Method for selectively desorbing carbon disulfide in coarse benzene
A carbon disulfide and selective technology, applied in the field of coal chemical industry, can solve the problems of non-recyclable carbon disulfide, high energy consumption, cumbersome process, etc., and achieve the effects of high selective adsorption and removal rate, mild adsorption operation conditions, and simplified operation process.
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Embodiment 1
[0017] Removal of carbon disulfide:
[0018] Dissolve carbon disulfide in pure benzene to make simulated crude benzene, so that the concentration of carbon disulfide in simulated crude benzene is 3000mg / kg. 200g of 5A-type silica-alumina molecular sieve (Nankai University Catalyst Factory) was fixed in the adsorber, under normal temperature and pressure, the space velocity ratio was 0.7h -1 , into simulated crude benzene, the reaction result is that the adsorption and removal rate of carbon disulfide is 100%.
[0019] Recovery of carbon disulfide:
[0020] After the 5A-type silica-alumina molecular sieve adsorbent is saturated, the N 2 Purge, heat up to 300°C within 2 hours, maintain 300°C for 3 hours to purify for the first regeneration, and record the 5A-type silica-alumina molecular sieve after the first regeneration as sample I. N after purge 2 After being condensed by the condenser, the carbon disulfide in it is condensed and recovered, and the condensate is recorded ...
Embodiment 2
[0023] Removal of carbon disulfide:
[0024] Dissolve carbon disulfide in pure benzene to make simulated crude benzene, so that the concentration of carbon disulfide in simulated crude benzene is 3000mg / kg. Fix 200g of sodium Y-type silica-alumina molecular sieve (Nankai University Catalyst Factory) in the adsorber, under normal temperature and pressure, the space velocity ratio is 0.7h -1 , into simulated crude benzene, the reaction result is that the adsorption and removal rate of carbon disulfide is 100%.
[0025] Recovery of carbon disulfide:
[0026] After the sodium Y-type silica-alumina molecular sieve adsorbent is saturated, N 2 Purge, heat up to 300°C within 2 hours, maintain 300°C for 3 hours to purify for the first regeneration, and record the sodium Y-type silica-alumina molecular sieve after the first regeneration as sample III. N after purge 2 After being condensed by the condenser, the carbon disulfide in it is condensed and recovered, and the condensate is ...
Embodiment 3
[0029] Removal of carbon disulfide:
[0030] Dissolve carbon disulfide in pure benzene to make simulated crude benzene, so that the concentration of carbon disulfide in simulated crude benzene is 3000mg / kg. 200g of 13X type 13X silica-alumina molecular sieve (Nankai University Catalyst Factory) was fixed in the adsorber, under normal temperature and pressure, the space velocity ratio was 0.7h -1 , into simulated crude benzene, the reaction result is that the adsorption and removal rate of carbon disulfide is 100%.
[0031] Recovery of carbon disulfide:
[0032] After the 13X-type silica-alumina molecular sieve adsorbent is saturated, N 2 Purge, heat up to 300°C within 2 hours, maintain 300°C for 3 hours to purify for the first regeneration, and record the 13X-type silica-alumina molecular sieve after the first regeneration as sample VI. N after purge 2 After being condensed by the condenser, the carbon disulfide in it is condensed and recovered, and the condensate is recor...
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