Production process and production system of fatty alcohol polyoxyethylene ether sodium sulfate
A technology of alcohol polyoxyethylene ether sodium sulfate and alcohol polyoxyethylene ether, which is applied in the production process and production system of sulfonated fatty alcohol polyoxyethylene ether, and in the field of SO3/air mixed gas, which can solve the impact on the quality of sulfonated products , complex operation, long process flow, etc., to achieve the effect of equipment cost and energy consumption reduction, simple control, and short process flow
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Embodiment 1
[0036] The present embodiment provides a kind of production technology of fatty alcohol polyoxyethylene ether sodium sulfate, and flow rate is 4580m 3 After the outside air is removed by the filter, it enters the Roots blower for compression, and the pressure at the outlet of the blower increases to about 56KPa, and then the gas enters the low-temperature air condenser; the hot air in the low-temperature air condenser is cooled by two cooling media in turn, respectively For cooling water and ethylene glycol solution at 0±4°C, the hot air passes through the two cooling media to obtain cooling air with a temperature of 8°C; the cooling air directly enters the sulfur furnace, and the flow rate of the liquid sulfur delivery pump is 240kg / h of liquid sulfur burns in a sulfur furnace to form SO 2 / air mixed gas, the outlet temperature of the sulfur furnace is 600°C; SO 2 / Air mixed gas is cooled to about 450°C through the air cooler on the upper part of the conversion tower, and t...
Embodiment 2
[0042] The present embodiment provides a kind of production technology of fatty alcohol polyoxyethylene ether sodium sulfate, and flow rate is 4200m 3 After the outside air is removed by the filter, it enters the Roots fan for compression, and the pressure at the outlet of the fan increases to about 55KPa, and then the gas enters the low-temperature air condenser; the hot air in the low-temperature air condenser is cooled by two cooling media in turn, respectively For cooling water and ethylene glycol solution at 0±4°C, the hot air passes through the two cooling media to obtain cooling air with a temperature of 8°C; the cooling air directly enters the sulfur furnace, and the flow rate of the liquid sulfur delivery pump is 240kg / h of liquid sulfur burns in a sulfur furnace to form SO 2 / air mixed gas, the outlet temperature of the sulfur furnace is 610°C; SO 2 / Air mixed gas is cooled to about 450°C through the air cooler on the upper part of the conversion tower, and then pa...
Embodiment 3
[0047] The present embodiment provides a kind of production technology of fatty alcohol polyoxyethylene ether sodium sulfate, and flow rate is 5775m 3 After the outside air is removed by the filter, it enters the Roots blower for compression, and the pressure at the outlet of the blower increases to about 56KPa, and then the gas enters the low-temperature air condenser; the hot air in the low-temperature air condenser is cooled by two cooling media in turn, respectively For cooling water and ethylene glycol solution at 0±4°C, the hot air passes through the two cooling media to obtain cooling air with a temperature of 8°C; the cooling air directly enters the sulfur furnace, and the flow rate of the liquid sulfur delivery pump is 330kg / h of liquid sulfur burns in a sulfur furnace to form SO 2 / air mixed gas, the outlet temperature of the sulfur furnace is 600°C; SO 2 / Air mixed gas is cooled to about 450°C through the air cooler on the upper part of the conversion tower, and t...
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