Method for producing soap wax and low melting point paraffin
A low melting point, paraffin technology, applied in the direction of petroleum wax recovery, can solve the problems of long production cycle and low product yield, and achieve the effects of low operating cost, low investment in equipment, and accelerated separation speed.
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Embodiment 1
[0044] This embodiment includes: A: emulsification and B: sweating.
[0045] A: emulsification
[0046] This part includes (A1) oil phase material preparation, (A2) water phase material preparation, (A3) emulsion preparation three steps.
[0047] (A1) Oil phase material preparation
[0048] Take Daqing crude oil Changsixian wax paste (melting point 41.5°C, oil content 13.2%) 85.0Kg, heat to 80°C and melt, add sorbitan monooleate 1.6Kg, sorbitan monolaurate 0.8Kg and Polyoxyethylene fatty acid ester 0.6 Kg, stir evenly.
[0049] (A2) Preparation of aqueous phase materials
[0050] Put 0.06Kg of CO at 25.0-25.2 atmospheric pressure (gauge pressure) 2 Dissolve in 11.94Kg of water and heat to 85°C.
[0051] (A3) Emulsion preparation
[0052] Pressurize the oil phase material to 25.0-25.2 atmospheres (gauge pressure), and stir at a speed of 500r / min; add the water phase material to the oil phase material, and continue stirring for 30 minutes to form a water-in-oil emulsion. ...
Embodiment 2
[0068] This embodiment includes: A: emulsification and B: sweating.
[0069] A: emulsification
[0070] This part includes (A1) oil phase material preparation, (A2) water phase material preparation, (A3) emulsion preparation three steps.
[0071] (A1) Oil phase material preparation
[0072] Take 80.0Kg of Daqing crude oil Changsixian wax paste (the properties are the same as in Example 1), heat to 80°C and melt, add 2.5Kg of sorbitan monostearate, 0.6Kg of polyoxyethylene fatty acid ester, lauryl Betaine 0.4Kg, stir evenly.
[0073] (A2) Preparation of aqueous phase materials
[0074] With 27.5% H 2 o 2 solution, solid NaOH and H2 O formulated with H 2 o 2 1.0%, NaOH 6.0 mg / Kg aqueous solution, take 16.5Kg, pressurize to 25.0-25.2 atmospheres (gauge pressure) under nitrogen condition, and heat to 85°C.
[0075] (A3) Emulsion preparation
[0076] Pressurize the oil-phase material to 25.0-25.2 atmospheres (gauge pressure) under nitrogen, and stir at a speed of 800 r / mi...
Embodiment 3
[0081] This embodiment includes: A: emulsification and B: sweating.
[0082] A: emulsification
[0083] This part includes (A1) oil phase material preparation, (A2) water phase material preparation, (A3) emulsion preparation three steps.
[0084] (A1) Oil phase material preparation
[0085] Take 82.5Kg of Daqing crude oil minus second-line wax paste (melting point 50.6°C, oil content 21.4%), heat to 85°C and melt, add 1.5Kg of sorbitan monostearate, 0.7Kg of diethylene glycol monolaurate, Triacetamide oleate 0.3Kg, stir evenly.
[0086] (A2) Preparation of aqueous phase materials
[0087] Put 0.2Kg of CO under 28.0-28.2 atmospheric pressure (gauge pressure) 2 Dissolve in 14.8Kg of water and heat to 90°C.
[0088] (A3) Emulsion preparation
[0089] Pressurize the oil phase material to 28.0-28.2 atmospheres (gauge pressure), and stir at a speed of 400 r / min; add the water phase material to the oil phase material, and continue stirring for 25 minutes to form a water-in-oil ...
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