation tank, the mill is provided with a conveyor for conveying bauxite, and the pre-desilication tank is provided with a heating Heating pipeline, a mixer for stirring is installed in the secondary mixing tank; the process conditions include NK concentration of low-concentration batching mother liquor 190g/l, high-concentration batching NK concentration 210g/l, solid content of primary batching not less than 400g/l, The solid content of the secondary batching is 280g/l, the NK concentration of the primary batching pulp is 180g/l, and the NK concentration of the secondary batching is not less than 190g/l. After the secondary batching is completed, the requirements of desiliconization efficiency and dissolution economy are satisfied at the same time. The technological process of the present invention Simple and efficient. |
| priorityDate | 2021-10-18-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| type | http://data.epo.org/linked-data/def/patent/Publication |
Incoming Links
Total number of triples: 23.