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    • 83. 发明授权
    • Process for purifying gaseous formaldehyde
    • 甲醛净化方法
    • US4203735A
    • 1980-05-20
    • US895553
    • 1978-04-12
    • Paolo ColomboPierino Radici
    • Paolo ColomboPierino Radici
    • C07C47/058C07C45/00C07C45/78C07C47/04C07C67/00B01D53/12
    • C07C45/79
    • Raw gaseous formaldehyde is purified by passing it through a first series of superimposed fluidized beds of solid adsorbent, maintained at 80.degree.-140.degree. C., while continuously circulating solid adsorbent from each bed to the underlying bed and discharging from the lowermost bed the spent adsorbent, delivering the latter to the uppermost bed of a second series of superimposed fluidized beds of solid adsorbent, passing through the latter a stream of inert gas to strip the adsorbed formaldehyde at 130.degree.-150.degree. C., while continuously circulating said spent adsorbent from each bed to the underlying bed and discharging from the lowermost bed the adsorbent thus treated, delivering the latter to the uppermost bed of a third series of fluidized beds of solid adsorbent, and passing through the latter a stream of inert gas to regenerate the adsorbent at 145.degree.-250.degree. C., while continuously circulating the adsorbent from each bed to the underlying bed, discharging the regenerated adsorbent from the lowermost bed and recycling said regenerated adsorbent to the uppermost bed of the first series.
    • 通过将原始气态甲醛通过固体吸附剂的第一系列叠加的流化床,保持在80-140℃,同时将固体吸附剂从每个床连续循环到下面的床并从最下面的床排出,从而净化 吸附剂,将其输送到固体吸附剂的第二系列叠加流化床的最上层,通过惰性气体流在130-150℃下分离吸附的甲醛,同时连续循环所述废吸附剂 从每个床到下面的床,并从最下层的床排出由此处理的吸附剂,将其输送到固体吸附剂的第三系列流化床的最上层,并通过惰性气体流再生吸附剂 在145°-250℃下,同时将吸附剂从每个床连续循环到下层床,排出再生吸附剂 t并将所述再生吸附剂再循环到第一系列的最上层。