Experimental temperature: 50˚C.

Experimental water: the simulated water is prepared according to the ion composition of the mixed water in the oilfield at the present stage. The mineralization degree is 13,930 mg/L. the ion composition is shown in Table 1.

Experimental drug:

Partially hydrolyzed polyacrylamide (HPAM, industrial product, molecular weight of 1200 × 10⁴ g/mol, hydrolysis degree 21.2%), structural polymer A (solid content 91.22%, molecular weight 1200 × 10⁴ g/mol, hydrolysis 21.65%), structural polymer B(molecular weight 600 × 10⁴ g/mol), gel (partially hydrolyzed polyacrylamide and phenolic resin crosslinking agent and auxiliaries) Gel system).

1) Viscosity concentration relationship before and after shearing

The simulated formation water was used to prepare different polymer mother liquor (5000 mg/L) and diluted to different polymer concentrations. The polymer was sheared with a warming agitator at a shear rate of 3000 r/min and a shearing time of 20 s. The viscosity and viscosity retention rate of polymer solution before and after shear were measured, and the viscosity concentration relationship and viscosity retention curve before and after shear were drawn. The viscosity and concentration of all kinds of polymers and gels before and after shearing were determined.

The apparent viscosity retention was calculated according to the formula

R v = η t η 0 × 100 %

where,

R_v—apparent viscosity retention rate, expressed as a percentage;

η₀, η_t—apparent viscosity of polymer solution before and after stirring, unit: mPa∙s.

2) Resistance coefficient and residual resistance coefficient

The resistance coefficient and the residual resistance coefficient are the technical indicators of the ability of the PPG system to improve mobility ratio and reduce reservoir permeability. The experimental device is shown in Figure 1, and the flow rate was 1 mL/min. Experimental steps are as follows:

a) All devices were connected according to Figure 1;

b) The simulated water and PPG solution was put into the middle containers respectively;

c) The incubator was preheat to the experimental temperature of 65˚C;

d) Water was injected into the sand pack at a constant flow rate until the pressure is stable, at which the pressure difference is ΔP_wi;

e) PPG solution was injected with the same flow rate as the water injection until the pressure is stable, at which the pressure difference is ΔP_wh;

f) The simulated water was injected with the same flow rate as the water injection until the pressure is stable, at which the pressure difference is ΔP_wa.

The resistance coefficient is shown in formula (1) and the residual resistance coefficient is shown in formula (2):

F R = Δ P w h Δ P w i (1)

F R R = Δ P w a Δ P w i (2)

where,

F_R—the resistance coefficient;

F_RR—the residual resistance coefficient;

ΔP_wh—Pressure difference when the pressure of PPG solution is stable, MPa;

ΔP_wi—Pressure difference when the pressure of initial waterflooding is stable, MPa;

ΔP_wa—The pressure difference when the PPG solution is injected and the pressure of subsequent waterflooding is stable, MPa.

3) Oil displacement experiment with parallel sand pack

The parallel sand pack experiment reflects the heterogeneity of the formation and the profile adjustment of the system. The experimental process is as follows:

a) Connect all devices according to Figure 2;

b) Put the simulated water, simulated oil and chemical solution into the container in the middle respectively;

c) Preheat the incubator to the experimental temperature of 65˚C;

d) The permeability of water phase in sand pack is calculated when the pressure is stable after injecting water in a constant flow rate;

e) Saturate the simulated oil at high temperature to prevent core damage or sand migration caused by too high viscosity of the simulated oil. The saturation temperature should be 10˚C higher than the experimental temperature. Record the volume of displaced water, and that value is the saturated oil volume. (recording must be finished at experimental temperature, and the device must be sealed well to prevent loss caused by volatilization);

f) Aging sand pack: close the inlet and outlet and age for 72 hours at the experimental temperature;

g) Set water cut for water flooding;

h) Inject the chemical solution at same flow rate as water injection until the pressure is stable;

i) Inject the simulated water at same flow rate as water injection to the target water cut.

1) Partially hydrolyzed polyacrylamide

Dilute the mother liquor of partially hydrolyzed polyacrylamide to 1000 mg/L, 2000 mg/L, 3000 mg/L and 4000 mg/L, and shear with Wuyin stirrer. Determine the viscosity after shearing, viscosity concentration relationship and viscosity retention rate are shown in Figure 3.

2) structural polymer A

The mother liquor of structural polymer A was diluted to 1000 mg/L, 2000 mg/L, 3000 mg/L and 4000 mg/L. the shear viscosity was determined by Wu Yin agitator. The viscosity concentration relationship and viscosity retention rate were shown in Figure 4.

