Method for improving producible oil index by use of starch wastewater
A starch wastewater and recovery technology, applied in chemical instruments and methods, mining fluids, earth drilling and mining, etc., can solve the problem of high cost of activators, and achieve the effect of simple operation, cost reduction and good effect
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Embodiment 1
[0029] Embodiment 1, taking a certain block A of Shengli Oilfield as an example
[0030] A block A in Shengli Oilfield is a high-salinity, medium-high-viscosity unconsolidated sandstone reservoir. The reservoir temperature is 65°C, the reservoir pressure is 15MPa, the permeability variation coefficient is 0.518, the porosity is 34.0%, and the pore volume is 3.6×10 4 m 3 , recoverable reserves 3.6×10 4 t, the formation water salinity is 16000mg / L. Utilize the method of the present invention to improve this block recovery rate, concrete implementation steps are:
[0031] (1) Starch wastewater pretreatment
[0032] First, the starch wastewater is filtered to remove solid waste and residues, and secondly, the pH of the starch wastewater is adjusted to 6.0.
[0033] (2) Determination of the volume concentration of nitrogen source and phosphorus source
[0034] The determination of the volume concentration of nitrogen source and phosphorus source adopts the static culture metho...
Embodiment 2
[0044] Embodiment 2, taking a block B of Shengli Oilfield as an example:
[0045] In a block B of Shengli Oilfield, the reservoir temperature is 70°C, the reservoir pressure is 12MPa, the permeability variation coefficient is 0.426, the porosity is 35.0%, and the pore volume is 5.8×10 4 m 3 , recoverable reserves 7.3×10 4t, the formation water salinity is 9600mg / L. Utilize the method of the present invention to improve this block recovery rate, concrete implementation steps are:
[0046] (1) Starch wastewater pretreatment
[0047] Firstly, the starch wastewater is filtered to remove solid waste and residues, and secondly, the pH of the starch wastewater is adjusted to 7.0.
[0048] (2) Determination of the volume concentration of nitrogen source and phosphorus source
[0049] The determination of the volume concentration of nitrogen source and phosphorus source adopts the static culture method, the specific method is as follows: ① take 100mL of pretreated starch wastewate...
Embodiment 3
[0059] Embodiment 3, taking a block C in Shengli Oilfield as an example:
[0060] The temperature of reservoir C in a block of Shengli Oilfield is 75°C, and the reservoir pressure is 10MPa. The coefficient of variation of permeability is 0.336, the porosity is 30.0%, and the pore volume is 2.1×10 4 m 3 , recoverable reserves 5.2×10 4 t, the formation water salinity is 12000mg / L. Utilize the method of the present invention to improve this block recovery rate, concrete implementation steps are:
[0061] (1) Starch wastewater pretreatment
[0062] Firstly, the starch wastewater is filtered to remove solid waste and residues, and secondly, the pH of the starch wastewater is adjusted to 8.0.
[0063] (2) Determination of the volume concentration of nitrogen source and phosphorus source
[0064] The determination of the volume concentration of nitrogen source and phosphorus source adopts the static culture method, the specific method is as follows: ① take 100mL of pretreated s...
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