Preparation of boron trifluoride and sulfuric acid from boron trifluoride hydrate
A technology of boron trifluoride and hydrate, applied in the direction of boron halide compounds, sulfur trioxide/sulfuric acid, sulfur compounds, etc.
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Embodiment 1
[0038] A setup consisting of two reactors in series was used. The first reactor has a volume of 400 ml (200 ml is the effective volume of the reaction medium) and is equipped with a helical stirrer (4 blades) with a diameter of 4 cm; the rotational speed of the stirrer head is 500 revolutions per minute. The temperature was maintained at 104-107°C in order to extract the heat of reaction and the reactor was jacketed with a heat transfer fluid flow.
[0039] Continuous weighing of two reactants - Industrial BF 3 Hydrate and 65% oleum were added to the reactor which initially contained 200 ml of 100% sulfuric acid. Industrial BF powered by peristaltic pumps 3 The hydrate and the fuming sulfuric acid provided by the piston metering pump enter the reaction medium through two dip tubes installed side by side. The overflow of this reactor flows to a second reactor having the same characteristics (volume, agitation, etc.) as the first reactor. Industrial BF 3 Hydrates have the f...
Embodiment 2
[0050] Example 2 (Compared)
[0051] The same procedure as in Example 1 was followed except that no hydrogen peroxide was added to the second reactor. BF recovered in the first reactor 3 Has commodity BF 3 characteristics (organic carbon content less than 5 mg / kg BF 3 , did not detect any trace CO 2 ), but the sulfuric acid discharged from the second reactor was black and contained 20 mg organic carbon / kg H 2 SO 4 .
Embodiment 3
[0052] Example 3 :(Compared)
[0053] Use an industrial BF with the following characteristics 3 Hydrate:
[0054] BF 3 =47.7%
[0055] h 2 O = 52.3%
[0056] Density = 1.38
[0057] Organic carbon content: 620 mg / kg industrial BF 3 Hydrate Repeat the method of Example 2.
[0058] Industrial BF 3 The feed rate of hydrate was 188 g / hour and the feed rate of oleum was 681 g / hour. The residual sulfuric acid flow from the second reactor overflow was 784 g / h. Before blowing off the sulfuric acid, BF 3 The mass concentration is 1.3%. blowing off BF with air 3 After that, the sulfuric acid concentration was 98.4% H 2 SO 4 and 1.6% H 2 O.
[0059] BF released is recovered in a trap at the top of the first reactor 3 , analyzing the BF trapped with water 3 , to determine its organic and inorganic carbon (CO 2 ) content; it per kilogram BF 3 contains less than 10 mg of organic carbon.
[0060] The sulfuric acid recovered in the overflow of the second reactor co...
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