3) structural polymer B

Dilute the mother liquor of structural polymer B to 1000 mg/L, 2000 mg/L, 3000 mg/L, 4000 mg/L, and shear with Wuyin agitator. Determine the viscosity after shearing. See Figure 5 for viscosity concentration relationship and viscosity retention rate.

4) gel

Gel composition: 1000 mg/L - 3000 mg/L structural polymer A +0.15% main crosslinking agent +0.15 cross linking agent, main crosslinking agent and auxiliary crosslinking agent concentration unchanged, changing polymer viscosity. Crosslinking time: 30 h, crosslinking temperature: 50˚C. As the concentration of the main crosslinking agent and the crosslinking agent is unchanged, the consistency of the gel before and after shearing is shown in Figure 6 with the polymer concentration as the abscissa.

Gel stability is an important property that restricts its application. Static gel aging for 15 days at different concentrations of 50˚C is shown in Table 2. From Table 2, it is known that gel 2000 mg/L has higher viscosity and higher shear retention rate after gelation. When polymer concentration is 3000 mg/L, long time static will lead to gel dehydration, so the polymer concentration in gel formula is 2000 - 2500 mg/L, and the performance is better.

The data in Figures 2-5 are summarized to get Table 3. Table 3 shows that the viscosity of ordinary polymer and structural polymer B is lower before and after shearing. The viscosity of structural polymer A is higher before and after shearing. The higher the concentration, the higher the viscosity retention rate, the highest viscosity of the gel system, and the best shear resistance. and gel were used to carry out the experiment of drag coefficient and residual resistance coefficient.

The porosity of sand filling pipe with permeability of 10 μm² and 20 μM² is

higher than 35%. The drag coefficient and residual resistance coefficient were determined by injecting structural polymer A or gels respectively. The structural

polymer A concentration is 1250 mg/L - 3000 mg/L, the results are shown in Table 4, Table 5; gel formula is 1500 mg/L polymer +1500 mg/L phenolic resin cross-linking agent +1500 mg/L assistant, and the results are shown in Table 6.

It can be seen from Table 4 to Table 5 that the resistance coefficient building ability of structural polymer A varies greatly among different flow rates under the permeability model of 10 μm². High flow rate of 1.5 ml/min at low concentration has strong resistance building ability, and low flow rate of 0.5 ml/min at high concentration has the maximum resistance building ability. When the permeability is greater than 10 μm², the influence of each flow rate on resistance coefficient establishment ability is small, from the point of view of resistance building ability, it is considered that polymer is not suitable for formations with permeability above 10 μm². From Table 6, it is known that when the permeability of the gel system is 10 μm² the resistance coefficient of 0.5 mL/min is minimum. When the permeability is greater than 10 μm², the smaller the flow rate, the greater the drag coefficient and the residual resistance coefficient. The gel system has stronger ability to establish resistance coefficient and residual resistance than structural polymer A flooding system.

Use the parallel sand filling pipe model to study on gel enhanced oil recovery capability.

Formula: 2500 mg/L polymer + 0.15% cocrosslinking agent + 0.15% cocrosslinking agent。

Injection volume: 0.3 times of total pore volume。

The permeability and porosity of high-low permeability model and the change of diversion efficiency and recovery degree in each stage of displacement experiment were recorded in the process of displacement (Table 7).

With the injection pore volume multiplier as the abscissa, the pressure recovery and moisture content were used as the ordinate to draw the parallel recovery factor and water cut curve of weak gel system see in Figure 7.

Taking the multiple of injected pore volume as the abscissa and the diversion rate as the ordinate, the variation trend chart of diversion rate with the change of injection stage in high and low permeability formation is drawn as shown in Figure 8.

The results were as follows

1) Under the condition of stage difference 2, the recovery rate of low permeability water drive is 22.63%, and that of high permeability water drive is 31.6%.

2) The recovery of low permeability polymer flooding is 24.37%, and that of high permeability polymer flooding is 29.31%.

3) Under the condition of stage difference 2, the recovery rate of water flooding after low permeability is 14.66%, and that of water flooding after high permeability is 17.86%.

4) Analysis of the diversion rate curve shows that in the water drive stage, the low permeability basically does not enter the liquid, the diversion rate is low, polymer flooding effectively improves the diversion rate, and finally in the later water drive stage, the diversion rate is effectively improved.