We manufacture nitrogen plants and oxygen plants as per the latest technology & design of the Company ING. L. & A., BOSCHI, ITALY. This technology has been proven all over the world for its working efficiency & trouble free operation.
Theory
UCCA.UCCB nitrogen-purifying process using carbon as a catalyst. Reactions between carbon catalyst and the remainder oxygen in the feed nitrogen at certain temperatures, produce CO2, chemical equation is C+O2 , if the content of oxygen is less than 5 ppm then it removes water and Co2 through the dry adsorption process, and impurities are removed through filter. Nitrogen with the purity higher than 99.9995% is thus obtained .UCC nitrogen- purifying plants The plant needs feed nitrogen according to 1.1 times of the purity nitrogen output. When the feed nitrogen purity is 99.99%. it gives the ideal operating cost.UCCA is for single-de oxy-tower process users, where the users do not want continuous working. UCCB for dual-deoxy-tower process, users can operate the equipment when adding catalyst, applicable to the users who need continuous working.
UCHA NITROGN PURIFYING PLANT
THE DATA IN THE TABLE BASED ON TEMP. TO 32 DEGEE C
AMBIENT TEMP ., PURITY OF FEED NITROGEN IS WITHIN 99.9%
| MODEL |
FEED NITROGEN
|
PURITY NITROGEN |
H2 CONSUMPTION |
POWER |
COOLING WATER |
L*B*H |
| UCHA-10 |
11 |
10 |
0.11 |
2 |
0.4 |
1200*920*1650 |
| UCHA-20 |
22 |
20 |
0.22 |
3 |
0.8 |
1250*980*1650 |
| UCHA-40 |
44 |
40 |
0.44 |
4 |
1.2 |
1350*1020*1700 |
| UCHA-60 |
66 |
60 |
0.66 |
5 |
1.5 |
1380*1050*1700 |
| UCHA-80 |
88 |
80 |
0.88 |
6 |
1.5 |
1450*1050*1750 |
| UCHA-100 |
110 |
100 |
1.1 |
7 |
2.0 |
1480*1150*1800 |
| UCHA-150 |
165 |
150 |
1.65 |
9 |
2.8 |
1580*1250*1800 |
| UCHA-200 |
220 |
200 |
2.2 |
12 |
3.6 |
1680*1300*1900 |
| UCHA-400 |
440 |
400 |
4.4 |
20 |
5 |
1820*1500*1950 |
| UCHA-800 |
880 |
800 |
8.8 |
30 |
8 |
2020*1600*2100 |
| UCHA-2000 |
2200 |
2000 |
22 |
50 |
15 |
2056*1900*2300 |
| UCHA-3000 |
3300 |
3000 |
33 |
70 |
20 |
2900*2400*2500 |
UCHB NITROGN PURIFYING PLANT
THE DATA IN THE TABLE BASED ON TEMP. TO 32 DEGEE C
AMBIENT TEMP ., 99.5% NITROGEN PURITY.
| MODEL |
FEED NITROGEN
|
PURITY NITROGEN |
H2 CONSUMPTION |
POWER |
COOLING WATER |
L*B*H |
| UCHB-10 |
11 |
10 |
0.23 |
2 |
0.4 |
1200*920*1650 |
| UCHB-20 |
22 |
20 |
0.45 |
3 |
0.8 |
1250*980*1650 |
| UCHB-40 |
44 |
40 |
0.9 |
4 |
1.2 |
1350*1020*1700 |
| UCHB-60 |
66 |
60 |
1.35 |
5 |
1.5 |
1380*1050*1700 |
| UCHB-80 |
88 |
80 |
1.8 |
6 |
1.5 |
1450*1050*1750 |
| UCHB-100 |
110 |
100 |
2.25 |
7 |
2.0 |
1480*1150*1800 |
| UCHB-150 |
165 |
150 |
3.4 |
9 |
2.8 |
1580*1250*1800 |
| UCHB-200 |
220 |
200 |
4.5 |
12 |
3.6 |
1680*1300*1900 |
| UCHB-400 |
440 |
400 |
9 |
20 |
5 |
1820*1500*1950 |
| UCHB-800 |
880 |
800 |
18 |
30 |
8 |
2020*1600*2100 |
| UCHB-2000 |
2200 |
2000 |
45 |
50 |
15 |
2056*1900*2300 |
| UCHB-3000 |
3300 |
3000 |
67 |
70 |
20 |
2900*2400*2500 |
THE PURITY OF FEED NITROGEN IS WITHIN 99-99.9%,DIFFERENT FEED NITROGEN
PURITY WITH DIFFRENT HYDROGEN
CONSUMPTION.
UCC NITROGN PURIFYING PLANT
GAS PURITY >99.995% OXYGEN CONTENT<5PPM DEW POINT <-60DEGREEC CO2CONTENT<3PPM
| MODEL |
FEED NITROGEN
|
PURITY NITROGEN |
CATALYST FILLED |
POWER |
COOLING WATER |
L*B*H |
| UCC-10 |
11 |
10 |
16 |
0.7 |
0.7 |
1120*920*1600 |
| UCC-20 |
22 |
20 |
32 |
1.5 |
1.5 |
1180*980*1630 |
| UCC-40 |
44 |
40 |
64 |
2.5 |
2.5 |
1260*1190*1750 |
| UCC-60 |
66 |
60 |
96 |
3.2 |
3.2 |
1380*1270*1820 |
| UCC-80 |
88 |
80 |
128 |
4.8 |
4.8 |
1460*1360*1850 |
| UCC-100 |
110 |
100 |
160 |
6.3 |
6.3 |
1620*1480*1900 |
| UCC-150 |
165 |
150 |
240 |
9.2 |
9.2 |
1780*1560*2000 |
| UCC-200 |
220 |
200 |
320 |
15.8 |
15.8 |
1920*1740*2050 |
| UCC-300 |
330 |
300 |
480 |
22.0 |
22.0 |
2210*1980*2150 |
| UCC-500 |
550 |
500 |
800 |
30.0 |
30.0 |
2500*2100*2150 |
