A kind of energy supply system of epichlorohydrin saponification process
An energy supply system, epichlorohydrin technology, applied in the chemical industry, organic chemistry, sustainable manufacturing/processing, etc., can solve the problems of large saponification waste water, heat energy cannot be comprehensively utilized, and the connection is not closely connected, so as to save production cost, to achieve optimal utilization, to achieve the effect of energy
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Embodiment 1
[0020] The high-specification steam condensate (5) from the epichlorohydrin main production process enters the high-temperature condensate heat exchanger (1) and exchanges heat with the cold material from the low-temperature condensate heat exchanger (2). The steam condensate (5) enters the condensate recovery system (6) after condensation, and the hot stream generated during the heat exchange process is sent to the steam generating device (3); the low-specification steam condensate ( 7) Exchange heat with the condensate from the steam generating device (3), and send a part of the low-standard steam condensate (7) to the lime emulsification ash section (8) after heat exchange to a certain temperature, and the other part is used as a high-temperature condensate for heat exchange The cold material input from the device (1); the steam generating device (3) de-flashes the raw steam (10), and heats the hot stream from the high-temperature condensate heat exchanger (1) to generate st...
Embodiment 2
[0022] Taking the scale of an epichlorohydrin plant with an annual output of 30,000 tons as an example, the main production process of 30,000 tons / year epichlorohydrin steam produces high-standard steam with a condensate volume of 28-30t / h (about 144°C), and the auxiliary production process The amount of low-specification steam condensate produced is 17t / h (about 70°C), and the steam consumption of traditional saponification process is about 10t / h (5barA).
[0023] After adopting the energy supply system of this patent, the steam used in the epichlorohydrin production equipment of the same scale is 10t / h (10barA) steam, and the high-standard steam condensate produced by the epichlorohydrin main production process is 4barA as an example. The heat recovered by the condensate heat exchanger is equivalent to 1t / h of 5barA steam; based on the water volume of 7t / h (88°C) in the deashing section, the heat recovered by the low-temperature condensate heat exchanger is equivalent to 0.3t...
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