Mother liquid treatment method during production of pentaerythritol
A pentaerythritol and treatment method technology, applied in natural water treatment, chemical instruments and methods, water/sewage multi-stage treatment, etc., can solve the problems affecting the quality of sodium formate products, reducing the yield of pentaerythritol, affecting the stability of the system, etc., to improve System stability, organic content reduction, good product quality
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example 1
[0027] like figure 2 As shown, first set the first settling tank V1, its volume is 100 m 3 , the inside of the settling tank V1 is equipped with a steam heating coil and agitator, and the outside of the settling tank V1 is equipped with a circulating pump. The inlet of the circulating pump is connected to the bottom of the settling tank V1, and the outlet is respectively connected to the upper inlet of the settling tank V1 and the second settling tank V's entrance. Behind the first settling tank V1, the second settling tank V2, the third settling tank V3, the fourth settling tank V4, the fifth settling tank V5, and the sixth settling tank V6 are arranged in sequence. Each settling tank V2.... Settling tank V6 There are steam heating coils and agitators inside. Each settling tank V2.... Settling tank V5 is equipped with a circulating pump outside. The inlet of the circulating pump is connected to the bottom of the settling tank of this stage, and the outlet is respectively co...
example 2
[0031] The mother liquor from the system, according to the flow rate of 10m 3 / h for V1 tank, open the V1 tank to heat the steam to control the temperature at 65~70°C, open the V1 tank to stir, adjust the stirring speed to 40~50r / min, turn on the circulation pump, and adjust the circulation flow to 35~40m 3 / h, the control flow rate from production to V2 tank is 10m 3 / h, control the liquid level of V1 tank to remain unchanged; after extracting the mother liquor to V2 tank, control the temperature at 65~70°C, turn on V2 tank for stirring, adjust the stirring speed to 40~50r / min, turn on the circulation pump, and adjust the circulation flow to 25~30m 3 / h, the control flow rate from production to V3 tank is 10m 3 / h, control the liquid level of V2 tank to remain unchanged; after extracting the mother liquor to V3 tank, control the temperature at 45~50°C, turn on V3 tank to stir, adjust the stirring speed to 40~50r / min, turn on the circulation pump, and adjust the circulation ...
example 3
[0033] The mother liquor from the system, according to the flow rate of 10m 3 / h for V1 tank, open the V1 tank to heat the steam to control the temperature at 65~70°C, open the V1 tank to stir, adjust the stirring speed to 40~50r / min, turn on the circulation pump, and adjust the circulation flow to 35~40m 3 / h, the control flow rate from production to V2 tank is 10m 3 / h, control the liquid level of V1 tank to remain unchanged; after extracting the mother liquor to V2 tank, control the temperature at 65~70°C, turn on V2 tank for stirring, adjust the stirring speed to 40~50r / min, turn on the circulation pump, and adjust the circulation flow to 25~30m 3 / h, the control flow rate from production to V3 tank is 10m3 / h, control the liquid level of V2 tank to remain unchanged; after extracting the mother liquor to V3 tank, control the temperature at 45~50°C, turn on V3 tank to stir, adjust the stirring speed to 40~50r / min, turn on the circulation pump, and adjust the circulation fl...
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