Hydrocarbon fluid flow improver
A flow improver, fluid technology, applied in (dendrimer), identifying the claimed field, able to solve problems such as high cost
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[0056] Three embodiments of flow improvers were prepared according to the present disclosure. BoltornH20 was obtained from Perstorp (Sweden) and used without further purification. Boltorn H20 is believed to have an average molecular weight of 1750 g / mol. Lauric acid (C 12 ), palmitic acid (C 16 ) and stearic acid (C 18 ) were obtained from laboratory supplies and used without further purification. p-Toluenesulfonic acid (TsOH) was obtained from a laboratory supply and used without further purification.
example 1
[0058] 36.6 g of lauric acid (183 mmol) were mixed with 20 g of Boltorn H20 (11 mmol) and a catalytic amount of p-toluenesulfonic acid (-0.01%). The mixture was heated to 140°C and stirred for 1 hour, then placed under vacuum and stirred for a further 7 hours to yield 47.73 g of a brown viscous liquid, laurate of Boltorn H20.
example 2
[0060] Example 2 was prepared in the same manner as Example 1, using a slight molar excess (above 16 eq.) of palmitic acid. Example 3 was prepared in the same manner as Example 1, using a slight molar excess (above 16 eq.) of stearic acid. Product appearance is detailed in Table 1 below.
[0061] Table 1: Product Physical Properties
[0062] sample
Exterior
Example 1
liquid / amber
Example 2
solid / light brown
Example 3
solid / dark brown
[0063] The oil and gas fluid used as a sample is a waxy condensate. The product was observed for paraffin crystal formation and deposition, pour point temperature (PPT) reduction, rheological profile and viscosity at 4°C and 20°C.
[0064] As shown in Table 2 below, to simulate the potential deep water use of each example, each example was diluted to 25% with xylene. Initial viscosity evaluations showed that Example 1 at a concentration of 50% was within the viscosity range required for u...
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Abstract
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