Multifunctional crude oil tank farm treating agent
A multi-functional, treating agent technology, applied in the direction of chemical dehydration/demulsification, etc., can solve the problems of large usage and narrow application range, and achieve the effects of low usage, increase effective tank capacity, and save labor costs.
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Embodiment 1
[0012] This example is a field application test
[0013] Proportion of treatment agent used: nonylphenolic resin polyether 60%, SP-169 10%, polyacrylic acid 3%, diethylene glycol butyl ether 20%, naphtha 7%. The process steps to produce 1 ton are: first add 200 kg of diethylene glycol butyl ether to the reactor, start stirring, heat to 35-40 degrees Celsius, add 70 kg of naphtha, 600 kg of nonylphenolic resin polyether, SP- 169 100 kg, stirring for 30 minutes, then adding 30 kg of polyacrylic acid, stirring for 30 minutes, standing still, cooling to 20 degrees Celsius, the finished product can be obtained.
[0014] The application site is a crude oil tank area of an oil refinery, and the average daily processing capacity of the device is 3,000 tons / d. The salt content of the crude oil entering the tank is 98.53ppm, and 15ppm of this compounding agent is added before entering the tank, the salt content of the crude oil leaving the tank is 25.15ppm, the desalination rate is c...
Embodiment 2
[0016] This example is a field application test
[0017] Proportion of treatment agent used: tert-butylphenolic resin polyether 55%, SP-169 15%, polyacrylic acid 2%, diethylene glycol butyl ether 18%, terpene 10%. The process steps to produce 1 ton include: first add 180 kg of diethylene glycol butyl ether to the reactor, start stirring, heat to 35-40 degrees Celsius, add 100 kg of terpene, 550 kg of tertiary butylphenolic resin polyether, SP- 169 150 kg, stir for 30 minutes, then add 20 kg of polyacrylic acid, stir for 25 minutes, let it stand, and cool to 20 degrees Celsius to get the finished product.
[0018] The application site is a crude oil tank area of an oil refinery, and the average daily processing capacity of the device is 15,000 tons / d. The salt content of the crude oil entering the tank is 74.6ppm, and 12ppm of this compounding agent is added before entering the tank, the salt content of the crude oil leaving the tank is 21.2ppm, the desalination rate is cont...
Embodiment 3
[0020] This example is a field application test
[0021] Proportion of treatment agent used: 30% nonylphenol aldehyde resin polyether, 35% tert-butyl phenolic resin polyether, 10% SP-169, 5% polyacrylic acid, 5% diethylene glycol butyl ether, naphtha 15%. The process steps for producing 1 ton include: adding 50 kilograms of diethylene glycol butyl ether to the reactor first, stirring, heating to 35-40 degrees Celsius, adding 150 kilograms of naphtha, 300 kilograms of nonylphenol-amine-formaldehyde resin polyether, 350 kg of tert-butylphenolic resin polyether, 100 kg of SP-169, stirred for 25 minutes, then added 30 kg of polyacrylic acid, stirred for 40 minutes, allowed to stand, and cooled to 20 degrees Celsius to obtain the finished product.
[0022] The application site is a crude oil tank area of an oil refinery, and the average daily processing capacity of the device is 30,000 tons / d. The salt content of the crude oil entering the tank is 121.31ppm, and 10ppm of this c...
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