
基本信息:
- 专利标题: 处理氯化镁溶液的方法
- 申请号:CN201480036874.0 申请日:2014-07-02
- 公开(公告)号:CN105358484B 公开(公告)日:2018-02-06
- 发明人: J·J·德弗里斯 , R·弗雷迪安斯亚 , A·B·德哈恩
- 申请人: 普拉克生化公司
- 申请人地址: 荷兰霍林赫姆
- 专利权人: 普拉克生化公司
- 当前专利权人: 普拉克生化公司
- 当前专利权人地址: 荷兰霍林赫姆
- 代理机构: 中国国际贸易促进委员会专利商标事务所
- 代理人: 孙爱
- 优先权: 13174834.5 2013.07.03 EP
- 国际申请: PCT/EP2014/064059 2014.07.02
- 国际公布: WO2015/000956 EN 2015.01.08
- 进入国家日期: 2015-12-28
- 主分类号: C01F5/10
- IPC分类号: C01F5/10 ; C12P7/40 ; C01B13/18 ; C01F5/06
The invention pertains to a method for processing MgCl2 solutions comprising the steps of - providing an aqueous solution comprising 5-25 wt.% of MgCl2 and optionally organic contaminants to an evaporation step, wherein water and, where present, organic components are evaporated, - withdrawing an aqueous solution with a MgCl2 concentration of 25-35 wt.% from an evaporation step and providing it to a preconcentrator where it is contacted with a HCl containing gas stream with a temperature of at least 300°C, - providing an aqueous solution with a MgCl2 concentration of 35-45 wt.% resulting from the preconcentrator to a thermohydrolysis reactor, the reactor being at a temperature of at least 300°C, - withdrawing MgO from the thermohydrolysis reactor in solid form, and withdrawing a HCl containing gas stream from the thermohydrolysis reactor, said HCl-containing gas stream having a temperature of at least 300°C, - providing the HCl-containing gas stream with a temperature of at least 300°C to the preconcentrator, - withdrawing a HCl-containing gas stream with a temperature of at most 150°C from the preconcentrator. It has been found that the process according to the invention can be integrated into a fermentation process in such a manner that a stable and efficient process is obtained.
公开/授权文献:
- CN105358484A 处理氯化镁溶液的方法 公开/授权日:2016-02-24
IPC结构图谱:
C | 化学;冶金 |
--C01 | 无机化学 |
----C01F | 金属铍、镁、铝、钙、锶、钡、镭、钍的化合物,或稀土金属的化合物 |
------C01F5/00 | 镁的化合物 |
--------C01F5/02 | .氧化镁 |
----------C01F5/06 | ..用镁化合物的热分解法 |
------------C01F5/10 | ...用氯化镁与水蒸气的热分解法 |