Hydrogen chloride dehydration method
AssigneeTokuyama Corporation
InventorsJunya Sakai, Shoji Iiyama
Life of this patent
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Abstract
A dehydration method in accordance with an embodiment of the present invention includes: a first dehydration step of bringing hydrogen chloride gas (21) and concentrated sulfuric acid (13A) into contact with each other; and a second dehydration step of bringing hydrogen chloride gas (21A) that has been obtained through the first dehydration step into contact with concentrated sulfuric acid (13B). A concentration of the concentrated sulfuric acid used in the second dehydration step is higher than a concentration of the concentrated sulfuric acid used in the first dehydration step.
Claims4
A method of dehydrating hydrogen chloride gas through a multi-step process, the method comprising:
- a first dehydration step of bringing hydrogen chloride gas and concentrated sulfuric acid into contact with each other;
- and
- a second dehydration step of bringing hydrogen chloride gas that has been obtained through the first dehydration step into contact with concentrated sulfuric acid,
- wherein a concentration of the concentrated sulfuric acid used in the second dehydration step is higher than a concentration of the concentrated sulfuric acid used in the first dehydration step,
- wherein at least part of the concentrated sulfuric acid that has been used in the second dehydration step is reused in the first dehydration step,
- wherein the multi-step process consists of the first dehydration step, the second dehydration step, and a third dehydration step carried out after the second dehydration step,
- wherein at least part of concentrated sulfuric acid that has been used in the third dehydration step is reused in the second dehydration step,
- a concentration of the concentrated sulfuric acid reused in the second dehydration step after having been used in the third dehydration step is not lower than 96 wt %,
- a concentration of the concentrated sulfuric acid reused in the first dehydration step after having been used in the second dehydration step is not lower than 85 wt % and lower than 96 wt %, and
- a concentration of the concentrated sulfuric acid after having been used in the first dehydration step is not lower than 75 wt % and lower than 85 wt %.
Dependencies are inferred from the claim text.