|
5A |
|
|
|
|
||
|
1.7-2.5 |
2.0-3.0 |
|||||
|
(RH75%,25 degree )% |
23 |
23 |
23 |
|
||
|
(25 degree ,760mmHg) |
10 |
10 |
11 |
|
||
|
(25 degree ,760mmHg) |
30 |
30 |
30 |
|
||
|
CH4adsorption |
16 |
16 |
16 |
|
||
|
30 |
30 |
40 |
|
|||
|
0.74±0.02 |
0.74±0.02 |
0.74±0.02 |
|
|||
|
0.30 |
0.30 |
0.30 |
|
|||
|
98 |
98 |
98 |
|
|||
5A molecular sieve has a well-developed three-dimensional pore structure, and the pore diameter of the crystal is 0.5nm mainly used in (PSA) variable pressure adsorption H₂, CO and O₂ production devices and large-scale n-isomeric alkane separation devices in petrochemical enterprises and other industrial fields.
1.Conversion gas or hydrogen reforming
2.Methanol cracking gas or methanol choke gas
3.Ammonia tail gas
4.Coke oven gas, barren gas, water gas
5.Refinery hydrogenation low fraction gas
6.Catalytic dry gas
The purity of hydrogen production is usually increased to 99.9+%, and the hydrogen recovery rate is 60% ~ 90%.
Feed hydrogen concentration > 55% is considered economical and reasonable
If the feed hydrogen content is between 40% and 50%, it can be economically upgraded according to the site specific requirements
If the feed hydrogen content is below 40%, it is difficult to achieve economic rationality
25KG carton, lined with PP sealed bag
235L sealed steel drum(net weight:150kg )
Lined with sealed polypropylene container bag (600KG or 750KG)
Minimum order quantity 1kg
Total supply 10000
Delivery period Delivery within 5 days from the date of payment
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