Reuse treatment system and treatment method for high-temperature separated water of steam injection boiler
A technology for a steam injection boiler and a treatment system, which is applied in the field of high-temperature separation water reuse treatment system for steam injection boilers, can solve the problems of a large amount of cooling water, the inability of effective resource utilization of heat energy, and the blockage of traditional membrane processes, so as to reduce heat loss. Effect
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Embodiment 1
[0060] 1) The high-temperature separated water produced by the steam injection boiler enters the flash tank; the high-temperature separated water of the steam injection boiler generates secondary steam at a temperature of about 140°C in the flash tank, and at the same time produces part of the flash condensate with a temperature of about 140°C. The flash condensate produced by the steamer is about 60% of the high temperature separated water;
[0061] 2) The secondary steam generated by the flash tank is used as the ejection steam of the TVC unit, and enters the TVC unit with the secondary steam generated by the crystallization separation unit;
[0062] 3) The flash condensate passes through the first heat exchanger 12 and the second heat exchanger 1 to exchange heat with the silicon removal wastewater and boiler feed water, and then enters the regulating pool at a temperature of about 80°C, and the pH in the regulating pool is adjusted to 7-10;
[0063] 4) The adjustment tank ...
Embodiment 2
[0070] 1) The high-temperature separated water produced by the steam injection boiler enters the flash tank; the high-temperature separated water of the steam injection boiler generates secondary steam at a temperature of about 160°C in the flash tank, and at the same time produces part of the flash condensate with a temperature of about 160°C. The flash condensate produced by the steamer is about 50% of the high temperature separated water;
[0071] 2) The secondary steam generated by the flash tank is used as the ejection steam of the TVC unit, and enters the TVC unit with the secondary steam generated by the crystallization separation unit;
[0072] 3) The flash condensate passes through the first heat exchanger 12 and the second heat exchanger 1 to exchange heat with the silicon removal waste water and the boiler feed water, and then enters the regulating tank at a temperature of about 65°C, and adjusts the pH in the regulating tank to 7-10;
[0073] 4) The adjustment tank i...
Embodiment 3
[0080] 1) The high-temperature separated water produced by the steam injection boiler enters the flash tank; the high-temperature separated water of the steam injection boiler generates secondary steam at a temperature of about 160°C in the flash tank, and at the same time produces part of the flash condensate with a temperature of about 160°C. The flash condensate produced by the steamer is about 50% of the high temperature separated water;
[0081] 2) The secondary steam generated by the flash tank is used as the ejection steam of the TVC unit, and enters the TVC unit with the secondary steam generated by the crystallization separation unit;
[0082] 3) The flash condensate passes through the first heat exchanger 12 and the second heat exchanger 1 to exchange heat with the silicon removal waste water and the boiler feed water, and then enters the regulating tank at a temperature of about 65°C, and adjusts the pH in the regulating tank to 7-10;
[0083] 4) The adjustment tank...
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