Abstract
The turbulence generator is a key component of medium consistency centrifugal pulp pumps, with functions to fluidize the medium consistency pulp and to separate gas from the liquid. Structure sizes of the generator affect the hydraulic performance. The radius and the blade laying angle are two important structural sizes of a turbulence generator. Starting with the research on the flow inside and shearing characteristics of the MC pulp, a simple mathematical model at the flow section of the shearing chamber is built, and the formula and procedure to calculate the radius of the turbulence generator are established. The blade laying angle is referenced from the turbine agitator which has the similar shape with the turbulence generator, and the CFD simulation is applied to study the different flow fields with different blade laying angles. Then the recommended blade laying angle of the turbulence generator is formed to be between 60° and 75°.
1. Introduction
MC (Medium Consistency) pulp pumps are key equipment to transport pulp in modern paper mills. Paper pulp suspension contains three kinds of media, namely, fibers, water, and air, which results in a high flow complexity and particularity in the pump itself. The pulp cannot move when the pulp mass consistency is more than 6%. In order to transport the medium with the consistency over 6%, the MC pulp pumps must have the ability to fluidize the pulp. The turbulence generator is the key component of the MC centrifugal pulp pump, which fluidizes the MC pulp and separates the gas from the pulp suspension. The structure of MC pulp pumps is shown in Figure 1.
Some research had been done in China [1–4], including the simulation of fluidization of paper pulp suspension and the optimized designs of the turbulence generator. But the systemic design theories and methods are still not built. Starting with the research on the flow and shearing characteristics of the MC pulp, a simple mathematic model is built, and the formula for calculating the radius of the turbulence generator is established. The range of the blade laying angle is obtained by the recommended blade laying angle from the turbine agitator which has the same shape as the turbulence generator, and the CFD simulation is applied to study the different flow fields with different blade laying angles.
2. Deducing the Critical Shear Velocity Gradient
The flow of MC pulp suspension is neither similar to usual water flow, nor to two-phase flow or liquid-particle flow. It is a kind of three-phase fluid, consisting of gas-liquid (water)-solid (fiber) flow. It has very complicated flow characteristics, changing with the species, consistency, and velocity of the paper pulp and the fiber shape.
High consistency of the fibers and gas/air in the MC pulp makes the fiber suspensions fail to move forward freely. By high-speed rotation, the turbulence generator introduces high shearing force to distribute fibrous reticulum and also avoid fibers to flocculate again. In this situation, pulp fiber suspensions show the flow characteristics as similar to water. Therefore it is defined as fluidization [4].
The minimum shear force which makes fibrous reticulum of the MC pulp suspension distributed is called the critical shear force. Based on experimental researches on sulphated wood pulp by Hemstrom et al. [5], the critical shear force can be given as where and are the coefficients related to the species of the paper pulp. For given species of the paper pulp, the critical shear force is only related to , which is the mass consistency of the paper pulp suspension.
The apparent viscosity of the non-Newtonian fluid is defined as the ratio of the shear force to the shear velocity [6]. The apparent viscosity, (Pa·s), is given by where is the shear force (Pa) and is the shear velocity gradient (1/). We can get the critical shear velocity gradient of the paper pulp by (1), but for the actual generator design, there is no direct relationship between the critical shear force and the geometric parameters. So we need to change the condition parameter of the fluidization from the critical shear force to the critical shear velocity gradient, by analyzing the relationship between the shear force, the shear velocity, and the shear velocity gradient.
Duffy et al. [7] obtained the apparent viscosity of straw wood pulp by experiments. The apparent viscosity, , is given by simultaneously by (2) and (3) where is the shear velocity gradient for the fluidization of paper pulp.
Simultaneously by (1) and (4) Gullichsen and Harkonen [8] and Kefu [9] obtained the values of and with shearing experiments on MC pulp. Based on the experimental data and the formulations above, ( = 15%) and of seven common kinds of paper pulp are obtained, as shown in Table 1.
3. Parameters of the Turbulence Generator
The turbulence generator in this research consists of a hub and three blades. The blade working face is perpendicular to the surface of the hub. Outside surfaces and inside surfaces of blades are all cylindrical surfaces.
Main parameters of a turbulence generator are shown in Figure 2.
