阳高新闻:A11VO60DR/10R-NPC12K -NPC12K52
分级的操作法使底部的晶粒与上部未生长到产品粒度的互相分，取出管是插在底部，因此产品取出来的都是均匀的球状大粒结晶，这是它大优点。但是循环泵的输送量在整个结晶器内是一定的，这就造成结晶器内晶粒的流态化的终端速度和晶浆浓度(也就是空隙率的大小)的限制，这样必然带来两个缺点:个是过饱和度较大，但是安全的过饱和介稳区域一般都是很狭窄的，而且生产上往往不允许越过介稳区的上限，一般都在介稳区中部或偏上一点。
A11VO40LRS/10R-NSC12N00
A11VO40LRS/10R-NPC12N00 R-NSC12N00
A11VO40LRH2/10R-NPC12N00
A11VO40DRS/10R-NSC12N00
A11VO40DRS/10R-NPC12N00
A11VO60LRS/10R-NSC12N00
A11VO60LRS/10R-NPC12N00
A11VO60LRS/10R-NSC12K01
A11VO60LRS/10R-NPC12K01
A11VO60LRH2/10R-NSC12N00
A11VO60LRH2/10R-NPC12N00
A11VO60LRH2/10R-NSC12K01
A11VO60LRH2/10R-NPC12K01
A11VO60DRS/10R-NSC12N00
A11VO60DRS/10R-NPC12N00
A11VO60DRS/10R-NSC12K01
A11VO60DRS/10R-NPC12K01
A11VO75LRS/10R-NSD12N00
A11VO75LRS/10R-NPD12N00
A11VO75LRS/10R-NSD12K01
A11VO75LRS/10R-NPD12K01
0R-NPD12N00 R-NSD12K01
A11VO75LRH2/10R-NPD12K01
A11VO75DRS/10R-NSD12N00
A11VO75DRS/10R-NPD12N00
A11VO75DRS/10R-NSD12K01
A11VO75DRS/10R-NPD12K01
A11VO95LRS/10R-NSD12N00
A11VO95LRS/10R-NPD12N00
A11VO95LRS/10R-NSD12K01
A11VO95LRS/10R-NPD12K01
A11VO95LRH2/10R-NSD12N00
A11VO95LRH2/10R-NPD12N00
A11VO95LRH2/10R-NSD12K01
A11VO95LRH2/10R-NPD12K01
A11VO95DRS/10R-NSD12N00
A11VO95DRS/10R-NPD12N00
A11VO95DRS/10R-NSD12K01
A11VO95DRS/10R-NPD12K01
A11VO130LRS/10R-NSD12N00
A11VO130LRS/10R-NPD12N00
A11VO130LRS/10R-NSD12K02
A11VO130LRS/10R-NPD12K0 /10R-NSD12N0 /10R-NPD12N0 /10R-NSD12K0 /10R-NPD12K02
0R-NPD12N00 R-NSD12K02
A11VO130DRS/10R-NPD12K02
A11VLO190LRS/11R-NSD12N00
A11VLO190LRS/11R-NPD12N00
A11VLO190LRS/11R-NSD12K02
A11VLO190LRS/11R-NPD12K02
A11VOL190LRS/11R-NSD12N00
A11VOL190LRS/11R-NPD12N00
A11VOL190LRS/11R-NSD12K02
A11VOL190LRS/11R-NPD12K02
