A method for reducing the accumulation of nitrogen trichloride during the use of liquid chlorine
A nitrogen trichloride and liquid chlorine technology, applied in the container discharge method, container filling method, gas treatment/storage purpose, etc., can solve problems such as equipment damage, accumulation of nitrogen trichloride, casualties, etc., to eliminate explosions effect of risk
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Embodiment 1
[0032] The storage tank used has a feed inlet higher than the discharge outlet, and the inclination of the cylinder is 5°. The vaporizer used has the inlet at the top and the outlet at the bottom. The buffer tank used has its inlet and outlet on the same level.
[0033] When the liquid chlorine tank truck 1 unloads, the liquid chlorine pressure in the liquid chlorine storage tank 2 is about 0.6MPa, and the pressure of the liquid chlorine coming out of the storage tank 2 outlets is raised to about 0.8MPa by the discharge pump 3, and the The flow rate of about 200kg / hr is delivered to vaporizer 4. The vaporizer 4 is heated by hot water to keep the temperature inside the vaporizer 4 at about 30° C., and the chlorine gas obtained at the outlet of the vaporizer 4 enters the buffer tank 5 . The chlorine gas with a pressure of about 0.8MPa obtained at the outlet of the buffer tank 5 enters the tank car 1, so that the liquid chlorine in the tank car 1 is continuously discharged to t...
Embodiment 2
[0037] In the storage tank used, its feed inlet is higher than the discharge outlet, and the angle formed by the inclined plane formed by the horizontal height of the feed inlet and the horizontal height of the discharge outlet and the horizontal plane is 20°. In the vaporizer used, the feed inlet is higher than the discharge outlet, and the angle between the inclined plane formed by the level of the feed inlet and the level of the discharge outlet and the horizontal plane is 30°. In the buffer tank used, the feed inlet is higher than the discharge outlet, and the angle between the inclined plane formed by the level of the feed inlet and the level of the discharge outlet and the horizontal plane is 40°.
[0038] When the liquid chlorine tank truck 1 was unloading, the liquid chlorine pressure in the liquid chlorine storage tank 2 was about 0.7MPa, and the pressure of the liquid chlorine coming out of the storage tank 2 discharge port was raised to about 0.9MPa by the discharge ...
Embodiment 3
[0042] In the storage tank used, its feed inlet is higher than the discharge outlet, and the angle formed between the inclined plane formed by the level of the feed inlet and the level of the discharge outlet and the horizontal plane is 45°. The vaporizer used has its inlet and outlet on the same level. The buffer tank used has the inlet at the top and the outlet at the bottom.
[0043] When the liquid chlorine tank truck 1 was unloading, the liquid chlorine pressure in the liquid chlorine storage tank 2 was about 0.8MPa, and the pressure of the liquid chlorine coming out of the storage tank 2 discharge port was raised to about 1.0MPa by the discharge pump 3, and the pressure was increased to about 1.0MPa with The flow rate of about 400kg / hr is sent to vaporizer 4. The vaporizer 4 is heated by hot water to keep the temperature inside the vaporizer 4 at about 39° C., and the chlorine gas obtained at the outlet of the vaporizer 4 enters the buffer tank 5 . The chlorine gas wit...
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