摘要:
There is provided a method for protecting an apparatus from corrosion, which apparatus treats a nitric acid solution containing heavy metal(s) and/or compound(s) thereof, in which method stainless steel with a silicon content of 1% by weight or blow is used as the material composing the apparatus, and an NOx gas is compulsorily added into the nitric acid solution.
摘要:
A high-silicon-nickel-chromium steel resistant to concentrated nitric acid with a good workability and a good weldability, comprises
carbon in an amount of not more than 0.03% (C ≤ 0.03%), silicon in an amount of from more than 5%to not more than 7% (5% manganese in an amount of not more than 10% (Mn ≤ 10%), chromium in an amount of from not less than 7% to not more than 16% (7% ≤ Cr ≤ 16%), nickel in an amount of from not less than 10% to less than 19% (10% ≤ Ni and the balance being iron and inevitable impurities. percentages being by weight.
This steel can be used to provide corrosion resistant surfaces in apparatuses to be brought into contact with concentrated nitric acid.
摘要:
A method for improving (reducing or avoiding) surface defects in a specific steel resistant to concentrated nitric acid is described, wherein the specific steel in the molten state is either a stainless steel comprising C≦ 0.1 wt%. 2.5≦Si≦ 5 wt%. Mn≦2 wt%.
15≦Cr≦20 wt%. 10≦Ni≦22 wt%. C x 10≦ at least one of Nb. Ta and Zr≦2.5 wt%. the balance being iron and inevitable impurities. or a high-silicon-nickel-chromium steel comprising C≦0.03 wt% 5≦ Si≦7 wt%. Mn≦10 wt%. 7≦Cr≦16 wt% 10≦Ni≦19 wt%. C 4≦ at least one of Nb. Ta and Zr≦ 2 wt%
the balance being iron and inevitable impurities. and is admixed with titanium (0.05≦Ti≦0.2wt%) when producing said steel.
摘要:
To descale the inside of the jacket of a glass-lined vessel (e.g., reaction vessel) or conduit, especially of glass-and-metal, there is used a descaling solution of hydrochloric acid, preferably 5 to 15% by wt., containing 50 to 1,000 ppm of laurylamine, lauryldimethylamine or propargyl alcohol, at a temperature of 40 to 70°C., and optionally containing 0.1 to 5% by wt., of tin (II) chloride. The cleaning solution is circulated normally for 2 to 6 hours and drained and the jacket rinsed and neutralised with alkali. Iron oxide scale is thus totally removed, without damage by generation of hydrogen gas and without corrosion.
摘要:
An aqueous solution of hydroxylamine sulfate and a solution of nitric acid are each circulated from tanks (5, 6) through alternate adjacent chambers in an electrodialysis cell (2) or diffusion dialysis cell, the chambers being separated by cation exchange membrane (1); dialysis occurs so that NH₃OH⁺ and H⁺ ions pass through the membrane and the nitric acid is converted to hydroxylamine nitrate product. The solutions are recirculated by pumps (7, 8). In the hydroxylamine sulfate solution, the SO₄⁻⁻ anions remain, and since the H⁺ ions permeate thereinto, sulfuric acid is formed; and at a concentration of above 0.2 N the SO₄⁻ ion passes through the membrane and would contaminate the product. The NH₃OHNO₃ solution is therefore circulated simultaneously into a diffusion dialysis cell (22) having a number of anion exchange membranes (21); pure water is circulated countercurrently through alternate chambers in the cell (22) to remove the acid.
摘要:
An aqueous solution of hydroxylamine sulfate and a solution of nitric acid are each circulated from tanks (5, 6) through alternate adjacent chambers in an electrodialysis cell (2) or diffusion dialysis cell, the chambers being separated by cation exchange membrane (1); dialysis occurs so that NH₃OH⁺ and H⁺ ions pass through the membrane and the nitric acid is converted to hydroxylamine nitrate product. The solutions are recirculated by pumps (7, 8). In the hydroxylamine sulfate solution, the SO₄⁻⁻ anions remain, and since the H⁺ ions permeate thereinto, sulfuric acid is formed; and at a concentration of above 0.2 N the SO₄⁻ ion passes through the membrane and would contaminate the product. The NH₃OHNO₃ solution is therefore circulated simultaneously into a diffusion dialysis cell (22) having a number of anion exchange membranes (21); pure water is circulated countercurrently through alternate chambers in the cell (22) to remove the acid.