The blade outlet radius and the blade laying angle are the most important design parameters, which are the preconditions of other structure sizes, deciding the working range and efficiency of the MC pulp pumps.
4. Blade Outlet Radius of Turbulence Generator
In this part, starting with the researches on the flow characteristics of the MC pulp suspension, a series of formulas are deduced to qualify the critical fluidization of MC pulp. The formulas for calculating the radius of the turbulence generator have then been established by simplifying the model of the flow field of the turbulence generator.
4.1. Calculating Blade Outlet Radius
As shown in Figure 3, supposing that the paper pulp suspension fills within the full flow passage, we analyze the force of laminar flow in the torus field at a section of the shearing chamber of the turbulence generator.
When the turbulence generator is rotating at a high speed, neglecting axial velocity, we can consider the paper pulp flow being laminar in the area from blade top of the turbulence generator to the inside wall of the shearing chamber. We note the shear force inside as and outside as , as shown in Figure 3. At the normal running condition, the momentum moment to axis in the grid flow field keeps constant. So the whole moment is zero. That is,
So, where is a constant and is the circumferential shear force at radius position.
Based on formulas above, given the shearing chamber radius and the shear force at the inside wall , we can obtain the momentum moment :
Combine (4), (7), and (8). is given by, where is the radial velocity gradient when the radius is .
In conditions of a laminar flow, the shear velocity gradient is inversely proportional to the distance to the rotating axis in the area from the blade top of the turbulence generator to the inside wall of the shearing chamber. So the shear force near the inside wall of the shearing chamber is the smallest. We can consider that the whole flow field becomes turbulent, if the shear velocity gradient near the inside wall reaches the critical value.
Define as where is a constant which is decided by the species of the paper pulp and the shearing chamber radius .
So (9) becomes,
The velocity of pulp at the blade outlet of the turbulent generator is given by
From the formulas above, we can get the critical shear force from Table 1. Let be equal to , and we get the minimal from (10). Then can be obtained from (14).
4.2. Design Example
The design parameters of an MC pulp pump are taken as follows: = 60 m3/h, = 50 m, r/min, = 8%–15%, and the pump inlet diameter (shearing chamber diameter) = 150 mm.
Based on the parameters above and Table 1 when is 15%, the critical shear force = = 5818.66 Pa, the shearing chamber radius = = 75 mm. So we get the following from (13):
Finally, we obtain from (14) that = 62.47 mm. Let = 65 mm after roundness.
By the experiment of the MC pulp pump with the turbulence generator of the sizes given above, the performance of the pump is checked and achieved in the paper published before [10]. This paper introduced the main structure of the test bed for the centrifugal pulp pump. The test result showed that the pump could run stably and efficiently under the 11% stock consistency in that test condition, with the efficiency to 40%. It testified the MC pump had a good performance, satisfying the pulp transporting needs.
5. Blade Laying Angles of Turbulence Generator
5.1. Setting Blade Laying Angle
The principle of the turbulence generator is similar to an agitator. The blade structure is similar to a pitched turbine agitator, as shown in Figure 4. The viscosity coefficient of the transporting medium in one agitator can reach 100 Pa.s, which matches up to that in the turbulence generator of the MC pulp pump. According to [11], the recommended blade laying angles are 45°, 60°, and 90°. The initial axial velocity inside the agitator is usually zero, but it is not null inside the pump. Compared to the recommended blade laying angle of the pitched turbine type agitator, the angle of the turbulence generator should be modified according to the actual flow.
Figure 5 shows the outlet streamline of the turbulence generator. is the correction angle, which means the angle between relative velocity direction and circumferential velocity direction at the blade outlet; is the recommended blade laying angle of the turbine agitator; is the blade laying angle of outlet streamline.
We can obtain the following equations from Figure 5 where is the volumetric flow (m3/h); is the axial velocity (m/s); is the relative velocity (m/s); is the linear velocity at the blade outlet (m/s); is the shearing chamber radius of the turbulence generator ().
In the application of the MC pulp pump, the rotating direction of the turbulence generator should be contrary to the pump impeller. The blade laying angle cannot exceed 90°, so should be 0° when is already 90°.
The blade correction angle is 10.8° after calculation by (17). According to (16), three blade laying angles of the turbulence generator are 55.8°, 70.8°, and 90°, respectively.
