MODEL CONTENTS |
KDN- 225(D) |
KDN- 500(D) |
KDN-800/40Y(F) |
KDN- 1000(D) |
KDN- 1000/40Y(Z) | |
流程形式 Type Process |
液氮倒灌 LIN-inject |
液氮倒灌 LIN-inject |
返流膨胀 Reverse flow |
液氮倒灌 LIN-inject |
正流膨胀 Common flow | |
氮气产量GAN flow |
Nm3/h |
225 |
500 |
800 |
1000 |
1000 |
液氮产量LIN flow |
L/h |
— |
— |
40 |
— |
40 |
产品氮纯度Nitrogen Purity |
ppm(O2) |
≤2 |
≤2 |
≤3 |
≤2 |
≤5 |
氮气压力GAN pressure |
MPa |
≤0.85 |
≤0.85 |
~0.7 |
≤0.85 |
≤0.3 |
启动时间Start-up time |
小时 h |
~12 |
~12 |
~18 |
~12 |
~16 |
设备运行周期Operating period |
年 year |
≥1 |
≥1 |
≥1 |
≥1 |
≥1 |
续前表1:
MODEL CONTENTS |
KDN- 1000/50Y(F) |
KDN- 1200/60Y(F) |
KDN- 1500/70Y(F) |
KDN- 1600/150Y(F) |
KDN- 2000/80Y(F) | |
流程形式 Type Process |
返流膨胀 Reverse flow |
返流膨胀 Reverse flow |
返流膨胀 Reverse flow |
返流膨胀 Reverse flow |
返流膨胀 Reverse flow | |
氮气产量GAN flow |
Nm3/h |
1000 |
1200 |
1500 |
1600 |
2000 |
液氮产量LIN flow |
L/h |
50 |
60 |
70 |
150 |
80 |
产品氮纯度Nitrogen Purity |
ppm(O2) |
≤2 |
≤2 |
≤10 |
≤10 |
≤2 |
氮气压力GAN pressure |
MPa |
≤0.85 |
~0.7 |
≤0.85 |
~0.3 |
≤0.85 |
启动时间Start-up time |
小时 h |
~18 |
~18 |
~16 |
~16 |
~20 |
设备运行周期Operating period |
年 year |
≥1 |
≥1 |
≥2 |
≥2 |
≥2 |
续前表2:
MODEL CONTENTS |
KDN- 3000/80Y(F) |
KDN- 4000/150Y(F) |
KDN- 4500/150Y(F) |
KDN- 5000 (Z) |
KDN- 6000/200Y(F) | |
流程形式 Type Process |
返流膨胀 Reverse flow |
返流膨胀 Reverse flow |
返流膨胀 Reverse flow |
正流膨胀 Common flow |
返流膨胀 Reverse flow | |
氮气产量GAN flow |
Nm3/h |
3000 |
4000 |
4500 |
5000 |
6000 |
液氮产量LIN flow |
L/h |
80 |
150 |
150 |
— |
200 |
产品氮纯度Nitrogen Purity |
ppm(O2) |
≤5 |
≤2 |
≤2 |
≤0.5 |
≤2 |
氮气压力GAN pressure |
MPa |
~0.65 |
~0.7 |
~0.6 |
~0.23 |
~0.6 |
启动时间Start-up time |
小时 h |
~18 |
~20 |
~20 |
~24 |
~20 |
设备运行周期Operating period |
年 year |
≥2 |
≥2 |
≥2 |
≥2 |
≥2 |