5.2. CFD Simulation Model
CFD (Computational Fluid Dynamics) is used to calculate and analyze the flow field through solving basic equations, such as the momentum conservation equations, the mass conservation equations, and the energy conservation equations. The numerical simulations in this paper are performed using FLUENT 6.2.
The flow of the MC pulp suspension after fluidization is a turbulence flow, and the flow characteristics are similar to the gas-water two-phase flow, but the large amount of gas inside the pulp will influence the flow.
The research on the inner flow in the MC pulp pump focuses on the movement and distribution of gas in the paper pulp, interaction between gas and liquid, as well as the turbulence distribution in the flow field. So in the CFD simulation of the fiber suspension flow in the shearing chamber, we apply Eulerian gas-liquid phase model and RNG κ-ε model, with RANS as momentum equations [12]. We use the MRF (Multiple Reference Frames) [13, 14] to build the frame, Phase Coupled SIMPLE to deal with the coupling of pressure and velocity, and the implicit steady-state segregating solution to solve the equations.
5.3. Building 3D Models and Boundary Conditions
We establish a 3D model and define the grid for the flow field of the turbulence generator when the blade laying angles are 55.8°, 70.8° and 90°, respectively. We make the field a whole field to simplify the computation, as shown in Figure 6. Boundary conditions are determined as the real running conditions of the turbulence generator. The gas volume fraction is 20%.
5.4. Analysis of the Simulation Results
Simulation results are compared and analyzed, which are the effects on the gas-liquid separation, the turbulent kinetic energy, the torque produced by the turbulence generator, and the pressure changing from the outlet to the inlet of the turbulence generator.
(1) Effects on Gas-Liquid Separation
From Figure 7, we can observe that there is no big difference of effects on gas-liquid separation, with the gas volume fraction reaching almost 95% at the end of the turbulence generator. The blade impact angle from the medium will increase with the enlargement of the blade laying angle, which results in the low pressure field being strengthened and expanded on the suction face at the blade front part. So we can find that the bigger the blade laying angle is, the shorter the gas-liquid separation field is to the blade front part.
| (a) = 55.8° |
| (b) = 70.8° |
| (c) = 90° |
(2) Turbulent Kinetic Energy Distribution
According to Figure 8, the turbulent kinetic energy in the field between the blade outlets to the inside wall of the shearing chamber is lower than that around blades. And the distribution of the turbulent kinetic energy trends to be well distributed with the increase of the blade laying angle.
| (a) = 55.8° |
| (b) = 70.8° |
| (c) = 90° |
(3) Targeted Values
From Table 2, we can get that, with the increase of the blade laying angles , the turbulence intensity will also increase, so did the torque value of the turbulence generator. But the differential pressure in the flow field from outlet to inlet decreases continuously.
Theoretical analyses show that, with the increase of the blade laying angles , the guiding role that blades were playing for the paper pulp decreases, which causes the torque value produced by the turbulence generator to be increased. Meanwhile the increase of the impact from the blades to the medium makes the flow more complicated, which results in a stronger turbulence flow. When blade laying angle becomes small, the axial thrust applied to the paper pulp produced by the blades makes the outlet pressure bigger than the inlet pressure. When increases to a certain value, the axial trust will offset the frictional head loss as of the paper pulp flow. There will be no axial thrust when is 90°, and the frictional loss causes the outlet pressure to become smaller than the inlet pressure.
Based on the results of the numerical simulation, the recommended blade laying angle of the turbulence generator is from 60° to 75°.
6. Conclusions
(1)We analyzed the principle and the conditions of the fluidization of medium consistency pulp. We established the fluidization expression formulas with the characteristic parameters as variables of the MC pulp pump. (2)We established the flow mathematical model inside the shearing chamber and obtained the formula to calculate the blade outlet radius of the turbulence generator. (3)We simulated the pulp flow inside the turbulence generator. Blade laying angle of the turbulence generator has a small influence on the gas-liquid separation. But the bigger the blade laying angle is, the nearer the gas-liquid separation field is to the blade front part. And the distribution of the turbulent kinetic energy trends to be well distributed with the increase of the blade laying angles. (4)The recommended blade laying angle of the turbulence generator is from 60° to 75°.Acknowledgment
This paper is is supported by high technology project of Jiangsu province, China, ID: SBE201000567, R&D of MC paper pulp pumping system.